air individual permit part 70 reissuance #13900001-004 for ......air individual permit part 70...
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Air Individual Permit Part 70 Reissuance
13900001- 004 Permittee: Silgan Containers Mfg Corp - Savage
Facility name: Silgan Containers Mfg Corp - Savage 12130 Lynn Avenue South Savage, MN 55378 Scott County
Expiration date: January 25, 2022 * All Title I Conditions do not expire Part 70 Reissuance: January 25, 2017 Permit characteristics: Federal; Part 70/ Limits to avoid NSR; Limits to avoid NSR The emission units, control equipment and emission stacks at the stationary source authorized in this permit reissuance are as described in the Permit Applications Table. This permit reissuance supersedes Air Emission Permit No. 13900001- 002 and authorizes the Permittee to operate the stationary source at the address listed above unless otherwise noted in the permit. The Permittee must comply with all the conditions of the permit. Any changes or modifications to the stationary source must be performed in compliance with Minn. R. 7007.1150 to 7007.1500. Terms used in the permit are as defined in the state air pollution control rules unless the term is explicitly defined in the permit. Unless otherwise indicated, all the Minnesota rules cited as the origin of the permit terms are incorporated into the SIP under 40 CFR § 52.1220 and as such as are enforceable by EPA Administrator or citizens under the Clean Air Act.
Signature: Toni Volkmeier This document has been electronically signed. for the Minnesota Pollution Control Agency
for Don Smith, P.E., Manager Air Quality Permits Section Industrial Division
Table of Contents
Page
1. Permit applications table ............................................................................................................................................. 3 2. Where to send submittals ............................................................................................................................................ 4 3. Facility description ....................................................................................................................................................... 5 4. Summary of subject items ........................................................................................................................................... 6 5. Limits and other requirements .................................................................................................................................... 8 6. Submittal/action requirements ................................................................................................................................. 22 7. Appendices ................................................................................................................................................................. 24
Appendix A. Insignificant Activities and General Applicable Requirements ............................................................ 24 Appendix B. Maximum Contents of Materials…………………………………………………………………………………………………….25
Permit issued: January 25, 2017 13900001- 004 Permit expires: January 25, 2022 Page 3 of 25
1. Permit applications table Subsequent permit applications: Title description Application receipt date Action number Notification of Replace of Unit 03/02/2011 13900001- 004 Part 70 Reissuance 05/03/2007 with supplemental
information received 07/13/16 and 08/19/16
13900001- 004
Permit issued: January 25, 2017 13900001- 004 Permit expires: January 25, 2022 Page 4 of 25
2. Where to send submittals
Send submittals that are required to be submitted to the U.S. EPA regional office to: Chief Air Enforcement Air and Radiation Branch EPA Region V 77 West Jackson Boulevard Chicago, Illinois 60604
Each submittal must be postmarked or received by the date specified in the applicable Table. Those submittals required by Minn. R. 7007.0100 to 7007.1850 must be certified by a responsible official, defined in Minn. R. 7007.0100, subp. 21. Other submittals shall be certified as appropriate if certification is required by an applicable rule or permit condition.
Send submittals that are required by the Acid Rain Program to:
U.S. Environmental Protection Agency Clean Air Markets Division 1200 Pennsylvania Avenue NW (6204N) Washington, D.C. 20460
Send any application for a permit or permit amendment to:
Fiscal Services – 6th Floor Minnesota Pollution Control Agency 520 Lafayette Road North St. Paul, Minnesota 55155-4194
Also, where required by an applicable rule or permit condition, send to the Permit Document Coordinator notices of:
a. Accumulated insignificant activities b. Installation of control equipment c. Replacement of an emissions unit, and d. Changes that contravene a permit term
Unless another person is identified in the applicable Table, send all other submittals to:
AQ Compliance Tracking Coordinator Industrial Division Minnesota Pollution Control Agency 520 Lafayette Road North St. Paul, Minnesota 55155-4194
Permit issued: January 25, 2017 13900001- 004 Permit expires: January 25, 2022 Page 5 of 25
3. Facility description
The Silgan Containers Mfg Corp - Savage (Facility) is located at 12130 Lynn Avenue South in Savage, Scott County, Minnesota. Silgan Containers Corporation (the Permittee) manufacturers two-piece cans, three-piece cans and can ends at its Savage facility. Steel coil is the raw material for the process and can be coated at this site or arrive at the plant precoated. Currently, the majority of the coil arrives at the facility coated and the decision to bring in uncoated or precoated steel coil is made based on the current market conditions. The coating is done to prevent corrosion, and when done at this plant, is a source of air emissions. There are no air emissions from the manufacturing of the two-piece cans. Air emissions from the manufacture of the three-piece cans are due primarily to the end seal compound which is used as an aid in developing a seal between the can end and the sidewall. The air emissions from this plant are primarily Volatile Organic Compounds (VOC) and Hazardous Air Pollutants (HAPs). VOC and HAP emissions from the coating lines are controlled by a catalytic oxidizer.
Permit issued: January 25, 2017 13900001- 004 Permit expires: January 25, 2022 Page 6 of 25
4. Summary of subject items
SI ID: Description
Relationship Type
Related SI ID: Description
ACTV3: Air Insignificant Activities
COMG1: VOC sources in Group Limit
has members
EQUI1, EQUI12, EQUI13, EQUI14, EQUI15, EQUI16, EQUI17, EQUI18, EQUI41, EQUI42
EQUI12: Washer - Gang Press - 211A
EQUI13: Washer -Gang Press - 300A
EQUI14: Washer -Gang Press - 300B
EQUI15: Washer -Gang Press - 300
EQUI16: Washer -Gang Press - 211B
EQUI17: Washer -Gang Press - 211C
EQUI18: Washer -Shell Press LIne (DRT)
EQUI1: Clean-up Solvents
EQUI38: Make-up Air Heater
EQUI39: Make-up Air Heater
EQUI41: Coating Line 3 (with oven)
EQUI42: Coating Line #2 (with oven)
EQUI43: Coating Line 3 oven - combustion
EQUI44: Coating Line 2 oven - combustion
EQUI8: Make-up Air Heater
EQUI9: Make-up
SI ID: Description
Relationship Type
Related SI ID: Description
Air Heater STRU10: Catalytic Oxidizer
receives from
EQUI41: Coating Line 3 (with oven)
STRU10: Catalytic Oxidizer
receives from
EQUI42: Coating Line #2 (with oven)
STRU10: Catalytic Oxidizer
receives from
EQUI43: Coating Line 3 oven - combustion
STRU10: Catalytic Oxidizer
receives from
EQUI44: Coating Line 2 oven - combustion
STRU12: Gang Press 5
receives from
EQUI16: Washer -Gang Press - 211B
STRU13: Gang Press 6
receives from
EQUI17: Washer -Gang Press - 211C
STRU14: Shell Press (DRT)
receives from
EQUI18: Washer -Shell Press LIne (DRT)
STRU21: Manufacturing Area
STRU22: Office Area
STRU6: Gang Press 1 - 4
receives from
EQUI12: Washer - Gang Press - 211A
STRU6: Gang Press 1 - 4
receives from
EQUI13: Washer -Gang Press - 300A
STRU6: Gang Press 1 - 4
receives from
EQUI14: Washer -Gang Press - 300B
STRU6: Gang Press 1 - 4
receives from
EQUI15: Washer -Gang Press - 300
STRU7: Oxy-Dry Waxer
TFAC1: Silgan Containers Mfg Corp - Savage
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 7 of 25
SI ID: Description
Relationship Type
Related SI ID: Description
TREA1: Catalytic Afterburner w/Heat Exchanger
controls EQUI41: Coating Line 3 (with oven)
TREA1: Catalytic Afterburner w/Heat Exchanger
controls EQUI42: Coating Line #2 (with oven)
TREA1: Catalytic Afterburner
controls EQUI43: Coating Line 3
SI ID: Description
Relationship Type
Related SI ID: Description
w/Heat Exchanger oven - combustion
TREA1: Catalytic Afterburner w/Heat Exchanger
controls EQUI44: Coating Line 2 oven - combustion
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 8 of 25
5. Limits and other requirements Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation TFAC 1 13900001 Silgan Containers
Mfg Corp - Savage
5.1.1 Permit Appendices: This permit contains appendices as listed in the permit Table of Contents. The Permittee shall comply with all requirements contained in Appendices A: Insignificant Activities and General Applicable Requirements and B: Maximum Contents of Materials. [Minn. R. 7007.0800, subp. 2]
5.1.2 PERMIT SHIELD: Subject to the limitations in Minn. R. 7007.1800, compliance with the conditions of this permit shall be deemed compliance with the specific provision of the applicable requirement identified in the permit as the basis of each condition. Subject to the limitations of Minn. R. 7007.1800 and 7017.0100, subp. 2, notwithstanding the conditions of this permit specifying compliance practices for applicable requirements, any person (including the Permittee) may also use other credible evidence to establish compliance or noncompliance with applicable requirements. This permit shall not alter or affect the liability of the Permittee for any violation of applicable requirements prior to or at the time of permit issuance. [Minn. R. 7007.1800, (A)(2)]
5.1.3 The Permittee shall comply with National Primary and Secondary Ambient Air Quality Standards, 40 CFR pt. 50, and the Minnesota Ambient Air Quality Standards, Minn. R. 7009.0010 to 7009.0080. Compliance shall be demonstrated upon written request by the MPCA. [Minn. R. 7007.0100, subp. 7(A), 7(L), & 7(M), Minn. R. 7007.0800, subp. 4, Minn. R. 7007.0800, subps. 1-2, Minn. Stat. 116.07, subd. 4a, Minn. Stat. 116.07, subd. 9]
5.1.4 Circumvention: Do not install or use a device or means that conceals or dilutes emissions, which would otherwise violate a federal or state air pollution control rule, without reducing the total amount of pollutant emitted. [Minn. R. 7011.0020]
5.1.5 Air Pollution Control Equipment: Operate all pollution control equipment whenever the corresponding process equipment and emission units are operated. [Minn. R. 7007.0800, subp. 16(J), Minn. R. 7007.0800, subp. 2]
5.1.6 Operation and Maintenance Plan: Retain at the stationary source an operation and maintenance plan for all air pollution control equipment. At a minimum, the O & M plan shall identify all air pollution control equipment and control practices and shall include a preventative maintenance program for the equipment and practices, a description of (the minimum but not necessarily the only) corrective actions to be taken to restore the equipment and practices to proper operation to meet applicable permit conditions, a description of the employee training program for proper operation and
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 9 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation maintenance of the control equipment and practices, and the records kept to demonstrate plan implementation. [Minn. R. 7007.0800, subp. 14, Minn. R. 7007.0800, subp. 16(J)]
5.1.7 Operation Changes: In any shutdown, breakdown, or deviation the Permittee shall immediately take all practical steps to modify operations to reduce the emission of any regulated air pollutant. The Commissioner may require feasible and practical modifications in the operation to reduce emissions of air pollutants. No emissions units that have an unreasonable shutdown or breakdown frequency of process or control equipment shall be permitted to operate. [Minn. R. 7019.1000, subp. 4]
5.1.8 Fugitive Emissions: Do not cause or permit the handling, use, transporting, or storage of any material in a manner which may allow avoidable amounts of particulate matter to become airborne. Comply with all other requirements listed in Minn. R. 7011.0150. [Minn. R. 7011.0150]
5.1.9 Noise: The Permittee shall comply with the noise standards set forth in Minn. R. 7030.0010 to 7030.0080 at all times during the operation of any emission units. This is a state only requirement and is not enforceable by the EPA Administrator or citizens under the Clean Air Act. [Minn. R. 7030.0010-7030.0080]
5.1.10 Inspections: The Permittee shall comply with the inspection procedures and requirements as found in Minn. R. 7007.0800, subp. 9(A). [Minn. R. 7007.0800, subp. 9(A)]
5.1.11 The Permittee shall comply with the General Conditions listed in Minn. R. 7007.0800, subp. 16. [Minn. R. 7007.0800, subp. 16]
5.1.12 Performance Testing: Conduct all performance tests in accordance with Minn. R. ch. 7017 unless otherwise noted in in this permit. [Minn. R. ch. 7017]
5.1.13 Performance Test Notifications and Submittals: Performance Tests are due as outlined in this permit. Performance Test Notification (written): due 30 days before each Performance Test Performance Test Plan: due 30 days before each Performance Test Performance Test Pre-test Meeting: due 7 days before each Performance Test Performance Test Report: due 45 days after each Performance Test Performance Test Report - Microfiche Copy: due 105 days after each Performance Test The Notification, Test Plan, and Test Report may be submitted in an alternative format as allowed by Minn. R. 7017.2018. [Minn. R. 7017.2018, Minn. R. 7017.2030, subps. 1-4, Minn. R. 7017.2035, subps. 1-2]
5.1.14 Limits set as a result of a performance test (conducted before or after permit issuance) apply until superseded as stated in
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 10 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation the MPCA's Notice of Compliance letter granting preliminary approval. Preliminary approval is based on formal review of a subsequent performance test on the same unit as specified by Minn. R. 7017.2025, subp. 3. The limit is final upon issuance of a permit amendment incorporating the change. [Minn. R. 7017.2025, subp. 3]
5.1.15 Monitoring Equipment Calibration - The Permittee shall either: 1. Calibrate or replace required monitoring equipment every 12 months; or 2. Calibrate at the frequency stated in the manufacturer's specifications. For each monitor, the Permittee shall maintain a record of all calibrations, including the date conducted, and any corrective action that resulted. The Permittee shall include the calibration frequencies, procedures, and manufacturer's specifications (if applicable) in the Operations and Maintenance Plan. Any requirements applying to continuous emission monitors are listed separately in this permit. [Minn. R. 7007.0800, subp. 4(D)]
5.1.16 Operation of Monitoring Equipment: Unless noted elsewhere in this permit, monitoring a process or control equipment connected to that process is not necessary during periods when the process is shutdown, or during checks of the monitoring systems, such as calibration checks and zero and span adjustments. If monitoring records are required, they should reflect any such periods of process shutdown or checks of the monitoring system. [Minn. R. 7007.0800, subp. 4(D)]
5.1.17 Recordkeeping: Retain all records at the stationary source, unless otherwise specified within this permit, for a period of five (5) years from the date of monitoring, sample, measurement, or report. Records which must be retained at this location include all calibration and maintenance records, all original recordings for continuous monitoring instrumentation, and copies of all reports required by the permit. Records must conform to the requirements listed in Minn. R. 7007.0800, subp. 5(A). [Minn. R. 7007.0800, subp. 5(C)]
5.1.18 Recordkeeping: Maintain records describing any insignificant modifications (as required by Minn. R. 7007.1250, subp. 3) or changes contravening permit terms (as required by Minn. R. 7007.1350, subp. 2), including records of the emissions resulting from those changes. [Minn. R. 7007.0800, subp. 5(B)]
5.1.19 If the Permittee determines that no permit amendment or notification is required prior to making a change, the Permittee must retain records of all calculations required under Minn. R. 7007.1200. For expiring permits, these records shall be kept for a period of five years from the date the change was made or until permit reissuance, whichever is longer. The records shall be kept at the stationary source for the current calendar year of operation and may be kept at the
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 11 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation stationary source or office of the stationary source for all other years. The records may be maintained in either electronic or paper format. [Minn. R. 7007.1200, subp. 4]
5.1.20 Shutdown Notifications: Notify the Commissioner at least 24 hours in advance of a planned shutdown of any control equipment or process equipment if the shutdown would cause any increase in the emissions of any regulated air pollutant. If the owner or operator does not have advance knowledge of the shutdown, notification shall be made to the Commissioner as soon as possible after the shutdown. However, notification is not required in the circumstances outlined in Items A, B and C of Minn. R. 7019.1000, subp. 3. At the time of notification, the owner or operator shall inform the Commissioner of the cause of the shutdown and the estimated duration. The owner or operator shall notify the Commissioner when the shutdown is over. [Minn. R. 7019.1000, subp. 3]
5.1.21 Breakdown Notifications: Notify the Commissioner within 24 hours of a breakdown of more than one hour duration of any control equipment or process equipment if the breakdown causes any increase in the emissions of any regulated air pollutant. The 24-hour time period starts when the breakdown was discovered or reasonably should have been discovered by the owner or operator. However, notification is not required in the circumstances outlined in Items A, B and C of Minn. R. 7019.1000, subp. 2. At the time of notification or as soon as possible thereafter, the owner or operator shall inform the Commissioner of the cause of the breakdown and the estimated duration. The owner or operator shall notify the Commissioner when the breakdown is over. [Minn. R. 7019.1000, subp. 2]
5.1.22 Notification of Deviations Endangering Human Health or the Environment: As soon as possible after discovery, notify the Commissioner or the state duty officer, either orally or by facsimile, of any deviation from permit conditions which could endanger human health or the environment. [Minn. R. 7019.1000, subp. 1]
5.1.23 Notification of Deviations Endangering Human Health or the Environment Report: Within 2 working days of discovery, notify the Commissioner in writing of any deviation from permit conditions which could endanger human health or the environment. Include the following information in this written description: 1. the cause of the deviation; 2. the exact dates of the period of the deviation, if the deviation has been corrected; 3. whether or not the deviation has been corrected; 4. the anticipated time by which the deviation is expected to be corrected, if not yet corrected; and 5. steps taken or planned to reduce, eliminate, and prevent
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 12 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation reoccurrence of the deviation. [Minn. R. 7019.1000, subp. 1]
5.1.24 Application for Permit Amendment: If a permit amendment is needed, submit an application in accordance with the requirements of Minn. R. 7007.1150 through Minn. R. 7007.1500. Submittal dates vary, depending on the type of amendment needed. Upon adoption of a new or amended federal applicable requirement, and if there are more than 3 years remaining in the permit term, the Permittee shall file an application for an amendment within nine months of promulgation of the applicable requirement, pursuant to Minn. R. 7007.0400, subp. 3. [Minn. R. 7007.0400, subp. 3, Minn. R. 7007.1150 - 7007.1500]
5.1.25 Extension Requests: The Permittee may apply for an Administrative Amendment to extend a deadline in a permit by no more than 120 days, provided the proposed deadline extension meets the requirements of Minn. R. 7007.1400, subp. 1(H). Performance testing deadlines from the General Provisions of 40 CFR pt. 60 and pt. 63 are examples of deadlines for which the MPCA does not have authority to grant extensions and therefore do not meet the requirements of Minn. R. 7007.1400, subp. 1(H). [Minn. R. 7007.1400, subp. 1(H)]
5.1.26 Emission Inventory Report: due on or before April 1 of each calendar year following permit issuance, to be submitted on a form approved by the Commissioner. [Minn. R. 7019.3000-7019.3100]
5.1.27 Emission Fees: due 30 days after receipt of an MPCA bill. [Minn. R. 7002.0005-7002.0095]
5.1.28 This permit establishes limits on the facility to keep it a minor source under New Source Review and NESHAPS. The Permittee cannot make any change at the source that would make the source a major source under New Source Review and NESHAPS until a permit amendment has been issued. This includes changes that might otherwise qualify as insignificant modifications and minor or moderate amendments. [Title I Condition: Avoid major modification under 40 CFR 52.21(b)(2) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 63.2]
5.1.29 Equipment Labeling: The Permittee shall permanently affix a unique number to each emissions unit for tracking purposes. The numbers shall correlate the unit to the appropriate Subject Item numbers used in this permit. The number can be affixed by placard, stencil, or other means. The number shall be maintained so that it is readable and visible at all times from a safe distance. If equipment is added, it shall be given a new unique number; numbers from replaced or removed equipment shall not be reused. [Minn. R. 7007.0800, subp. 2]
5.1.30 Equipment Inventory: The Permittee shall maintain a written
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 13 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation list of all emissions units and control equipment on site. The Permittee shall update the list to include any replaced, modified, or new equipment prior to making the change. The list shall correlate the units to the Subject Item numbers used in this permit and shall include the data on GI-04, GI-05B, and GI-05C. The date of construction shall be the date the change was made for replaced, modified, or new equipment. [Minn. R. 7007.0800, subp. 2]
COMG 1 GP001 VOC sources in
Group Limit
5.2.1 The Permittee shall limit emissions of Volatile Organic Compounds <= 240 tons per year 12-month rolling sum to be calculated by the 15th day of each month for the previous 12-month period as described later in this permit. All VOC-emitting equipment at the Facility is subject to this limit except for the following: natural gas combustion equipment and insignificant activities. If the Permittee replaces any existing VOC-emitting equipment, adds new VOC-emitting equipment, or modifies the existing equipment, such equipment is subject to this permit limit as well as all of the requirements COMG 1. Prior to making such a change, the Permittee shall apply for and obtain the appropriate permit amendment, as applicable. The Permittee is not required to complete VOC calculations described in Minn. R. 7007.1200, subp. 2. A permit amendment will still be needed regardless of the emissions increase if the change will be subject to a new applicable requirement or requires revisions to the limits or monitoring and recordkeeping in this permit. VOC contents for each VOC-containing material shall be determined as described under the Material Content requirement in COMG 1. The calculation of VOCs used may take into account recovered/recycled VOCs as described under the Waste Credit requirement in COMG 1. [Title I Condition: Avoid major modification under 40 CFR 52.21(b)(2) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
5.2.2 The Permittee shall limit emissions of HAPs - Single <= 9 tons per year 12-month rolling sum to be calculated by the 15th day of each month for the previous 12-month period. All HAP-emitting equipment at the Facility is covered by this limit except for the following: natural gas combustion equipment and insignificant activities. If the Permittee replaces any existing HAP-emitting equipment or adds new HAP-emitting equipment, such equipment is subject to this permit limit as well as all of the requirements of COMG 1. Prior to making such a change, the Permittee shall apply for and obtain the appropriate permit amendment, as applicable. A
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 14 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation permit amendment may be needed if the change will be subject to a new applicable requirement or requires revisions to limits or the monitoring and recordkeeping in this permit. HAP contents for each HAP-containing material shall be determined as described under the Material Content requirement in COMG 1. The calculation of HAPs used may take into account recovered/recycled HAPs as described under the Waste Credit requirement in COMG 1. [Title I Condition: Avoid major source under 40 CFR 63.2]
5.2.3 The Permittee shall limit emissions of HAPs - Total <= 23 tons per year 12-month rolling sum to be calculated by the 15th day of each month for the previous 12-month period. All HAP-emitting equipment at the Facility is covered by this limit except for the following: natural gas combustion equipment and insignificant activities. If the Permittee replaces any existing HAP-emitting equipment or adds new HAP-emitting equipment, such equipment is subject to this permit limit as well as all of the requirements of COMG 1. Prior to making such a change, the Permittee shall apply for and obtain the appropriate permit amendment, as applicable. A permit amendment may be needed if the change will be subject to a new applicable requirement or requires revisions to limits or the monitoring and recordkeeping in this permit. HAP contents for each HAP-containing material shall be determined as described under the Material Content requirement in COMG 1. The calculation of HAPs used may take into account recovered/recycled HAPs as described under the Waste Credit requirement in COMG 1. [Title I Condition: Avoid major source under 40 CFR 63.2]
5.2.4 Daily Recordkeeping. On each day of operation, the Permittee shall calculate, record, and maintain the total quantity of all coatings and other VOC and HAP-containing materials used at the facility. This shall be based on written usage logs. [Title I Condition: Avoid major modification under 40 CFR 52.21(b)(2) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 63.2]
5.2.5 Volatile Organic Compounds: Monthly Recordkeeping -- VOC Emissions. By the 15th of the month, the Permittee shall calculate and record the following: 1) The total usage of VOC-containing materials for the previous calendar month using the daily usage records. This record shall also include the VOC and solids contents of each material as determined by the Material Content requirement of this permit; 2) The VOC emissions for the previous month using the formulas specified in this permit; and 3) The 12-month rolling sum VOC emissions for the previous
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 15 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation 12-month period by summing the monthly VOC emissions data for the previous 12 months. [Minn. R. 7007.0800, subps. 4-5]
5.2.6 Volatile Organic Compounds: Monthly Calculation -- VOC Emissions. The Permittee shall calculate VOC emissions using the following equations: VOC (tons/month) = (V1 - W1) x (1-Ce) + (V2-W2) V# = (A1 x B1) + (A2 x B2) + (A3 x B3) + ..... W #= (C1 x D1) + (C2 x D2) + (C3 x D3) + ..... where: V1 = total VOC used in tons/month in emissions units that vent to the catalytic oxidizer; V2 = total VOC used in tons/month in emissions units that do not vent to the catalytic oxidizer; A# = amount of each VOC-containing material used, in tons/month; B# = weight percent VOC in A#, as a fraction; W1 = the amount of VOC collected from equipment that vents to the oxidizer that is shipped in waste, in tons/month; W2 = the amount of VOC collected from equipment that does not vent to the oxidizer that is shipped in waste, in tons/month; C# = amount, in tons/month, of each VOC-containing waste material shipped. If the Permittee chooses to not take credit for waste shipments, this parameter would be zero; D# = weight percent of VOC in C#, as a fraction; and Ce = Control efficiency of catalytic oxidizer, 95%. [Minn. R. 7007.0800, subps. 4-5]
5.2.7 HAPs: Monthly Recordkeeping. By the 15th of the month, the Permittee shall calculate and record the following using the formulas specified in this permit: 1) The total HAP-containing materials used in the previous calendar month using the daily usage records. This record shall also include the individual and total HAP contents of each HAP-containing material used in the previous month, as determined by the Material Content requirement of this permit; 2) The total and individual HAP emissions for the previous month using the formulas specified in this permit; and 3) The 12-month rolling sum total and individual HAP emissions for the previous 12-month period by summing the monthly emissions data for the previous 12 months. [Minn. R. 7007.0800, subps. 4-5]
5.2.8 HAPs: Monthly Calculation -- HAP Emissions. The Permittee shall calculate each individual HAP and total HAP emissions using the following equations: HAP Emissions (tons/month) = (H1 - W1) x (1-Ce) + (H2-W2) H# = (A1 x B1) + (A2 x B2) + (A3 x B3) + .... W# = (C1 x D1) + (C2 x D2) + (C3 x D3) + ....
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 16 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation Where: H1 = the amount of each pollutant (either total HAP or each individual HAP), used, in tons/month in emissions units that vent to the catalytic oxidizer; H2 = the amount of each pollutant (either total HAP or each individual HAP), used, in tons/month in emissions units that do not vent to the catalytic oxidizer; A# = Amount of each HAP-containing material used in the previous month, in tons/month; B# = weight percent of each individual or total HAP in A#, as a fraction (e.g., 50% is 0.50); W1 = the amount of each pollutant (either total HAP or each individual HAP) collected from equipment that vents to the oxidizer that is shipped in waste, in tons/month; W2 = the amount of each pollutant (either total HAP or each individual HAP) collected from equipment that does not vent to the oxidizer that is shipped in waste, in tons/month; C# = amount, in tons/month, of each HAP-containing waste material shipped. If the Permittee chooses to not take credit for waste shipments, this parameter would be zero; D# = weight percent of each individual or total HAP in C#, as a fraction; and Ce = Control efficiency of catalytic oxidizer, 95%. [Minn. R. 7007.0800, subps. 4-5]
5.2.9 Maximum Contents of Materials: The Permittee assumed certain worst-case contents of materials when determining the short term potential to emit of units in COMG 1. These assumptions are listed in Appendix B of this permit. Changing to a material that has a higher content of any of the given pollutants is considered a change in method of operation that must be evaluated under Minn. R. 7007.1200, subp. 3 to determine if a permit amendment or notification is required under Minn. R. 7007.1150. [Minn. R. 7005.0100, subp. 35a]
5.2.10 Waste Credit: If the Permittee elects to obtain credit for HAPs and/or VOC shipped in waste materials, the Permittee shall either use item 1 or 2 to determine the VOC and/or total and individual HAP content for each credited shipment. 1) The Permittee shall analyze a composite sample of each waste shipment to determine the weight content of VOC, total HAP, and each individual HAP, excluding water. 2) The Permittee may use supplier data for raw materials to determine the VOC and total and individual HAP contents of each waste shipment, using the same content data used to determine the content of raw materials. If the waste contains several materials, the content of mixed waste shall be assumed to be the lowest VOC and total and individual HAP content of any of the materials. [Minn. R. 7007.0800, subps. 4-5]
5.2.11 Material Content. VOC and HAPs contents in coating materials
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Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation shall be determined by the Safety Data Sheet (SDS) or the Material Safety Data Sheet (MSDS) provided by the supplier for each material used. If a material content range is given on the SDS or the MSDS, the highest number in the range shall be used in all compliance calculations. If there is information provided in the Regulatory Section of the SDS, the highest number in the range of that section may be used. Other alternative methods approved by the MPCA may be used to determine the VOC and HAP contents. The Commissioner reserves the right to require the Permittee to determine the VOC and HAP contents of any material, according to EPA or ASTM reference methods. If an EPA or ASTM reference method is used for material content determination, the data obtained shall supersede the SDS or the MSDS. [Minn. R. 7007.0800, subps. 4-5]
EQUI 8 EU020 Make-up Air
Heater
5.3.1 Total Particulate Matter <= 0.40 pounds per million Btu heat input The potential to emit from the unit is 0.01 lb/MMBtu due to equipment design and allowable fuels. [Minn. R. 7011.0515, subp. 1]
5.3.2 Opacity <= 20 percent opacity except for one six-minute period per hour of not more than 60 percent opacity. [Minn. R. 7011.0515, subp. 2]
5.3.3 Fuel Type: Natural gas only. [Minn. R. 7005.0100, subp. 35a] 5.3.4 The Permittee shall keep records of fuel type on a monthly
basis. [Minn. R. 7007.0800, subps. 4&5] EQUI 9 EU021 Make-up Air
Heater
5.4.1 Total Particulate Matter <= 0.40 pounds per million Btu heat input The potential to emit from the unit is 0.01 lb/MMBtu due to equipment design and allowable fuels. [Minn. R. 7011.0515, subp. 1]
5.4.2 Opacity <= 20 percent opacity except for one six-minute period per hour of not more than 60 percent opacity. [Minn. R. 7011.0515, subp. 2]
5.4.3 Fuel Type: Natural gas only. [Minn. R. 7005.0100, subp. 35a] 5.4.4 The Permittee shall keep records of fuel type on a monthly
basis. [Minn. R. 7007.0800, subps. 4&5] EQUI 38 EU026 Make-up Air
Heater
5.5.1 Total Particulate Matter <= 0.40 pounds per million Btu heat input The potential to emit from the unit is 0.008 lb/MMBtu due to equipment design and allowable fuels. [Minn. R. 7011.0515, subp. 1]
5.5.2 Opacity <= 20 percent opacity except for one six-minute period per hour of not more than 60 percent opacity. [Minn. R. 7011.0515, subp. 2]
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Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation 5.5.3 Fuel Type: Natural gas only. [Minn. R. 7005.0100, subp. 35a] 5.5.4 The Permittee shall keep records of fuel type on a monthly
basis. [Minn. R. 7007.0800, subps. 4&5] EQUI 39 EU027 Make-up Air
Heater
5.6.1 Total Particulate Matter <= 0.40 pounds per million Btu heat input The potential to emit from the unit is 0.008 lb/MMBtu due to equipment design and allowable fuels. [Minn. R. 7011.0515, subp. 1]
5.6.2 Opacity <= 20 percent opacity except for one six-minute period per hour of not more than 60 percent opacity. [Minn. R. 7011.0515, subp. 2]
5.6.3 Fuel Type: Natural gas only. [Minn. R. 7005.0100, subp. 35a] 5.6.4 The Permittee shall keep records of fuel type on a monthly
basis. [Minn. R. 7007.0800, subps. 4&5] EQUI 41 EU004 Coating Line 3
(with oven)
5.7.1 The Permittee shall vent emissions from EQUI 41 to control equipment meeting the requirements of TREA 1 whenever EQUI 41 operates. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
EQUI 42 EU025 Coating Line #2
(with oven)
5.8.1 The Permittee shall vent emissions from EQUI 42 to control equipment meeting the requirements of TREA 1 whenever EQUI 42 operates. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
EQUI 43 EU006 Coating Line 3
oven - combustion
5.9.1 Total Particulate Matter <= 0.30 grains per dry standard cubic foot of exhaust gas unless required to further reduce emissions to comply with the less stringent limit of either Minn. R. 7011.0730 or Minn. R. 7011.0735. [Minn. R. 7011.0610, subp. 1(A)(1)]
5.9.2 Opacity <= 20 percent opacity except for one six-minute period per hour of not more than 60 percent opacity. [Minn. R. 7011.0610, subp. 1(A)(2)]
5.9.3 Fuel Type: Natural gas with propane as a back-up. [Minn. R. 7005.0100, subp. 35a]
5.9.4 The Permittee shall keep records of fuel type on a monthly basis. [Minn. R. 7007.0800, subps. 4&5]
5.9.5 The Permittee shall vent emissions from EQUI 43 to control equipment meeting the requirements of TREA 1 whenever EQUI 43 operates. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
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Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation EQUI 44 EU003 Coating Line 2
oven - combustion
5.10.1 Total Particulate Matter <= 0.30 grains per dry standard cubic foot of exhaust gas unless required to further reduce emissions to comply with the less stringent limit of either Minn. R. 7011.0730 or Minn. R. 7011.0735. [Minn. R. 7011.0610, subp. 1(A)(1)]
5.10.2 Opacity <= 20 percent opacity except for one six-minute period per hour of not more than 60 percent opacity. [Minn. R. 7011.0610, subp. 1(A)(2)]
5.10.3 Fuel Type: Natural gas with propane as a back-up. [Minn. R. 7005.0100, subp. 35a]
5.10.4 The Permittee shall keep records of fuel type on a monthly basis. [Minn. R. 7007.0800, subps. 4&5]
5.10.5 The Permittee shall vent emissions from EQUI 44 to control equipment meeting the requirements of TREA 1 whenever EQUI 44 operates. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
TREA 1 CE003 Catalytic
Afterburner w/Heat Exchanger
5.11.1 The Permittee shall operate and maintain control equipment such that it achieves an overall control efficiency for Volatile Organic Compounds >= 95 percent control efficiency. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
5.11.2 Temperature >= 674 degrees Fahrenheit 3-hour rolling average at the oxidizer inlet as determined during the December 8, 2015 performance test, unless a new limit is set pursuant to Minn. R. 7017.2025, subp. 3 based on the values recorded during the most recent MPCA-approved performance test where compliance was demonstrated. The new limit shall be implemented upon receipt of the Notice of Compliance letter granting preliminary approval. The limit is final upon issuance of a permit amendment incorporating the change. If the 3-hour rolling average temperature is below the minimum inlet temperature limit, the VOC used during that time shall be considered uncontrolled until the average inlet temperature is above the minimum temperature limit. This shall be reported as a deviation. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
5.11.3 Total Particulate Matter <= 0.30 grains per dry standard cubic foot of exhaust gas unless required to further reduce emissions to comply with the less stringent limit of either Minn. R. 7011.0730 or Minn. R. 7011.0735. [Minn. R. 7011.0610, subp. 1(A)(1)]
5.11.4 Opacity <= 20 percent opacity except for one six-minute period per hour of not more than 60 percent opacity. [Minn. R.
