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Copyright © 2007 OSIsoft, Inc. All rights reserved. Production Accounting: Cornerstone for Pacesetter MES Architecture Patrick Truesdale Senior Consultant Sidi Mohamed DRISSI SMAÏLI Director MIS Department

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Page 1: MES Architecture - cdn.osisoft.com...Manual Entry Real Time Data Acquisition ... Management System, Operating Expense, Security, Supply and ... Merox LPG Merox LSR Gasoline HDT/Reforming

Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Production Accounting: Cornerstone for Pacesetter MES Architecture Patrick Truesdale Senior Consultant 

Sidi Mohamed DRISSI SMAÏLI Director MIS Department

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Agenda 

l Business Challenge l Solution Description l Case Studies l Future Plans

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Global IT Business Integration

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Real­Time Business Process 

DCS, Instrumentation, Analyzers, RTDB (PI), Bar Coders, Inventory Levels, Gate Entry Security, Process Control, 

Environmental Monitoring Stations, Lab Sample Data Entry, Manual Entry 

Real  Time Data Acquisition

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Operation Business Process Applications 

Logistics, Operations, LIMS, EDMS, Balancing/Data Reconciliation, Production Accounting and Loss, Maintenance Management System, Operating Expense, Security, Supply and Distribution, Planning and Scheduling, Operations Monitoring, 

Environmental, and Quality Assurance 

Operations Management

Page 6: MES Architecture - cdn.osisoft.com...Manual Entry Real Time Data Acquisition ... Management System, Operating Expense, Security, Supply and ... Merox LPG Merox LSR Gasoline HDT/Reforming

Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Business Process Applications 

Global Management, Accounting and Financials, Administration Management, Purchasing, Materials Management, SCM, Asset 

Management, Invoicing and Cash Flow Management, Communication and Technology, Key Performance Indices (KPI), 

Government and Regulatory Reporting 

Business Management

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Typical Refinery MES Architecture 

Production Accounting •Receipts/Shipments 

•Stock •Yields •Utilities 

Consistent Consistent Economics Economics 

& & Process Process Models Models 

& & Data Data 

CORPORATE ACCOUNTING CORPORATE ACCOUNTING CORPORATE PLANNING CORPORATE PLANNING 

Maintenance Maintenance Planning Planning 

Production Planning Production Planning 

Scheduling Scheduling 

Process Process Simulation Simulation 

Operations Orders Operations Orders 

Target Setting Target Setting 

Asset Utilization Asset Utilization 

Profitability Profitability 

KPI KPI’ ’s s 

Quality Assurance Quality Assurance 

Process / Equipment Process / Equipment Monitoring Monitoring 

ADVANCED PROCESS ADVANCED PROCESS CONTROL CONTROL 

PRODUCT HANDLING PRODUCT HANDLING /STORAGE CONTROL /STORAGE CONTROL DCS DCS 

Business Business Information Information System (BIS) System (BIS)

Production Production Management Management System (MES) System (MES)

Real Real Time Time System System 

SCM SCM

Page 8: MES Architecture - cdn.osisoft.com...Manual Entry Real Time Data Acquisition ... Management System, Operating Expense, Security, Supply and ... Merox LPG Merox LSR Gasoline HDT/Reforming

Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Supply Chain Management – Logical Architecture 

Business Systems Business Systems ERP ERP 

Headquarters Headquarters 

Logistics Database Logistics Database 

Plant Database Plant Database 

Production Balance /Exchange 

Business Financial 

Accounting 

Sales 

• Marketing & Sales • Feedstock Purchasing • Trading •Supply Operations 

Feedstock/Product Distribution & Transportation 

Planning & Scheduling 

Performance Metrics 

Operation Monitoring 

Production Accounting 

Supply Chain Management Supply Chain Management Database Database 

3 rd Party Exchanges & Processing 

Customers 

Inventory Management 

Marketing Forecast (Demands) 

Production 

Feedstock Planning 

Terminals Database Terminals Database 

Inventory  Production Accounting 

Receipts Shipments

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Where are the Losses? –  Supply Chain 

Primary Depots 

Refinery Terminals 

Refinery Depots 

Retail Stations

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Types of Errors 

Gross  Substitution of redundant value. 

