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MMI Engineering www.mmiengineering.com The State of Process Safety QRA and The Road to Meaningful and Actionable Decisions PERF Workshop Environmental QRA June 28-29, 2017 Houston Andrew Staszak MMI Engineering Email: [email protected] Tel: (1) 281-810-5011 Mob: (1) 979-575-1897

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Page 1: The State of Process Safety QRA and The Road to …perf.org/main/wp-content/uploads/2017/07/QRA_01_Staszak.pdf · Risk in Definition Quantitative Risk Assessment (QRA) utilizes a

MMI Engineeringwww.mmiengineering.com

The State of Process Safety QRA and The

Road to Meaningful and Actionable Decisions

PERF Workshop – Environmental QRA

June 28-29, 2017 Houston

Andrew StaszakMMI Engineering

Email: [email protected]

Tel: (1) 281-810-5011

Mob: (1) 979-575-1897

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Topics Covered:

▪ What is ‘Quantitative Risk Assessment’ in

Process Safety?

▪ Who and What are the/our Drivers?

▪ The Quantitative Risk Assessment Construct

▪ Metrics

▪ QRA in Application – Case Study

▪ Pitfalls / Hotbed Issues

Overview

QRA in Process Safety

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Risk in Definition

Quantitative Risk Assessment (QRA)

utilizes a systematic process to identify

potential impacts and consequences of

events, while considering their

likelihood of occurrence; with

cumulative consideration against a pre-

defined set of metrics.

Risk (according to Merriam-Webster)

▪ Possibility of loss or injury

▪ Someone or something that creates or suggests a hazard

▪ The chance of loss or the perils to the subject matter of an insurance contract

▪ Etc., etc., etc…

Pioneered in the nuclear industry in early 1960s.

O&G applications stated in early 1980s.

Driven by large scale incidents:

• Flixborough, UK 1974 (VCE – 28 fatalities)

• Bhopal, India 1984 (Toxic exposure – 4000

fatalities)

• Mexico City, Mexico 1984 (VCE/BLEVE – 650

fatalities)

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Globally

▪ Multiple regulatory bodies (UK HSE, New South Wales,

Singapore, Australia, ...)

▪ Long history with strict requirements and specific

methods

United States

▪ No single governing body or driver

▪ Sub-sets have limited but specific requirements (FERC –

LNG, PHMSA)

▪ Multiple regulatory bodies utilize the word and recognize

the practice of risk assessment but have little or no

specifics (OSHA PSM)

▪ Guidance comes from industry bodies – CCPS, API, etc.

Numerous sources with numerous focuses

▪ Corporate policies and requirements:

BP GP and Chevron RiskMan

The Drivers

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Who:

Us

• Corp

• Insurance

• People and Cultures

The Drivers Cont.

What:

Best Practices!?!?

• Ever changing and ever argued

• Depends on who you ask

• In many cases swayed by our own biases,

experiences, morals, …

Despite this, there exists a base general method for QRA which falls under generally

accepted and best practices. But, unless driven by an individual company, no two

QRAs will be identical.

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The Construct of a QRA

Risk = f (scenario, consequence, frequency)

Construct a quantitative assessment that allows ‘us’ to adequately

evaluate risk; such that safeguards, corrective actions, and/or

engineered modifications can be used for risk reduction.

This function can be EXTREMELY complex, with numerous different

measures and assumptions required to close the equation.

A QRA of a large scale Refinery could have 1000s of base scenarios,

100,000s of end point consequences, and 1,000,000s of historical data

points considered.

Easy Right?

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The Construct of QRA

Define

Objectives

Hazard

IdentificationHAZID

Frequency

Assessment

Consequence

Assessment

Risk

Formulation

Risk

EvaluationMitigations

Operations/Design Cont. –

Continuous Evaluation

Acceptable

Intolerable

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HazID (Qualitative / Semi-Quantitative):

▪ Conducted to determine what potential upset conditions may

need to be captured

• Natural disasters (tsunami, earthquake, etc.)

