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1 Tim Overton Chief Process Safety Engineer The Dow Chemical Company Meeting Today’s Societal Expectations: Process Risk Management Programs of The Dow Chemical Company

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Page 1: Meeting Today’s Societal Expectations: Process Risk ...PLANT LAYOUT 2.1 Indoor Versus Outdoor Plant Operations 2.2 Layout and Separation of Facilities ... 3.7 Mineral Oil Filled

1

Tim Overton

Chief Process Safety Engineer

The Dow Chemical Company

Meeting Today’s Societal Expectations: Process Risk Management Programs of

The Dow Chemical Company

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2

An Unsettled Public

Growing Concerns About Safety

in the Chemical Industry

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3

An Overview

• Dow’s Commitment to EH&S Excellence

– Drive to Zero

– 2005 EH&S Goals

– 2015 Sustainability Goals

• Developing a Rigorous Process Safety Program

– Work Processes and Operating Discipline

– Metrics

– Culture

– Personalization

• The Role of the Chemical Industry

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4

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5

Goals set in 1996 for 2005

Injuries and Illnesses: Reduce 90%

LOPCs: Reduce 90%

Transportation incidents: Reduce 90%

Process Safety incidents: Reduce 90%

Motor vehicle incidents: Reduce 50%

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6

Performance vs. Goals1996-2005

• Process Safety: Goal to reduce by 90%

PSCM Performance vs M&E MI Plan Target

193

193

156

127

103

83

67

5544

3629

2319

0

20

40

60

80

100

120

140

160

180

200

1994 1995 1996 1997 1998 1999 2000 2001 2002 2003 2004 2005

PS

CM

Co

un

t

Baseline

Target - constant % improvement PSCM Performance vs M&E MI Plan Target

193

143137

110

8475

81 7867

52 56

138

193

156

127

103

83

67

5544

3629

2319

0

20

40

60

80

100

120

140

160

180

200

1994 1995 1996 1997 1998 1999 2000 2001 2002 2003 2004 2005

PS

CM

Co

un

t

ActualBaselineTarget - constant % improvement

Actual reduction: 71%

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7

• LOPCs:Down 72%

• Transportation incidents:Down 65%

• Injury and Illnesses:Down 84%

• Motor vehicle incidents:Down 39%

’96

’05

’96

’05

’96

’05

’96

’05

Performance vs. Goals1996-2005

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8

Putting it another way…

During the past 10 years…

• 13,000 employees did not suffer an injury or illness

• 10,500 LOPCs did not occur

• 150 motor vehicle accidents, with potential to cause injury or fatality did not occur

• 1,100 Process Safety incidents did not occur

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9

2015 Sustainability Goals

CollaborateListening, learning, talking and taking action –

we’re helping our communities to be better places to live and work for everyone.

ElevateWe seek to understand

our impact on global

ecosystems, and will work

towards the efficient and

effective use of our

precious resources.

InnovateWe will use our technology to

develop products to improve the quality of life around the world, while

ensuring those products are managed safely throughout their

lifecycles.

This is sustainability at Dow.

PerformWe’re raising the sustainability bar, setting targets to

address some of the world’s most pressing challenges and tracking our performance publicly,

year after year.

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10

2015 Sustainability Goals

By 2015, Dow will achieve, on average, a 75 percent improvement based on 2005 results.

• Injury rate of 0.08 for Dow and contractors combined

– 75 percent reduction in severity, and NO FATALITIES

• All sites combined will have fewer than 75 LOPCs

• All sites will reduce process safety incidents by 75 percent, reduced severity rate by 95 percent

• All Dow employees combined will reduce the MVA rate to 1.5

• Additional goals: security, waste and emission reduction or

resource conservation

• ….(other goals)

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11

Pyramid of Process Safety Performance

Organization, Work Processes and

Operating Discipline

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Organization, Work Process and Operating Discipline

• Process safety beings with the design and control of a facility

Organization:• 25 Technology Centers worldwide• 30 full-time process safety professionals (Process Safety

Technology Leaders)• Chief Process Safety Engineer• Dedicated analytical research roles for reactive chemicals

program• Strong dedication to process safety issues by internal Process

Automation and Process Engineering functions• Key Manufacturing and EH&S roles: Production Leaders,

