dresden station units 2 and 3 hydraulic calculations.f-80 is the most hydraulically remote fire hose...
TRANSCRIPT
Volume 10
AMENDMENT 13
DRESDEN 2 & 3
HYDRAULIC CALCULATIONS
TABLE OF CONTENTS
Tab Numbers Book 2
System Numbers Suppression System Descriptions
DR01 DR02 DR03 DR04 DR05
DR06 DR07 DROS DR09 DRIO
DRI I DRI2 DRI3 DR14 & 15 DR16
DR17 DR18 & 19 DR20 to 25 DR26 DR27
DR28 DR29 DR30 DR31 DR32
DR33 DR34 DR35 DR36 DR37
4
5
6
I
III-i
Unit 2 Condensate Pumps Unit 3 Condensate Pumps
Unit 2 Component Cooling Service Water Pumps
Unit 2 HPCI Pump Unit 3 HPCI Pump
Unit 2 Trackway Unit 3 Trackway Units 2 and 3 EHC Oil Reservoir Unit 2 Instrument Air Compressor Unit 2 Bus Duct Penetration
Unit 3 Bus Duct Penetration Units 2 and 3 Turbine Mezzanine (C-D and 40-48)
Units 2 and 3 Turbine Mezzanine (D-H and 43-45)
Units 2 and 3 Turbine Lube Oil Reservoir
Unit 2 Hydrogen Seal Oil Unit
Unit 3 Hydrogen Seal Oil Unit
Unit 2 Turbine Mezzanine Cable Concentration Units 2 and 3 Cable Tunnel Unit 2 ACAD Air Compressor Unit 3 ACAD Air Compressor
Units 2 and 3 Fire Pump and Fuel Day Tank
Unit I Fire Pump and Fuel Day Tank
Unit 3 Turbine Condenser Pit (Hotwell)
Unit 2 Turbine Condenser Pit (Hotwell)
Unit 2 High Pressure Heater Bay
Unit 3 High Pressure Heater Bay Unit 2 Low Pressure Heater Bay Unit 3 Low Pressure Heater Bay Unit 2 Oil Storage Area
Units 2 and 3 Auxiliary Heating Boiler
AMENDMENT 13 DRESDEN 2 & 3
HYDRAULIC CALCULATIONS
TABLE OF CONTENTS
Tab Numbers System Numbers Suppression System Descriptions Book 2
7 DR38 Unit 2 Main Transformer DR39 Unit 2 Auxiliary Transforner 21 DR40 Unit 2 Auxiliary Transfonner 22, PLC 8/1-2/84, Grinnell
5-3-89 DR41 Unit 3 Main Transfomler (refer to Calculations DRE 96
0145 and DRE 97-0290 for Unit 3 Main Power Transformer hydraulic requirenients)
DR42 Unit 3 Auxiliary Transformer 31
8 DR43 Unit 3 Auxiliary Transformer 32 APPROI Unit 3 Reactor Building Ladder Penetration APPR02 Unit 3 Reactor Building Hatchway APPR03 Unit 2 Reactor Building Hatchway and Stairwell APPR04 Unit 2 Reactor Building Ladder Penetration
9 APPR05 Units 2 and 3 Turbine Building Corridor APPR07B Unit 3 CRD and CCSW Pump Rooms APPRO8 Crib House Lower Level Deluge (Diesel Generator
Cooling Water Pump) APPR09 Crib House Lower Level Ceiling APPRIOA Crib House Upper Level-East Half, Crib House Upper
Level-West Half
10 AREA LL Units 2 and 3 Crib House Cable Tray Deluge System
11 Units 2 and 3 Makeup Dernineralizer System Demineralizer Resin Storage Room
12 Hydraulic Analysis of Fire Suppression System Demands
13 APPR10 Hydraulic Analysis of the Dresden Station Unit 2/3 Crib House Fire Suppression System APPR10
III-]]
Volume 11
AMENDMENT 13
DRESDEN 2 & 3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Volume Index
Volume 11 - Hydraulic Calculations (Continued)
IV C-Factor Verilication Data (C=80)
V Supplement One - Hydraulic Verification Study
VI Supplement Two - Hydraulic Verification Study
VII Supplement Three - Hydraulic Verification Study
VIII Supplement Four -- Hydraulic Verification Study
IX Unit 2/3 Turbine Building Hose Station Hydraulic Analysis
Mia 1)A77.-rA'j 0 KT/z / t,
CALCULATION TITLE PAGE Page No. 1.0
Dresden Station CALCULATION NO: DREOO-0008 DESCRIPTION CODE (C018): FOO
[ ]U1 [ U2 []U3 [X] Unit 0 DISCIPLINE CODE (C011): M SYSTEM CODE: 41 ELEVATION CODE (C016): 561'-6"
Title: Unit 213 Turbine Building Hose Station Hydraulic Analysis
[ ] Safety Related [X] Augmented Quality ] Non-Safety Related
REFERENCE NUMBERS: (C011 Panel)
Type Number Type Number
COMPONENT EPN: (c014 Panel) DOCUMENT NUMBERS: (CO12 Panel) (Calc. References)
EPN Component Type DocType SubType Document Number DWGC M-23, Sht 2
DWGC M-375, Sht 2
- -. = ,- - J I |•Il•SI%
REMARKS: This calculation was performed under the Comt--approvea 4 1 a Quality Assurance Program. QA documentation and data files are retained with
NTSC.REV. REVISING
No. ORGANIZATION
IX-1
CornEd CALCULATION REVISION PAGE
CALCULATION NO. DREOO-0008 PAGE NO.: 2.0 I REVISION SUMMARIES
I
Supplemental Review Required? [ ] Yes (NEP-12-05 documentation attached) [ 3 No
s..... vI.,_,s (CornEd USE ONLY)
ou t:lv"Ibul
DO ANY ASSUMPTIONS IN THE CALCULATION REQUIRE LATER VERIFICATION? []YES [X] NO
Tracked by: (NTS#, AT#, EWCS#)
IX-2
REV: 0 REVISION SUMMARY:
The hydraulic demand for the Unit 2 Turbine Deck hose stations F-75 and F-80, and for Unit 3
Turbine Deck hose station F-126, is calculated herein.
Electronic Calculation Data Files: (Program Name, Version, File name extlsize/datefhour/min)
Prepared by: I '/ Pdnt/Sign/Initial Date
Reviewed by: "• -. / /-/74' Print/Sign/Initi I Date
Type of Review [X] Detailed [ ] Alternate [ Test [ ] By Repetitive Calc
Review
upplemental Review Required? Yes (NEP-12-05 documentation attached) No Supervisor (ComEd USE ONLY)
DO ANY ASSUMPTIONS IN THE CALCULATION REQUIRE LATER VERIFICATION? []YES [X] NO
Tracked by: (NTS#, AT#, EWCS#) N/A
REV: R•EVISION SUMMARY:
Electronic Calculation Data Files: (Program Name, Version, File name extlsize/date/hour/:min)
Prepared by: Print/Sign/Initial Date
Reviewed by: Print/Sign/Initial Date
Type of Review []Detailed []Alternate []Test []By Repetitive Calc
Review
Calculation Table of Contents Page
CALCULATION NO. DREOO-0008 REV. NO. 0 PAGE NO. 3.0
SECTION: PAGE NO. SUB-PAGE NO.
"TITLE PAGE 1.0
REVISION SUMMARY 2.0
TABLE OF CONTENTS 3.0
PURPOSE/OBJECTIVE 4.0
METHODOLOGY AND ACCEPTANCE CRITERIA 4.0
ASSUMPTIONS 5.0
DESIGN INPUT 5.0
REFERENCES 5.0
CALCULATIONS 6.0
SUMMARY AND CONCLUSIONS 7.0
ATTACHMENTS:
A: NFPA 14 Deviation Close Out Matrix, NTSC Al to A2
Report No. 93-124, Rev. 0. B: SPRINK-1000 output data, Fire Hose Station B1 to B27
F-80 C: SPRINK-1000 output data, Fire Hose Station C1 to C27
F-75 D: SPRINK-1000 output data, Fire Hose Station D1 to D27
Ff-126
IX-3
I
COMED COMPANY CALCULATION PAGE
CALCULATION NO. DREOO-0008 PAGE NO. 4.0
PURPOSE I OBJECTIVE
NFPA 14-1974, Paragraph 219, requires standpipes to be at least 2 inches in diameter. However, some
Turbine Building standpipes are 1-1/2 inches in diameter as documented in Deviation No. 14-02, listed in
the Dresden Unit 2/3 NFPA 14 Deviation Close Out Matrix (Ref. 1). The purpose of this report is to
provide a technical justification for this deviation.
METHODOLOGY AND ACCEPTANCE CRITERIA
The SPRINK-1000 computer program (Ref. 4) was used to verify that the fire water system is capable of
supplying a minimum flow rate of 100 gpm at 65 psi at the outlet of the most hydraulically remote 1-1/2"
hose station. The design criteria that was used satisfies the requirements of NFPA 14, Standard for the
Installation of Standpipe and Hose Systems (Design Input 1, Paragraph 541).
FIRE HOSE STATION SELECTION- -� .L.. � .- �4+b� � lr�cp �t 2 tinn�
In order to determine if the fire water system can adequately meet me uemanu Uv ...
whose piping is less than 2 inches, three hose stations were selected for hydraulic analysis based on their
physical location in the plant. Two of these hose stations are located in the Unit 2 Turbine Building, and
one is located in the Unit 3 Turbine Building. All three are located at the 561 '-0" elevation. Piping
layout drawings (Ref. 3), P&IDs (Ref. 2), and engineering judgment were used to determine the most
hydraulically remote hose stations.
The latest revision of the station drawings was used as design input for this report. Pending changes to
the drawings were reviewed and verified not to affect the hydraulic calculations.
Only the Turbine Building was studied because it was the only building identified in the NFPA 14
Deviation Close Out Matrix (Ref. 1) to contain fire hose stations that did not satisfy the NFPA 14 (Design
Input 1, Paragraph 219) requirement for minimum 2" piping.
Hose stations F-75 and F-80 on the Unit 2 Turbine Deck (El. 561 '-6") and F-126 on the Unit 3 Turbine
Deck (El. 561 '-6") were selected.
STATION MODEL APPLICATION
An existing hydraulic calculation (Design Input 2) that uses the SPRINK-1000 computer program (Ref. 4)
was used in this analysis to model the fire water system. The referenced calculation models the
underground and above-ground fire protection loop piping.
REVISION NO. 0
IX-4
COMED COMPANY CALCULATION PAGE
CALCULATION NO. DREOO-0008 PAGE N. 5.0
FIRE HOSE STATION HYDRAULIC SUPPLY CALCULATION
"rL. ....... tl,, Of the fire hose station to the fire water system was located on the P&IDs (Ref. 2) and the
pipin the n
FAIl
The An i No.
AS5
Non
DE
RE
ag layout drawings (Ket 3). Piping data w as a,. . . .. .... ... Lode point nearest to the hose station connection to the fire water system.
LURE SCENARIO
Unit I Diesel Fire Pump (U1 DFP) out of service is the only failure scenario analyzed in this report.
noperable U I DFP was determined to be the worst-case scenario based on the results of Calculation
DRE97-0256, Rev. 2 (Design Input 2).
3UMPTIONS
Le.
SIGN INPUT
1. NFPA 14, Standard for the Installation of Standpipe and Hose Systems, 1974 Edition.
2. Dresden Calculation DRE97-0256, Rev. 2, "Dresden Station Fire Protection System Design Basis
Hydraulic Calculations," dated 8/21/98.
"FERENCES
1. Table A, NFPA 14 Deviation Close Out Matrix, NTSC Report No. 93-124, Rev. 0, dated 5/16/94.
2. Dresden Station P&IDs:
M-23, Sht. 2, Rev. P M-375, Sht. 2, Rev. L
F•-253, Rev. 1 F-254, Rev. B
F-434, Sht. 1, Rev. R
F-434, Sht. 2, Rev. D
REVISION NO. 01
IX-5
S.. .. ,-.,.x .n__:__ .1^÷ .... . elA, tn• the station fire water system hydraulic model at
1 -1 - 1- 1 - 1 -
COMED COMPANY CALCULATION PAGE
CALCULATION NO. DREOO-0008 PAGE
I NO. 6.0
3. Dresden Station Piping Layout Drawings:
M-103, Rev. H M-108, Rev. U M-121, Rev. S M-427, Rev. H M-43 1, Rev. L
4. SPRINK-1000, A Microcomputer Program for the Hydraulic Analysis of Fire Sprinkler Systems,
Version 11.00. Municipal Hydraulics Ltd.
5. NFPA Fire Protection Handbook, Eighteenth Edition.
CALCULATIONS
The SPRINK-1000, Version 11.00, computer program (Ref. 4) was used to calculate the fire water system
supply for the two most hydraulically remote hose stations in the Unit 2 Turbine Building, and one in the
Unit 3 Turbine Building.
The accuracy of the computer program was validated against a controlled output file in accordance with
the NTSC Quality Assurance Program.
The K-Factor for the hose stations used in the calculation is as follows:
K = QI/ 1i- Derived from Ref. 5, Page 6-171
Design Criteria per NFPA 14 Design Input 1, Paragraph 541
Q 100 gpm P 65 psi
K= 100/,r65= 12.4
The SPRINK-1000 output files containing the available pressure and flow rate for hose stations F-75, F
80 and F-126 are included in Attachments B, C and D.
[REVISION NO. 0I
IX-6
COMED COMPANY CALCULATION PAGE
CALCULATION NO. DREOO-0008 PAGE NO. 7.0 of 7.0
SUMMARY AND CONCLUSIONS
F-80 is the most hydraulically remote fire hose station based on the hydraulic calculations. The results of
the calculation show that the fire water system is capable of supplying 119 gpm at 92 psi to hose station
F-80. As a result, the Dresden Station fire water system is capable of supplying the demand of the fire
hose stations in the Turbine Building.
REV/ISION NO. 0
IX-7
CALCULATION NO. DREOO-0008 Revision No. 0
ATTACHMENT A
NFPA 14 DEVIATION CLOSE OUT MATRIX
IX-8
322I
NFPA #14 DEVIATION CLOSE OUT MATRIX
TABLEA
Deviation justification
Rec ndd Action
The addition of hose reel numbers to P&Ios and F-Drawings have been updated DD
the F-drawings would simplify the (Ref.2, pg 1.1-12, item 4.1).
gathering of needed information (Ref.1,
pg 8,•pare 2)
In the Turbine Building some standpipe A hydraulic analysis was performed on Locate hydraulic
sizes are less than 2 inches (Ref.1, pg three hose stations to verify adequacy calcs and reference
8, pars 5). of 1-1/2" supply pipe. The analysis them in the
indicates the required amount of water adjacent
Several plant areas shown in Table 3.1
can be delivered (Ref.1, pg 8, pare 5). NTSC could not find the analysis
referenced in the above justification.
In specified areas, due to the minimal
amount of combustibles and other fire
justifione.on.
None.
S.. .. cannot be reached W• E • ovi ed the...
a 30' hose stream (Ref.1, pg 9, 10, protection features provided, tne existing configuration Is adequate (Ref.1, pg 9, 10, 11).
Recommendation made for additional hose Procedure 4114-06
to select hose stations with less than does not require
100 ft hose (Ref.1, pg 17, Item 4.3). 100' of hose to be verified(except for
ones that are justified in Table 3.1). Revise Procedure. Add justified hoses to this deviation.
14-04 342 As identified in Table 3.1 standpipes Table 3.1 does not reference any stand 0DDt
not provided with 1-1/2" outlets at pipes without 1 1/2 inch outlets.
each floor (Ref.1, pg 11, pare 3).
- oved hose is at The additional hose length is required None.
som e hose stations (Ref.1, pg 11, pare to provide adequate coverage for the
7). Two 150 ft hard rubber hoses are control room (NTSC)o
provided to protect the Control Room.
14-06 43 Labels Indicating use and operating The fire hoses are for use by the fire None.
Instructions ape not provided on hose brigade only. Signs have been provided
racks (Ref.1, pg 11, pars 8). on each hose station identifying that only the fire brigade can use the
*hoses. All fire brigade member have been adequately trained to handle
hoses. As a result, operating instructions on the hose stations are
unnecessary (NTSC).
Note: References are located on the last page of this matrix.
>
Deviation
14-01
14-02
I /�-O3
I
NFPA #14 DEVIATION
CLOSE OUT MATRIX TABLE A
Deviation I Code Deviation Justification RecActon No.I secti(on.I1-1
14-07 44; OSHA Sub- Pressure reducing devices are not CECo policy is not to use pressure None. part L provided for standpipes exceeding 100 reducing devices ... (Ref.2, pg 1.1-12,
psi (Ref.1, pg 12, pare 3). Item 4.4) Fire hoses are for the use of the fire brigade only. ALL brigade members have been adequately trained to handle hoses subject to high pressure.
(NTSC)
14-08 6 The main 2/3 discharge valve is not of A NTSC walkdown found that an indicator DD an indicating type as required (Ref.1, has been installed on the valve. pg 15, para 2).
14-09 67 Water flow switches are not provided on A primary function of a flow switch Is None. alt standpipes (Ref.1, pg 1S, pare 5). to provide notification of unauthorized
use. Since access to a nuclear power plant is controlled, unauthorized operation is not normally a concern. in addition, operation of a hose station should activate the fire purp running alarm (NTSC).
References: 1. An Evaluation of Standard for the Installation of Standpipe and Hose Systems (NFPA# 14) at the Dresden Nuctear Power Station,
Units 2 and 3 for CommonweaLth Edison Company, 5/30/85, Rev.1
2. Sargent and Lundy Letter dated 8/7/87 from J.W. Zesuteck to R.J. Whalen, Project 7927-05 >
•= 3 S
Page AZ- o"/2p
I
o
CALCULATION NO. DREOO-0008 Revision No. 0
ATTACHMENT B
SPRINK-1000 OUTPUT DATA HOSE STATION F-80
IX-1I
KevisIon U Attachment B
DESIGN PROGRAM FOR SPRINKLER SYSTEMS P 7c
by
MUNICIPAL HYDRAULICS LTD, LADYSMITH, B.C. CANADA
COPYRIGHT (C) 1995 MUNICIPAL HYDRAULICS LTD
VERSION 11.00
COMPANY Nexus Technical Services Corporation
DESIGNER : BY: BRIAN FOX CHECKED:,•A& L/"j/7
CLIENT : ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT : Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. U2TB Hose Station F-80
FIX
C-62
p 01 01 02 3.5 11.938
P 02 02 03 16.1 11.938 1GV ITT 3SE CV
P 03 03 04 21.2 7.981 2SE
C-132
P 04 04 05 60.0 11.2 HE SE 3ZSE(7)
P 05 05 06 13.5 11.2 TT GV
C-66
P 06 06 07 156.6 7.85
P 07 07 08 161.0 7.85
P 14 08 13 86.0 7.981 ITT
C-55
P 15 13 14 54.6 7.981
P 750 700 701 72.8 7.981 4HE
P 16 14 15 14.1 11.2 GV
P 17 15 700 44.5 11.2 GV
P 751 701 16 29.3 11.2
C-86
P 18 16 35 9.1 11.2
P 19 35 702 82.7 11.2 HE
P 752 702 17 41.9 7.85
P 20 17 726 119.6 7.85 HE
P 21 725 19 97.9 7.85
P 725 18 725 6.8 11.2 GV
P 726 18 726 4.5 11.2 GV
P 727 18 727 2.1 11.2 GV
C-59
P 762 723 919 12.5 8.385 GV
P 922 919 19 29.2 7.85
C-66
P 22 20 723 82.2 8.385 TT SE ZSE(S)
P 23 20 21 133.3 8.385 TT 3HE GV
P 30 27 703 4.0 7.981 1GV
P 753 703 21 26.0 7.85 TT
C-86
P 29 21 26 147.0 7.981 ITT
P 28 26 25 146.0.7.981 2SE
C-62
P 27 25 601 81.9 7.981 6SE IGV
P 601 601 24 10.8 7.981 ISE
P 754 602 704 58.7 7.981 4SE IHE ITT 1GV
P 602 602 24 123.0 7.981 5SE 2HE GV
P 755 704 705 221.92 7.981 7SE 2HE ITT
C-86
P 756 705 727 141.27 7.981 2HE ITT IX-12
C-62
P 300 24 200 136.5 7.981 5SE IGV ITT
P 26 200 923 7.5 7.981 ISE ITT 1GV
P 757 704 706 197.01 4.026 8SE 4HE GV
P 758 706 923 178.37 4.026 12SE 4HE GV
P 925 923 23 21.25 7.981 3SE ITT 1GV
C-132
P 25 22 724 75.0 11.2 TT 4HE
C-62
P 719 719 23 5.86 7.981 2HE
C-86
P 763 724 719 26.0 7.85
C-132
P 24 05 22 149.9 11.2 GV TT
C-35
P 50 45 48 255.0 9.564 5SE 2GV IHE
*.NE***************
/. NOTE
THE FOLLOWING PIPES HAD A*
/ CALCULATED C FACTOR OF 27.4. DUE*
/ TO LIMITATIONS OF THE SPRINK
/ PROGRAM, A C OF 35 WAS USED*
/* (THE MINIMUM) AND PIPE LENGTHS*
/* ADJUSTED TO REFLECT EQUIVALENT*
/* FRICTION LOSS.*
P ACTUAL LENGTHS ARE AS FOLLOWS:*
/*PIPE 41 - 10.8"
/-PIPE 42 - 9.8*
/-PIPE 45 - 22.3*
/-PIPE 46 - 10.0
/-PIPE 49 = 2.0'
**************************** *****,,
p 41 40 41 17.0 10.02
P 42 41 42 15.4 10.02 1HE 1GV ICV ISE
P 45 42 45 35.1 10.02 ITT
P 46 37 38 15.1 7.981 IGV SE 2HE
P 49 45 37 3.5 7.981 ITT
C-132
P 47 38 39 230.0 11.2 3SE 2HE 4ZSE(7) 3ZSE(3)
P 48 39 22 59.3 11.2
C-62
P 55 48 67 115.92 10.02 7SE
P 70 67 69 3.25 10.02
P 69 69 80 2.17 10.02
P 68 80 64 5.33 10.02 1GV
P 67 64 63 86.75 7.981 9SE 2TT 1GV 2HE
P 66 63 62 36.93 6.065 4SE IGV ITT
P 65 62 61 70.08 6.065 3SE 2HE
P 64 61 60 130.25 6.065 3SE 4HE ITT
P 63 60 59 30.83 6.065
P 62 59 58 6.75 6.065
P 302 58 201 80.0 6.065 1GV 4HE
P 303 201 202 482.5 10.02 2TT
P 305 57 201 89.0 6.065 ISE IGV 2HE
P 60 56 57 1.0 7.981
P 59 55 56 15.08 7.981 4HE
P 58 54 55 107.58 7.981 2HE
P 57 53 54 15.5 7.981
P 56 70 53 118.25 7.981 7SE 1HE IGV IX-13
Revision 0 Attachment B
P 54 51 70 11.67 10.02
P 53 50 51 2.33 10.02
P 52 49 50 1.0 10.02
P 51 48 49 6.0 10.02 ITT
P 8 8 9 30.0 7.981 bGV
P 9 9 10 110.0 4.026 2SE 1HE 2TT 1GV
P 10 10 12 215.42 4.026 15SE 7HE 2GV ITT
P 11 10 11 77.5 4.026 5SE 2HE 1GV
P 12 11 12 80.25 4.026 8SE 4HE 1GV
P 13 12 15 34.75 4.026 4SE 1GV ITT
P 83 70 68 2.33 10.02 1GV
P 82 68 71 89.83 7.981 3SE
P 81 71 72 54.75 7.981 4SE 1HE
P 80 72 73 15.58 7.981
p 79 73 74 103.58 7.981
P 78 74 75 1.75 7.981
p 77 75 76 14.50 7.981
P 76 76 77 21.50 6.065 2SE
P 75 77 78 175.67 6.065 4SE 2HE 1GV
P 74 78 79 65.83 6.065 2HE
p 73 79 98 122.0 6.065 2SE 2HE
P 72 98 81 32.25 6.065 3SE 2TT 1HE
P 71 81 63 84.83 6.065 IGV
P 110 64 102 0.5 10.02
P 84 102 82 10.5 10.02
P 99 82 86 1.0 10.02 ITT
p 100 86 85 48.5 6.065 2SE 3HE 1GV
P 102 97 84 14.33 7.981 2HE ITT
P i03 84 66 1.50 7.981
P 104 66 47 27.75 7.981 4SE 2GV SR
P 105 47 28 115.0 7.981 ISE 1GV ITT
C-56
P 31 28 721 125.0 7.981
P 761 721 720 17.0 8.385 2HE
P 760 720 27 75.5 7.981 ISE
C-62
P 90 82 88 1.00 10.02 ITT
P 93 88 87 66.0 6.065 4SE 3HE 1GV ITT
P 95 96 83 14.17 7.981 2HE ITt
P 96 83 65 1.50 7.981
P 97 65 46 31.25 7.981 5SE 2GV 1SR
P 98 46 29 112.0 7.981 1SE 1GV ITT
C-56
P 932 29 929 2.5 7.981
P 32 929 928 184.0 8.425 2SE 5HE 2GV
P 931 928 28 98.2 7.981
P 33 30 29 20.0 7.981
C-41
P 40 37 36 160.0 7.981 1GV ITT 4SE 3HE
C-61
P 39 36 52 160.0 7.981
P 38 52 34 10.00 7 .981
P 37 34 33 280.0 7.981 5SE 1HE
C-55
P 36
C-71
33 32 300.0 7.981
P 35 32 31 285.0 7.981
C-61
P 34 31 30 285.0 7.981
/ ...... *...*...........A......... IX-14
Revision 0 Attachment B
F¾Ct 9P3
NOTE/-
/* THE FOLLOWING PIPES WERE
/* ADDED TO ATTACH SYSTEMS
/ TO THE BASE MODEL
C-120
P 611
p 612
P 621
P 834
R 834
p 803
R 800
P 804
601 611 4.5 6.065 2SE ITT
611 612 1.0 6.065
602 621 3.6 6.065 3SE ITT
54 834 28.6 6.065 2SE 2HE 2TT 1GV
536.3
834 800 30.9 6.065 3SE IHE
518.3
800 801 121.75 5.047 7SE 4HE
R
P
R
P
I
GV
*801 509.0
822 801 804 5.5 3.068 ITT
1 804 509.0
805 56 805 25.75 7.981 1HE ITT
805 529.3
P 815 805 819 6.0 7.981 ISE
R 819 536.0
P 816 819 820 6.58 6.065 IHE ITT 1GV
R 820 526.5
P 819 819 822 16.75 6.065 iSE iHE 1GV
R 822 526.5
p 809 77 808 1.0 2.469 ITT tGV
R 808 554.5
P 106 51 812 1.0 7.981 ITT tGV ISE
R 812 538.8
P 806 49 849 84.1 4.026 3SE 2HE ITT 1
P 808 849 815 18.0 4.026 4SE IKE 1GV
P 807 849 814 2.5 4.026 ISE ITT 1GV
R 849 541.8
R 814 541.8
R 815 544.5
P 810 60 809 28.08 4.026 2SE ITT
R 809 549.5
P 842 809 810 23.33 3.068 ISE 1GV
R 810 549.5
P 811 79 811 51.5 3.068 4SE ITT 2GV
R 811 546.0
P 833 98 833 25.58 6.065 ISE ITT 1GV
R 833 554.5
P 836 833 828 75.92 6.065 9SE 2TT
R 828 552.92
P 837 828 829 100 6.065 8SE 2HE ITT
R 829 488.0
P 832 61 832 9.9 6.065 ISE 1GV ITT
R 832 554.5
P 835 73 835 24.5 6.065 ITT 2SE 2HE
R 835 536.3
P 812 55 813 62.7 7.981 4SE 4HE ITT
R 813 525.5
P 813 813 817 1.0 2.469 1TT iGV
R 817 525.5
P 814 813 818 1.5 7.981 1GV
R 818 522.8
P 841 75 823 32.0 7.981 ITT 2SE IHE
R 823 523.3
P 820 76 824 32.0 7.981 2SE 1TT iHEIX-15
1GV
Attachment B
a a - KCVIUIOfl U
0-824 523.3
P 821 824 825 23.25 6.065 ISE iHE IGV
R 825 523.3
P 826 824 826 6.3 6.065 ITT IHE lGV
R 826 523.3
p 850 93 850 12.5 6.065 1GV 2SE ITT
R 850 521.0
P 87 92 93 152.1 4.026 2SE 6HE
P 86 91 92 16.0 6.065 2HE IGV ITT
P 85 82 91 1.0 10.020 ITT
R 91 526.2
R 92 527.0
R 93 527.0
P 851 89 851 12.9 4.026 3SE ITT IGV IHE
R 851 521.5
P 91 88 89 166.9 4.026 yGV 8HE
R 89 527.0
P 800 928 802 33.83 6.065 ITT lGV 2SE
R 802 519.5
P 802 802 803 115.08 4.026 2HE iTT 4SE lGV
R 803 527.7
P 840 838 845 117.8 4.026 5HE 2SE ITT IGV
R 845 591.0
C-62
P 839 96 838 62.4 6.065 1HE 1GV ITT
P 94 838 87 206.1 6.065 6SE 2HE ITT
P 860 97 860 51.5 6.065 1GV IHE
P 101 860 85 168.5 6.065 7SE 3HE
C-120
R 838 505.5
P 861 860 861 119.75 4.026 3HE 3SE TT GV
R 860 505.5
R 861 593.3
P 827 102 855 4.39 6.065 ITT IGV iHE ISE
P 831 42 837 11.0 10.02 2HE
P 824 835 836 63.5 6.065 iGV 5SE 3HE 4TT ICV
R 836 527.08
P 823 836 827 121.5 5.047 4HE 8SE
R 827 509.8
R 837 510.9
R 855 527.9
C-62
P 828 200 839 2.3 6.065 ITT
P 829 839 831 3.0 6.065
P 304 831 202 2.7 6.065
C-120
R 839 527.5
R 831 527.5 ****************** ** ******* *
END
/ ******.****.*******************
C-120
P 500 97 400 26.17 6.065 1HE
P 501 400 401 132.67 6.065 2SE 4HE ITT iGV
P 502 401 402 52.17 4.026 3SE ITT 2GV
P 503 96 403 7.75 6.065 1HE
P 504 403 404 132.33 6.065 ITT 2SE 3HE 1GV
P 505 404 405 47.0 4.026 ITT 3SE 2GV
/* ...... * .... **n.......... * pipes
/* The following nodes and pipes *
Attachment B
IX-16
Revision 0
/* refer to hose stations. To Attachment
/* switch between hose stations, * • •1
/'change the S to an R and remove *
/ the flow and K-factor on the hose *
/ stations that you do not want
/ to flow. /***********************************
/ HOSE STATION F-75
P 600 57 600 13.5 1.610 TT 2SE GV
R 600 566.5
/HOSE STATION F-80
P 651 61 651 49.1 1.610 TT 2SE GV
S 651 566.5 100 12.4 / . *************** **.********
END
R 02 509.5
R 03 516.0
R 04 510.8
R 05 510.8
R 06 510.8
R 07 510.3
R 08 509.6
R 09 509.6
R 10 515.5
R 11 554.2
R 12 515.5
R 13 509.8
R 14 509.3
R 15 509.1
R 16 510.9
R 17 510.1
R 18 509.3
R 19 509.4
R 20 511.4
R 21 510.6
R 22 511.5
R 23 511.5
R 24 525.0
R 25 511.0
R 26 511.5
R 27 510.5
R 28 512.0
R 29 512.0
R 30 511.2
R 31 512.2
R 32 513.0
R 33 512.0
R 34 511.7
R 35 510.1
R 36 512.5
R 37 510.9
R 38 511.0
R 39 511.1
R 41 510.9
R 42 510.9
R 45 510.9
R 46 513.0
R 47 513.0
R 48 529.5 IX-17
AMENDMENT 13 Caic. No. DREOO-OOOS Revision 0
Attachment B R 49 535.5
R 50 536.5
R 51 538.8
R 52 511.7
R 53 556.0
R 54 556.0
R 55 556.0
R 56 556.0
R 57 556.0
R 58 554.5
R 59 554.5
R 60 554.5
R 61 554.4
R 62 562.5
R 63 569.6
R 64 526.0
R 65 520.5
R 66 520.5
R 67 526.0
R 68 552.7
R 69 526.0
R 70 550.5
R 71 558.5
R 72 555.5
R 73 555.5
R 74 555.5
R 75 555.5
R 76 555.5
R 77 555.5
R 78 554.5
R 79 554.5
R 80 526.0
R 81 569.7
R 82 526.0
R 83 519.0
R 84 519.0
R 85 517.5
R 86 526.0
R 87 517.5
R 88 526.3
R 96 505.5
R 97 505.5
R 98 551.2
R 102 526.0
R 200 535.5
R 201 556.0
R 202 535.5
R 400 505.5
R 401 601.0
R 402 593.3
R 403 505.5
R 404 601.0
R 405 593.3
R 601 525.0
R 602 528.3
R 611 532.5
R 612 532.5
R 621 527.3
R 720 512.0
R 721 512.0 IX-18
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment B
R 723 510.5
R 724 511.5 - g
R 700 509.1
R 701 510.4
R 702 510.6
R 703 512.0
R 704 528.5
R 705 511.3
R 706 524.7
R 719 511.5
R 725 509.3
R 726 509.3
R 727 509.3
R 919 510.5
R 923 541.0
R 928 512.0
R 929 512.0 /*****************************************************
NOTE
/ TO DEACTIVATE PUMP UNIT 1:*
I. CHANGE:*
/* 1 01 500.0 0.0 150 2000 150 2500 140 3750 91 3751 10*
/* TO:
/* R 01 500.0 /************************************ .******t*****
R 01 500.0 /***t********************** ****** *****************
NOTE
/* TO DEACTIVATE PUMP UNIT 2/3:*
/- CHANGE:*
/* I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10*
/* TO:*
/* R 40 500.0
I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10
LENGTH DIAMETER FLOW HEAD ELEVATION PRESSURE
UNITS BEING USED: FEET INCHES US GPM FEET FEET PSI
HAZEN-WILLIAMS FORMULA USED
FITTINGS SPECIFIED AS NFPA
ITERATION STOPS WHEN GREATEST FLOW CHANGE IS .05000 IN ANY PIPE
MULTIPLICATIVE FACTOR OF EACH CONSUMPTION IS 1.00000
DEFAULT ROUGHNESS COEFFICIENT - C-120.0
THERE ARE 1 SPRINKLERS AND 0 BOOSTER PUMPS
THERE ARE 181 PIPES AND 169 REFERENCE POINTS
THE NUMBER OF INPUT POINTS IN SYSTEM IS I
NODE NO. OF PUMPS PUMP INPUT PUMP PARAMETERS
NO. IN PARALLEL ELEVATION FRACTION OR X-Y COORDINATES
40 1 500.00 1.00 .0 2250.0 3000.0 3600.0 4900.0 4901.0
150.0 150.0 131.0 120.0 110.0 10.0
IX-19
AMENDMNT 13 Caic. No. DREOO-OOOS AMENDMNT 13 Revision 0
Attachmncn B
Initial estimate of demand on the system is
NET UNBALANCED DEMAND ON THE SYSTEM - .00000
LOOP PIPES
1 651 65 66 67 68 69 70 55 50 45
2 65 64 63 62 302 305 60 59 58 57
66
54 83 82 81 80 79 78 77 76 75
52 53
68 110 84 90 93 94 839 95 96 97
50 55 70 69
303 305 60 59 58 57 56 54 53 52
26 828 829 304
99 90 93 94 839 95 96 97 98 932
932 33 34 35 36 37 38 39 40 46
28 29 753 30 760 761 31 931 32
754 757 758 26 300 602
25 24 5 6 7 14 15 16 17 750
758 925 719 763
725 727 756 755 754 602 601 27 28 29
14 8 9 10 13 16 15
10 11 12
BANDWIDTH 5 5
Iteration # 0 Max change in flow is
Iteration # 1 Max change in flow is
Iteration 6 2 Max change in flow is
Iteration # 3 Max change in flow is
Iteration # 4 Max change in flow is
Iteration # 5 Max change in flow is
NUMBER OF ITERATIONS= 6
42 41
56 54 53 52 51 55 70 69 68 67
74 73 72 71 67 68 69 70 55 51
98 33 34 35 36 37 38 39 40 49
51 50 49 46 47 48 25 763 719 925
32 931 105 104 103 102 860 101 100
47 48 25 763 719 925 26 300 601 27
751 18 19 752 20 726 727 756 755 757
23 22 762 922 21
74.714 in loop # 2
33.536 in loop # 3
15.510 in loop # 3
4.344 in loop # 3
.456 in loop # 3
.005 in loop # 3
IX-20
100.00
f 1c ( 7 C Re0-0
3
4
5
6
7
8
9
10
11
12
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment B
SUMMARY REPORT
COMPANY Nexus Technical Services Corporation PAGE 90 :e
DESIGNER BY: BRIAN FOX CHECKED: LDATE 2000 JAN 6
CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT UI DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. U2TB Hose Station F-80
MINIMUM FLOW OF ALL OPERATING SPRINKLER HEADS IS 118.89
AVERAGE FLOW FROM ALL OPERATING SPRINKLER HEADS IS 118.89
TOTAL FLOW FROM ALL OPERATING SPRINKLER HEADS IS 118.89
TOTAL DEMAND ON THE WHOLE SYSTEM IS 118.89
SPECIFIED AVAILABLE PRESSURE AT INPUT NODE IS 346.40 FEET
OR 150.00 P.S.I.