• Man-made external causes (airplane, rail, or truck crash)

• Outside of normal operating conditions (human error, runaway

reaction, etc.)

• SIMOPS

▪ Risk rank (qualitative risk matrix) scenario and include in QRA if

necessary (identified as credible ???)

▪ Can include intentional acts – security vulnerability assessment

Hazard Identification - Qual

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Process Breakdown:

▪ Scenario Development

• Examine P&IDs, PFDs, H&M Balance sheets, General

Arrangement

• Discretize: Breakdown process based on logical sections

(physical separation, isolation valves, process barriers)

• Determine suite of releases/hole sizes. A representation of

random failures (leaks, breaks, ruptures, manufacturing flaws,

etc..)

3 is usually considered acceptable – but may not be a good representation.

• It is possible to group similar sections; multiplies the risk

• Upset conditions (from HAZID). How will they be represented?

• What operational conditions will be evaluated?

Normal, temporary, batch, emergency, …

Hazard Identification - Quant

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Process Breakdown:

▪ Frequency Assessment

• Perform parts count and use appropriate failure frequency

database to determine leak frequency for defined process

sections (on/off-shore, cryogenic, custom)

How will frequencies be discretized (median, log average, upper/lower

biased)

Most release frequency is biased to less than 25mm hole sizes

Are there cases that results in no-consequence and can be filtered (<3mm)

• Perform LOPA style analysis to determine failure frequency for

upset scenarios

• Develop frequencies for “unknown/unique events”, requires

input from industry experts and “best” engineering judgment

• Determine if process is operating as designed?

Hazard Identification – Quant 2

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Modeling:

▪ Define outcomes for each scenario – end point consequences –

build event tree

• Careful! – how deep down the rabbit hole do you go?

▪ Determine level of “models” to be used…

▪ Perform consequence analysis to determine extent of impact to

targets of interest

• Toxic lethality

• Blast loadings

• Thermal impacts

• Building damage

• Kinetic impacts

• Dispersion

▪ Exceedance or continual damage model

Consequence Assessment

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Consequence Assessment 2

Events and Probabilities:

▪ Apply modifying probabilities

• Weather (direction and speed, seasonal, yearly,

average, …)

• Lethality

• Exposure duration (time discretization)

• Ignition, and so on

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Example event tree

Consequence Assessment 3

Two-Phase Release Event Tree

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▪ Risk is a relative metric, it means

nothing on its own.

▪ Define risk criteria metrics

Risk Matrix (qualitative)

Individual Risk (IRPA)

Societal Risk (F-N curve)

Fatal Accident Rate (FAR)

Risk Indices

Injury Rate

Potential Loss of Life (PLL)

Cost Analysis…

▪ If possible the criteria should be

selected before the project begins.

▪ Risk is typically defined uniformly for

all hazards and across all business

types.

▪ Define how it will be evaluated and

implemented.

▪ Can the criteria be reached and

maintained?

Risk Criteria

The universal choice

1x10-4

But why?

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Individual Risk:

▪ Typically a single value that is defined as: consequence at a

given rate

• Fatalities/year

• Injuries/year

• $ lost/year

• Environmental impact/year

▪ There are multiple indices in which individual risk can be

measured by:

• LSIR (location specific)

• IRPA (per annum)

• PLL (Potential Loss of Life)

• Average IR

• Maximum IR

Risk Criteria 2

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Societal Risk:

Risk Criteria 3

Societal Risk Criteria

1.00E-09

1.00E-08

1.00E-07

1.00E-06

1.00E-05

1.00E-04

1.00E-03

1.00E-02

1 10 100 1000

N (Number of Fatalities)

F (

the F

req

uen

cy o

f N

or m

ore F

ata

liti

es)

Intolerable

NegligibleALARP

Intolerable

Negligible

Can and is evaluated for on and off-site.