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Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation 7011.0610, subp. 1(A)(2)]
5.11.5 The Permittee shall vent emissions from EQUI 41, EQUI 42, EUQI 43, and EQUI 44 to TREA 1 whenever EQUI 41, EQUI 42, EQUI 43, and EQUI 44 operate, and operate and maintain TREA 1 at all times that any emissions are vented to TREA 1. The Permittee shall document periods of non-operation of the control equipment TREA 1 whenever EQUI 41, EQUI 42, EQUI 43, and EQUI 44 are operating. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
5.11.6 The Permittee shall operate and maintain the catalytic oxidizer in accordance with the Operation and Maintenance (O & M) Plan. The Permittee shall keep copies of the O & M Plan available onsite for use by staff and MPCA staff. [Minn. R. 7007.0800, subp. 14]
5.11.7 Documentation of Need for Improved Monitoring: If the Permittee fails to achieve compliance with an emission limitation or standard for which the monitoring did not provide an indication of an excursion or exceedance while providing valid data, or the results of compliance or performance testing document a need to modify the existing pressure drop range, the Permittee shall promptly notify the MPCA and, if necessary, submit a permit amendment application to address the necessary monitoring change. [40 CFR 64.7(e), Minn. R. 7017.0200]
5.11.8 As required by 40 CFR Section 64.9(a)(2), for the Semi-Annual Deviations Report required by this permit and/or the Notification of Deviations Endangering Human Health and the Environment required by this permit, as applicable, the Permittee shall include the following related to the monitoring identified as required by 40 CFR pt. 64: 1) Summary information on the number, duration, and cause of excursions or exceedances, as applicable, and the corrective action taken; and 2) Summary information on the number, duration, and cause for monitor downtime incidents. [40 CFR 64.9(a)(2), Minn. R. 7017.0200]
5.11.9 The Permittee shall maintain records of monitoring data, monitor performance data, corrective actions taken, and other supporting information required to be maintained. The Permittee may maintain records on alternative media, such as microfilm, computer files, magnetic tape disks, or microfiche, provided that the use of such alternative media allows for expeditious inspection and review, and does not conflict with other applicable recordkeeping requirements. [40 CFR 64.9(b), Minn. R. 7017.0200]
5.11.10 The Permittee shall maintain and operate a thermocouple monitoring device that continuously indicates and records both the inlet and outlet temperatures of the catalytic oxidizer. The monitoring device shall have a margin of error less than the greater of +/- 0.75 percent of the temperature being measured or +/- 2.5 degrees Celsius. The recording device shall also calculate the three-hour rolling average inlet
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Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation temperature. [40 CFR 64.7(b), Minn. R. 7017.0200, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
5.11.11 Daily Monitoring: The Permittee shall physically verify the operation of the temperature recording device at least once every 24 hours to verify that it is working and recording properly. The Permittee shall maintain a written record of the daily verifications. [40 CFR 64.3, Minn. R. 7017.0200, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 63.2]
5.11.12 Monitoring Equipment: The Permittee shall install and maintain thermocouples to conduct temperature monitoring required by this permit. The monitoring equipment must be installed, in use, and properly maintained whenever operation of the monitored control equipment is required. [40 CFR 64.7, Minn. R. 7007.0800, subps. 4-5]
5.11.13 The Permittee shall maintain a continuous hard copy readout or computer disk file of the temperature readings and calculated three hour rolling average temperatures at the inlet to the combustion chamber. [40 CFR 64.3, Minn. R. 7017.0200, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
5.11.14 Annual Calibration: The Permittee shall calibrate the temperature monitor at least once every 12 months and shall maintain a written record of the calibration and any action resulting from the calibration. [40 CFR 64.3, Minn. R. 7017.0200]
5.11.15 Monthly Monitoring: At least once each month during normal operation, the Permittee shall record the temperature rise across the catalyst (outlet temp. - inlet temp.) while the process is running. If it is determined that the catalyst reactivity has been impaired, by comparison of the observed temperature rise to the past temperature rise records, the Permittee shall follow the corrective actions in the Operation and Maintenance Plan. The Permittee shall maintain written records of the monitoring and any corrective actions taken. [40 CFR 64.3, Minn. R. 7007.0800, subp. 5]
5.11.16 Quarterly Inspections: At least once per calendar quarter, the Permittee shall inspect the control equipment internal and external system components, including but not limited to the refractory, heat exchanger, and electrical systems. The Permittee shall maintain a written record of the inspection and any corrective actions taken resulting from the inspection. [Minn. R. 7007.0800, subp. 14, Minn. R. 7007.0800, subp. 4, Minn. R. 7007.0800, subp. 5]
5.11.17 Annual Inspection: At least once per calendar year, the Permittee shall conduct an internal inspection of the control device that includes all operating systems of the control device. The Permittee shall maintain a written record of the inspection and any action resulting from the inspection. [Minn.
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Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation R. 7007.0800, subp. 14, Minn. R. 7007.0800, subp. 4, Minn. R. 7007.0800, subp. 5]
5.11.18 For periods when the catalytic oxidizer is operated above the minimum inlet temperature, the Permittee shall use either one of the following when completing calculations as required elsewhere in this permit: a. The overall control efficiency limit specified in this permit for this equipment; or b. The overall control efficiency determined during the most recent MPCA approved performance test. If the tested efficiency is less than the efficiency limit in this permit, the Permittee must use the tested value in all calculations until the efficiency is demonstrated to be above the permit limit through a new test. [Minn. R. 7007.0800, subps. 4-5, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 63.2]
5.11.19 Corrective Actions: If the temperature is below the minimum specified by this permit or if the catalytic oxidizer or any of its components are found during the inspections to need repair, the Permittee shall take corrective action as soon as possible. Corrective actions shall return the temperature to at least the permitted minimum and/or include completion of necessary repairs identified during the inspection, as applicable. Corrective actions include, but are not limited to, those outlined in the O & M Plan for the catalytic oxidizer. The Permittee shall keep a record of the type and date of any corrective action taken. [40 CFR 64.7(d), Minn. R. 7017.0200]
5.11.20 The Permittee shall operate and maintain control equipment such that it achieves an overall control efficiency for HAPs - Total >= 95 percent control efficiency. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
5.11.21 The Permittee shall operate and maintain control equipment such that it achieves an overall control efficiency for HAPs - Single >= 95 percent control efficiency. [Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
6. Submittal/action requirements
This section lists most of the submittals required by this permit. Please note that some submittal requirements may appear in the Limits and Other Requirements section, or, if applicable, within a Compliance Schedule section.
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation TFAC 1 13900001 Silgan Containers
Mfg Corp -
Permit Issued: January 25, 2017 13900001- 004 Permit Expires: January 25, 2022 Page 23 of 25
Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation Savage
6.1.1 The Permittee shall submit an application for permit reissuance : Due 180 calendar days before Permit Expiration Date. [Minn. R. 7007.0400, subp. 2]
6.1.2 The Permittee shall submit a semiannual deviations report : Due semiannually, by the 30th of January and July The first semiannual report submitted by the Permittee shall cover the calendar half-year in which the permit is issued. The first report of each calendar year covers January 1 - June 30. The second report of each calendar year covers July 1 - December 31. If no deviations have occurred, the Permittee shall submit the report stating no deviations. [Minn. R. 7007.0800, subp. 6(A)(2)]
6.1.3 The Permittee shall submit a compliance certification : Due annually, by the 31st of January (for the previous calendar year). The Permittee shall submit this to the Commissioner on a form approved by the Commissioner. This report covers all deviations experienced during the calendar year. [Minn. R. 7007.0800, subp. 6(C)]
6.1.4 The Permittee shall submit an annual report : Due annually, by the 31st of January The report shall describe the changes made at the Facility during the previous calendar year using the latest MPCA application forms. The report shall include information for any new or replaced Subject Items. The report shall document the VOC, Single HAP, and Total HAP 12-month rolling sum calculations for the previous calendar year. The report shall be submitted with the annual Compliance Certification required by this permit. As part of the Annual Report, the Permittee shall verify and certify that the Facility has maintained minor source status for New Source Review. [Minn. R. 7007.0800, subp. 2]
TREA 1 CE003 Catalytic
Afterburner w/Heat Exchanger
6.2.1 The Permittee shall submit sample analysis : Due every 24 months. The Permittee shall send a representative sample of the catalyst to a laboratory to test the catalyst's destruction efficiency. If test results show a destruction efficiency of less than 95%, the Permittee shall follow the corrective actions contained in the Operation and Maintenance Plan. [Minn. R. 7007.0800, subps. 4-5, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
6.2.2 Volatile Organic Compounds : The Permittee shall conduct a performance test : Due before 12/20/2020 every 60 months thereafter to verify VOC control efficiency. The first test is due by the date specified and all subsequent tests are due by the end of each 60-month period following that date. The performance test shall be conducted at worst case conditions as defined at Minn. R. 7017.2025, subp. 2, using EPA Reference Method 25A, or other method approved by MPCA in the performance test plan approval.
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Subject Item Sec.SI.Reqt SI des:SI desc Requirement & Citation Testing conducted during the 60 days prior to the performance test due date satisfies the performance test due date, and will not reset the test due date for future testing as required: 1) by this permit; 2) by the most recently approved Performance Test Frequency Plan; or 3) within a Notice of Compliance letter. Testing conducted more than two months prior to the performance test due date satisfies this test due date requirement and will reset the performance test due date. [Minn. R. 7017.2020, subp. 1, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000]
7. Appendices
Appendix A. Insignificant Activities and General Applicable Requirements The table below lists the insignificant activities that are currently at the Facility and their associated general applicable requirements.
Minn. R. Rule description of the activity General applicable requirement Minn. R. 7007.1300, subp. 3(B)(1) Infrared electric ovens Opacity <= 20% (Minn. R. 7011.0105 or
7011.0110) Minn. R. 7007.1300, subp. 3(E)(2) Nonhazardous air pollutant VOC storage
tanks with total capacity not more than 10,000 gallons meeting certain vapor pressure requirements There are 5 individual tanks with a total storage capacity of less than 9,000 gallons.
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0710/0715)
Minn. R. 7007.1300, subp. 3(H)(3) Brazing, soldering or welding equipment PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0710/0715)
Minn. R. 7007.1300, subp. 3(H)(4) Blueprint copiers and photographic processes
Opacity <= 20% (Minn. R. 7011.0105 or 7011.0110)
Minn. R. 7007.1300, subp. 3(H)(5) Equipment used exclusively for melting or application of wax
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0710/0715)
Minn. R. 7007.1300, subp. 3(H)(7) Cleaning operations: alkaline/phosphate cleaners and associated cleaners and associated burners
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0610 & Minn. R. 7011.0710/0715)
Minn. R. 7007.1300, subp. 3(I) Individual units with potential emissions less than 2000 lb/year of certain pollutants These are 2 furnaces and 14 space heaters (total heat input is 0.725 MMBtu/hr that burn natural gas. There are also 2 videojet
PM ≤ 0.6 or 0.4 lb/MMBtu, depending on year constructed Opacity ≤ 20% with exceptions (Minn. R. 7011.0510/0515)
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Minn. R. Rule description of the activity General applicable requirement printers that have minimal methanol emissions.
Minn. R. 7007.1300, subp. 3(J) Fugitive dust emissions from unpaved entrance roads and parking lots
Requirement to take reasonable measures to prevent PM from becoming airborne (Minn. R. 7011.0150)
Minn. R. 7007.1300, subp. 3(K) Infrequent use of spray paint equipment for routine housekeeping or plant upkeep activities not associated with primary production processes at the stationary source
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0710/0715)
Appendix B. Maximum Contents of Materials The maximum capacity of each coating line and can liner is given in the table below for the specified unit. The units that apply coatings to the can ends (presses) are broken down into the separate steps that occur within each unit. Changing to a material with a higher VOC content is considered a change in method of operation that must be evaluated under Minn. R. 7007.1200, subp. 3 to determine if a permit amendment or notification is required.
Emission Unit (EQUI)
Maximum Application Rate (gallons coating/hr unless otherwise noted)
Maximum VOC Content, as applied (lb/gallon)
Presses 12 (Liner) 2.59 3.59
12 (Mister) 0.11 (lb/hr) 6.84 12 (Lubricator) 0.72 6.84
13 (Liner) 2.75 3.59 13 (Mister) 0.11 (lb/hr) 6.84
13 (Lubricator) 0.72 (lb/hr) 6.84 14 (Liner) 2.75 3.59
14 (Mister) 0.11 (lb/hr) 6.84 14 (Lubricator) 0.72 (lb/hr) 6.84
15 (Liner) 2.86 3.59 15 (Mister) 0.08 6.30
15 (Lubricator) 0.72 (lb/hr) 6.84 16 (Liner) 2.59 3.59
16 (Mister) 0.11 (lb/hr) 6.84 16 (Lubricator) 0.72 (lb/hr) 6.84
17 (Liner) 2.59 3.59 17 (Mister) 0.11 (lb/hr) 6.84 18 (Liner) 4.77 3.59
18 (Mister) 0.50 (lb/hr) 6.30 Coating Lines
41 53.3 5.91 42 53.3 5.91
Technical Support Document, Permit Number: 13900001- 004 Page 1 of 10
Technical Support Document
For Air Emission Permit No. 13900001- 004
This technical support document (TSD) is intended for all parties interested in the permit and to meet the requirements that have been set forth by the federal and state regulations (40 CFR § 70.7(a)(5) and Minn. R. 7007.0850, subp. 1). The purpose of this document is to provide the legal and factual justification for each applicable requirement or policy decision considered in the determination to issue the permit. 1. General information
1.1 Applicant and stationary source location Table 1. Applicant and source address
Applicant/Address Stationary source/Address (SIC Code: 3411 - Metal Cans)
Tim White 1190 Corporate Center Dr Oconomowoc, Wisconsin 53066
Silgan Containers Mfg Corp - Savage 12130 Lynn Ave S Savage MN 55378
Contact: Tim White Phone: 262-569-5848
1.2 Facility description
Silgan Containers Corporation (the Permittee) manufacturers two-piece cans, three-piece cans and can ends at its Savage facility. Steel coil is the raw material for the process and can be coated at this site or arrive at the plant precoated. Currently, the majority of the coil arrives at the facility coated and the decision to bring in uncoated or precoated steel coil is made based on the current market conditions. The coating is done to prevent corrosion, and when done at this plant, is a source of air emissions. There are no air emissions from the manufacturing of the two-piece cans. Air emissions from the manufacture of the three-piece cans are due primarily to the end seal compound which is used as an aid in developing a seal between the can end and the sidewall. The air emissions from this plant are primarily Volatile Organic Compounds (VOC) and Hazardous Air Pollutants (HAPs). VOC and HAP emissions from the coating lines are controlled by a catalytic oxidizer.
1.3 Description of the activities allowed by this permit action
This permit action is Part 70 Reissuance. No changes are authorized under this permit action. This action incorporates a reopening from 2006 to amend the minimum temperature for the oxidizer and a notification of replacement for two air makeup units. The new air makeup units qualify as insignificant activities and have been added to the insignificant activity list.
1.4 Description of notifications and applications included in this action
Table 2. Notifications and applications included in this action
Date received Application/Notification type and description 03/02/2011 Notification of Replacement of Unit – IND20110001 05/03/2007 Part 70 Permit Reissuance – IND20070001
Technical Support Document, Permit Number: 13900001- 004 Page 2 of 10
Date received Application/Notification type and description 09/13/2006 Permit Reopening – IND20060001
1.5 Facility emissions
Table 2. Total facility potential to emit summary
PM tpy
PM10 tpy
PM2.5 tpy
SO2 tpy
NOx tpy
CO tpy
CO2e tpy
VOC tpy
Single HAP tpy
All HAPs tpy
Total facility limited potential emissions 1.57 1.57 1.57 0.12 20.6 17.3
2.49E+04 241 9.37 23.4
Total facility actual emissions (2105) 0.007 0.007 0.004 0.021 3.44 2.88 * 165 *
*Not reported in Minnesota emission inventory. Table 3. Facility classification
Classification Major Synthetic minor/area Minor/Area New Source Review X Part 70 X Part 63 X
1.6 Changes to permit The permit does not authorize any specific modifications, however, the MPCA has a combined operating and construction permitting program under Minnesota Rules Chapter 7007, and under Minn. R. 7007.0800, the MPCA has authority to include additional requirements in a permit. Under that authority, the following changes to the permit are also made through this permit action: · The permit has been updated to reflect current MPCA templates and standard citation formatting. · Completed requirements and the requirements for equipment that have been removed have been
deleted. · Some requirements have been reordered to help with clarity (i.e., similar requirements are grouped). · CAM has been added as discussed in Table 4 of this TSD. · The control efficiency of TREA 1 was lowered from 98.4% to 95% per the Permittee’s request. They often
have trouble meeting that efficiency and the catalyst is very expensive to replace. This change does not affect the applicability of any rule.
· Removed EUs 007, 017, 018, 019, and 24, since they have been removed from the facility. · Removed SVs 003, 006, 008, 009, 011, 016, and 017 since they are either associated with insignificant
activities or have been removed from the facility. · Removed GPs 002, 004, and 005 and placed the requirements in these groups at the individual units. · Added control efficiency to the Monthly HAP Emissions Calculations requirement. All HAPs reported are
volatile and therefore assumed to be controlled by the catalytic oxidizer. · Updated catalytic oxidizer temperature minimum based on the results of the most recent performance
test. · Added EQUIs 38, 39, and 40 as part of the notification of replacement incorporated in this permit. · SVs 12, 13, 18, 19, and 20 were removed from the permit because they do not actually exist. These
stacks correlated to the air makeup units at the plant, however, the air makeup units do not actually have stack and instead vent directly inside the facility.
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2. Regulatory and/or statutory basis
2.1 New source review (NSR) The permit carries forward limits on the facility such that it is a minor source under New Source Review regulations. No changes are authorized by this permit.
2.2 Part 70 permit program The facility is a major source under the Part 70 permit program.
2.3 New source performance standards (NSPS) The Permittee has stated that no New Source Performance Standards apply to the operations at this facility. During this reissuance it was determined that 40 CFR, pt. 60, subp. TT does not apply to the facility. NSPS TT defines “metal coil surface coating operation” as “the application system used to apply an organic coating to the surface of any continuous metal strip...that is packaged in a roll or coil”. Silgan coats metal that is delivered as a coil but the coil is cut into sheets prior to coating. The final product at this facility are can lids that are then stamped out of the coated sheets. The coating lines at the facility do not have the capability to coat a continuous sheet or coil. In addition, an applicability determination made by EPA for a facility in South Carolina (Control #9600143) stated “Metal coil surface coating is a linear process by which protective or decorative organic coatings are applied in a continuous process to flat metal sheet or strip which is packaged in rolls or coils.”
2.4 National emission standards for hazardous air pollutants (NESHAP) The facility has accepted limits on HAP emissions such that it is an area source under 40 CFR pt. 63. Thus, no major source NESHAPs apply. In addition, the Permittee has stated that no area source NESHAPs apply to the facility.
2.5 Compliance assurance monitoring (CAM)
The table below lists the sources which are subject to CAM, whether the source is a large pollutant specific emission unit (PSEU), and the monitoring for the applicable pollutants. Table 4. CAM summary
Unit Control CAM applicability Pollutant
EQUI 41 TREA 1 Catalytic Oxidizer Other VOC/HAPs
EQUI 42 TREA 1 Catalytic Oxidizer Other VOC/HAPs
For large pollutant specific emission units, records of the monitored parameter must be made at a minimum of 4 times per hour, or once every 15 minutes. For other PSEUs (not large), records must be made at a minimum of once per 24 hours. See Attachment 3 to this document for the CAM Plan submitted by the applicant.
2.6 Minnesota State Rules Portions of the facility are subject to the following Minnesota Standards of Performance:
· Minn. R. 7011.0515 Standards of Performance for New Indirect Heating Equipment · Minn. R. 7011.0610 Standards of Performance for Fossil-Fuel-Burning Direct Heating Equipment
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Table 5. Regulatory overview of facility
Subject item* Applicable regulations Rationale
COMG 1 (VOC Sources)
40 CFR § 52.21 PSD. Limits on VOC emissions to avoid major source classification.
40 CFR § 63.2
National Emissions Standards for Hazardous Air Pollutants (NESHAPs). Limits taken to avoid major source classification under the NESHAPs for both individual and total HAPs.
EQUI 8, 9, 38, and 39 (Air Make-up) Minn. R. 7011.0515
Standards of Performance for New Indirect Heating Equipment Determination of applicable limits from rule:
· the facility is located inside the MSP Air Quality Control Region;
· the units and the site have < 250 MMBtu/hr capacity.
EQUI 43 and EQUI 44 (Dryers/Ovens) Minn. R. 7011.0610
Standards of Performance for Fossil-Fuel-Burning Direct Heating Equipment. Determination of applicable limits from rule:
· the facility is located inside the MSP Air Quality Control Region;
· the units burn natural gas only.
TREA 1 (Catalytic Oxidizer)
40 CFR § 52.21 PSD. Catalytic oxidizer control efficiencies set to avoid classification as a major source.
40 CFR pt. 64 Compliance Assurance Monitoring (CAM). The oxidizer is used to control VOC and HAPs. Units are considered as other PSEUs.
Minn. R. 7011.0610
Standards of Performance for Fossil-Fuel-Burning Direct Heating Equipment. Determination of applicable limits from rule:
· the facility is located inside the MSP Air Quality Control Region;
· the unit burns natural gas only. *Location of the requirement in the permit (e.g., EQUI 1, STRU 2, etc.).
3. Technical information
3.1 Calculations of potential to emit (PTE) Attachment 1 summarizes the PTE of the Facility and contains detailed spreadsheets and supporting information prepared by the MPCA and the Permittee. Coatings are applied on metal sheets via rollers on coating lines EQUI 41 and 42; therefore, there are no PM emissions from coating processes. VOC and HAP emissions are calculated based on material usage and control efficiency. The control efficiencies for VOC and HAPs are considered be to equal because each HAP the facility has reported to use is volatile. The coating lines are enclosed in a permanent total enclosure that ducts VOC and HAPs emissions to a catalytic oxidizer. The oxidizer burns natural gas and propane. Emissions from the oxidizer are calculated using AP-42 emissions factors. After coating, can ends are punched out of the sheet metal and a seal is applied around the edge of the can end. This process is done using the gang presses. Emissions from this process are broken down into three calculations for each press and include the liner, mister, and lubricator. The only emissions from the presses are VOCs. The liner and lubricator are extruded onto the can lids. While the name of the misters suggests there are particulate emissions, the material is not actually atomized and is supplied as a drip; therefore, there are no PM emissions. VOC emissions from the presses are calculated based on material density, solids
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and solvent content, production speed of the presses (can ends per hour), and the application rate (mg per end). Emissions are not vented to control equipment. No HAPs are emitted by the presses. The combustion potential emissions are calculated based on equipment capacity, allowable fuels, and published emissions factors from AP-42.
3.2 Performance Testing
The Permittee conducts a performance test of the catalytic oxidizer every 5 years to verify the VOC destruction efficiency. The catalyst has previously caused TREA 1 to fail to meet the previous control efficiency of 98.4% during the performance test. When the catalyst fails the facility must spend ~$500,000 replacing the catalyst. The Permittee requested to lower the control efficiency of the oxidizer by 3.4% to 95%. Lowering the efficiency does not affect the Permittee’s ability to meet limits set in the permit or the applicability of any rule. A summary of past performance tests can be found in Table 6. Table 6. Performance Testing Results
Test Date VOC Limit (%) Test Result (%) Compliance 08 December 2015 98.4 99.8 Compliant
19 August 2015 98.4 94.9 Non-compliant 26 March 2010 98.4 99.5 Compliant 30 March 2005 98.4 99.6 Compliant
3.3 Precap The permit includes a PreCap for VOC and HAP emitting equipment. The cap is written to cover the emissions/usage of coating lines and VOC-emitting units at the facility regardless of whether or not they are existing, modified or new. If the Permittee wishes to make changes to any of the units or add new units, the changed or new equipment will be subject to the cap. However, an amendment may still be needed to make the change based on the hourly emissions increase and/or the non-emissions increase amendment triggers (e.g., change to monitoring, recordkeeping, etc.).
3.4 Monitoring In accordance with the Clean Air Act, it is the responsibility of the owner or operator of a facility to have sufficient knowledge of the facility to certify that the facility is in compliance with all applicable requirements. For CAM, the Permittee submitted a CAM proposal as required by 40 CFR § 64.3. It can be found in Attachment 3 to this TSD. Further discussion of decisions about CAM can be found in Table 4. In evaluating the monitoring included in the permit, the MPCA considered the following:
· the likelihood of the facility violating the applicable requirements; · whether add-on controls are necessary to meet the emission limits; · the variability of emissions over time; · the type of monitoring, process, maintenance, or control equipment data already available for the
emission unit; · the technical and economic feasibility of possible periodic monitoring methods; and · the kind of monitoring found on similar units elsewhere.
Table 7 summarizes the monitoring requirements.
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Table 7. Monitoring
Subject Item* Requirement (basis) Monitoring Discussion
COMG 1 (VOC Sources)
Volatile Organic Compounds <= 240 tons per year 12-month rolling sum (To avoid NSR)
Recordkeeping: Daily records of coating usage; On-going MSDS records of coating contents: Monthly calculations of emissions
Records are generated on a daily basis based on usage/production logs and maintained in a database. Credit can be taken for waste materials collected and shipped off-site (dispensed - waste = emissions). Since this is done at most monthly, calculating emissions more frequently than monthly would result in large spikes (while waste is accumulating) and dips (when waste is shipped) – resulting in possible paperwork violations and days with negative emissions. For these reasons, 12 month rolling limits are reasonable for this facility.
HAPs - Single <= 9 tons per year 12-month rolling sum [To avoid major source under 40 CFR 63.2)
Recordkeeping: Daily records of coating usage; On-going MSDS records of coating contents: Monthly calculations of emissions
Records are generated on a daily basis based on usage/production logs and maintained in a database. Credit can be taken for waste materials collected and shipped off-site (dispensed - waste = emissions). Since this is done at most monthly, calculating emissions more frequently than monthly would result in large spikes (while waste is accumulating) and dips (when waste is shipped) – resulting in possible paperwork violations and days with negative emissions. For these reasons, 12 month rolling limits are reasonable for this facility.
HAPs - Total <= 23 tons per year 12-month rolling sum. (To avoid major source under 40 CFR 63.2)
Recordkeeping: Daily records of coating usage; On-going MSDS records of coating contents: Monthly calculations of emissions
Records are generated on a daily basis based on usage/production logs and maintained in a database. Credit can be taken for waste materials collected and shipped off-site (dispensed - waste = emissions). Since this is done at most monthly, calculating emissions more frequently than monthly would result in large spikes (while waste is accumulating) and dips (when waste is shipped) – resulting in possible paperwork violations and days with negative emissions. For these reasons, 12 month rolling limits are reasonable for this facility.
EQUIs 8, 9, 38, and 39 (Air Make-up)
Total Particulate Matter <= 0.40 pounds per million Btu heat input Opacity <= 20 percent opacity (Minn. R. 7011.0515)
Monthly fuel records
The units use natural gas; therefore, the likelihood of violating either of the emission limits is very small. The potential to emit from the units are < 0.01 lb/MMBtu due to equipment design and allowable fuels.
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Subject Item* Requirement (basis) Monitoring Discussion
EQUIs 43 and 44 (Dryers/Ovens)
Total Particulate Matter <= 0.30 grains per dry standard cubic foot Opacity <= 20 percent opacity (Minn. R. 7011.0610)
Monthly fuel records
The units use natural gas; therefore, the likelihood of violating these limits is very small.