IX-21
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment B
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I PAGE 0JAN 1 JDATE 2000 JAN6COMPANY Nexus Technical Services Corporation
DESIGNER BY: BRIAN FOX CHECKED:
CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT 1U1 DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB No. IU2TB nose -~' a .
I I PIPE DIAMETERI PIPE/FTG TOTAL 1HEAD LOSSIHEAD LOSS I STATIC TOTAL ROUGH) WATER I VELOC.I
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH I PER FT. OVER PIPE 1HEAD LOSSIHEAD LOSS NESS IVELOCITYi PRESS.!
INO. I NODES (US GPM) I (IN) (IN) I # (FT) (FT) I (PSI) (PSI) (PSI) I (PSI) ICOEFFI (FT/SEC)i (PSI) 0•00,II.00
I I_ I __ _ _ _ __ _ _ _ _
1 1
2
3
4
6 71 81
9O
10I
11
12
13
14
15
1 2
2 3
3 4
4 5
5 6
6 7
7 8
8 9
9 10
10 12
10 11
11 12
12 15
8 13
13 14
0.00
0.00
0.00
0.00
13.47
13.47
13.47
1.54
1.54
0.71
0.83
0.83
1.54
11.93
11.93
4.114 62 1
12 12
12
12
8
12
12
12
12
12
.p 11.94 C:
11.94 C
1'
1 13
7.98 C
2
11.20 C
1
II
3
11.20 C
7.85
7.85I
7.98
4 .03
4.03
40
4.03
4.03
4.03
7.98
7.98
____________I I__________ I _____I_______
IX-22
SAM
SAM GV
TT
SE
CV
SAM
SE
SAM
HE
SE
3ZSE
CSAM
TT
IGV
CSAM
CSAM
CSAM
1GV
CSAM
2SE
1HE
2TT
IGV
CSAM
5SE
7HE
2GV
ITT
CSAM
5SE
2HE
1GV
CSAM
8SE
4HE
1GV
CSAM
4SE
1GV
lTT
CSAM lITT
CSAM
3.5 16.1
1.7
17.2
23.3
18.7
21.2
10.0
60.0
11 .1I
23.0
21.0
13.5
51.2
5.1
156.6
161.0
30.0
1.1
110.0
5.9
1.2
11.8
0.6
215.4
44 .2
8.2
1.2
5.9
77.5
14 .7
2.4
0.6
80.3
23.6
4.7
0.6
34.8
11.8
0.6
5.9
86.0
11.0
54.6
8
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
4
8
3.5 0.000 0.000
77.0 0.000 0.000
31.2 0.000 0.000
115.1 0.000 0.000
69.8 10.516E-6 10.00003601
156.6 10.000010 1 0.00165 1
161.0 10.000010 0.00169 1
31.1 10.197E-6 10.0000061 1
129.4 10.00000551 0.000715 1
II
274.9 10.00000131 0.000360 1
II
I I
95.2 10.00000171 0.000168
109.1 10.00000171 0.000192
53.0 10.00000551 0.0002931
97.0 10.00000771 0.000750 1
54.6 10.000010 0.000592 1
4.114 2.815
-2.252
0.000
0.000 10.
-0.217 1
-0.303 1
0.000 l0
2.555 1
0.000
16.758
-16.758
-2.771
0.0866
-0.217
2.815
-2.252
0.000 I
0000360
-0.215
-0.301
.0000061
2.556
0.000360
16.758
-16.758
-2.771
0.0873
-0.216
62
62
.32
132
66
66
62
62
62
62
62
62
66
55
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.0439 10.13E-41
0.0893 10.53E-41
0.0893 10.53E-41
0.00990 0.66E-61
0.0389 10.10E-41
I I
0.01-79 10.21E-51
I I I I I I I I
0.0210 10.29E-51
I I I I I I
0.0389 10.10E-41
0.0765 10.39E-41
I I 0.0765 10.39E-41
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment B
PAGE B 12.HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG TOTAL
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH
INO. I NODES (US GPM) I (IN) (IN) I # (FT) (FT)
IHEAD LOSSIHEAD LOSS
PER FT. JOVER PIPE
I (PSI) (PSI)
STATIC TOTAL
HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
IROUGHJ WATER I VELOC.I
INESS IVELOCITYI PRESS.L
ICOEFFI (FT/SEC)I (PSI) I
I I I I __________ ______ I ______ _______ I ______ I _______ ( ____ I ______ I _____ I - H ______________________________
16
17
18
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
14 15
15 700
16 35
35 702
17 726
725 19
723 20
20 21
22 5
22 724
923 200
601 25
25 26
26 21
703 27
721 28
929 928
30 29
31 30
32 31
33 32
34 33
52 34
11.93
13.47
13.47
13.47
13.47
8.61
8.61
8.61
13.47
40.36
39.32
3.04
3.04
3.04
11.66
11.66
2.08
14.29
14.29
14.29
14.29
14.29
14.29
12
12
12
8
8
8
8
8
8
8
12
12
12
12
8
8
8
8
8
8
8
8
8
8
8
8
8
______ I _____ I _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I ____ I ____ I
IX-23
U2TB Hose St
11.20 CSAM
1GV
11.20 CSAM
1GV
11.20 CSAM
11.20 CSAM
1HE
7.85 CSAM
1HE
7.85 CSAM
8.39 CSAM
ITT
ISE
I1ZSE 8.39 CSAM
ITT 3HE
IGV
11.20 CSAM
1GV
ITT
11.20 CSAM
ITT
4HE
7.98 CSAM
ISE
ITT
1GV
7.98 CSAM
6SE
I1GV 7.98 CSAM
2SE
7.98 CSAM
ITT
7.98 CSAM
1GV
7.98 CSAM
8.43 CSAM
2SE
5HE
2GV
7.98 CSAM
7.98 CSAM
7.98 CSAM
7.98 CSAM
7.98 CSAM
5SE
IHE 7.98 CSAM
14.1
1.0
44.5
1.0
9.1
82.7
5.0
119.6
4.2
97.9
82.2
13.9
7.2
5.0
133.3
13.9
10.7
1.6
149.9
5.1
51.2
75.0
51.2
44.3 3
7.5
5.0
9.8
1.1I
81.9
30.1
1.1I
146.0
18.4
147.0
17.9
4.0
1.3
125.0
184.0
10.8
13.5
2.4
20.0
285.0
285.0
300.0
280.0
24.3
2.4
10.0
15.1 10.000002010.0000315
45.5 10.00000261 0.000119
9.1 10.000001110.0000104
87.7 10.000001110.0001000
123.8 10.00000641 0.000797
1 1 97.9 10.00000281 0.000275
108.3 10.00000331 0.000361
159.6 10.00000331 0.000531
206.2 10.516E-6 0.000106
II II
170.5 10.00000391 0.000670
23.4 0.000079 1 0.00185
113.1 10.693E-6 10.0000784
1 I I I
164.4 10.378E-6 10.0000622
164.9 10.378E-6 10.0000623
1 1 5.3 I0.000007410.0000390
125.0 0.000010 1 0.00126
210.7 10.316E-6 10.0000667
1 1
1 I
20.0 10.000014 0.000293
285.0 10.000012 0.00357
285.0 10.00000941 0.00269
300.0 10.000015 0.00455
306.8 0.000012 0.00384
10.0 10.000012 0.000125
I I
-0.0866
0.000
-0.346
0.217
-0.346
0.0433
0.390
-0.346
-0.303
0.000
-2.382
-6.062
0.217
-0.390
-0.650
0.000
0.000
0.346
-0.433
-0.346
0.433
0.130
0.000
-0.0866
0.000119
-0.346
0.217
-0.346
0.0436
0.390
-0.346
-0.303
0.000670
-2.38060
-6.062
0.217
-0.390
-0.649
0.00126
0.0000667
0.347
-0.429
-0.344
0.438
0.134
0.000125
55
55
86
86
86
86
66
66
132
132
62
62
86
86
66
56
56
56
61
71
55
61
61
0.0388 10.10E-41
1 I 0.0439 I0.13E-41
0.0439 0.1E-41
0.0439 10.13E-41
1 1 0.0893 10.53E-41
0.0571 10.21E-41
0.0500 10.16E-41
I I I I
0.0500 10.16E-41
I I
I
0.0439 10.13E-41
II
0.131 10.000111
0.252 10.000421
1 1
0.0195 10.25E-51
II 0.0195 10.25E-51
1 1
0.0195 I0.25E-51
1 1 0.0748 I0.37E-41
I i 0.0748 10.37E-41
0.0119 10.96E-61
1o.0917 10.56E-41 0.0917 10.56E-41
0.0917 10.56E-41
0.0917 10.56E-41
0.0917 I0.56E-41
I I I I
0.0917 10.56E-41
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment B
PAGE a(.3HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I IPIPEI PIPE
INO. NODES (I
PIPE DIAMETERI
FLOW NOM ACTUALI
US GPM)l (IN) (IN) I
PI PE/FTG
CODE LENGTH
# (FT)
TOTAL LENGTH
(FT)
IHEAD LOSSIHEAD LOSS
PER FT. lOVER PIPE
I (PSI) I (PSI)
STATIC TOTAL IROUGHI WATER VELOC.I STATIC I TOTAL
IHEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
I ________ I ____________________ I __________________ I __________________________ I ______________________________ I ________________ I __________________ I ____________________ I __________________ ____________________ 0.00200 I 0.346 I -0.344 I
39
40
41
42
45
46
47
48
49
50
51
52
53
54
55
56
57
58
59
60
62
63
36 52
37 36
40 41
41 42
42 45
37 38
38 39
39 22
45 37
45 48
48 49
49 50
50 51
51 70
48 67
70 53
53 54
54 55
55 56
56 57
58 59
59 60
14.29
14.29
118.89
118.89
118.89
53.83
53.83
53.83
68.12
50.77
22.24
22.24
22.24
22.24
28.52
9.47
9.47
9.47
9.47
9.47
51.64
51.64
7.98 CSAM
7.98 CSAM
8 I1GV
8 ITT
8 4SE
8 3HE
10.02 CSAM
10.02 CSAM
10 IHE
10 1GV
10 ICV 10 ISE
10.02 CSAM
10 ITT
7.98 CSAM
8 1GV
8 ISE
8 2HE
11.20 CSAM
12 3SE
12 2HE
12 4ZSE
12 3ZSE
11.20 CSAM
7.98 CSAM
8 ITT
9.56 CSAM
10 5SE
10 2GV
10 IHE
10.02 CSAM
10 ITT
10.02 CSAM
10.02 CSAM
10.02 CSAM
10.02 CSAM
10 7SE
7.98 CSAM
8 7SE
8 IHE
8 IGV
7.98 CSAM
7.98 CSAM
8 2HE
7.98 CSAM
8 4HE
7.98 CSAM
6.07 CSAM
6.07 CSAM
160.0160.0
160.0
0.5
4.5
9.3
3.5
17.0
15.4
1.1
0.5
5.6
2.2
35.1
5.1
15.1
0.4
1.7
1.7
230.0
69.1
22.2
28.0
9.0
59.3
3.5
3.4
255.0
9.0
0.8
0.9
6.0
14 .7
1.0
2.3
11.7
115.9
45.3
118 .3
35.1
2.5
1.1
15.5
107.6
5.0
15.1
10.0
1.0
6.8
30.8
160.0 0.000012
177.9 10.000026
17.0 10.000584
24.9 10.000584
40.2 10.000584
19.0 10.000408
358.2 10.00000671
1 I
1 1
59.3 10.00000671
6.9 10.000631 1
265.7 10.000152
20.7 10.00000901
1 11.0 2.3
10.00000901
10.00000901
11.7 l0.00000901
161.3 10.000014 I
1 I 157.0 10.00000561
1 I 1 I
15.5 10.00000561
112.6 10.00000561
I 1 25.1 10.00000561
I 1 1.0 10.00000561
6.8 10.000499 1
30.8 10.000499 1
IROUGHI WATER I NESS IVELOCITYI
ICOEFFI(FT/SEC)l
VELOC. PRESS.
(PS I)
I 1 ___ _ _ _
I0.00200 0.00465
0.00993
0.0145
0.0235
0.00774
0.00240
0.000398
0.00434
0.0403
0.000188
0.0000090
0.0000212
0.000106
0.00232
0.000890
0.0000878
0.000638
0.000142
0.0000056
0.00337
0.0154
______ I _____ I _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I ____ ____ I
DX-24
U2TB Hose St
-0.346 -0.344 0.693 0.697
4.720 4.730
0.000 0.0145
0.000 0.0235
0.0433 0.0510
0.0433 0.0457
0.173 0.174
0.000 0.00434
8.054 8.095
2.598 2.598
0.433 0.433
0.996 0.996
5.066 5.066
-1.516 -1.513
2.382 2.383
0.000 10.0000878
0.000 1 0.000638
0.000 1 0.000142
0.000 10.0000056
0.000 1 0.00337
0.000 I 0.0154
61
41
35
35
35
35
132
132
35
35
62
62
62
62
62
62
62
62
62
62
62
62
0.0917 10.56E-41 0.0917 10.56E-41
0.484 10.0015
0.484 10.0015
0.484 0.0015
0.345 10.000801
I 1
1 1 I 1
i
0.175 10.000201
0.437 10.0012 1
1 1
0.227 10.000341
1 1 1 I
1 1
0.0905 0.550-4
1 1
0.0905 10.55E-41
0.0905 10.55E-41
0.0905 10.55E-41
0.116 10.90E-41
0.0607 10.24E-41
I I II II
0.0607 10.24E-41
0.0607 10.24E-41
1 1
0.0607 10.24E-41
0.0607 10.24E-41
0.573 10.0022 1
0.573 0.0022 1
AMENDMENT 13 Calc- No. DREOO-OOOS Rev ision 0 Attachment B
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
PIPE DIAMETERI
PIPE FLOW I NOM ACTUALI
NODES (US GPM) (IN) (IN) I
PIPE/FTG
CODE LENGTH
# (FT)
TOTAL IHEAD LOSSIHEAD LOSS I STATIC I TOTAL IROUGHI WATER
LENGTH I PER FT. OVER PIPE HEAD LOSSIHEAD LOSS INESS IVELOCITYI
(FT) I (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI(FT/SEC)l
____________ __________ _______________I _________________ _________ __________ ______ I ______ I ___ I _____ I ____ I
86.6 0.000814
63.1 0.000814
0.0797
0.0704
0.0514
I 130.3 1 159.7 10.000499
__________________ I ________________ I _______________________ I ___________________________ I ______________ I ________________ I __________________ I _________________ I __________________ l...................I ______________ I ____________ I
IX-25
U2TB Hose St PAGE ,i4-,
VELOC.
PRESS.
(PSI)
64
65
66
67
68
69
70
71
72
73
74
75
76
77
78
79
80
81
82
83
84
60 61
62 61
63 62
64 63
80 64
69 80
67 69
81 63
98 81
79 98
78 79
77 78
76 77
75 76
74 75
73 74
72 73
71 72
68 71
70 68
82 102
51.64
67.25
67.25
54.47
28.52
28.52
28.52
12.77
12.77
12.77
12.77
12.77
12.77
12.77
12.77
12.77
12.77
12.77
12.77
12.77
25.95
6.07
6
6
6
6.07
6
6
6.07
6
6
6
7.98
8
8
8
8
10.02
10
10.02
10.02
6.07
6
6.07
6
6
6
6.07
6
6
6.07
6
6.07
6
6
6
6.07
6
7.98
7.98
7.98
7.98
7.98
8
8
7.98
8
10.02
10
10.02
I-
CSAM
3SE
4HE
ITT
CSAM
3SE
2HE
CSAM
4SE
yGV
ITT
CSAM
9SE
2TT
1GV
2HE
CSAM
1GV
CSAM
CSAM
CSAM
1GV
CSAM
3SE
2TT
1HE
CSAM
2SE
2HE
CSAM
2HE
CSAM
4SE
2HE
IGV
CSAM
2SE
CSAM
CSAM
CSAM
CSAM
CSAM
4SE
IHE
CSAM
3SE
CSAM
IGV
CSAM
12.4
8.2
8.8
70.1
12 .4
4.1
36.9
16.5
0.9
8.8
86.8
45.2
19.5
1.1
5.0
5.3
1.5
2.2
3.3
84.8
0.9
32 . 3
12.4
17.7
2.1
122.0
8.2
4.1
65.8
4.1
175.7
16.5
4.1
0.9
21.5
8.2
14.5
1.8
103.6
15.6
54.8
20.1
2.5
89.8
15.1
2.3
1.5
10.5
157.6 10.000145 0.0228
6.8 10.000014 10.0000981
1 1 2.2 10.000014 0.0000313
3.3 0.00014 10.0000469
85.7 10.0000371 0.00322
I I 64.3 10.0000371 0.00242
134.4 10.0000371 0.00505
70.0 10.000037 1 0.00263
1 1 197.2 10.000037 0.00740
29.7 10.000037 0.00112
14.5 10.00000981 0.000143
1.8 10.000009810.0000173
103.6 10.00000981 0.00102
15.6 10.00000981 0.000154
77.3 10.00000981 0.000763
1 I
104.9 10.00000981 0.00103
3.8 I0.000003210.0000124
I 1 10.5 10.000012 1 0.000127
I 1
-0.0433 0.0364
-3.507 -3.437
-3.074 -3.023
18.880 18.903
0.000 10.0000981 1
I I 0.000 10.0000313
0.000 0.0000469
-0.0433 1 -0.0401
8.011 8.013
-1.429 -1.424
0.000 0.00263
-0.433 -0.426
0.000 0.00112
0.000 0.000143
0.000 10.0000173 1
0.000 0.00102
0.000 0.000154
-1.299 -1.298
2.512 2.513
0.953 0.953
0.000 0.000127
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
0.573 10.0022 1
1 1
I 1
0.747 10.0037 1
1 1
0.747 10.0037 1
1 I I 1
0.349 10.000821
1 1 1 1 1 1
0.116 0.90E-4
0.116 10.90E-41
0.116 I0.9E-41
0.142 10.000131
I 1
0.142 10.000131
0.142 10.000131
1 1 1 1
0.142 10.000131 1 1
0.142 10.000131 1 1
0.0142 0.45E-41
1 1 1 1
0.142 10.000131
1 1
0.0819 10.45E-41
0.0819 10.45E-41
0.0819 10.45E-41
0.0819 10.45E-41
0.0819 10.45E-41
I I 1 1
0.0819 10.45E-41
1 1 0.0520 10.18E-41
1 1 0.106 10.75E-41
I I
AMENDMENT 13 r.Calc. No. DREOO-OOOS F Revision 0 ,i Attachment B
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I IPIPEI PIPE
NO. NODES
I - 1 -1.....I ________________
85
86
87
90
91
93
94
95
96 97
98
99
1100
101
I102
1103
2I
31
82 91
91 92
92 93
88 82
88 89
87 88
838 87
83 96
65 83
46 65
29 46
86 82
85 86
860 85
84 97
66 84
PIPE DIAMETERI
FLOW I NOM ACTUALI
US GPM) (IN) (IN)
PIPE/FTG
CODE LENGTH
# (FT)
"TOTAL HEAD LOSSIHEAD LOSS
LENGTH PER FT. lOVER PIPE
(FT) I (PSI) I (PSI)
STATIC I TOTAL HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
IROUGHI WATER I VELOC.IROUGHI WATER I INESS IVELOCITYI
ICOEFFI (FT/SEC) IPRESS.
(PSI)
_____ ________ I _________ I _____ I _____ I ______ I _____ ______ I ___ _____ I ____
0.0866 I 0.0866 I 120 0.000 0.0000.00
0.00
0.00
12.22
0.00
12.22
12.22
12.22
12.22
12.22
12.22
13.73
13.73
13.73
13.73
13.73
10.02 CSAM
10 ITT 6.07 CSAM
6 2HE
6 I1GV
6 ITT
4.03 CSAM
4 2SE
4 6HE
10.02 CSAM
10 ITT
4.03 CSAM
4 IGV
4 8HE
6.07 CSAM
6 4SE
6 3HE
6 I1GV 6 ITT
6.07 CSAM
6 6SE
6 2HE
6 ITT
7.98 CSAM
8 2HE
8 ITT
7.98 CSAM
7.98 CSAM
8 5SE
8 2GV
8 I1SR
7.98 CSAM
8 ISE
8 IGV
8 ITT
10.02 CSAM
10 ITT
6.07 CSAM
6 2SE
6 3HE
6 1GV
6.07 CSAM
6 7SE
6 3HE
7.98 CSAM
B 2HE
8 ITT
7.98 CSAM
1.0
50.0
16.0
14.0
3.0
30.0
152.1
20.0
24.0
1.0
14.7
166.9
2.0
32.0
66.0
16.5
6.2
0.9
8.8
206.1
24 .7
4.1
8.8
14.2
5.0
9.8
1.5
31.3
25.1
2.2
19.5
112.0
5.0
9.8
1.0
14.7
48.5
8.2
6.2
0.9
168.5
28.9
6.2
14.3
5.0
9.8
1.5
51.0 0.000 0.000
63.0 0.000 0.000
196.1 0.000 0.000
15.7 10.0000030 0.0000471
1 1 200.9 0.000 0.000
98.4 0.000034 0.00340
243.8 0.000034 0.00843
28.9 10.00000901 0.000263
1 1 1 1
1.5 10.000009010.0000136
78.1 10.00000901 0.000709
1 1
I I
127.9 10.00000901 0.00116
15.7 10.000003710.0000585
63.8 10.000042 0.00274
I I
1 1
203.5 10.000042 0.00874
29.1 0.000011 0.000328
1.5 10-000011 10.0000169
II
0.0866
0.346
0.000
-0.130
0.303
3.811
5.196
5.846
-0.650
3.248
0 .433
0.000 0.
3.681
5.196
-5.846
-0.650
0.0866
0.346
0.000
-0.130
0.303
3.814
5.205
-5.846
-0.650
3.248
0.434
0000585
3.683
5.205
-5.845
-0.650
120
120
120
62
120
62
62
62
62
62
62
62
62
62
62
62
__ _ _I_ _ _ I_ _ _ _ I_ _ _ __I _I__ -I- _ _1_ 11 1 _ __ 1 _ _ 1_ I1 __1_ I I _ _ _ I _
IX-26
U2TB Hose StP A G E J3 1 -5
0.000 0.000
0.000 0.000
0.000 0.000
0.0497 10.16E-4
0.000 0.000
0.136 10.00012
0.136 10.00012
0.0784 10.41E-4
0.0784 10.41E-4
0.0784 10.41E-4
0.0784 10.41E-4
0.0559 I0.21E-4
0.153 0.00015
0.153 0.00015
0.0881 0.52E-4
0.0881 10.52E-4
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment B
PAGE 6 lbHYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
PIPE DIAMETERI
FLOW NOM ACTUALI
(US GPM)I (IN) (IN) I
PI PE/FTG
CODE LENGTH
# (FT)
TOTAL
LENGTH
(FT)
HEAD LOSSIHEAD LOSS
PER FT. OVER PIPE
I (PSI) I (PSI)
I STATIC I TOTAL ROUGH I WATER I VELOC.ISTATIC ITOTAL HEAD LOSSIHEAD LOSS
I (PSI) (PSI)
IROUGHI WATER I NESS IVELOCITYI
ICOEFFI (FT/SEC)l
I I I _____ ________ I _________ I _____ _____ I ______ I _____ I ______ I ___ I _____ ____ 3.248 3 248 62 I 0.0881 I0.52E-4I
Ii
I'
I]
I:
I:
04
105
06
110
300
302
303
304
305
500
501
502
503
504
505
47 66
28 47
51 812
102 64
24 200
201 58
202 201
831 202
57 201
97 400
400 401
401 402
96 403
403 404
404 405
13.73
13.73
0.00
25.95
2.85
51.64
42 .17
42.17
9.47
0.00
0.00
0.00
0.00
0.00
0.00
8
8
8
8
8
8
8
8
8
8
8
8
6
6
10
6
6
6
6
6 6
6
4
4
4
6
6
6
6
6
4
4
4
7.98 CSAM
4SE
2GV
ISR
7.98 CSAM
ISE
1GV
ITT
7.98 CSAM
ITT
1GV
ISE
10.02 CSAM
7.98 CSAM
5SE
IGV
ITT
6.07 CSAM
1GV
4HE
10.02 CSAM
2TT
6.07 CSAM
6.07 CSAM
ISE
IGV
2HE
6.07 CSAM
IHE
6.07 CSAM
2SE
4HE
ITT
IGV
4.03 CSAM
3SE
ITT
2GV
6.07 CSAM
IHE
6.07 CSAM
ITT
2SE
3HE
1GV
4.03 CSAM
ITT
3SE
2GV
_____ I _____ I _______ I ________ I ____ I _____ ______ I _____ I _____ I ___ I ____ ____ I
U2TB Hose St
I I IPIPEI
I NO.
