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23rd International System Safety Conference 2005 Risk-based System Safety Assessment of Ammunition Process Facility Authors ~ Francis Loi, (Presenter) Defence Science & Technology Agency, Singapore Andreas F. Bienz, Bienz, Kummer & Partner Ltd, Switzerland Alfred Tan, Defence Science & Technology Agency, Singapore

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Page 1: Risk-based System Safety Assessment of Ammunition Process ... · Risk-based System Safety Assessment of Ammunition Process Facility ... Personnel- and vehicle-density ... Risk-based

23rd International System Safety Conference 2005

Risk-based System Safety Assessmentof Ammunition Process Facility

Authors ~

Francis Loi, (Presenter) Defence Science & Technology Agency, Singapore

Andreas F. Bienz, Bienz, Kummer & Partner Ltd, Switzerland

Alfred Tan, Defence Science & Technology Agency, Singapore

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Scope

� Introduction

� Approach

� Data Collection

� Quantitative Risk Analysis

� Summary of Results

� Benefits

� Subsequent Actions and Conclusion

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Introduction

� Schematic of the Ammunition Process Facility (APF)

� Sited within a disused granite quarry

� Partial reinforced concrete structure and partial rock cavern

Preparation Area

Admin./Utility

Rooms

ZONE A

Test Cell

Preparation Area

Admin./Utility Rooms

Test Cell

ControlRoom

ControlRoom

EntranceBlast Door

EntranceBlast Door

Test CellBlast Door

Test CellBlast Door

ZONE B

* Not to Scale

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Approach

� 3-tiered approach:

� General data collectionon 6 system elements:

� Ordnance-specificanalysis

� Situational analysis

ORDNANCE

PERSONNEL

PROCEDURES

LOCATION

INFRASTRUCTURE

EQUIPMENT

1st Tier: General Data Collection

2nd Tier: Ordnance-specific Analysis

3rd Tier: Situational Analysis

1st Tier

3rdt Tier

2nd Tier

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Data Collection

� 1. Location

� Layout (nearby buildings and road networks)

� Functions of nearby buildings / facilities

� Personnel- and vehicle-density

Preparation Area

Admin./Utility

Rooms

ZONE A

Test Cell

Preparation Area

Admin./Utility Rooms

Test Cell

ControlRoom

ControlRoom

EntranceBlast Door

EntranceBlast Door

Test CellBlast Door

Test CellBlast Door

ZONE B

* Not to Scale

APF Footprint

Within quarry

Outside quarry

ORDNANCE

PERSONNEL

PROCEDURES

LOCATION

INFRASTRUCTURE

EQUIPMENT

1st Tier

3rdt Tier

2nd Tier

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Data Collection

� 2. Infrastructure

� Type of building construction

� Presence of hazardous materials

� Presence of unique building systems (e.g., blastdoors, fire protection systems, electrical equipmentclassification)

ORDNANCE

PERSONNEL

PROCEDURES

LOCATION

INFRASTRUCTURE

EQUIPMENT

1st Tier

3rdt Tier

2nd Tier

Page 7: Risk-based System Safety Assessment of Ammunition Process ... · Risk-based System Safety Assessment of Ammunition Process Facility ... Personnel- and vehicle-density ... Risk-based

Data Collection

� 3. Ordnance

� 5 primary ordnance systems (T1 - T5)were selected

� Basic characteristics (e.g, net explosivesquantity (NEQ), hazard classification,physical conditions, packaging)