TREA 1 (Catalytic Oxidizer)
Overall control efficiency for Volatile Organic Compounds >= 95 percent Overall control efficiency for Total and Single HAPs >= 95 percent Temperature >= 674 degrees Fahrenheit 3-hour rolling average (to avoid NSR)
Temperature Limit; Continuous temperature readings; Daily verification of operation of temperature recording device; Inspections, O&M, calibrations recordkeeping, corrective actions, Performance testing
Monitoring based on the Permittee’s CAM Plan and on Minnesota Performance Standard for Control Equipment is adequate to have a reasonable assurance of compliance. As an other PSEU under CAM the Permittee is not required to perform continuous monitoring, so the current continuous temperature monitoring is more than sufficient for CAM purposes. Periodic performance tests to verify the efficiency of the oxidizer over the last 12 years show that the control efficiency can be met.
Total Particulate Matter <= 0.30 grains per dry standard cubic foot Opacity <= 20 percent opacity (Minn. R. 7011.0610) None
The oxidizer uses natural gas; therefore, the likelihood of violating these limits is very small.
*Location of the requirement in the permit (e.g., EQUI0000000001, STRU0000000002, etc.).
3.5 Insignificant activities Silgan Containers Mfg Corp - Savage has several operations which are classified as insignificant activities under the MPCA’s permitting rules. These are listed in Appendix A to the permit. The permit is required to include periodic monitoring for all emissions units, including insignificant activities, per EPA guidance. The insignificant activities at this Facility are only subject to general applicable requirements. Using the criteria outlined earlier in this TSD, the following table documents the justification why no additional periodic monitoring is necessary for the current insignificant activities. See Attachment 1 of this TSD for PTE information for the insignificant activities. Table 8. Insignificant activities
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Insignificant activity General applicable emission limit Discussion
Infrared electric ovens Opacity <= 20% (Minn. R. 7011.0105 or 7011.0110)
These units are not likely to have any emissions of particulate matter at this site (used to dry off VOCs). It is highly unlikely that they could violate the applicable requirement.
VOC storage tanks with total capacity not more than 10,000 gallons meeting certain vapor pressure requirements
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0710/0715)
There are 5 individual tanks with a total storage capacity of less than 9,000 gallons. These units are not likely to have any particulate emissions. These units are unlikely to violate the applicable requirement.
Brazing, soldering or welding equipment
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0710/0715)
For these units, based on EPA published emissions factors, it is highly unlikely that they could violate the applicable requirement. In addition, these units are typically operated and vented inside a building, so testing for PM or opacity is not feasible.
Blueprint copiers and photographic processes
Opacity <= 20% (Minn. R. 7011.0105 or 7011.0110)
While no known emissions estimation method exists for these units, based on general knowledge of how they operate, it is highly unlikely that they could generate visible emissions. In addition, these units would be operated and vented directly into an office area, so monitoring or testing is not feasible.
Equipment used exclusively for melting or application of wax
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0710/0715)
While no known emissions estimation method exists for these units, based on general knowledge of how they operate, it is highly unlikely that they could generate visible emissions.
Cleaning operations: alkaline/phosphate cleaners and associated cleaners and associated burners
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0610 & Minn. R. 7011.0710/0715)
For these units, there are some factors available for the burners, but very little information regarding the cleaning operation itself. However, based on general knowledge of how they operate, it is highly unlikely that they could violate the applicable requirement or that testing would be feasible.
Individual units with potential emissions less than 2000 lb/year of certain pollutants
PM ≤ 0.6 or 0.4 lb/MMBtu, depending on year constructed Opacity ≤ 20% with exceptions (Minn. R. 7011.0510/0515)
These are 2 furnaces and 14 space heaters (total heat input is 0.725 MMBtu/hr that burn natural gas. For the natural gas units and generator, based on the fuels used and EPA published emissions factors, it is highly unlikely that they could violate the applicable requirement. In addition, all of these units are operated and vented inside a building, so testing for PM or opacity is not feasible. There are also 2 videojet printers that have minimal methanol emissions.
Fugitive dust emissions from unpaved entrance roads and parking lots
Requirement to take reasonable measures to prevent PM from becoming airborne (Minn. R. 7011.0150)
The Facility is located in the Metro area and has all paved parking lots and few private roads. Nearly all surfaces are currently paved, with the exception of one driveway behind the facility. The permit does contain a general requirement that this standard must be met. The Permittee has stated that no additional unpaved surfaces will be added in the future.
Infrequent use of spray paint equipment for routine housekeeping or plant upkeep activities not associated with primary production processes at the stationary source
PM, variable depending on airflow Opacity <= 20% (Minn. R. 7011.0710/0715)
While spray equipment will have the potential to emit particulate matter, these particular activities are those not associated with production, so they would be infrequent and usually occur outdoors. Testing or monitoring is not feasible.
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3.6 Permit organization In general, the permit meets the MPCA Tempo Guidance for ordering and grouping of requirements. One area where this permit deviates slightly from Tempo guidance is in the use of appendices. While appendices are fully enforceable parts of the permit, in general, any requirement that the MPCA thinks should be electronically tracked (e.g., limits, submittals, etc.), should be in the Requirements table in Tempo. The main reason is that the appendices are word processing sections and are not part of the electronic tracking system. Violation of the appendices can be enforced, but the computer system will not automatically generate the necessary enforcement notices or documents. Staff must generate these.
3.7 Comments received This section will be completed after the public notice period. Public Notice Period: December 4, 2016– January 2, 2017 EPA Review Period: January 4, 2017 – January 19, 2017 Comments were not received from the public during the public notice period. Comments were not received from EPA during their review period.
4. Permit fee assessment This permit action is the reissuance of an individual Part 70; therefore, no application fees apply under Minn. R. 7002.0016, subp. 1.
5. Conclusion
Based on the information provided by Silgan Containers Mfg Corp - Savage the MPCA has reasonable assurance that the proposed operation of the emission facility, as described in the Air Emission Permit No. 13900001- 004 and this TSD, will not cause or contribute to a violation of applicable federal regulations and Minnesota Rules. Staff members on permit team: Kirsten Baker (permit engineer)
Sarah Sevcik (peer reviewer) Beckie Olson (permit writing assistant) Laurie O’Brien (administrative support) Marc Severin (stack testing) Dan Dietrich (enforcement)
TEMPO360 Activities: Notification of Replacement of Unit (IND20110001), Part 70 Permit Reissuance (IND20070001), Permit Reopening (IND20060002)
Attachments: 1. PTE summary and calculation spreadsheets 2. Subject item inventory and facility requirements 3. CAM Plan
ATTACHMENT 1: Emissions Summary Calculation Spreadsheets
Pollutant Summary
Controlled Uncontrolled ControlledGrand Total (lbs/hr) (tons/yr) (tons/yr)
VOC 193 3173 2411330-20-7 (Xylene) 28.11 2462.83 9.00
100-41-4 (Ethylbenzene) 5.86 513 9.00108-10-1 (MIBK) 8.56 750 9.00
108-88-3 (Toluene) 0.54 46.97 9.00112-07-2 (Butyl Cel) 4.63 405 9.00
CO 3.96 17.33 17.33CO2 5652 24756 24756
PM/PM10/PM2.5 0.36 1.57 1.57SO2 0.03 0.12 0.12NOX 4.71 20.63 20.63CO2e 5686 24903 24903CH4 0.11 0.47 0.47N2O 0.10 0.45 0.45
Total HAPs 69.02 3023 23.35Single HAP 28.11 2462.83 9.34
Pollutant Summary
Summary VOC by Emission Unit
Silgan Containers - Ft. Madison, IA Summary VOC by Emission Unit Page C-2
Silgan Containers Manufacturing CorporationSavageSample Calculations
Annual Liner VOC Emissions by Emission UnitControlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled Actual
EQUI 12 (EU008) -211A Liner EQUI 12 (EU008) -211A Liner EQUI 12 (EU008) -211A Liner EQUI 12 (EU008) -211A Liner EQUI 16 (EU012) -211B Liner EQUI 16 (EU012) -211B Liner EQUI 16 (EU012) -211B Liner EQUI 16 (EU012) -211B LinerMaterial (lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
VOC 10.2 40.6 40.6 10.2 40.6 40.61330-20-7 (Xylene)
100-41-4 (Ethylbenzene)108-10-1 (MIBK)
108-88-3 (Toluene)112-07-2 (Butyl Cel)
Controlled Uncontrolled Controlled(lbs/hr) (tons/yr) (tons/yr)
Liner Plant Wide Total: 82.2 327.4 327.4Coating Plant Wide Total 31.45 2754.83 137.74
Total 113.7 3082.2 465.1
Annual Mister Spray VOC Emissions by Emission UnitControlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled Actual
EQUI 12 (EU008) -211A Mister EQUI 12 (EU008) -211A Mister EQUI 12 (EU008) -211A Mister EQUI 12 (EU008) -211A Mister EQUI 16 (EU012) -211B Mister EQUI 16 (EU012) -211B Mister EQUI 16 (EU012) -211B Mister EQUI 16 (EU012) -211B MisterMaterial (lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
VOC 0.1 0.5 0.5 0.1 0.5 0.5
Annual Lube VOC Emissions by Emission Unit
Controlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled ActualEQUI 12 (EU008) -211A Lube EQUI 12 (EU008) -211A Lube EQUI 12 (EU008) -211A Lube EQUI 12 (EU008) -211A Lube EQUI 16 (EU012) -211B Lube EQUI 16 (EU012) -211B Lube EQUI 16 (EU012) -211B Lube EQUI 16 (EU012) -211B Lube
Material (lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
VOC 0.7 3.15 3.15 0.7 3.15 3.15
TOTAL (Mister +Lube) 11.0 44.2 44.2 11.0 44.2 44.2Controlled Uncontrolled Controlled Actual
(lbs/hr) (tons/yr) (tons/yr) (tons/yr)Liner, Mister Spray & Lube Plant Wide Total: 5.0 22.1 22.1 3.0
Annual VideoJet Ink VOC Emissions
MaterialControlled Uncontrolled Controlled Actual
VOC (lbs/hr) (tons/yr) (tons/yr) (tons/yr)Videojet Ink 168605 & 168606 Total: 0.0 0.4 0.4 0.4
Annual Cleanup VOC Emissions by Emission Unit
EQUI 1 (EU 023) Controlled Uncontrolled Controlled ActualMaterial (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
VOC Aromatic 100 18.13 2.54 2.54 0.01 IPA 16.48 2.31 2.31 0.01
Heptane 14.50 8.70 8.70 3.42 Acetone 0 - - -
Butyl (Coating) 3.75 18.75 0.94 0.73E30 (Coating) 3.67 29.32 1.47 0.34 PMA (coating) 1.01 2.01 0.10 0.06 Mineral Spirits 16.25 2.28 2.28 1.06
Total 73.77 65.90 18.32 5.62Liner/Coater/Lube/Mister Total 192.47 3170.54 505.88 9.00
Controlled Uncontrolled ControlledGrand Total (lbs/hr) (tons/yr) (tons/yr)
VOC 192.73 3171.68 507.011330-20-7 (Xylene) 28.11 2462.83 123.14
100-41-4 (Ethylbenzene) 5.86 513.37 25.67108-10-1 (MIBK) 8.56 749.98 37.50
108-88-3 (Toluene) 0.54 46.97 2.35112-07-2 (Butyl Cel - Glycol Ether) 4.63 405.38 20.27
Total HAPS 69.02 3023.17 151.16
Summary VOC by Emission Unit
Silgan Containers - Ft. Madison, IA Summary VOC by Emission Unit Page C-3
Silgan Containe SavageSample Calculations
Annual Liner VOC Em
Material
VOC1330-20-7 (Xylene)
100-41-4 (Ethylbenzene)108-10-1 (MIBK)
108-88-3 (Toluene)112-07-2 (Butyl Cel)
Annual Mister Spray
Material
VOC
Annual Lube VOC Em
Material
VOC
TOTAL (Mister +Lube)
Annual VideoJet Ink V
Material
VOC
Annual Cleanup VOC
EQUI 1 (EU 023)Material
VOC
Controlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled ActualEQUI 17 (EU013) -211C Liner EQUI 17 (EU013) -211C Liner EQUI 17 (EU013) -211C Liner EQUI 17 (EU013) -211C Liner EQUI 13 (EU009) -300A Liner EQUI 13 (EU009) -300A Liner EQUI 13 (EU009) -300A Liner EQUI 13 (EU009) -300A Liner
(lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
10.2 40.6 40.6 10.8 43.0 43.0
Controlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled ActualEQUI 17 (EU013) -211C Mister EQUI 17 (EU013) -211C Mister EQUI 17 (EU013) -211C Mister EQUI 17 (EU013) -211C Mister EQUI 13 (EU009) -300A Mister EQUI 13 (EU009) -300A Mister EQUI 13 (EU009) -300A Mister EQUI 13 (EU009) -300A Mister
(lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
0.0 0.0 0.0 0.1 0.5 0.5
Controlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled ActualEQUI 17 (EU013) -211C Lube EQUI 17 (EU013) -211C Lube EQUI 17 (EU013) -211C Lube EQUI 17 (EU013) -211C Lube EQUI 13 (EU009) -300A Lube EQUI 13 (EU009) -300A Lube EQUI 13 (EU009) -300A Lube EQUI 13 (EU009) -300A Lube
(lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
0.7 3.15 3.15
10.2 40.6 40.6 11.6 46.6 46.6
Summary VOC by Emission Unit
Silgan Containers - Ft. Madison, IA Summary VOC by Emission Unit Page C-4
Silgan Containe SavageSample Calculations
Annual Liner VOC Em
Material
VOC1330-20-7 (Xylene)
100-41-4 (Ethylbenzene)108-10-1 (MIBK)
108-88-3 (Toluene)112-07-2 (Butyl Cel)
Annual Mister Spray
Material
VOC
Annual Lube VOC Em
Material
VOC
TOTAL (Mister +Lube)
Annual VideoJet Ink V
Material
VOC
Annual Cleanup VOC
EQUI 1 (EU 023)Material
VOC
Controlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled ActualEQUI 14 (EU010) -300B Liner EQUI 14 (EU010) -300B Liner EQUI 14 (EU010) -300B Liner EQUI 14 (EU010) -300B Liner EQUI 15 (EU011) -300 Liner EQUI 15 (EU011) -300 Liner EQUI 15 (EU011) -300 Liner EQUI 15 (EU011) -300 Liner
(lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
10.80 43.0 43.0 11.26 44.82 44.82
Controlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled ActualEQUI 14 (EU010) -300B Mister EQUI 14 (EU010) -300B Mister EQUI 14 (EU010) -300B Mister EQUI 14 (EU010) -300B Mister EQUI 15 (EU011) -300 Mister EQUI 15 (EU011) -300 Mister EQUI 15 (EU011) -300 Mister EQUI 15 (EU011) -303 Mister
(lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
0.1 0.5 0.5 0.3 0.5 2.2 2.2 0.2
Controlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled ActualEQUI 14 (EU010) -300B Lube EQUI 14 (EU010) -300B Lube EQUI 14 (EU010) -300B Lube EQUI 14 (EU010) -300B Lube EQUI 15 (EU011) -300 Lube EQUI 15 (EU011) -300 Lube EQUI 15 (EU011) -300 Lube EQUI 15 (EU011) -300 Lube
(lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
0.7 3.15 3.15 2.24 0.7 3.15 3.15
11.6 46.6 46.6 2.5 12.5 50.2 50.2 0.2
Summary VOC by Emission Unit
Silgan Containers - Ft. Madison, IA Summary VOC by Emission Unit Page C-5
Silgan Containe SavageSample Calculations
Annual Liner VOC Em
Material
VOC1330-20-7 (Xylene)
100-41-4 (Ethylbenzene)108-10-1 (MIBK)
108-88-3 (Toluene)112-07-2 (Butyl Cel)
Annual Mister Spray
Material
VOC
Annual Lube VOC Em
Material
VOC
TOTAL (Mister +Lube)
Annual VideoJet Ink V
Material
VOC
Annual Cleanup VOC
EQUI 1 (EU 023)Material
VOC
Controlled Uncontrolled Controlled Actual Controlled Uncontrolled Controlled Controlled Uncontrolled ControlledEQUI 18 (EU014) -DRT Liner EQUI 18 (EU014) -DRT Liner EQUI 18 (EU014) -DRT Liner EQUI 18 (EU014) -DRT Liner EQUI 42 (EU025) Coater EQUI 42 (EU025) Coater EQUI 42 (EU025) Coater EQUI 41 (EU04) Coater 3 EQUI 41 (EU04) Coater 3 EQUI 41 (EU04) Coater 3
(lbs/hr) (tons/yr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr)
18.78 74.76 74.76 15.72 1377.42 68.87 15.72 1377.42 68.8714.06 1231.41 61.57 14.06 1231.41 61.572.93 256.68 12.83 2.93 256.68 12.834.28 374.99 18.75 4.28 374.99 18.750.27 23.49 1.17 0.27 23.49 1.172.89 253.51 12.68 1.73 151.87 7.59
Controlled Uncontrolled Controlled ActualEQUI 18 (EU014) -DRT Mister EQUI 18 (EU014) -DRT Mister EQUI 18 (EU014) -DRT Mister EQUI 18 (EU014) -DRT Mister
(lbs/hr) (tons/yr) (tons/yr) (tons/yr)
0.5 2.2 2.2 0.3
Controlled Uncontrolled Controlled ActualEQUI 18 (EU014) -DRT Mister EQUI 18 (EU014) -DRT Mister EQUI 18 (EU014) -DRT Mister EQUI 18 (EU014) -DRT Mister
(lbs/hr) (tons/yr) (tons/yr) (tons/yr)
19.3 77.0 77.0 0.3
Summary by Plant HEAT
Silgan Containers - Ft. Madison, IA Summary by Plant HEAT Page C-6
Silgan Containers Manufacturing CorporationSavageSample Calculations
Annual Liner VOC Emissions by Emission UnitControlled Uncontrolled Controlled Actual
EQUI44(EU003) EQUI44 (EU003) EQUI44 (EU003) EQUI44 (EU003)Material EF (lbs/hr) (tons/yr) (tons/yr) (tons/yr)
VOC 5.5 0.024 0.10 0.10CO 84 0.36 1.59 1.59
CO2 120000 517.65 2267.29 2267.29PM 7.6 0.03 0.14 0.14SO2 0.6 0.0026 0.0113 0.0113NOX 100 0.43 1.89 1.89PM10 0.03 0.14 0.14PM2.5 0.03 0.14 0.14CH4 0.0099 0.04 0.04N2O 0.0095 0.04 0.04
CO2e 521 2281 2281
Controlled Uncontrolled Controlled(lbs/hr) (tons/yr) (tons/yr)
VOC 0.26 1.13 1.13CO 3.96 17.33 17.33
CO2 5652 24756 24756PM 0.36 1.57 1.57SO2 0.03 0.12 0.12NOX 4.71 20.63 20.63PM10 0.36 1.57 1.57PM2.5 0.36 1.57 1.57CH4 0.11 0.47 0.47N2O 0.10 0.45 0.45
CO2e 5685.65 24903.13 24903.13
Summary by Plant HEAT
Silgan Containers - Ft. Madison, IA Summary by Plant HEAT Page C-7
Silgan Containers SavageSample Calculations
Annual Liner VOC Emissi
MaterialVOCCO
CO2PMSO2NOXPM10PM2.5CH4N2O
CO2e
Controlled Uncontrolled Controlled Controlled Uncontrolled ControlledEQUI43 (EU006) EQUI43 (EU006) EQUI43 (EU006) EQUI8 (EU020) EQUI8 (EU020) EQUI8 (EU020)
(lbs/hr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr)0.04 0.16 0.16 0.06 0.28 0.280.54 2.38 2.38 0.97 4.26 4.26
776.47 3400.94 3400.94 1387.94 6079.18 6079.180.05 0.22 0.22 0.09 0.39 0.39
0.0039 0.0170 0.0170 0.0069 0.0304 0.03040.65 2.83 2.83 1.16 5.07 5.070.05 0.22 0.22 0.09 0.39 0.390.05 0.22 0.22 0.09 0.39 0.390.015 0.07 0.07 0.027 0.12 0.120.014 0.06 0.06 0.025 0.11 0.11781 3421 3421 1396 6115 6115
Summary by Plant HEAT
Silgan Containers - Ft. Madison, IA Summary by Plant HEAT Page C-8
Silgan Containers SavageSample Calculations
Annual Liner VOC Emissi
MaterialVOCCO
CO2PMSO2NOXPM10PM2.5CH4N2O
CO2e
Controlled Uncontrolled Controlled Controlled Uncontrolled ControlledEQUI9 (EU021) EQUI9 (EU021) EQUI9 (EU021) TREA 1 (EU024) TREA 1 (EU024) TREA 1 (EU024)
(lbs/hr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr)0.04 0.17 0.17 0.07 0.29 0.290.58 2.54 2.54 1.00 4.36 4.36
828.24 3627.67 3627.67 1423.53 6235.06 6235.060.05 0.23 0.23 0.09 0.39 0.39
0.0041 0.0181 0.0181 0.0071 0.0312 0.03120.69 3.02 3.02 1.19 5.20 5.200.05 0.23 0.23 0.09 0.39 0.390.05 0.23 0.23 0.09 0.39 0.390.016 0.07 0.07 0.027 0.12 0.120.015 0.07 0.07 0.026 0.11 0.11833 3649 3649 1432 6272 6272
Summary by Plant HEAT
Silgan Containers - Ft. Madison, IA Summary by Plant HEAT Page C-9
Silgan Containers SavageSample Calculations
Annual Liner VOC Emissi
MaterialVOCCO
CO2PMSO2NOXPM10PM2.5CH4N2O
CO2e
Controlled Uncontrolled Controlled Controlled Uncontrolled ControlledEQUI38 (EU026) EQUI38 (EU026) EQUI38 (EU026) EQUI39 (EU027) EQUI39 (EU027) EQUI39 (EU027)
(lbs/hr) (tons/yr) (tons/yr) (lbs/hr) (tons/yr) (tons/yr)0.0166 0.0727 0.0727 0.0163 0.0714 0.0714
0.25 1.11 1.11 0.25 1.09 1.09362.35 1587.11 1587.11 355.88 1558.76 1558.760.0229 0.1005 0.1005 0.0225 0.0987 0.09870.0018 0.0079 0.0079 0.0018 0.0078 0.00780.30 1.32 1.32 0.30 1.30 1.30
0.0229 0.1005 0.1005 0.0225 0.0987 0.09870.0229 0.1005 0.1005 0.0225 0.0987 0.09870.0069 0.0304 0.0304 0.0068 0.0299 0.02990.0066 0.0291 0.0291 0.0065 0.0286 0.0286
365 1597 1597 358 1568 1568
PTE and Actual HAPS
325 6.50 2,112 325
92 7.42 171 23
5.00 6.59 33 5.00
3.00 7.25 22 3.00
498 6.84 3,403 498
245 5.80 1,421 245 496
67 6.30 423 67 1.41
2.68 6.59 18 2.68 7.86
1.00 6.59 6.61 1.00 1.24
ACETONE GA
IPA GA
HEPTANE GA
KDRAW_1204 GA
10,040 245
KDRAW_165 GA
EQUI 12 (EU008)9385HC57 84,337 LB 8.40 84,337
DYNA 143 GA
AROMATIC 100 GA
MINERAL SPIRITS GA
168600 Qt
EU000168605 356 Qt 6.67 594 89
Usage UOM Density Material Usage (lbs)
Material Usage
HazardousWaste (lbs)
Plant Number: 1501/1/2013 - 12/31/2013
Aggregate Usage Grouped by Emission Unit
EU Material ID
PTE and Actual HAPS
4,211 7.74 4,211 544 5.51
602 6.84 4,115 602
293 5.80 1,700 293 583
84 6.30 531 84 1.74
2.57 6.59 17 2.57 7.95
0.79 6.59 5.21 0.79 0.98
655 6.84 4,481 655
333 5.80 1,933 333 653
89 6.30 562 89 1.81
2.84 6.59 19 2.84 8.75
0.95 6.59 6.24 0.95 1.17
ACETONE GA
IPA GA
HEPTANE GA
KDRAW_1204 GA
14,391 343
KDRAW_165 GA
IPA GA
EQUI 14 (EU010)9385HC57 120,883 LB 8.40 120,883
KDRAW_1204 GA
ACETONE GA
KDRAW_165 GA
HEPTANE GA
12,345 304
SLC6179HC535 LB
EQUI 13 (EU009)9385HC57 103,699 LB 8.40 103,699
PTE and Actual HAPS
229 5.80 1,330 229 451
66 6.30 415 66 1.35
1.15 6.59 7.55 1.15 4.13
0.57 6.59 3.76 0.57 0.71
537 6.84 3,670 537
269 5.80 1,562 269 479
68 6.30 431 68 1.02
1.95 6.59 13 1.95 5.05
1.08 6.59 7.12 1.08 1.34
414 6.84 2,832 414
222 5.80 1,285 222 467
60 6.30 378 60 1.48
1.84 6.59 12 1.84 6.52
0.33 6.59 2.19 0.33 0.41
ACETONE GA
IPA GA
HEPTANE GA
KDRAW_1204 GA
8,749 246
KDRAW_165 GA
EQUI 17 (EU013)9385HC57 73,490 LB 8.40 73,490
ACETONE GA
IPA GA
HEPTANE GA
KDRAW_1204 GA
11,309 215
KDRAW_165 GA
IPA GA
EQUI 16 (EU012)9385HC57 94,998 LB 8.40 94,998
KDRAW_1204 GA
ACETONE GA
9,847 242
HEPTANE GA
EQUI 15 (EU011)9385HC57 82,717 LB 8.40 82,717
PTE and Actual HAPS
298 5.80 1,731 298 557
85 6.30 536 85 1.64
1.97 6.59 13 1.97 6.10
0.28 6.59 1.82 0.28 0.34
41,742 8.11 338,531 41,742 6,412
16,867 8.05 135,783 16,867 2,351
13,125 8.02 105,263 13,125 1,440
8,100 9.46 76,626 8,100 1,392
3,373 7.33 24,724 3,373 17,479
2,825 9.40 26,555 2,825 660
1,430 11.23 16,059 1,430 290
1,320 8.74 11,537 1,320 278
1,155 8.40 9,706 1,155 122
1,092 8.00 8,734 1,092 102
921 7.50 6,910 921 118
732 8.16 5,971 732 221
681 8.75 5,955 681 79
575 9.74 5,600 575 71
360 8.05 2,898 360 15
190 8.05 1,529 190 25
151 8.75 1,324 151 86
44 12.47 549 44 2.88
19 7.23 136 19 2.06
11 8.33 92 11 0.87
6.26 11.50 72 6.26 0.61
6.00 8.04 48 6.00 0.46
1.68 7.35 12 1.68 0.39
6256054 GA
297C915 GA
9840909 GA
9350104 GA
4623105 GA
6661011 GA
PMA GA
3610HVL GA
4001S13V GA
9844511 GA
9372535 GA
5092802 GA
H56110 GA
BUTYL GA
26S29AAUS GA
3846910 GA
2521401 GA
16S61EAUS GA
89X053K GA
E30 GA
4348802 GA
6256069 GA
IPA GA
EQUI 42 (EUC02)9372025 GA
KDRAW_1204 GA
ACETONE GA
11,936 281
HEPTANE GA
EQUI 18 (EU014)9385HC57 100,266 LB 8.40 100,266
PTE and Actual HAPS
Non-Controlled98.5% Permit Rule 40 CFR 53.31, Minn R 7007.300099.5% CE
25,155 8.02 201,742 25,155 4,242
18,480 8.95 165,396 18,480 2,732
10,900 8.11 88,395 10,900 1,023
10,665 8.05 85,853 10,665 1,819
7,599 8.75 66,489 7,599 1,261
6,556 7.57 49,629 6,556 1,062
5,967 8.40 50,119 5,967 871
3,191 7.50 23,930 3,191 1,500
2,902 7.33 21,272 2,902 14,939
1,975 8.50 16,787 1,975 174
945 8.16 7,713 945 126
935 8.03 7,508 935 116
878 8.05 7,064 878 105
858 12.47 10,699 858 206
530 14.78 7,833 530 127
408 8.00 3,266 408 78
400 8.35 3,340 400 115
385 8.47 3,261 385 81
345 11.50 3,964 345 88
101 8.05 814 101 12
82 7.52 617 82 10
82 8.04 659 82 8.22
78 8.75 686 78 6.52
70 8.25 578 70 6.77
65 8.57 557 65 7.45
53 7.23 384 53 6.79
34 8.05 274 34 2.60
18 10.96 197 18 2.64
14 7.44 104 14 1.54
3.32 7.35 24 3.32 0.52
2.00 7.80 16 2.00 0.2110S80AA GA
8701004 GA
297C915 GA
21S00AA GA
31S02EB GA
31S46AD GA
6661011 GA
5092802 GA
640C260 GA
5698015 GA
6256054 GA
9350104 GA
PMA GA
20S67WE GA
14S47WA GA
1949101 GA
H56110 GA
4348802 GA
4623105 GA
9372535 GA
5061056 GA
E30 GA
188306 GA
3846910 GA
BUTYL GA
3610HVL GA
5698014 GA
9372025 GA
9844511 GA
EQUI 41 (EUC03)6256069 GA
86X066F GA
PTE and Actual HAPS
Non-Controlled95% Permit Rule 40 CFR 52.21, Minn R 7007.300099.5% CE
2,416,205 303,433 67,508EU 042 (EUCO2)HAPS PTE Non-Controlled95% Permit Rule 40 CFR 52.21, Minn R 7007.3000
EQUI 41 EU 004 (EUCO3)HAPS PTE Non-Controlled95% Permit Rule 40 CFR 52.21, Minn R 7007.3000
24,288Misc
4.20 102,014
Plant Total:
PROPANE 24,288 GA
Note: Density is expressed in pounds/gallon. All other units are expressed in gallons unless otherwise noted
PTE and Actual HAPS
EQUI 12 (EU008)
EU000
Plant Number: 1501/1/2013 - 12/31/2013
EUXylene (%) Xylene (Tons) Ethylbenzene (%) Ethylbenzene (Tons)
325
23
5.00
3.00445
498
160
67
1.49
0.8110,737
Material Usage
1.19 9.83
0.19 5.36
86 925
0.22 422
29 84,092 10,011
3,403
33
22
594 89
2,113
171
Hazardous Waste
Consumed(lbs)
Consumed(GA)
Xylene Ethylbenzene
9/18/2014
PTE and Actual HAPS
EQUI 14 (EU010)
EQUI 13 (EU009)
543
602
193
84
1.36
0.6413,732
655
221
89
1.52
0.7715,317
1.33 9.99
0.18 5.06
113 1,280
0.29 560
41 120,540 14,350
4,481
0.15 4.23
0.28 529
1.21 8.98
4,115
101 1,117
36 103,395 12,309
0.71 4,205
PTE and Actual HAPS
EQUI 17 (EU013)
EQUI 16 (EU012)
EQUI 15 (EU011)
152
66
0.52
0.4610,037
537
187
68
1.18
0.8812,077
414
141
60
0.86
0.279,335
0.99 5.64
0.06 1.77
81 818
0.23 376
29 73,245 8,720
2,832
0.77 7.77
0.20 5.78
83 1,083
0.16 430
26 94,783 11,284
3,670
0.11 3.05
0.21 413
0.63 3.42
29 82,475 9,818
78 879
PTE and Actual HAPS
EQUI 42 (EUC02)
EQUI 18 (EU014)
202
85
1.04
0.2212,191
40,952 24.1% 40.02 5.0% 8.30
16,575 0.6% 0.40
12,946 1.1% 0.57
7,953 0.9% 0.34 0.2% 0.08
988 55.0% 1.99 15.0% 0.54
2,755
1,404
1,288
1,141 4.1% 0.20 1.3% 0.06
1,079 17.3% 0.75 3.8% 0.16
906
705 22.5% 0.65 4.7% 0.14
672 0.1% 0.00
568 1.6% 0.04 0.3% 0.01
358 0.9% 0.01
187
141
44 14.1% 0.04 2.9% 0.01
19 73.4% 0.05 15.3% 0.01
11 1.4% 0.00 0.1% 0.00
6.21 10.1% 0.00 2.1% 0.00
5.94 0.1% 0.00
1.63
0.06 48
0.05 12
0.10 91
0.05 71
0.23 546
0.29 134
3.07 1,504
9.79 1,238
7.31 5,529
1.89 2,883
27 5,750
9.01 5,876
13 8,632
16 6,793
32 11,259
15 9,584
70 25,895
26 15,769
147 75,234
2,385 7,245
292 133,432
180 103,823
0.05 1.48
791 332,119
0.26 534
0.93 6.87
33 99,985 11,903
96 1,174
PTE and Actual HAPS
Non-Controlled98.5% Permit Rule 99.5% CEEQUI 41 (EUC03)
90,704 73.4% 45.06 15.3% 9.312.25 0.470.23 0.05
24,626 1.1% 1.09
18,175 0.2% 0.16 0.1% 0.08
10,773 33.6% 14.68 5.0% 2.18
10,439 0.9% 0.38
7,455
6,416 0.1% 0.02
5,863 4.1% 1.01 1.3% 0.32
2,991
864 55.0% 1.74 15.0% 0.47
1,955
930 22.5% 0.85 4.7% 0.18
921 0.3% 0.01
865 0.6% 0.02
841 14.1% 0.74 2.9% 0.15
521
398 17.3% 0.28 3.8% 0.06
386 1.1% 0.02 0.2% 0.00
375 9.0% 0.14 1.9% 0.03
337 10.1% 0.20 2.1% 0.04
100
81 0.5% 0.00
81 0.1% 0.00
78 0.1% 0.00
69 28.9% 0.08 6.7% 0.02
64 9.5% 0.03 2.0% 0.01
52 73.4% 0.14 15.3% 0.03
34 3.5% 0.00 0.6% 0.00
18 1.9% 0.00 0.2% 0.00
14 61.5% 0.03 12.8% 0.01
3.24
1.970.03 15
0.21 103
0.07 24
0.32 271
0.24 195
0.87 550
0.94 378
0.75 680
0.82 571
1.35 607
1.02 651
7.65 3,876
1.48 802
14 3,225
9.62 3,180
8.59 7,706
9.75 3,188
13 6,959
17 10,493
15 7,587
14 7,392
2,038 6,333
20 16,614
104 49,248
200 22,430
144 65,228
140 48,567
126 87,372
226 84,034
529 197,500
305 162,664
PTE and Actual HAPS
Non-Controlled95% Permit Rule 4 99.5% CE
EU 042 (EUCO2)HAPS PTE Non-Co95% Permit Rule 4
EQUI 41 EU 004 (EHAPS PTE Non-Co95% Permit Rule 4
Misc
Note: Density is express
95,725 73.4% 21.85 15.3% 3.631.09 0.180.11 0.020.33 0.06
24,288
294,590(lb/hr) (tpy) (lb/hr) (tpy)
281.14 1231.41 58.60 256.6814.06 61.57 2.93 12.83
(lb/hr) (tpy) (lb/hr) (tpy)281.14 1231.41 58.60 256.68
14.06 61.57 2.93 12.83
102,014 24,288
8,843 2,348,698
Report: MU_02.rpt
Record Source: udf_Report_MU_02
Page 3 of 3
PTE and Actual HAPS
EQUI 12 (EU008)
EU000
Plant Number: 1501/1/2013 - 12/31/2013
EUMIBK (%) MIBK (Tons) Toluene (%) Toluene (Tons) Butyl Cel (%) Butyl Cel (Tons) Methanol (%) Methanol (Tons)
28% 0.02
HAPS (Actual)MethanolToluene Butyl Cel MIBK
PTE and Actual HAPS
EQUI 14 (EU010)
EQUI 13 (EU009)
PTE and Actual HAPS
EQUI 17 (EU013)
EQUI 16 (EU012)
EQUI 15 (EU011)
PTE and Actual HAPS
EQUI 42 (EUC02)
EQUI 18 (EU014)
3.9% 6.48 0.40% 0.66
8.5% 0.67
12.5% 0.70
3.9% 0.11 0.40% 0.01
5.3% 0.16
1.6% 0.04 0.10% 0.00
1.9% 0.01 0.30% 0.00
1.40% 0.00
7.2% 0.00
1.6% 0.00 0.20% 0.00
20.1% 0.00
PTE and Actual HAPS
Non-Controlled98.5% Permit Rule 99.5% CEEQUI 41 (EUC03)
20.1% 6.65 1.40% 0.68 12.5% 1.53 28% 0.020.33 0.03 0.020.03 0.00 0.01
0.10% 0.08
3.9% 1.70 0.40% 0.17
7.7% 0.64
3.9% 0.15 0.40% 0.02
15.6% 0.58
1.9% 0.10 0.30% 0.02
0.10% 0.00
1.6% 0.03 0.20% 0.00
20.1% 0.07
5.3% 0.02
0.20% 0.00
1.40% 0.00
0.10% 0.00
1.10% 0.00
PTE and Actual HAPS
Non-Controlled95% Permit Rule 4 99.5% CE
EU 042 (EUCO2)HAPS PTE Non-Co95% Permit Rule 4
EQUI 41 EU 004 (EHAPS PTE Non-Co95% Permit Rule 4
Misc
Note: Density is express
20.1% 2.66 1.40% 0.30 7.7% 0.66 0% 0.000.13 0.01 0.030.01 0.00 0.000.05 0.00 0.01 0.00
Totalnon-controlledControlled total
Individual HAPS (PTE) (tpy)(lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy)
85.61 374.99 5.36 23.49 57.88 253.514.28 18.75 0.27 1.17 2.89 12.68
(lb/hr) (tpy) (lb/hr) (tpy) (lb/hr) (tpy)85.61 374.99 5.36 23.49 34.67 151.87
4.28 18.75 0.27 1.17 1.73 7.59
PTE and Actual HAPS
EQUI 12 (EU008)
EU000
Plant Number: 1501/1/2013 - 12/31/2013
EU Totallbs/ga lbs Tons
6.67 593.629994 0.296814997
6.5 2112.499997 1.056249998 1.056249998 CLEANUP SOLVENTS
7.42 170.6600104 0.085330005
6.59 32.95000527 0.016475003
7.25 21.75 0.0108751.465745003
3.59 35939.44871 17.96972435
6.84 3403.442396 1.70172119820.3448971 END COMPOUND & MISTER
5.8 925.2621941 0.462631097
6.3 421.6408995 0.21082045
0
6.59 5.36464881 0.00268232420.34757942 0.002682324 CLEANUP SOLVENTS
VOC (Actual)
PTE and Actual HAPS
EQUI 14 (EU010)
EQUI 13 (EU009)3.59 44188.96591 22.09448296
3.59 1950.430009 0.975215005
6.84 4115.448393 2.05772419725.95047166 END COMPOUND & MISTER
5.8 1116.700608 0.558350304
6.3 529.3983883 0.264699194
0
6.59 4.23113586 0.00211556825.95258722 0.002115568 CLEANUP SOLVENTS
3.59 51516.37594 25.75818797
6.84 4481.429939 2.24071496928.91879041 END COMPOUND & MISTER
5.8 1279.610961 0.63980548
6.3 560.1639891 0.280081995
0
6.59 5.063341489 0.00253167128.92132208 0.002531671 CLEANUP SOLVENTS
PTE and Actual HAPS
EQUI 17 (EU013)
EQUI 16 (EU012)
EQUI 15 (EU011)3.59 35248.1277 17.62406385
5.8 878.9076475 0.439453824
6.3 413.3986032 0.20669930217.83076315 END COMPOUND & MISTER
0
6.59 3.054159883 0.0015270818.27174405 0.440980904 CLEANUP SOLVENTS
3.59 40508.37186 20.25418593
6.84 3670.05021 1.83502510522.84588691 END COMPOUND & MISTER
5.8 1082.898681 0.541449341
6.3 430.4530774 0.215226539
0
6.59 5.778472473 0.00288923622.84877615 0.002889236 CLEANUP SOLVENTS
3.59 31303.31305 15.65165653
6.84 2831.829076 1.41591453817.66455788 END COMPOUND & MISTER
5.8 817.867925 0.408933962
6.3 376.1056971 0.188052849
0
6.59 1.77492424 0.00088746217.66544534 0.000887462 CLEANUP SOLVENTS
PTE and Actual HAPS
EQUI 42 (EUC02)
EQUI 18 (EU014)3.59 42731.83908 21.36591954
5.8 1173.743867 0.586871933
6.3 534.3799463 0.26718997321.63310952 END COMPOUND & MISTER
0
6.59 1.481509103 0.00074075522.2207222 0.587612688 CLEANUP SOLVENTS
5.39 220730.11 110.37
5.43 90004.55 45.00
5.29 68482.06 34.24
3.19 25369.48 12.68
7.33 7245.16 3.62
4.42 12176.32 6.09
4.27 5995.83 3.00
5.16 6647.06 3.32
5.5 6275.42 3.14
4.96 5351.96 2.68
7.5 6792.56 3.40
5.17 3642.90 1.82
5.66 3801.14 1.90
4.68 2656.79 1.33
5.07 1815.63 0.91
8.05 1504.25 0.75 0.39 CLEANUP SOLVENTS
1.76 249.01 0.12
5.14 224.97 0.11
6.51 120.71 0.06
5.45 59.38 0.03
4.82 29.93 0.01
5.31 31.56 0.02
6.28 10.25 0.01
PTE and Actual HAPS
Non-Controlled98.5% Permit Rule 99.5% CEEQUI 41 (EUC03)
63.26 469217.03 234.613.16 7038.26 11.730.32 2346.09 1.17
5.29 130271.40 65.14
3.13 56886.95 28.44
5.39 58068.50 29.03
5.07 52926.03 26.46
1.76 13120.17 6.56
3.2 20530.34 10.27
5.5 32245.57 16.12
7.5 22429.70 11.21
7.33 6333.13 3.17
4.85 9479.75 4.74
5.17 4807.01 2.40
5.27 4851.49 2.43
5.43 4694.40 2.35
5.14 4325.26 2.16
3.33 1736.30 0.87
4.96 1976.48 0.99
5.51 2128.11 1.06
5.3 1989.54 0.99
4.82 1624.74 0.81
8.05 801.85 0.40 0.739117005 CLEANUP SOLVENTS
3.11 250.83 0.13
5.31 429.99 0.21
5.66 439.58 0.22
4.67 323.07 0.16
5.14 329.63 0.16
6.51 340.04 0.17
5.23 176.13 0.09
5.48 97.32 0.05
5.61 77.38 0.04
6.28 20.37 0.01
7.27 14.35 0.01