PIPE
NODES
VELOC. PRESS.
(PSI)
27.8
20.1
2.2
19.5
115.0
5.0
1.1
9.8
1.0
33 .1i
3.8
17.0
0.5
136.5
25.1
1.1
9.8
80.0
0.9
8.2
482.5
29.4
2.7
89.0
4.1
0.9
4.1
26.2
7.0
132.7
28.0
28 .0
30.0
3.0
52.2
30.0
20.0
4.0
7.8
7.0
132.3
30.0
28.0
21.0
3.0
47.0
20.0
30.0
4.0
69.6 10.
130.9 10.
55.0
0.5 10.
172.5 10.
89.1 10.
511.9 0.
2.7 10.
98.1 I0.
33.2 1
221.7
106.2
14.8
214.3
101.0
000011 0.000785
000011 0.00148
0.000 0.000
000012 10.0000060
612E-6 0.000105
000499 0.0445
000029 0.0152
000343 0.000926
000021 0.00212
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
11I
IX-27
3 .248
0.433
0.000
0.000
4.547
-0.650
8.877
3.464
0.000
0.000
41.354
-3.334
0.000
41.354
-3.334
3 .248
0 .435
0.000
0.0000060
4.547
-0.605
8.892
3.465
0.03212
0.000
41.354
-3.334
0.000
41.354
-3.334
62
62
120
62
62
62
62
62
62
120
120
120
120
120
120
0.0881 10.52E-41
0.000 0.000
0.106 10.75E-41
0.0183 10.22E-51
II
I 0.573 0.0022 1
I 1
0.172 10.000191
0.468 10.0014 1
0.105 I0.74E-41
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
AMENDMENT 13Calc. No. DREOO-000S Revision 0 Attachment B
PAGE 131 -7HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I IPIPEI PIPE I•JA Nc•DF.
PIPE DIAMETERI
FLOW NOM ACTUALI
(US GPM)j (IN) (IN) I
PIPE/FTG
CODE LENGTH
# (FT)
TOTAL
LENGTH
(FT)
HEAD LOSSIHEAD LOSS I STATIC I TOTAL IROUGHI WATER I VELOC.1
PER FT. IOVER PIPE HEAD LOSS IHEAD LOSS NESS IVELOCITYi PRESS.
(PSI) I (PSI) (PSI) I (PSI) ICOEFFI(FT/SEC) (PSI)
.I -
600
1601
1602
1611
1612
1621
1651
719
725
1726
727
1750
751
75
175
175
57 600
24 601
602 24
601 611
611 612
602 621
61 651
719 23
18 725
726 18
18 727
700 701
701 16
702 17
21 703
4 704 602
5 705 704
6 727 705
0.00
1
1
3.04
5.89
0.00
0.00
0.00
118.89
40.36
8.61
13.47
4 .86
13.47
13.47
13 .47
11 .66
5.89
4.86
4.86
______ I _____ I _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I _____ I ____ I
IX-28
U2TB Hose St
1.61 CSAM
1/2 ITT
1/2 2SE
1/2 1GV
7.98 CSAM
8 ISE
7.98 CSAM
8 5SE
8 2HE
8 IGV
6.07 CSAM
6 2SE
6 ITT
6.07 CSAM
6.07 CSAM
6 3SE
6 ITT
1.61 CSAM
1/2 ITT
1/2 2SE
1/2 IGV
7.98 CSANM
8 I2HE 11.20 CSAM
12 1GV
11.20 CSAM
12 IGV
11.20 CSAM
12 1GV
7.98 CSAM
8 I4HE
11.20 CSAM
7.85 CSAM
7.85 CSAM
8 ITT
7.98 CSAM
8 4SE
8 iHE
8 ITT
8 1GV
7.98 CSAM
8 7SE
8 2HE
8 1 TT
7.98 CSAM
8 2HE
8 ITT
13.5
8.0
8.0
1.0
10.8
5.0
123.0
25.1
5.0
1.1
4.5
28.0
30.0
1.0
3.6
42.0
30.0
49.1
8.0
8.0
1.0
5.9
5.0
6.8
2.3
4.5
2.3
2.1
2.3
72.8
8.0
29.3
41.9
26.0
10.1
58.7
20.1
2.5
9.8
1.1 1
221.9
35.1
5.0
9.8
141.3
9.2
17.9
30.5 0.000 0.000
15.8 0.693E-6 10.0000110
154.2 10.00000231 0.000363
1 I
62.5 0.000 0.000
1.0 0.000 0.000
75.6 0.000 0.000
66.1 0.439 1 29.048
10.9 10.000083 0.000903
1 I 9.1 10.498E-6 10.0000045
6.8 10.000001110-0000077
1 i 4.4 0.172E-6 10.00000076
1 I 80.8 10.000013 1 0.00110
1 i 29.3 10.000002610.0000764
41.9 10.00000641 0.000270
36.1 10.00000801 0.000290
1 1 92.1 10.00000231 0.000217
271.8 10.00000161 0.000448
1 1 1 1 1 1
168.3 I0.898E-6 0.000151
II II
I I
4.547 4.547
0.000 10.0000110 1
-1.429 -1.429
3.248 3.248
0.000 0.000
-0.433 -0.433
5.240 34.287
0.000 0.000903
0.000 10.0000045 1
0.000 10.0000077 1
0.000 10.000000761
0.563 0.564 1
0.217 0.217
-0.217 -0.216
0.606 0.607
-0.0866 -0.0864
7.448 7.448
0.866 0.866
120
62
62
120
120
120
120
62
86
86
86
55
55
86
66
62
62
86
0.000 0.000
0.0195 10.25E-51
1 1 0.0378 10.96E-51
II
0.000 I0.000
0.000 0.000
0.000 I0.000
18.736 2.362
0.259 10.000451
0.0280 10.52E-51
0.0439 10.13E-41
I i 0.0158 I0.16E-51
0.0864 10.50E-41
0.0439 10.13E-41
0.0893 10.53E-41
0.0773 10.40E-41
0.0378 10.96E-51
II
0.0312 10.65E-51
0.0312 10.65E-51
I
Calc. No. DREOO-OOOS AMENDMENT 13 Revision 0
Attachment B
PAGE 0 isHYDRAULIC CALCULATIONS - PIPE CHARACTERISTICS
I I PIPE DIAMETERI PIPE/FTG TOTAL
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH
INO. I NODES (US GPM)I (IN) (IN) I # (FT) (FT)
IHEAD LOSSIHEAD LOSS
I PER FT. JOVER PIPE
I (PSI) I (PSI)
STATIC TOTAL HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
IROUGHI WATER I VELOC.1
NESS IVELOCITYI PRESS.!
ICOEFFI(FT/SEC)I (PSI) i
I I I ____________ _____________ I _______ i __________ I _________ I
I I I I ___________ I ______ _______ I ________ I _______ I ________ ____ ______ _____ I 62 I �.0260 !0.45E.5
1757 1
1 I I I 1 1 1758 1
1 1 1 1
1760
1761
762 1
1 1 1763
1800
1802
1803
1804
1805
1806
807
1808
1809
706 704
923 706
27 720
720 721
919 723
724 719
928 802
802 803
834 800
800 801
56 805
49 849
849 814
849 815
77 808
1.03
1.03
L1.66
11.66
8.61
40.36
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
4.03 CSAM
4 8SE
4 4HE
4 IGV
4.03 CSAM
4 12SE
4 4HE
4 1GV
7.98 CSAM
8 ISE
8.39 CSAM
8 2HE
8.39 CSAM
8 1GV
7.85 CSAM
6.07 CSAM
6 ITT
6 1GV
6 2SE
4 .03 CSAM
4 2HE
4 ITT
4 4SE
4 IGV
6.07 CSAM
6 3SE
6 IHE
5.05 CSAM
5 7SE
5 4HE
7.98 CSAM
8 1HE
8 ITT
4.03 CSAM
4 3SE
4 2HE
4 1TT
4 IGV
4.03 CSAM
4 ISE
4 ITT
4 1GV
4.03 CSAM
4 4SE
4 IHE
4 IGV
2.47 CSAM
2 1/2 I iTT
2 1/2 I1GV
197.0
23.6
4.7
0.6
178.4
35.3
4.7
0.6
75.5
4.2
17.0
5.3
12.5
1.3
26.0
33.8
30.0
3.0
28.0
115.1
8.0
20.0
40.0
2.0
30.9
42.0
7.0
121.8
84.0
20.0
25.8
8.5
33.1
84.1
30.0
8.0
20.0
2.0
2.5
10.0
20.0
2.0
18.0
40.0
4.0
2.0
1.0
12.0
1.0
I ______ I _____ I ________ I _________ I _____ _____ I ______ I _____ I ______ I ___ I _____ I ____ I
LX-29
U2TB Hose St
225.9 10.00000261 0.0005921
219.0 10.00000261 0.000574 1
79.7 10.000010 0.000801
22.3 10.00000791 0.000176
13.8 i0.000004110.0000565 1
26.0 10.000049 0.00128
94.8 0.000 0.000
185.1 0.000 1 0.000
79.9 0.000 0.000
225.8 0.000 0.000
67.4 0.000 0.000
144.1 0.000 0.000
34.5 0.000 1 0.000
64.0 0.000 1 0.000
14.0 0.000 0.000
1.645 1.646
-7.058 -7.058
0.650 0.650
0.000 0.000176
0.000 10.0000565
0.000 0.00128
3.248 3.248
3.551 3.551
-7.794 -7.794
-4.027 -4.027
-11.562 -11.562
2.728 2.728
0.000 0.00(
1.169 1.16
-0.433 -0.43
62
62
56
56
59
86
120
120
120
; 120
120
120
0 120
9 120
3 120
0.0260 !0.45E-5
0.0260 ;0.45E-5:
0.0748 10.37E-41
0.0677 10.30E-4:
0.0500 10.16E-4;
1 I
0.268 10.000481
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 I0.000 I
0.000 0.000
0.000 1 0.000
0.000 0.000
0.000 0.000
0.000 0.000
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment B
U2T8 Hose St HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I PIPE DIANETERI PIPE/FTG I TOTAL HEAD LOSSIHEAD LOSS I STATIC I TOTAL IROUGHI WATER I
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH I PER FT. lOVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITYI
NO. I NODES (US GPM) I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI (FT/SEC)
I I I I I
VELOC.
PRESS.
(PSI)
I I I 1 ~ 1 - 1 1 -______________ I ________I_________ __________I_________
1810
1811I
1812
1813
1814 1
1815 1
1816
819
1820
1821
1822
1823
1824
1826
1_
I- - - - 20 I 0.000 I 0.000 I
I ______________I ____________ __________________I ____________________ I____________ ____________ I______________ _____________ I__________________________I
IX-30
60 809
79 811
55 813
813 817
813 818
805 819
819 820
819 822
76 824
824 825
801 804
836 827
835 836
I . 824 826 I
0.00
4 4
0.00
3
3
3
0.00
8 18
18
0.00
2 1/2
2 1/2
0.00
8
0.00
0.00
6
6
6
0.00
6
6 16
0.00
8
8
8
0.00
6
6 16
0.00
3
0.00
5
5
0.00
6
6
6
6
6
0.00
6
6 6
I
4.03 CS
2S
I11 3.07 CS
4I 14
2(
7.98 C
4•
41
2.47 C
I
-7.98 C Ii
7.98 C
1
6.07 C
79
6.07 I
7.98
6.07
3.07
5.05
6.07
6.07
20 1o.o00o 0,0001AM
SE
T
SAM
SE
TT
GV
SAM
SE
HE
TT
SAM
TT
GV
SAM
GV
ZSAM
2SE
SAM
iHE
ITT
IGV
CSAM
OSE
IHE
1GV
CSAM
2SE
1TT
IHE
CSAM
ISE
CHE
1GV
CSAM
4TT
CSAM
4HE
8SE
CSAM
1GV
5SE
3HE
4TT
lC`V
CSAM
ITT
1HE
IGV
28.1
20.0
20.0
51.5
28.0
15.0
2.0
62.7
68.2
34.1
33 .1i
1.0
12.0
1.0
1.5
3.8
6.0
17.0
6.6
7.0
30.0
3.0
16.8
14.0
7.0
3.0
32.0
34.1
33.1
8.5
23.3
14.0
7.0
3.0
5.5
15.0
121.5
20.0
96.0
63.5
3.0
70.0
21.0
120.0
32.0
6.3
30.0
7.0
3.0
68.1
96.5
198.1
14.0
5.3
23.0
46.6
40.8
107.7
47.3 3
20.5
237.5
309.5
46.3
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
-2.165
-3.681
-13.207
0.000
-1.169
2.901
-4.114
-4.114
-13.943
0.000
0.000
-7.483
-3.992
0.000
-2 .165 1:
-3.681
-13.207
0.000
-1.169
2.901
-4.114
-4.114
-13.943
0.000
0.000
-7.483
-3.992
0.000
20
20
20
.20
120 J
120
120
120
120
120
120
120
120
0.000 0
0.000 0
0.000 0
0.000 0
0.000 I
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
.000
.000
'.000I
.000I
3.000I
0.000
0 .ooo
O.ooo
0.000
0.000
0.000
0.000
0.000
0.00
AMENDMENT 13Calc No. L)KLUU-UUU3 Revision 0 Attachment B
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I PIPE DIAMETERI
IPIPEI PIPE I FLOW NOM ACTUALI COI
NO. I NODES I (US GPM)I (IN) (IN) I#
1I 1 ...-....-... _____________ ____________ __________________I_____________________ ___________ ___________
1827 1
1828 I
829 1
1831
1832 I
I 1
I I
833 1
1 1 1 I
1834
1835
1836
1837
1839
1840
1841
102 855
200 839
839 831
42 837
61 832
98 833
54 834
73 835
833 828
828 829
96 838
838 845
75 823
I
PIPE/FTG
DE LENGTH
(FT)
TOTAL HEAD LOSSJHEAD LOSS I STATIC TOTAL
LENGTH PER FT. lOVER PIPE HEAD LOSSIHEAD LOSS
(FT) I (PSI) I (PSI) (PSI) I (PSI)
IROUGHI WATER I VELOC.INESSGH WATELOITY PRESS.
ICOEFFI (FT/SEC) I (PSI) I
0 000 I0.00
42.17
42.17
0.00
0.00
0.00
0.00
0.00
0.00
0.00
12.22
0.00
0.00
0.823 0.823 I 120 I 0.000 I 0.000 I
6.07 CSAM
6 ITT
6 I1GV
6 1HE
6 ISE
6.07 CSAM
6 ITT
6.07 CSAM
10.02 CSAM
10 2HE
6.07 CSAM
6 ISE
6 IGV
6 1TT
6.07 CSAM
6 ISE
6 ITT
6 I1GV
6.07 CSAM
6 2SE
6 2HE
6 2TT
6 IGV
6.07 CSAM
6 ITT
6 2SE
6 2HE
6 IGV
6.07 CSAM
6 9SE
6 2TT
6.07 CSAM
6 8SE
6 2HE
6 ITT
6.07 CSAM
6 IHE
6 I1GV
6 ITT
4.03 CSAM
4 SHE
4 2SE
4 ITT
4 I1GV
7.98 CSAM
8 ITT
8 2SE
8 IHE
4.4
30.0
3.0
7.0
14.0
2.3
8.8
3.0
11.0
22.0
9.9
14.0
3.0
30.0
25.6
14.0
30.0
3.0
28.6
28.0
14.0o
60.0
3.0
24.5
30.0
28.0
14.0
3.0
75.9
126.0
60.0
100.0
112.0
14.0
30.0
62.4
2.1
0.9
8.8
117.8
20.0
20.0
20.0
2.0
32.0
33.1
34.1
8.5
58.4 0.000
11.1 0.000343
3.0 0.000343
33.0 I 0.000
56.9 0.000
72.6 0.000
133.6 0.000
99.5 0.000
261.9 0.000
256.0 0.000
74.2 10.000034
179.8 0.000
107.7 0.000
______ I _____ I ________ I _________ I _____ I _____ I ______ I _____ I ______ I ___ I ____ I ____ I
IX-31
U2TB Hose St
0.000
0.00382
0.00103
0.000
0.000
0.000
0.000
0 .000
0.000
0.000
0.00257
0.000
0.000
0.823
-3.464
0.000
0.000
0.0433
1.429
-8.531
-8 .314
-0.684
-28.112
0.000
37.024
-13.943
0.823 120
-3.460 62
0.00103 62
0.000 120
0.0433 120
1.429 120
-8.531 120
-8.314 120
-0.684 120
-28.112 120
0.00257 62
37.024 120
-13.943 120
I--
PAGE i:3,26
0.000 0.000
0.468 0.0014
0.460 0.0014
0.000 0.000
0.000 0.000
0.000 0.0(00
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.136 10.000121
1 1 1 1
. 0
0.000 0.000
0.000 I0.000
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment B
PAGE E3z-HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I PIPE DIAMETER! PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
IPIPEi PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. OVER PIPE
INO. I NODES (US GPM) (IN) (IN) # (FT) (FT) I (PSI) (PSI)
STATIC I TOTAL
HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
IROUGHI WATER I VELOC.I INESS IVELOCITYI PRESS.I
ICOEFFI(FT/SEC)i (PSI)
I I I t
I I I I _____________ I _______ I _______ I ________ I _______ ________ I ____ _______ I ______________________________
______________________________________________ o 000 I 0 000 120 0.000 0.000 I1842 1
I 1
1850 1
1 1 1 I
1851
1860
1861
1922
1925
1931
1932
809 810
93 850
89 851
97 860
860 861
19 919
23 923
928 28
29 929
0.00
0.00
0.00
13.73
0.00
8.61
40.36
2.08
2.08
3.07 CSAM
ISE
1GV
6.07 CSAM
1GV
2SE
ITT
4.03 CSAM
3SE
ITT
1GV
IHE 6.07 CSAM
IGV
IHE
4.03 CSAM
3HE
3SE
1TT
1GV
7.85 CSAM
7.98 CSAM
3SE
ITT
1GV
7.98 CSAM
7.98 CSAM
23.323. 3
7.0
1.0
12.5
3.0
28.0
30.0
12.9
30.0
20.0
2.0
4.0
51.5
0.9
2.1
119.8
12.0
30.0
20.0
2.0
29.2
21.2
15.1
9.8
1.1
98.2
2.5
31.3 0.000
73.5 0.000
68.9 0.000
54.4 10.000042
183.8 0.000
29.2 10.0000056
47.2 10.000083
1 1
98.2 I0.412E-6
2.5 I0.412E-6
0.0000.000
0.000
0.000
0.00234
0.000
0.000165
0.00392
10.0000404
,0.0000010
I I
1 - 1 1.......I- 1 -1_________ ____________I_________________ ____________________1 __ 1_ I1 _ _ _ _ _ I1 -_ _ _ _I_ _1 - 1_ _ _ __ _ I_
IX-32
U2TB Hose St
0.000 0.000
-2.598 -2.598
-2.382 -2.382
0.000 0.00234
38.020 38.020
0.476 0.476
12.774 12.778
0.000 10.0000404
0.000 I0.0000010
120
120
120
62
120
59
62
56
56
0.000 0.000
0.000 0.000
0.000 0.000
0.153 10.000151
1 1
0.000 0.000
0.0571 10.21E-41 0.259 10.000451
I I
I I 1 I
0.0133 0.11E-51
0.0133 10-11E-51
Caic. No. DREOO-OOOS AMENDMENT 13 Revision 0
Attachment B
HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS
COMPANY Nexus Technical Services Corporation IPAGE Z
DESIGNER BY BRIAN FOX CHECKED: IDATE 2000 JAN 6
CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT I Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
I JOB NO. IU2TB Hose Station F-B0
SPRINKLER/NOZZLE{N) POINTS REFERENCE POINTS INPUT POINTS POINT REQUIRED
ELEVATION DISCHARGE K-FACTORs
I NO. IDISCHG. GPM P.S.I. NO. IDISCHG. GPM I P.S.I. NO. IDEMAND GPM I P.S.I. (FT) I (US GPM)
1 149.937 500.000
2 145.823 509.500
3 143.009 516.000
4 145.260 510.800
5 145.260 510.800
6 145.260 510.800
7 145.475 510.300
8 145.777 509.600
9 145.777 509.600
i 0 143.221 515.500
I11 126.463 554.200
12 143.221 515.500
13 145.689 509.800
14 145.905 509.300
15 145.992 509.100
16 145.211 510.900
17 145.557 510.100
18 145.903 509.300
19 145.859 509.400
20 144.993 511.400
211 145.338 510.600 1 1
221 144.957 511.500 1
23 1 144.955 511.500
241 139.103 525.000
251 145.165 511.000
26 144.949 511.500
27 145.381 510.500
28 144.730 512.000
29 144.730 512.000
30 145.076 511.200
31 144.647 512.200
32 144.303 513.000
33 144.741 512.000
34 144.875 511.700
35 145.558 510.100
361 144.530 512.500
371 145.228 510.900
38 145.177 511.000
39 145.131 511.100
40 118.89 150.000 500.000
41 145.270 510.900
42 145.256 510.900
45 145.232 510.900
46 144.295 513.000
IX-33
AMENDMENT 13Caic. No. DRPUE-UUO0 Revision 0 Attachment B
U2TB Hose StHYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED I ELEVATION DISCHARGE K-FACTORI
NO. IDISCHG. GPM P.S. . NO. IDISCHG. GPM P.S.I. NO. IDErAND GPM I P.S.I. I (FT) (US GPM) I
47 144.295
48 137.138
49 134.539
50 134.106
51 133.110
52 144.875
53 125.661
54 125.661
55 125.660
56 125.660
57 125.660
58 126.263
59 126.260
60 126.245
61 126.208
62 122.771
63 119.748
64 138.651
65 141.047
66 141.047
67 138.651
68 127.091
69 138.651
70 128.044
I71 124.578
72 125.877
73 125.877
74 125.876
I 75 125.876
76 125.875
77 125.874
78 126.300
79 126.297
80 138.651
81 119.708
82 138.651
83 141.697
84 141.696
85 142.334
86 138.651
87 142.335
88 138.521
89 138.218
91 138.564
92 138.218
93 138.218
96 147.542
97 147.542
98 127.721
513.000
I I
______________ ______________I............ _____________ I______________I.........l______________ _____________ _____________II_______I___
IX-34
PAGE 0 2-
513.000 529.500
535.500
536.500
538.800
511.700
556.000
556.000
556.000
556.000
556.000
554.500
554.500
554.500
554.400
562.500
569.600
526.000
520.500
520.500
526.000
552.700
526.000
550.500
558.500
555.500
555.500
555.500
555.500
555.500
555.500
554.500
554.500
526.000
569.700
526.000
519.000
519.000
517.500
526.000
517.500
526.300
527.000
526.200
527.000
527.000
505.500
505.500
551.200
AMENDMENT 13Calc. No. DKLUU-0UUW Revision 0 Attachment B
U2TB Hose StPAGE BZ4-
HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED
ELEVATION DISCHARGE
INO. DISCHG- GPM P.S.I. NO. IDISCHG. GPM P.S.I. NO. IDEMAND GPM I P.S.I. I (FT) I (US GPM)
IK- FACTOR I
I I I I
102 138.651
200 134.556
201 125.658
202 134.550
400 147.542
401 106.188
402 109.522
403 147.542
404 106.188
405 109.523
600 121.114
601 139.103
602 137.674
611 135.855
612 135.855
1 621 138.107
651 1 118.89 91.921
700 145.992
701 145.428
702 145.341
7031 144.732 1 I
704 1 137.588 1
7051 145.037
7061 139.234
719 1 144.955
1 -7201 144.731
1 721 144.731
723 145.383
724 144.957
725 145.903
726 145.903
7271 1 145.903
800 141.986
801 146.013
802 141.482
803 137.931
804 146.013
8051 137.222
1 8081 126.307
1 809 128.410
810 128.410
811 129.978
812 133.110
813 138.868
I I814 131.811
I 815 130.642
I 817 138.868
I 818 140.037
I 819 134.321
-I26.000
526.000 535.500
556.000
535.500
505.500
601.000
593.300
505.500
601.000
593.300
566.500
525.000
528.300
532.500
532.500
527.300
566.500
509.100
510.400
510.600
512.000
528.500
511.300
524 .700
511.500
512.000
512.000
510.500
511.500
509.300
509.300
509.300
518.300
509.000
519.500
527.700
509.000
529.300
554.500
549.500
549.500
546.000
538.800
525.500
541.800
544.500
525.500
522.800
536.000
100.00 12.400
_____________________ ____________________ I ________ _____________________I ____________________ I................I _____________________I ____________________ I _____________________I _________________ I______________ I
IX-35
I
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment B
U2T8 Hose St HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS PAGE F
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS INPUT POINTS POINT REQUIRED
ELEVATION DISCHARGE K-FACTC=.
I NO. DISCHG. GPM I P.S.I. NO. IDISCHG. GPM I P.S.I. I NO. DEMAND GPM I P.S.I. I (FT) (US GPM)
820 138.435 526.500
822 138.435 526.500
823 139.819 523.300
824 139.819 523.300
825 139.819 523.300
826 139.819 523.300
827 145.666 509.800
828 126.976 552.920
829 155.088 488.000
831 138.016 527.500
832 126.165 554.500
833 126.292 554.500
834 134.192 536.300
835 134.191 536.300
836 138.183 527.080
I 837 145.256 510.900
838 147.540 505.500
839 138.017 527.500
845 110.516 591.000
849 131.811 541.800
850 140.816 521.000
851 140.599 521.500
855 137.828 527.900
860 1 147.539 505.500
861 1 109.520 593.300
919 1 145.383 510.500
923 132.176 541.000
928 144.730 512.000
929 144.730 512.000
IX-36
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment B
WARNING: THE FOLLOWING PIPE(S) HAVE FLOW(S) SMALLER THAN 0.1 GPM
2 3 4 85 86 87 91 106 500
501 502 503 504 505 600 611 612 621 800
802 803 804 805 806 807 808 809 810 811
812 813 814 815 816 819 820 821 822 823
824 826 827 831 832 833 834 835 836 837
840 841 842 850 851 861
MAXIMUM UNBALANCED HEAD LOSS= .00001 IN LOOP # I
IX-37
AMENDMENT 13
15X-
Calc. No. DREO0-000S Revision 0 Attachment B
[,•ý b2-7 -F P-/-7
'P
1131R
IE
is
Is
IU
761 R
IE
X is operating point for
Co-ordinates are
FLOW = 118.89
PRESSURE - 150.00
SPECIFIED pressure
0 1635 3268 4901
Pump Curve Input Point No.
FLOW
40
IX-38
391
AMENDMENT 13
CALCULATION NO. DREOO-0008 Revision No. 0
ATTACHMENT C
SPRINK-1000 OUTPUT FIRE HOSE STATION
DATA F-75
IX-39
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0
Attachment C
DESIGN PROGRAM FOR SPRINKLER SYSTEMS C cl
by
MUNICIPAL HYDRAULICS LTD, LADYSMITH, B.C. CANADA
COPYRIGHT (C) 1995 MUNICIPAL HYDRAULICS LTD
VERSION 11.00
COMPANY : Nexus Technical Services Corporation
DESIGNER BY: BRIAN FOX CHECKED:,f_;-L . -I&'' CLIENT : CornEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. : U2TB Hose Station F-75
FIX
C-62
P 01 01 02 3.5 11.938
P 02 02 03 16.1 11.938 1GV ITT 3SE CV
P 03 03 04 21.2 7.981 2SE
C-132
P 04 04 05 60.0 11.2 HE SE 3ZSE(7)
P 05 05 06 13.5 11.2 TT GV
C-66
P 06 06 07 156.6 7.85
P 07 07 08 161.0 7.85
P 14 08 13 86.0 7.981 ITT
C=55
P 15 13 14 54.6 7.981
P 750 700 701 72.8 7.981 4HE
P 16 14 15 14.1 11.2 GV
P 17 15 700 44.5 11.2 GV
P 751 701 16 29.3 11.2
C-86
P 18 16 35 9.1 11.2
P 19 35 702 82.7 11.2 HE
P 752 702 17 41.9 7.85
P 20 17 726 119.6 7.85 HE
P 21 725 19 97.9 7.85
P 725 18 725 6.8 11.2 GV
P 726 18 726 4.5 11.2 GV
P 727 18 727 2.1 11.2 GV
C-59
P 762 723 919 12.5 8.385 GV
P 922 919 19 29.2 7.85
C-66
P 22 20 723 82.2 8.385 TT SE ZSE(5)
P 23 20 21 133.3 8.385 TT 3HE GV
P 30 27 703 4.0 7.981 1GV
P 753 703 21 26.0 7.85 TT
C-86
P 29 21 26 147.0 7.981 ITT
P 28 26 25 146.0 7.981 2SE
C-62
P 27 25 601 81.9 7.981 6SE 1GV
P 601 601 24 10.8 7.981 ISE
P 754 602 704 58.7 7.981 4SE iHE lTT lGV
P 602 602 24 123.0 7.981 5SE 2HE GV
P 755 704 705 221.92 7.981 7SE 2HE ITT
C-86 [X-40
AMENDMENT 13 Cakc No. DREOO-OOOS Revision 0
P 756 705 727 141.27 7.981 2HE ITT
C=62
P 300 24 200 136-5 7.981 5SE 1GV ITT
P 26 200 923 7.5 7.981 ISE ITT 1GV
p 757 704 706 197.01 4.026 8SE 4HE GV
P 758 706 923 178.37 4.026 12SE 4HE GV
P 925 923 23 21.25 7.981 3SE ITT IGV
C=132
P 25 22 724 75.0 11.2 TT 4HE
C-62
P 719 719 23 5.86 7.981 2HE
C-86
P 763 724 719 26.0 7.85
C-132
P 24 05 22 149.9 11.2 GV TT
C-35
P 50 45 48 255.0 9.564 5SE 2GV IHE
***********************************
NOTE *
/* THE FOLLOWING PIPES HAD A*
/* CALCULATED C FACTOR OF 27.4. DUE*
/- TO LIMITATIONS OF THE SPRINK*
/* PROGRAM, A C OF 35 WAS USED*
/* (THE MINIMUM) AND PIPE LENGTHS*
/* ADJUSTED TO REFLECT EQUIVALENT*
/ FRICTION LOSS.*
/- ACTUAL LENGTHS ARE AS FOLLOWS:*
/-PIPE 41 - 10.8*
/-PIPE 42 - 9.8*
/-PIPE 45 = 22.3*
/-PIPE 46 = 10.0"
/-PIPE 49 = 2.0*
P/....... **..****
P 41 40 41 17.0 10.02
P 42 41 42 15.4 10.02 IHE 1GV 1CV ISE
P 45 42 45 35.1 10.02 ITT
P 46 37 38 15.1 7.981 IGV SE 2HE
P 49 45 37 3.5 7.981 ITT
C-132
P 47 38 39 230.0 11.2 3SE 2HE 4ZSE(7) 3ZSE(3)
P 48 39 22 59.3 11.2
C-62
P 55 48 67 115.92 10.02 7SE
P 70 67 69 3.25 10.02
P 69 69 80 2.17 10.02
P 68 80 64 5.33 10.02 1GV
P 67 64 63 86.75 7.981 9SE 2TT 1GV 2HE
P 66 63 62 36.93 6.065 4SE IGV ITT
P 65 62 61 70.08 6.065 3SE 2HE
P 64 61 60 130.25 6.065 3SE 4HE ITT
P 63 60 59 30.83 6. 065
P 62 59 58 6.75 6.065
P 302 58 201 80.0 6.065 1GV 4HE
P 303 201 202 482.5 10.02 2TT
P 305 57 201 89.0 6.065 ISE 1GV 2HE
P 60 56 57 1.0 7.981
P 59 55 56 15.08 7.981 4HE
P 58 54 55 107.58 7.981 2HE
P 57 53 54 15.5 7.981
Attachment C
p." 'c-- c_.z.
