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Meetings

Roundtable Meeting — June 2-3, 1999

Benchmarking Process Safety Programs

Briefing Paper No. 4

Mary Kay O’Connor Process Safety Center Roundtable Meeting
June 2-3, 1999, George Bush Presidential Conference Center
College Station, Texas

John Noronha
Eastman Kodak Company
Kodak Park, Worldwide Engineering Division
5th Floor, Bldg 23
Rochester, NY 14652-4390

 

 Table of Contents

Section

Title

Page

I

Background of Overall Chemical Safety Assessment Program

3

II

Benchmarking Project Primary Focus: Can Benchmarking Lead to Objective Results?

4

III

Some Preliminary Benchmarking Information and Reference

4

III A)

Regulatory and Industrial Chemical Safety Programs to be Evaluated in Benchmarking

4

III B)

Stakeholders Used in Benchmarking

5

III C)

Benchmarking for Goals/Objectives of Stakeholders

5

III D)

Potential Benchmarking Reporting Facilities

5

III E)

Potential Accidental Release Data

5

III F)

Developing Metrics and Measurements

7

III G)

Develop Report

7

IV

Additional Work to Improve this Draft

7

  Appendices

8

  References

8

Figures

Titles

Page

1

Objectives

9

2

Stakeholders

10

3

Some Key Regulations

11

4

Project Team

12

5

Case History Basis

13

6

Ten EPA Selected North American Industrial Classification System (NAICS) Codes

14

7

Phased Approach

15

8

Phase I Describe Evolution of Chemical Safety

16,17

9

Phase II Determine/Describe Stakeholders Goals and Objectives for Improving Chemical Safety

18

10

Phase III Develop Indicators, Measures, and Metrics to Measure Progress Towards Goals

19,20

11

Phase IV Develop Report

21

12

Five White Papers for June 2-3, 1999 Meeting

22

13

Benchmarking Proposal

23

14

Local Emergency Planning Committee Guidebook

24

 

I. BACKGROUND OF OVERALL CHEMICAL SAFETY ASSESSMENT PROGRAM

The benchmarking project is an integral part of the program, and will be used in various phases of the program. So we will describe the background of the overall program. Later we will focus on some benchmarking aspects.

The objectives of the overall chemical safety assessment program are very important to the public, industry and the government. They will impact, not only safety issues, but also on business being more competitive (Fig. 1).

The Stakeholders and the Regulations noted in Fig. 1 are shown in Fig. 2 & 3. Special attention should be paid to the last two regulations in Fig. 3, namely; OSHA, PSM, and EPA RMP. They represent a unique turn for regulatory agencies. Both were mandated to be developed under the Clean Air Act amendments and can be considered unique because they essentially require affected sites to establish a proactive business philosophy toward preventing and responding to chemical releases. They do this by requiring management systems to be developed. Neither regulation has many hard and fast detailed requirements.

The benefit to a plant site comes from avoiding the damage that may result from an accidental release. The benefits to the public living or working in the vulnerability zone include a stronger sense of security about the chemical plant that may be a neighbor.

The project team (Fig. 4) and case history basis (Fig. 5) are vital aspects of this chemical safety assessment program. The 66,000 reporting facilities under RMP are generally classified under 10 categories noted in Fig. 6.

The program will be done in 4 phases (Fig. 7) to establish different segments of the program and to allow reflection on how and whether to proceed to the next phase.

The four phases are:

  • Phase I: Describe the evolution of chemical safety (Fig. 8, two pages).
  • Phase II: Describe shareholder goals and objectives for improving chemical safety (Fig. 9).
  • Phase III: Develop indicators, measures and metrics to measure progress towards goals and objectives, (Fig. 10, two pages), and
  • Phase IV: Develop reports (Fig. 11).

At this June 2 & 3, 1999 meeting, five white papers (Fig. 12) will be presented and discussed with about 50 representatives from the public, industry and government. They will relate primarily to Phases I and II, but also touch on Phases III and IV. They are:

  1. Overview of chemical safety
  2. History of process safety and risk management
  3. What do various accident data bases tell us?
  4. Use of benchmarking to assess process safety and risk management programs
  5. Insurance perspective on future direction of process safety and risk management programs.

II BENCHMARKING PROJECT PRIMARY FOCUS: CAN BENCHMARKING LEAD TO OBJECTIVE RESULTS?

As noted earlier, benchmarking is an integral part of the entire program, and it is intended to be used in various phases of the overall program.