PTE and Actual HAPS
Non-Controlled95% Permit Rule 4 99.5% CE
EU 042 (EUCO2)HAPS PTE Non-Co95% Permit Rule 4
EQUI 41 EU 004 (EHAPS PTE Non-Co95% Permit Rule 4
Misc
Note: Density is express
29.10 433725.40 216.861.45 6505.88 10.840.15 2168.63 1.080.46 2.26 3.22 TOTAL CLEANUP SOLVENTS
92.35 609.174.62 180.27
Total HAPS (tpy) Total HAPS (lb/hr)1,512 345.1175.58 17.26
Total HAPS (tpy) Total HAPS (lb/hr)1512 345.1175.58 17.26
PTE and Actual HAPS
EQUI 12 (EU008)
EU000
Plant Number: 1501/1/2013 - 12/31/2013
EU
PTE and Actual HAPS
EQUI 14 (EU010)
EQUI 13 (EU009)
PTE and Actual HAPS
EQUI 17 (EU013)
EQUI 16 (EU012)
EQUI 15 (EU011)
PTE and Actual HAPS
EQUI 42 (EUC02)
EQUI 18 (EU014)
PTE and Actual HAPS
Non-Controlled98.5% Permit Rule 99.5% CEEQUI 41 (EUC03)
PTE and Actual HAPS
Non-Controlled95% Permit Rule 4 99.5% CE
EU 042 (EUCO2)HAPS PTE Non-Co95% Permit Rule 4
EQUI 41 EU 004 (EHAPS PTE Non-Co95% Permit Rule 4
Misc
Note: Density is express
PTE and Actual HAPS
EQUI 12 (EU008)
EU000
Plant Number: 1501/1/2013 - 12/31/2013
EU
PTE and Actual HAPS
EQUI 14 (EU010)
EQUI 13 (EU009)
PTE and Actual HAPS
EQUI 17 (EU013)
EQUI 16 (EU012)
EQUI 15 (EU011)
PTE and Actual HAPS
EQUI 42 (EUC02)
EQUI 18 (EU014)
PTE and Actual HAPS
Non-Controlled98.5% Permit Rule 99.5% CEEQUI 41 (EUC03)
PTE and Actual HAPS
Non-Controlled95% Permit Rule 4 99.5% CE
EU 042 (EUCO2)HAPS PTE Non-Co95% Permit Rule 4
EQUI 41 EU 004 (EHAPS PTE Non-Co95% Permit Rule 4
Misc
Note: Density is express
Silgan Containers - Ft. Madison, IA Summary Requirements Page C-46
Silgan Containers Manufacturing CorporationSavage, MNProduction Numbers
Maximum MaximumCan / End Maximum Potential Anticipated
Equipment / Manufacturer / Sizes Line/ Strokes Units Units Annual AnnualProduction Line Model Number Produced EU per minute per stroke per minute Production Production
Coating Line #2 EU001 100 1 100 52,560,000Coating Line #3 EU004 100 1 100 52,560,000
maximum sheets coated per year 105,120,000 0Kdraw 1204 Kdraw 165
35500 ends/oz 5867 ends/oz**Gang Press 211A 211 EU008/EUP01 120 11 1320 693,792,000 693,792,000 0.11 lb/hr 0.72 lb/hr**Gang Press 211B 211 EU009/EUP02 120 12 1440 756,864,000 756,864,000**Gang Press 211C 211 EU010/EUP03 120 12 1440 756,864,000 756,864,000**Gang Press 300A 300 EU011/EUP04 120 11 1320 693,792,000 693,792,000**Gang Press 300B 300 EU012/EUP05 120 11 1320 693,792,000 693,792,000**Gang Press 303 303 EU013/EUP06 120 11 1320 693,792,000 693,792,000**DRT Shell Press Line 300 EU014/EUP010 275 10 2750 1,445,400,000 1,445,400,000
Max shells per year 5,734,296,000 5,734,296,000
211A Liners 211 Line 1 EU008 (EUP01) 350 4 1400 735,840,000 735,840,000 4 Liners211B Liners 211 Line 2 EU012 (EUP02) 350 4 1400 735,840,000 735,840,000 4 Liners211C Liners 211 Line 3 EU013 (EUP03) 350 4 1400 735,840,000 735,840,000 4 Liners300A Liners 300 Line 4 EU009 (EUP04) 350 4 1400 735,840,000 735,840,000 4 Liners300B Liners 300 Line 5 EU010 (EUP05) 350 4 1400 735,840,000 735,840,000 4 Liners303 Liners 303 Line 6 EU011 (EUP06) 350 4 1400 735,840,000 735,840,000 4 LinersDRT Liners Rotating 300 Line 10 EU014 (EUP10) 900 3 2700 1,419,120,000 1,419,120,000 3 liners, 6 guns each
Maximum shells lined per year 5,834,160,000 5,834,160,000
** This equipment does not have material usages or emissions that contain any air contaminants
IA - INK Methanol PTE
Press Video JetManufacturer/Model No.Number of Units 3Hours of Operation - PTE Hours/ Year 8760
Process RateEnds/ minute @100% Eff. 480
Process Rate Ends/ Hour 28800Production Ends/ Year 252288000
Ink VideoJet 16-168600QDensity Lb./ gal 7.42Methanol Content Percent/ weight 0.28Material Usage Ends Produced/ Gal. 9600000Material Usage Gal./ year 26.28Material Usage Lb./ HR 0.06678Material Usage Tons/ YR 0.8774892HAP Emissions Lb./ HR 0.0249312 218 lb/yr/unitHAP Emissions Tons/ YR 0.436794624
DRD Video Jet Series 10Manufacturer/Model No.Number of Units 3Hours of Operation - PTE Hours/ Year 8760
Process RateEnds/ minute @100% Eff. 480
Process Rate Ends/ Hour 28800Production Ends/ Year 252288000
Ink VideoJet 16-8600QDensity Lb./ gal 7.42Methanol Content Percent/ weight 0.78Material Usage Ends Produced/ Gal. 9600000Material Usage Gal./ year 26.28Material Usage Lb./ HR 0.06678Material Usage Tons/ YR 0.8774892VOM Emissions Lb./ HR 0.0520884 456 lb/yr/unitVOM Emissions Tons/ YR 0.684441576
IA - Combustion
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Modine Space Heaters 14 (Used 1/4 per yr)Was EU 007
Emission Source mmbtu/hr
Nat Gas Fired units 0.225 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfAmmonia 3.2 lbs/mmscf
Calculating standard cubic feet per hour
0.225 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 225,000 btu per hour/ 1,020 average btu/scf
= 220.59 standard cubic feet per hourx 14.00 number of units
= 3,088 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
3,088 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 29,758,235 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 29.76 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
29,758,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 226.16 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.026 lbs of particulate matter per hour
Maximum 8760 hrs/yr
IA - Combustion
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
226.16 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.113 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
29,758,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 163.67 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.019 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
163.67 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.08 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
29,758,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 17.85 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0020 lbs of SO2 per hour
Calculating tons of SO2 per year
17.85 pounds of SO2 per year/ 2,000 pounds per ton
= 0.009 tons of SO2 per year
Calculating pounds of NOx per hour
29,758,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 2,975.82 pounds of NOx per year/ 8,760 maximum hours per year
= 0.34 lbs of NOx per hour
IA - Combustion
Calculating tons of NOx per year
2,976 pounds of NOx per year/ 2,000 pounds per ton
= 1.49 tons of NOx per year
Calculating pounds of CO per hour
29,758,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 2,500 pounds of CO per year/ 8,760 maximum hours per year
= 0.29 lbs of CO per hour
Calculating tons of CO per year
2,500 pounds of CO per year/ 2,000 pounds per ton
= 1.25 tons of CO per year
Calculating pounds of CO2 per hour
29,758,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO factor in lbs per million standard cubic feet
= 3,570,988 pounds of CO per year/ 8,760 maximum hours per year
= 407.65 lbs of CO per hour
Calculating tons of CO2 per year
3,570,988 pounds of CO per year/ 2,000 pounds per ton
= 1,785.49 tons of CO2 per year
Calculating pounds of ammonia (NH3) per hour
29,758,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 3.2000 lead factor in lbs per million standard cubic feet
= 95.226 pounds of ammonia per year/ 8,760 maximum hours per year
= 0.0109 lbs of ammonia per hour
IA - Combustion
Calculating tons of ammonia (NH3) per year
95.226 pounds of ammonia per year/ 2,000 pounds per ton
= 0.048 tons of ammonia per year
IA - Combustion 2
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Evcon Furnace
Emission Source mmbtu/hr
Nat Gas Fired units 0.150 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
0.150 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 150,000 btu per hour/ 1,020 average btu/scf
= 147.06 standard cubic feet per hourx 1.00 number of units
= 147 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
147 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 1.42 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 10.77 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.001 lbs of particulate matter per hour
Maximum 8760 hrs/yr
IA - Combustion 2
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
10.77 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.005 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 7.79 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.001 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
7.79 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.004 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 0.85 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0001 lbs of SO2 per hour
Calculating tons of SO2 per year
0.85 pounds of SO2 per year/ 2,000 pounds per ton
= 0.0004 tons of SO2 per year
Calculating pounds of NOx per hour
1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 141.71 pounds of NOx per year/ 8,760 maximum hours per year
= 0.02 lbs of NOx per hour
IA - Combustion 2
Calculating tons of NOx per year
142 pounds of NOx per year/ 2,000 pounds per ton
= 0.07 tons of NOx per year
Calculating pounds of CO per hour
1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 119 pounds of CO per year/ 8,760 maximum hours per year
= 0.01 lbs of CO per hour
Calculating tons of CO per year
119 pounds of CO per year/ 2,000 pounds per ton
= 0.06 tons of CO per year
Calculating pounds of CO2 per hour
1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 170,047 pounds of CO2 per year/ 8,760 maximum hours per year
= 19 lbs of CO2 per hour
Calculating tons of CO2 per year
170,047 pounds of CO2 per year/ 2,000 pounds per ton
= 85 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 3.259 pounds of methane per year/ 8,760 maximum hours per year
= 0.0004 lbs of methane per hour
IA - Combustion 2
Calculating tons of methane (CH4) per year
3.259 pounds of methane per year/ 2,000 pounds per ton
= 0.002 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
1,417,059 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 3.118 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0004 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
3.118 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.002 tons of nitrous oxide per year
Calculating pounds of CO2e per hour20
Calculating pounds of CO2e per year86
IA - Combustion 3
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Weil Mclain GV Boiler
Emission Source mmbtu/hr
Nat Gas Fired units 0.350 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
0.350 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 350,000 btu per hour/ 1,020 average btu/scf
= 343.14 standard cubic feet per hourx 1.00 number of units
= 343 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
343 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 3.31 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 25.13 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.003 lbs of particulate matter per hour
Maximum 8760 hrs/yr
IA - Combustion 3
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
25.13 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.013 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 18.19 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.002 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
18.19 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.01 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 1.98 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0002 lbs of SO2 per hour
Calculating tons of SO2 per year
1.98 pounds of SO2 per year/ 2,000 pounds per ton
= 0.001 tons of SO2 per year
Calculating pounds of NOx per hour
3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 330.65 pounds of NOx per year/ 8,760 maximum hours per year
= 0.04 lbs of NOx per hour
IA - Combustion 3
Calculating tons of NOx per year
331 pounds of NOx per year/ 2,000 pounds per ton
= 0.17 tons of NOx per year
Calculating pounds of CO per hour
3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 278 pounds of CO per year/ 8,760 maximum hours per year
= 0.03 lbs of CO per hour
Calculating tons of CO per year
278 pounds of CO per year/ 2,000 pounds per ton
= 0.14 tons of CO per year
Calculating pounds of CO2 per hour
3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 396,776 pounds of CO2 per year/ 8,760 maximum hours per year
= 45 lbs of CO2 per hour
Calculating tons of CO2 per year
396,776 pounds of CO2 per year/ 2,000 pounds per ton
= 198 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 7.605 pounds of methane per year/ 8,760 maximum hours per year
= 0.0009 lbs of methane per hour
IA - Combustion 3
Calculating tons of methane (CH4) per year
7.605 pounds of methane per year/ 2,000 pounds per ton
= 0.004 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
3,306,471 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 7.274 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0008 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
7.274 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.004 tons of nitrous oxide per year
Calculating pounds of CO2e per hour46
Calculating pounds of CO2e per year200
EQUI 1 (EU23) Cleaning Solvents
Silgan Containers - Ft. Dodge, IA Confidential EQUI 1 (EU23) Cleaning Solvents Page C-60
Silgan Containers Manufacturing CorporationSavage, MNCleaning Solvents Sample Calculations
Total capacity 35.00
Material: Aromatic 100 gallons/hr
700 maximum anticipated gallons used for presses7.25 density pounds per gallon
0.00% volume percent water and exempt solvents7.25 VOC content pounds per gallon less water
5,075.00 total pounds of VOC evolved from Aromatic 1002.54 total tons of VOC evolved from Aromatic 1002.50 maximum anticipated gallons used per hour
18.13 total pounds of VOC evolved per hour
Isopropyl Alcohol(IPA)
700 maximum anticipated gallons used for presses6.59 density pounds per gallon
0.00% volume percent water and exempt solvents6.59 VOC content pounds per gallon less water
4,613.00 total pounds of VOC evolved from IPA2.31 total tons of VOC evolved from IPA2.50 maximum anticipated gallons used per hour
16.48 total pounds of VOC evolved per hour
Heptane3,000 maximum anticipated gallons used for presses
5.80 density pounds per gallon0.00% volume percent water and exempt solvents
5.80 VOC content pounds per gallon less water17,400.00 total pounds of VOC evolved from Heptane
8.70 total tons of VOC evolved from Heptane2.50 maximum anticipated gallons used per hour
14.50 total pounds of VOC evolved per hour
Acetone200 maximum anticipated gallons used for presses6.59 density pounds per gallon
100.00% volume percent water and exempt solvents0.00 VOC content pounds per gallon less water- total pounds of VOC evolved from D60- total tons of VOC evolved from D602.5 maximum anticipated gallons used per hour
0 total pounds of VOC evolved per hour
EQUI 1 (EU23) Cleaning Solvents
Silgan Containers - Ft. Dodge, IA Confidential EQUI 1 (EU23) Cleaning Solvents Page C-61
Butyl
5,000 maximum anticipated gallons used7.50 density pounds per gallon
0.00% volume percent water and exempt solvents7.50 VOC content pounds per gallon less water
37,500.00 total pounds of VOC evolved from Butyl18.75 total tons of VOC evolved from Butyl10.00 maximum anticipated gallons used per hour75.00 total pounds of VOC evolved per hour
E30
8,000 maximum anticipated gallons used7.33 density pounds per gallon
0.00% volume percent water and exempt solvents7.33 VOC content pounds per gallon less water
58,640.00 total pounds of VOC evolved from E3029.32 total tons of VOC evolved from E3010.00 maximum anticipated gallons used per hour73.30 total pounds of VOC evolved per hour
Mineral Spirits
700 maximum anticipated gallons used6.50 density pounds per gallon
0.00% volume percent water and exempt solvents6.50 VOC content pounds per gallon less water
4,550.00 total pounds of VOC evolved 2.28 total tons of VOC evolved 2.50 maximum anticipated gallons used per hour
16.25 total pounds of VOC evolved per hour
PMA
500 maximum anticipated gallons used8.05 density pounds per gallon
0.00% volume percent water and exempt solvents8.05 VOC content pounds per gallon less water
4,025.00 total pounds of VOC evolved 2.01 total tons of VOC evolved 2.50 maximum anticipated gallons used per hour
20.13 total pounds of VOC evolved per hour
EQUI 42 (EU025)
Campbell Soup Company Confidential EQUI 42 (EU025) Page C-62
Savage Sample Calculations
Sheet Size InformationCoater Line 2
Max Sheet Max SheetSize SpeedSQ IN (x) SPM (y)1417.8 100
Production Requirements
100 maximum sheets per minutex 60 minutes per hour
= 6,000 maximum sheets per hour
6,000 maximum sheets per hour
End coating Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Coating 21S00AA 8.56 density pounds per gallonCoating 30.88% percent solids
0.00% volume percent water and exempt solvents5.91 VOC content pounds per gallon less water
10633.50 film weight (milligrams of solids per sheet)
Calculating milligrams of solids per 1000 sheets manufactured
10633.500 film weight (milligrams of solids per sheet)x 1,000 sheets per 1000 sheets
= 10,633,500.00 milligrams of solids per 1000 sheets
Calculating pounds of solids per gallon of coating material
8.56 density pounds per gallonx 30.88% percent solids
= 2.643 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
2.643 pounds of solids per gallonx 453,600 milligrams per pound
= 1,199,013.581 milligrams of solids per gallon of coating
EQUI 42 (EU025)
Campbell Soup Company Confidential EQUI 42 (EU025) Page C-63
Calculating gallons of coating material per 1000 sheets manufactured
10,633,500.000 milligrams of solids per 1000 sheets/ 1,199,013.581 milligrams of solids per gallon of coating
= 8.868540 gallons of coating material per 1000 sheets
Converting from gallons per end to sheets per gallon
1,000 sheets per 1000 sheets/ 8.868540 standard yield of coating per 1000 sheets
= 112.758 sheets per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.000 volume percent water and exempt solventsx 5.91 VOC content pounds per gallon less water
= 5.91 VOCWX pounds per gallon
Calculating maximum gallons per hour
6,000 maximum sheets per hour/ 112.758 sheets per gallon
= 53.211 maximum Gallons per hour
Calculating pounds of material used per hour
53.211 maximum Gallons per hourx 8.560 density pounds per gallon
= 455.488 pounds of coating per hour
Calculating total hourly pounds of VOC emissions
53.211 maximum Gallons per hourx 5.910 VOCWX pounds per gallon
= 314.478 pounds per hour of VOC without controls
= 314.48 maximum pounds of VOC without controls= 15.724 maximum pounds of VOC with controls (95% CE)
Calculating worst case hourly pounds of emissions at stack
314.478 maximum pounds of VOC without controlsx 100% capture efficiency of coating applicators
= 314.48 maximum pounds per hour of VOC at stack
EQUI 42 (EU025)
Campbell Soup Company Confidential EQUI 42 (EU025) Page C-64
Calculating worst case hourly pounds of uncaptured VOC emissions
314.478 maximum pounds of VOC without controlsx 0% percent of hourly emissions uncaptured
= 0.000 maximum pounds per hour of VOC fugitive
Calculating annual coating usage in gallons
6,000 maximum sheets per hour/ 112.758 sheets per gallonx 8760.000 hours per year
= 466,130.467 maximum annual coating usage in gallons
Calculating annual coating usage in tons
466,130.467 maximum annual coating usage in gallonsx 8.56 density pounds per gallon
= 3,990,076.795 maximum annual coating usage in pounds/ 2000.000 pounds per ton
= 1995.038 maximum annual coating usage in tons
Calculating maximum tons per year of VOC without controls
466,130.467 maximum annual coating usage in gallonsx 5.910 VOCWX pounds per gallon
= 2,754,831.058 maximum pounds per year of VOC/ 2,000 pounds per ton
= 1377.4 maximum tons per year of VOC without controls
Calculating worst case annual tons of emissions at stack
1377.416 maximum tons per year of VOC without controlsx 100% capture efficiency of coating applicators
= 1377.4 maximum tons per year of VOC at stack
Controlled emissions tpy
1377.4 maximum tons per year of VOC without controlsx 95.0% percent control
= 68.9 maximum tons per year of VOC uncaptured
EQUI 41 (EU004)
Campbell Soup Company Confidential EQUI 41 (EU004) Page C-65
Savage Sample Calculations
Sheet Size InformationCoater Line 3
Max Sheet Max SheetSize SpeedSQ IN (x) SPM (y)1417.8 100
Production Requirements
100 maximum sheets per minutex 60 minutes per hour
= 6,000 maximum sheets per hour
6,000 maximum sheets per hour
End coating Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Coating 21S00AA 8.56 density pounds per gallonCoating 30.88% percent solids
0.00% volume percent water and exempt solvents5.91 VOC content pounds per gallon less water
10633.50 film weight (milligrams of solids per sheet)
Calculating milligrams of solids per 1000 sheets manufactured
10633.500 film weight (milligrams of solids per sheet)x 1,000 sheets per 1000 sheets
= 10,633,500.00 milligrams of solids per 1000 sheets
Calculating pounds of solids per gallon of coating material
8.56 density pounds per gallonx 30.88% percent solids
= 2.643 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
2.643 pounds of solids per gallonx 453,600 milligrams per pound
= 1,199,013.581 milligrams of solids per gallon of coating
EQUI 41 (EU004)
Campbell Soup Company Confidential EQUI 41 (EU004) Page C-66
Calculating gallons of coating material per 1000 sheets manufactured
10,633,500.000 milligrams of solids per 1000 sheets/ 1,199,013.581 milligrams of solids per gallon of coating
= 8.868540 gallons of coating material per 1000 sheets
Converting from gallons per end to sheets per gallon
1,000 sheets per 1000 sheets/ 8.868540 standard yield of coating per 1000 sheets
= 112.758 sheets per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.000 volume percent water and exempt solventsx 5.91 VOC content pounds per gallon less water
= 5.91 VOCWX pounds per gallon
Calculating maximum gallons per hour
6,000 maximum sheets per hour/ 112.758 sheets per gallon
= 53.211 maximum Gallons per hour
Calculating pounds of material used per hour
53.211 maximum Gallons per hourx 8.560 density pounds per gallon
= 455.488 pounds of coating per hour
Calculating total hourly pounds of VOC emissions
53.211 maximum Gallons per hourx 5.910 VOCWX pounds per gallon
= 314.478 pounds per hour of VOC without controls
= 314.48 maximum pounds of VOC without controls= 15.724 maximum pounds of VOC with controls (99.5% CE)
Calculating worst case hourly pounds of emissions at stack
314.478 maximum pounds of VOC without controlsx 100% capture efficiency of coating applicators
= 314.48 maximum pounds per hour of VOC at stack
EQUI 41 (EU004)
Campbell Soup Company Confidential EQUI 41 (EU004) Page C-67
Calculating worst case hourly pounds of uncaptured VOC emissions
314.478 maximum pounds of VOC without controlsx 0% percent of hourly emissions uncaptured
= 0.000 maximum pounds per hour of VOC fugitive
Calculating annual coating usage in gallons
6,000 maximum sheets per hour/ 112.758 sheets per gallonx 8760.000 hours per year
= 466,130.467 maximum annual coating usage in gallons
Calculating annual coating usage in tons
466,130.467 maximum annual coating usage in gallonsx 8.56 density pounds per gallon
= 3,990,076.795 maximum annual coating usage in pounds/ 2000.000 pounds per ton
= 1995.038 maximum annual coating usage in tons
Calculating maximum tons per year of VOC without controls
466,130.467 maximum annual coating usage in gallonsx 5.910 VOCWX pounds per gallon
= 2,754,831.058 maximum pounds per year of VOC/ 2,000 pounds per ton
= 1377.4 maximum tons per year of VOC without controls
Calculating worst case annual tons of emissions at stack
1377.416 maximum tons per year of VOC without controlsx 100% capture efficiency of coating applicators
= 1377.4 maximum tons per year of VOC at stack
Controlled Emissions tpy
1377.4 maximum tons per year of VOC without controlsx 95.0% percent control
= 68.9 maximum tons per year of VOC uncaptured
Sheet Size
Max Sheet Max SheetSize SpeedSQ IN (x) SPM (y)
Coaters 1417.8 100
(a) (e) Max TONMax Coating (b) ( c) (d) Lbs VOC (f) (g) VOC/YR
Silgan Weight Density Weight % Max Gals per Gal Max LBS Max TON After ControlsCoating ID MGS/4 SQ IN LBS/GAL Solids ctg/hr CTG VOC/HR VOC/HR 99.5% Effic.A.19.1 13 8.03 34.80 21.8 5.24 114.3 500.6 2.5A.30.5 15 8.27 30.90 27.5 5.72 157.4 689.5 3.4A.45.5 18 7.95 34.16 31.1 5.23 162.5 711.9 3.6A.45.6 20 7.95 34.55 34.1 5.2 177.5 777.5 3.9A.64.2 18 8.39 32.56 30.9 5.66 174.9 765.9 3.8A.67.4 24 8.39 34.50 38.9 5.49 213.4 934.8 4.7C.10.1 20 8.72 42.14 25.5 5.05 128.9 564.4 2.8C.17.5 23 8.4 37.03 34.7 5.29 183.4 803.3 4.0C.22.5 24 8.3 55.10 24.6 3.73 91.8 402.0 2.0E.1.11 21 7.98 31.42 39.3 5.47 214.8 940.8 4.7E.1.7 18 7.97 30.82 34.4 5.51 189.3 829.2 4.1E.1.9 25 7.98 31.75 46.3 5.45 252.1 1104.3 5.5E.2.1 16 8.14 37.66 24.5 5.07 124.1 543.4 2.7E.13.5 16 7.95 30.41 31.0 5.54 171.9 752.9 3.8E.25.5 13 7.95 29.52 26.0 5.6 145.4 637.0 3.2E.36.5 18 7.97 31.19 33.9 5.49 186.4 816.4 4.1E.43.5 20 8.04 32.00 36.4 5.47 199.4 873.2 4.4E.43.6 30 8.06 32.94 53.0 5.41 286.6 1255.4 6.3 21S00AAE.54.5 18 7.95 30.35 35.0 5.54 193.8 848.7 4.2E.59.5 17 7.99 32.16 31.0 5.42 168.1 736.4 3.7G.41.5 16 8.08 31.87 29.1 5.51 160.5 703.0 3.5G.41.6 18 8.09 32.31 32.3 5.48 176.9 775.0 3.9O.116.1 12 8.12 33.70 20.6 5.38 110.6 484.5 2.4O.116.2 18 8.12 33.70 30.8 5.38 165.9 726.7 3.6V.20.5 35 8.8 57.18 32.6 3.77 122.9 538.5 2.7W.34.5 34 9.49 46.61 36.0 5.07 182.7 800.3 4.0
(d) = (((a/4)*(x)*(y))/453600)/b*c/100 * 60(f) = (d) * (e)(g) = ((f)*8760/2000)
EQUI44 (EU003)
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Wagner Coating Oven Line 2
Emission Source mmbtu/hr
Nat Gas Fired Ovens 4.000 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
4.000 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 4,000,000 btu per hour/ 1,020 average btu/scf
= 3,921.57 standard cubic feet per hourx 1.00 number of ovens
= 3,922 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
3,922 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 37.79 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 287.19 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.033 lbs of particulate matter per hour
Maximum 8760 hrs/yr
EQUI44 (EU003)
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
287.19 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.144 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 207.84 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.023725 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
207.84 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.1039 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 22.67 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0026 lbs of SO2 per hour
Calculating tons of SO2 per year
22.67 pounds of SO2 per year/ 2,000 pounds per ton
= 0.011 tons of SO2 per year
Calculating pounds of NOx per hour
37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 3,778.82 pounds of NOx per year/ 8,760 maximum hours per year
= 0.43 lbs of NOx per hour
EQUI44 (EU003)
Calculating tons of NOx per year
3,779 pounds of NOx per year/ 2,000 pounds per ton
= 1.89 tons of NOx per year
Calculating pounds of CO per hour
37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 3,174 pounds of CO per year/ 8,760 maximum hours per year
= 0.36 lbs of CO per hour
Calculating tons of CO per year
3,174 pounds of CO per year/ 2,000 pounds per ton
= 1.59 tons of CO per year
Calculating pounds of CO2 per hour
37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 4,534,588 pounds of CO2 per year/ 8,760 maximum hours per year
= 518 lbs of CO2 per hour
Calculating tons of CO2 per year
4,534,588 pounds of CO2 per year/ 2,000 pounds per ton
= 2,267 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 86.913 pounds of methane per year/ 8,760 maximum hours per year
= 0.0099 lbs of methane per hour
EQUI44 (EU003)
Calculating tons of methane (CH4) per year
86.913 pounds of methane per year/ 2,000 pounds per ton
= 0.043 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
37,788,235 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 83.134 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0095 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
83.134 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.042 tons of nitrous oxide per year
Calculating pounds of CO2e per hour521
Calculating pounds of CO2e per year2,281
EQUI 43 (EU006)
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Wagner Coating Oven Line 3
Emission Source mmbtu/hr
Nat Gas Fired Ovens 6.000 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
6.000 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 6,000,000 btu per hour/ 1,020 average btu/scf
= 5,882.35 standard cubic feet per hourx 1.00 number of ovens
= 5,882 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
5,882 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 56.68 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 430.79 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.049 lbs of particulate matter per hour
Maximum 8760 hrs/yr
EQUI 43 (EU006)
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
430.79 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.215 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 311.75 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.036 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
311.75 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.16 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 34.01 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0039 lbs of SO2 per hour
Calculating tons of SO2 per year
34.01 pounds of SO2 per year/ 2,000 pounds per ton
= 0.017 tons of SO2 per year
Calculating pounds of NOx per hour
56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 5,668.24 pounds of NOx per year/ 8,760 maximum hours per year
= 0.65 lbs of NOx per hour
EQUI 43 (EU006)
Calculating tons of NOx per year
5,668 pounds of NOx per year/ 2,000 pounds per ton
= 2.83 tons of NOx per year
Calculating pounds of CO per hour
56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 4,761 pounds of CO per year/ 8,760 maximum hours per year
= 0.54 lbs of CO per hour
Calculating tons of CO per year
4,761 pounds of CO per year/ 2,000 pounds per ton
= 2.38 tons of CO per year
Calculating pounds of CO2 per hour
56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 6,801,882 pounds of CO2 per year/ 8,760 maximum hours per year
= 776 lbs of CO2 per hour
Calculating tons of CO2 per year
6,801,882 pounds of CO2 per year/ 2,000 pounds per ton
= 3,401 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 130.369 pounds of methane per year/ 8,760 maximum hours per year
= 0.0149 lbs of methane per hour
EQUI 43 (EU006)
Calculating tons of methane (CH4) per year
130.369 pounds of methane per year/ 2,000 pounds per ton
= 0.065 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
56,682,353 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 124.701 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0142 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
124.701 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.062 tons of nitrous oxide per year
Calculating pounds of CO2e per hour781
Calculating pounds of CO2e per year3,421
EQUI 8 (EU020)
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Rapid Make-up Air Heater
Emission Source mmbtu/hr
Nat Gas Fired units 10.725 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
10.725 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 10,725,000 btu per hour/ 1,020 average btu/scf
= 10,514.71 standard cubic feet per hourx 1.00 number of units
= 10,515 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
10,515 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 101.32 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 770.03 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.088 lbs of particulate matter per hour
Maximum 8760 hrs/yr
EQUI 8 (EU020)
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