Bias 

Substitution of redundant value. 

Random Treatment using a mathematical algorithm. 

Description  Detection  Correction Errors 

Error occurring without any probability. 

Error occurring without any probability but may be a function of time or temperature. 

Error occurring with statistical distribution around mean, μ, and a standard deviation, σ 

Values exceeding +/­ 3 standard deviation, σ. 

Three or more values exceeding +/­1.5 standard deviation, σ or 7 continuous values that are on either side of the mean, µ. 

Imbalances that remain after correction of gross and bias errors.

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Impact of Refinery Losses ­ Typical 

l With poor instrumentation and procedures: u  1.5 ­ 2.5% Mass 

l With average instrumentation and procedures: u  0.7 – 1.5% Mass 

l With good instrumentation and procedures: u  < 0.5% Mass 

l Good information enhances all business functions: u  Planning and Scheduling u  Process Operations u  Management Decision

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Industry Relative Benefits 

Benefits(M$/year) Stand Alone Application Prod Data Integration ERP Integration 

Health,safety and environment 

Production Management 

Planning optimization 

0  0.5  1  1.5  2  2.5  3  3.5  4 

Material Management 

Financial/Accounting 

Laboratory(LIMS) 

Project/design engineering 

Corporate planning 

Document Management 

Maintenance Management 

Performance Monitoring 

Operations scheduling 

52% 

37% 

11% 

Courtesy: “Hydrocarbon Processing”

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Benefit Potential MM$/Yr 

0.0  5.0  10.0  15.0  20.0  25.0  30.0 

Hydrocarbon Losses 

Asset Utilization 

Planning & Scheduling 

Saleable Yield 

Productivity 

Crude Selection 

EII 

Inventory Reduction 

Quality Giveaway 

HSE 

Mechanical Reliability 

Chemical & Catalyst 

$1.35/bbl total For ca 160,000 BPD

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Agenda 

l Business Challenge l Solution Description l Case Studies l Future Plans

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

RTDB (PI) 

Relational Data Base 

PADR Application Scope 

Stock,  Yield, and Utilities, 

Unreconciled Reports 

Receipts/Shipments 

Business Processes 

Analyst 

Trial Balances

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

RTDB (PI) 

Relational Data Base 

PADR Application Scope 

Stock,  Yield, and Utilities, 

Unreconciled Reports 

Receipts/Shipments 

Stock,  Yield, and Utilities, 

Reconciled Reports 

Business Processes Analyst 

Trial Balances Reconciliation

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

RTDB (PI) 

Relational Data Base 

PADR Application Scope 

Tank Composition (Crude and Blends) 

KPI Reporting 

Stock,  Yield, and Utilities, 

Unreconciled Reports 

Receipts/Shipments 

Stock,  Yield, and Utilities, 

Reconciled Reports 

Business Processes Analyst 

Trial Balances Reconciliation Engineers Planners

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Balances: Production Accounting Results 

Type of Balances §  Volume §  Mass §  Tank §  Product §  Fuel gas/Fuel Oil §  Bitumen/Lube/Coke/Sulfur §  H2 §  Steam §  Environmental (NO, SO, Greenhouse)

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

PADR Business Process Flow 

Period End Cutoff Data Period End Cutoff Data 

Gross Error Detection and Diagnostics 

Gross Error Detection and Diagnostics 

Trial Balancing Trial 

Balancing Resolution or Reconciliation Resolution or Reconciliation  Checking Checking 

Modifications Adjustments Modifications Adjustments Refinery 

Configuration Models 

Refinery Configuration 

Models 

Measurements Movements Lab Data 

Meter Tickets Surveyor Documents 

Tank Inventories Blends 

Measurements Movements Lab Data 

Meter Tickets Surveyor Documents 

Tank Inventories Blends 

Results Generation Results 

Generation 

Manual Input 

Automatic Data Collection 

Reconciled Balances, Yield, Loss and Inventory 

Reporting 

Reconciled Balances, Yield, Loss and Inventory 

Reporting 

Production Management Data Base 

Production Management Data Base 

Integrate with Other Systems 

(SCM, SAP, LP, etc) 