The primary focus is to evaluate whether we can use benchmarking objectively to assess chemical safety and risk management programs, including technologies and subprograms (Fig. 13).

Two specific questions are:

1) Can we benchmark to understand where we are in comparison to national chemical safety goals (that is, if we are able to establish these elusive goals?), and

2) Can we benchmark to develop metrics and measurements systems measuring progress towards these national chemical safety goals?

If the answer is yes to both these questions, then how would the work progress? What kind of data would we have to collect? Where would the data come from? And how would the whole issue of benchmarking be handled?

III SOME PRELIMINARY BENCHMARKING INFORMATION AND REFERENCE

III A) Regulatory and Industrial Chemical Safety Programs to be Evaluated in Benchmarking

For benchmarking, the major regulatory chemical safety programs relating to toxic, reactive, flammable and explosive of accidental releases are shown in Figure 3.

For industrial safety programs, they are:

    1. AIChE Loss Prevention Annual Symposia ( 1967 to present)
    2. API especially 520, 521
    3. ASME Ad Hoc Committee Guidelines on Incorporating Risk Based Principles in Boiler and Pressure Vessel Codes
    4. Various CCPS guidelines
    5. DIERS Risk Guidelines for Runaway Reactions
    6. NFPA especially 30, 68, 69

III B) Stakeholders Used in Benchmarking

In benchmarking, there are many types of stakeholders involved in the effort to reduce the risk of toxic, flammable and explosive substances due to accidental releases as shown in Fig. 2. They are regulatory, state and local governments, industry, emergency response organizations, environmental groups and the public.

III C) Benchmarking for Goals/Objectives of Stakeholders

1) Determining National Safety Goals

The goals and objectives of the overall chemical safety assessment program and of stakeholders are shown in Fig. 1, and discussed earlier in this report.

Different stakeholders will likely have different goals and objectives? Some examples of goals are as follows: How many deaths and injuries would be acceptable in a given period of time? How much property damage and business down time is acceptable? How many releases and how large a release is acceptable? How much time and money can be spent on hazard analysis?

Our project goal is to get benchmarking data from a representative sample of stakeholders (Fig. 2) to determine their goals and objectives. Then identify commonalties and differences, and then identify what we will consider national chemical safety goals (Fig. 9).

III D) Potential Benchmarking Reporting Facilities

Our benchmarking efforts could be based on (Fig. 5):

    1. A sample representative of the 66,000 reporting facilities under RMP, or
    2. those industries, processes, and chemicals identified as hazard concerns in the accidental Release Information Program (ARIP), or
    3. narrow industry groups such as Chlorine, Ammonia, Phosgene, and Ethylene.

III E) Potential Accidental Release Data

There are several sources of accidental release data (Fig. 8) for benchmarking. A key reference (Ref. 4) is entitled, "Accident History Database: An Opportunity, "(M. Sam Mannan and T. Michael O’Connor and Harry West) accepted for publication in Environmental Progress. Here are some examples:

  1. RMP Data Elements from the 66,000 reporting facilities (Appendix 1, Ref.1, pages 189-200 for a hypothetical example for propane.)
  2. Local emergency Planning Committees (LEPC)

LEPC’s have program requirements (Fig. 14) which relate to various safety programs used and the 5-year accident history. Program 1 is the least stringent RMP for "lower hazard" processes. A process qualifies for Program 1 if:

    • It has not had an accident with an off-site effect in the past five years,
    • The worst-case scenario (WCS) endpoint distance determined by accepted modeling techniques does not reach the nearest public receptor of concern, and
    • Emergency response activities have been coordinated with local emergency planning committees.

A process is in Program 3 if it does not qualify for Program 1 and it is either:

    • Covered by OSHA’s Process Safety Management standard, or
    • Considered within one of ten EPA selected North American Industrial Classification System (NAICS) codes (see Fig. 5).

Details of the 5-year history are shown in Ref. 2, page 26. They relate to both on-site and off-site deaths, injuries, property (see also Fig. 8) on Phase I - Data and Analysis of Accidental Releases.

3) Company Plant Accident Reports

Companies are required to report accidents due to government regulations, and often because of internal company policies.

Appendix 2 (Ref. 2, pages 249-252) entitled "Example of plant Accident/Incident Reporting Procedures" describes the details, the purpose, scope, policies, procedures, for both the Safety Department and Line Departments; and the Guidelines for conducting a formal investigation of accidents.

4) Industry Group Surveys

Another potential data source is the recently initiated CCPS Incident Database program. It reviews how data is collected and analyzed for about 25 companies who volunteered and paid dues to be part of the program and is only available to those companies.