770.03 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.385 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 557.26 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.064 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
557.26 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.28 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 60.79 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0069 lbs of SO2 per hour
Calculating tons of SO2 per year
60.79 pounds of SO2 per year/ 2,000 pounds per ton
= 0.030 tons of SO2 per year
Calculating pounds of NOx per hour
101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 10,131.97 pounds of NOx per year/ 8,760 maximum hours per year
= 1.16 lbs of NOx per hour
EQUI 8 (EU020)
Calculating tons of NOx per year
10,132 pounds of NOx per year/ 2,000 pounds per ton
= 5.07 tons of NOx per year
Calculating pounds of CO per hour
101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 8,511 pounds of CO per year/ 8,760 maximum hours per year
= 0.97 lbs of CO per hour
Calculating tons of CO per year
8,511 pounds of CO per year/ 2,000 pounds per ton
= 4.26 tons of CO per year
Calculating pounds of CO2 per hour
101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 12,158,365 pounds of CO2 per year/ 8,760 maximum hours per year
= 1,388 lbs of CO2 per hour
Calculating tons of CO2 per year
12,158,365 pounds of CO2 per year/ 2,000 pounds per ton
= 6,079 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 233.035 pounds of methane per year/ 8,760 maximum hours per year
= 0.0266 lbs of methane per hour
EQUI 8 (EU020)
Calculating tons of methane (CH4) per year
233.035 pounds of methane per year/ 2,000 pounds per ton
= 0.117 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
101,319,706 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 222.903 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0254 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
222.903 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.111 tons of nitrous oxide per year
Calculating pounds of CO2e per hour1,396
Calculating pounds of CO2e per year6,115
EQUI 9 (EU021)
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Rapid Make-up Air Heater
Emission Source mmbtu/hr
Nat Gas Fired units 6.400 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
6.400 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 6,400,000 btu per hour/ 1,020 average btu/scf
= 6,274.51 standard cubic feet per hourx 1.00 number of units
= 6,275 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
6,275 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 60.46 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 459.50 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.052 lbs of particulate matter per hour
Maximum 8760 hrs/yr
EQUI 9 (EU021)
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
459.50 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.230 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 332.54 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.038 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
332.54 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.17 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 36.28 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0041 lbs of SO2 per hour
Calculating tons of SO2 per year
36.28 pounds of SO2 per year/ 2,000 pounds per ton
= 0.018 tons of SO2 per year
Calculating pounds of NOx per hour
60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 6,046.12 pounds of NOx per year/ 8,760 maximum hours per year
= 0.69 lbs of NOx per hour
EQUI 9 (EU021)
Calculating tons of NOx per year
6,046 pounds of NOx per year/ 2,000 pounds per ton
= 3.02 tons of NOx per year
Calculating pounds of CO per hour
60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 5,079 pounds of CO per year/ 8,760 maximum hours per year
= 0.58 lbs of CO per hour
Calculating tons of CO per year
5,079 pounds of CO per year/ 2,000 pounds per ton
= 2.54 tons of CO per year
Calculating pounds of CO2 per hour
60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 7,255,341 pounds of CO2 per year/ 8,760 maximum hours per year
= 828 lbs of CO2 per hour
Calculating tons of CO2 per year
7,255,341 pounds of CO2 per year/ 2,000 pounds per ton
= 3,628 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 139.061 pounds of methane per year/ 8,760 maximum hours per year
= 0.0159 lbs of methane per hour
EQUI 9 (EU021)
Calculating tons of methane (CH4) per year
139.061 pounds of methane per year/ 2,000 pounds per ton
= 0.070 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
60,461,176 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 133.015 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0152 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
133.015 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.067 tons of nitrous oxide per year
Calculating pounds of CO2e per hour833
Calculating pounds of CO2e per year3,649
TREA 1 (EU024)
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
TEC Magnum 24000 Catalytic Oxidizer
Emission Source mmbtu/hr
Nat Gas Fired units 11.000 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
11.000 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 11,000,000 btu per hour/ 1,020 average btu/scf
= 10,784.31 standard cubic feet per hourx 1.00 number of units
= 10,784 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
10,784 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 103.92 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 789.77 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.090 lbs of particulate matter per hour
Maximum 8760 hrs/yr
TREA 1 (EU024)
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
789.77 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.395 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 571.55 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.065 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
571.55 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.29 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 62.35 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0071 lbs of SO2 per hour
Calculating tons of SO2 per year
62.35 pounds of SO2 per year/ 2,000 pounds per ton
= 0.031 tons of SO2 per year
Calculating pounds of NOx per hour
103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 10,391.76 pounds of NOx per year/ 8,760 maximum hours per year
= 1.19 lbs of NOx per hour
TREA 1 (EU024)
Calculating tons of NOx per year
10,392 pounds of NOx per year/ 2,000 pounds per ton
= 5.20 tons of NOx per year
Calculating pounds of CO per hour
103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 8,729 pounds of CO per year/ 8,760 maximum hours per year
= 1.00 lbs of CO per hour
Calculating tons of CO per year
8,729 pounds of CO per year/ 2,000 pounds per ton
= 4.36 tons of CO per year
Calculating pounds of CO2 per hour
103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 12,470,118 pounds of CO2 per year/ 8,760 maximum hours per year
= 1,424 lbs of CO2 per hour
Calculating tons of CO2 per year
12,470,118 pounds of CO2 per year/ 2,000 pounds per ton
= 6,235 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 239.011 pounds of methane per year/ 8,760 maximum hours per year
= 0.0273 lbs of methane per hour
TREA 1 (EU024)
Calculating tons of methane (CH4) per year
239.011 pounds of methane per year/ 2,000 pounds per ton
= 0.120 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
103,917,647 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 228.619 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0261 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
228.619 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.114 tons of nitrous oxide per year
Calculating pounds of CO2e per hour1,432
Calculating pounds of CO2e per year6,272
EQUI 38 (EU026)
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Applied Air System Make-up Air Heater
Emission Source mmbtu/hr
Nat Gas Fired units 2.800 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
2.800 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 2,800,000 btu per hour/ 1,020 average btu/scf
= 2,745.10 standard cubic feet per hourx 1.00 number of units
= 2,745 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
2,745 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 26.45 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 201.03 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.023 lbs of particulate matter per hour
Maximum 8760 hrs/yr
EQUI 38 (EU026)
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
201.03 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.101 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 145.48 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.017 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
145.48 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.07 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 15.87 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0018 lbs of SO2 per hour
Calculating tons of SO2 per year
15.87 pounds of SO2 per year/ 2,000 pounds per ton
= 0.008 tons of SO2 per year
Calculating pounds of NOx per hour
26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 2,645.18 pounds of NOx per year/ 8,760 maximum hours per year
= 0.30 lbs of NOx per hour
EQUI 38 (EU026)
Calculating tons of NOx per year
2,645 pounds of NOx per year/ 2,000 pounds per ton
= 1.32 tons of NOx per year
Calculating pounds of CO per hour
26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 2,222 pounds of CO per year/ 8,760 maximum hours per year
= 0.25 lbs of CO per hour
Calculating tons of CO per year
2,222 pounds of CO per year/ 2,000 pounds per ton
= 1.11 tons of CO per year
Calculating pounds of CO2 per hour
26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 3,174,212 pounds of CO2 per year/ 8,760 maximum hours per year
= 362 lbs of CO2 per hour
Calculating tons of CO2 per year
3,174,212 pounds of CO2 per year/ 2,000 pounds per ton
= 1,587 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 60.839 pounds of methane per year/ 8,760 maximum hours per year
= 0.0069 lbs of methane per hour
EQUI 38 (EU026)
Calculating tons of methane (CH4) per year
60.839 pounds of methane per year/ 2,000 pounds per ton
= 0.030 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
26,451,765 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 58.194 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0066 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
58.194 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.029 tons of nitrous oxide per year
Calculating pounds of CO2e per hour365
Calculating pounds of CO2e per year1,597
EQUI 39 (EU027)
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
ICE Make-up Air Heater
Emission Source mmbtu/hr
Nat Gas Fired units 2.750 Max Firing Rate
Emissions Factors (EF)
PM 7.6 lbs/mmscf AP-42 Chapter 1.4PM10 7.6 lbs/mmscfPM2.5 7.6 lbs/mmscfSO2 0.6 lbs/mmscf Average natural gas heating value = 1,020 btu/scfNOx 100.0 lbs/mmscfCO 84.0 lbs/mmscfCO2 120,000.0 lbs/mmscfVOC 5.5 lbs/mmscfMethane 2.3 lbs/mmscfN2O 2.2 lbs/mmscf
Calculating standard cubic feet per hour
2.750 million btu per hour maximum firing ratex 1,000,000 btu per mmbtu
= 2,750,000 btu per hour/ 1,020 average btu/scf
= 2,696.08 standard cubic feet per hourx 1.00 number of units
= 2,696 maximum standard cubic feet per houraverage consumption
Calculating standard cubic feet of natural gas per year
2,696 standard cubic feet per hourx 8,760 maximum hours per yearx 1.10 startup and shutdown factor
= 25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 standard cubic feet per million standard cubic feet (mmscf)
= 25.98 million standard cubic feet of natural gas burned per year
Calculating pounds of particulate matter (PM, PM10 and PM2.5) per hour
25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 7.60 PM factor in lbs per million standard cubic feet
= 197.44 pounds of particulate matter per year/ 8,760 maximum hours per year
= 0.023 lbs of particulate matter per hour
Maximum 8760 hrs/yr
EQUI 39 (EU027)
Calculating tons of particulate matter (PM, PM10 and PM2.5) per year
197.44 pounds of particulate matter per year/ 2,000 pounds per ton
= 0.099 tons of particulate matter per year
Calculating pounds of non-methane VOC per hour
25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 5.50 non-methane VOC factor in lbs per million standard cubic feet
= 142.89 pounds of non-methane VOC per year/ 8,760 maximum hours per year
= 0.016 lbs of non-methane VOC per hour
Calculating tons of non-methane VOC per year
142.89 pounds of non-methane VOC per year/ 2,000 pounds per ton
= 0.07 tons of non-methane VOC per year
Calculating pounds of SO2 per hour
25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 0.60 SO2 factor in lbs per million standard cubic feet
= 15.59 pounds of SO2 per year/ 8,760 maximum hours per year
= 0.0018 lbs of SO2 per hour
Calculating tons of SO2 per year
15.59 pounds of SO2 per year/ 2,000 pounds per ton
= 0.008 tons of SO2 per year
Calculating pounds of NOx per hour
25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 100.0 NOx factor in lbs per million standard cubic feet
= 2,597.94 pounds of NOx per year/ 8,760 maximum hours per year
= 0.30 lbs of NOx per hour
EQUI 39 (EU027)
Calculating tons of NOx per year
2,598 pounds of NOx per year/ 2,000 pounds per ton
= 1.30 tons of NOx per year
Calculating pounds of CO per hour
25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 84.00 CO factor in lbs per million standard cubic feet
= 2,182 pounds of CO per year/ 8,760 maximum hours per year
= 0.25 lbs of CO per hour
Calculating tons of CO per year
2,182 pounds of CO per year/ 2,000 pounds per ton
= 1.09 tons of CO per year
Calculating pounds of CO2 per hour
25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 120,000.00 CO2 factor in lbs per million standard cubic feet
= 3,117,529 pounds of CO2 per year/ 8,760 maximum hours per year
= 356 lbs of CO2 per hour
Calculating tons of CO2 per year
3,117,529 pounds of CO2 per year/ 2,000 pounds per ton
= 1,559 tons of CO2 per year
Calculating pounds of methane (CH4) per hour
25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.3000 methane factor in lbs per million standard cubic feet
= 59.753 pounds of methane per year/ 8,760 maximum hours per year
= 0.0068 lbs of methane per hour
EQUI 39 (EU027)
Calculating tons of methane (CH4) per year
59.753 pounds of methane per year/ 2,000 pounds per ton
= 0.030 tons of methane per year
Calculating pounds of nitrous oxide (N2O) per hour
25,979,412 standard cubic feet of natural gas burned per year/ 1,000,000 scf per mmscfx 2.2000 nitrous oxide factor in lbs per million standard cubic feet
= 57.155 pounds of nitrous oxide per year/ 8,760 maximum hours per year
= 0.0065 lbs of nitrous oxide per hour
Calculating tons of nitrous oxide (N2O) per year
57.155 pounds of nitrous oxide per year/ 2,000 pounds per ton
= 0.029 tons of nitrous oxide per year
Calculating pounds of CO2e per hour358
Calculating pounds of CO2e per year1,568
Combustion HAPs
HAP Name CAS
(lbs/million scf)Total Group CapacityGroup Fuel ComsumptionPOM* 0.0000863Benzene 71-43-2 0.0021Dichlorobenzene 25321-22-6 1.20E-03Formaldehyde 50-00-0 0.075Hexane 110-54-3 1.8Naphthalene 91-20-3 0.00061Toluene 108-88-3 0.0034Arsenic 7440-38-2 0.0002Beryllium 7440-41-7 0.000012Cadmium 7440-43-9 0.0011Chromium 7440-47-3 0.0014Cobalt 7440-48-4 0.000084Manganese 7439-96-5 0.00038Mercury 7439-97-6 0.00026Nickel 7440-02-0 0.0021Selenium 7782-49-2 0.000024SUM
7a) Fuel Type Natural Gas7d) Heat Value: 1020 Btu/cfSource of Data - AP-42, table 1.4-3 dated 7/98
Emission Factor*
Combustion HAPs
*POM = Sum of pollutants identified as POM in AP-42 Table 1.4-3, dated 3/98:Acenaphthene 0.0000018Acenaphthylene 0.0000018Anthracene 0.0000024Benz(a)anthracene 0.0000018Benzo(a)pyrene 0.0000012Benzo(b)fluoranthene 0.0000018Benzo(g,h,i)perylene 0.0000012Benzo(k)fluoranthene 0.0000018Chrysene 0.0000018Dibenzo(a,h)anthrancene 0.00000127,12-Dimethylbenz(a)anthracene 0.000016Fluoranthene 0.000003Fluorene 0.0000028Indo(1,2,3-ed)pyrene 0.00000182-Methylnaphthalene 0.0000243-Methylchloranthrene 0.0000018Phenanthrene 0.000017Pyrene 0.000005
Sum 0.0000863
Combustion HAPs
HAP Name
Total Group CapacityGroup Fuel ComsumptionPOM*BenzeneDichlorobenzeneFormaldehydeHexaneNaphthaleneTolueneArsenicBerylliumCadmiumChromiumCobaltManganeseMercuryNickelSeleniumSUM
7a) Fuel Type7d) Heat Value:Source of Data - AP-42, table 1.4-3 dated 7/98
(lb/hr) (tons/yr) (lb/hr) (tons/yr)4 Mmbtu/hr 6 MMbtu/hr
3921.57 cf/hr 5882.35 cf/hr3.38E-07 1.48E-06 5.08E-07 2.22E-068.24E-06 3.61E-05 1.24E-05 5.41E-054.71E-06 2.06E-05 7.06E-06 3.09E-052.94E-04 1.29E-03 4.41E-04 1.93E-037.06E-03 3.09E-02 1.06E-02 4.64E-022.39E-06 1.05E-05 3.59E-06 1.57E-051.33E-05 5.84E-05 2.00E-05 8.76E-057.84E-07 3.44E-06 1.18E-06 5.15E-064.71E-08 2.06E-07 7.06E-08 3.09E-074.31E-06 1.89E-05 6.47E-06 2.83E-055.49E-06 2.40E-05 8.24E-06 3.61E-053.29E-07 1.44E-06 4.94E-07 2.16E-061.49E-06 6.53E-06 2.24E-06 9.79E-061.02E-06 4.47E-06 1.53E-06 6.70E-068.24E-06 3.61E-05 1.24E-05 5.41E-059.41E-08 4.12E-07 1.41E-07 6.18E-077.40E-03 3.24E-02 1.11E-02 4.86E-02
max ind. HAP
EQUI44 (EU 003) EQUI43 (EU 006)
Emission Rate Max Uncontrolled Emissions Emission Rate Max Uncontrolled
Emissions
Combustion HAPs
*POM = Sum of pollutants identified as POM in AP-42 Tab AcenaphtheneAcenaphthyleneAnthraceneBenz(a)anthraceneBenzo(a)pyreneBenzo(b)fluorantheneBenzo(g,h,i)peryleneBenzo(k)fluorantheneChryseneDibenzo(a,h)anthrancene7,12-Dimethylbenz(a)anthraceneFluorantheneFluoreneIndo(1,2,3-ed)pyrene2-Methylnaphthalene3-MethylchloranthrenePhenanthrenePyrene
Sum
Combustion HAPs
HAP Name
Total Group CapacityGroup Fuel ComsumptionPOM*BenzeneDichlorobenzeneFormaldehydeHexaneNaphthaleneTolueneArsenicBerylliumCadmiumChromiumCobaltManganeseMercuryNickelSeleniumSUM
7a) Fuel Type7d) Heat Value:Source of Data - AP-42, table 1.4-3 dated 7/98
(lb/hr) (tons/yr) (lb/hr) (tons/yr)10.725 MMbtu/hr 6.4 MMbtu/hr
10514.71 cf/hr 6274.51 cf/hr9.07E-07 3.97E-06 5.41E-07 2.37E-062.21E-05 9.67E-05 1.32E-05 5.77E-051.26E-05 5.53E-05 7.53E-06 3.30E-057.89E-04 3.45E-03 4.71E-04 2.06E-031.89E-02 8.29E-02 1.13E-02 4.95E-026.41E-06 2.81E-05 3.83E-06 1.68E-053.58E-05 1.57E-04 2.13E-05 9.34E-052.10E-06 9.21E-06 1.25E-06 5.50E-061.26E-07 5.53E-07 7.53E-08 3.30E-071.16E-05 5.07E-05 6.90E-06 3.02E-051.47E-05 6.45E-05 8.78E-06 3.85E-058.83E-07 3.87E-06 5.27E-07 2.31E-064.00E-06 1.75E-05 2.38E-06 1.04E-052.73E-06 1.20E-05 1.63E-06 7.15E-062.21E-05 9.67E-05 1.32E-05 5.77E-052.52E-07 1.11E-06 1.51E-07 6.60E-071.99E-02 8.69E-02 1.18E-02 5.19E-02
EQUI8 (EU 020)
Emission Rate Max Uncontrolled Emissions
EQUI9 (EU 021)
Emission Rate Max Uncontrolled Emissions
Combustion HAPs
*POM = Sum of pollutants identified as POM in AP-42 Tab AcenaphtheneAcenaphthyleneAnthraceneBenz(a)anthraceneBenzo(a)pyreneBenzo(b)fluorantheneBenzo(g,h,i)peryleneBenzo(k)fluorantheneChryseneDibenzo(a,h)anthrancene7,12-Dimethylbenz(a)anthraceneFluorantheneFluoreneIndo(1,2,3-ed)pyrene2-Methylnaphthalene3-MethylchloranthrenePhenanthrenePyrene
Sum
Combustion HAPs
HAP Name
Total Group CapacityGroup Fuel ComsumptionPOM*BenzeneDichlorobenzeneFormaldehydeHexaneNaphthaleneTolueneArsenicBerylliumCadmiumChromiumCobaltManganeseMercuryNickelSeleniumSUM
7a) Fuel Type7d) Heat Value:Source of Data - AP-42, table 1.4-3 dated 7/98
(lb/hr) (tons/yr) (lb/hr) (tons/yr)11 MMbtu/hr 2.8 MMbtu/hr
10784.31 cf/hr 2745.10 cf/hr9.31E-07 4.08E-06 2.37E-07 1.04E-062.26E-05 9.92E-05 5.76E-06 2.52E-051.29E-05 5.67E-05 3.29E-06 1.44E-058.09E-04 3.54E-03 2.06E-04 9.02E-041.94E-02 8.50E-02 4.94E-03 2.16E-026.58E-06 2.88E-05 1.67E-06 7.33E-063.67E-05 1.61E-04 9.33E-06 4.09E-052.16E-06 9.45E-06 5.49E-07 2.40E-061.29E-07 5.67E-07 3.29E-08 1.44E-071.19E-05 5.20E-05 3.02E-06 1.32E-051.51E-05 6.61E-05 3.84E-06 1.68E-059.06E-07 3.97E-06 2.31E-07 1.01E-064.10E-06 1.79E-05 1.04E-06 4.57E-062.80E-06 1.23E-05 7.14E-07 3.13E-062.26E-05 9.92E-05 5.76E-06 2.52E-052.59E-07 1.13E-06 6.59E-08 2.89E-072.04E-02 8.92E-02 5.18E-03 2.27E-02
TREA1 (EU 024)
Emission Rate Max Uncontrolled Emissions
EQUI 38 (EU 026)
Emission Rate Max Uncontrolled Emissions
Combustion HAPs
*POM = Sum of pollutants identified as POM in AP-42 Tab AcenaphtheneAcenaphthyleneAnthraceneBenz(a)anthraceneBenzo(a)pyreneBenzo(b)fluorantheneBenzo(g,h,i)peryleneBenzo(k)fluorantheneChryseneDibenzo(a,h)anthrancene7,12-Dimethylbenz(a)anthraceneFluorantheneFluoreneIndo(1,2,3-ed)pyrene2-Methylnaphthalene3-MethylchloranthrenePhenanthrenePyrene
Sum
Combustion HAPs
HAP Name
Total Group CapacityGroup Fuel ComsumptionPOM*BenzeneDichlorobenzeneFormaldehydeHexaneNaphthaleneTolueneArsenicBerylliumCadmiumChromiumCobaltManganeseMercuryNickelSeleniumSUM
7a) Fuel Type7d) Heat Value:Source of Data - AP-42, table 1.4-3 dated 7/98
(lb/hr) (tons/yr) (lb/hr) (tons/yr)2.75 MMbtu/hr 0.15 MMbtu/hr
2696.08 cf/hr 147.06 cf/hr2.33E-07 1.02E-06 1.27E-08 5.56E-085.66E-06 2.48E-05 3.09E-07 1.35E-063.24E-06 1.42E-05 1.76E-07 7.73E-072.02E-04 8.86E-04 1.10E-05 4.83E-054.85E-03 2.13E-02 2.65E-04 1.16E-031.64E-06 7.20E-06 8.97E-08 3.93E-079.17E-06 4.02E-05 5.00E-07 2.19E-065.39E-07 2.36E-06 2.94E-08 1.29E-073.24E-08 1.42E-07 1.76E-09 7.73E-092.97E-06 1.30E-05 1.62E-07 7.09E-073.77E-06 1.65E-05 2.06E-07 9.02E-072.26E-07 9.92E-07 1.24E-08 5.41E-081.02E-06 4.49E-06 5.59E-08 2.45E-077.01E-07 3.07E-06 3.82E-08 1.67E-075.66E-06 2.48E-05 3.09E-07 1.35E-066.47E-08 2.83E-07 3.53E-09 1.55E-085.09E-03 2.23E-02 2.78E-04 1.22E-03
EQUI39 (EU 027)
Emission Rate Max Uncontrolled Emissions
IA - EU 028
Emission Rate Max Uncontrolled Emissions
Combustion HAPs
*POM = Sum of pollutants identified as POM in AP-42 Tab AcenaphtheneAcenaphthyleneAnthraceneBenz(a)anthraceneBenzo(a)pyreneBenzo(b)fluorantheneBenzo(g,h,i)peryleneBenzo(k)fluorantheneChryseneDibenzo(a,h)anthrancene7,12-Dimethylbenz(a)anthraceneFluorantheneFluoreneIndo(1,2,3-ed)pyrene2-Methylnaphthalene3-MethylchloranthrenePhenanthrenePyrene
Sum
Combustion HAPs
HAP Name
Total Group CapacityGroup Fuel ComsumptionPOM*BenzeneDichlorobenzeneFormaldehydeHexaneNaphthaleneTolueneArsenicBerylliumCadmiumChromiumCobaltManganeseMercuryNickelSeleniumSUM
7a) Fuel Type7d) Heat Value:Source of Data - AP-42, table 1.4-3 dated 7/98
Sum
(lb/hr) (tons/yr) (tons/yr)0.35 MMbtu/hr
343.14 cf/hr2.96E-08 1.30E-07 1.62E-057.21E-07 3.16E-06 3.94E-044.12E-07 1.80E-06 2.25E-042.57E-05 1.13E-04 1.41E-026.18E-04 2.71E-03 3.38E-012.09E-07 9.17E-07 1.14E-041.17E-06 5.11E-06 6.38E-046.86E-08 3.01E-07 3.75E-054.12E-09 1.80E-08 2.25E-063.77E-07 1.65E-06 2.06E-044.80E-07 2.10E-06 2.63E-042.88E-08 1.26E-07 1.58E-051.30E-07 5.71E-07 7.13E-058.92E-08 3.91E-07 4.88E-057.21E-07 3.16E-06 3.94E-048.24E-09 3.61E-08 4.50E-066.48E-04 2.84E-03 3.54E-01
Max single HAP 3.38E-01
Max Uncontroll
IA - EU 029
Emission Rate Max Uncontrolled Emissions
Combustion HAPs
*POM = Sum of pollutants identified as POM in AP-42 Tab AcenaphtheneAcenaphthyleneAnthraceneBenz(a)anthraceneBenzo(a)pyreneBenzo(b)fluorantheneBenzo(g,h,i)peryleneBenzo(k)fluorantheneChryseneDibenzo(a,h)anthrancene7,12-Dimethylbenz(a)anthraceneFluorantheneFluoreneIndo(1,2,3-ed)pyrene2-Methylnaphthalene3-MethylchloranthrenePhenanthrenePyrene
Sum
EQUI 12 (EU008) -211A Liner
Campbell Soup Company Confidential EQUI 12 (EU008) -211A Liner Page C-109
Savage Sample Calculations
End Size Information211A Ends
Production Requirements
1,400 maximum ends per minutex 60 minutes per hour
= 84,000 maximum ends per hour
735,840,000 maximum ends per year
End Compound Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Compound: Darex 9385HC57 8.40 density pounds per gallonEnd Compound Liner 57.00% percent solids
0.40% volume percent water and exempt solvents3.59 VOC content pounds per gallon less water
67.00 film weight (milligrams of solids per end)
Calculating milligrams of solids per 1000 ends manufactured
67.000 film weight (milligrams of solids per end)x 1,000 ends per 1000 ends
= 67,000.00 milligrams of solids per 1000 ends
Calculating pounds of solids per gallon of coating material
8.40 density pounds per gallonx 57.00% percent solids
= 4.788 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
4.788 pounds of solids per gallonx 453,600 milligrams per pound
= 2,171,836.800 milligrams of solids per gallon of coating
Calculating gallons of coating material per 1000 ends manufactured
67,000.000 milligrams of solids per 1000 ends/ 2,171,836.800 milligrams of solids per gallon of coating
= 0.030849 gallons of coating material per 1000 ends
EQUI 12 (EU008) -211A Liner
Campbell Soup Company Confidential EQUI 12 (EU008) -211A Liner Page C-110
Converting from gallons per end to ends per gallon
1,000 ends per 1000 ends/ 0.030849 standard yield of coating per 1000 ends
= 32,415.475 ends per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.004 volume percent water and exempt solventsx 3.59 VOC content pounds per gallon less water
= 3.58 VOCWX pounds per gallon
Calculating maximum gallons per hour
84,000 maximum ends per hour/ 32,415.475 ends per gallon
= 2.591 maximum Gallons per hour
Calculating pounds of material used per hour
2.591 maximum Gallons per hourx 8.400 density pounds per gallon
= 21.767 pounds of compound per hour
Calculating total hourly pounds of VOC emissions
2.591 maximum Gallons per hourx 3.576 VOCWX pounds per gallon
= 9.266 pounds per hour of VOC without controlsx 1.100 ten percent variance allowance
= 10.192 maximum pounds of VOC without controls
Calculating worst case hourly pounds of emissions at stack
9.266 maximum pounds of VOC without controlsx 90% capture efficiency of compound applicators
= 8.339 maximum pounds per hour of VOC at stack
Calculating worst case hourly pounds of uncaptured VOC emissions
9.266 maximum pounds of VOC without controlsx 10% percent of hourly emissions uncaptured
= 0.927 maximum pounds per hour of VOC fugitive
EQUI 12 (EU008) -211A Liner
Campbell Soup Company Confidential EQUI 12 (EU008) -211A Liner Page C-111
Calculating annual compound usage in gallons
735,840,000 maximum ends per year/ 32,415.475 ends per gallon
= 22,700.269 maximum annual compound usage in gallons
Calculating annual compound usage in tons
22,700.269 maximum annual compound usage in gallonsx 8.40 density pounds per gallon
= 190,682.261 maximum annual compound usage in pounds/ 2000.000 pounds per ton
= 95.341 maximum annual compound usage in tons
Calculating maximum tons per year of VOC without controls
22,700.269 maximum annual compound usage in gallonsx 3.576 VOCWX pounds per gallon
= 81,167.991 maximum pounds per year of VOC/ 2,000 pounds per ton
= 40.584 maximum tons per year of VOC without controls
EQUI 12 (EU008) -Mister 211A
Silgan Containers - Ft. Madison, IA EQUI 12 (EU008) -Mister 211A Page C-112
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 211a
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 1204 6.84 density pounds per gallonMister Spray 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.11 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.11 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.02 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.02 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.11 maximum pounds per hour of mister spray
Calculating maximum pounds per hour of VOC without controls
0.02 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.11 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.11 maximum pounds of VOC per hour from mister spray
EQUI 12 (EU008) -Mister 211A
Silgan Containers - Ft. Madison, IA EQUI 12 (EU008) -Mister 211A Page C-113
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.02 maximum gallons of mister spray used per applicator per hour
= 140.88 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 140.88 total gallons of misting spray per year
Calculating annual mister spray usage in tons
140.88 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 963.60 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 0.48 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 0.48 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
140.88 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 963.60 maximum pounds per year of VOC/ 2,000 pounds per ton
= 0.48 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
0.48 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 0.48 total tons of VOC emissions from misting spray
EQUI 12 (EU008) Lubricator211A
Silgan Containers - Ft. Madison, IA EQUI 12 (EU008) Lubricator211A Page C-114
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 211a
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 165 6.84 density pounds per gallonLube 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.72 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.72 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.11 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.11 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.72 maximum pounds per hour of mister spray
Calculating maximum pounds per hour of VOC without controls
0.11 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.72 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.72 maximum pounds of VOC per hour from mister spray
EQUI 12 (EU008) Lubricator211A
Silgan Containers - Ft. Madison, IA EQUI 12 (EU008) Lubricator211A Page C-115
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.11 maximum gallons of mister spray used per applicator per hour
= 922.11 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 922.11 total gallons of misting spray per year
Calculating annual mister spray usage in tons
922.11 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 6,307.20 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 3.15 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 3.15 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
922.11 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 6,307.20 maximum pounds per year of VOC/ 2,000 pounds per ton
= 3.15 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
3.15 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 3.15 total tons of VOC emissions from misting spray
EQUI 16 (EU012) -211B Liner
Campbell Soup Company Confidential EQUI 16 (EU012) -211B Liner Page C-116
Savage Sample Calculations
End Size Information211B Ends
Production Requirements
1400 maximum ends per minutex 60 minutes per hour
= 84,000 maximum ends per hour
735,840,000 maximum ends per year
End Compound Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Compound: Darex 9385HC57 8.40 density pounds per gallonEnd Compound Liner 57.00% percent solids
0.40% volume percent water and exempt solvents3.59 VOC content pounds per gallon less water
67.00 film weight (milligrams of solids per end)
Calculating milligrams of solids per 1000 ends manufactured
67.000 film weight (milligrams of solids per end)x 1,000 ends per 1000 ends
= 67,000.00 milligrams of solids per 1000 ends
Calculating pounds of solids per gallon of coating material
8.40 density pounds per gallonx 57.00% percent solids
= 4.788 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
4.788 pounds of solids per gallonx 453,600 milligrams per pound
= 2,171,836.800 milligrams of solids per gallon of coating
Calculating gallons of coating material per 1000 ends manufactured
67,000.000 milligrams of solids per 1000 ends/ 2,171,836.800 milligrams of solids per gallon of coating
= 0.030849 gallons of coating material per 1000 ends
EQUI 16 (EU012) -211B Liner
Campbell Soup Company Confidential EQUI 16 (EU012) -211B Liner Page C-117
Converting from gallons per end to ends per gallon
1,000 ends per 1000 ends/ 0.030849 standard yield of coating per 1000 ends
= 32,415.475 ends per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.004 volume percent water and exempt solventsx 3.59 VOC content pounds per gallon less water
= 3.58 VOCWX pounds per gallon
Calculating maximum gallons per hour
84,000 maximum ends per hour/ 32,415.475 ends per gallon