� Ordnance utilisation/exposure periods

ORDNANCE

PERSONNEL

PROCEDURES

LOCATION

INFRASTRUCTURE

EQUIPMENT

1st Tier

3rdt Tier

2nd Tier

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Data Collection

� 4. Equipment

� Unique equipment used in thetransporting, handling and processing ofordnance

� E.g., ordnance-handling vehicles, cranes,compressed air system

ORDNANCE

PERSONNEL

PROCEDURES

LOCATION

INFRASTRUCTURE

EQUIPMENT

1st Tier

3rdt Tier

2nd Tier

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Data Collection

� 5. Personnel

� Number of personnel

� Location of personnel

� Tasks/duties of personnel

� Exposure period to hazardous activities

ORDNANCE

PERSONNEL

PROCEDURES

LOCATION

INFRASTRUCTURE

EQUIPMENT

1st Tier

3rdt Tier

2nd Tier

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Data Collection

� 6. Procedures / Workflow

� Procedures and duration of normaloperations at the APF, including in-loading, preparation, testing / processing,out-loading were documented andcategorised into specific situations

� Quantity and location of personnel andordnance were traced to workflow

ORDNANCE

PERSONNEL

PROCEDURES

LOCATION

INFRASTRUCTURE

EQUIPMENT

1st Tier

3rdt Tier

2nd Tier

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Data Collection

� Consolidation of workflow dataBasic Data: Work Flow for Ordnance T3

Room

Preparation

2 t NEQ 2 t NEQ 1.6 t 1.6 t 2 t NEQ 1.6 t 1.6 t 1.6 t 2 t 2 t NEQ

4 Pers. 5 Pers. 0 Pers. 1 Pers. 5 Pers. 1 Pers. 0 Pers. 1 Pers. 5 Pers. 4 Pers.

Take ammo out Disassemble Storage various Assemble / var. Storage various Ass. Put ammo back

Inspection Disassemble Inspection

Test Cell

500 kg NEQ 500 kg NEQ 500 kg NEQ 500 kg NEQ

4 Pers. 4 Pers. 4 Pers. 4 Pers.

Preparation Clean up Preparation Clean up

Control5 Pers. 5 Pers.

Controlling Controlling

Adminor other 1 Pers. 1 Pers.

various various

4-5 h 5-6 h 6-7 h 7-8 h0-1 h 1-2 h 2-3 h 3-4 h

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Data Collection

� Consolidation of workflow data into specific situationsResulting Situations for Ordnance T3

Room

Preparation(Inspection)

2 t NEQ 2 t NEQ 1.6 t NEQ 1.6 t NEQ4 Pers. 5 Pers. 1 Pers. 0 Pers.Take ammo out Disassemble/Assemble various StorageVisual inspection

Test Cell

500 kg 500 kg4 Pers. 0 Pers.Preparation Testing

Control5 Pers.Controlling

Adminor other 1 Pers.

various

Situation 4Testing

Situation 3Situation 1Preparation

Situation 2Disassemble/Assemble

2 h / ShiftBefore/After Test

2 h / Shift2 h / Shift 2 h / Shift

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Quantitative Risk Analysis

� 4 systematic procedures:

� Event analysis

� Effect analysis

� Exposure analysis

� Risk calculationE1

P1 Pi Pn

Ej

EmR

Risk Calculation

location of eventstype of reactionsprobabilitiesdecisive quantities

distribution of hazardous effectsinjuries/lethality of persons

number, location, time and length of stay of possibly exposed persons

calculation of individual and collective risks

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Event Analysis

� Identified the list of hazardous incidents which could occurdue to relevant, multi-folded reasons

� Incidents were derived based on location, decisivequantities of explosives, nature of activity, its duration andbasic frequency

� Basic frequency was obtained from BK&P’s BasicFrequency System, which is a database of eventprobabilities based on statistical, analytical andexperiential approachesS/N Ordnance Location NEQ (kg) Activity Duration (hr) Basic Frequency (1/yr)1.1 2000 Unpack/Pack 2 1.00E-051.2 2000 Drain/Refuel 2 1.00E-041.3 1600 Change/Clean 1.00E-051.4 Test Cell 600 Prepare 3.00E-051.5 Preparation Area 1600 Change/Clean 1.00E-051.6 Test Cell 600 Testing 1.00E-03

Preparation Area

T1 2

2

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Effect Analysis

� General effects associated with an explosion wereconsidered (e.g., airblast, debris, fire, building damage)