The proposed 1999 DIERS benchmarking project (Appendix 4) is yet another potential data source of benchmarking on how engineering systems are designed and analyzed to prevent and mitigate accidental releases from exothermic runaway and decomposition reaction systems. It is based on a paper entitled, "Why DIERS Technology Should be used in Risk Assessment: Call for 1999 Worldwide Benchmarking Survey on Various Risk Reduction Methods Used." (Ref. 5).

III F) Developing Metrics and Measurements

A key element of the overall program is to evaluate whether we can, in fact, use benchmarking to assess chemical safety programs including technologies, and subprograms (Fig. 13).

To do so, we need to develop methods for metrics and measurements (Fig. 10). We would need to analyze data by the identification of general normalized measures, including qualitative and quantitative measures. Appendix 5 is an example of plant follow-up procedures for accidental investigation. (Ref. 2., pages 249-252). Ref. 4 is a good reference of "accountability" objectives and goals of process safety as a management function. (Ref. 3, Chapter 3, pages 15 to 23).

As shown in Figs. 8 to 10, we need to identify factors that are responsible for trends. We could use Delphi Technique on companies that are likely to comply with safety programs. We could use confidential interviews for companies (that are not complying) to determine if their safety records are statistically worse, better, or the same.

We need to analyze whether only subjective conclusions are possible (rather than objective conclusions.) from the proposed benchmarking.

III G) Develop Report

Finally, we would need to develop a report to meet the objectives of the chemical safety assessment program.

Then benchmarking effort and related efforts discussed would be key to its success. A general outline of the report is described in Fig. 11.

IV ADDITIONAL WORK TO IMPROVE THIS DRAFT

John Noronha will present this as a white paper at this June 2-3,1999 meeting of key members of the program and key stakeholders. This is in preparation for the October 27-28 conference, and ultimately for the actual benchmarking project work and the final report on the overall program.

APPENDICES

  1. Hypothetical Propane Application of Risk Management Plan Elements (Pages 188-200, ref. 3)
  2. Example of Plant Accident/Incident reporting procedures (Pages 249-252, Ref. 2)
  3. CCPS Process Safety Incident Data Base Demonstration", CCPS technical Steering Committee Meeting, Jan 20,1998.
  4. Draft of Proposed 1999 Worldwide Anonymous Benchmarking survey On Why DIERS Should Be Used and On Various Risk Reduction Measures Used In Runaway Reaction Risk Applications.
  5. Example of Analyzing an Accident Report ( Pages 246-248, Ref. 2)
REFERENCES
  1. "Practical Compliance with the EPA Risk Management Program", Walter, R.J., 1999, CCPS/AIChE, 3 Park Avenue, NY, NY 10016-5901.
  2. "Local Emergency Planning Committee Guidebook-Understanding the EPA Risk Management Program Role", Walter, R.J., 1998, CCPS/AIChE, 3 Park Avenue, NY, NY 10016-5901.
  3. Accounting Objectives and Goals of Process Safety as a Management Function (Chapter 3, "Plant Guidelines for Technical Management of Chemical Process Safety," 1992 CCPS/AIChE, 3 Park Avenue, New York, NY 10016-5901).
  4. Mannan, M.S., T.M. O’Connor, and H.H. West, "Accident History Database: An Opportunity", Environmental Progress, vol. 18, no. 1, Spring 1999, pp. 1-6.
  5. "Why DIERS Technology Should be used in Risk Assessment: Cell for 1999 Worldwide Benchmarking Survey on Various Risk Reduction Methods Used", Noronha, John, and Torres, Anthony, Loss Prevention Symposium, AIChE National Meeting, March 1997, Houston, Texas (also to be published in Process Safety Progress summer 1999)

 Figure 1: OBJECTIVES

  • Develop Methodology (Metrics and Measurements) for Assessment of Chemical Safety Programs and Risk Management Programs.
  • Apply Methodology in Analysis of Impact of Stakeholders of Regulatory and Industry Programs (Fig. 2) for:
  • Prevention and Protection of Accidental Releases from Stationary Sources of Reactive, Flammable and Toxic Chemicals
  • Identify Programs that should be Emphasized, Enhanced, Modified, or Dropped.
  • Develop Concepts on How We Could Reduce or Eliminate Some Safety Requirements in the Design, Production, Maintenance, and Training (so as to Make Business More Competitive While Still Operating at Generally Acceptable Risks).