IX-41
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0
P 56 70 53 118.25 7.981 7SE IHE 1GV Attachment C
P 54 51 70 11.67 10.02
P 53 50 51 2.33 10.02
P 52 49 50 1.0 10.02
P 51 48 49 6.0 10.02 ITT
P 8 8 9 30.0 7.981 IGV
p 9 9 10 110.0 4.026 2SE IHE 2TT IGV
P 10 10 12 215.42 4.026 15SE 7HE 2GV ITT
P 11 10 11 77.5 4.026 5SE 2HE 1GV
P 12 11 12 80.25 4.026 8SE 4HE 1GV
P 13 12 15 34.75 4.026 4SE 1GV ITT
P 83 70 68 2.33 10.02 1GV
P 82 68 71 89.83 7.981 3SE
P 81 71 72 54.75 7.981 4SE IHE
P 80 72 73 15.58 7.981
P 79 73 74 103.58 7.981
P 78 74 75 1.75 7.981
P 77 75 76 14.50 7.981
P 76 76 77 21.50 6.065 2SE
P 75 77 78 175.67 6.065 4SE 2HE 1GV
P 74 78 79 65.83 6.065 2HE
P 73 79 98 122.0 6.065 2SE 2HE
P 72 98 81 32.25 6.065 3SE 2TT IHE
P 71 81 63 84.83 6.065 IGV
P 110 64 102 0.5 10.02
P 84 102 82 10.5 10.02
P 99 82 86 1.0 10.02 ITT
P 100 86 85 48.5 6.065 2SE 3HE IGV
P 102 97 84 14.33 7.981 2HE ITT
P 103 84 66 1.50 7.981
P 104 66 47 27.75 7.981 4SE 2GV SR
P 105 47 28 115.0 7.981 ISE 1GV ITT
C-56
P 31 28 721 125.0 7.981
P 761 721 720 17.0 8.385 2HE
P 760 720 27 75.5 7.981 ISE
C-62
P 90 82 88 1.00 10.02 ITT
P 93 88 87 66.0 6.065 4SE 3HE 1GV ITT
P 95 96 83 14.17 7.981 2HE ITT
P 96 83 65 1.50 7.981
P 97 65 46 31.25 7.981 5SE 2GV 1SR
P 98 46 29 112.0 7.981 ISE IGV ITT
C-56
P 932 29 929 2.5 7.981
P 32 929 928 184.0 8.425 2SE 5HE 2GV
P 931 928 28 98.2 7.981
P 33 30 29 20.0 7.981
C-41
P 40 37 36 160.0 7.981 1GV ITT 4SE 3HE
C-61
P 39 36 52 160.0 7.981
P 38 52 34 10.00 7.981
P 37 34 33 280.0 7.981 5SE iHE
C-55
P 36 33 32 300.0 7.981
C-71
P 35 32 31 285.0 7.981
C-61
P 34 31 30 285.0 7.981 IX-42
AMENDMENT 13
........................
NOTE*
/ THE FOLLOWING PIPES WERE
/ ADDED TO ATTACH SYSTEMS *
/ TO THE BASE MODEL * */********************************
C=120
P 611
P 612
P 621
P 834
R 834
P 803
R 800
P 804
R 801
P 822
R 804
P 805
R 805
P 815
R 819
P 816
R 820
P 819
R 822
P 809
R 808
P 106
R 812
P 806
P 808
P 807
R 849
R 814
R 815
P 810
R 809
P 842
R 810
P 81)
R 811
P 83:
R 83:
P 83'
R 821
P 83
R 82'
P 83
Calc. No. DREO0-0008 Revision 0 Attachment C
601 611 4.5 6.065 2SE ITT
611 612 1.0 6.065
602 621 3.6 6.065 3SE ITT
54 834 28.6 6.065 2SE 2HE 2TT IGV
536.3
834 800 30.9 6.065 3SE 1HE
518.3
800 801 121.75 5.047 7SE 4HE
509.0
801 804 5.5 3.068 ITT
509.0
56 805 25.75 7.981 1HE ITT
529.3
805 819 6.0 7.981 ISE
536.0
819 820 6.58 6.065 iHE ITT IGV
526.5
819 822 16.75 6.065 ISE 1HE 1GV
526.5
77 808 1.0 2.469 ITT IGV
554.5
51 812 1.0 7.981 ITT 1GV ISE
538.8
49 849 84.1 4.026 3SE 2HE ITT 1GV
849 815 18.0 4.026 4SE IHE IGV
849 814 2.5 4.026 lEE ITT 1GV
541.8
541.8
544.5
60 809 28.08 4.026 2SE ITT
549.5
809 810 23.33 3.068 ISE 1GV
549.5
79 811 51.5 3.068 4SE ITT 2GV
546.0
3 98 833 25.58 6.065 ISE ITT IGV
3 554.5
6 833 828 75.92 6.065 9SE 2TT
8 552.92
7 828 829 100 6.065 8SE 2HE ITT
9 488.0
2 61 832 9.9 6.065 ISE 1GV ITT
R 832 554.5
P 835 73 835
R 835 536.3
P 812 55 813
R 813 525.5
P 813 813 811
R 817 525.5
P 814 813 811
R 818 522.8
P 841 75 823
R 823 523.3
24.5 6.065 ITT 2SE 2HE 1GV
62.7 7.981 4SE 4HE ITT
7 1.0 2.469 ITT
8 1.5 7.981 IGV
32.0 7.981 ITT
IGV
2SE IHE
IX-43
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0 Attachment C
P 820 76 824 32.0 7.981 2SE ITT IHE
R 824 523.3
P 821 824 825 23.25 6.065 ISE 1HE 1GV
R 825 523.3
P 826 824 826 6.3 6.065 ITT 1HE 1GV
R 826 523.3
P 850 93 850 12.5 6.065 1GV 2SE iTT
R 850 521.0
P 87 92 93 152.1 4.026 2SE 6HE
P 86 91 92 16.0 6.065 2HE 1GV ITT
P 85 82 91 1.0 10.020 ITT
* 91 526.2
* 92 527.0
R 93 527.0
P 851 89 851 12.9 4.026 3SE ITT 1GV 1HE
R 851 521.5
P 91 88 89 166.9 4.026 GV 81HE
R 89 527.0
P 800 928 802 33.83 6.065 ITT IGV 2SE
R 802 519.5
P 802 802 803 115.08 4.026 2HE ITT 4SE IGV
R 803 527.7
P 840 838 845 117.8 4.026 5HE 2SE ITT iGV
R 845 591.0
C-62
P 839 96 838 62.4 6.065 1HE 1GV ITT
P 94 838 87 206.1 6.065 6SE 2HE ITT
P 860 97 860 51.5 6.065 iGV 1HE
P i01 860 85 168.5 6.065 7SE 3HE
C-120
R 838 505.5
P 861 860 861 119.75 4.026 3HE 3SE TT GV
R 860 505.5
R 861 593.3
P 827 102 855 4.39 6.065 ITT iGV 1HE ISE
P 831 42 837 11.0 10.02 2HE
P 824 835 836 63.5 6.065 iGV 5SE 3HE 4TT iCV
R 836 527.08
P 823 836 827 121.5 5.047 4HE 8SE
R 827 509.8
R 837 510.9
R 855 527.9
C-62
P 828 200 839 2.3 6.065 iTT
P 829 839 831 3.0 6.065
P 304 831 202 2.7 6.065
C-120
R 839 527.5
R 831 527.5 / **********.*.************
END *
*/.........**fl.**.***** * A.....
C-120
P 500 97 400 26.17 6.065 IHE
P 501 400 401 132.67 6.065 2SE 4HE ITT 1GV
P 502 401 402 52.17 4.026 3SE iTT 2GV
P 503 96 403 7.75 6.065 IHE
P 504 403 404 132.33 6.065 ITT 2SE 3HE iGV
P 505 404 405 47.0 4.026 ITT 3SE 2GV
/-....... .**.......* . * ........ * ....*
Attc C
IX-44
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0
/* The following nodes and pipes Attachment C
/ r refer to hose stations. o To
/" switch between hose stations, Cf.
/ change the S to an R and remove *
/, the flow and K-factor on the hose *
/* stations that you do not want *
/* to flow. *
/ HOSE STATION F-75
P 600 57 600 13.5 1.610 TT 2SE GV
S 600 566.5 100 12.4
/HOSE STATION F-80
P 651 61 651 49.1 1.610 TT 2SE GV
R 651 566.5 * A************* * *********
END *
R 02 509.5
R 03 516.0
R 04 510.8
R 05 510.8
R 06 510.8
R 07 510.3
R 08 509.6
R 09 509.6
R 10 515.5
R 11 554.2
R 12 515.5
R 13 509.8
R 14 509.3
R 15 509.1
R 16 510.9
R 17 510.1
R 18 509.3
R 19 509.4
R 20 511.4
R 21 510.6
R 22 511.5
R 23 511.5
R 24 525.0
R 25 511.0
R 26 511.5
R 27 510.5
R 28 512.0
R 29 512.0
R 30 511.2
R 31 512.2
R 32 513.0
R 33 512.0
R 34 511.7
R 35 510.1
R 36 512.5
R 37 510.9
R 38 511.0
R 39 511.1
R 41 510.9
R 42 510.9
R 45 510.9
R 46 513.0
R 47 513.0 IX-45
AMENDMENT 13
R 48 529.5
R 49 535.5
R 50 536.5
R 51 538.8
R 52 511.7
R 53 556.0
R 54 556.0
R 55 556.0
R 56 556.0
R 57 556.0
R 58 554.5
R 59 554.5
R 60 554.5
R 61 554.4
R 62 562.5
R 63 569.6
R 64 526.0
R 65 520.5
R 66 520.5
R 67 526.0
R 68 552.7
R 69 526.0
R 70 550.5
R 71 558.5
R 72 555.5
R 73 555.5
R 74 555.5
R 75 555.5
R 76 555.5
R 77 555.5
R 78 554.5
R 79 554.5
R 80 526.0
R 81 569.7
R 82 526.0
R 83 519.0
R 84 519.0
R 85 517.5
R 86 526.0
R 87 517.5
R 88 526.3
R 96 505.5
R 97 505.5
R 98 551.2
R 102 526.0
R 200 535.5
R 201 556.0
R 202 535.5
R 400 505.5
R 401 601.0
R 402 593.3
R 403 505.5
R 404 601.0
R 405 593.3
R 601 525.0
R 602 528.3
R 611 532.5
R 612 532.5
R 621 527.3
R 720 512.0
Calc. No. DREOO-OOOS Revision 0 Attachment C
phq-C-Il
IX-46
R 721 512.0
R 723 510.5
R 724 511.5
R 700 509.1
R 701 510.4
R 702 510.6
R 703 512.0
R 704 528.5
R 705 511.3
R 706 524.7
R 719 511.5
R 725 509.3
R 726 509.3
R 727 509.3
R 919 510.5
R 923 541.0
R 928 512.0
R 929 512.0
NOTE
/ TO DEACTIVATE PUMP UNIT 1:*
/* CHANGE:*
/* I 01 500.0 0.0 150 2000 150 2500 140 3750 91 3751 10'
/* TO:*
/* R 01 500.0
/t*t **************************** ****
R 01 500.0
.......... .....* .....................***............*****
/* NOTE *
/. TO DEACTIVATE PUMP UNIT 2/3:*
/* CHANGE:*
/* I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10*
/ TO:*
/ R 40 500.0
I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10
LENGTH DIAMETER FLOW HEAD ELEVATION PRESSURE
UNITS BEING USED: FEET INCHES US GPM FEET FEET PSI
HAZEN-WILLIAMS FORMULA USED
FITTINGS SPECIFIED AS NFPA
ITERATION STOPS WHEN GREATEST FLOW CHANGE IS .05000 IN ANY PIPE
MULTIPLICATIVE FACTOR OF EACH CONSUMPTION IS 1.00000
DEFAULT ROUGHNESS COEFFICIENT - C=120.0
THERE ARE 1 SPRINKLERS AND 0 BOOSTER PUMPS
THERE ARE 181 PIPES AND 169 REFERENCE POINTS
THE NUMBER OF INPUT POINTS IN SYSTEM IS 1
NODE NO. OF PUMPS PUMP INPUT PUMP PARAMETERS
NO. IN PARALLEL ELEVATION FRACTION OR X-Y COORDINATES
40 1 500.00 1.00 .0 2250.0 3000.0 3600.0 4900.0 4901.0
150.0 150.0 131.0 120.0 110.0 10.0
IX-47
-aic. NO. UJKLUU-VUUU)
AMENDMNT 13 Revision 0 AMENMEN 13 Attachment C
Attachme Co
AMENDMENT 13Caic. No. DKLUO-UUU• Revision 0 Attachment C
Initial estimate of demand on the system is 100.00
NET UNBALANCED DEMAND ON THE SYSTEM = .00000
LOOP PIPES
1 600 60 59 58 57 56 54 53 52 51
2 65 64 63 62 302 305 60 59 58 57
66
3 54 83 82 81 80 79 78 77 76 75
52 53
68 110 84 90 93 94 839 95 96 97
50 55 70 69
5 303 305 60 59 58 57 56 54 53 52
26 828 829 304
6 99 90 93 94 839 95 96 97 98 932
7 932 33 34 35 36 37 38 39 40 46
28 29 753 30 760 761 31 931 32
8 754 757 758 26 300 602
9 25 24 5 6 7 14 15 16 17 750
758 925 719 763
10 725 727 756 755 754 602 601 27 28 29
11 14 8 9 10 13 16 15
12 10 11 12
50 45 42 41
56 54 53 52 51 55 70 69 68 67
74 73 72 71 67 68 69 70 55 51
98 33 34 35 36 37 38 39 40 49
51 50 49 46 47 48 25 763 719 925
32 931 105 104 103 102 860 101 100
47 48 25 763 719 925 26 300 601 27
751 18 19 752 20 726 727 756 755 757
23 22 762 922 21
BANDWIDTH - 5
Iteration # 0 Max change in flow is
Iteration # 1 Max change in flow is
Iteration # 2 Max change in flow is
Iteration # 3 Max change in flow is
Iteration # 4 Max change in flow is
Iteration # 5 Max change in flow is
NUMBER OF ITERATIONS= 6
80.582 in loop # 27.711 in loop #
6.840 in loop #
2.551 in loop #
.600 in loop #
.040 in loop #
5 5
3
3
3
3
IX-48
AMENDMENT 13Caic. No. DREOO-000S Revision 0 Attachment C
SUMMARY REPORT
IPAGE •/o
COMPANY I Nexus Technical Services Corporation IDATE 2000 JAN
DESIGNER BY: BRIAN FOX CHECKED: " -iDL
200JA
CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. I U2TB Hose Station F-75
__ _ _I
MINIMUM FLOW OF ALL OPERATING SPRINKLER HEADS IS
AVERAGE FLOW FROM ALL OPERATING SPRINKLER HEADS IS
TOTAL FLOW FROM ALL OPERATING SPRINKLER HEADS IS
TOTAL DEMAND ON THE WHOLE SYSTEM IS
127.53
127.53
127.53
127.53
SPECIFIED AVAILABLE PRESSURE AT INPUT NODE IS 346.40 FEET OR 150.00 P.S.I.
IX-49
AMENDMENT 13Caic. No. DREOO-000O Revision 0 Attachment C
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
COMPANY Nexus Technical Services Corporation
DESIGNER BY: BRIAN FOX CHECKED: -- e
CLIENT ComEd. Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT UI DFP Out. 10% Degraded C-Factors. 10% Deg. U2/3 DFP
- Hose.I Staon mi F-75
DPATE c20 I) J
[DATE 2000 JAN 6 ;
JOBNV. I u
I I PIPE DIAMETERI PIPE/FTG I TOTAL IHEAD LOSSIHEAD LOSS I STATIC I TOTAL !ROUGHI WATER VELOC.1
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. OVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITY! PRESS.I
INO. I NODES (US GPM) (IN) (IN) # (FT) I (FT) I (PSI) I (PSI) (PSI) i (PSI) ICOEFF[ (FT/SEC)l (PSI)
_ _ _ _ _ _ _ ___ _ I_ _ _ _ I _ _ _ _ _ _ _ _ I___ __ _ _ _ ___I._ _
____________________ I __________________ 11.94 I CSAN
11
21
3
4
6
7
8
91
10
11I
12
13
14
i15
1 2
2 3
3 4
4 I
5 6
6 7 7 8
8 9
9 10
10 12
10 11I
11 12
12 15
8 13
13 14
1
1
I ....-.... _____-____________ _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I _____ I ____
IX-50
3.5 I0.00
0.00
0.00
0.00
14.47
14 .47
14.47
1.66
1.66
0.76
0.90
0.90
1.66
12.81
12.81
11.94 C 11.94 C
2 1
.2 I1
2 3
.2 1
7.98 C
8 2
11.20 C
12 I
12 I
12 3
11.20 I
12
12
7.85
7.85
7.98
8
4.03
4
4
4
4
4.03
4 l
4
4
4
4.03
4
4
4
4.03
4
4
4 4.03
4
4
4 7.98
8 7 I 7.98I
SAM
SAM GV
TT
SE
CV
SAM
SE
:SAM
HE
SE
3ZSE
'SAM
ITT
LGV
CSAM
CSAM
CSAM
IGV
CSAM
2SE
1HE
2TT
IGV
CSAM
5SE
7HE
2GV
1TT
CSAM
5SE
2HE
IGV
CSAM
8SE
4HE
1GV
CSAM
4SE
IGV
iTT
CSAM
1TT
CSAM
3.5 16.1
1.7
17.2
23.3 I 18.7
21.2
10.0
60.0
11.1
23 .0
21.0
13.5
51.2
5.1
156.6
161.0
30.0
1.1
110.0
5.9
1.2
11.8
0.6
215.4
44 .2
8.2
1.2
5.9
77.5
14.7
2.4
0.6
80.3
23.6
4.7
0.6
34.8
11.8
0.6
5.9
86.0
11.0
54.6
3.5 0.000 1 0.000 77.0 0.000 1 0.000
31.2 0.000 1 0.000
115.1 0.000 1 0.000
69.8 10.589E-6 0.0000411
156.6 10.0000121 0.00188
161.0 0.000012 1 0.00193
31.1 10.225E-6 10.0000070
129.4 10.00000631 0.000816
274.9 10.00000151 0.000411 1
95.2 10.00000201 0.000192 1
109.1 10.00000201 0.000220 1
53.0 10.00000631 0.000334 1
97.0 10.00000881 0.000857 1
54.6 10.000012 I 0.000676 I
4.114 4.114 2.815 2.815
-2.252 -2.252
0.000 0.000
0.000 10.0000411
-0.217 1 -0.215
-0.303 1 -0.301
0.000 10.0000070
2.555 1 2.556
0.000 1 0.000411
16.758 16.758
-16.758 -16.758
-2.771 -2.771
0.0866 0.0875
-0.217 -0.216
62
62
62
132
132
66
66
62
62
62
62
62
62
66
55
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.0471 10.15E-41
0.0959 I0.61E-4'
0.0959 0.61E-4
0.0106 10.76E-6
0.0418 10.11E-4
0.0192 I0.24E-5
0.0226 10.34E-5
0.0226 10.34E-5
0.0418 10.11E-4
0.0822 10.45E-4
I 10.0822 10.45E-4
AMENDMENT 13t-aIC. No. UKtUU-UUUV Revision 0 Attachment C
HYDRAULIC CALCULATIONS " - PIPE CHARACTERISTICS
I I IPIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS I STATIC I TOTAL IROUGHI WATER I VELOC.I
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH I PER FT. JOVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITYL PRESS.I
INO. NODES (US GPM)l (IN) (IN) I# (FT) (FT) I (PSI) (PSI) (PSI) I (PSI) ICOEFFI (FT/SEC) I (PSI)
0 .086 I5' 0.47I.IE1
112 I CS 14.-11
16
17
18
19
20
21
22
23
24
25
26
27
21
2
3
3
3
3
3
3:
3.
91
0
1
2
.3
14
15
16
37
38
14 15
15 700
16 35
35 702
17 726
725 19
723 20
20 21
22 5
22 724
923 200
601 25
25 26
26 21
703 27
721 28
929 928
30 29
31 30
32 31 I 33 32 1
34 33 I
52 34
12.81
14.47
14.4-7 '
14.47
14.47
14 .47I
8.93
8.93
8.93
14 .47
44.25
43.24
0.82
0.82
0.82
9.75
9.75
3.33
15.03
15.03
15.03
15.03
15.03
15.03
2
2
2
8
1
1
1
] I.I 11.20 CS$
IG'
11.20 CSI
IG
11.20 CS,
11.20 CS
IH
7.85 CS
IH
7.85 CS
8.39 CS
I 1S 12
8 I 1 8.39 CS
8 i
8 31
8 11
11.20 C
2 1(
2 i1'
11.20 C
2 1
12 4
7.98 C
8 1
8 i
8 I
7.98 C
8 E
8
7.98
8 .9a
7.98
8I
7.98
8
7.98 8.43
8 79
7.98
7.98
7.98
7.98
-7.98
8
7.98
%M v
AM
V
AM
AM
E
AM
{E
AM
lAM
3V
SE
ZSE
SAM
rT
HE
GV
SAM
GV
TT
SAM
TT
HE
SAM
1SE
iTT
IGV
CSAM
CSE
IGV
CSAM
2SE
CSAM
ITT
CSAM
CGV
CSAM
CSAM
2SE
5HE
2GV
CSAM
CSAM
CSAM
CSAM
CSAM
5SE
1HE
CSA.M
_ -_-__ _ I _I__
(1T7T Nose SL.
14 .1 1.0
44 .5
1.0
9.1
82.7
5.0
119.6 6
4.2 2
97 .9
82 .2
13.9
7.2
5.0
133.3
13.9
10.7
1.6 6
149.9 9
5.1 1
51.2
75.0
51.2
44.3
7.5
5.0
9.8
1.1i
81.9
30.1
1.1
146.0
18.4
147.0
17.9
4.0
1.3
125.0
184 .0
10.8
13.5
2.4
20.0
285.0
285.0
300.0
280.0
24.3
2.4
10.0
125.0 10.00000721
210.7 10.757E-6
20.0 10.000016
285.0 10.000013
285.0 10.000010
300.0 0.000016
306.8 10.000013
I 1 10.0 0o.o0oo13I
0.000903
0.000160
0.000322
0.00391
0.00295
0.00499
0.00421
0.000137
_I0.0866 1 5!
I -
IX-51
I
PAGE c- i 2,
15.1 10.000002310.0000359 1
I I 1
45.5 10.00000291 0.000136
I I
9.1 i0.000001310.0000118
87.7 0o.0000013I 0.0001141
I 123.8 10.00000731 0.000910
I 97.9 10.00000301 0.000294
108.3 10.00000351 0.000386
1 1
159.6 10.00000351 0.000568 I
206.2 10.589E-6 I 0.000121
170.5 10.00000461 0.000795
1 1
23.4 10.0000941 0.00221
113.1 I0.614E-7 0.0000069
1 1
1 I
164.4 1O.335E-7 10.0000055
1 1 164.9 IO.335E-7 100005
1 1 5.3 10.000005310.0000
2 80
0.0B66
0.000
-0.346
0.217
-0.346
0.0433
0.390
-0.346
-0.303
0.000
-2.382
-6.062
0.217
-0.390
-0.650
0.000
0.000
0.346
-0.433
-0.346
0.433
0.130
0.000
____________________ I __________________ I ____________________ � ________________ I ______________
0.000136 5
-0.346 8
0.217 8
-0.346 8
0.0436 8
0.390 6
-0.346
-0.303 I:
0.000795
-2.379
-6.062
0 0.217
-0.390
-0.650
0.000903
0.000160
0.347
-0.429
-0.343
0.438
0.134
0.000137
-i 5 0.0
5 0.0
6 0.
6 0.
6 0.
16 0. 56 0.
66 0.
32 0.
32
62
62 10.
86 10.
86 10.
66 1 0
56 1
56 1
56
61
71
55
61
61
417 10.11E-41
3471 .15E-4
0471 10.15E-41
0471 10.15E-41
Ii 0959 10.61E-41
0592 10.23E-41
0519 10.18E-41
II
0519 10.18E-41
0471 10.15E-41
0.144 10.000141
0.277 0.00051
00528 0.18E-6'
00528 IO.18E-61
00528 I0.18E-6;
1 I
0.0626 10.26E-41
0.0626 10.26E-41
0.0191 10.24E-5 1
0.0964 10.62E-4'
0.0964 I0.62E-4!
0.0964 10.62E-41
0.0964 0.62E-4!
0.0964 10.62E-4'
0.0964 10.62E-41
AMENDMENT 13taic. tNO. UKrLUU-UUU Revision 0 Attachment C
HYDRAULIC CALCULATIONS -. PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS I STATIC TOTAL IROUGHI WATER I VELOC.I
IPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH I LENGTH I PER FT. lOVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITYI PRESS.I
lNO. I NODES I (US GPM) (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI(FT/SEC)i (PSI) I ,1__________ I I
[ _ _ _ _I _ _
_______________________ ____________________ I _____________________________ 7.98 I CS.h�M 160.0
39
40
41
42
45
46
47
48
4.
5(
5
5
5
5
5
5
-0.346 I
I_ II
U2TB Hose St
9
0
II
2
3
4
s5
56
57
58
59
60
62
63
_-I.
AM 160.0
IX-52
36 52
37 36
40 41
41 42
42 45
37 38
38 39
39 22
45 37
45 48
48 49
49 50
50 51
51 70
67 48
70 53
53 54 54 55
55 56 I
56 57
59 58
60 59
15.03
15.03
127.53
127.53
127.53
58.72
58.72
58.72
73.74
53.78
66.19
66.19
66.19
66.19
12.41
69.01
69.01
69.01
69.01
69.01
9.55
9.55
7.98 CS.
7.98 CS
8 IG 8 IT
8 4S
8 I3H 10.02 CS
10.02 CS
10 IH
10 1i
10 1I
10 is
10.02 Cc
10 1
7.98 C,
8 i
8 1
8 21
11.20 C
12 3
12 2
12 4
12 3
11.20 C
7.98 C
8 I
9.56 C
10 I 10
10
10.02
10
10.02
10.02
10.02
10.02
10
7.98
8
8
8
7.98
7.98
8 79
7.98
8
7.98
6.07
6.07
PAGE ý 1.3
AM V
T
E
AM
A•M CE
V
SE
TT
SAM GV
SE
HE SAM
$ E
H E ZSE
ZSE
SAM
SAM
TT
SAM
5SE
2GV
1HE
CSAM
ITT
CSAM
CSAM
CSAM
CSAM
7SE
CSAM
7SE
1HE
IGV
CSAM
CSAM
2HE
CSAM
4HE
CSAM
CSAM
CSAM
160.0 0.5
4.5
9.3
3.5
17.0
15.4
1.1
0.5
5.6
2.2
35.1
5.1
15.1
0.4
1.7
1.7
230.0
69.1
22.2
28.0
9.0
59.3
3.5
3.4
255.0
9.0
0.8
0.9
6.0
14.7
1.0
2.3
11.7
115.9
45.3
118.3
35.1
2.5
1.1
15.5
107.6
5.0
15.1
10.0
1.0
6.8
30.8
II
160.0 10.000013 0.00220 177.9 10.000028 0.00510
17.0 10.000665 1 0.0113
24.9 10.000665 1 0.0166
II I I
40.2 10.000665 1 0.0268 1
19.0 10.000479 1 0.00909 1
1 1 I I
358.2 10.00000781 0.00282
I 1 1 1
59.3 10.00000781 0.000467
6.9 10.000731 0.00503
265.7 0.000169 0.0448
20.7 10.0000681 0.00142
1 I 1.0 10.000068 10.0000685
2.3 10.000068 0.000160
11.7 10.000068 0.000800
161.3 10.00000301 0.000498
1 1 157.0 10.000224 0.0352
15.5 10.000224 0.00347
112.6 10.000224 1 0.0252
25.1 10.000224 0.00563
1 1 1.0 10.000224 0.000224
6.8 10.000021 0.000148
30.8 0.000021 0.000676
-0.346 0.693
4.720
0.000
0.000
0.0433
0.0433
0.173
0.000
8.054
2.598
0.433
0.996
5.066
1.516
2.382
0.000
0.000
0.000
0.000
0.000
0.000
-0.344 61 10.0964 10 0.698 41 1 0.0964 0
4.731 1 35 0.519 Ic
0.0166 1 35 1 0.519 1
0.0268 1 35 1 0.519
0.0524 1 35 0.377
0.0461 132 0.191 1
0.174 132 0.191
0.00503 35 0.473
8.099 35 0.240
II
2.600 1 62 1 0.269
0.433 62 0.269
0.996 62 0.269
5.067 62 0.269
1.516 62 0.0505
2.417 62 0.443
0.00347 62 0.443
0.0252 62 0.443
0.00563 62 0.443
0.000224 62 0.443
0.000148 62 0.106
0.000676 62 0.106
.62E-41 ).62E-41
0.0018
0.0018
0.0018
0.000951
0.000241
0.000241
0.0015
10.000381
I 1 I
10.000481
10.000481
10.000481
0.00048 I 10.17E-4i
S0 1
10.0013
10.0013 10.0013 10.0013I I
10.0013
10.75E-4
10.75E-4
I
AMENDMENT 13Calc. No. DREOO-000U Revision 0 Attachment C
PAGE :14,HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE
INO. NODES I (US GPM)l (IN) (IN) I # (FT) (FT) I (PSI) I (PSI)
I 1 1 __ 1_1 I _ _ _ __ _ __ _ _ _ __ _ _I__ _ _ _ _ _ _
64
65
66 6
67
68
69
70
71
72
73
74
75
76
77
78
79
80
81
82
83
84
61 60
62 61
63 62
64 63
64 80
80 69
69 67
63 81
81 98
98 79
79 78
78 77
77 76
76 75
75 74
74 73
73 72
72 71
71 68
68 70
82 102
130.3 I9.55
9.55
9.55
12.37
12.41
12.41
12.41
2.82
2.82
2.82
2 .82
2.82
2.82
2.82
2.82
2.82
2.82
2.82
2.82
2.82
24 .78
6.07 CSAM
6 3SE
6 4HE
6 ITT
6.07 CSAM
6 3SE
6 2HE
6.07 CSAM
6 4SE
6 I1GV
6 ITT
7.98 CSAM
8 9SE
8 2TT
8 I1GV
8 2HE
10.02 CSAI
10 1GV
10.02 CSM
10.02 CSAf
6.07 CSAJ
6 1GV
6.07 CSAJ
6 3SE
6 2TT
6 iHE
6.07 CSA.
6 2SE
6 2HE
6.07 CSA
6 2HE
6.07 CSA
6 4SE
6 2HE
6 I1GV
6.07 CS•
6 2SE
7.98 CS•
7.98 CS•
7.98 CS•
7.98 CS
7.98 CS
8 4S
8 1HE
7.98 CSJ
8 3Si
10.02 CS;
10 IG
10.02 CS
STATIC TOTAL IROUGHI WATER I VELOC.ISTATIC TOTAL
HEAD LOSSIHEAD LOSS
(PSI) (PSI)INESS IVELOCITYI PRISS.