� Effects (or consequences) were normalised in terms oflethality rates at three locations:

� APF Donor Zone

(PES)

� APF Acceptor Zone

(ES)

� Area outside APF

(ES)

Donor Zone NEQ/QTNT Preparation Area Test Cell Control RoomsPreparation Area 1 - 4 ton 100% 100% 100%

200 - 400 kg 5% - 100% 2% - 13% 5% - 20%Test Cell X00 kg 75% - 100% 100% 1%

50 kg 1% 100% 0%

Event in Lethality in Donor Zone

Event in Donor ZoneNEQ/QTNT

2 - 4 ton 0.5%1 - 2 ton 0.2%

0.3 - 1 ton 0.1%< 0.3 ton 0%

Lethality in Acceptor Zone

LethalityDebris Mass

Density (kg/m 2) 1 ton 2 ton 3 ton

75% 7 20 40 7030% 1.8 110 130 1605% 0.25 240 260 290

0.5% 0.025 400 420 4500.05% 0.0025 550 570 600

Effects Distance (m) for NEQ/Q TNT

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Exposure Analysis

� Personnel exposure information were duration- andlocation-specific

� Exposure rate in the Donor zone (PES) was derivedbased on situations or activities

� An average exposure rate was assumed in the Acceptorzones (ES) (i.e., adjacent APF Zone & surrounding areas)due to the low risk-relevance from the lower assumedlethality rates and more-or-less random operations

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Risk Calculation

� Quantitative risks were calculated using risk matricescombining data from event, effect and exposure analyses

� Risk categories considered:

� Individual risk

� Real collective risk

- or group risk

� Perceived collective risk

- with aversion factor, ϕ

Risk = Probability • Consequences

effects simultaneity t

dangerous eventprobability p

individual i

Individual: Society: Responsible Party:

( = Aversion)ϕϕϕϕ

Individual Risk:

r i = p. λλλλi .t i

Real Collective Risk:

Rr= p.Σλλλλi.t i=p.C

λλλλ i

i

Rp = ϕ.ϕ.ϕ.ϕ. Rr

Perceived Coll. Risk:

Page 18: Risk-based System Safety Assessment of Ammunition Process ... · Risk-based System Safety Assessment of Ammunition Process Facility ... Personnel- and vehicle-density ... Risk-based

Risk Calculation

� Individual Risk Calculation MatrixRisk Calculation Zone: A

Ammo Type: T1Period of Situation (1 Shift) [h/8766 h]: 0.22 Situation No: 1 - 2

Room Event Pers. PW1-1 PW1-2 PW1-3 PW1-B PW1-EO1 PW1-EO2 PW1-EO3 PW1-E O4

No. No. n 4 3 1 9 2 20 20 20

A A1/1-1 fbi 1.00E-05 tij 25 25 25 25 1.25 2.5 2.5 1.25

λλλλAB 100 100 100 0.5

λλλλDT 90 50 0.1 20

λBD

λFr

λFi

λij 100 100 100 0.5 90 50 0.1 20

Rri 5.14E-06 rij 5.50E-07 5.50E-07 5.50E-07 2.75E-09 2.48E-08 2.75E-08 5.50E-11 5.50E-09

A A1/2-1 fbi 1.00E-04 tij 25 25 25 25 1.25 2.5 2.5 1.25

λλλλAB 100 100 100 0.5

λλλλDT 90 50 0.1 20

λBD

λFr

λFi

λij 100 100 100 0.5 90 50 0.1 20

Rri 5.14E-05 rij 5.50E-06 5.50E-06 5.50E-06 2.75E-08 2.48E-07 2.75E-07 5.50E-10 5.50E-08

Risks in Acceptor Zone (B)

λAB - Lethality rate due to air blastλDT - Lethality rate due to debris throw

Event Persons j

Risks in Donor Zone (A) Risks outside IAPFLegend:Event

Effect

Exposure

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Risk Evaluation

� A risk assessment is not complete without risk evaluation andthe definition of the safety (or risk acceptance) criteriapertaining to the case