Integrate with Other Systems 

(SCM, SAP, LP, etc)

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Gross Margin versus Weight Loss 

0.2 

0.4 

0.6 

0.8 

1.2 

1.4 

1.6 

1.8 

Jan­01 

Feb­01 

Mar­01 

Apr­01 

May­01 

Jun­01 

Jul­01 

Aug­01 

Sep­01 

Oct­01 

Nov­01 

Dec­01 

Jan­02 

Feb­02 

Mar­02 

Apr­02 

Month 

Wt %

 Weigh

t Los

50 

100 

150 

200 

250 

Gross Margin in k$ 

Weight Loss  Gross Margin 

KPIs Reporting

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Benefit of Daily Plan vs Actual Information 

Where did it happen? •  Models •  Process •  Data Quality 

Before (Monthly) 

Plan/Schedule 

1  2  3  4  5  6  7  8  9  10  11  12  13  14 Time (Weeks) 

Actual Operation 

•  Capacity 

•  Utilization 

•  Production rate 

•  Quality 

•  Energy 

•  Yield 

•  Reliability 

•  Environmental 

What went right?? 

What went wrong?? 

After (Daily)

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

PADR Reporting 

Reduce Hydrocarbon Loss by 0.5%: Prize = 56,000,000 BPY x 0.5% Loss reduction  x 50% capture x $62.50/Bbl = $8,750,000 /year 

Cornerstone for KPIs reports: •  Actual Unit Balance versus Plan •  Unit Constraint Cost Versus Plan •  Energy Intensity Index •  Clean Product Yield Growth •  Qualities Give­away Cost 

Must find daily discrepancies/data problems that cause imbalance 

PADR must achieve plant wide balance 

Delta  Economics$/day Plan Reconciled Product  Measured 

37 174 210 1 37 72 ­35 

Gross Margin :73 1,502 586 844 72 

1,429 1,047 382 

8,650 8,687 8,603 Production 3,890 4,400 360 

6,350 2,300 

­ 83 Gain/ Loss 

3,716 3,584 ULSD 4,610 4,672 PUL 361 347 FUEL GAS 

8,687 8,686 Total Feed : 6,422 6,399 Crude B 2,265 2,287 Crude A 

Plant Wide Balance Actual versus Plan  11Dec2006 

8,650

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Agenda 

l Business Challenge l Solution Description l Case Studies l Future Plans

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Studies 

1.  North African Refinery 2.  Asia Pacific Refinery 3.  Supply Chain Management

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Studies 

1.  North African Refinery 2.  Asia Pacific Refinery 3.  Supply Chain Management

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 1:  SAMIR

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27 

Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 1:  SAMIR Configuration 

Crude distillation Lubes oil Units

Merox LPG

Merox LSR

Gasoline HDT/Reforming

Kerosene Merox/HDS

Gas oil HDS

LPG Unit

Gasoline Blending

Propane Butane Regular Super Unleaded Jet A1 Gasoil Fuel oil

Crude oil storage Sidi Kacem

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 1:  SAMIR Global Business Process

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 1:  SAMIR Global Business Process

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Studies 

1.  North African Refinery 2.  Asia Pacific Refinery 3.  Supply Chain Management

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 2:  PETRONAS (Melaka Refinery) 

l  200,000 BPD Refinery in Melaka, Malaysia produces: u  LPG u  Petrochemical Naphtha u  Motor Gasoline u  Dual Purpose Kerosene u  Diesel u  Low Sulfur Waxy Residue u  Fuel Oil u  Lubricant Base Stocks u  BTX

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 2:  PETRONAS Architecture

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 2:  PETRONAS Benefits 

l All data collected in real time from source u  Flow rates – from DCS u  Transfer Data – from OAS u  Density – from LIMS 

l Reduced Oil Accounting work by ca. 50% l Insure financial security 

u  PI­Security u  PI­Audit Trails

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Studies 

1.  North African Refinery 2.  Asia Pacific Refinery 3.  Supply Chain Management

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 3:  Refining Company SCM 

l REFINERY •  Movement Tracking •  Process Unit Balances •  Fuel and H2 Balances •  Receipt and Shipment Accounting •  Inventory Balances •  Oil Loss Accounting •  Refinery Planning and Scheduling Models 

l SUPPLY AND DISTRIBUTION •  Movement Tracking •  Receipt and Shipment Accounting •  Inventory Balances •  Oil Loss Accounting •  S&D Models 