ICOE-FFI (FT/SEC) I (PSI) I
I ______ I ______ ___ I _____ I ____ I 0.0433 0 0468 62 I 0.106 I0.75E.41
4
M
am
M
M
E
AM
AM
v
AM
130.3 12 .4
8.2
8.8
70.1
12.4
4.1
36.9
16.5
0.9
8.8
86.8
45.2
19.5
1.1
5.0
5.3
1.5
2.2
3.3
84.8
0.9
32.3 3
12.4
17.7
2.1
122.0
8.2
4.1
65.8
4.1
175.7
16.5
4.1
0.9
21.5
8.2
14 .5
1.8
103.6
15.6
54.8
20.1
2.5
89.8
15.1
2.3
1.5
10.5
______ I _____ I _______ I _________ I _____ I _____ I ______ _____ I ______ I ___ I ____ I ____ I
IX-53
U2TB Hose St
159.7 10.000021 1 0.00350
86.6 10.000021 0.00190
63.1 10.000021 0.00138
157.6 10.00000921 0.00146
6.8 10.000003010.0000210
2.2 10.000003010.0000067
3.3 10.000003010-0000100
85.7 10.00000221 0.000196
64.3 10.0000022! 0.000147
134.4 10.00000221 0.0003071
70.0 10.00000221 0.0001601
197.2 10.00000221 0.000450 1
29.7 10.000002210.0000679 1
14.5 10.6O0E-6 10.00000871
1.8 10.600E-6 I0.00000 1 0
103.6 10.600E-6 10.0000621
15.6 10.600E-6 10.0000093
77.3 0.600E-6 10.0000464
104.9 10.600E-6 10.00006291
3.8 10.198E-6 10.000000751
10.5 10.000011 0.000117 1
0.0433 0.0468
-3.507 -3.506
-3.074 -3.073
18.880 18.881
0.000 10.0000210
0.000 10.0000067
0.000 10.0000100
0.0433 0.0435
-8.011 -8.011
1.429 1.429
0.000 0.000160
0.433 0.433
0.000 10.0000679
0.000 10.0000087
0.000 10.0000010
0.000 10.0000621
0.000 10.0000093
1.299 1 1.299
-2.512 -2.511
-0.953 -0.953
0.000 0.000117
I
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
I~O Io I•a
0.106 10.75E-41 1 I
1 1
0.106 10.75E-41
0.0793 0.42E-41
II II
0.0505 10.17E-41
0.0505 I0.17E-41
0.0505 10.17E-41
0.0313 10.65E-51
0.0313 10.65E-51 II
0.0313 10.65E-51
II I
0.0313 10.65E-51
0.0313 10.65E-51
II
0.0181 10.225E-51
10.0181 10.22E-51 0.0181 10.22E-51
0.0181 10.22E-51
1 0.0181 10.22E-5I
II I
0.0181 10.225-5I
0.0115 10.88E-61
II I 0.101 0.68E-41
II I
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment C
PAGE <zi.-HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I
IPIPEi PIPE
PIPE DIAMETERI
FLOW NOM ACTUALI
(US GPM)l (IN) (IN) I
PIPE/FTG
CODE LENGTH
# (FT)
TOTAL
LENGTH
(FT)
HEAD LOSSIHEAD LOSS
PER FT. lOVER PIPE
I (PSI) I (PSI)
STATIC I TOTAL
HEAD LOSS HEAD LOSS
I (PSI) I (PSI)
IROUGHI WATER VELOC.IROUGHI WATER I NESS IVELOCITYI
ICOEFFI(FT/SEC)
- I NODES ____ _____I___I __ ___ __ ______ I ___ I _____ I ____ I
85
86
87
90
91
93
94
95
96
97
98
99
1100
101
102
1103
82 91
91 92
92 93
88 82
88 89
87 88
838 87
83 96
65 83
46 65
29 46
86 82
85 86
860 85
84 97
66 84
____ ________ I _________ I _____ I _____ I ______ I _____ I ______ I ___ I _____ I ____ I
IX-54
U2TB Hose St
VELOC. PRESS.
(PSI)
1--
0.00
0.00
0.00
11.70
0.00
11.70
11.70
11.70
11.70
11.70
11.70
13.08
13.08
13.08
13.08
13.08
10.02 C
10 1
6.07 C
6 2
6 1
6 I 4.03 C
4 2
4 E 10.02 C
10 1
4.03 C
4
4
6.07
6
6
6
6
6.07
6
6
6
7.98
8
8
7.98
7.98
8
8
B
7.98
8
8
8
10.02
10
6.07
6
6
6
6.07
6
6
7.98
8
8
7.98
"SAM "TT SAM
HE
GV
TT
:SAM
SE
HE
:SAM
.TT
CSAM
IGV
HE
CSAM
4SE
3HE
IGV
ITT
CSAM
6SE
2HE
ITT
CSAM
2HE
ITT
CSAM
CSAM
5SE
2GV
ISR
CSAM
ISE
IGV
ITT
CSAM
ITT
CSAM
2SE
3HE
IGV
CSAM
7SE
3HE
CSAM
2HE
ITT
CSAM
1.0
50.0
16.0
14.0
3.0
30.0
152.1
20.0
24.0
1.0
14.7
166.9
2.0
32.0
66.0
16.5
6.2
0.9
8.8
206.1
24.7
4.1
8.8
14.2
5.0
9.8
1.5
31.3
25.1
2.2
19.5
112.0
5.0
1.1
9.8
1.0
14.7
48.5
8.2
6.2
0.9
168.5
28.9
6.2
14.3
5.0
9.8
1.5
51.0 0.000 0.000
63.0 0.000 0.000
196.1 0.000 0.000
15.7 10.000002710.0000435
1 1 200.9 1 0.000 1 0.000
98.4 10.000031 0.00314
243.8 10.000031 0.00778
28.9 10.00000831 0.000243
1 1
1.5 10.000008310.0000126
78.1 10.00000831 0.000655
1 1 1 1
127.9 10.00000831 0.00107
15.7 10.000003410.0000535
1 1 63.8 0.000039 1 0.00250
1 1 1 1 1 1
203.5 10.000039 0.00799
1 1 1 1
29.1 10.000010 0.000300
1.5 10.000010 10.0000155
0.0866 0.0866
0.346 0.346
0.000 0.000
-0.130 -0.130
0.303 0.303
3.811 3.814
5.196 5.204
-5.846 -5.846
-0.650 -0.650
3.248 3.248
0.433 0.434
0.000 10.0000535
3.681 3.683
5.196 5.204
-5.846 -5.846
-0.650 -0.650
120
120
120
62
120
62
62
62
62
62
62
62
62
62
62
62
0.000 0.000
0.000 0.000
0.000 0.000
0.0476 I0.15E-41
0.000 0.000
0.130 10 000111
0.130 10.000111
0.0750 0.37E-41
0.0750 10.37E-41
0.0750 I0.37E-41
0.0750 10.37E-4!
II
0.0532 I0.19E-41
1 1 0.145 10.000141
II II
0.145 0.000141
0.0839 10.47E-41
3 1I II
0.0839 I0.47E-41
I I I i
AMENDMENT 13Calc. No. DRE00-000S Revision 0 Attachment C
PAGE n /4HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
PIPEJ PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. lOVER PIPE
NO. I NODES (US GPM)I (IN) (IN) I # (FT) (FT) I (PSI) I (PSI)
__ I ______ I ______ I ________ I _________ I _____ SAN
1104
105
1106
1110
300 I 1 1 1 1
302
I 303
1304
1305
I500
1501
1502
1503
1504
1505
STATIC I TOTAL
HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
ROUGH) WATER VELOC.)
INESS IVELOCITYI PRESS.I
ICOEFFI(FT/SEC)I (PSI) I
I ______ I ______ I ___ I _____ I ____ I 3.248 I 3.248 62 I 0.0839 I0.47E 41
47 66 I
28 47
51 812
102 64 2
24 200
58 201
202 201
831 202
201 57
97 400
400 401
401 402
96 403
403 404
404 405
8
8
8
3.08
3.08
0.00
4.78
5.73
9.55
48.96
48.96
58.52
0.00
0.00
0.00
0.00
0.00
0.00
8
8
8
8
8
8
8
8
8
6
6
10
6
6
6
6
6
6
6
6
4
4
4
6
6
6
6
6
4
4
4
I I ______ I _____ I ________ I _________ I _____ I _____ I ______ I _____ ______ ___ I _____ I ____ I
IX-55
U2TB Hose St
7.98 C
4
2
1
7.98 C
100
Ii
7.98 (
6.07
10.02
6.07
6.07
6.07
6.07
4.03
6.07
6.07
4.03
SAM SE
GV
SR
SSAM
SE
GV
TT
SAM
.TT
.GV
SSE
CSAM
CSAM
5SE
LGV
ITT
CSAM
IGV
4HE
CSAM
2TT
CSAM
CSAM
ISE
1GV
2HE
CSAM
IHE
CSAM
2SE
4HE
ITT
IGV
CSAM
3SE
ITT
2GV
CSAM
IHE
CSAM
ITT
2SE
3HE
1GV
CSAM
ITT
3SE
2GV
27.8 8
20.1
2.2
19.5
115.0
5.0
1.i1
9.8
1.0
33.1
3.8
17.0 0
0.5
136.5
25.1
1.1
9.8
80.0
0.9
8.2
482.5
29.4
2.7
89.0
4.1
0.9
4.1
26.2
7.0
132.7
28.0
28.0
30.0
3.0
52.2
30.0
20.0
4.0
7.8
7.0
132.3
30.0
28.0
21.0
3.0
47.0
20.0
30.0
4.0
69.6 10.00
130.9 0.00
55.0 0
0.5 10.00
172.5 10.00
89.1 I0.00
511.9 10.0
2 .7 0.0
98.1 10.0
33.2 1
221.7
106.2
14.8
214.3
101.0
0010 0.000717
0010 0.00135
.000 0.000
00011 10.0000055
0000221 0.000385 1
00021 0.00195
00039 0.0201
00452 0.00122
00629 0.0617
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
3 .248 3 .248
0.433 0.434
0.000 0.000
0.000 10.0000055
4.547 1 4.547
0.650 1 0.651
8.877 8.897
3 .464 3.465
0.000 0.0617
0.000 0.000
41.354 41.354
-3.334 -3.334
0.000 0.00(
41.354 41.35'
-3.334 -3.33.
I
I-1-
0
4
4
62
62
120
62
62
62
62
62
62
120
120
120
120
120
120
0.0839 0.47E-41
0.0839 10.47E-41
0.000 0.000
0.101 10.68E-41
0.0367 10.90E-51
I I
0.106 10.75E-41 II II
0.199 0.000261
0.544 0.0019
0.650 10.0028
0 0
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
AMENDMENT 13Calc. No. UKLUU-UUUW Revision 0 Attachment C
PAGE c i 7HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
JPIPEI PIPE FLOW I NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE
NO. I NODES I (US GPM) I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)
1I _ _I_ _- 1I _ __ __ _ _
1600 1
1 1 1 1 1 1
601
602
1611
612
621 1
1651
1719
1725
1726
1727
1750
1751
1752
1753
1754
1755
1756
r
STATIC TOTAL HEAD LOSSIHEAD LOSS
I (PSI) i (PSI)
IROUGHI WATER I VELOC. IIROUGHI WATER I NESS IVELOCITYI
ICOEFFI(FT/SEC)l
VELOC. PRESS.
(PSI)
II I I i
- I ______________ I ________________ I __________________ I ________________ I __________________ I _________ 4.547 19.810 120 2
157 600
24 601
602 24
601 611
611 612
602 621
61 651
719 23
18 725
726 18
18 727
700 701
701 16
702 17
21 703
704 602
705 704
727 705
27.53
1
0.82
6.55
0.00
0.00
0.00
0.00
1
44.25
8.93
14.47
5.54
14.47
14.47
14.47
9.75
6.55
5.54
5.54
1 1 _ _ I__ _ _ I _ __ __ _ _ I~...
1.61 CSAM
1/2 ITT
1/2 2SE
1/2 1GV
7.98 CSAM
8 ISE
7.98 CSAM
8 5SE
8 2HE
8 1GV
6.07 CSAM
6 2SE
6 ITT
6.07 CSAM
6.07 CSAM
6 3SE
6 ITT
1.61 CSAM
1/2 ITT
1/2 2SE
1/2 IGV
7.98 CSAM
8 2HE
11.20 CSAM
12 1GV
11.20 CSAM
12 1GV
11.20 CSAM
12 IGV
7.98 CSAM
84HE
11.20 CSAM
7.85 CSAM
7.85 CSAM
ITT
7.98 CSAM
8 4SE
8 IHE
8 ITT
8 1GV
7.98 CSAM
8 7SE
8 2HE
8 iTT
7.98 CSAM
8 2HE
8 ITT
IX-56
U2TB Hose St
13.5
8.0
8.0
1.0
10.8
5.0
123.0
25.1
5.0
1.1
4.5
28.0
30.0
1.0
3.6
42.0o
30.0
49.1
8.0
8.0
1.0
5.9
5.0
6.8
2.3
4.5
2.3
2.1
2.3
72.8
8.0
29.3
41.9
26.0
10.1
58.7
20.1
2.5
9.8
1.1
221.9
35.1
5.0
9.8
141.3
9.2
17.9
30.5 0.500 15.263
15.8 10.614E-7 10.000000971
154.2 10.00000281 0.000442 1
62,5 1 0.000 0.000
1.0 0.000 0.000
75.6 0.000 0.000
66.1 0.000 1 0.000
10.9 10.000098 0.00107
9.1 10.532E-6 10-0000048
6.8 10.000001310.0000088
4.4 0.220E-6 0000000971
80.8 10.000015 0.00125
29.3 10.000002910.0000873
41.9 10.00000731 0.000308
36.1 10.00000571 0.000209
92.1 10.00000281 0.000264
271.8 10.00000211 0.000571
168.3 10.00000111 0.000193
4.547 19.810
0.000 10.000000971
-1.429 -1.429
3.248 3.248
0.000 0.000
-0.433 -0.433
5.240 5.240
0.000 0.00107
0.000 10.0000048
0.000 10.0000088
0.000 10.00000097
0.563 1 0.564
0.217 I 0.217
-0.217 -0.216
0.606 0.606
-0.0866 -0.0863
7.448 7.449
0.866 0.866
120 2
62 0.
62 10
120
120
120
120
62
86
86
86
55
55
86
66
62
62
86
____________________ I ________________ I __________________ I ____________________ I __________________ I ____________________ 1...................I ________________ I ______________ I
0.097 2.718
00528 10.18E-61
.0420 J0.11E-41
0.000 0.000
0.000 0.000 0.000 0.000
0.000 0.000
0.284 0.00054'
0.0291 10.56E-51
0.0471 10.15E-4,
0.0180 10.21E-51
0.0928 10.58E-4
0.0471 I0.15E-4'
0.0959 10.61E-4i
0.0647 I0.28E-4
0.0420 10.11E-41
0.0355 0.85E-5
0.0355 10.85E-51
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment C
PAGE C./ /HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
IIPIPE DIAMETERI PIPE/FTG TOTAL JHEAD LOSSIHEAD LOSS
PIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH I PER FT. JOVER PIPE
NO. I NODES (US GPM) (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)
STATIC TOTAL IROUGHI WATER VELOC.IISTATIC ITOTAL HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)NESS IVELOCITYI PRESS.I
lCOEFFI (FT/SEC) I (PSI) I
! - 1 -__________ 1 -- 1__________ _______________I________________
175
175
17
76 18
16
76
18
18
18
17
18
18
7 706 704
8 923 706
0 27 720
1 720 721
62 919 723
63 724 719
00 928 802
02 802 803
03 834 800
04 800 801
05 56 805
806 49 849
807 849 814
808 849 815
809 77 808
1.01
1.01
9.75
9.75
8.93
44.25
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
0.00
4.03 CSAM
4 8SE
4 4HE
4 1GV
4.03 CSAM
4 12SE
4 4HE
4 IGV
7.98 CSAM
8 iSE
8.39 CSAM
8 2HE
8.39 CSAM
8 IGV
7.85 CSAM
6.07 CSAM
6 ITT
6 1GV
6 2SE
4 .03 CSAM
4 2HE
4 ITT
4 4SE
4 IGV 6.07 CSAtM
6 3SE
6 iHE
5.05 CSAM
5 7SE
5 4HE
7.98 CSAM
8 IHE
8 I1TT 4 .03 CSAM
4 3SE
4 2HE
4 ITT
4 1GV
4.03 CSAM
4 ISE
4 ITT
4 1GV
4.03 CSAM
4 4SE
4 IHE
4 1GV
2.47 CSAM
2 1/2 ITT
2 1/2 IGV
197.0
23.6
4.7
0.6
178.4
35.3
4.7
0.6
75.5
4.2
17.0
5.3
12 .5
1.3
26.0
33.8
30.0
3.0
28.0
115.1
a.0
20.0
40.0
2.0
30.9
42.0
7.0
121.8
84.0
20.0
25.8
8.5
33.1
84.1
30.0
8.0
20.0
2.0
2.5
10.0
20.0
2.0
18.0
40.0
4.0
2.0
1.0
12.0
1.0
_______________________ I __________________________ I _____________ I ____________________ I __________________ I 1.645 I 1 64� I 62 0.0254 l0.43E-5I
225.9 10.00000251 0.000566
1 1
219.0 10.00000251 0.000549
1 1
79.7 10.00000721 0.000576
1 1 22.3 10.00000561 0.000127
13.8 10.000004310.0000604
26.0 10.0000581 0.00151
94.8 0.000 0.000
185.1 0.000 0.000
79.9 0.000 0.000
225.8 0.000 0.00C
67.4 0.000 0.00(
144.1 0.000 0.00(
34.5 0.000 0.00*
64.0 0.000 0.00
14.0 0.000 0.00
31 0
0
0
0
0
0I
I1- 1I____________ _____________________ I _____________________________ I __________________________________ I __________________ ____________________ _______________________ I ____________________ I _______________________ I ____________ __________________ I _______________ I
IX-57
U2TB Hose St
1.645
-7.058
0.650
0.000
0.000 I0
0.000
3.248
3.551
-7.794
-4.027
-11.562
2.728
0.000
1.169
-0.433
-1-1-1.646
-7.058
0.650
0.000127
0.0000604
0.00151
3.248
3.551
-7.794
-4.027
-11.562
2.728
0.000
1.169
-0.433
62 10.0254 10-43E-51
II
I 1I
I I 62 1 0.0254 I0.43E-S1
I 1 I
I I I 5610.0626 I0.26E-41
5610.0567 0O.21E-4I
59 1 0.0519 10.18E-41
I 1 1 86 1 0.293 10.000571
120 1 0.000 1 0.000
120 0.000 0.000
120 0.000 10.000
120 0.000 0.000
120 0.000 0.000
120 0.000 10.000
120 0.000 0.000
120 0.000 0.000
120 0.000 0.000
AMENDMENT 13Calc. No. DKREU-IUU) Revision 0 Attachment C
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I IPIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
IPIPEL PIPE I FLOW I NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE
NO. I NODES (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)
STATIC TOTAL IROUGHI WATER I VELOC.
jHEAD LOSSIHEAD LOSS
I(PSI) I(PSI)
I I I I I ______________________________ I ________________ __________________ I ____________________ I __________________
28.1 I 0.000 I 0.000 I -2.165
1810 I
1811I
1812
1813
1814 I
1 1 1815 1
1 1 816 1
1819
1820
1821
822
823
824
1826
1
4.03 I ,AM60 809
79 811
55 813
813 817
813 818
805 819
819 820
819 822
76 824
824 825
801 804
836 827
835 836
824 826
68.1 I0.00
4
4
0.00
3
3
3
0.00
8
8 8
0.00
2 1/2
2 1/2
0.00
18
0.00
8
0.00
6
6
0.00
6
6
6
0.00
18
B 8
18
0.00
6
6
6
0.00
13 0.00
5
5
0.00
6
6
6
6
6
0.00
6
6
6
IROUGHI WATER I VELOC. NESS IVELOCITYI PRESS.
ICOEFFI(FT/SEC)l (PSI)
1 1_ - 1__ _ _ _
4.03 C• 2.
3.07 C
4•
2
7.98 C
4
4
1
2.47- C
7.98 C
1 7.98 IC
I] 6.07 C
6.07
7.98
6.07
3.07
5.05
6.07
6.07
SAM
SE
TT
SAM
SE
TT
GV
SAM
SE
HE
TT
:SAM
[GV
:SAM
IGV
=SAM
[SE
CSAM
[HE
ITT
1GV
CSAM
ISE
IHE
1GV
CSAM
2SE
ITT
1HE
CSAM
ISE
1HE
1GV
CSAM
ITT
CSAM
4HE
8SE
CSAM
IGV
SSE
3HE
4TT
ICv
CSAM
ITT
IHE
1GV
.1 ____________________ I __________________ I _________________________ I ______________________________ I ________________ I __________________ I ____________________ I __________________ I ____________________ I __________ I ________________ I ______________
IX-58
U2TB Hose St
28.1
20.0 20.0
51.5
28.0
15.0
2.0
62.7
68.2
34 .1
33.1
1.0
12.0
1.0
1.5
3.8
6.0
17.0
6.6
7.0
30.0
3.0
16.8
14.0
7.0
3.0
32 .0
34.1
33.1
8.5
23.3
14.0
7.0
3.0
5.5
15.0
121.5
20.0
96.0
63.5
3.0
70.0
21.0
120.0
32.0
6.3
30.0
7.0
3.0
PACE C- /gy
68.1
96.5
198.1 i
14.0
5.3
23.0
46.6 6
40.8
107.7
47.3 3
20.5
237.5
309.5
46.3
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
-2.165
-3.681
13.207
0.000
-1.169
2.901
-4.114
-4.114
-13.943
0.000
0.000
-7.483
-3.992
0.000
-2.165 I1:
-3.681 i1
-13.207 1
0.000 1
-1.169 I1
2.901 1
-4.114 I
-4.114
-13.943
0.000
0.000
-7.483
-3.992
0.000
20
20
20
20
.20
.20
120
120
120
120
120
120
120
20 10.000 10.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
AMENDMENT 13Revision 0 Attachment C
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS PAGE CZ0
I I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAl) LOSSIHEAD LOSS
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH I PER FT. OVER PIPE
INO. I NODES (US GPM) (IN) (IN) # (FT) (FT) I (PSI) I (PSI)
STATIC I TOTAL
;HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
IROUGHI WATER I VELOC.I
NESS IVELOCITYI PRESS.I
ICOEFFI(FT/SEC)l (PSI) I
I I I I I I_I I I ___________ I ______ I _______ I ________ ____ 0.823 I IC I
. _I. --
182
182
182
83
183
183
183
8
18
1I
iI
71
8
9
2
33
34
35
.36
837
839
840
841
102 855
200 839 1 4
839 831 4
42 837
61 832
98 833
54 834
73 835
833 828
828 829
96 838
838 845 J
75 823
I__ 4.40.00
8.96
8.96
0.00
0.00
0.00
0.00
0.00
0.00
0.00
11.70
0.00
0.00
I6.07 CS
6 IT
6 1G
6 i1
6 is
6.07 CS
6 11
6.07 CS
10.02 CS
10 21
6.07 C
6 1,
6 I
6 i1' 6.07 C
6 I1
6 1
6 1,
6.07 C
6 2
6 2
6 2
6 1
6.07 C
6 1
6
6
6
6.07
6
6
6.07
6
6
6
6.07
6
6
6
4.03
4
4
4
4
7.98
8
8
8
AM
T
'V
;E
IE
AM
I.T
SAM
SAM
HE
SAM
SE
GV
TT
SAM
SE
TT
GV
:SAM
SE
HE
2TT
LGV
:SAM
2TT
2SE
2HE
lGV
CSAM
9SE
2TT
CSAM
8SE
2HE
ITT
CSAM
1HE
IGV
ITT
CSAM
SHE
2SE
ITT
lGV
CSAM
ITT
2SE
1HE
I _______________________ I ___________________________ I _______________ I ________________ I __________________ I ________________ I __________________ l.....................I ______________ I ____________
IX-59
U2TB Hose St
30.0
3.0
7.0
14.0
2.3
8.8
3.0
11.0
22.0
9.9
14.0
3.0
30.0
25.6
14.0
30.0
3.0
28.6
28.0
14.0
60.0
3.0
24.5
30.0
28.0
14.0
3.0
75.9
126.0
60.0
100.0
112.0
14.0
30.0
62.4
2.1
0.9
8.8
117.8
20.0
20.0
20.0
2.0
32.0
33.1
34.1
8.5
1-1-1-
58.4 0.000oo II
II
11.1 10.000452
3.0 10.000452
33.0 1 0.000
56.9 0.000
72.6 1 0.000
133.6 0.000
99.5 0.000
261.9 0.000
256.0 0.000
74.2 10.000031
179.8 0.000
107.7 0.000
0.000
0.00503
0.00136
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.00237
0.000
0.000
0.823
-3.464
0.000
0.000
0.0433
1.429
-8.531
-8.314
-0.684
-28.112
0.000
37.024
-13.943
0.823 12
-3.459
0.00136
0.000
0.0433
1.429 1
-8.531 1
-8.314 1
-0.684
-28.112
0.00237
37.024
-13.943
20
62
62
20
20
20
120
120
120
120
62
120
120
0.000 0.000
0.544 10.0019
0.544 10.0019
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 O.00C
0.000 0.00(
0.130 10.000
0.000 0.00
0.000 0.00
0
0
0
o0
AMENDMENT 13
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG I TOTAL IHEAD LOSSIHEAD LOSS I STATIC TOTAL
IPIPEI PIPE I FLOW I NOM ACTUALI CODE LENGTH I LENGTH I PER FT. OVER PIPE HEAD LOSSIHEAD LOSS
NO. I NODES I (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI) (PSI) (PSI)
CaIc. No. DREOO-00O0 Revision 0 Attachment C
PAGE : I
IROUGHI WATER I INESS IVELOCITYI
ICOEFFI (FT/SEC)l
VELOC.I
PRESS.