� Typical levels of risk evaluation:

� Definition of safety (or risk acceptance) criteria

� Proof of safety Responsible party

Safety analyst

Definition of safety criteria

Proof of safety

Responsible party

Safety analyst

Definition of safety criteria

Proof of safety

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Risk Evaluation

� Safety (or Risk Acceptance) criteria for individual risk

� Upper Limiting Values Principle

� According to current Swiss safety criteria, maximumacceptable individual risk is

� 10-4/year for directly involved personnel

� 5x10-5/year for indirectly involved personnelUpper Limiting Values Principle:

max

r (Person p)Accepted

Not Accepted

Individual Risk r

Maximum Individual Fatal Risk / Year:

accepted

not accepted

10-2

10

10

10

-3

-4

-5

Risk[1/year]

RiskCategories

directly involved persons indirectly involved persons third persons

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Risk Evaluation

� Safety (or Risk Acceptance) criteria for collective risk

� Willingness-to-pay & Marginal Cost Principles

� According to current Swiss safety criteria,

� Marginal cost to prevent one directly-involved fatality isCHF 4m (or SGD 5m or USD 3m)

Marginal Cost Principle:

Tangent ofMarginal Cost[Money/Saved Life]

Optimum Package of Safety Measures

Collective Risk R

Racc

Cost of Safety Measures

Marginal Cost for Preventing 1 Fatality:

RiskCate-gories

100

10

1accepted

Cost[mill CHF]

directly involved persons indirectly involved persons third persons

not accepted

not accepted

1 2 3 4

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Summary of Results

� Individual risks

� Within the acceptable Swiss safety criteria for individualrisks

Safety Check (for 1 shift and 1 working year) Ammo Type: T1 (Donor-) Zone: A

Events

PW1-1 PW1-2 PW1-3 PW1-B PW1-EO1 PW1-EO2

n=4 n=4 n=3 n=3 n=1 n=1 n=9 n=9 n=2 n=2 n=20 n=20

Rr [1/y] Rr [1/y] Rr [1/y] Rr [1/y] II DI II DI II DI II DI II DI II DI

Safety Check

Requ. SafetyInvestment

582 [S$/y] r1 = 8.65E-06 r2 = 9.36E-06 r3 = 8.40E-06 r4 = 3.74E-0 8 r5 = 3.73E-07 r6 = 9.34E-07

Total R 1.16E-04 9.37E-05 7.10E-05 2.27E-05 1.04E-08 8.64 E-06 1.04E-08 9.35E-06 1.04E-08 8.39E-06 3.74E-08 0.00E+00 3.73E-07 0.00E+00 9.34E-07 0.00E+00Ammo Type T2 62% 7.08E-09 7.08E-09 7.08E-09 - 7.08E-09 7.08E-09Ammo Type T3 9% 1.50E-09 1.50E-09 1.50E-09 - 1.50E-09 1.50E-09Ammo Type T4 12% 0.00E+00 0.00E+00 0.00E+00 - 0.00E+00 0.00E+00 Ammo Type T5 18% 1.83E-09 1.83E-09 1.83E-09 - 1.83E-09 1.83E-09