Business Manufacturing Leader, EH&S BOL, Site EH&S Responsible Care Leaders

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13

Dow’s Process Safety History

PrePre--19601960 -- Fire Protection EngineeringFire Protection Engineering

19631963 -- Corporate Safety & Loss Prevention Department formed Corporate Safety & Loss Prevention Department formed

19641964 -- Fire and Explosion Index (Risk Analysis)Fire and Explosion Index (Risk Analysis)

19661966 -- Reactive Chemicals ProgramReactive Chemicals Program

19741974 -- Loss Prevention Principles issuedLoss Prevention Principles issued

19761976 -- Minimum Requirements (First Edition)Minimum Requirements (First Edition)

19781978 -- Operations Practices (Minimum Requirements Emphasis)Operations Practices (Minimum Requirements Emphasis)

19821982 -- Fire Protection Practice ManualFire Protection Practice Manual

19861986 -- Chemical Exposure Index (CEI)Chemical Exposure Index (CEI)

19901990 -- Chemical Engineering Hazard Guidelines issued. Chemical Engineering Hazard Guidelines issued.

19911991 -- Guidelines for Management of ChangeGuidelines for Management of Change

1994 1994 -- Process Risk Management Guidelines for Facilities and DistributProcess Risk Management Guidelines for Facilities and Distributionion

1994 1994 -- Guidelines for Hazard and Operability StudyGuidelines for Hazard and Operability Study

1997 1997 -- Process Safety Expertise Center establishedProcess Safety Expertise Center established

1997 1997 -- Global Reactive Chemicals Global Standard issuedGlobal Reactive Chemicals Global Standard issued

1998 1998 -- TDCC Business EH&S Risk Evaluation Work Process TDCC Business EH&S Risk Evaluation Work Process

1999 1999 -- Global Mechanical Integrity Standard issuedGlobal Mechanical Integrity Standard issued

2000 2000 -- Introduction of Layers of Protection Analysis toolIntroduction of Layers of Protection Analysis tool

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Dow’s Process Safety History

And our “history” never stops growing. We continuously improve upon our existing programs….

PrePre--19601960 -- Fire Protection EngineeringFire Protection Engineering

19631963 -- Corporate Safety & Loss Prevention Department formed Corporate Safety & Loss Prevention Department formed

19641964 -- Fire and Explosion Index (Risk Analysis)Fire and Explosion Index (Risk Analysis)

19661966 -- Reactive Chemicals ProgramReactive Chemicals Program

19741974 -- Loss Prevention Principles issuedLoss Prevention Principles issued

19761976 -- Minimum Requirements (First Edition)Minimum Requirements (First Edition)

19781978 -- Operations Practices (Minimum Requirements Emphasis)Operations Practices (Minimum Requirements Emphasis)

19821982 -- Fire Protection Practice ManualFire Protection Practice Manual

19861986 -- Chemical Exposure Index (CEI)Chemical Exposure Index (CEI)

19901990 -- Chemical Engineering Hazard Guidelines issued. Chemical Engineering Hazard Guidelines issued.

19911991 -- Guidelines for Management of ChangeGuidelines for Management of Change

1994 1994 -- Process Risk Management Guidelines for Facilities and DistributProcess Risk Management Guidelines for Facilities and Distributionion

1994 1994 -- Guidelines for Hazard and Operability StudyGuidelines for Hazard and Operability Study

1997 1997 -- Process Safety Expertise Center establishedProcess Safety Expertise Center established

1997 1997 -- Global Reactive Chemicals Global Standard issuedGlobal Reactive Chemicals Global Standard issued

1998 1998 -- TDCC Business EH&S Risk Evaluation Work Process TDCC Business EH&S Risk Evaluation Work Process

1999 1999 -- Global Mechanical Integrity Standard issuedGlobal Mechanical Integrity Standard issued

2000 2000 -- Introduction of Layers of Protection Analysis toolIntroduction of Layers of Protection Analysis tool

2001 - Enhanced Process Risk Management Program2002 - Enhanced Layers of Protection Analysis2004 - Update to all Dow Loss Prevention Principles2006 - Enhanced Building Overpressure Analysis

…. and many more…..