(PSI)
1842 I 809 810 0.00
850 1 93 850 0.00
I I I I 1851 89 851 I 0.o00
I I
I I 1860 I 97 860 I 13.08
861 860 861 0.00
I I I I
II
1922 19 919 8.93
1925 23 923 44.25
1931 928 28 3.33
932 29 929 3.33
1 ____________ I ___________I____________
3.07 I CSAM3.07 CSAM
ISE
1GV
6.07 CSAM
1GV
2SE
ITT
4.03 CSAM
3SE
ITT
1GV
IHE
6.07 CSAM
1GV
1HE
4.03 CSAM
3HE
3SE
ITT
IGV
7.85 CSAM
7.98 CSAM
3SE
ITT
IGV
7.98 CSA!
7.98 CSAM
23.3 I23 .3
7.0
1.0
12 .5
3.0
28.0
30.0
12.9
30.0
20.0
2.0
4.0
51.5
0.9
2.1
119.8
12.0
30.0
20.0
2.0
29.2
21 .2
15.1
9.8
1.1
98.2
2.5
31.3 I 0.000 I 0.000I
12 II 0.000 I 0.000 II
I _____ I ______ I ___ I _____ I ____ I______________________ I ____________________ I _____________________________ I __________________________________ I __________________ I ____________________ I
IX-60
U2TB Hose St
I
31.3 0.000 0.000
73.5 0.000 0.000
68.9 0.000 0.000
54.4 10.0000391 0.00214
183.8 0.000 0.000
29.2 10.00000601 0.000176
47.2 0.000098 1 0.00464
1 1
1 1
98.2 0.98SE-6 10.0000968
2.5 10.985E-6 0.0000024
0.000 0.000
-2.598 -2.598
-2.382 -2.382
0.000 0.00214
38.020 38.020
0.476 0.477
12.774 12.779
0.000 10.0000968
0.000 10.0000024
120
120
120
62
120
59
62
56
56
0.000 0.000
0.000 0.000
0.000 0.000
0.145 10.000141
1 1 1 1
0.000 0.000
0.0592 10.23E-41 0.284 10.000541
I I
I I
0.0213 10.30E-51
0.0213 I0.30E-51
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment C
HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS
COMPANY Nexus Technical Services Corporation IPAGE 200J
DESIGNER BY: BRIAN FOX CHECKED: J
A.-." G DATE 2000 JAN 6
CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. U2TB Hose Station F-75
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED 1
1 ELEVATION DISCHARGE I K-FACTORI
NO. JDISCHG. GPM P.S.I. NO. IDISCHG. GPM I P.S.I. I NO. jDEMAND GPM P.S.I. (FT) (US GPM)
i1 149.928 500.000
2 145.814 509.500
3 142.999 516.000
4 145.25i 510.800
5 145.251 510.800
6 1 1 145.251 510.800
7 145.466 510.300
8 145.767 509.600
9 145.767 509.600
1 I 10 143.211
515.500
I1 126.453 554.200
12 143.211 515.500
13 145.679 509.800 I
14 145.895 509.300
I 15 1 145.982 509.100
16 145.201 510.900
17 145.547 510.100
le 145.892 509.300
9I 145.849 509.400
20 144.982 511.400
21 145.328 510.600
22 144.948 511.500 I
23 144.945 511.500
24 139.093 525.000
25 145.155 511.000
26 144.938 511.500
27 145.371 510.500
28 144.720 512.000
29 144.720 512.000
30 145.067 511.200 I
31 144.638 512.200 I
32 144.294 513.000 I
33 144.732 512.000
34 144.867 511.700
35 145.547 1 1 1 510.100 1
361 1 144.522 1 1 1 512.500 1
37 145.220 510.900
38 145.168 511.000 1 I
39 145.122 511.100 1
1 401 127.53 1 150.000 1 500.000 I
41 145.2691 1 1 1510.9001
42 145.252 510.900 1
45 145.225 510.9001
46 144.286 513.000 1
IX-61
AMENDMENT 13Calc. No. DREOO-0008 Revision 0 Attachment C
HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS INPUT POINTS POINT REQUIRED ELEVATION DISCHARGE K-FACTOR'
NO. IDISCHG. GPM P.S.I. NO. IDISCHG. GPM P.S.I. NO. IDEMAND GPM I PSI. - (FT) I (US GPM)
47 144.286 513.000 1
48 137.126 529.500 1
49 134.527 535.500
50 134.094 536.500
51 133.098 538.800
52 144.867 511.700
53 125.614 556.000
54 125.610 556.000
55 125.585 556.000
56 125.579 556.000
57 125.579 556.000
58 126.292 554.500
59 126.292 554.500 1
60 126.293 554.500
61 126.340 554.400
62 122.834 562.500
63 119.761 569.600
64 138.642 526.000 1
65 141.038 520.500 1
66 141.037 520.500 1
67 138.642 526.000
68 127.078 552.700
69 138.642 526.000
I70 128.030 550.500
71 124.566 558.500
72 125.865 555.500
73 125.865 555.500
74 125.865 555.500
75 125.865 555.500
76 125.865 555.500
77 125.866 555.500
78 126.299 554.500
79 126.299 554.5000
80 138.642 526.000
81 119.718 569.700 1
82 138.643 526.000
83 141.687 519.000
84 141.687 519.000
85 142.326 517.500
86 138.643 526.000
87 142.326 517.500
88 138.513 526.300
89 138.210 527.000
91 138.556 526.200
92 138.210 527.000
93 138.210 527.000
96 147.533 505.500
97 147.532 505.500
98 127.728 551.200
IX-62
U2TB Hose StPAGE CZ3
Cabc. No. DREOO-OOOS AMENDMENT 13 Rcvision 0
Attachment C
HYDRAULIC CALCULATIONS .. NODE CHARACTERISTICS
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED
ELEVATION DISCHARGE
df IrnTCHG. GPM P.S.I. NO. IDISCHG- GPM I P.S.I. NO. IDEMAND GPM I P.S.I. I (FT) I (US GPM)
526.00_ _ _ _ _ _ _ _ _ _ _ _ __.__ _ _ _ _ __I_ _ _ _ _ _ _ _I.. . . . . . . . ._
_ _ _ _ _ 1 ..........I _ _ _ _ _ _ _ _ _ _ _ _ _ _ _
102 138.642 I
200 134.545 1
201 125.641 1
202 134.538
400 147.532
401 106.178
4021 109.513
4031 147.533
404 106.179 1
405 109.513 1
600 127.53 1 105.769
601 139.093
602 137.664
611 135.845
612 135.845
621 138.097 1
651 121.100 1
700 145.982 1
701 145.418 1
7021 145.331 1
703 144.722
704 137.578
705 145.026
706 139.224
7191 144.946
720 144.721
721 144.721
723 145.372
724 144.947
725 145.892
1 1 1 726 145.892
1 I 1 727 145.892 1 I
1 1 800 1 141.935
1 1 801 1 145.962
1 1 802 141.472
1 803 137.922
804 145.962
805 137.141
808 126.299 1 1
809 128.458
810 128.458
811 129.980
812 133.098
813 138.792
814 131.799
815 130.630
817 138.792
818 139.961
819 134.240 I
________________________ I ________________________ l...................I ________________________ I ________________________
K-.FACTOR
526.000 535.500
556.000
535.500
505.500
601.000
593.300
505.500
601.000
593.300
566.500
525.000
528.300
532.500
532.500
527.300
566.500
509.100
510.400
510.600
512.000
528.500
511.300
524.700
511.500
512.000
512.000
510.500
511.500
509.300
509.300
509.300
518.300
509.000
519.500
527.700
509.000
529.300
554.500
549.500
549.500
546.000
538.800
525.500
541.800
544.500
525.500
522.800
536.000
_ _ _- _I -_ _
IX-63
U2TB Hose St
PA GE. No <R0-000
I I
I I
I I
I I
I I
100.00 I
I I
I I
I I
I I
I I
I I
I I
I P
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
I I
i00.00 12.400
AMENDMENT 13Calc. No. DRE0O-OOS Revision 0 Attachment C
PAGE CZ5HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS
I SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS INPUT POINTS POINT
ELEVATION
I NO.' IDST•CHC_ GPM P.S.I. NO. DEMAND GPM I P.S.I. I (FT)
IREQUIREDI DISCHARGE K-FACTOR
I (US GPM) I
IX-64
U2TB Hose St
NO. IDISCHG. GPM1- .I. .... ........ ....
820 138.353 526.500 1
822 138.353 526.500
823 139.809 523.300
824 139.809 523.300
825 139.809 523.300
826 139.809 523.300
827 145.655 509.800
828 126.984 552.920
829 155.096 488.000
831 138.003 527.500
832 126.297 554.500
833 126.299 554.500
834 134.141 536.300
835 134.179 536.300
836 138.172 527.080
837 145.252 510.900
838 147.531 505.500
839 138.005 527.500
845 110.507 591.000
1 849 131.799 541.800
1 850 140.808 521.000
851 140.591 521.500 1
855 137.820 527.900 1
I 860 147.530 505.500 1 I
I 861 109.511 593.300 1
919 145.372 510.500
923 132.166 541.000
928 144.720 512.000
929 144.720 512.000
Calc. No. DREOO-OOOS AMENDMENT 13 Re% ision 0
Attachment C
WARNING: THE FOLLOWING PIPE(S) HAVE FLOW(S) SMALLER THAN 0.1 GPM - c__•
1 2 3 4 85 86 87 91 106 500
501 502 503 504 505 611 612 621 651 800
802 803 804 805 806 807 808 809 810 811
812 813 814 815 816 819 820 821 822 823
824 826 827 831 832 833 834 835 836 837
840 841 842 850 851 861
MAXIMUM UNBALANCED HEAD LOSS= .00006 IN LOOP 8 1
IX-65
AMENDMENT 13Calc. No. DREOO-0008 Revision 0 Attachment C
lP-NC C27 o -C._-
IE
Is
Is I U
391 X is operating point for SPECIFIED pressure
I Co-ordinates are
I FLOW - 127.53
PRESSURE 150.00
1 1635 3268 4901
Pump Curve Input Point No.
FLOW 40
IX-66
AMENDMENT 13
CALCULATION NO. DREOO-0008
Revision No. 0
ATTACHMENT D
SPRINK-1000 OUTPUT DATA FIRE HOSE STATION F-126
IX-67
Cakc. No. DREOO-OOOS AMENDMENT 13 Revision 0
Attachment D
DESIGN PROGRAM FOR SPRINKLER SYSTEMS
by
MUNICIPAL HYDRAULICS LTD, LADYSMITH, B.C. CANADA
COPYRIGHT (C) 1995 MUNICIPAL HYDRAULICS LTD
VERSION 11.00
COMPANY Nexus Technical Services Corporation
DESIGNER BY: CARL BALINGIT CHECKED:,J4 7"• ILLT CLIENT ComEd. Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. U3TB Hose Station F-126
FIX
C-62
P 01 01 02 3.5 11.938
P 02 02 03 16.1 11.938 1GV ITT 3SE CV
P 03 03 04 21.2 7.981 2SE
C-132
P 04 04 05 60.0 11.2 HE SE 3ZSE(7)
P 05 05 06 13.5 11.2 TT GV
C-66
P 06 06 07 156.6 7.85
P 07 07 08 161.0 7.85
P 14 08 13 86.0 7.981 ITT
C-55
P 15 13 14 54.6 7.981
P 750 700 701 72.8 7.981 4HE
P 16 14 15 14.1 11.2 GV
P 17 15 700 44.5 11.2 GV
P 751 701 16 29.3 11.2
C-86
P 18 16 35 9.1 11.2
P 19 35 702 82.7 11.2 HE
P 752 702 17 41.9 7.85
P 20 17 726 119.6 7.85 HE
P 21 725 19 97.9 7.85
P 725 18 725 6.8 11.2 GV
P 726 18 726 4.5 11.2 GV
P 727 18 727 2.1 11.2 GV
C-59
P 762 723 919 12.5 8.385 GV
P 922 919 19 29.2 7.85
C-66
P 22 20 723 82.2 8.385 TT SE ZSE(5)
P 23 20 21 133.3 8.385 TT 3HE GV
P 30 27 703 4.0 7.981 1GV
P 753 703 21 26.0 7.85 TT
C-86
P 29 21 26 147.0 7.981 ITT
P 28 26 25 146.0 7.981 2SE
C-62
P 27 25 601 81.9 7.981 6SE IGV
P 601 601 24 10.8 7.981 ISE
P 754 602 704 58.7 7.981 4SE iHE ITT 1GV
P 602 602 24 123.0 7.981 5SE 2HE GV
P 755 704 705 221.92 7.981 7SE 2HE ITT
IX-68
AMENDMNT 13Caic. No. DREOO.OOOS AMENDMNT 13Revision 0
Attachmnent D
P 756 705 727 141.27 7.981 2HE ITT
C-62
P 300 24 200 136.5 7.981 5SE 1GV ITT
P 26 200 923 7.5 7.981 ISE ITT IGV
P 757 704 706 197.01 4.026 8SE 4HE GV
P 758 706 923 178.37 4.026 12SE 4HE GV
P 925 923 23 21.25 7.981 3SE ITT iGV
C=132
P 25 22 724 75.0 11.2 TT 4HE
C-62
P 719 719 23 5.86 7.981 2HE
C-86
P 763 724 719 26.0 7.85
C-132
P 24 05 22 149.9 11.2 GV TT
C-35
P 50 45 48 255.0 9.564 5SE 2GV IHE
NOTE *
/* THE FOLLOWING PIPES HAD A
/* CALCULATED C FACTOR OF 27.4. DUE*
/- TO LIMITATIONS OF THE SPRINK*
/* PROGRAM, A C OF 35 WAS USED*
/* (THE MINIMUM) AND PIPE LENGTHS*
/- ADJUSTED TO REFLECT EQUIVALENT
/* FRICTION LOSS.*
/* ACTUAL LENGTHS ARE AS FOLLOWS:
/-PIPE 41 - 10.8*
/-PIPE 42 = 9.8*
/-PIPE 45 = 22.3*
/*PIPE 46 = 10.0.
/*PIPE 49 - 2.0*
/.
P 41 40 41 17.0 10.02
P 42 41 42 15.4 10.02 1HE IG1CV ICy iSE
P 45 42 45 35.1 10.02 ITT
P 46 37 38 15.1 7.981 iGV SE 2HE
P 49 45 37 3.5 7.981 ITT
C-132
P 47 38 39 230.0 11.2 3SE 2HE 4ZSE(7) 3ZSE(3)
P 48 39 22 59.3 11.2
C-62
P 55 48 67 115.92 10.02 7SE
P 70 67 69 3.25 10.02
P 69 69 80 2.17 10.02
P 68 80 64 5.33 10.02 1GV
P 67 64 63 86.75 7.981 9SE 2TT IGV 2HE
P 66 63 62 36.93 6.065 4SE IGV ITT
P 65 62 61 70.08 6.065 3SE 2HE
P 64 61 60 130.25 6.065 3SE 4HE ITT
P 63 60 59 30.83 6.065
P 62 59 58 6.75 6.065
P 302 58 201 80.0 6.065 IGV 4HE
P 303 201 202 482.5 10.02 2TT
P 305 57 201 89.0 6.065 iSE IGV 2HE
P 60 56 57 1.0 7.981
P 59 55 56 15.08 7.981 4HE
P 58 54 55 107.58 7.981 2HE
P 57 53 54 15.5 7.981
F.(:C, t)z-
IX-69
AMENDMENT 13 Calc. No. DREOO-OOOS Revision 0
P 56 70 53 118.25 7-981 7SE 1HE 1GV
Attachment D
P 54 51 70 11.67 10.02
P 53 50 51 2.33 10.02
P 52 49 50 1.0 10.02
P 51 48 49 6.0 10.02 ITT
P 8 8 9 30.0 7.981 IGV
p 9 9 10 110.0 4.026 2SE IHE 2TT 1GV
P 10 10 12 215.42 4.026 15SE 7HE 2GV ITT
p 11 10 11 77.5 4.026 5SE 2HE 1GV
P 12 11 12 80.25 4.026 8SE 4HE 1GV
P 13 12 15 34.75 4.026 4SE 1GV ITT
P 83 70 68 2.33 10.02 1GV
P 82 68 71 89.83 7.981 3SE
P 81 71 72 54.75 7.981 4SE IHE
P 80 72 73 15.58 7.981
P 79 73 74 103.58 7.981
p 78 74 75 1.75 7.981
P 77 75 76 14.50 7.981
P 76 76 77 21.50 6.065 2SE
P 75 77 78 175.67 6.065 4SE 2HE IGV
P 74 78 79 65.83 6.065 2HE
P 73 79 98 122.0 6.065 2SE 2HE
P 72 98 81 32.25 6.065 3SE 2TT IHE
P 71 81 63 84.83 6.065 IGV
P 110 64 102 0.5 10.02
P 84 102 82 10.5 10.02
P 99 82 86 1.0 10.02 ITT
P 100 86 85 48.5 6.065 2SE 3HE 1GV
P 102 97 84 14.33 7.981 2HE 1TT
P 103 84 66 1.50 7.981
P 104 66 47 27.75 7.981 4SE 2GV SR
P 105 47 28 115.0 7.981 ISE 1GV ITT
C-56
P 31 28 721 125.0 7.981
P 761 721 720 17.0 8.385 2HE
P 760 720 27 75.5 7.981 ISE
C-62
P 90 82 88 1.00 10.02 ITT
P 93 88 87 66.0 6.065 4SE 3HE 1GV ITT
P 95 96 83 14.17 7.981 2HE ITT
P 96 83 65 1.50 7.981
P 97 65 46 31.25 7.981 5SE 2GV 1SR
P 98 46 29 112.0 7.981 ISE 1GV ITT
C-56
P 932 29 929 2.5 7.981
P 32 929 928 184.0 8.425 2SE 5HE 2GV
P 931 928 28 98.2 7.981
P 33 30 29 20.0 7.981
C=41
P 40 37 36 160.0 7.981 IGV 1TT 4SE 3HE
C-61
P 39 36 52 160.0 7.981
P 38 52 34 10.00 7.981
P 37 34 33 280.0 7.981 5SE IHE
C-55
P 36 33 32 300.0 7.981
C.71
P 35 32 31 285.0 7.981
C-61
p 34 31 30 285.0 7.981 IX-70
............. **.. ****.
NOTE
/* THE FOLLOWING PIPES WERE *
/ ADDED TO ATTACH SYSTEMS *
/ TO THE BASE MODEL
/ . ** * ** *
C.120
P 611
P 612
P 621
P 834
R
P
AMENDMENT 13 Calc. No. DREOO-OOOS Rev.ision 0 Attachment D
&tc 14-
601 611 4.5 6.065 2SE iTT
611 612 1.0 6.065
602 621 3.6 6.065 3SE ITT
54 834 28.6 6.065 2SE 2HE 2TT IGV
834 536.3
803 834 800 30.9 6.065 3SE IHE
R 800
P 804
R 801
P 822
R 804
P 805
R 805
P 815
R 819
P 816
R 820
P 819
R 822
P 809
R 808
P 106
R 812
P 806
P 808
P 807
R 84
R 81
518.1518.3
800 801
509.0
801 804
121.75 5.047 7SE 4HE
5.5 3.068 ITT
509.0
56 805 25.75 7.981 1HE ITT
529.3
805 819 6.0 7.981 ISE
536.0
819 820 6.58 6.065 IHE ITT iGV
526.5
819 822 16.75 6.065 ISE 1HE 1GV
526.5
77 808 1.0 2.469 ITT .GV
554.5
51 812 1.0 7.981 ITT IGV ISE
538.8
49 849 84.1 4.026 3SE 2HE ITT 1GV
849 815 18.0 4.026 4SE IHE 1GV
7 849 814 2.5 4.026 ISE ITT yGV
9 541.8
4 541.8
R 815 544.5
P 810 60 809 28.08 4.026 2SE ITT
R 809 549-5
P 842 809 810 23.33 3.068 ISE IGV
R 810 549.5
P 811 79 811 51.5 3.068 4SE ITT 2GV
R 811 546.0
P 833 98 552 11.17 6.065
P 552 552 833 11.0 6.065 ISE iTT 1GV
R 833 554.5
P 836 833 828 75.92 6.065 9SE 2TT
R 828 552.92
P 837 828 829 100 6.065 8SE 2HE ITT
R 829 488.0
P 832 61 832 9.9 6.065 ISE iGV ITT
R 832 554.5
P 835 73 835 24.5--6.065 ITT 2SE 2HE 1GV
R 835 536.3
P 812 55 813 62.7 7.981 4SE 4HE ITT
R 813 525.5
P 813 813 817 1.0 2.469 ITT iGV
R 817 525.5
P 814 813 818 1.5 7.981 yGV
R 818 522.8
P 841 75 823 32.0 7.981 ITT 2SE IKEIX-71
i
Calc. No. DREOO-OOOS AMENDMENT 13 Revision 0
Attachment D
R 823 523.3
P 820 76 824 32.0 7.981 2SE ITT IHE
R 824 523.3
P 821 824 825 23.25 6.065 ISE iHE 1GV
R 825 523.3
P 826 824 826 6.3 6.065 ITT IHE 1GV
R 826 523.3
P 850 93 850 12-5 6.065 1GV 2SE iTT
R 850 521.0
P 87 92 93 152.1 4.026 2SE 6HE
P 86 91 92 16.0 6.065 2HE IGV ITT
P 85 82 91 1.0 10.020 ITT
R 91 526.2
R 92 527.0
R 93 527.0
P 851 89 851 12.9 4.026 3SE ITT 1GV iHE
R 851 521.5
P 91 88 89 166.9 4.026 IGV 8HE
R 89 527.0
P 800 928 802 33.83 6.065 iTT iGV 2SE
R 802 519.5
P 802 802 803 115.08 4.026 2HE ITT 4SE
R 803 527.7
P 840 838 845 117.8 4.026 5HE 2SE ITT 1
R 845 591.0
C-62
P 839 96 838 62.4 6.065 IHE 1GV iTT
P 94 838 87 206.1 6.065 6SE 2HE iTT
P 860 97 860 51.5 6.065 iGV IRE
P 101 860 85 168.5 6.065 7SE 3HE
C-120
R 838 505.5
P 861 860 861 119.75 4.026 3HE 3SE TT
R 860 505.5
R 861 593.3
P 827 102 855 4.39 6.065 ITT iGV IHE 1
P 831 42 837 11.0 10.02 2HE
P 824 835 836 63.5 6.065 IGV 5SE 3HE 4
R 836 527.08
P 823 836 827 121.5 5.047 4HE 8SE
R 827 509.8
R 837 510.9
R 855 527.9
C-62
P 828
P 829
P 304
1GV
GV
GV
SE
TT icV
200 839 2.3 6.065 ITT
839 831 3.0 6.065
831 202 2.7 6.065
C=120
R 839 527.5
R 831 527.5 */***************** ***********
END
.*** **.**********
C=120
p 500
P 501
P 502
P 503
P 504
P 505
97 400 26.17 6.065 iHE
400 401 132.67 6.065 2SE 4HE ITT IGV
401 402 52.17 4.026 3SE ITT 2GV
96 403 7.75 6.065 iHE
403 404 132.33 6.065 ITT 2SE 3HE IGV
404 405 47.0 4.026 ITT 3SE 2GV
PýNý tlS
IX-72
Calc. No. DREuU-000U
AMENDMENT 13 Revision 0 Attachment D
/ .... .. .. .. . * .. . . . . . * .
/. The following nodes and pipes
/ refer to hose stations. To *
/ switch between hose stations,
/ change the S to an R and remove
* the flow and K-factor on the hose *
/* stations that you do not want *
/ to flow.
/ HOSE STATION F-75
p 600 57 600 13.5 1.610 ITT 2SE 1GV
R 600 566.5
/HOSE STATION F-80
P 651 61 651 49.1 1.610 ITT 2SE 1GV
R 651 566.5
/ HOSE STATION F-126
P 550 552 550 21.33 6.065 ITT
P 551 550 551 28.75 1.610 2SE lGV
S 551 566.5 100 12.4
/************ ***************t*******
/, END
/.............. **** *
R 02 509.5
R 03 516.0
R 04 510.8
R 05 510.8
R 06 510.8
R 07 510.3
R 08 509.6
R 09 509.6
R 10 515.5
R 11 554.2
R 12 515.5
R 13 509.8
R 14 509.3
R 15 509.1
R 16 510.9
R 17 510.1
R 18 509.3
R 19 509.4
R 20 511.4
R 21 510.6
R 22 511.5
R 23 511.5
R 24 525.0
R 25 511.0
R 26 511.5
R 27 510.5
R 28 512.0
R 29 512.0
R 30 511.2
R 31 512.2
R 32 513.0
R 33 512.0
R 34 511.7
R 35 510.1
R 36 512.5
R 37 510.9
R 38 511.0
R 39 511.1 IX-73
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment D
S41 510.9
S42 510.9
S45 510.9
R 46 513.0
. 47 513.0
R 48 529.5
R 49 535.5
R 50 536.5
R 51 538.8
R 52 511.7
R 53 556.0
R 54 556.0
R 55 556.0
R 56 556.0
R 57 556.0
R 58 554.5
R 59 554.5
R 60 554.5
R 61 554.4
R 62 562.5
R 63 569.6
R 64 526.0
R 65 520.5
R 66 520.5
R 67 526.0
R 68 552.7
R 69 526.0
R 70 550.5
R 71 558.5
R 72 555.5
R 73 555.5
R 74 555.5
R 75 555.5
R 76 555.5
R 77 555.5
R 78 554.5
R 79 554.5
R 80 526.0
R 81 569.7
R 82 526.0
R 83 519.0
R 84 519.0
R 85 517.5
R 86 526.0
R 87 517.5
R 88 526.3
R 96 505.5
R 97 505.5
R 98 551.2
R 102 526.0
R 200 535.5
R 201 556.0
R 202 535.5
R 400 505.5
R 401 601.0
R 402 593.3
R 403 505.5
R 404 601.0
R 405 593.3
R 601 525.0
-PýC- P7
IX-74
Calc. No. DREOO-OOOS AMENDMENT 13 Revision 0
Attachment D
R 602 528.3
R 611 532.5 P' 7 .pb
R 612 532.5
R 621 527.3
R 120 512.0
R 721 512.0
R 723 510.5
R 724 511.5
R 700 509.1
R 701 510.4
R 702 510.6
R 703 512.0
R 704 528.5
R 705 511.3
R 706 524.7
R 719 511.5
R 725 509.3
R 726 509.3
R 727 509.3
R 919 510.5
R 923 541.0
R 928 512.0
R 929 512.0
R 552 554.5
R 550 554.5
/* NOTE
/* TO DEACTIVATE PUMP UNIT 1:*
/ CHANGE:*
/1 1 01 500.0 0.0 150 2000 150 2500 140 3750 91 3751 10"
/ TO:*
/ R 01 500.0
/***************** *** ******************
R 01 500.0 ********************************************************
NOTE
/ TO DEACTIVATE PUMP UNIT 2/3:*
/* CHANGE:'
1' 1 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10'
/* TO:'
/* R 40 500.0 *****************************************
I 40 500.0 0.0 150 2250 150 3000 131 3600 120 4900 110 4901 10
LENGTH DIAMETER FLOW HEAD ELEVATION PRESSURE
UNITS BEING USED: FEET INCHES US GPM FEET FEET PSI
HAZEN-WILLIAMS FORMULA USED
FITTINGS SPECIFIED AS NFPA
ITERATION STOPS W•IEN GREATEST FLOW CHANGE IS .05000 IN ANY PIPE
MULTIPLICATIVE FACTOR OF EACH CONSUMPTION IS 1.00000
DEFAULT ROUGHNESS COEFFICIENT - C-120.0
THERE ARE 1 SPRINKLERS AND 0 BOOSTER PUMPS
THERE ARE 184 PIPES AND 172 REFERENCE POINTS
IX-75
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0 Attachment D
THE NUMBER OF INPUT POINTS IN SYSTEM IS I
NODE NO. OF PUMPS PUMP INPUT PUMP PARAMETERS
NO. IN PARALLEL ELEVATION FRACTION OR X-Y COORDINATES
40 1 500.00 1.00 .0 2250.0 3000.0 3600.0 4900.0 4901.0
150.0 150.0 131.0 120.0 110.0 10.0
Initial estimate of demand on the system is 100.00
NET UNBALANCED DEMAND ON THE SYSTEM - .00000
LOOP PIPES
1 551 550 833 72 71 67 68 69
2 73 72 71 67 68 69 70 55
75 74
3 67 66 65 64 63 62 302 305
68
4 50 55 70 69 68 110 84 90
70 55 50
51 52 53
60 59 58
93 94 839
38 39 40 49
303 305 60 59 58 57 56 54 53 52 51
26 828 829 304
99 90 93 94 839 95 96 97 98 932 32
932 33 34 35 36 37 38 39 40 46 47
28 29 753 30 760 761 31 931 32
754 757 758 26 300 602
25 24 5 6 7 14 15 16 17 750 751
758 925 719 763
725 727 756 755 754 602 601 27 28 29 23
14 8 9 10 13 16 15
10 11 12
BANDWIDTH - 5
Iteration # 0 Max change in flow is
Iteration # 1 Max change in flow is
Iteration # 2 Max change in flow is
Iteration # 3 Max change in flow is
Iteration # 4 Max change in flow is
Iteration # 5 Max change in flow is
NUMBER OF ITERATIONS- 6
45 42 41 54 83 82 81
57 56 54 53
95 96 97 98
50 49 46 47
931 105 104 103
48 25 763 719
80 79 78 77 76
52 51 55 70 69
33 34 35 36 37
48 25 763 719 925
102 860 101 100
925 26 300 601 27
18 19 752 20 726 727 756 755 757
22 762 922 21
82.890 in loop 9 2
33.376 in loop # 2
17.310 in loop 9 5
2.817 in loop # 10
.221 in loop # 8
.008 in loop # 11
IX-76
F^ýC- fxq
5
6
7
8
9
10
11
12
AMENDMENT 13 Caic. No. DREOO-OOOS Revision 0 Attachment D
SUMMARY REPORT
PAGE tDj I COMPANY Nexus Technical Services Corporation
DATE 00 .
DESIGNER BY: CARL BALINGIT CHECKED: DATE 2000 JAN 13
CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT lUI DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. I U3TB Hose Station F-126
I ______I
MINIMUM FLOW OF ALL OPERATING SPRINKLER HEADS IS 125.54
AVERAGE FLOW FROM ALL OPERATING SPRINKLER HEADS IS 125.54
TOTAL FLOW FROM ALL OPERATING SPRINKLER HEADS IS 125.54
TOTAL DEMAND ON THE WHOLE SYSTEM IS 125.54
SPECIFIED AVAILABLE PRESSURE AT INPUT NODE IS 346.40 FEET
OR 150.00 P.S.I.
IX-77
AMENDMENT 13 Calc. No. DREOO-000S Revision 0 Attachment D
HYDRAULIC CALCULATIONS - PIPE CHARACTERISTICS
I PAGE 2 N13 ]DATE 2000 JAN 13I COMPANY Nexus Technical Services Corporation
DESIGNER BY: CARL BALINGIT CHECKED:
CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. I mU3T ose I
I PIPE DIETER PIPE/TG TOTA AD LOSSIHEAD LOSS I STATIC TOTAL IROUGHI WATER I VELOC.
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. OVER PIPE 1HEAD LOSSIHEAD LOSS INESS IVELOCITYI PRESS.[
NO. I NODES (US GPM)I (IN) (IN) I # (FT) I (FT) (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI (FT/SEC)l (PSI)
1 1 2 0.00 11.94 CSAM 3.5 3.5
2 2 3 0.00 11.94 CSAM 16.1 77.0
12 1GV 1.7
12 ITT 17.2
12 3SE 23.3
12 ICV 18.7
3 3 4 0.00 7.98 CSAM 21.2 31.2
8 2SE 10.0
4 4 5 0.00 11.20 CSAM 60.0 115.1
12 lHE 11.1
12 ISE 23.0
12 3ZSE 21.0
5 5 6 13.65 11.20 CSAM 13.5 69.8
12 ITT 51.2
12 1GV 5.1
6 6 7 13.65 7.85 CSAM 156.6 156.6
7 7 8 13.65 7 7.85 CSAM 161.0 161.0
8 8 9 1.56 7.98 CSAN 30.0 31.1
8 I1GV 1.1
9 9 10 1.56 4.03 CSAM 110.0 129.4
4 2SE 5.9
4 1HE 1.2
4 2TT 11.8
4 I1GV 0.6
10 I 10 12 0.72 4.03 CSAM 215.4 274.9
I 1 4 115SE 44.2 1
1 1 4 7HE 8.2
1 1 4 2GV 1.2
1 4 ITT 5.9
11 10 11 0.85 4.03 CSAM 77.5 95.2
4 5SE 14.7
4 2HE 2.4
4 1GV 0.6
12 11 12 0.85 4.03 CSAM 80.3 109.1
4 8SE 23.6
4 4HE 4.7
4 I1GV 0.6
13 12 15 1.56 4.03 CSAM 34.8 53.0
4 4SE 11.8
[4 1GV 0.6
I 4 I1TT 5.9
141 8 13 12.09 7.98 CSAN 86.0 97.0
I 8 ITT 11.0
15 I 13 14 12.09 7.98 CSAM 54.6 54.6
0.000 0.000 0.000 0.000
0.000 0.000
0.000 0.000
0.529E-6 10.0000369
0.000010 I 0.00169
-0000Z10 1 0.00173
,0.202E-6 10.0000062
;0.00000561 0.000733
10.00000131 0.000369
10.00000181 0.000172
l0.00000181 0.00019•
10.0000056I 0.00030
1 1
10.00000791 0.00076
S0 1 l0.000011 10.00060
7
0
9
7
4.11 .14 64.114 4.114 2.815 2.815
-2.252 -2.252
0.000 0.000
0.000 10.0000369
-0.217 -0.215
-0.303 -0.301
0.000 10.0000062
2.555 1 2.556
0.000 1 0.00036S
16.758 16.753
-16.758 -16.751
-2.771 -2.77
0.0866 0.087
-0.217 -0.21
Ii
8
4
6
62
62
62
32
32
66
66
62
62
62
62
62
62
66
55
0.0 .0
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.0445 10.13E-4
0.0905 10.55E-4
0.0905 10.55E-4
0.0100 10.67E.6
0.0394 10.10E-4
0.0181 10.22E-5
0.0213 10.30E-5:
0.0213 I0.30E-5
0.0394 10.10E-4'
0.0775 10.40E-41
0.0775 10.40E-41
I I I I
______________ I _____________ I __________________ I _____________________ I ___________ I ____________ ______________ I ____________ I ______________
IX-78
AMENDMENT 13Calc. No. DREOO-OOOS Revision 0
Attachment D
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSS IHEAD LOSS
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. lOVER PIPE
INO. I NODES (US GPM) I (IN) (IN) I # (FT) (FT) (PSI) I (PSI)
I STATIC TOTAL
HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
IROUGHI WATER I VELOC.IIROUGHI WATER I VELOC. INESS IVELOCITYI PRESS.1
ICOEFFI(FT/SEC) (PSI) I
I I ___________ I __________ 15.1 10.00000211
16
17
18i
19
20
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
14 15 I
15 700 1
16 35 I 35 702
17 726
725 19
723 20
20 21
22 5
22 724
923 200
601 25
25 26
26 21
703 27
721 28
929 928
30 29
31 30
32 31
33 32
34 33
52 34
2.09
3.65
.3.65
.3.65
L3.65
9.69
9.69
9.69
13.65
39.68
38.55
6.52
6.52
6.52
16.21
16.21
0.44
15.19
15.19
15.19
15.19
15.19
15.19
15.1 0.0000021
45.5 10.00000261
1 1 9.1 I0.00000111
87.7 10.0000011l
1 1 123.8 10.00000661
1 1 97.9 10.00000341
3.0000323 I0.0000323
0.000122
0.0000106
0.000103
0.000817
0.000342
•..