= 2.591 maximum Gallons per hour
Calculating pounds of material used per hour
2.591 maximum Gallons per hourx 8.400 density pounds per gallon
= 21.767 pounds of compound per hour
Calculating total hourly pounds of VOC emissions
2.591 maximum Gallons per hourx 3.576 VOCWX pounds per gallon
= 9.266 pounds per hour of VOC without controlsx 1.100 ten percent variance allowance
= 10.192 maximum pounds of VOC without controls
Calculating worst case hourly pounds of emissions at stack
9.266 maximum pounds of VOC without controlsx 90% capture efficiency of compound applicators
= 8.339 maximum pounds per hour of VOC at stack
Calculating worst case hourly pounds of uncaptured VOC emissions
9.266 maximum pounds of VOC without controlsx 10% percent of hourly emissions uncaptured
= 0.927 maximum pounds per hour of VOC fugitive
EQUI 16 (EU012) -211B Liner
Campbell Soup Company Confidential EQUI 16 (EU012) -211B Liner Page C-118
Calculating annual compound usage in gallons
735,840,000 maximum ends per year/ 32,415.475 ends per gallon
= 22,700.269 maximum annual compound usage in gallons
Calculating annual compound usage in tons
22,700.269 maximum annual compound usage in gallonsx 8.40 density pounds per gallon
= 190,682.261 maximum annual compound usage in pounds/ 2000.000 pounds per ton
= 95.341 maximum annual compound usage in tons
Calculating maximum tons per year of VOC without controls
22,700.269 maximum annual compound usage in gallonsx 3.576 VOCWX pounds per gallon
= 81,167.991 maximum pounds per year of VOC/ 2,000 pounds per ton
= 40.584 maximum tons per year of VOC without controls
EQUI 16 (EU012) -Mister 211B
Silgan Containers - Ft. Madison, IA EQUI 16 (EU012) -Mister 211B Page C-119
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 211b
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 1204 6.84 density pounds per gallonMister Spray 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.11 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.11 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.02 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.02 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.11 maximum pounds per hour of mister spray
EQUI 16 (EU012) -Mister 211B
Silgan Containers - Ft. Madison, IA EQUI 16 (EU012) -Mister 211B Page C-120
Calculating maximum pounds per hour of VOC without controls
0.02 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.11 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.11 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.02 maximum gallons of mister spray used per applicator per hour
= 140.88 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 140.88 total gallons of misting spray per year
Calculating annual mister spray usage in tons
140.88 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 963.60 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 0.48 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 0.48 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
140.88 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 963.60 maximum pounds per year of VOC/ 2,000 pounds per ton
= 0.48 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
0.48 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 0.48 total tons of VOC emissions from misting spray
EQUI 16 (EU012) Lubricator 211B
Silgan Containers - Ft. Madison, IA EQUI 16 (EU012) Lubricator 211B Page C-121
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 211b
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 165 6.84 density pounds per gallonLube 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.72 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.72 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.11 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.11 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.72 maximum pounds per hour of mister spray
EQUI 16 (EU012) Lubricator 211B
Silgan Containers - Ft. Madison, IA EQUI 16 (EU012) Lubricator 211B Page C-122
Calculating maximum pounds per hour of VOC without controls
0.11 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.72 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.72 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.11 maximum gallons of mister spray used per applicator per hour
= 922.11 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 922.11 total gallons of misting spray per year
Calculating annual mister spray usage in tons
922.11 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 6,307.20 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 3.15 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 3.15 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
922.11 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 6,307.20 maximum pounds per year of VOC/ 2,000 pounds per ton
= 3.15 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
3.15 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 3.15 total tons of VOC emissions from misting spray
EQUI 17 (EU013) -211C Liner
Campbell Soup Company Confidential EQUI 17 (EU013) -211C Liner Page C-123
Savage Sample Calculations
End Size Information211C Ends
Production Requirements
1400 maximum ends per minutex 60 minutes per hour
= 84,000 maximum ends per hour
735,840,000 maximum ends per year
End Compound Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Compound: Darex 9385HC57 8.40 density pounds per gallonEnd Compound Liner 57.00% percent solids
0.40% volume percent water and exempt solvents3.59 VOC content pounds per gallon less water
67.00 film weight (milligrams of solids per end)
Calculating milligrams of solids per 1000 ends manufactured
67.000 film weight (milligrams of solids per end)x 1,000 ends per 1000 ends
= 67,000.00 milligrams of solids per 1000 ends
Calculating pounds of solids per gallon of coating material
8.40 density pounds per gallonx 57.00% percent solids
= 4.788 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
4.788 pounds of solids per gallonx 453,600 milligrams per pound
= 2,171,836.800 milligrams of solids per gallon of coating
Calculating gallons of coating material per 1000 ends manufactured
67,000.000 milligrams of solids per 1000 ends/ 2,171,836.800 milligrams of solids per gallon of coating
= 0.030849 gallons of coating material per 1000 ends
EQUI 17 (EU013) -211C Liner
Campbell Soup Company Confidential EQUI 17 (EU013) -211C Liner Page C-124
Converting from gallons per end to ends per gallon
1,000 ends per 1000 ends/ 0.030849 standard yield of coating per 1000 ends
= 32,415.475 ends per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.004 volume percent water and exempt solventsx 3.59 VOC content pounds per gallon less water
= 3.58 VOCWX pounds per gallon
Calculating maximum gallons per hour
84,000 maximum ends per hour/ 32,415.475 ends per gallon
= 2.591 maximum Gallons per hour
Calculating pounds of material used per hour
2.591 maximum Gallons per hourx 8.400 density pounds per gallon
= 21.767 pounds of compound per hour
Calculating total hourly pounds of VOC emissions
2.591 maximum Gallons per hourx 3.576 VOCWX pounds per gallon
= 9.266 pounds per hour of VOC without controlsx 1.100 ten percent variance allowance
= 10.192 maximum pounds of VOC without controls
Calculating worst case hourly pounds of emissions at stack
9.266 maximum pounds of VOC without controlsx 90% capture efficiency of compound applicators
= 8.339 maximum pounds per hour of VOC at stack
EQUI 17 (EU013) -211C Liner
Campbell Soup Company Confidential EQUI 17 (EU013) -211C Liner Page C-125
Calculating worst case hourly pounds of uncaptured VOC emissions0
9.266 maximum pounds of VOC without controlsx 10% percent of hourly emissions uncaptured
= 0.927 maximum pounds per hour of VOC fugitive
Calculating annual compound usage in gallons
735,840,000 maximum ends per year/ 32,415.475 ends per gallon
= 22,700.269 maximum annual compound usage in gallons
Calculating annual compound usage in tons
22,700.269 maximum annual compound usage in gallonsx 8.40 density pounds per gallon
= 190,682.261 maximum annual compound usage in pounds/ 2000.000 pounds per ton
= 95.341 maximum annual compound usage in tons
Calculating maximum tons per year of VOC without controls
22,700.269 maximum annual compound usage in gallonsx 3.576 VOCWX pounds per gallon
= 81,167.991 maximum pounds per year of VOC/ 2,000 pounds per ton
= 40.584 maximum tons per year of VOC without controls
EQUI 17 (EU013) -Mister 211C
Silgan Containers - Ft. Madison, IA EQUI 17 (EU013) -Mister 211C Page C-126
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 211c
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 1204 6.84 density pounds per gallonMister Spray 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.11 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.11 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.02 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.02 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.11 maximum pounds per hour of mister spray
EQUI 17 (EU013) -Mister 211C
Silgan Containers - Ft. Madison, IA EQUI 17 (EU013) -Mister 211C Page C-127
Calculating maximum pounds per hour of VOC without controls
0.02 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.11 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.11 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.02 maximum gallons of mister spray used per applicator per hour
= 140.88 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 140.88 total gallons of misting spray per year
Calculating annual mister spray usage in tons
140.88 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 963.60 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 0.48 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 0.48 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
140.88 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 963.60 maximum pounds per year of VOC/ 2,000 pounds per ton
= 0.48 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
0.48 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 0.48 total tons of VOC emissions from misting spray
EQUI 13 (EU009) -300A Liner
Campbell Soup Company Confidential EQUI 13 (EU009) -300A Liner Page C-128
Savage Sample Calculations
End Size Information300A Ends
Production Requirements
1400 maximum ends per minutex 60 minutes per hour
= 84,000 maximum ends per hour
735,840,000 maximum ends per year
End Compound Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Compound: Darex 9385HC57 8.40 density pounds per gallonEnd Compound Liner 57.00% percent solids
0.40% volume percent water and exempt solvents3.59 VOC content pounds per gallon less water
71.00 film weight (milligrams of solids per end)
Calculating milligrams of solids per 1000 ends manufactured
71.000 film weight (milligrams of solids per end)x 1,000 ends per 1000 ends
= 71,000.00 milligrams of solids per 1000 ends
Calculating pounds of solids per gallon of coating material
8.40 density pounds per gallonx 57.00% percent solids
= 4.788 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
4.788 pounds of solids per gallonx 453,600 milligrams per pound
= 2,171,836.800 milligrams of solids per gallon of coating
Calculating gallons of coating material per 1000 ends manufactured
71,000.000 milligrams of solids per 1000 ends/ 2,171,836.800 milligrams of solids per gallon of coating
= 0.032691 gallons of coating material per 1000 ends
EQUI 13 (EU009) -300A Liner
Campbell Soup Company Confidential EQUI 13 (EU009) -300A Liner Page C-129
Converting from gallons per end to ends per gallon
1,000 ends per 1000 ends/ 0.032691 standard yield of coating per 1000 ends
= 30,589.251 ends per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.004 volume percent water and exempt solventsx 3.59 VOC content pounds per gallon less water
= 3.58 VOCWX pounds per gallon
Calculating maximum gallons per hour
84,000 maximum ends per hour/ 30,589.251 ends per gallon
= 2.746 maximum Gallons per hour
Calculating pounds of material used per hour
2.746 maximum Gallons per hourx 8.400 density pounds per gallon
= 23.067 pounds of compound per hour
Calculating total hourly pounds of VOC emissions
2.746 maximum Gallons per hourx 3.576 VOCWX pounds per gallon
= 9.819 pounds per hour of VOC without controlsx 1.100 ten percent variance allowance
= 10.801 maximum pounds of VOC without controls
Calculating worst case hourly pounds of emissions at stack
9.819 maximum pounds of VOC without controlsx 90% capture efficiency of compound applicators
= 8.837 maximum pounds per hour of VOC at stack
EQUI 13 (EU009) -300A Liner
Campbell Soup Company Confidential EQUI 13 (EU009) -300A Liner Page C-130
Calculating worst case hourly pounds of uncaptured VOC emissions
9.819 maximum pounds of VOC without controlsx 10% percent of hourly emissions uncaptured
= 0.982 maximum pounds per hour of VOC fugitive
Calculating annual compound usage in gallons
735,840,000 maximum ends per year/ 30,589.251 ends per gallon
= 24,055.509 maximum annual compound usage in gallons
Calculating annual compound usage in tons
24,055.509 maximum annual compound usage in gallonsx 8.40 density pounds per gallon
= 202,066.277 maximum annual compound usage in pounds/ 2000.000 pounds per ton
= 101.033 maximum annual compound usage in tons
Calculating maximum tons per year of VOC without controls
24,055.509 maximum annual compound usage in gallonsx 3.576 VOCWX pounds per gallon
= 86,013.841 maximum pounds per year of VOC/ 2,000 pounds per ton
= 43.007 maximum tons per year of VOC without controls
EQUI 13 (EU009) -Mister 300A
Silgan Containers - Ft. Madison, IA EQUI 13 (EU009) -Mister 300A Page C-131
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 300a
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 1204 6.84 density pounds per gallonMister Spray 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.11 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.11 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.02 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.02 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.11 maximum pounds per hour of mister spray
EQUI 13 (EU009) -Mister 300A
Silgan Containers - Ft. Madison, IA EQUI 13 (EU009) -Mister 300A Page C-132
Calculating maximum pounds per hour of VOC without controls
0.02 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.11 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.11 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.02 maximum gallons of mister spray used per applicator per hour
= 140.88 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 140.88 total gallons of misting spray per year
Calculating annual mister spray usage in tons
140.88 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 963.60 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 0.48 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 0.48 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
140.88 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 963.60 maximum pounds per year of VOC/ 2,000 pounds per ton
= 0.48 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
0.48 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 0.48 total tons of VOC emissions from misting spray
EQUI 13 (EU009 -Lubricator 300A
Silgan Containers - Ft. Madison, IA EQUI 13 (EU009 -Lubricator 300A Page C-133
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 300a
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 165 6.84 density pounds per gallonLube 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.72 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.72 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.11 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.11 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.72 maximum pounds per hour of mister spray
EQUI 13 (EU009 -Lubricator 300A
Silgan Containers - Ft. Madison, IA EQUI 13 (EU009 -Lubricator 300A Page C-134
Calculating maximum pounds per hour of VOC without controls
0.11 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.72 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.72 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.11 maximum gallons of mister spray used per applicator per hour
= 922.11 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 922.11 total gallons of misting spray per year
Calculating annual mister spray usage in tons
922.11 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 6,307.20 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 3.15 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 3.15 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
922.11 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 6,307.20 maximum pounds per year of VOC/ 2,000 pounds per ton
= 3.15 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
3.15 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 3.15 total tons of VOC emissions from misting spray
EQUI 14 (EU010) -300B liner
Campbell Soup Company Confidential EQUI 14 (EU010) -300B liner Page C-135
Savage Sample Calculations
End Size Information300B Ends
Production Requirements
1400 maximum ends per minutex 60 minutes per hour
= 84,000 maximum ends per hour
735,840,000 maximum ends per year
End Compound Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Compound: Darex 9385HC57 8.40 density pounds per gallonEnd Compound Liner 57.00% percent solids
0.40% volume percent water and exempt solvents3.59 VOC content pounds per gallon less water
71.00 film weight (milligrams of solids per end)
Calculating milligrams of solids per 1000 ends manufactured
71.000 film weight (milligrams of solids per end)x 1,000 ends per 1000 ends
= 71,000.00 milligrams of solids per 1000 ends
Calculating pounds of solids per gallon of coating material
8.40 density pounds per gallonx 57.00% percent solids
= 4.788 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
4.788 pounds of solids per gallonx 453,600 milligrams per pound
= 2,171,836.800 milligrams of solids per gallon of coating
Calculating gallons of coating material per 1000 ends manufactured
71,000.000 milligrams of solids per 1000 ends/ 2,171,836.800 milligrams of solids per gallon of coating
= 0.032691 gallons of coating material per 1000 ends
EQUI 14 (EU010) -300B liner
Campbell Soup Company Confidential EQUI 14 (EU010) -300B liner Page C-136
Converting from gallons per end to ends per gallon
1,000 ends per 1000 ends/ 0.032691 standard yield of coating per 1000 ends
= 30,589.251 ends per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.004 volume percent water and exempt solventsx 3.59 VOC content pounds per gallon less water
= 3.58 VOCWX pounds per gallon
Calculating maximum gallons per hour
84,000 maximum ends per hour/ 30,589.251 ends per gallon
= 2.746 maximum Gallons per hour
Calculating pounds of material used per hour
2.746 maximum Gallons per hourx 8.400 density pounds per gallon
= 23.067 pounds of compound per hour
Calculating total hourly pounds of VOC emissions
2.746 maximum Gallons per hourx 3.576 VOCWX pounds per gallon
= 9.819 pounds per hour of VOC without controlsx 1.100 ten percent variance allowance
= 10.801 maximum pounds of VOC without controls
Calculating worst case hourly pounds of emissions at stack
9.819 maximum pounds of VOC without controlsx 90% capture efficiency of compound applicators
= 8.837 maximum pounds per hour of VOC at stack
Calculating worst case hourly pounds of uncaptured VOC emissions
9.819 maximum pounds of VOC without controlsx 10% percent of hourly emissions uncaptured
= 0.982 maximum pounds per hour of VOC fugitive
EQUI 14 (EU010) -300B liner
Campbell Soup Company Confidential EQUI 14 (EU010) -300B liner Page C-137
Calculating annual compound usage in gallons
735,840,000 maximum ends per year/ 30,589.251 ends per gallon
= 24,055.509 maximum annual compound usage in gallons
Calculating annual compound usage in tons
24,055.509 maximum annual compound usage in gallonsx 8.40 density pounds per gallon
= 202,066.277 maximum annual compound usage in pounds/ 2000.000 pounds per ton
= 101.033 maximum annual compound usage in tons
Calculating maximum tons per year of VOC without controls
24,055.509 maximum annual compound usage in gallonsx 3.576 VOCWX pounds per gallon
= 86,013.841 maximum pounds per year of VOC/ 2,000 pounds per ton
= 43.007 maximum tons per year of VOC without controls
EQUI 14 (EU010) -Mister 300B
Silgan Containers - Ft. Madison, IA EQUI 14 (EU010) -Mister 300B Page C-138
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 300b
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 1204 6.84 density pounds per gallonMister Spray 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.11 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.11 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.02 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.02 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.11 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.11 maximum pounds per hour of mister spray
EQUI 14 (EU010) -Mister 300B
Silgan Containers - Ft. Madison, IA EQUI 14 (EU010) -Mister 300B Page C-139
Calculating maximum pounds per hour of VOC without controls
0.02 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.11 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.11 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.02 maximum gallons of mister spray used per applicator per hour
= 140.88 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 140.88 total gallons of misting spray per year
Calculating annual mister spray usage in tons
140.88 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 963.60 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 0.48 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 0.48 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
140.88 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 963.60 maximum pounds per year of VOC/ 2,000 pounds per ton
= 0.48 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
0.48 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 0.48 total tons of VOC emissions from misting spray
EQUI 14 (EU010 -Lubricator 300B
Silgan Containers - Ft. Madison, IA EQUI 14 (EU010 -Lubricator 300B Page C-140
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 300b
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 165 6.84 density pounds per gallonLube 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.72 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.72 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.11 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.11 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.72 maximum pounds per hour of mister spray
Calculating maximum pounds per hour of VOC without controls
0.11 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.72 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.72 maximum pounds of VOC per hour from mister spray
EQUI 14 (EU010 -Lubricator 300B
Silgan Containers - Ft. Madison, IA EQUI 14 (EU010 -Lubricator 300B Page C-141
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.11 maximum gallons of mister spray used per applicator per hour
= 922.11 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 922.11 total gallons of misting spray per year
Calculating annual mister spray usage in tons
922.11 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 6,307.20 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 3.15 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 3.15 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
922.11 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 6,307.20 maximum pounds per year of VOC/ 2,000 pounds per ton
= 3.15 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
3.15 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 3.15 total tons of VOC emissions from misting spray
EQUI 15 (EU011) -300 liner
Campbell Soup Company Confidential EQUI 15 (EU011) -300 liner Page C-142
Savage Sample Calculations
End Size Information303 Ends
Production Requirements
1400 maximum ends per minutex 60 minutes per hour
= 84,000 maximum ends per hour
735,840,000 maximum ends per year
End Compound Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Compound: Darex 9385HC57 8.40 density pounds per gallonEnd Compound Liner 57.00% percent solids
0.40% volume percent water and exempt solvents3.59 VOC content pounds per gallon less water
74.00 film weight (milligrams of solids per end)
Calculating milligrams of solids per 1000 ends manufactured
74.000 film weight (milligrams of solids per end)x 1,000 ends per 1000 ends
= 74,000.00 milligrams of solids per 1000 ends
Calculating pounds of solids per gallon of coating material
8.40 density pounds per gallonx 57.00% percent solids
= 4.788 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
4.788 pounds of solids per gallonx 453,600 milligrams per pound
= 2,171,836.800 milligrams of solids per gallon of coating
Calculating gallons of coating material per 1000 ends manufactured
74,000.000 milligrams of solids per 1000 ends/ 2,171,836.800 milligrams of solids per gallon of coating
EQUI 15 (EU011) -300 liner
Campbell Soup Company Confidential EQUI 15 (EU011) -300 liner Page C-143
= 0.034073 gallons of coating material per 1000 ends
Converting from gallons per end to ends per gallon
1,000 ends per 1000 ends/ 0.034073 standard yield of coating per 1000 ends
= 29,349.146 ends per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.004 volume percent water and exempt solventsx 3.59 VOC content pounds per gallon less water
= 3.58 VOCWX pounds per gallon
Calculating maximum gallons per hour
84,000 maximum ends per hour/ 29,349.146 ends per gallon
= 2.862 maximum Gallons per hour
Calculating pounds of material used per hour
2.862 maximum Gallons per hourx 8.400 density pounds per gallon
= 24.042 pounds of compound per hour
Calculating total hourly pounds of VOC emissions
2.862 maximum Gallons per hourx 3.576 VOCWX pounds per gallon
= 10.234 pounds per hour of VOC without controlsx 1.100 ten percent variance allowance
= 11.257 maximum pounds of VOC without controls
Calculating worst case hourly pounds of emissions at stack
10.234 maximum pounds of VOC without controlsx 90% capture efficiency of compound applicators
= 9.210 maximum pounds per hour of VOC at stack
Calculating worst case hourly pounds of uncaptured VOC emissions0
10.234 maximum pounds of VOC without controlsx 10% percent of hourly emissions uncaptured
EQUI 15 (EU011) -300 liner
Campbell Soup Company Confidential EQUI 15 (EU011) -300 liner Page C-144
= 1.023 maximum pounds per hour of VOC fugitive
Calculating annual compound usage in gallons
735,840,000 maximum ends per year/ 29,349.146 ends per gallon
= 25,071.939 maximum annual compound usage in gallons
Calculating annual compound usage in tons
25,071.939 maximum annual compound usage in gallonsx 8.40 density pounds per gallon
= 210,604.288 maximum annual compound usage in pounds/ 2000.000 pounds per ton
= 105.302 maximum annual compound usage in tons
Calculating maximum tons per year of VOC without controls
25,071.939 maximum annual compound usage in gallonsx 3.576 VOCWX pounds per gallon
= 89,648.228 maximum pounds per year of VOC/ 2,000 pounds per ton
= 44.824 maximum tons per year of VOC without controls
EQUI 15 (EU011) -Mister 300
Silgan Containers - Ft. Madison, IA EQUI 15 (EU011) -Mister 300 Page C-145
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 303
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 1204 6.30 density pounds per gallonMister Spray 0.00% percent solids
0.00% volume percent water and exempt solvents6.30 VOC content pounds per gallon less water0.50 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.50 maximum pounds of mister spray per applicator per hour/ 6.30 density pounds per gallon
= 0.08 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.30 VOC content pounds per gallon less water
= 6.30 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.50 maximum pounds of mister spray per applicator per hour6.30 density pounds per gallon
0.08 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.50 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.50 maximum pounds per hour of mister spray
EQUI 15 (EU011) -Mister 300
Silgan Containers - Ft. Madison, IA EQUI 15 (EU011) -Mister 300 Page C-146
Calculating maximum pounds per hour of VOC without controls
0.08 maximum gallons per hour of mister sprayx 6.30 VOCWX pounds per gallon
= 0.50 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.50 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.08 maximum gallons of mister spray used per applicator per hour
= 695.24 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 695.24 total gallons of misting spray per year
Calculating annual mister spray usage in tons
695.24 maximum gallons of mister spray per applicator per yearx 6.30 density pounds per gallon
= 4,380.00 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 2.19 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 2.19 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
695.24 maximum gallons of mister spray per applicator per yearx 6.30 VOCWX pounds per gallon
= 4,380.00 maximum pounds per year of VOC/ 2,000 pounds per ton
= 2.19 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
2.19 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 2.19 total tons of VOC emissions from misting spray
EQUI 15 (EU011) Lubricator 300
Silgan Containers - Ft. Madison, IA EQUI 15 (EU011) Lubricator 300 Page C-147
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner 211c
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 165 6.84 density pounds per gallonLube 0.00% percent solids
0.00% volume percent water and exempt solvents6.84 VOC content pounds per gallon less water0.72 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.72 maximum pounds of mister spray per applicator per hour/ 6.84 density pounds per gallon
= 0.11 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.84 VOC content pounds per gallon less water
= 6.84 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hour6.84 density pounds per gallon
0.11 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.72 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.72 maximum pounds per hour of mister spray
EQUI 15 (EU011) Lubricator 300
Silgan Containers - Ft. Madison, IA EQUI 15 (EU011) Lubricator 300 Page C-148
Calculating maximum pounds per hour of VOC without controls
0.11 maximum gallons per hour of mister sprayx 6.84 VOCWX pounds per gallon
= 0.72 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.72 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.11 maximum gallons of mister spray used per applicator per hour
= 922.11 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 922.11 total gallons of misting spray per year
Calculating annual mister spray usage in tons
922.11 maximum gallons of mister spray per applicator per yearx 6.84 density pounds per gallon
= 6,307.20 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 3.15 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 3.15 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
922.11 maximum gallons of mister spray per applicator per yearx 6.84 VOCWX pounds per gallon
= 6,307.20 maximum pounds per year of VOC/ 2,000 pounds per ton
= 3.15 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
3.15 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 3.15 total tons of VOC emissions from misting spray
EQUI 18 (EU014) -DRT liner
Campbell Soup Company Confidential EQUI 18 (EU014) -DRT liner Page C-149
Savage Sample Calculations
End Size InformationDRT 300 Ends
Production Requirements
2700 maximum ends per minutex 60 minutes per hour
= 162,000 maximum ends per hour
1,419,120,000 maximum ends per year
End Compound Liner Material Specifications
All material specifications are taken from MSDS, VOC Data, and Material Application sheets.