COMPANY WIDE •  Integrated Production Accounting 

• Foundation for Supply Chain Management

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 3:  Refinery Company ­ Region 

Area 6 Area 5 

Area 4 

South 

Area 8 

Area 3 

Area 2 

Refinery Area 1 

Area 9 Area 11 

East 

Area 10 

North 

= Distribution Terminal 

= Depot 

Area 7

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 3:  Refinery Company Losses 

l  Poor instrumentation: u  1.5 ­ 2.5% Mass 

l  Poor information affects other business functions: u  Planning and Scheduling u  Process Operations u  Management Decision u  Process Engineering u  Marketing 

l  Increased costs

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 3:  Refinery Company­Potential Benefits 

Note: Benefit estimates for 12 MM ton/yr refinery – y depots (truck and rail Crude = $210/ton 

Benefit  Benefit US$ pa 

Refinery  Oil Loss 

Planning Improvement 

Refinery Optimization 

Terminal Depots and Retail Stations  Oil Loss 

Operating Costs 

SCM  Inventory 

SCMO Total 

15,120,000 

3,000,000 

12,000,000 

380,000 

900,000 

2,050,000 

510,000 

33,960,000 

Area

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 3:  Refinery Company Losses 

Range  Estimate • Custody transfer (crude receipt, 

water %, shipments­railcar and tank trucks) 

0.35 to 0.55  0.45

• Fuel and H2 consumption understated– not real oil loss 

0.85 to 1.05  0.95

• Flare, oil in effluent, evaporation, BS&W loss, vents and leaks, FCC coke make calculation 

0.45 to 0.65  0.55 

TOTAL  1.65 to 2.25  1.95

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Case Study 3:  Refinery Benefit Calculation 

l  Estimate loss = 1.95% l  Custody Transfer Loss = 0.45% l  Flare, FCC Coke, Other Loss = 0.55% l  Apparent (understated fuel/H2 consumption) = 0.95% l  Improvement 

u  Achievable Goal = 0.4% u  Delta = (0.45%+0.55%­0.4% = 0.6%) u  0.6% x 12MM T/yr x 210US$/T = $15,120,000/yr 

l  Refinery optimization u  0.25 $/T x 12MM T/yr = $3,000,000/yr

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Case Study 3:  Depots/Retail Stations Benefits 

l  Weight Percent Oil Loss: u  Gasoline: 0.12% u  Diesel: 0.15% 

l  Improvement: 0.20%: l  Benefit: 

u  0.20% x 1,024,800 M3/yr x 0.8 x $230/t 

l  Operating cost reduction: u  Closure of 3 more depots u  Average cost = $200K to $400K/yr u  3 x $300K/yr = $900,000/yr savings

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Case Study 3:  Supply Chain Benefits 

l  Inventory Reduction: u  Refinery 50­60% Working Storage u  Depots 40­65% Working Storage 

l  Target: u  35­45% or 10% reduction u  Refinery = 2,066,000M3/Depots = 620,000M3 u  Carrying Costs = 8% u  One­time Inventory savings ($25,730,000) u  Plus annual reduced carrying costs ($2,050,000) 

l  Supply Chain Optimization: u  0.50$/ton X 1,024,000M3/yr x 0.8 M3/Ton  = $510,000/year

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Case Study 3:  Benefits – Business Process 

As is now  Target Now +5 Yr  Best achievable 

OPEX 

More test runs, 

simulations & “what ifs” 

Actual comparisons, 

Deviation analysis, Quantity & quality 

in $ 

Supply chain with no $ disconnects 

Best Practice 

Gross product value 

Feedstock costs 

Business Process Plan, Operate, Measure, Analyse, Improve 

Optimum crude selection and runs  More 

profitable plan 

Push the envelope 

Improve  ­ Operations Excellence 

Timely meetings, process 

actions, and $ outputs 

Simplify learning from performance 

and gaps 

Process units, and constraints tuned to 

models. 