Figure 2: STAKEHOLDERS 

  • Regulators (see Regulations on Figure 3)
  • State and Local Government
  • Industrial Associations (AIChE, API, ASME, ASTM, CMA, DIERS, NFPA, PSM, and RMP).
  • Response organizations
  • Environmental Groups, and
  • the Public

Figure 3: SOME KEY REGULATIONS

Year

Regulation

1985

Chemical Emergency Preparedness Program (CEPP)

1986

Emergency Planning and Community Right-to-Know Act (EPCRA)* [also known as Superfund Amendment and Reauthorization Act Title III (SARA)]

*Established LEPC’s nationwide

1986

Chemical Accident Prevention Program

1986

Chemical Safety Audity Program

1987

Accidental Release Information Program (ARIP)

1990

Clean Air Act Amendments (CAAA) Section 112(R)

1992

OSHA Process Safety Management (PSM) Regulation

1996

EPA Risk Management Program Rule (RMP)

Figure 4: PROJECT TEAM

  • Experts from Plant Operations, Chemical Safety Management, Risk Management, Metric Development, and Applications of Metrics and Public Policy Issues.
  • Also, Independent Ombudsman Group
  • They Should Not Be Involved in Method Development or Data Analysis
  • Some from Nuclear and Defense Industries

 Figure 5: CASE HISTORY BASIS

*Case Histories and Studies Could Be Based on
A) Sample Representative of:

1) 66,000 Reporting Facilities Under RMP, (Fig. 6) or

2) Those Industries, Processes, and Chemicals Identified as Hazard Concerns in ARIP Database.

or

B) Narrow Industry Groups, such as:

CL2, NH3, COCl2, C2H2

  • Where There are Multiple Locations (International)
  • Comparable Safety Records.

 

Figure 6: TEN EPA SELECTED NORTH AMERICAN INDUSTRIAL CLASSIFICATION SYSTEM (NAICS) CODES

NAICS Code

Industry

325181

Alkali and chlorine

325211

Plastics and resins

325311

Nitrogen fertilizers

32532

Pesticide and other agricultural chemicals

32411

Petroleum refineries

32211

Pulp mills only

32511

Petrochemical

325188

All other inorganic chemical manufacturing

325199

All other basic organic chemical manufacturing

325192

Other (covers cyclic crude and intermediate manufacturing

 

Figure 7: PHASED APPROACH

Purposes:

1) Establish Different Segments of Programs
2) Allows Reflection on How and Whether to Proceed

 Four Phases:

I. Describe Evolution of Chemical Safety

II. Describe Stakeholder's Goals and Objectives for Improving Chemical SAFETY

III. Develop Indicators, Measures and Metrics to Measure Progress Towards Goals and Objectives

IV. Develop Report

Figure 8: PHASE I DESCRIBE EVOLUTION OF CHEMICAL SAFETY

Page 1 of 2

Focus: Assessment of all available data2 and analysis techniques3, for accidental release rates1

1 Accidental release rates in terms of number of:

  • Low Level Failure/Precursors
  • Case Histories of Chemical Process Accidents
  • Number of Significant Chemical Accident
  • Fatalities On/Off Site
  • Injuries ON/Off Site
  • Property Damage
  • Environmental/Health Impacts

    5-year Accident History

Figure 8: PHASE I DESCRIBE EVOLUTION OF CHEMICAL SAFETY

Page 2 of 2

2 Data Sources Include:

  • Safety Metrics
  • Workers Compensation Databases
  • Insurers' Information
  • Toxic Release Inventory (TRI) (Ref. 1, pages 76-89, 193-200)
  • Accidental Release Information Program (ARIP) (Ref. 2, page 246)
  • Local EP Committee Information (Ref. 2, page 24)
  • County/Local Government Hazardous Materials Reporting Data
  • Private Companies

3Analysis Will Be Identification of General Normalized Measures, Including Qualitative and Quantitative Measures (As Available)

 

Figure 9: PHASE II DETERMINE/DESCRIBE STAKEHOLDERS GOALS

AND OBJECTIVES FOR IMPROVING CHEMICAL SAFETY

Goal: Determine What They Are?

How to do?

General: Study the Phase 1 Information and Applying Assessment Techniques

Specifically:

1) Identify Stakeholders (Fig. 2)

2) Identify Their Goals and Objectives

3) Identify the Commonalties and Differences of Goals

4) Identify National Chemical Safety Goals

 

Figure 10: PHASE III DEVELOP INDICATORS, MEASURES, AND METRICS TO MEASURE PROGRESS TOWARDS GOALS

Page 1 of 2

Goal: Identification of Programs and/or Other Factors that are Responsible for Trends

How to do?