A1/1-1 4.40E-06 5.50E-07 5.50E-07 5.50E-078.66E-07 2.75E-09 2.48E-08 2.75E-08

A1/2-1 4.40E-05 5.50E-06 5.50E-06 5.50E-068.66E-06 2.75E-08 2.48E-07 2.75E-07

A1/3-1 4.40E-06 5.50E-07 5.50E-07 5.50E-078.66E-07 2.75E-09 2.48E-08 2.75E-08

A1/3-2 1.21E-05 1.49E-06 1.65E-06 1.24E-064.60E-07 1.65E-09 4.13E-08 1.65E-08

A1/4-1 4.40E-06 5.50E-07 5.50E-07 5.50E-078.66E-07 2.75E-09 2.48E-08 2.75E-08

A1/4-2 1.65E-06 0.00E+00 5.50E-07 0.00E+001.10E-05 0.00E+00 0.00E+00 5.50E-07

Individual Risk

2.37E-05 1.27E-05

1.30E-05 1.26E-05

6.13E-06 5.27E-06

6.13E-05 5.27E-05

6.13E-06 5.27E-06

Individual Risks from Zone B

6.13E-06 5.27E-06

Collective Risk

Grp Adj. DI + II DI II

Donor Zone Acceptor Zone Outside APF

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Summary of Results

� Collective risks

� Applying the marginal cost of CHF 4m or SGD 5m to theperceived collective risk of 2.05x10-3/year, the maximumactual costs for significant risk mitigation is approximatelySGD 10,000/year

� No further physical risk mitigation measures can be foundand implemented.

� Sound procedural control is the next level of residual riskmitigation

Dura-tion

AZone

BZone

ExternalObjects

Real Risk(Grp. Adj.)

Estim.Avers.

PerceivedRisk [1/y]

Dura-tion

BZone

AZone

ExternalObjects

Real Risk(Grp. Adj.)

Estim.Avers.

PerceivedRisk [1/y]

T1 47% 6.67E-05 3.16E-07 2.10E-05 1.09E-04 4.00 4.38E-04 - - - - - - -T2 - - - - - - - 62% 7.68E-05 1.41E-07 9.12E-06 9.54E-05 3.48 3.32E-04T3 8.5% 7.85E-06 2.70E-08 2.05E-06 1.20E-05 2.30 2.76E-05 8.5% 7.84E-06 2.99E-08 2.52E-06 1.29E-05 2.30 2.97E-05T4 12% 1.15E-05 1.54E-08 1.33E-07 1.18E-05 2.00 2.36E-05 12% 1.08E-05 0.00E+00 9.25E-08 1.10E-05 2.00 2.21E-05T5 32% 6.09E-05 1.90E-07 6.85E-06 7.50E-05 10.56 7.92E-04 18% 3.43E-05 7.13E-08 3.53E-06 4.15E-05 9.19 3.81E-04

100% 1.47E-04 5.49E-07 3.01E-05 2.08E-04 - 1.28E-03 100% 1.30E-04 2.42E-07 1.53E-05 1.61E-04 - 7.65E-046,403 3,825

Perceived Collective Risk [1/year] 2.05E-03 Marginal Cost [S$/y] 10,228

Total Marginal Cost in S$ Marginal Cost in S$

Ordn.A Zone (Donor) B Zone (Donor)

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Summary of Results

� Statistical collective risks of different ordnance

� Provided an overview of the risk environment and acomparison of the risks inherent to the processing of eachordnance system

Statistical Collective Risk [1/year]

0.00E+00

2.00E-05

4.00E-05

6.00E-05

8.00E-05

1.00E-04

1.20E-04

1.40E-04

T1 T2 T3 T4 T5Ordnance

A Zone B Zone

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Benefits from the QRA

� Addressing the Maximum Credible Mishap

� Theoretical and mathematical perspective on potentiallydire consequences

� Objectivity and Details

� High level of objectivity and details through the perspectivesof the risk analysts and supported by statistical data

� Appreciation of Activity Interfaces

� Simultaneity of activities and their interfacing risks can bemathematically determined

� Thorough Consideration of Workflow and Procedures

� Early understanding of operations and workflow

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Conclusions

� Addressed the maximum credible mishap

� Provided safety assurance on APF engineering andexplosive safety designs, based on current Swiss safetystandards

� Increased the risk awareness of various APF stakeholdersand ordnance operators

Subsequent Actions� Qualitative analysis and safety documentation of the APF

engineering systems

� Qualitative O&S safety assessment to incorporate andintegrate operators’ directives and procedures

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The End

Acknowledgement ~

Andreas F. Bienz, Bienz, Kummer & Partner Ltd, Switzerland

Alfred Tan, Defence Science & Technology Agency, Singapore