Compound: Darex 9385HC57 8.40 density pounds per gallonEnd Compound Liner 57.00% percent solids
0.40% volume percent water and exempt solvents3.59 VOC content pounds per gallon less water
64.00 film weight (milligrams of solids per end)
Calculating milligrams of solids per 1000 ends manufactured
64.000 film weight (milligrams of solids per end)x 1,000 ends per 1000 ends
= 64,000.00 milligrams of solids per 1000 ends
Calculating pounds of solids per gallon of coating material
8.40 density pounds per gallonx 57.00% percent solids
= 4.788 pounds of solids per gallon
Calculating milligrams of solids per gallon of coating
4.788 pounds of solids per gallonx 453,600 milligrams per pound
= 2,171,836.800 milligrams of solids per gallon of coating
Calculating gallons of coating material per 1000 ends manufactured
64,000.000 milligrams of solids per 1000 ends/ 2,171,836.800 milligrams of solids per gallon of coating
= 0.029468 gallons of coating material per 1000 ends
EQUI 18 (EU014) -DRT liner
Campbell Soup Company Confidential EQUI 18 (EU014) -DRT liner Page C-150
Converting from gallons per end to ends per gallon
1,000 ends per 1000 ends/ 0.029468 standard yield of coating per 1000 ends
= 33,934.950 ends per gallon
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.004 volume percent water and exempt solventsx 3.59 VOC content pounds per gallon less water
= 3.58 VOCWX pounds per gallon
Calculating maximum gallons per hour
162,000 maximum ends per hour/ 33,934.950 ends per gallon
= 4.774 maximum Gallons per hour
Calculating pounds of material used per hour
4.774 maximum Gallons per hourx 8.400 density pounds per gallon
= 40.100 pounds of compound per hour
Calculating total hourly pounds of VOC emissions
4.774 maximum Gallons per hourx 3.576 VOCWX pounds per gallon
= 17.070 pounds per hour of VOC without controlsx 1.100 ten percent variance allowance
= 18.776 maximum pounds of VOC without controls
Calculating worst case hourly pounds of emissions at stack
17.070 maximum pounds of VOC without controlsx 90% capture efficiency of compound applicators
= 15.363 maximum pounds per hour of VOC at stack
Calculating worst case hourly pounds of uncaptured VOC emissions
17.070 maximum pounds of VOC without controlsx 10% percent of hourly emissions uncaptured
= 1.707 maximum pounds per hour of VOC fugitive
EQUI 18 (EU014) -DRT liner
Campbell Soup Company Confidential EQUI 18 (EU014) -DRT liner Page C-151
Calculating annual compound usage in gallons
1,419,120,000 maximum ends per year/ 33,934.950 ends per gallon
= 41,818.833 maximum annual compound usage in gallons
Calculating annual compound usage in tons
41,818.833 maximum annual compound usage in gallonsx 8.40 density pounds per gallon
= 351,278.195 maximum annual compound usage in pounds/ 2000.000 pounds per ton
= 175.639 maximum annual compound usage in tons
Calculating maximum tons per year of VOC without controls
41,818.833 maximum annual compound usage in gallonsx 3.576 VOCWX pounds per gallon
= 149,529.091 maximum pounds per year of VOC/ 2,000 pounds per ton
= 74.765 maximum tons per year of VOC without controls
EQUI 18 (EU014) -Mister DRT
Silgan Containers - Ft. Madison, IA EQUI 18 (EU014) -Mister DRT Page C-152
Silgan Containers Manufacturing CorporationSavage, MNSample Calculations
Liner Information
End Compound Liner DRT
Mister Spray Material Specifications
All material specifications are taken from MSDS and VOC Data sheets.
KDRAW 1204 6.30 density pounds per gallonMister Spray 0.00% percent solids
0.00% volume percent water and exempt solvents6.30 VOC content pounds per gallon less water0.50 maximum pounds of mister spray per applicator per hour
Calculating maximum gallons of mister spray used per applicator per hour
0.50 maximum pounds of mister spray per applicator per hour/ 6.30 density pounds per gallon
= 0.08 maximum gallons of mister spray used per applicator per hour
Calculating VOCWX (VOC content with water and exempt solvents)
100% Total volume of material- 0.00 volume percent water and exempt solventsx 6.30 VOC content pounds per gallon less water
= 6.30 VOCWX pounds per gallon
Calculating maximum gallons per hour mister spray material
0.50 maximum pounds of mister spray per applicator per hour6.30 density pounds per gallon
0.08 maximum gallons per hour of mister spray
Calculating maximum pounds per hour mister spray material
0.50 maximum pounds of mister spray per applicator per hourx 1 number of current misting spray applicators
= 0.50 maximum pounds per hour of mister spray
EQUI 18 (EU014) -Mister DRT
Silgan Containers - Ft. Madison, IA EQUI 18 (EU014) -Mister DRT Page C-153
Calculating maximum pounds per hour of VOC without controls
0.08 maximum gallons per hour of mister sprayx 6.30 VOCWX pounds per gallon
= 0.50 maximum pounds per hour of VOC without controlsx 1 number of current misting spray applicators
= 0.50 maximum pounds of VOC per hour from mister spray
Calculating maximum gallons of mister spray used per applicator per year
8,760.00 maximum hours of operation per applicatorx 100% anticipated operating efficiency
= 8,760.00 anticipated operating hour per applicatorx 0.08 maximum gallons of mister spray used per applicator per hour
= 695.24 maximum gallons of mister spray per applicator per yearx 1 number of current misting spray applicators
= 695.24 total gallons of misting spray per year
Calculating annual mister spray usage in tons
695.24 maximum gallons of mister spray per applicator per yearx 6.30 density pounds per gallon
= 4,380.00 maximum annual mister spray usage in pounds/ 2,000.00 pounds per ton
= 2.19 maximum annual mister spray usage in tonsx 1 number of current misting spray applicators
= 2.19 total tons of misting spray per year
Calculating maximum tons per year of VOC without controls
695.24 maximum gallons of mister spray per applicator per yearx 6.30 VOCWX pounds per gallon
= 4,380.00 maximum pounds per year of VOC/ 2,000 pounds per ton
= 2.19 maximum tons per applicator per year of VOC without controls
Calculating total VOC emissions from misting spray
2.19 maximum tons per applicator per year of VOC without controlsx 1 number of current misting spray applicators
= 2.19 total tons of VOC emissions from misting spray
Liner Film Weights
Film weights given by Dave BaldwinPress Type weight +/-DRT 3 pc 64 6211a 3 pc 67 7211b 3 pc 67 7211c 3 pc 67 7300a 3 pc 71 7300b 3 pc 71 7303 3 pc 74 7211a 2 pc 59 6211b 2 pc 59 6211c all 211c are 3 piece300a 2 pc 64 6300b 2 pc 64 6303 2 pc 64 6
ATTACHMENT 2:
Subject Item Inventory and Facility Requirements
List of SIs
Agency Interest Name Subject Item ID Subject Item Designation Subject Item Description Activity Type Label
Silgan Containers Mfg Corp ‐ Savage ACTV3 Air Insignificant Activities Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage AISI282 Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI1 EU023 Clean‐up Solvents Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI8 EU020 Make‐up Air Heater Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI9 EU021 Make‐up Air Heater Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI12 EU008 Washer ‐ Gang Press ‐ 211D Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI13 EU009 Washer ‐Gang Press ‐ 300D Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI14 EU010 Washer ‐Gang Press ‐ 300D Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI15 EU011 Washer ‐Gang Press ‐ 303D Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI16 EU012 Washer ‐Gang Press ‐ 211D Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI17 EU013 Washer ‐Gang Press ‐ 211D Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI18 EU014 Washer ‐Shell Press LIne (DRT) Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI38 EU026 Make‐up Air Heater Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI39 EU027 Make‐up Air Heater Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI41 EU004 Coating Line 3 (with oven) Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI42 EU025 Coating Line #2 (with oven) Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI43 EU006 Coating Line 3 oven ‐ combustion Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage EQUI44 EU003 Coating Line 2 oven ‐ combustion Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage STRU6 SV004 Gang Press 1 ‐ 4 Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage STRU7 SV010 Oxy‐Dry Waxer Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage STRU10 SV015 Catalytic Oxidizer Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage STRU12 SV005 Gang Press 5 Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage STRU14 SV007 Shell Press (DRT) Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage STRU21 Manufacturing Area Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage STRU22 Office Area Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage TFAC1 13900001 Silgan Containers Mfg Corp ‐ Savage Part 70 ReissuanceSilgan Containers Mfg Corp ‐ Savage TREA1 CE003 Catalytic Afterburner w/Heat Exchanger Part 70 Reissuance
Emission Units 1
Subject Item Type
DescriptionSubject Item ID
Subject Item
DesignationManufacturer Model
Max Design
Capacity
Max Design
Capacity Units
(numerator)
Max Design Capacity
Units (denominator)Material
Construction
Start Date
Operation
Start Date
Cleaning Equipment EQUI1 EU023 Brenntag Various 35 gallons hours Solvents 1/1/1957 1/1/1957
Pressing Equipment EQUI12 EU008 D&A 800 84000 each hours Product 1/1/1957 1/1/1957
Pressing Equipment EQUI13 EU009 D&A 800 84000 each hours Product 1/1/1957 1/1/1957
Pressing Equipment EQUI14 EU010 D&A 800 84000 each hours Product 1/1/1957 1/1/1957
Pressing Equipment EQUI15 EU011 D&A 800 84000 each hours Product 1/1/1957 1/1/1957
Pressing Equipment EQUI16 EU012 D&A 800 84000 each hours Product 12/15/1996 1/2/1997
Pressing Equipment EQUI17 EU013 D&A 800 84000 each hours Product 11/1/1997 12/1/1997
Pressing Equipment EQUI18 EU014 Preferred 100 162000 each hours Product 1/1/1991 1/1/1991
Spray Booth/Coating Line EQUI41 EU004 Wagner SG 4/4 DEF 100 each minutes Product 1/1/1990 1/1/1990
Spray Booth/Coating Line EQUI42 EU025 Wagner 15 X 44 Straight Coater 100 each minutes Product 12/12/2004 1/13/2005
Emission Units 2
Subject Item Type Description Subject Item IDSubject Item
DesignationManufacturer Model
Max Design
Capacity
Max Design Capacity Units
(numerator)
Max Design Capacity Units
(denominator)Material
Construction
Start Date
Operation
Start DateFiring Method
Dryer/Oven, direct fired EQUI43 EU006 Wagner SG 4/4 DEF 6 million British thermal units hours Heat 1/1/1990 1/1/1990 Not coal burningDryer/Oven, direct fired EQUI44 EU003 Wagner SG 4/4 DEF 4 million British thermal units hours Heat 1/1/1962 1/1/1962 Not coal burning
Other Combustion EQUI8 EU020 Rapid Mrg. 3100 10.73 million British thermal units hours Heat 1/1/1990 1/1/1990 Not coal burningOther Combustion EQUI9 EU021 Rapid Mfg. 3100 6.4 million British thermal units hours Heat 1/1/1990 1/1/1990 Not coal burningOther Combustion EQUI38 EU026 Applied Air DFC‐222‐HBR 2.8 million British thermal units hours Heat 1/1/1990 1/1/1990 Not coal burningOther Combustion EQUI39 EU027 ICE IMA‐130VTR 2.75 million British thermal units hours Heat 4/1/2011 4/1/2011 Not coal burning
Buildings
Subject Item Type Description Subject Item ID Subject Item Designation Height Units (height) Length Units (length) Width Units (width)
Building STRU21 28 feet 238 feet 160 feet
Building STRU22 19 feet 46 feet 30 feet
Component Group
Agency Interest Name Subject Item ID Subject Item Designation Subject Item Description Group Member ID
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI1
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI12
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI13
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI14
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI15
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI16
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI17
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI18
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI41
Silgan Containers Mfg Corp ‐ Savage COMG1 GP001 VOC sources in Group Limit EQUI42
StackVents
Subject Item Type
DescriptionSubject Item ID
Subject Item
Designation
Stack Height
(feet)
Stack Diameter
(feet)
Stack Length
(feet)
Stack Width
(feet)
Stack Flow Rate
(cubic ft/min)Discharge Temp (°F)
Info Source
DescriptionDischarge Direction
Stack/Vent STRU6 SV004 33 2 16000 70 Estimate Upwards with a cap on stack/ventStack/Vent STRU7 SV010 30 2 2.5 1000 100 Estimate Upwards with a cap on stack/ventStack/Vent STRU10 SV015 40 2.67 23000 350 Manufacturer Upwards with no cap on stack/ventStack/Vent STRU12 SV005 33 1.5 4000 70 Manufacturer Upwards with a cap on stack/ventStack/Vent STRU14 SV007 40 1 4000 70 Manufacturer Upwards with a cap on stack/vent
Catalytic Oxidizers
Subject Item Type
Description
Subject
Item ID
Subject Item
DesignationManufacturer Model
Install
Start Date
Pollutant
Controlled
(treatment)
Capture
Efficiency (%)
Destruction/Collection
Efficiency (%)
Subject
to CAM?Large PSEU? Efficiency Basis
Catalyst Bed
Reactivity (kat)
Burner Capacity
(MMBTU/hr)
Catatlytic Oxidizer
Inlet Temperature
(°F)
Outlet
Temperature
(°F)
020‐Catalytic Afterburner with Heat Exchanger
TREA1 CE003 TECMagnum 24000
10/1/2004 HAPs ‐ Single 100 95 Y N Test data 11 674 900
020‐Catalytic Afterburner with Heat Exchanger
TREA1 CE003 TECMagnum 24000
10/1/2004Volatile Organic Compounds
100 95 Y N Test data 11 674 900
Subject Item Category
DescriptionSubject Item Type Description Subject Item ID
Subject Item
DesignationSubject Item Description
Related
Subject
Item ID
Related Subject Item Type
Description
Start Date
(Subject Item
Related)
End Date
(Subject Item
Related)
Activity Insignificant Air Emissions Activity ACTV3 Air Insignificant ActivitiesAgency Interest Conventional Site AISI282
Component Group Air Component Group COMG1 GP001 VOC sources in Group Limit
Equipment Cleaning Equipment EQUI1 EU023 Clean‐up SolventsEquipment Dryer/Oven, direct fired EQUI43 EU006 Coating Line 3 oven ‐ combustion
Equipment Dryer/Oven, direct fired EQUI44 EU003 Coating Line 2 oven ‐ combustion
Equipment Other Combustion EQUI8 EU020 Make‐up Air HeaterEquipment Other Combustion EQUI9 EU021 Make‐up Air HeaterEquipment Other Combustion EQUI38 EU026 Make‐up Air HeaterEquipment Other Combustion EQUI39 EU027 Make‐up Air HeaterEquipment Other Combustion EQUI40 EU030 Make‐up Air HeaterEquipment Pressing Equipment EQUI12 EU008 Washer ‐ Gang Press ‐ 211DEquipment Pressing Equipment EQUI13 EU009 Washer ‐Gang Press ‐ 300DEquipment Pressing Equipment EQUI14 EU010 Washer ‐Gang Press ‐ 300DEquipment Pressing Equipment EQUI15 EU011 Washer ‐Gang Press ‐ 303DEquipment Pressing Equipment EQUI16 EU012 Washer ‐Gang Press ‐ 211DEquipment Pressing Equipment EQUI17 EU013 Washer ‐Gang Press ‐ 211DEquipment Pressing Equipment EQUI18 EU014 Washer ‐Shell Press LIne (DRT)Equipment Spray Booth/Coating Line EQUI41 EU004 Coating Line 3 (with oven)Equipment Spray Booth/Coating Line EQUI42 EU025 Coating Line #2 (with oven)Structure Building STRU21 Manufacturing AreaStructure Building STRU22 Office AreaStructure Stack/Vent STRU6 SV004 Gang Press 1 ‐ 4 EQUI12 Pressing Equipment 5/18/2016
Structure Stack/Vent STRU6 SV004 Gang Press 1 ‐ 4 EQUI13 Pressing Equipment 11/8/2002
Structure Stack/Vent STRU6 SV004 Gang Press 1 ‐ 4 EQUI14 Pressing Equipment 11/8/2002
Structure Stack/Vent STRU6 SV004 Gang Press 1 ‐ 4 EQUI15 Pressing Equipment 11/8/2002
Structure Stack/Vent STRU7 SV010 Oxy‐Dry Waxer
Structure Stack/Vent STRU10 SV015 Catalytic Oxidizer EQUI41 Spray Booth/Coating Line 10/6/2015
Structure Stack/Vent STRU10 SV015 Catalytic Oxidizer EQUI42 Spray Booth/Coating Line 10/6/2015
Structure Stack/Vent STRU10 SV015 Catalytic Oxidizer EQUI43 Dryer/Oven, direct fired 10/6/2015
Structure Stack/Vent STRU10 SV015 Catalytic Oxidizer EQUI44 Dryer/Oven, direct fired 10/6/2015
Structure Stack/Vent STRU12 SV005 Gang Press 5 EQUI16 Pressing Equipment 11/8/2002
Structure Stack/Vent STRU12 SV005 Gang Press 5 EQUI17 Pressing Equipment 5/18/2016
Structure Stack/Vent STRU14 SV007 Shell Press (DRT) EQUI18 Pressing Equipment 11/8/2002
Treatment020‐Catalytic Afterburner with Heat
ExchangerTREA1 CE003 Catalytic Afterburner w/Heat Exchanger EQUI41 Spray Booth/Coating Line 5/31/2006
Treatment020‐Catalytic Afterburner with Heat
ExchangerTREA1 CE003 Catalytic Afterburner w/Heat Exchanger EQUI42 Spray Booth/Coating Line 5/31/2006
Treatment020‐Catalytic Afterburner with Heat
ExchangerTREA1 CE003 Catalytic Afterburner w/Heat Exchanger EQUI43 Dryer/Oven, direct fired 5/31/2006
Treatment020‐Catalytic Afterburner with Heat
ExchangerTREA1 CE003 Catalytic Afterburner w/Heat Exchanger EQUI44 Dryer/Oven, direct fired 5/31/2006
Subject Item ID Requirement Citation
TFAC 1(13900001)
Permit Appendices: This permit contains appendices as listed in the permit Table of Contents. The Permittee shall comply with all requirements contained in Appendices A: Insignificant Activities and General Applicable Requirements and B: Maximum Contents of Materials. Minn. R. 7007.0800, subp. 2
TFAC 1(13900001)
PERMIT SHIELD: Subject to the limitations in Minn. R. 7007.1800, compliance with the conditions of this permit shall be deemed compliance with the specific provision of the applicable requirement identified in the permit as the basis of each condition. Subject to the limitations of Minn. R. 7007.1800 and 7017.0100, subp. 2, notwithstanding the conditions of this permit specifying compliance practices for applicable requirements, any person (including the Permittee) may also use other credible evidence to establish compliance or noncompliance with applicable requirements.
This permit shall not alter or affect the liability of the Permittee for any violation of applicable requirements prior to or at the time of permit issuance. Minn. R. 7007.1800, (A)(2)
TFAC 1(13900001)
The Permittee shall comply with National Primary and Secondary Ambient Air Quality Standards, 40 CFR pt. 50, and the Minnesota Ambient Air Quality Standards, Minn. R. 7009.0010 to 7009.0080. Compliance shall be demonstrated upon written request by the MPCA.
Minn. R. 7007.0100, subp. 7(A), 7(L), & 7(M), Minn. R. 7007.0800, subp. 4, Minn. R. 7007.0800, subps. 1‐2, Minn. Stat. 116.07, subd. 4a, Minn. Stat. 116.07, subd. 9
TFAC 1(13900001)
Circumvention: Do not install or use a device or means that conceals or dilutes emissions, which would otherwise violate a federal or state air pollution control rule, without reducing the total amount of pollutant emitted. Minn. R. 7011.0020
TFAC 1(13900001)
Air Pollution Control Equipment: Operate all pollution control equipment whenever the corresponding process equipment and emission units are operated.
Minn. R. 7007.0800, subp. 16(J), Minn. R. 7007.0800, subp. 2
TFAC 1(13900001)
Operation and Maintenance Plan: Retain at the stationary source an operation and maintenance plan for all air pollution control equipment. At a minimum, the O & M plan shall identify all air pollution control equipment and control practices and shall include a preventative maintenance program for the equipment and practices, a description of (the minimum but not necessarily the only) corrective actions to be taken to restore the equipment and practices to proper operation to meet applicable permit conditions, a description of the employee training program for proper operation and maintenance of the control equipment and practices, and the records kept to demonstrate plan implementation.
Minn. R. 7007.0800, subp. 14, Minn. R. 7007.0800, subp. 16(J)
TFAC 1(13900001)
Operation Changes: In any shutdown, breakdown, or deviation the Permittee shall immediately take all practical steps to modify operations to reduce the emission of any regulated air pollutant. The Commissioner may require feasible and practical modifications in the operation to reduce emissions of air pollutants. No emissions units that have an unreasonable shutdown or breakdown frequency of process or control equipment shall be permitted to operate. Minn. R. 7019.1000, subp. 4
TFAC 1(13900001)
Fugitive Emissions: Do not cause or permit the handling, use, transporting, or storage of any material in a manner which may allow avoidable amounts of particulate matter to become airborne. Comply with all other requirements listed in Minn. R. 7011.0150. Minn. R. 7011.0150
TFAC 1(13900001)
Noise: The Permittee shall comply with the noise standards set forth in Minn. R. 7030.0010 to 7030.0080 at all times during the operation of any emission units. This is a state only requirement and is not enforceable by the EPA Administrator or citizens under the Clean Air Act. Minn. R. 7030.0010‐7030.0080
TFAC 1(13900001)
Inspections: The Permittee shall comply with the inspection procedures and requirements as found in Minn. R. 7007.0800, subp. 9(A). Minn. R. 7007.0800, subp. 9(A)
TFAC 1(13900001) The Permittee shall comply with the General Conditions listed in Minn. R. 7007.0800, subp. 16. Minn. R. 7007.0800, subp. 16
TFAC 1(13900001)
Performance Testing: Conduct all performance tests in accordance with Minn. R. ch. 7017 unless otherwise noted in in this permit. Minn. R. ch. 7017
Subject Item ID Requirement Citation
TFAC 1(13900001)
Performance Test No fica ons and Submi als:
Performance Tests are due as outlined in this permit. Performance Test No fica on (wri en): due 30 days before each Performance TestPerformance Test Plan: due 30 days before each Performance TestPerformance Test Pre‐test Mee ng: due 7 days before each Performance TestPerformance Test Report: due 45 days a er each Performance TestPerformance Test Report ‐ Microfiche Copy: due 105 days a er each Performance Test
The Notification, Test Plan, and Test Report may be submitted in an alternative format as allowed by Minn. R. 7017.2018.
Minn. R. 7017.2018, Minn. R. 7017.2030, subps. 1‐4, Minn. R. 7017.2035, subps. 1‐2
TFAC 1(13900001)
Limits set as a result of a performance test (conducted before or after permit issuance) apply until superseded as stated in the MPCA's Notice of Compliance letter granting preliminary approval. Preliminary approval is based on formal review of a subsequent performance test on the same unit as specified by Minn. R. 7017.2025, subp. 3. The limit is final upon issuance of a permit amendment incorporating the change. Minn. R. 7017.2025, subp. 3
TFAC 1(13900001)
Monitoring Equipment Calibra on ‐ The Permi ee shall either:
1. Calibrate or replace required monitoring equipment every 12 months; or2. Calibrate at the frequency stated in the manufacturer's specifica ons.
For each monitor, the Permittee shall maintain a record of all calibrations, including the date conducted, and any corrective action that resulted. The Permittee shall include the calibration frequencies, procedures, and manufacturer's specifications (if applicable) in the Operations and Maintenance Plan. Any requirements applying to continuous emission monitors are listed separately in this permit. Minn. R. 7007.0800, subp. 4(D)
TFAC 1(13900001)
Operation of Monitoring Equipment: Unless noted elsewhere in this permit, monitoring a process or control equipment connected to that process is not necessary during periods when the process is shutdown, or during checks of the monitoring systems, such as calibration checks and zero and span adjustments. If monitoring records are required, they should reflect any such periods of process shutdown or checks of the monitoring system. Minn. R. 7007.0800, subp. 4(D)
TFAC 1(13900001)
The Permittee shall submit an application for permit reissuance : Due 180 calendar days before Permit Expiration Date. Minn. R. 7007.0400, subp. 2
TFAC 1(13900001)
Recordkeeping: Retain all records at the stationary source, unless otherwise specified within this permit, for a period of five (5) years from the date of monitoring, sample, measurement, or report. Records which must be retained at this location include all calibration and maintenance records, all original recordings for continuous monitoring instrumentation, and copies of all reports required by the permit. Records must conform to the requirements listed in Minn. R. 7007.0800, subp. 5(A). Minn. R. 7007.0800, subp. 5(C)
TFAC 1(13900001)
Recordkeeping: Maintain records describing any insignificant modifications (as required by Minn. R. 7007.1250, subp. 3) or changes contravening permit terms (as required by Minn. R. 7007.1350, subp. 2), including records of the emissions resulting from those changes. Minn. R. 7007.0800, subp. 5(B)
TFAC 1(13900001)
If the Permittee determines that no permit amendment or notification is required prior to making a change, the Permittee must retain records of all calculations required under Minn. R. 7007.1200. For expiring permits, these records shall be kept for a period of five years from the date the change was made or until permit reissuance, whichever is longer. The records shall be kept at the stationary source for the current calendar year of operation and may be kept at the stationary source or office of the stationary source for all other years. The records may be maintained in either electronic or paper format. Minn. R. 7007.1200, subp. 4
Subject Item ID Requirement Citation
TFAC 1(13900001)
Shutdown Notifications: Notify the Commissioner at least 24 hours in advance of a planned shutdown of any control equipment or process equipment if the shutdown would cause any increase in the emissions of any regulated air pollutant. If the owner or operator does not have advance knowledge of the shutdown, notification shall be made to the Commissioner as soon as possible after the shutdown. However, notification is not required in the circumstances outlined in Items A, B and C of Minn. R. 7019.1000, subp. 3.