Although we already had a rich tradition in Process Safety, with the integration of

best practices from UCC’s Operational Safety program we’ve added to or

enhanced several of our programs.

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15

The Bow-Tie Diagram

ENGINEERING

MAINTENANCE

OPERATIONS

HAZARD

UndesiredUndesired

EventEvent

C

O

N

S

E

Q

U

E

N

C

EBarriersMitigation &

Emergency

Preparedness

Measures

THREAT

THREAT

THREAT

Courtesy of Robin Pitblado DNV

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Work Processes and Guidelines

• Corporate-wide work processes and guidelines for implementation of Operating Discipline, Management of Change, Mechanical Integrity programs, Training, Project reviews and more

• Comprehensive “Loss Prevention Principles”: best practices, recommendations, and mandatory requirements for Dow facilities

Dow corporate

Operating Discipline

Management System

(ODMS)

Web based. Accessible

to all employees world-

wide

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Table of Contents for Dow LPPs:

Topic

P REFACE

TABLE OF CONTENTS

1. INTRODUCTION

1.1 In t roduct ion to Loss Pr event ion P rinciples

1.2 Fir e and E xplosion Index

1.3 Chemica l E xposure Index

1.4 Pr oject Review Pr ocess

1.5 Mater ial Hazard Ident ifica t ion

1.6 Loss Prevent ion Ch ecklist

1.7 Chemica l In terr eact ivity Charts

2. P LANT LAYOUT

2.1 Indoor Versus Outdoor Plan t Opera t ions

2.2 Layout and Separa t ion of Facilit ies

2.3 Access Roadways

2.4 Sewer an d Dr ain Systems

3. ELECTRICAL

3.1 E lect r ica l Ar ea Classifica t ions

3.2 Cable Tr ay Loca t ion and Protect ion

3.3 Light in g

3.4 Pr ocess Plan t Power Systems

3.5 Motor Control Center s and Elect r ica l Rooms

3.6 Sta t ic Elect r icit y

3.7 Min er a l Oil F illed Power Transfor mers

3.8 E lect r ica l Main tenance – Predict ive/Pr event ive Main tenance

4. F IRE WATER SYSTEMS

4.1 Fir e Water Pum p and Dr iver

4.2 Spr ink ler Dr ain Test

4.3 Water Mains an d Layout

4.4 Basic Hydraulics

4.5 Fir e Water Source

4.6 Fir e Water Demand

5. F OAM SYSTEMS

5.1 Foam Protect ion Applica t ions

5.2 Foam Protect ion for Tan ks

5.3 Types of Foams

5.4 High E xpansion Foams

5.5 Foam Proport ion ing Systems

5.6 Main ta in ing Foam Systems

6. EQUIP MENT

6.1 Cooling Towers

6.2 Air-Cooled Hea t Exchanger s

Topic

6.3 Tanks and Vessels

6.4 Glass and Transpa ren t Devices

6.5 Compr essed Gas Cylinder s

6.6 Min imum Requir ements for Fiber Rein for ced P la st ic Vessels

6.7 Meta ls, Alloys and Non-Meta llic Ma ter ia ls of Const r uct ion

6.8 Indust r ia l Tr uck Classificat ions

6.9 Use of Vacuum Trucks or Vacuum Equipment wit h F lammable,

Combust ible, or React ive Mater ia ls

7. STORAGE AND HANDLING OF CHEMICALS AND UTILITIES

7.1 Flammable Liqu ids

7.2 Liquefied Pet r oleum Gases

7.3 Combust ible Liqu ids

7.4 Unstable and React ive Chemica ls

7.5 Dikes and Conta inment

7.6 Stor age Cabinets for F lammable Liqu ids and Combust ible

Liqu ids

7.7 Iner t Gases and Nit rogen Ut ility Systems

7.8 Ut ility Air Systems Including Br eath ing Air

7.9 Potable Water Systems

7.10 Utility Water Systems (Excluding Potable Water)

7.11 Ut ility Steam and Condensa te Systems

