99975554 HAZID Worksheet FORM Rev 25 May 2012 Timas Premier Oil Indonesia

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  • HAZID WORKSHEET

    : ANOA PHASE 4 - AGX COMPRESSION RECONFIGURATION PROJECT

    : DLB Activities in the vicinity and moored alongside AGX Platform

    : 25 May 2012

    S L R S L R

    1 Anchor Handling

    (Running

    Messanger Line

    Under the

    Bridge) using

    Work Boat

    Work Boat collision with

    the platform / AHT

    Boat damage / lost boat

    Personnel injury

    5 2 HR 1. Approved Anchor Handling Procedure

    2. Reliable / maintained work boat

    3. Weather limit

    4. Adequate illumination of work area

    5. Trained work boat operation

    6. Maintain good communication

    7. JSA for work boat operation

    8. FRC/MOB Boat ready at all time

    9. Suitable PPE: include work vest

    1 1 LR

    Lost control of wire due

    to failure of

    comunication or control

    system

    Damage to redundant

    umbilical / subsea structure

    3 2 MR 1. Approved Anchor Handling Procedure

    2. DP Vessel as AHT

    3. Reliable and well maintained vessel (with

    MWS approval)

    4. Competence Vessel Captain

    5. Maintain good communication between

    Anchor Tower and AHT

    3 1 LR

    AHT collision with the

    platform / complex

    Damage to vessel or

    complex (damage to riser)

    Personnel injury

    Schedule delay

    5 3 HR 1. Approved Anchor Handling Procedure

    2. JSA for Anchor Handling

    3. Weather limit for Anchor Handling

    4. Parachute Buoy

    5. DP Vessel as AHT

    6. Reliable and well maintained vessel (with

    MWS approval)

    7. Competence Vessel Captain

    8. Maintain good communication between

    Anchor Tower and AHT

    9. Weather limit

    10. Briefing about the facility for all Vessel

    Captain including the location of risers

    11. Secondary AHT standby in the field at all

    time

    3 1 LR

    Project

    Node Description

    Date of HAZID Study

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    2 Running Anchor

    / Anchor Wire

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 1 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Drop/Drag Anchor on

    Subsea Facility

    Damage Subsea Facility

    Environmental HC

    Discharge

    Potential fire/explosion

    Company reputation

    5 3 HR 1. Subsea / Seabed Survey DONE

    2. Approved Anchor Handling Procedure and

    Approved Anchor Pattern

    3. Anchor on Deck of AHT

    4. Mooring Analysis

    5. BMS/Survey Equipment Calibration

    6. Pull test the anchors

    7. Continue anchor wire tension monitoring by

    Anchor Tower

    8. Shut Down & Depressurize West Lobe line

    9. Compliance with POI Marine Procedure

    3 1 LR

    3 DLB Approach /

    Final Departure

    of AGX

    DLB colission with

    platform and riser

    Damage to both DLB and

    Platform

    Personnel injury / Lost of life

    Schedule delay

    Environmental impact

    5 2 HR 1. Approved Anchor Handling Procedure

    (Step by Step DLB Approach to AGX)

    2. Weather limit

    3. Maintain good communication with all

    parties

    4. Final approach only after all anchors are

    installed / laid and DAY Light only.

    5. Shut Down the platform and Depressurize

    West Lobe line during Final Approach

    6. AGX Riser is inside the Jacket

    7. Responsible person on DLB monitoring the

    gangway tip during final approach

    8. Minimize personnel on AGX during DLB

    final approach

    9. Complete GO and No GO Checklist for the

    DLB Final Approach to AGX

    10. Anchor removal for final departure is

    the reverse of anchor installation. (Meeting

    will be performed with relevant parties

    including MWS for removal anchors).

    3 1 LR

    2 Running Anchor

    / Anchor Wire

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 2 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Dropped loads / objects

    on Topside of AGX /

    Subsea Facilities

    Damage asset causing HC

    leak

    Personnel injury

    Schedule delay

    Environmental delay

    5 4 HR 1. Approved Lifting Procedure

    2. Certified and good condition Crane (include

    MWS inspection/approval)

    3. Certified and good condition Rigging

    4. Certified and experienced Crane Operator

    and Rigging Personnel

    5. Maintain good communication among

    parties involved

    6. All lift within the SWL of the crane / rigging

    7. Weather limit

    8. Stay clear from load

    9. Suitable PPE

    4 1 MR

    Crane Boom collision

    with the AGX Topside

    and/or with Other Crane

    Damage asset causing HC

    leak

    Personnel injury

    Schedule delay

    4 3 HR 1. All Cranes will be under the control of the

    Project (CTR).