I 006 I 0086 I 55 II
11.20 C
12 1'
11.20 C
12 1
11.20 C
11.20 C
12 1
7.85 C
8 1
7.85 C
8.39 C
8 1
8 1
8 1
8.39 I 8
8
8
11.20
12
12
11.20
12
12
7.98
8
8
8
7.98
8
8
7.98
8
7.98
8
7.98
8
7.98
8.43 3
8
8
8
7.98
7.98
7.98
7.98
7.98
8
8
7.98
I ______ I _____ I _______ I ________ I ____ I _____ I ______ I _____ I ______ I ___ I _____ I ____ I
IX-79
U3TB Hose St
SAM
GV
SAM
GV
SAM
SAM
HE
SAM
HHE
SAM
SAM
TT
SE
.ZSE
:SAM
ITT
3HE
LGV
CSAM
1GV
ITT
CSAM
ITT
4HE
CSAM
ISE
ITT
1GV
CSAM
6SE
1GV
CSAM
2SE
CSAM
ITT
CSAM
1GV
CSAM
CSAM
2SE
5HE
2GV
CSAM
CSAM
CSAM
CSAM
CSAM
5SE
1HE
CSAM
14.1
1.0
44.5
1.0
9.1
82.7
5.0
119.6
4.2
97.9
82.2
13.9
7.2
5.0
133.3
13.9
10.7
1.6
149.9
5.1
51.2
75.0
51.2
44 .3
7.5
5.0
9.8
1.1
81.9
30.1
1.1
146.0
18.4
147.0
17.9
4.0
1.3
125.0
184.0
10.8
13.5
2.4
20.0
285.0O
285.0
300.0
280.0
24.3
2.4
10.0
108.3 10.00000411 0.0004481
159.6 10.00000411 0.000660 1
206.2 10.529E-6 0.000109
170.5 10.00000381 0.000650
23.4 10.000076 1 0.00178
113.1 10.00000281 0.000321
164.4 I0.00000151 0.000255
1 1 164.9 10.00000151 0.000256
5.3 10.000013 10.0000717
125.0 10.000018 0.00231
210.7 I0.176E-7 10.0000037
1 1 1 1 1 1
20.0 0.000016 0.000328
285.0 0.000014 0.00399
285.0 10.000010 0.00302
300.0 10.000017 0.00509
306.8 10.000014 0.00430
10.0 10.000014 0.000140
PAGE p i"Z-,
-0.0866
0.000 0
-0.346
0.217
-0.346
0.0433
0.390
-0.346
-0.303
0.000
-2.382
-6.062
0.217
-0.390
-0.650
0.000
0.000
0.346
-0.433
-0.346
0.433
0.130
0.000
-0.0866
.000122
-0.346
0.217
-0.346
0.0436
0.390
-0.346
-0.303
0.000650
-2.380
-6.062
0.217
-0.389
-0.649
0.00231
0.0000037
0.347
-0.429
-0.343
0.438
0.134
0.000140
55
55
86
86
86
86 66
66
132
132
62
62
86
86
66
56
56
56
61
71
55
61
61
0.0394 10.10E-41 1 I
0.0445 10.13E-41
1 I 0.0445 10.13E-41
0.0445 10.13E-41
1 1 0.0905 10.55E-41
1 I 0.0642 10.27E-41
0.0563 10.21E-41
0.0563 10.21E-41
0.0445 10.13E-41
1 1 1 1
0.129 10.00011
0.247 10.000411
1 I
0.0418 10.IXE-41
II
0.0418 10.11E-41
0.0418 1 .11E-4
0.0418 10.1E-4
0.104 0.72E-41
1 I 0.104 10.72E-41
0.00251 10.42E-71
III
III 1 0.0974 10.63E-41
0.0974 10.63E-41
0.0974 10.63E-41
0.0974 10.63E-41
1 0.0974 10.63E-41
I 0 I
10.0974 10.63E-41
AMENDMENT 13Calc. No. DKLUU-Utluu Revision 0 Attachment D
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS PAGE C13
I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. JOVER PIPE
NO. I NODES (US GPM) (IN) (IN) I # (FT) (FT) I (PSI) I (PSI)
_______________ - ____________ _______________ I _________________ _________ I __________ -0346 I -0.344 160 0 10.000014 I 0.00224 I
39
40
41
42
45
46
47
48
49
50
51
52
53 54
55
56
57 58
59
60
62
63
I STATIC I TOTAL VELOC. I IROUGHI WATER IISTATIC I TOTAL HEAD LOSSIHEAD LOSS
I (PSI) I (PSI)
IROUGHI WATER I NESS IVELOCITYI
ICOEFFI (FT/SEC)I
VELOC. PRESS.
(PSI)
36 52
37 36
40 41
41 42
42 45
37 38
38 39
39 22
45 37
45 48
48 49
49 50
50 51
51 70
48 67
53 70
54 53
55 54
56 55
57 56
58 59
59 60
61 0.0974 I0. I4
15.19
15.19
125.54
125.54
125.54
53.33
53.33
53.33
68.52
57.02
28.58
28.58
28.58
28.58
28.44
16.46
16.46
16.46
16.46
16.46
20.66
20.66
8 8
8
8
10
10
10
10
10
8
8
8
12
12
12
12
8
10
10
10
10
10
8
8
8
8
8
____________________ I __________________ I __________________________ I ______________________________ I ________________ I __________________ I ____________________ I __________________
IX-80
U3TB Hose St
7.98 CSAM
7.98 CSAM
1GV
ITT
4SE
3HE
10.02 CSAM
10.02 CSAM
IHE
I1GV
ICV
ISE
10.02 CSAM
ITT
7.98 CSAM
1GV
ISE
2HE
11.20 CSAM
3SE
2HE
4ZSE
3ZSE
11.20 CSAM
7.98 CSAM
ITT
9.56 CSAM
5SE
2GV
IHE
10.02 CSAM
ITT
10.02 CSAM
10.02 CSAM
10.02 CSA1M
10.02 CSAM
7SE
7.98 CSAM
7SE
1HE
1GV
7.98 CSAM
7.98 CSAM
2HE
7.98 CSAM
4HE
7.98 CSAM
6.07 CSAM
6.07 CSAM
I
160.0
160.0
0.5
4.5
9.3
3.5
17.0
15.4
1.1
0.5
5.6
2.2
35.1
5.1
15.1
0.4 J
1.7
1.7
230.0
69.1
22.2
28.0
9.0
59.3
3.5
3.4
255.0
9.0
0.8
0.9
6.0
14.7
1.0
2.3
11.7
115.9
45.3
118.3
35.1
2.5
1.1
15.5
107.6
5.0
15.1
10.0
1.0
6.8
30.8
160.0 10.000014 1 0.00224 1
177.9 10.000029 0.00520
17.0 10.000646 1 0.0110
24.9 10.000646 1 0.0161
40.2 10.000646 1 0.0260
19.0 10.000401 0.00761
358.2 10.00000651 0.00236
1 1 1 1
I 1 59.3 10.00000651 0.000391
6.9 0.000638 0.00439
265.7 10.000188 0.0500
20.7 10.000014 0.000300 1
1.0 10.000014 I0.0000145 1
2.3 10.000014 10.00003371
11.7 10.000014 0.000169
161.3 0.000014 0.00231
157.0 10.000015 0.00248
15.5 10.000015 0.000244
112.6 10.000015 0.00178
25.1 10.000015 0.000396
1.0 10.000015 10.0000158
6.8 10.000091 0.000618
30.8 10.000091 0.00282
-0.346 -0.344 0.693 0.698
4.720 4.731
0.000 0.0161
0.000 0.0260
0.0433 0.0509
0.0433 0.0457
0.173 0.174
0.000 0.00439
8.054 8.104
2.598 2.598
0.433 0.433
0.996 0.996
5.066 5.067
-1.516 -1.513
-2.382 -2.379
0.000 0.000244
0.000 0.00178
0.000 0.000396
0.000 10.0000158
0.000 0.000618
0.000 0.00282
I61
41
35
35
35
35
132
132
35
35
62
62
62
62
62
62
62
62
62
62
62
62
0.0974 10.63E-41
0.0974 10.63E-41
0.511 0.0017
0.511 0.0017
0.511 10.0017
0.342 0.000781
1 1
0.174 I0.000201 1 1
1 1
0.174 10.000201
0.439 10.0013 1
0.255 0.000431
I 1 1 1
0.116 10.91E-4
0.116 0.91E-4
0.116 10.91E-41
0.116 10.91E-41
0.116 10.90E-41
II 0.106 I0.79E-41
0.116 10.91E-41 0.116 10.90E-41
0.106 10.75E-41 0.106 10.75E-41 0.106 10.75E-41
0.106 10.75E-41
I I 0.106 10.'75E-41
0.229 10.000351
0.229 10.000351
1 I
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS
IPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. lOVER PIPE
NO. NODES I (US GPM)I (IN) (IN) # (FT) (FT) (PSI) I (PSI)
______-___________-_________I_-________________I __________________________________ I I ____________________ 0.0146 0.0433 I 0.0287
I
159.7 10.000091 I64
65
66
67
68
69
70
71
72
73
74
75
76
77
78 79
80
81
82
83
84
I
STATIC TOTAL IROUGHI WATER VELOC.
ISTATIC I TOTAL HEAD LOSSIHEAD LOSS
I (PSI) (PSI)
IROUGHI WATER I VELOC. NESS IVELOCITYI PRESS.
ICOEFFI(FT/SEC)I (PSI)
I I I I
60 61
61 62
62 63
64 63
80 64
69 80
67 69
63 81
81 98
79 98
78 79
77 78
76 77
75 76
74 75
73 74
72 73
71 72
68 71
70 68
82 102
(2 0.29 0000I
20.66
20.66
20.66
59.84
28.44
28.44
28.44
80.50
80.50
45.04
45.04
45.04
45.04
45.04
45.04
45.04
45.04
45.04
45.04
45.04
31.40
6.07 CSAM
6 3SE
6 4HE
6 ITT
6.07 CSAM
6 3SE
6 2HE
6.07 CSAM
6 4SE
6 1GV
6 ITT
7.98 CSAM
8 9SE
8 2TT
8 1GV
8 2HE
10.02 CSAM
10 1GV
10.02 CSAM
10.02 CSAM
6.07 CSAM
6 I1GV 6.07 CSAM
6 3SE
6 2TT
6 IHE
6.07 CSAt
6 2SE
6 2HE
6.07 CSAI
6 I2HE 6.07 CSAJ
6 4SE
6 2HE
6 I1GV 6.07 CSA
6 2SE
7.98 CSA
7.98 CSA
7.98 CSA
7.98 CSA
7.98 CS•
8 4SE
8 1HE
7.98 CS•
8 3SE
10.02 CS7
10 IG\
10.02 CS)
M
M
M
14
'M
'M
LM
UM
AM
1 - - 1 1 -____________I __________I _______________I__________________I _________I___________I____________
IX-81
U3TB Hose St
rkIviJ-...L ,1�Aifl.A�a A ± Revision U Attachment D
PAGE L/4-
130.3 12.4
8.2
8.8
70.1
12.4
4.1
36.9
16.5
0.9
8.8
86.8
45.2
19.5
1.1i
5.0
5.3
1.5
2.2
3 .3
84.8
0.9
32.3
12 .4
17.7
2.1
122 .0
8.2
4.1
65.8
4.1
175.7
16.5
4.1
0.9
21.5
8.2
14.5
1.8
103.6
15.6
54.8
20.1
2.5
89.8
15.1
2.3
1.5
10.5
159.7 10000091
86.6 10.000091
63.1 10.000091
157.6 10.000172
6.8 10.000014
2.2 10.000014
3.3 10.000014
85.7 1 0.00114
64.3 0.00114
134.4 10.000387
70.0 10.000387
197.2 0.000387
29.7 10.000387
14.5 10.000102
1.8 0.000102
103.6 10.000102
15.6 10.000102
77.3 0.000102
104.9 10.000102
3.8 10.000033
10.5 10.000017
0.0146
0.00792
0.00578
0.0271
0.0000975
0.0000311
0.0000466
0.0973
0.0731
0.0520
0.0271
0.0764
0.0115
0.00148
0.000171
0.0105
0.00151
0.0078
0.010
0.00012
0.00018
5 8 8 5 8 7 7 8 1
71
81
_____ I ______ I ___ I _____ I ____
0.0433 -0.0287
3.507 3.515
3.074 3.080
18.880 18.907
0.000 10.0000975
0.000 10.0000311
0.000 0.0000466
0.0433 0.141
-8.011 -7.938
-1.429 -1.377
0.000 0.0271
-0.433 -0.357
0.000 0.0115
0.000 0.00148
0.000 0.000178
0.000 0.0105
0.000 0.00158
-1.299 -1.291
2.512 2.52
0.953 0.95:
0.000 0.00018
3
5I
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
62
0.229 10.00035
0.229 10.00035'
0.229 10.00035
0.384 10.00099'
0.116 10.90E-4t
0.116 10.90E-4,
0.116 10.90E-4
0.894 10.0053
0.894 10.0053
0.500 10.0016
0.500 10.0016
0.500 0.0016
0.500 10.0016 i
0.289 0.000561
0.289 10.000561
0.289 0.00056:
0.289 10.000561
0.289 10.000561
0.289 0.00056!
0.183 10.000221
0.128 10-00011
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I IPIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
IPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. OVER PIPE
INO. I NODES I (US GPM)j (IN) (IN) # (FT) (FT) (PSI) (PSI)
1 - 1- 1 -_____________ 50I 0.0 I - 0.000
85
86
87
90
91
93
94
95
96
97
98
99
1100
101
1102
1103
I-
IAN 1.0
82 91 1
91 92
92 93
88 82
88 89
87 88 I
838 87 ]
83 96
65 83
46 65
29 46
86 82
85 86
860 85
84 97
66 84
0.00
0.00
0.00
4.76
0.00
4.76
4 .76
14.76
14 .76
14 .76
14.76
16.65
16.65
16.65
16.65
16.65
10.02 C
10 1'
6.07 C
6 2
6 i1
6 I
4.03 C
4 2
4 6
10.02 C
10 1
4.03 C
4 I
4 8
6.07 C
6 4
6
6
6
6.07
6
6
6
7.98
8
8
7.98
7.98
8
8
8
7.98
8
8
8
10.02
10
6.07
6
6
6
6.07
6
6
7.98
8
8 7.98
STATIC TOTAL IROUGHI WATER VELOC.ISTATIC ITOTAL
IHEAD LOSSIHEAD LOSS
I (PSI) (PSI)
S AM TT
SAX
HE
GV
TT
SAM
SE
HE
SAM
TT SAM
GV
IHE
7SAM
SSE
IHE
LGV
ITT
CSAM
6SE
2HE
ITT
CSA•M
2HE
ITT
CSAM
CSAlM
5SE
2GV
ISR
CSAM
ISE
IGV
ITT
CSAM
ITT
CSAM
2SE
3HE
1GV
CSAM
7SE
3HE
CSAM
2HE
ITT
CSAM
IROUGHI WATER IVELOC.j NESS IVELOCITYI PRESS.
ICOEFFI(FT/SEC)l (PSI) I
1.0 50.0
16.0
14.0
3.0
30.0
152.1
20.0
24.0
1.0
14.7
166.9
2.0
32.0
66.0
16.5
6.2
0.9
8.8
206.1
24 .7
4.1
8.8
14.2
5.0
9.8
1.5
31.3
25.1
2.2
19.5
112.0
5.0
1.1
9.8
1.0
14.7
48.5
8.2
6.2
0.9
168.5
28.9
6.2
14.3
5.0
9.8
1.5
0
___ -________ 1 _____1____ I- ________________ - 1_______________ - 1______
_________ -___________I__________I___________ _____ ________ ______
IX-82
U3TB Hose St
J-1AY.kJ.�,I � A Kevision U Attachment D
PAGE b 15
51.0 0.000
63.0 0.000
196.1 0.000
15.7 10.00000421
1 1 200.9 0.000 1
98.4 10.000049 1
243.8 10.000049
28.9 10.000012
1.5 10.000012
78.1 10.000012
127.9 0.000012
15.7 10.0000053
63.8 10.000061
203.5 0.000061
29.1 10.000016
1.5 10.000016
0
0.000
0.000
0.000
.0000669
0.000
0.00483
0.0120
0.000373
0.0000193
0.00101
0.00165
0.0000836
0.00391
0.0125
0.000469
10.0000242
0.0866 0.0866
0.346 0.346
0.000 0.000
-0.130 -0.130
0.303 0.303
3.811 3.815
5.196 5.208
-5.846 -5.845
-0.650 -0.650
3.248 3.249
0.433 0.435
0.000 10.0000836
3.681 3.685
5.196 5.209
-5.846 -5.845
-0.650 -0.650
120
120
120
62
120
62
62
62
62
62
62
62
62
62
62
62
_1
0.000 0.000
0.000 0.000
0.000 0.000
0.0600 l0.24E-4i
0.000 0.000
0.164 0.00018
0.164 10.00018
0.0946 10.60E-4
0.0946 10.60E-4
0.0946 10.60E-4
0.0946 0.60E-4
0.0677 10.30E-4
0.185 10.00023
0.185 10.0002:
0.107 10.76E-'
0.107 10.76E--
HYDRAULIC CALCULATIONS .- PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS
IPIPEI PIPE FLOW I NOM ACTUALI CODE LENGTH I LENGTH I PER FT. lOVER PIPE
NO. I NODES (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)
I STATIC TOTAL IROUGHI WATER VELOC. I IHEAD LOSSIHEAD LOSS NESS IVELOCITYI PRESS.I
I (PSI) I (PSI) ICOEFFI(FT/SEC)i (PSI) I
I I I I I II I I I - 1_____________ 1 ________________I_________I_____ 1____ _________
1104
105
1106
1110
1300 1
1 1
1302
1303
1304 1
1305 1
1500
1501
1502
1503
1504
1505
1
-I69.6 10.00
3.248 I 3.249 I I 0
47 66
28 47
51 812
102 64
200 24
201 58
202 201
831 202
201 57
97 400
400 401
401 402
96 403
403 404
404 405
16.65
16.65
0.00
31 .40
1.43
20.66
37. 12
37.12
16.46
0.00
0.00
0.00
0.00
0.00
0.00
7.98 CSAM
8 4SE
8 2GV
8 I1SR
7.98 CSAM
8 ISE
8 I1GV
8 ITT
7.98 CSAM
8 ITT
8 IGV
8 ISE
10.02 CSAM
7.98 CSAM
8 5SE
8 IGV
8 ITT
6.07 CSAM
6 1GV
6 4HE
10.02 CSAf
10 2TT
6.07 CSAM
6.07 CSA"
6 ISE
6 1GV
6 2HE
6.07 CSAI
6 IRE
6.07 CSAJ
6 2SE
6 4HE
6 IiTT
6 IGV
4.03 CSA
4 3SE
4 1TT
4 2GV
6.07 CSA
6 1HE
6.07 CS•
6 ITT
6 2SE
6 3 HEf1 M
6 I1G\
4.03 CS)
4 1Tr
4 3S1
4 2G•
.1 ______________________ I _____________________ I _____________________________ I __________________________________ I __________________ I _____________________ I _______________________ I _____________________ I _______________________ I ___________
IX-83
U3TB Hose St
ZJVlI ¥ xL.,1 .L-I - IJ.. A - NuI,1UIb V Attachment D
PAGE L)I
4
M
M
M km
EM
v
27.8
20.1
2.2
19.5
115.0
5.0
1.1i
9.8
1.0
33.1
3.8
17.0
0.5
136.5
25.1
1.1
9.8
80.0
0.9
8.2
482.5
29.4
2.7
89.0
4.1 I 0.9
4.1
26.2
7.0
132.7
28.0
28.0
30.0
3.0
52 .2
30.0
20.0
4.0
7.8
7.0
132.3
30.0
28.0
21.0
3.0
47.0o
20.0
30.0
4.0
130.9 10.00
55.0 1
0.5 10.0¢
172.5 10.17
89.1 10.0
511.9 10.0
2.7 10.0
98.1 10.0
33.2
221.7
106.2
14.8
214.3
101.0
0016 0.00112
0016 0.00211
0.000 0.000
00017 10.0000086
71E-6 10.0000295 1
00091 0.00815
00023 0.0120
00271 0.000731
00060 I0.00589
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
_________ 1__
3.248
0.433
0.000
0.000 10
-4.547 1
-0.650 1
8.877 1
3.464
0.000
0.000
41.354
-3.334
0.000
41.354
-3.334
3 .249 1 6
0.435
0.000
.0000086
-4.547
-0.641
8.889
3.465
0.00589
0.000
41.354
-3.334
0.000
41.354
-3.334
52 0
62 0
20 0
62 0
62 10.0
62 1 0
62 1
62 1
62 1
120
120
120
120
120
120
.107 10.76E-41
.107 I0.76E-41
II II
.000 0.000
.128 10.000111
0917 I0.56E-61
.229 10.000351
1 1
0.151 10.000151
0.412 10.0011
0.183 10.00022
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
HYDRAULIC CALCULATIONS -" PIPE CHARACTERISTICS
I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS STATIC I TOTAL IROUGHI WATER I VELOC.
IPIPEI PIPE FLOW NOM ACTUALI CODE LENGTH LENGTH PER FT. lOVER PIPE HEAD LOSSIHEAD LOSS NESS IVELOCITYI PRESS.
NO. I NODES (US GPM)I (IN) (IN) N (FT) (FT) I (PSI) I (PSI) I (PSI) I (PSI) ICOEFFI(FT/SEC)I (PSI)
I_ _ _ _ 1 _ 1 _ 1 _ 1
1 ___________ I ___________ I_______________
1550
1551
552
600
160
160
61
61
160
16
1
7
1
16
552 550
550 551
552 833
57 600
1 24 601
2 602 24
1I 601 611
.2 1 611 612
21 602 621
51 1 61 651
19 719 23
25 18 725
26 726 18
27 18 727
750 700 701
751 701 16
752 702 17
753 21 703
754 704 602
I 125.54
6
125.54
1 1/2
1 1/2
0.00
6
6
6
0.00
1 1/2
1 1/2
1 1/2
6.52
18
5.09
8
8
18
0.00
6
6
0.00
0.00
6
6
0.00
i 1/:
I1 1if
39.68
8
9.69
12
13.65
12
3.97
12
13.65
8
13.65
13.65
16.21
8
5.09
8
8 8
18
6.07 CSAM ITT
1.61 CSAM
2SE
1GV
6.07 CSAM
ISE
ITT
IGV
1.61 CSAM
1TT
2SE
1GV
7.98 CSAM
ISE
7.98 CSAM
SSE
2HE
1GV
6.07 CSAM
2SE
ITT
6.07 CSAM
6.07 CSAM
3SE
ITT
1.61 CSAM
2 ITT
2 2SE
2 1GV
7.98 CSAM
2HE
11.20 CSAM
I1GV
11.20 CSA4
1GV
11.20 CSAM
1GV
7.98 CSAM
4HE
11.20 CSAM
7.85 CSAM
7.85 CSAM
ITT
7.98 CSAM
4SE
1HE
I1TT
IGV
1 _ __ __ _. _______ I _____ I _____ I ______ I _____ I ______ I ___ I
IX-84
U3TB Hose St
A1VL•lNLIlVILlN" " I.) I\CV Iblul U Attachment D
21.3
30.0
28.8
8.0
1.0
11.0
14.0
30.0
3.0
13.5
8.0
8.0
1.0
10.8
5.0
123.0
25.1
5.0
1.1
4.5
28.0
30.0
1.0
3.6
42.0
30.0
49.1
8.0
8.0
1.0
5.9
5.0
6.8
2.3
4.5
2.3
2.1
2.3
72.8
8.0
29.3
41.9
26.0
10.1
58.7
20.1
2.5
9.8
1.1
51.3 0.000761 0.0391
37.8 0.486 18.350
58.0 0.000 0.000
30.5 0.000 0.000
15.8 10.000002810.0000449 1
154.2 10.00000181 0.000277 1
62.5 0.000 0.000
1.0 0.000 0.000
75.6 0.000 0.000
66.1 0.000 0.000
10.9 0.000080 1 0.000875
I 1 9.1 10.619E-6 10.0000056
6.8 10.000001110.0000079
1 1 4.4 10.118E-6 10.00000052
I I 80.8 10.0000131 0.00113
29.3 10.000002610.0000783
41.9 10.00000661 0.000276
36.1 I0.000014 0.000534
I 1 92.1 l0.00000181 0.000166
II
PAGE L>0
0.000 0.0391 12
5.196 23.546 12
0.000 0.000 12
4.547 4.547 12
0.000 10.0000449 1
1 1 -1.429 -1.429
3.248 3.248 1
0.000 0.000 1
-0.433 -0.433 1
5.240 5.240
0.000 0.000875
0.000 10.0000056.
II
0.000 10.000007 9
0.000 10.000000521
1 1 0.563 1 0.564 1
0.217 0.217
-0.217 -0.216
0.606 0.607
-0.0866 -0.0864
0
0
.0
20
62
62
20
.20
120
120
62
86
86
86
55
55
86
66
62
1.394 10.0131
19.785 2.634
0.000 0.000
0.000 0.000
0.0418 10.11E
0.0327 10.71E
0.000 0.000
0.000 0.00C
0.000 .0QOC
0.000 0.00(
0.254 10.000
II
0.0315 I0.67E
0.0445 10.13E
0.0129 10.11E
0.0876 10.51E II
0.0445 10.13E
0.0905 1o.55E
0.107 10.771
0.0327 10.711 II
II
II
-I-
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I I PIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
IPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE
NO. I NODES I (US GPM)j (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)
STATIC TOTAL IROUCHI WATER VELOC.
STATIC ITOTAL HEAD LOSS HEAD LOSS
(PSI) (PSI)NESS IVELOCITYI PRESS.
ICOEFFI (FT/SEC) I (PSI)
I I I I I __ __
271.8_ I0.000 1I 0.000
175
175
175
175
1
Is
5 705 704 1
6 1 727 705 1
-7 706 704 1
8 923 706 1
60 1 27 720 1
1 1 61 1 720 721 1
62 919 723
63 724 719
00 928 802
02 1 802 803
803 834 800
804 1 800 801
805 56 805
806 49 849
807 1 849 814
7.9 - CsM 22.
I -
3.97
3.97
1.13
1.13
16.21
16.21
9.69
39-68
0.00
0.00
0.00
0.00
0.00
0.00
0.00
221.97.98 CS 8 7S
8 2H
8 1'
7.98 CS
8 21
8 11
4.03 C€
4 8
4 4
4 1
4.03 C
4 12
4 4
4 i1
7.98 C
8 1
8.39 C
8 2
8.39 C
8 1
7.85 C
6.07 C
6 1
6 1
6 2
4.03
4
4
4
4
6.07
6
6
5.05
5
5 7.98
8
8
4.03
4
4
4
4
4.03
4
4 4
•AM
LE
•E
rT
SAM
HE
TT
SAM
SE
HE
GV
SAM
SE
HE
GV
"SAM SE
:SAM
HE
SAM
LGV
SAM
SAM
ITT
IGV
2SE
CSAM
2HE
ITT
4SE
1GV
CSAM
3SE
IHE
CSAM
7SE
4HE
CSAM
IHE
ITT
CSAM
3SE
2HE
1TT
IGV
CSAM
ISE
ITT
1GV
I~~~~~~~~~~~ II___ __ ___ _____I___I___I__
IX-85
U3TB Hose St
t-1Yil-liNL)1V11-,4 I 1.) Attachment D
35.1 5.0
9.8
141.3
9.2
17.9
197.0
23.6
4.7
0.6
178.4
35.3
4.7
0.6
75.5
4.2
17.0
5.3
12.5
1.3
26.0
33.8
30.0
3.0
28.0
115.1
8.0
20.0
40.0
2.0
30.9
42.0
7.0
121.8
84.0
20.0
25.8
8.5
33.1
84.1
30.0
8.0
20.0
2.0
2.5
10.0
20.0
2.0
PAGE : L->iE
I 271.8 100000011 0.000307
168.3 I0.617E-6 0.000104
225.9 10.00000301 0.000696
1 I
219.0 J0.00000301 0.000675
1 1 1 1
79.7 10.000018 I 0.00147
1 1 22.3 10.000014 1 0.000324
13.8 10.000005010.0000702
26.0 0.000047 I 0.00124
94.8 0.000 1 0.000
185.1 0.000 0.OOC
79.9 0.000 0.004
225.8 0.000 0.00
67.4 0.000 0.00
144.1 0.000 0.00
34.5 0.000 0.OC
__________________________ I _____________ I ____________________ I -
0
0
0
0
0
7.448 7.448
0.866 0.866
1.645 1.646
-7.058 -7.058
0.650 0.651
0.000 0.000324
0.000 10.0000702 I
0.000 0.00124
3.248 3.248
3.551 3.551
-7.794 -7.794
-4.027 -4.027
-11.562 -11.562
2.728 2.728
0.000 0.000
62
86
62
62
56
56
59
86
120
120
120
120
120
120
120
0.0254 I0.43E-5
0.0254 10.43E-5
0.0284 I0.54E-!
0.0284 J0.54E-!
0.104 10.72E-
0.0942 10.59E
0.0563 10.21E
1 0.263 10.0004
0.000 0.000
0.000 0.00c
0.000 0.00(
0.000 0.00(
0.000 0.00,
0.000 0.00
0.000 0.00
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
.tAAVILINLJIVI-•L,14 1 A J
PAGE rlej
I I PIPE DIAMETERI PIPE/FTG TOTAL IHEAD LOSSIHEAD LOSS I STATIC TOTAL IROUGHI WATER I VELOC.I
IPIPEI PIPE I FLOW NOM ACTUAL[ CODE LENGTH LENGTH I PER FT. lOVER PIPE JHEAD LOSSIHEAD LOSS NESS IVELOCITY1 PRESS.