7.12 Utility Natur al Gas Systems

8. LOADING AND UNLOADING STATIONS

8.1 Tank Cars and Tank Tr ucks

8.2 Ships and Barges

9. DETECTION SYSTEMS

9.1 Fire Detector s

9.2 Combust ible Gas Detectors

10. FIRE DAMAGE CONTROL SYSTEMS

10.1 Preamble to F ir e Damage Control Systems

10.2 Use of Iner t Gas for Padding (DE LE TE D)

10.3 Wet and Dr y P ipe Spr inkler Systems

10.4 Deluge Systems

10.5 Carbon Dioxide Systems

10.6 Dry Chemica l Systems

10.7 The Use of Halon

10.8 Fireproofing

10.9 Water Curta ins

10.10 Insu la t ion for F ire Pr ot ect ion

10.11 Inspect ion , Test ing and Main tenance of F ir e Protect ion

Systems

10.12 Explosion Suppression

10.13 Fire Doors

Topic

11. COMBUSTIBLE DUSTS AND SOLIDS

11.1 Com bu st ible Dusts

11.2 Foamed Plast ics

11.3 Foamed Plast ic Insula t ion

12. BUILDINGS

12.1 Purged Control Rooms

12.2 Occupied Plant Buildings Subject to Extern al Hazards

12.3 Office Buildin gs

12.4 Warehouse Buildings

12.5 Labora tor ies

12.6 Labora tory Fume Hoods

12.7 Process An alyzer Out door Buildings/Enclosures

13. FIRED EQUIP MENT

13.1 Safety and Control of Fired Equipment

13.2 Hea t Exchange Systems

13.3 Outdoor Oil Fir ed Boiler s

13.4 Furnaces Hea t ing Flammable Mat eria ls

14. RELIEF AND VENT SYSTEMS

14.1 Pressure/Vacuum Relief Syst em s

14.2 Fla r e Systems

14.3 Flame Arresters and Detona t ion Ar rest ers

15. INSTRUMENT AND COMP UTER CONTROL

15.1 Inst rument Insta lla t ion

15.2 Emergency Shutdown

15.3 Process Con trol Computer and Business Mini-Computer

Safeguards

15.4 Safety Inst rument ed Systems

16. ROTATING P ROCESS EQUIP MENT

16.1 Crit ica l Rota t ing Equipment

16.2 Safe Operat ion of Gas Turbin es

16.3 Steam Turbine Genera tors

16.4 Deadh eaded Pumps

17. P IP ING

17.1 In t roduct ion and Scope

17.2 Defin it ions and Abbrevia t ion s

17.3 Codes and References

17.4 Piping Materia ls

17.5 Piping Materia l Specifica t ions

17.6 Piping Design

17.7 Piping Fabrica t ion

17.8 Piping Insta lla t ion

17.9 Piping Opera t ion and Maintenance

17.10 Utilit y Pipin g (DELETED)

17.11 Potable Water and Brea th ing Air (DELETED)

Topic

P REFACE

TABLE OF CONTENTS

1. INTRODUCTION

1.1 In trodu ct ion to Loss Prevent ion Pr inciples

1.2 F ire and Explosion Index

1.3 Chemica l Exposure Index

1.4 Project Review Process

1.5 Mater ia l Hazard Iden t ifica t ion

1.6 Loss Prevent ion Ch ecklist

1.7 Chemica l In terreact ivity Char ts

2. P LANT LAYOUT

2.1 In door Versus Outdoor P lan t Opera t ions

2.2 Layout and Separa t ion of Facilit ies

2.3 Access Roadways

2.4 Sewer an d Dra in Systems

3. ELECTRICAL

3.1 E lectr ica l Area Classifica t ions

3.2 Cable Tray Locat ion and Protect ion

3.3 Light ing

3.4 Process Plan t Power Systems

3.5 Motor Cont rol Centers and E lect r ica l Rooms

3.6 Sta t ic Elect r icity

3.7 Min era l Oil Filled Power Transformers

3.8 E lectr ica l Main ten ance – Predict ive/Preven t ive Main ten ance

4. FIRE WATER SYSTEMS

4.1 F ire Water Pu mp and Driver

4.2 Spr inkler Dra in Test

4.3 Water Mains an d Layout

4.4 Basic Hydraulics

4.5 F ire Water Source

4.6 F ire Water Demand

5. FOAM SYSTEMS

5.1 Foam Protect ion Applica t ions

5.2 Foam Protect ion for Tanks

5.3 Types of Foams