1) Delphi Technique on Chemical Companies (Because They are More Likely to Comply)

2) Confidential Interviews will be Made with Companies (that are not complying) to Determine if Their Safety Records are Worse (Better) or Statistically Different

3) Analyze Whether Only Subjective Conclusions are Possible (Rather Than Objective Conclusions)

Figure 10: PHASE III DEVELOP INDICATORS, MEASURES, AND METRICS TO MEASURE PROGRESS TOWARDS GOALS

Page 2 of 2

Specifically:

1) Identify Measures/Indications for National Chemical Safety Goals

2) Identify Activities (Of Stakeholder Programs) That Contribute To Indicators And Data Collection From Stakeholders For Measures (Ref. 3, page 5)

3) Determine Cause/Effect Relationship Between Stakeholders Goals And Activities

- Is It Possible To Measure The Individual Contribution Of Various Programs (PSM), RMP, CMA's Responsible Care) To Chemical Safety?

4) Identify Gaps in Meeting National Chemical Safety Goals

*5) Identify Ineffective Activities Which Should Be Improved Or Eliminated

6) Develop Metrics to Measure Progress Towards National Chemical Safety Goals

Figure 11: PHASE IV DEVELOP REPORT

To Include:

    1. Identify information and measurements (that should be gathered in the future) to monitor the progress and help improvement of process safety.

- Detailed description of metric, and application of metrics in measuring progress towards meeting national chemical safety goals.

*2) Identify programs that should be emphasized, enhanced, modified or dropped (AIChE, API, ASME, ASTM, CMA, DIERS, NFPA, PSM, AND RMP).

3) Identify what trends in the industry may lead to future problems or improvements (for example, does TRI Reporting cause companies to take actions that result in process safety improvements).

4) List concepts on how we could reduce or eliminate some safety requirements in the design, production, maintenance, and training (so as to make business more competitive while still operating at generally acceptable risks).

 

Figure 12: FIVE WHITE PAPERS FOR JUNE 2-3, 1999 MEETING

1. Overview of Chemical Safety (Dr. Irv Rosenthal/Dr. Sam Mannan)

2. History of Chemical Safety and Risk Management. (Jon Averbach)

3. What Do Various Accident Databases Tell Us (Fig. 8)? (Eboni McGray)

4. Use of Benchmarking to Assess Chemical Safety and Risk Management Programs.

(John Noronha)

5. Insurance Perspective on Future Direction of Chemical Safety and Risk Management Programs. (Paris Stavrianidis)

 

Figure 13: BENCHMARKING PROPOSAL

FOCUS: The Ability to Use Benchmarking to Assess Chemical Safety and Risk Management Programs, Including Technologies and Subprograms

Question: Can We Benchmark to:

Q 1) Understand Where We are in Comparison to National Chemical Safety Goals (if we are able to establish these elusive goals) (Fig. 9)? or

Q 2) Develop Metrics and Measurement Systems for (Measuring) Progress Towards National Chemical Safety Goals (Ref. 2, pages 246-250)?

If Answer is Yes to Q1 and Q2, Then,

1) How Would the Process Work?

2) What Kind of Data Would We Have to Collect?

3) Where Would The Data Come From?

4) How Would The Whole Issue Of Benchmarking Be Handled?

 

Figure 14: LOCAL EMERGENCY PLANNING COMMITTEE GUIDEBOOK

Program Requirements Summary

 

PROGRAM LEVEL

1

2

3

Worst Case Release Scenario
  • One toxic or flammable for each Program 1 process

X

  • Single toxic for all covered Program 2 or 3 processes (see note)

X

X

  • Single flammable for all covered Program 2 or 3 processes (see note)

X

X

Alternative Release Scenario
  • At least one for each toxic in each covered Program 2 or 3 processes

X

X

  • At lease one to cover flammables covered Program 2 or 3 processes

X

X

Five-Year Accident History

X

X

X

Management System

X

X

X

Prevention Program

X

X

Emergency Response
  • Local agencies or facility provide; site must coordinate with response

X

  • Develop and implement site program

X

X

Submission of RMPlan
  • Certification statement

X

X

X

  • Worst-case analysis results

X

X

X

  • Alternative case analysis results

X

X

  • Five-year accident history

X

X

X

  • Data on prevention program elements

X

X

Note: Must submit additional worst-case scenarios for a hazard class, if different public receptors are potentially affected.

 


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