    2. Designated Person In Charge for Every Lift

    3. Good illumincation

    4. Procedure control for Cranes Operations

    (SIMOPS)

    5. Detail planning meeting for Crane

    Operations

    6. Trained and experienced Crane Operator

    and Rigging Personnel

    7. Maintain good communication among all

    involved parties

    3 1 LR

    1 1. Risk Assessment to be

    performed for using the

    Crawler Crane for Personnel

    Transfer related to the

    visibility (ability of the Crane

    Operator to see the FROG)

    Timas/POI

    2 2. Review Crawler Crane

    Operation Procedure

    Timas

    3 2 MR 1. Weather limit

    2. Barge rails in place

    3. Certified and good condition crane

    4. Certified and good condition rigging

    equipment

    5. Certified and experienced Crane Operator

    and Rigging Personnel

    6. Operate cranes within the design limit

    3

    4 DLB Crane

    Operation

    Crawler Crane fall over

    the side due to bad

    weather related during

    lifting (overloaded /

    dynamic load)

    Damage asset causing HC

    leak / Environmental impact

    Personnel injury

    Schedule delay

    1 LR

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 3 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    DLB Exhaust Increase risk of

    Fire/Explosion in the event

    of HC release

    1 1 LR 1. DLB Exhausts are located on the STBD

    Forward.

    2. Gas is lighter than air (Gas-Gas Exchanger

    is +16 elevation)

    3. F&G and ESD System on AGX

    4. ERP Procedures

    5. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    6. PM on platform e.g. leaks prevention

    7. Portable Multi-Gas Detector on Stern of

    DLB

    NOTE: based on 10mm hole during the study,

    the dispersion of HC release / gas cloud

    would NOT reach the DLB.

    1 1 LR

    Electrical Equipment on

    DLB (Lights, Etc)

    Increase risk of

    Fire/Explosion in the event

    of HC release

    1 1 LR 1. Gas is lighter than air (Gas-Gas Exchanger

    is +16 elevation)

    2. F&G and ESD System on AGX

    3. ERP Procedures

    4. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    5. PM on platform e.g. leaks prevention

    6. Switch off the light on Crane Boom during

    the Day Light

    7. Weather proof lighting/electrical system on

    the barge deck and crane boom

    8. DLB can be pulled / winched away (winch

    speed approx 60m per minute)

    9. Construction activities around process area

    controlled by PTW asper integrated project

    plan

    10. Portable Multi-Gas Detector on Stern of

    DLB

    NOTE: based on 10mm hole during the study,

    the dispersion of HC release / gas cloud

    would NOT reach the DLB.

    1 1 LR 3 Explore the possibility to

    switch off the lights and other

    ignition source on crane

    Timas

    5 Ignition Source

    on DLB

    - Gas Release

    (10mm hole on

    Gas-Gas

    Exchanger) with

    20knots wind

    speed toward

    the DLB

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 4 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Crawler Crane Exhaust Increase risk of

    Fire/Explosion in the event

    of HC release

    1 1 LR 1. Crawler Crane is located more than 60

    meters away

    2. Crawler Crane Exchaust is fitted with Spark

    Arrestor

    3. Gas is lighter than air (Gas-Gas Exchanger

    is +16 elevation)

    4. F&G and ESD System on AGX

    5. ERP Procedures

    6. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    7. PM on platform e.g. leaks prevention

    NOTE: based on 10mm hole during the study,

    the dispersion of HC release / gas cloud

    would NOT reach the DLB.

    1 1 LR

    Welding Machines on

    DLB

    Increase risk of

    Fire/Explosion in the event

    of HC release

    1 1 LR 1. During SIMOPS, Welding Machines are

    located on DLB are 60m away from the

    platform.

    2. Standby Persons to disconnect the welding

    leads to Platform and shut down (turn off) the

    welding machines on DLB.