. ... ,-, f I I (PSI) I (PSI) ICOEFFI (FT/SEC)i (PSI)
- I NODES I (US GPM)I (IN) (IN) I#I,".,.
__________________ I __________________________ I _______________________________ I ________________ I __________________
I _____________________ I _______________________ l................1 __________________ I _______________ I 1.169 I 1.169 I 0.000 I 0.000 I
1808
1809
1810 I
1811 1
1812
1813 1
814
1815I
1816
1819
1820
1821
822
1823
849 815
77 808
60 809
79 811
55 813
813 817
813 818
805 819
819 820
819 822
76 824
824 825
801 804
836 827
____ -_________ 1 -__________ 1______________ I___________________I__________ __________
IX-86
U3TB Hose St
Attachment D
AM 18.0 I0.00
4 4
4
0.00
2 1/2
2 1/2
0.00
4
4
0.00
3
3
3
0.00
8
8
8
0.00
2 1/2
2 1/2
0.00
8
0.00
8
0.00
6
6
6
0.00
6
6
6
0.00
8
8
18
0.00
6
6
6
0.00
3
0.00
5
5
000 I
4.03 CS
4S
I C
2.47 CS
11
1(
4.03 C,
2)
3.07 C:
4
1
2 7.98 C
4
4 1
2.47 C
7.98 C
7.98
6.07
6.07
7.98
6.07
3.07
5.05
jAM
LE
rE
lv
lAM
SAM
ST
GV
SAM
SE
TT
SAM
SE
TT
GV
SAM
SE
HE
ITT
SAM
"ITT 1GV
CSAM
1GV
CSAM
ISE
CSAIM
IHE
ITT
IGV
CSAM
ISE
IHE
1GV
CSAM
2SE
ITT
1HE
CSAM
ISE
1HE
1GV
CSAM
ITT
CSAM 4HE
8SE
18.0
40.0
4 .0 2.0
1.0
12.0
1.0
28.1
20.0
20.0
51.5
28.0
15.0
2.0
62.7
68.2
34.1
33.1
1.0
12.0
1.0
1.5
3.8
6.0 .
17.0
6.6 6
7.0
30.0
3.0
16.8
14.0
7.0
3.0
32.0
34 .1
33.1
8.5
23.3
14.0
7.0
3.0
5.5
15.0
121.5
20.0
96.0
64.0
14.0
68.1I
96.5
198.1
14.0
5.3 I
23.0
46.6
40.8
107.7
47.3
20.5
237.5
_______ 1_____ _____ 1_____ ____________ ............ I1_________ _1 _____
(FT I... . . . ýP j
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
0.000
1.169
-0.433
-2.165
-3.681
-13.207
0.000
-1.169
2.901
-4.114
-4.114
-13.943
0.000
0.000
-7.483
1.169 12
-0.433 i1:
-2.165 I:
-3.681 1
-13.207 1
0.000 I
-1.169
2.901
-4.114
-4.114
-13.943
0.000
0.000
-7.483
20
20
20
20
20
120
120
120
120
120
120
120
120
120
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.OOc
0.000 0.000
0,000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I IPIPE DIAMETERI PIPE/FTG TOTAL HEAD LOSSIHEAD LOSS
IPIPEI PIPE FLOW I NOM ACTUALI CODE LENGTH I LENGTH PER FT. lOVER PIPE
INO. I NODES I (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)
STATIC TOTAL IROUGHI WATER I HEAD LOSSIHEAD LOSS INESS IVELOCITYI
I (PSI) I (PSI) ICOEFFI (FT/SEC)
VELOC.
VELOC. PRESS.
(PSI)
I I I I ______________ I ________ _________ I __________ _________ I _________ I _____ _______ I ______ 0.000 I -3.992 -3.992 1: 20 I 0.000 I 0.000
1824 1
I 1
1 1
826 1
1 1 1 1
1827
1 1
1828 1
1 1 1829 1
1831
832
833
1834
1835
1836
1837
1839
83
8
1
309.5 I 0.000 II - , -
8
8
1
35 836
24 826
02 855
00 839 3
839 831 3
42 837
61 832
98 552
54 834
73 835
833 828
828 829
96 838
I -
____ I _______ I _________ I ____ I _____ I ______ I _____ I ______ I ___ I ____ I ____
IX-87
U3TB Hose St
ZILII!¥1J •Nlj-lvl~ul 1 x A •'
PAGE C)ZO
0.00
0.00
0.00
7.12
7.12
0.00
0.00
25.54
0.00
0.00
0.00
0.00
14.76
6
6
6
6
6
6
6
6
6
6
6
6
6
10
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
6
].
I
6.07 CSAM
I1GV 5SE
3HE
4TT
1CV
6.07 CSAM
ITT
1HE
1GV
6.07 CSAM
ITT
1GV
1HE
ISE
6.07 CSAM
ITT
6.07 CSAM
10.02 CSAM
2HE
6.07 CSAM
ISE
IGV
ITT
6.07 CSAM
6.07 CSAM
2SE
2HE
2TT
1GV
6.07 CSAM
ITT
2SE
2HE
1GV
6.07 CSAM
9SE
2TT
6.07 CSAM
8SE
2HE
ITT
6.07 CSAM
1HE
1GV
ITT
63.5 3.0
70.0
21.0
120.0
32.0
6.3
30.0
7.0
3.0
4.4
30.0
3.0
7.0
14.0
2.3
8.8
3.0
11.0
22.0
9.9
14.0
3.0
30.0
11.2
28.6
28.0
14.0
60.0
3.0
24 .5
30.0
28.0
14.0
3.0
75.9
126.0
60.0
100.0
112.0
14.0
30.0
62.4
2.1
0.9
8.8
1-1-1
KeVlsion u Attachment D
309.5 0.000
46.3 0.000
58.4 0.000
11.1 10.000271
3.0 10.000271
33.0 0.000
56.9 0.000
11.2 10.000761
133.6 0.000
99.5 0.000
261.9 0.000
256.0 0.000
74.2 10.000049
0.000
0.000
0.000
0.00301
0.000812
0.000
0.000
0.00850
0.000
0.000
0.000
0.000
0.00364
-3.992
0.000
0.823
-3.464
0.000
0.000
0.0433
1 .429
-8.531
-8.314
-0.684
-28.112
0.000
-3 .992 1:
0.000 1
0.823 1
-3.461
0.000812
0.000 1
0.0433
1.437
-8.531
-8.314
-0.684
-28.112
0.00364
20
20
20
62
62
.20
120
120
120
120
120
120
62
0.000 0.000
0.000 0.000
0.000 0.000
0.412 10.0011
0.412 10.0011
0.000 0.000
0.000 0.000
1.394 10.0131
0.000 0.000
0.000 0.000
0.000 0.000
0.000 0.000
0.164 0.000181
HYDRAULIC CALCULATIONS -- PIPE CHARACTERISTICS
I I IPIPE DIAMETERI PIPE/FTG I TOTAL IHEAD LOSSIHEAD LOSS
JPIPEI PIPE I FLOW NOM ACTUALI CODE LENGTH I LENGTH PER FT. OVER PIPE
INO. I NODES I (US GPM)I (IN) (IN) I # (FT) I (FT) I (PSI) I (PSI)
STATIC TOTAL IROUGHI WATER I VELOC.IISTATIC I TOTAL IROUGH1 WATER I VELOC.1 HEAD LOSSIHEAD LOSS INESS IVELOCITYI PRESS.l
(PSI) I (PSI) ICOEFFI(FT/SEC)I (PSI) I
12 .0 0.00I _ _ _ _ _ _I_ _ _ __ _ _I_ _ _ _ 704 3.2
1 - 1 -****.... ____________I _________ 179.8 I 0.000 0.000 I1840 1
I 1
1841 1
842
850
1851
1860
861
1922
925
931
1932
I-
838 845
75 823
809 810
93 850
89 851
97 860
860 861
19 919
23 923
928 28
29 929
I 0.00
0.00
0.00
0.00
0.00
16.65
0.00
9.69
39.68
0.44
0.44
____________________ I __________________ I ___________________________ I ______________________________ I ________________ I __________________ I ____________________ I __________________ I ____________________ I�..................-I ________________ I ______________ I
IX-88
U3TB Hose St
1ýllvjkl-li 141-11VIA-11 1 - - -
PAGE Dzi
4
4
4
4
8
8
8
3
3
6
6
6
4
4
4
4
6
6
4
4
4
4
8
8
8
4.03 CSAM 5HE
2SE
ITT
IGV
7.98 CSAM
ITT
2SE
IHE
3.07 CSAM
ISE
1GV
6.07 CSAM
1GV
2SE
ITT
4.03 CSAM
3SE
ITT
IGV
IHE
6.07 CSAM
1GV
IHE
4 .03 CSAM
3HE
3SE
ITT
1GV
7.85 CSAM
7.98 CSAM
3SE
ITT
XGV
7.98 CSAM
7.98 CSAM
117.8 1
20.0
20.0
20.0
2.0
32.0
33.1
34.1i
8.5
23.3
7.0
1.0
12.5
3.0
28.0
30.0
12.9
30.0
20.0
2.0
4.0
51.5
0.9
2.1
119.8
12.0
30.0
20.0
2.0
29.2
21.2
15.1
9.8
1. I 98.2
2.5
Kevslon U Attachment D
179.8 0.000 0.000
107.7 0.000 0.000
31.3 0.000 0.000
73.5 0.000 1 0.000
68.9 0.000 1 0.000
54.4 0.000061 0.00334
183.8 0.000 0.000
29.2 10.00000701 0.000205
47.2 10.000080 0.00379
I 1
98.2 10.229E.7 10.0000022
2.5 10.229E-7 10.572E-7
37.024 37.024
-13.943 -13.943
0.000 0.000
-2.598 -2.598
-2.382 -2.382
0.000 0.00334
38.020 38.020
0.476 0.477
12.774 12.778
0.000 10.0000022
0.000 10.572E-7
120 0.000
120 0.000
120 0.000
120 0.000
120 0.000
62 1 0.18!
120 0.00(
59 0.064:
62 0.25
1 56 10.0028
56 10.0028
I I- II I
0.000
0.000
0.000
0.000
0.000
S10.000231
1 0.000
2 10.27E-41
4 0.000431 II
II
0 10.52E-71
0 10.52E-71
"II-VI1LINJ IVI..IN 1 I - Revision 0 Attachment D
HYDRAULIC CALCULATIONS - NODE CHARACTERISTICS
COMPANY Nexus Technical Services Corporation IPAGE 20 A
I DESIGNER BY: CARL BALINGIT CHECKED: ODATE 2000 JAN 13
I CLIENT ComEd, Dresden Nuclear Power Station - Hose Station Hydraulic Analysis
PROJECT Ul DFP Out, 10% Degraded C-Factors, 10% Deg. U2/3 DFP
JOB NO. I U3TB Hose Station F-126
SPRINKLER/NOZZLE(N) POINTS I REFERENCE POINTS INPUT POINTS POINT I REQUIRED I
ELEVATION IDISCHARGE I K-FACTOR.
I I.. .. . . NO. JDEMAND GPM I P.S.I. I (FT) I {US GPM) II
IX-89
NO. IDISCHG. GPM P.S.I. NO. JDISCHG. GPM I....
1 500.000 I 1 149.932 5
I 2 145.818 5 16.00 0
I 3 143.004 516.000 1 1
I I 4I ~ I I510.800I S4 145.255
5 145.255 I 510.800
6 145.255 1 1 510.800
7 145.470 1 510.300
8 145.772 1 509.600
9 145.772 51509.600 1
I10 143.216 515.500 1I 126.458 554.200 1
12 143.216 515.500
131 145.684 509.800
14 1 145.900 509.300
15 1 145.987 509.100
16 1 145.206 510.900
17 1 145.552 510.100
18 1 145.898 509.300
19 1 145.854 509.400
201 144.987 511.400
21 145.333 510.600
22 144.952 511.500
23 144.950 511.5000
24 139.098 525.000
25 I 145.160 1 1 511.000
26 144.943 1 1 511.500
27 145.376 510.500
28 144.722 1 512.000
29 144.722 1 512.000 1 I
1 30 145.069 I 511.200
31 144.640 512.200
32 144.296 513.000
331 144.734 512.000
34 1 144.869 511.700 1
35 145.552 510.100
36 144.525 1 512.500
37 145.223 1 510.900
38 145.172 1 511.000
I 39 145.126 1 511.100 3 1 401 125.54 1 150.000 1 500.000
I 510.900
I 41 145.269 510.900
I I I 42 145.253 510.900
I 45 145.227 510.900
I 46 144.287 513.000
I _____ I______________ ______________ ______I______________ I______________ ............ ______________I______________ ______________I ___________ __________
Attachment D
U3TB Hose St HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS PAGE DC-3
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED
ELEVATION IDISCHARGE K-FACTORI
NO. IDISCHG. GPM P.S.I. NO. IDISCHG. GPM P.S.I. I NO. DEMAND GPM I P.S.I. (FT) I (US GPM)
47 144.287 513.000
48 137.123 529.500
49 134.524 535.500
50 134.091 536.500
51 133.095 538.800
52 144.869 511.700
53 125.650 556.000
54 125.650 556.000
55 125.652 556.000
56 125.652 556.000
57 125.652 556.000
58 126.299 554.500
59 126.299 554.500
60 126.296 554.500
61 126.325 554.400
62 122.809 562.500
63 119.729 569.600
1 64 138.636 526.000
65 141.039 1 520.500
66 141.038 520.500
67 138.636 526.000
68 127.076 552.700
691 138.636 5526.000
701 128.029 550.500
71 124.554 558.500 721 125.845 555.500 72 125.843 555,500 74 125.833 555.500
75 125.833 555.500
76 125.831 555.500
77 125.820 555.500
78 126.176 554.500
79 126.149 554.500
80 138.636 526.000
81 119.588 569.700
82 138.636 526.000
83 141.688 519.000
84 141.687 519.000
85 142.321 517.500
86 138.636 526.000
87 142.322 517.500
88 138.506 526.300
89 138.203 527.000
91 138.549 526.200
92 138.203 527.000
93 138.203 527.000
96 147.534 505.500
97 147.533 505.500
98 127.526 551.200
IX-90
I-luvil-I 14A-111- I - - -
U3TB Hose St HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS INPUT POINTS POINT REQUIRED
ELEVATION DISCHARGE
NO. IDISCHG. GPM I P.S.I. NO. IDISCHG. GPM P.S.I. NO. DEMAND GPM P.S.1. I (FT) (US GPM)
- 526.000
102 138.636
200 134.551
201 125.658
202 134.547
400 147.533
401 106.179
402 109.513
403 147.534
404 106.180
405 109.514
550 126.050
551 1 125.54 102.503
1 552 126.089
600 121.105
601 139.098
602 137.670
611 135.850
612 135.850
621 138.103
651 121.085
700 145.987
I701 145.423
702 145.336
703 144.726
I704 137.583
705 145.031
706 139.229
I719 144.951
720 144.725
721 144.724
723 145.377
724 144.952
725 145.898
726 145.898
727 145.898
800 141.975
801 146.002
802 141.474
803 137.923
804 146.002
805 137.214
808 126.253
809 128.461
810 128.461
811 129.830
812 133.095
813 138.859
814 131.796
815 130.627
K-FACTOR
I __________ I ________________________ I ________________________ I __________ I ________________________ I ________________________ I....................I ________________________ ________________________ ____________________ I _________________
IX-91
Attachment D
PAGE oz4- ,
526.000 535.500
556.000
535.500
505.500
601.000
593.300
505.500
601.000
593.300
554.500
566.500
554.500
566.500
525.000
528.300
532.500
532.500
527.300
566.500
509.100
510.400
510.600
512.000
528.500
511.300
524.700
511.500
512.000
512.000
510.500
511.500
509.300
509.300
509.300
518.300
509.000
519.500
527.700
509.000
529.300
554.500
549.500
549.500
546.000
538.800
525.500
541.800
544.500
100.00 12.400
Attachment D
U3TB Hose St HYDRAULIC CALCULATIONS -- NODE CHARACTERISTICS PAGE ,. 2 g.
SPRINKLER/NOZZLE(N) POINTS REFERENCE POINTS I INPUT POINTS POINT REQUIRED I I ELEVATION DISCHARGE I K-FACTORI
NO. IDISCHG GPM P.S.I. NO. IDISCHG. GPM P.S.I. NO. DEMAND GPM I P.S.I. (FT) I (US GPM) I
817 138.859 525.500
818 140.028 522.800
819 134.313 536.000
820 138.426 526.500
822 138.426 526.500
823 139.776 523.300
824 139.775 523.300
825 139.775 523.300
826 139.775 523.300
827 145.633 509.800 1
8281 126.773 552.920
829 I 154.885 I 488.000
831 138.012 527.500
832 126.281 554.500
833 126.089 554.500
834 134.180 536.300
835 134.157 536.300
836 138.150 527.080
837 145.253 510.900
838 147.530 505.500
839 138.013 527.500
845 110.506 591.000
849 131.796 541.800
850 140.801 521.000
851 140.585 521.500
855 137.813 527.900
860 147.530 505.500
861 109.510 593.300
919 145.377 510.500
923 132.172 541.000
928 144.722 512.000
929 144.722 512.000
IX-92
Attachmernt D
" WARNING: THE FOLLOWING PIPE(S) HAVE FLOW(S) SMALLER THAN 0.1 GPM
1 2 3 4 85 86 87 91 106 500
501 502 503 504 505 552 600 611 612 621
651 800 802 803 804 805 806 807 808 809
8i0 811 812 813 814 815 816 819 820 821
822 823 824 826 827 831 832 834 835 836
837 840 841 842 850 851 861
MAXIMUM UNBAILANCED HEAD LOSS- .00005 IN LOOP # 1
IX-93
A-MfNIJMLItN 1 1.
15X*
Revision 0 Attachment D
R-ýC- DZI --F UVz1
IP
1131R
IE Is
is
It! 761 R
IE
391 X is operating point for SPECIFIED pressure
Co-ordinates are
FLOW - 125.54
PRESSURE = 150.00
0 1635 3268 4901
FLOW
Pump Curve Input Point No. 40
IX-94
Volume 12
AMENDMENT 13
DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Volume Index
VOLUME 12 - REFERENCES
I. Fire Protection Program Audit and Open Item Closure
1. S&L closure of PLC Evaluation Report Open Items.
2. PLC Fire Protection Program Evaluation.
3. Fire Protection Modification Review.
11. Previous Commitment Review and Open Item Closure
1. Proposed Fire Protection Licensing Amendment (Open Item Closure).
2. Review of Fire Protection Requirements (12/2/85).
3. PLC Review of Previous Fire Protection Commitments.
4. NRC Fire Protection Commitment Matrix Status.
5. September 29, 1994, Review of Modifications Committed to Under 1978
SER.
6. March 15, 1993, Fire Protection Engineering Evaluation.
Ili. PLC Review of Procedures in Support of Technical Specifications
IV. Fire Protection Procedures
I. List of Fire Protection Procedures.
2. Fire Protection Program.
V. Pre-Fire Plans
VI. Suppression Effects Analysis
I
AMENDMENT 13
DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Volume Index
VOLUME 12 - REFERENCES (Continued)
VII. Fire Protection Reevaluation Project Plan
1. Fire Protection Evaluation Report.
2. Appendix R Fire Protection File Index
VIII. Fire Protection Evaluation Plan
IX. Audit/Inspection Reports, Responses and Closure
I. Fire Protection Closure Documentation and NFPA Review.
2. PLC Fire Detection and Alarm Survey.
3. PLC Fire Suppression System Survey.
4. PLC Fire Suppression Hydraulic Analysis.
5. PLC Technical Specification Evaluation.
6. PLC Supplemental Guidance Review.
7. PLC Suppression Effects Analysis.
8. Appendix R Fire Protection-Recommendation Summary, Rev. 15.
9. Annual Fire Protection - Audit (April 10-14 1989) Report.
10. August 18, 1989, Letter from PLC to CECo responding to finding of
Annual Fire Protection Audit.
11. Fire Protection for Quality Records.
12. Dresden Fire Protection Assessment January 9-11, 1989.
13. Offsite Quality Assurance Audit 12-87-Il. Open Item #03.
14. Dresden Station Site Quality Verification Audit 12-94-01.
2
AMENDMENT 13
DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Volume Index
VOLUME 12 - REFERENCES (Continued)
15. 1994 Trienmial Fire Protection Audit 12-94-01B.
16. Dresden Station Site Quality Verification Audit #12-95-10.
17. Site Quality Verification Audit # 12-96-13.
18. Triennial Fire Protection Program Audit 12-97-13.
19. Quality & Safety Assessment Audit CornEd 98-01.
20. Nuclear Oversight Audit 12-98-04.
3
AMENDMENT 13
DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Previous Commitment Review and Open Item Closure
Tab Title
1. Proposed Fire Protection Licensing Amendment (Open Item Closure)
2. Review of Fire Protection Requirements (12/2/85)
3. PLC Review of Previous Fire Protection Commitments
4. NRC Fire Protection Commitment Matrix Status
5. September 29, 1994, Review of Modifications Committed to Under 1978 SER
6. March 15, 1993, Fire Protection Engineering Evaluation
11-i
Volume 13
AMENDMENT 13
DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Fire Protection Supporting Calculations
Tab Title
1. Radiological Consequences of Fire in the Off-Gas System (NSLD Calc.
No. 2-78-D2&3)
2. Primary System (RPV) Makeup by Control Rod Drivc Mechanism Flow
(NSLD Calc. 3C2-0584-001 and 3C3-0382-001)
3. Timelines for Spuriously Open Electronic Relief Valves (Preliminary)
4. Isolation Condenser Inboard Valves Transfer Starters (EPED Calc. No.
6779-31-19-1)
5. Torus Water Temperature (Quad Cities NSLD Caic. No. 3C3-0779-001)
6. Control Rod Drive Pump Crosstie (MAD Calc. No. 81-568)
7. Spurious Valvc Operations Analysis (September 2, 1987)
8. System Supporting Documents
9. IE Information Notice 85-09 Analysis (Dresden 85-09 Analysis) Revision
0
10. Technical Basis of Dresden Station Fire Damper Surveillance Program,
August 1985
11. Evaluation for the Effects of the December Unit 3 Poly-urethane Fire
12. Safe Shutdown Appendix R Analysis for Dresden Nuclear Power Station
Units 2 & 3
13. Using the Service Water System as Backup for the Fire Water System
14. Electrical Cable Review Calculations (S&L Calc. Nos. 7927-05-19-1,
7923-06-19-2, 6972-62-19-1)
X.0-i
AMENDMENT 13 DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Electrical Cable Review Calculations
(S&L Calc. Nos. 7927-05-19-1, 7923-06-19-2, 6972-62-19- 1)
Paoe Title
X.14-1 Calc. For Consideration of Fire Induced "Hot Shorts," between Medium
and Low Voltage Cables (S&L Caic. No. 7927-05-19-1).
X.14-10 Appendix R "Hot shorts," between Medium and LV Cables in Common
Enclosures (S&L Calc. No. 7923-06-19-2).
X.14-50 Cable Ampacity Derating for Cable Trays Wrapped in 3M Fire Wrap
(S&L Calc. No. 6972-62-19-1).
X. 14-i
AMENDMENT 13
DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Appendix R Station Modification Meetings
Title Pan
Station Modification Meeting, January 27, 1984 XI.1-1
Station Modification Meeting, February 29, 1984 XI. 1-7
Station Modification Meeting, April 23, 1987 XI. 1-13
Station Modification Meeting, August 20, 1987 XI.1-19
Station Modification Meeting. September18, 1987 XI.1-26
Station Modification Meeting, October 23, 1987 XI.1-33
XI.1-i
I
AMENDMENT 13
DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
General Appendix R Meeting Notes
Title Page
April 6 and 7, 1987, Fire Protection Exemption Items Walkdown XI.2-1
August 3 and 12. 1987, Meetings to Prepare for Upcoming Appendix R Audit XI.2-9
April 6 and 7, 1987, Review of Draft SER (Meeting Notes) XI.2-36
August 17, 1988 Conference Call with NRC on Automatic
Depressurization System I OCFR50 Appendix R Concerns XI.2-43
February 2, 1989, Teleconference with NRC on Out-of-Service
Equipment XI.2-46
October 13, 1987, Meeting Notes XI.2-49
XI.2-i
AMENDMENT 13
DRESDEN 2 & 3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Letters and Memos
Title PA9e
February 11, 1985 Fusing of Control Power Transformers XI.3-1
December 15, 1987 Carbon Dioxide Monitoring for Fire Detection XI.3-3
December 29, 1988 Update of Dresden FHA and Appendix R Safe XI.3-21
Shutdown Analysis
September 7, 1989 Dresden Radwaste Upgrade Project XI.3-30
February 23, 1987 S&L letter from B. M. Barth to .1. J. McDonald (CECo), XI.3-33
discussing Fire Zone Designations on the Turbine Building Ground Floor
June 12, 1986 telecon between C. E. Ruth (S&L) and C. Ksobiech (CECo), XI.3-35
Extension of Preaction Suppression System Snubber Recorder Shack
May 5. 1997 NDIT No. S040-DH-0445 Standby Gas Treatment System XI.3-36
and the Appendix R Analysis
XI.3-i
COMED NUCLEAR DESIGN INFORMATION TRANSMITTAL
Z SAFETY-RELATED Originating Organization NDIT No. S040-DH-0445 SNON-SAFETY RELATED LI ComEd SREGULATORY RELATED Z Other (specify) S&L
Station Dresden Unit(s) 2&3 Page 1 of 2
Design Change Authority No.:
System Designation: 7500 - C om__
__________________________________________To J. Steiner - CornEd
Subject Standby Gas Treatment System and esindix R AwIvsi
C. M. Launi Division Mana er 5 Preparer Position P a Date
B. J. Andrews Project EnQineer . Reviewer Position Si nature Date
C. M_ Launi Division Manager Approver Position K __App 1 wver's Signature Date Status of Information: Approved for Use
Method and Schedule of Verification for Unverified NDITs:
Description of Information:
During the Dresden Independent Safety Inspection (ISI), a question arose about the HPCI turbine gland seal leak value (Question 3260-002). A gland seal leak value of 216 Ibm/hr was used in the room thermal response zalculation. This number is 10% of the leakage that would occur from a locked rotor condition resulting from a water slug damage in the turbine which is 2160 Ibm/hr (0.6 lbm/s)(UFSAR Section 6.3.3.1.3.2.1.5). Noncondensables are removed from the HPCI gland seal condenser by the gland seal exhauster (gland seal leak off blower) via the (cont'd on page 2)
XI.3-36
Purpose of Issuance:
This information is being issued to close out NTS Items 237-201-96-56101-01, 237-201-96-56101-02, 237-201-9656101-03 and 237-20196-56101-04. Since the SGTS does not need to be incorporated into the Appendix R safe shutdown analysis, the actions required by these NTS items are no longer required.
Source of Information:
UFSAR Section 6.3.3.1.3.2.1.5; Fire Protection Reports, Volume 2; Drawings M-49, Rev. QG; M-51, Rev. BF; M-269 shý 1, Rev. C; sh. 2, Rev. A; M-374, Rev. BP; M-529, sh. 1,Rev. D, sh. 2, Rev. A; Response to ISI Question 3260-002.
Distribution: E. Connell - CornEd, J. Dawn - CornEd, T. Behringer D. Bianchini - 23
File No.: CHRON No.: Project No.: 10128-040
AAVrJV'qNIVIc_•I,4i i-1
"PAIVA ,IAN "; V 11-1 N I I -
COMED NDIT. S040-DH-0445
NUCLEAR DESIGN INFORMATION TRANSMITTAL Page 2 of 2
Description of Information (Continued):
standby gas treatment system. During the ISI, it was assumed that failure of the gland seal exhauster could result in
failure of the gland seals resulting in the a leakage rate equal tothat of the locked rotor condition. For the 1 OCFR50
Appendix R scennrin faiiures to equipment oocur only as a result of damage from the fire. Single failures are not
required to be postulated. A fire that damaged the gland seal exhauster or cables that power and control the
exhauster would also prevent operation of the HPCI system and an alternate means of shutting down the reactor is
provided (isolation condenser/CRD pump per Fire Protection Reports, Volume 2). For the safe shutdown paths that
ust. trie HPCI system for reactor water makeup (C and D) for a fire in Fire Areas RB2-l and RB3-1, the gland seal
exhauster would be operable. However, during the ISI, it was thought that the Standby Gas Treatment System
(SGTS) is needed to accommodate the exhaust from the gland seal blower. The SGTS is not currently included in the
Appendix R analysis.
The assumption that the SGTS was needed to accommodate the exhaust from the exhauster was based on the failure
of the reactor building ventilation system due to loss of offsite power and no flow path through the reactor ventilation
system to the reactor building. However, review of P&IDs M-49 and M-269 sheets 1, 2 for Unit 2 and M-49 and M-529
sheets 1,2 for Unit 3 indicates that a path exists to the reactor building from the gland seal exhauster. This path is via
lines 2(3) 2320-3", 2(3)-7501-6" and 2(3)-7504-18" into the reactor building ventilation ducts.
Based on the existence of a pathway to the reactor building to accommodate the discharge flow from the gland seal
exhauster, the SGTS does not need to be included in the 10CFR50 Appendix R safe shutdown analysis.
Since a design basis accident is not postulated to occur with a fire, fuel damage is not postulated. Therefore, any
release to the reactor building will contain the normal operation source terms. The radiological consequences of this
release are bounded by the design basis accident (LOCA) since the number of curies released to the environment for
the DBA would be several orders of magnitude greater.
XI.3-37
AMENDMENT 13
DRESDEN 2&3
FIRE PROTECTION PROGRAM DOCUMENTATION PACKAGE
Microfiche Indcx
Microfiche Pocket Title
A This has been intentionally deleted.
B.C Technical Basis of Dresden Station Fire Damper
Surveillance Program, dated August 1985. (This
document contains "Licensing Classification of Fire
Dampers," Rev. I - See Pocket G, below.)
D,E Evaluation for the Effects of the Dresden Unit 3
Polyurethane Fire.
F Resolution of Consequences of the Dresden Unit 3
Polyurethane Fire, June 4, 1988.
G Licensing Classification of Fire Dampers, Rev. 2.
XII.0-i