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Alternate Risk Result Applications:

Risk Criteria 4

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Risk Interpretation and Mitigation Strategies:

▪ If risk criteria is exceeded, then you must determine what/how to

mitigate:

• Threat (change process, alter scenario, application of

consequence, etc.)

• Target (adjust occupancy, strengthen buildings or equipment,

add shielding, etc.)

• Determine level and priority of required mitigations, may include

quantification for ALARP.

▪ Sensitivity calculations – Do you understand what is driving

the risk.

• Should assumptions, frequency, or consequence be further

investigated?

▪ Is the project / activity / operation still feasible?

▪ What will be the revalidation interval, or what changes (MOC) will

trigger a reval?

Risk Evaluation

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Case Study: Asset Protection

▪ Data generated during a QRA can be utilized in risk based design of

asset protection systems.

• Guidance documents provide – prescriptive steps, but significant

cost and operational constraints can be reduced in performance

(risk) based design.

• Quantitative risk analysis allows us to do this.

▪ Using QRA a performance of the system can be evaluated against a

desired criteria.

▪ In this case, setting the survivability of equipment to a return

period (/year selection) and constrained by evacuation time.

▪ The analysis can determine what level of passive fire protection is

required for various elements of the system.

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Case Study: Asset Protection 2

Peak Heat Flux

Background Heat Flux

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Case Study: Personnel Safety

▪ Individual Risk (IR) is a critical metric in QRA evaluation.

• Allows the identification of risk to specific people and locations on a

site.

• Allows identification of where or what events may be contributing to

risk.

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Case Study: Personnel Safety 2

Sensitivity Case

LSIR Category (/yr)

Jet Fire Pool Fire Explosion

/ FF JF + EXP

/ FF Total

BC 4.57E-05 0.00E-00 6.12E-05 3.24E-06 1.10E-04

S-1 5.99E-05 0.00E-00 1.18E-04 4.90E-06 1.83E-04

S-2 5.99E-05 0.00E-00 7.87E-05 4.22E-06 1.43E-04

S-3 4.57E-05 0.00E-00 4.08E-05 2.89E-08 8.94E-05

S-4 5.86E-05 0.00E-00 1.18E-04 4.48E-06 1.82E-04

Percent Change from Base Case

S-1 31% 0% 93% 51% 66%

S-2 31% 0% 29% 30% 30%

S-3 0% 0% -33% -99% -19%

S-4 28% 0% 93% 38% 65%

▪ If risk is identified as unacceptable/ALARP:

• Investigate data to identify best course of mitigation….i.e. “Best Bag

for the Buck”

• Sensitives can confirm reduction to an appropriate level.

Inclusion of

increased detection

capabilities,

improved isolation,

and control room

protection.

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Issues that arise…

▪ Which frequency database to use

• Onshore vs. offshore

• Is the data relevant?

• Do incidents need to be filtered or revised?

• What if the frequency does not exist or is limited?

▪ Which modifiers to use

• Assume weather parameters are dependent or treat independently

• Process modifiers (as per API 581)

• Ignition probability (many different models)

• Does the frequency database adequately represent the

equipment/process?

• Is the process operating as designed?

• Should we utilize facility specific data (existing sites) or known

company data?

Pitfalls & Hotbed Issues

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Issues that arise…

▪ The calculated risk is based on a snap-shot in time

• How do we account for continued changes during design?

• How do we account for changes/additions to a process or facility?

• What if the location or layout of the facility changes?

• Risk during turn-around?

▪ Risk criteria can vary both intercompany and across countries/

governing bodies, how do we handle this?

▪ In an effort to make risk “As low as reasonably practicable” where do

we stop?

• Analyzing the risk away

• Safety vs Cost

• Perceived Risk…viewed from the public

▪ Mitigations can reduce risk but they can also displace them to

somewhere / something else.

Pitfalls & Hotbed Issues 2

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MMI Engineeringwww.mmiengineering.com

Questions ???

And Thanks!