Best Practice

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Case Study 3:  Intangible Benefits 

l  Inaccurate measurements highlighted and selectively corrected 

l  Inconsistent analyses identified l  Validated and reconciled data 

available to all l  Reliable, statistically correct 

production data available daily 

l  Early detection of losses and inefficiencies 

l  Instills systematic approach to optimization 

l  Improvements statistically proven 

l  Data can be integrated with ERP 

l  Accurate data available for LP model

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Agenda 

l Business Challenge l Solution Description l Case Studies l Future Plans

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Future Plans 

l  Provide Front end Studies and After Project support services u  Development of Business Case u  Stock loss surveys u  Analysis of measurement systems/procedures (compliance with SOX) u  Post audit of benefit achieved u  Measurement system support/maintenance 

l  Provide Total Solution/worldwide l  Follow Industry Integration Standards l  Other Industries 

u  Terminals and depots u  Petrochemical u  Oil and gas u  Power and water u  Metals and Mining

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

•  ASSET OPTIMISATION Machinery Health & Asset Management 

•  BROOKS Flow Measurement 

•  FISHER CONTROLS Control Valves and Regulators 

•  MICROMOTION Coriolis Mass Flow 

•  PROCESS SYSTEMS & SOLUTIONS Process Automation Systems 

•  POWER & WATER SOLUTIONS Power, Water and Waste Water Control Systems 

•  ROSEMOUNT Pressure and Temperature Transmitters, Flow and Level Instruments 

•  ROSEMOUNT ANALYTICAL Gas and Liquid Analysis 

Process Management 

23% 

Process Management 

23% Appliance & 

Tools 23% 

Network Power 17% 

Climate Technologies 

19% Industrial Automation 

18% 

Emerson’s Total Solution ­ Capability Emerson’s Total Solution ­ Capability

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Plant Topology Configuration 

Third Party Access 

Tank Gauging System 

Laboratory System 

Production Accounting 

Blend Control and Optimization 

Terminal Management 

Inventory Management 

Master Data Administration 

Movement Automation 

Real­time data 

Transactional data 

Reference data 

Control System 

Common Data Architecture 

Order Management 

Recipe Management 

Business Applications (ERP) 

Emerson’s Total Solution – SmartProcess™ Emerson’s Total Solution – SmartProcess™

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Copyright © 2007 OSIsoft, Inc. All rights reserved. 

Albany Atlanta 

Beaumont Boston Charlotte Chicago Cincinnati Cleveland Denver Detroit Houston 

Indianapolis Kansas City Los Angeles Louisville 

Marshalltown Memphis 

Minneapolis New Orleans New York 

Philadelphia Pittsburgh Richmond St. Louis 

Salt Lake City San Francisco 

Tampa Tulsa Wichita 

Dhahran Jedda` 

LaHabra 

Austin 

Sao Paulo 

Buenos Aires 

Haan Leicester 

Paris Minneapolis 

Mexico City 

Santiago 

Bombay Johannesburg 

Madrid 

Singapore 

Melbourne 

Bangkok 

Vienna 

Seoul 

Moscow 

Alleroed  Karlstadt Rijswijk 

Jakarta 

Kuala Lumpur 

Calgary Cambridge Edmonton London 

Montreal Regina Toronto 

Vancouver Winnipeg 

San Juan 

Bogota 

Manila 

Shanghai Taipei 

Milano 

Brussels Kiev 

Dubai 

Lagos 

Cairo 

Kuwait City 

Tokyo 

Auckland Caracas 

Rome 

Cincinnati  Kobe 

Karlstadt 

PorsgrunnVantaa 

Emerson’s Total Solution ­ Worldwide Emerson’s Total Solution ­ Worldwide

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Emerson’s Total Solution ­ Structure 

TAS 

PAS 

Business Layer 

Regulatory Control 

Movement Automation 

Gantry Automation 

Movement Control 

Gantry Control 

Order Mngt/Prod. Accounting 

Basic Control 

Business Layer 

MES Layer 

Control Layer 

Field Layer  Field Layer  Field 

Overlap 

ERP 

ISA S95

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Copyright © 2007 OSIsoft, Inc. All rights reserved.