5.4 High Expansion Foams

5.5 Foam Propor t ion ing Systems

5.6 Main ta in ing Foam Systems

6. EQUIP MENT

6.1 Cooling Towers

6.2 Air -Cooled Hea t Exchangers

Topic

6.3 Tanks and Vessels

6.4 Glass and Transparen t Devices

6.5 Compressed Gas Cylinder s

6.6 Minimum Requirements for Fiber Reinforced Plast ic Vessels

6.7 Meta ls, Alloys and Non-Meta llic Mater ials of Construct ion

6.8 In dustr ia l Truck Classifica t ions

6.9 Use of Vacuum Tru cks or Vacuum Equipment with Flammable,

Combust ible, or React ive Mater ia ls

7. STORAGE AND HANDLING OF CHEMICALS AND UTILITIES

7.1 F lammable Liqu ids

7.2 Liquefied Petroleum Gases

7.3 Combust ible Liqu ids

7.4 Unstable and React ive Chemica ls

7.5 Dikes and Conta inment

7.6 Storage Cabinet s for F lammable Liqu ids and Combust ible

Liqu ids

7.7 In er t Gases and Nit rogen Utility Systems

7.8 Utility Air Systems Including Brea th ing Air

7.9 Potable Water Systems

7.10 Utility Water Systems (Excluding Potable Water)

7.11 Utility Steam and Condensa te Systems

7.12 Utility Natura l Gas Systems

8. LOADING AND UNLOADING STATIONS

8.1 Tank Cars and Tank Trucks

8.2 Ships and Barges

9. DETECTION SYSTEMS

9.1 F ire Detector s

9.2 Combust ible Gas Detectors

10. FIRE DAMAGE CONTROL SYSTEMS

10.1 Preamble to F ir e Damage Control Systems

10.2 Use of Iner t Gas for Padding (DELETED)

10.3 Wet and Dry P ipe Spr inkler Systems

10.4 Deluge Systems

10.5 Carbon Dioxide Systems

10.6 Dry Chemica l Systems

10.7 The Use of Halon

10.8 F ireproofin g

10.9 Water Cur ta ins

10.10 In su la t ion for F ir e P rotect ion

10.11 In spect ion , Test ing and Main ten an ce of F ir e Protect ion

Systems

10.12 Explosion Suppression

10.13 Fire Doors

Topic

11. COMBUSTIBLE DUSTS AND SOLIDS

11.1 Combustible Dusts

11.2 Foamed Plast ics

11.3 Foamed Plast ic Insu la t ion

12. BUILDINGS

12.1 Purged Cont rol Rooms

12.2 Occupied P lan t Buildings Subject to External Hazards

12.3 Office Buildings

12.4 Warehouse Buildings

12.5 Labora tor ies

12.6 Labora tory Fume Hoods

12.7 Process Analyzer Outdoor Buildings/Enclosures

13. FIRED EQUIP MENT

13.1 Safety and Control of F ired Equipment

13.2 Heat Exchange Systems

13.3 Outdoor Oil Fired Boilers

13.4 Furnaces Heating Flammable Mater ia ls

14. RELIEF AND VENT SYSTEMS

14.1 Pressure/Vacuum Relief Systems

14.2 Flare Systems

14.3 Flame Arrester s and Detonat ion Arrester s

15. INSTRUMENT AND COMP UTER CONTROL

15.1 Instrument Insta lla t ion

15.2 Emergency Shutdown

15.3 Process Cont rol Computer and Business Min i-Computer

Safeguards

15.4 Safety Instrumented Systems

16. ROTATING P ROCESS EQUIP MENT

16.1 Cr it ica l Rota t ing Equipment

16.2 Safe Opera t ion of Gas Turbines

16.3 Steam Turbine Genera tors

16.4 Deadheaded Pumps

17. P IP ING

17.1 In t roduct ion and Scope

17.2 Defin it ions and Abbrevia t ions

17.3 Codes and References

17.4 Piping Mater ia ls

17.5 Piping Mater ia l Specifica t ions

17.6 Piping Design

17.7 Piping Fabrica t ion

17.8 Piping Insta lla t ion

17.9 Piping Opera t ion and Main tenance

17.10 Utility Piping (DELETED)

17.11 Potable Water and Brea thing Air (DELETED)

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• State Based Control - Like pressing the “Easy” button