At the time of notification, the owner or operator shall inform the Commissioner of the cause of the shutdown and the estimated duration. The owner or operator shall notify the Commissioner when the shutdown is over. Minn. R. 7019.1000, subp. 3
TFAC 1(13900001)
Breakdown Notifications: Notify the Commissioner within 24 hours of a breakdown of more than one hour duration of any control equipment or process equipment if the breakdown causes any increase in the emissions of any regulated air pollutant. The 24‐hour time period starts when the breakdown was discovered or reasonably should have been discovered by the owner or operator. However, notification is not required in the circumstances outlined in Items A, B and C of Minn. R. 7019.1000, subp. 2.
At the time of notification or as soon as possible thereafter, the owner or operator shall inform the Commissioner of the cause of the breakdown and the estimated duration. The owner or operator shall notify the Commissioner when the breakdown is over. Minn. R. 7019.1000, subp. 2
TFAC 1(13900001)
Notification of Deviations Endangering Human Health or the Environment: As soon as possible after discovery, notify the Commissioner or the state duty officer, either orally or by facsimile, of any deviation from permit conditions which could endanger human health or the environment. Minn. R. 7019.1000, subp. 1
TFAC 1(13900001)
Notification of Deviations Endangering Human Health or the Environment Report: Within 2 working days of discovery, notify the Commissioner in writing of any deviation from permit conditions which could endanger human health or the environment. Include the following informa on in this wri en descrip on: 1. the cause of the devia on; 2. the exact dates of the period of the devia on, if the devia on has been corrected;3. whether or not the devia on has been corrected; 4. the anticipated time by which the deviation is expected to be corrected, if not yet corrected; and
5. steps taken or planned to reduce, eliminate, and prevent reoccurrence of the deviation. Minn. R. 7019.1000, subp. 1
TFAC 1(13900001)
The Permittee shall submit a semiannual deviations report : Due semiannually, by the 30th of January and July The first semiannual report submitted by the Permittee shall cover the calendar half‐year in which the permit is issued. The first report of each calendar year covers January 1 ‐ June 30. The second report of each calendar year covers July 1 ‐ December 31. If no deviations have occurred, the Permittee shall submit the report stating no deviations.
Minn. R. 7007.0800, subp. 6(A)(2)
TFAC 1(13900001)
Application for Permit Amendment: If a permit amendment is needed, submit an application in accordance with the requirements of Minn. R. 7007.1150 through Minn. R. 7007.1500. Submittal dates vary, depending on the type of amendment needed.
Upon adoption of a new or amended federal applicable requirement, and if there are more than 3 years remaining in the permit term, the Permittee shall file an application for an amendment within nine months of promulgation of the applicable requirement, pursuant to Minn. R. 7007.0400, subp. 3.
Minn. R. 7007.0400, subp. 3, Minn. R. 7007.1150 ‐ 7007.1500
TFAC 1(13900001)
Extension Requests: The Permittee may apply for an Administrative Amendment to extend a deadline in a permit by no more than 120 days, provided the proposed deadline extension meets the requirements of Minn. R. 7007.1400, subp. 1(H). Performance testing deadlines from the General Provisions of 40 CFR pt. 60 and pt. 63 are examples of deadlines for which the MPCA does not have authority to grant extensions and therefore do not meet the requirements of Minn. R. 7007.1400, subp. 1(H). Minn. R. 7007.1400, subp. 1(H)
TFAC 1(13900001)
The Permittee shall submit a compliance certification : Due annually, by the 31st of January (for the previous calendar year). The Permittee shall submit this to the Commissioner on a form approved by the Commissioner. This report covers all deviations experienced during the calendar year. Minn. R. 7007.0800, subp. 6(C)
Subject Item ID Requirement Citation
TFAC 1(13900001)
Emission Inventory Report: due on or before April 1 of each calendar year following permit issuance, to be submitted on a form approved by the Commissioner. Minn. R. 7019.3000‐7019.3100
TFAC 1(13900001) Emission Fees: due 30 days after receipt of an MPCA bill. Minn. R. 7002.0005‐7002.0095
TFAC 1(13900001)
This permit establishes limits on the facility to keep it a minor source under New Source Review and NESHAPS. The Permittee cannot make any change at the source that would make the source a major source under New Source Review and NESHAPS until a permit amendment has been issued. This includes changes that might otherwise qualify as insignificant modifications and minor or moderate amendments.
Title I Condition: Avoid major modification under 40 CFR 52.21(b)(2) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 63.2
TFAC 1(13900001)
The Permittee shall submit an annual report : Due annually, by the 31st of January The report shall describe the changes made at the Facility during the previous calendar year using the latest MPCA application forms. The report shall include information for any new or replaced Subject Items. The report shall document the VOC, Single HAP, and Total HAP 12‐month rolling sum calculations for the previous calendar year. The report shall be submitted with the annual Compliance Certification required by this permit. As part of the Annual Report, the Permittee shall verify and certify that the Facility has maintained minor source status for New Source Review. Minn. R. 7007.0800, subp. 2
TFAC 1(13900001)
Equipment Labeling: The Permittee shall permanently affix a unique number to each emissions unit for tracking purposes. The numbers shall correlate the unit to the appropriate Subject Item numbers used in this permit. The number can be affixed by placard, stencil, or other means. The number shall be maintained so that it is readable and visible at all times from a safe distance. If equipment is added, it shall be given a new unique number; numbers from replaced or removed equipment shall not be reused. Minn. R. 7007.0800, subp. 2
TFAC 1(13900001)
Equipment Inventory: The Permittee shall maintain a written list of all emissions units and control equipment on site. The Permittee shall update the list to include any replaced, modified, or new equipment prior to making the change.
The list shall correlate the units to the Subject Item numbers used in this permit and shall include the data on GI‐04, GI‐05B, and GI‐05C. The date of construction shall be the date the change was made for replaced, modified, or new equipment. Minn. R. 7007.0800, subp. 2
COMG 1(GP001)
The Permittee shall limit emissions of Volatile Organic Compounds <= 240 tons per year 12‐month rolling sum to be calculated by the 15th day of each month for the previous 12‐month period as described later in this permit. All VOC‐emitting equipment at the Facility is subject to this limit except for the following: natural gas combustion equipment and insignificant activities. If the Permittee replaces any existing VOC‐emitting equipment, adds new VOC‐emitting equipment, or modifies the existing equipment, such equipment is subject to this permit limit as well as all of the requirements COMG 1. Prior to making such a change, the Permittee shall apply for and obtain the appropriate permit amendment, as applicable. The Permittee is not required to complete VOC calculations described in Minn. R. 7007.1200, subp. 2. A permit amendment will still be needed regardless of the emissions increase if the change will be subject to a new applicable requirement or requires revisions to the limits or monitoring and recordkeeping in this permit.
VOC contents for each VOC‐containing material shall be determined as described under the Material Content requirement in COMG 1. The calculation of VOCs used may take into account recovered/recycled VOCs as described under the Waste Credit requirement in COMG 1.
Title I Condition: Avoid major modification under 40 CFR 52.21(b)(2) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
Subject Item ID Requirement Citation
COMG 1(GP001)
The Permittee shall limit emissions of HAPs ‐ Single <= 9 tons per year 12‐month rolling sum to be calculated by the 15th day of each month for the previous 12‐month period. All HAP‐emitting equipment at the Facility is covered by this limit except for the following: natural gas combustion equipment and insignificant activities. If the Permittee replaces any existing HAP‐emitting equipment or adds new HAP‐emitting equipment, such equipment is subject to this permit limit as well as all of the requirements of COMG 1. Prior to making such a change, the Permittee shall apply for and obtain the appropriate permit amendment, as applicable. A permit amendment may be needed if the change will be subject to a new applicable requirement or requires revisions to limits or the monitoring and recordkeeping in this permit.
HAP contents for each HAP‐containing material shall be determined as described under the Material Content requirement in COMG 1. The calculation of HAPs used may take into account recovered/recycled HAPs as described under the Waste Credit requirement in COMG 1.
Title I Condition: Avoid major source under 40 CFR 63.2
COMG 1(GP001)
The Permittee shall limit emissions of HAPs ‐ Total <= 23 tons per year 12‐month rolling sum to be calculated by the 15th day of each month for the previous 12‐month period. All HAP‐emitting equipment at the Facility is covered by this limit except for the following: natural gas combustion equipment and insignificant activities. If the Permittee replaces any existing HAP‐emitting equipment or adds new HAP‐emitting equipment, such equipment is subject to this permit limit as well as all of the requirements of COMG 1. Prior to making such a change, the Permittee shall apply for and obtain the appropriate permit amendment, as applicable. A permit amendment may be needed if the change will be subject to a new applicable requirement or requires revisions to limits or the monitoring and recordkeeping in this permit.
HAP contents for each HAP‐containing material shall be determined as described under the Material Content requirement in COMG 1. The calculation of HAPs used may take into account recovered/recycled HAPs as described under the Waste Credit requirement in COMG 1.
Title I Condition: Avoid major source under 40 CFR 63.2
COMG 1(GP001)
Daily Recordkeeping. On each day of operation, the Permittee shall calculate, record, and maintain the total quantity of all coatings and other VOC and HAP‐containing materials used at the facility. This shall be based on written usage logs.
Title I Condition: Avoid major modification under 40 CFR 52.21(b)(2) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 63.2
COMG 1(GP001)
Vola le Organic Compounds: Monthly Recordkeeping ‐‐ VOC Emissions.
By the 15th of the month, the Permi ee shall calculate and record the following:1) The total usage of VOC‐containing materials for the previous calendar month using the daily usage records. This record shall also include the VOC and solids contents of each material as determined by the Material Content requirement of this permit;
2) The VOC emissions for the previous month using the formulas specified in this permit; and3) The 12‐month rolling sum VOC emissions for the previous 12‐month period by summing the monthly VOC emissions data for the previous 12 months. Minn. R. 7007.0800, subps. 4‐5
Subject Item ID Requirement Citation
COMG 1(GP001)
Volatile Organic Compounds: Monthly Calculation ‐‐ VOC Emissions.
The Permittee shall calculate VOC emissions using the following equations: VOC (tons/month) = (V1 ‐ W1) x (1‐Ce) + (V2‐W2)
V# = (A1 x B1) + (A2 x B2) + (A3 x B3) + ..... W #= (C1 x D1) + (C2 x D2) + (C3 x D3) + ..... where: V1 = total VOC used in tons/month in emissions units that vent to the catalytic oxidizer; V2 = total VOC used in tons/month in emissions units that do not vent to the catalytic oxidizer; A# = amount of each VOC‐containing material used, in tons/month;
B# = weight percent VOC in A#, as a fraction; W1 = the amount of VOC collected from equipment that vents to the oxidizer that is shipped in waste, in tons/month; W2 = the amount of VOC collected from equipment that does not vent to the oxidizer that is shipped in waste, in tons/month;
C# = amount, in tons/month, of each VOC‐containing waste material shipped. If the Permittee chooses to not take credit for waste shipments, this parameter would be zero; D# = weight percent of VOC in C#, as a fraction; and Ce = Control efficiency of catalytic oxidizer, 95%. Minn. R. 7007.0800, subps. 4‐5
COMG 1(GP001)
HAPs: Monthly Recordkeeping. By the 15th of the month, the Permittee shall calculate and record the following using the formulas specified in this permit:
1) The total HAP‐containing materials used in the previous calendar month using the daily usage records. This record shall also include the individual and total HAP contents of each HAP‐containing material used in the previous month, as determined by the Material Content requirement of this permit;
2) The total and individual HAP emissions for the previous month using the formulas specified in this permit; and3) The 12‐month rolling sum total and individual HAP emissions for the previous 12‐month period by summing the monthly emissions data for the previous 12 months. Minn. R. 7007.0800, subps. 4‐5
COMG 1(GP001)
HAPs: Monthly Calculation ‐‐ HAP Emissions. The Permittee shall calculate each individual HAP and total HAP emissions using the following equations: HAP Emissions (tons/month) = (H1 ‐ W1) x (1‐Ce) + (H2‐W2)
H# = (A1 x B1) + (A2 x B2) + (A3 x B3) + .... W# = (C1 x D1) + (C2 x D2) + (C3 x D3) + .... Where:
H1 = the amount of each pollutant (either total HAP or each individual HAP), used, in tons/month in emissions units that vent to the catalytic oxidizer; H2 = the amount of each pollutant (either total HAP or each individual HAP), used, in tons/month in emissions units that do not vent to the catalytic oxidizer; A# = Amount of each HAP‐containing material used in the previous month, in tons/month;
B# = weight percent of each individual or total HAP in A#, as a fraction (e.g., 50% is 0.50); W1 = the amount of each pollutant (either total HAP or each individual HAP) collected from equipment that vents to the oxidizer that is shipped in waste, in tons/month; W2 = the amount of each pollutant (either total HAP or each individual HAP) collected from equipment that does not vent to the oxidizer that is shipped in waste, in tons/month;
C# = amount, in tons/month, of each HAP‐containing waste material shipped. If the Permittee chooses to not take credit for waste shipments, this parameter would be zero; D# = weight percent of each individual or total HAP in C#, as a fraction; and Ce = Control efficiency of catalytic oxidizer, 95%. Minn. R. 7007.0800, subps. 4‐5
Subject Item ID Requirement Citation
COMG 1(GP001)
Maximum Contents of Materials: The Permittee assumed certain worst‐case contents of materials when determining the short term potential to emit of units in COMG 1. These assumptions are listed in Appendix B of this permit. Changing to a material that has a higher content of any of the given pollutants is considered a change in method of operation that must be evaluated under Minn. R. 7007.1200, subp. 3 to determine if a permit amendment or notification is required under Minn. R. 7007.1150. Minn. R. 7005.0100, subp. 35a
COMG 1(GP001)
Waste Credit: If the Permittee elects to obtain credit for HAPs and/or VOC shipped in waste materials, the Permittee shall either use item 1 or 2 to determine the VOC and/or total and individual HAP content for each credited shipment.
1) The Permittee shall analyze a composite sample of each waste shipment to determine the weight content of VOC, total HAP, and each individual HAP, excluding water.
2) The Permittee may use supplier data for raw materials to determine the VOC and total and individual HAP contents of each waste shipment, using the same content data used to determine the content of raw materials. If the waste contains several materials, the content of mixed waste shall be assumed to be the lowest VOC and total and individual HAP content of any of the materials. Minn. R. 7007.0800, subps. 4‐5
COMG 1(GP001)
Material Content. VOC and HAPs contents in coating materials shall be determined by the Safety Data Sheet (SDS) or the Material Safety Data Sheet (MSDS) provided by the supplier for each material used. If a material content range is given on the SDS or the MSDS, the highest number in the range shall be used in all compliance calculations. If there is information provided in the Regulatory Section of the SDS, the highest number in the range of that section may be used. Other alternative methods approved by the MPCA may be used to determine the VOC and HAP contents. The Commissioner reserves the right to require the Permittee to determine the VOC and HAP contents of any material, according to EPA or ASTM reference methods. If an EPA or ASTM reference method is used for material content determination, the data obtained shall supersede the SDS or the MSDS. Minn. R. 7007.0800, subps. 4‐5
EQUI 8(EU020)
Total Particulate Matter <= 0.40 pounds per million Btu heat input The potential to emit from the unit is 0.01 lb/MMBtu due to equipment design and allowable fuels. Minn. R. 7011.0515, subp. 1
EQUI 8(EU020)
Opacity <= 20 percent opacity except for one six‐minute period per hour of not more than 60 percent opacity. Minn. R. 7011.0515, subp. 2
EQUI 8(EU020) Fuel Type: Natural gas only. Minn. R. 7005.0100, subp. 35aEQUI 8(EU020) The Permittee shall keep records of fuel type on a monthly basis.
Minn. R. 7007.0800, subps. 4&5
EQUI 9(EU021)
Total Particulate Matter <= 0.40 pounds per million Btu heat input The potential to emit from the unit is 0.01 lb/MMBtu due to equipment design and allowable fuels. Minn. R. 7011.0515, subp. 1
EQUI 9(EU021)
Opacity <= 20 percent opacity except for one six‐minute period per hour of not more than 60 percent opacity. Minn. R. 7011.0515, subp. 2
EQUI 9(EU021) Fuel Type: Natural gas only. Minn. R. 7005.0100, subp. 35aEQUI 9(EU021) The Permittee shall keep records of fuel type on a monthly basis.
Minn. R. 7007.0800, subps. 4&5
EQUI 38(EU026)
Total Particulate Matter <= 0.40 pounds per million Btu heat input The potential to emit from the unit is 0.008 lb/MMBtu due to equipment design and allowable fuels. Minn. R. 7011.0515, subp. 1
EQUI 38(EU026)
Opacity <= 20 percent opacity except for one six‐minute period per hour of not more than 60 percent opacity. Minn. R. 7011.0515, subp. 2
EQUI 38(EU026) Fuel Type: Natural gas only. Minn. R. 7005.0100, subp. 35aEQUI 38(EU026) The Permittee shall keep records of fuel type on a monthly basis.
Minn. R. 7007.0800, subps. 4&5
EQUI 39(EU027)
Total Particulate Matter <= 0.40 pounds per million Btu heat input The potential to emit from the unit is 0.008 lb/MMBtu due to equipment design and allowable fuels. Minn. R. 7011.0515, subp. 1
EQUI 39(EU027)
Opacity <= 20 percent opacity except for one six‐minute period per hour of not more than 60 percent opacity. Minn. R. 7011.0515, subp. 2
EQUI 39(EU027) Fuel Type: Natural gas only. Minn. R. 7005.0100, subp. 35a
Subject Item ID Requirement Citation
EQUI 39(EU027) The Permittee shall keep records of fuel type on a monthly basis.
Minn. R. 7007.0800, subps. 4&5
EQUI 41(EU004)
The Permittee shall vent emissions from EQUI 41 to control equipment meeting the requirements of TREA 1 whenever EQUI 41 operates.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
EQUI 42(EU025)
The Permittee shall vent emissions from EQUI 42 to control equipment meeting the requirements of TREA 1 whenever EQUI 42 operates.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
EQUI 43(EU006)
Total Particulate Matter <= 0.30 grains per dry standard cubic foot of exhaust gas unless required to further reduce emissions to comply with the less stringent limit of either Minn. R. 7011.0730 or Minn. R. 7011.0735.
Minn. R. 7011.0610, subp. 1(A)(1)
EQUI 43(EU006)
Opacity <= 20 percent opacity except for one six‐minute period per hour of not more than 60 percent opacity.
Minn. R. 7011.0610, subp. 1(A)(2)
EQUI 43(EU006) Fuel Type: Natural gas with propane as a back‐up. Minn. R. 7005.0100, subp. 35aEQUI 43(EU006) The Permittee shall keep records of fuel type on a monthly basis.
Minn. R. 7007.0800, subps. 4&5
EQUI 43(EU006)
The Permittee shall vent emissions from EQUI 43 to control equipment meeting the requirements of TREA 1 whenever EQUI 43 operates.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
EQUI 44(EU003)
Total Particulate Matter <= 0.30 grains per dry standard cubic foot of exhaust gas unless required to further reduce emissions to comply with the less stringent limit of either Minn. R. 7011.0730 or Minn. R. 7011.0735.
Minn. R. 7011.0610, subp. 1(A)(1)
EQUI 44(EU003)
Opacity <= 20 percent opacity except for one six‐minute period per hour of not more than 60 percent opacity.
Minn. R. 7011.0610, subp. 1(A)(2)
EQUI 44(EU003) Fuel Type: Natural gas with propane as a back‐up. Minn. R. 7005.0100, subp. 35aEQUI 44(EU003) The Permittee shall keep records of fuel type on a monthly basis.
Minn. R. 7007.0800, subps. 4&5
EQUI 44(EU003)
The Permittee shall vent emissions from EQUI 44 to control equipment meeting the requirements of TREA 1 whenever EQUI 44 operates.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
TREA 1(CE003)
The Permittee shall operate and maintain control equipment such that it achieves an overall control efficiency for Volatile Organic Compounds >= 95 percent control efficiency.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
TREA 1(CE003)
Temperature >= 674 degrees Fahrenheit 3‐hour rolling average at the oxidizer inlet as determined during the December 8, 2015 performance test, unless a new limit is set pursuant to Minn. R. 7017.2025, subp. 3 based on the values recorded during the most recent MPCA‐approved performance test where compliance was demonstrated. The new limit shall be implemented upon receipt of the Notice of Compliance letter granting preliminary approval. The limit is final upon issuance of a permit amendment incorporating the change. If the 3‐hour rolling average temperature is below the minimum inlet temperature limit, the VOC used during that time shall be considered uncontrolled until the average inlet temperature is above the minimum temperature limit. This shall be reported as a deviation.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
TREA 1(CE003)
Total Particulate Matter <= 0.30 grains per dry standard cubic foot of exhaust gas unless required to further reduce emissions to comply with the less stringent limit of either Minn. R. 7011.0730 or Minn. R. 7011.0735.
Minn. R. 7011.0610, subp. 1(A)(1)
TREA 1(CE003)
Opacity <= 20 percent opacity except for one six‐minute period per hour of not more than 60 percent opacity.
Minn. R. 7011.0610, subp. 1(A)(2)
TREA 1(CE003)
The Permittee shall vent emissions from EQUI 41, EQUI 42, EUQI 43, and EQUI 44 to TREA 1 whenever EQUI 41, EQUI 42, EQUI 43, and EQUI 44 operate, and operate and maintain TREA 1 at all times that any emissions are vented to TREA 1. The Permittee shall document periods of non‐operation of the control equipment TREA 1 whenever EQUI 41, EQUI 42, EQUI 43, and EQUI 44 are operating.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
Subject Item ID Requirement Citation
TREA 1(CE003)
The Permittee shall operate and maintain the catalytic oxidizer in accordance with the Operation and Maintenance (O & M) Plan. The Permittee shall keep copies of the O & M Plan available onsite for use by staff and MPCA staff. Minn. R. 7007.0800, subp. 14
TREA 1(CE003)
Documentation of Need for Improved Monitoring: If the Permittee fails to achieve compliance with an emission limitation or standard for which the monitoring did not provide an indication of an excursion or exceedance while providing valid data, or the results of compliance or performance testing document a need to modify the existing pressure drop range, the Permittee shall promptly notify the MPCA and, if necessary, submit a permit amendment application to address the necessary monitoring change.
40 CFR 64.7(e), Minn. R. 7017.0200
TREA 1(CE003)
As required by 40 CFR Section 64.9(a)(2), for the Semi‐Annual Deviations Report required by this permit and/or the Notification of Deviations Endangering Human Health and the Environment required by this permit, as applicable, the Permittee shall include the following related to the monitoring identified as required by 40 CFR pt. 64: 1) Summary information on the number, duration, and cause of excursions or exceedances, as applicable, and the corrective action taken; and 2) Summary information on the number, duration, and cause for monitor downtime incidents.
40 CFR 64.9(a)(2), Minn. R. 7017.0200
TREA 1(CE003)
The Permittee shall maintain records of monitoring data, monitor performance data, corrective actions taken, and other supporting information required to be maintained. The Permittee may maintain records on alternative media, such as microfilm, computer files, magnetic tape disks, or microfiche, provided that the use of such alternative media allows for expeditious inspection and review, and does not conflict with other applicable recordkeeping requirements.
40 CFR 64.9(b), Minn. R. 7017.0200
TREA 1(CE003)
The Permittee shall maintain and operate a thermocouple monitoring device that continuously indicates and records both the inlet and outlet temperatures of the catalytic oxidizer. The monitoring device shall have a margin of error less than the greater of +/‐ 0.75 percent of the temperature being measured or +/‐ 2.5 degrees Celsius. The recording device shall also calculate the three‐hour rolling average inlet temperature.
40 CFR 64.7(b), Minn. R. 7017.0200, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
TREA 1(CE003)
Daily Monitoring: The Permittee shall physically verify the operation of the temperature recording device at least once every 24 hours to verify that it is working and recording properly. The Permittee shall maintain a written record of the daily verifications.
40 CFR 64.3, Minn. R. 7017.0200, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 63.2
TREA 1(CE003)
The Permittee shall submit sample analysis : Due every 24 months. The Permittee shall send a representative sample of the catalyst to a laboratory to test the catalyst's destruction efficiency. If test results show a destruction efficiency of less than 95%, the Permittee shall follow the corrective actions contained in the Operation and Maintenance Plan.
Minn. R. 7007.0800, subps. 4‐5, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
TREA 1(CE003)
Monitoring Equipment: The Permittee shall install and maintain thermocouples to conduct temperature monitoring required by this permit. The monitoring equipment must be installed, in use, and properly maintained whenever operation of the monitored control equipment is required.
40 CFR 64.7, Minn. R. 7007.0800, subps. 4‐5
TREA 1(CE003)
The Permittee shall maintain a continuous hard copy readout or computer disk file of the temperature readings and calculated three hour rolling average temperatures at the inlet to the combustion chamber.
40 CFR 64.3, Minn. R. 7017.0200, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
TREA 1(CE003)
Annual Calibration: The Permittee shall calibrate the temperature monitor at least once every 12 months and shall maintain a written record of the calibration and any action resulting from the calibration.
40 CFR 64.3, Minn. R. 7017.0200
Subject Item ID Requirement Citation
TREA 1(CE003)
Monthly Monitoring: At least once each month during normal operation, the Permittee shall record the temperature rise across the catalyst (outlet temp. ‐ inlet temp.) while the process is running. If it is determined that the catalyst reactivity has been impaired, by comparison of the observed temperature rise to the past temperature rise records, the Permittee shall follow the corrective actions in the Operation and Maintenance Plan. The Permittee shall maintain written records of the monitoring and any corrective actions taken.
40 CFR 64.3, Minn. R. 7007.0800, subp. 5
TREA 1(CE003)
Quarterly Inspections: At least once per calendar quarter, the Permittee shall inspect the control equipment internal and external system components, including but not limited to the refractory, heat exchanger, and electrical systems. The Permittee shall maintain a written record of the inspection and any corrective actions taken resulting from the inspection.
Minn. R. 7007.0800, subp.144, Minn. R. 7007.0800, subp. 4, Minn. R. 7007.0800, subp. 5
TREA 1(CE003)
Annual Inspection: At least once per calendar year, the Permittee shall conduct an internal inspection of the control device that includes all operating systems of the control device. The Permittee shall maintain a written record of the inspection and any action resulting from the inspection.
Minn. R. 7007.0800, subp. 14, Minn. R. 7007.0800, subp. 4, Minn. R. 7007.0800, subp. 5
TREA 1(CE003)
For periods when the catalytic oxidizer is operated above the minimum inlet temperature, the Permittee shall use either one of the following when completing calculations as required elsewhere in this permit:
a. The overall control efficiency limit specified in this permit for this equipment; orb. The overall control efficiency determined during the most recent MPCA approved performance test. If the tested efficiency is less than the efficiency limit in this permit, the Permittee must use the tested value in all calculations until the efficiency is demonstrated to be above the permit limit
through a new test.
Minn. R. 7007.0800, subps. 4‐5, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000, Title I Condition: Avoid major source under 40 CFR 63.2
TREA 1(CE003)
Corrective Actions: If the temperature is below the minimum specified by this permit or if the catalytic oxidizer or any of its components are found during the inspections to need repair, the Permittee shall take corrective action as soon as possible. Corrective actions shall return the temperature to at least the permitted minimum and/or include completion of necessary repairs identified during the inspection, as applicable. Corrective actions include, but are not limited to, those outlined in the O & M Plan for the catalytic oxidizer. The Permittee shall keep a record of the type and date of any corrective action taken.
40 CFR 64.7(d), Minn. R. 7017.0200
TREA 1(CE003)
Volatile Organic Compounds : The Permittee shall conduct a performance test : Due before 12/20/2020 every 60 months thereafter to verify VOC control efficiency. The first test is due by the date specified and all subsequent tests are due by the end of each 60‐month period following that date. The performance test shall be conducted at worst case conditions as defined at Minn. R. 7017.2025, subp. 2, using EPA Reference Method 25A, or other method approved by MPCA in the performance test plan approval.
Testing conducted during the 60 days prior to the performance test due date satisfies the performance test due date, and will not reset the test due date for future tes ng as required: 1) by this permit; 2) by the most recently approved Performance Test Frequency Plan; or 3) within a Notice of Compliance letter. Testing conducted more than two months prior to the performance test due date satisfies this test due date requirement and will reset the performance test due date.
Minn. R. 7017.2020, subp. 1, Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
TREA 1(CE003)
The Permittee shall operate and maintain control equipment such that it achieves an overall control efficiency for HAPs ‐ Total >= 95 percent control efficiency.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
TREA 1(CE003)
The Permittee shall operate and maintain control equipment such that it achieves an overall control efficiency for HAPs ‐ Single >= 95 percent control efficiency.
Title I Condition: Avoid major source under 40 CFR 52.21(b)(1)(i) and Minn. R. 7007.3000
ATTACHMENT 3:
CAM Plan
COMPLIANCE ASSURANCE MONITORING (CAM) PLAN
Silgan Containers Manufacturing Corporation Savage, MN AQ Facility ID No: 13900001-002
Emission Units: EQUI041, EQUI042, EQUI043, and EQUI04 2 Control: TREA001 Stack: STRU010
Plan Element Description 1. Indicator
A. Measurement Approach Catalytic oxidizer inlet temperature. 1. Indicator
A. Measurement Approach The inlet temperature will be measured using a thermocouple. II. Indicator Range For the inlet temperature, the excursion is defined as temperature readings
less than 674°F while one or both production lines are operating, unless a performance test has determined that a lower inlet temperature is acceptable. An excursion will trigger an investigation of the occurrence and corrective action.
III. Performance Criteria The inlet temperature is measured using a thermocouple located in the air stream before the catalyst beds.
A. Data Representativeness The minimum tolerance of a thermocouple is ±0.75% of the temperature being measured or ±2.5°C, whichever is greater. The thermocouple will be calibrated or replaced with calibrated thermocouples annually.
B. Verification of Operational Status
The temperature recording device will be monitored and verified daily.
C. Quality Assurance and Control Practices
The catalytic oxidizer will be operated, maintained, and inspected according to procedures that take into account manufacturer's specifications.
D. Monitoring Frequency E. Data Collection Procedure F. Averaging Period
The frequency of measurement will be continuous. D. Monitoring Frequency E. Data Collection Procedure F. Averaging Period
Record automatically at least every 15 minutes. D. Monitoring Frequency E. Data Collection Procedure F. Averaging Period There is no averaging done.