– Dow internally developed control system beginning in 1970’s

– Automated Operator Work Processes (Startup, Shutdown, Runs steps)

– Automated Process State Degradation Handling (Abnormal SituationManagement)

– In 2001, Dow Standardized on the ABB 800xA

• Integrated Safety and Basic Automation Systems within the DCS– Partitioned TüV Certified Execution Environments

– Single Development Language

– Shared or Dedicated Sensors for BPCS and SIS Based on Requirements

• Full Simulation for Control Code Validation and Operator Training

• Reliability/Fault Tolerance– Total System Design (Hardware, System Software, Applications, Network,

Support, etc.)

– Not Sensitive to Single Point Failures

– Diagnostics

– Pre-defined Degradation Path

Dow’s Key Process Automation

Systems and Tools

State Based Control: • Plant-Wide Coordination of Startup and Degradation• Automation of Frequent Operations• Process Upsets Handled by Automation Program• Alarms Only Enabled when Required• Control Strategies are State Dependent

Benefits:• Increased productivity• Reduced variability• Improved EH&S performance• Fewer nuisance alarms• Enforces operating discipline

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Pyramid of Process Safety Performance

Work Processes and Operating Discipline

Metrics

Loss of Primary Containment

(LOPC)

Overdue action itemsProcess Safety Near Misses

Reactive Chemical incidents

(including any unplanned

fires)

LPP Compliance & Gap

Closure

Compliance Plan status

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Pyramid of Process Safety Performance

Work Processes and Operating Discipline

Metrics

Culture

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Culture – Ownership and Accountability at all levels

Company and Business Leaders

• Set Performance Vision

• Provide the resources

• Hold organization accountable

• Hold themselves accountable

– Annual ratings, bonuses and career opportunities hinge on success

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Culture – Ownership and Accountability at all levels

Plant Leaders

The most important player with respect to culture!

• Their pay and career movement must be dependent on safety performance

• Must be held responsible for results not just implementation

• Dow performs a “New Leader Review” within the first six months of any new Production Leader arriving to a new role. This NLR isintended to demonstrate knowledge/competency of the reactive chemical and process safety hazards present in the plant.

– As the final reviewer of all MOCs, we want the Production Leader to be fully aware of the hazards and mitigations in placeto prevent incidents in the plant prior to approving changes.

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Culture – Ownership and Accountability at all levels

Plant Operators

• Where it all comes together; your front line of defense

• Employment must be contingent upon safety performance

• Plant Leader must hold employees accountable

• “Balance of Consequences” applied to behaviors

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Culture – Ownership and Accountability at all levels

Process Engineers, Process Automation, Design

• Utilize Inherently Safer designs

• Incorporate Process Automation which will take a plant to a safestate even without operator intervention

• Follow recognized industry standards

• Emphasis the importance of Management of Change and Pre-Startup Safety Reviews whenever building or changing the process.

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Pyramid of Process Safety Performance

Work Processes and Operating Discipline

Metrics

Culture

Personalization

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Characteristics of Safety Performance Intangibles

• The entire organization must personalize process safety and what it means to them.

• Communication is constant, timely, and personal

• Make safety performance data relevant– go beyond the numbers

• The consequences of an incident are internalized, individually…from the operator level to the corporate leader level.

• Total ownership of performance across the entire organization

• Must be kept fresh, creativity is the key

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Pyramid of Process Safety Performance

Organization, Work Processes and Operating Discipline

Metrics

Culture

Personalization

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A Call to Action

Chemical Industry’s Reputation

for Safety Grows

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Thank You