    3. Gas is lighter than air (Gas-Gas Exchanger

    is +16 elevation)

    4. F&G and ESD System on AGX

    5. ERP Procedures

    6. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    7. PM on platform e.g. leaks prevention

    8. Portable Multi-Gas Detector on Stern of

    DLB

    NOTE: based on 10mm hole during the study,

    the dispersion of HC release / gas cloud

    would NOT reach the DLB.

    1 1 LR

    5 Ignition Source

    on DLB

    - Gas Release

    (10mm hole on

    Gas-Gas

    Exchanger) with

    20knots wind

    speed toward

    the DLB

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 5 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Hot Works on DLB Increase risk of

    Fire/Explosion in the event

    of HC release

    1 1 LR 1. All Hot Works on DLB Deck will be covered

    by PTW

    2. Standby Persons to disconnect the welding

    lead to Platform and shut down (turn off) the

    welding machines on DLB.

    3. Gas is lighter than air (Gas-Gas Exchanger

    is +16 elevation)

    4. F&G and ESD System on AGX

    . ERP Procedures

    5. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    6. PM on platform e.g. leaks prevention

    7. Portable Multi-Gas Detector on Stern of

    DLB

    NOTE: based on 10mm hole during the study,

    the dispersion of HC release / gas cloud

    would NOT reach the DLB.

    1 1 LR

    5 Ignition Source

    on DLB

    - Gas Release

    (10mm hole on

    Gas-Gas

    Exchanger) with

    20knots wind

    speed toward

    the DLB

    COMMENT: The probability (frequency) of having leaks will be further elaborated (POI)

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 6 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    DLB Exhaust Increase risk of

    Fire/Explosion in the event

    of HC release

    1 1 LR The release of HC with 100mm hole is demonstrated to unlikely because:

    1. As per QRA

    2. Process Integrity Management e.g. FLIR

    Camera, rectification of significant TSS Matrix

    Integrity Related Defect. All Integrity related check

    and improvement are included on the GO and NO

    GO Process.

    3. No break of containment the process system

    during SIMOPS

    4. No Heavy Lifting over the process during

    SIMOPS (Most construction activities involved

    small weights - structure lifted in around the

    platform edges west and south

    5. Drop Object Protection is in place for Gas Gas

    Exchanger

    The risk of release of gas has been reduced to

    ALARP, if it would occur the severity would be less.

    Additional Safeguards:

    1. DLB Exhausts are located on the STBD

    Forward.

    2. Gas is lighter than air (Gas-Gas Exchanger is

    +16 elevation)

    3. F&G and ESD System on AGX

    4. ERP Procedures

    5. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    6. PM on platform e.g. leaks prevention

    7. Portable Multi-Gas Detector on Stern of DLB

    NOTE: based on 100mm hole during the study, the

    dispersion of HC release / gas cloud would NOT

    reach the DLB Exhaust.

    1 1 LR6 Ignition Source

    on DLB

    - Gas Release

    (100mm hole on

    Gas-Gas

    Exchanger) with

    20knots wind

    speed toward

    the DLB

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 7 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Electrical Equipment on

    STERN of DLB (Lights,

    Etc)

    Increase risk of

    Fire/Explosion in the event

    of HC release

    5 1 HR The release of HC with 100mm hole is demonstrated to unlikely because:

    1. As per QRA

    2. Process Integrity Management e.g. FLIR

    Camera, rectification of significant TSS Matrix

    Integrity Related Defect. All Integrity related check

    and improvement are included on the GO and NO

    GO Process.

    3. No break of containment the process system

    during SIMOPS

    4. No Heavy Lifting over the process during

    SIMOPS (Most construction activities involved

    small weights - structure lifted in around the

    platform edges west and south

    5. Drop Object Protection is in place for Gas Gas

    Exchanger

    The risk of release of gas has been reduced to

    ALARP, if it would aoccur the severity would be

    less.

    Additional Safguards are:

    1. F&G and ESD System on AGX

    2. ERP Procedures

    3. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    4. Close water tight doors on the crane tub

    5. Portable Multi Gas Detector on the Stern of

    DLB.

    6. Any lifting over the process during the SIMOPS

    shall be covered by PTW, Risk Assessment.

    4 1 MR 4 Requirement of Multi Gas

    Detector on the STERN of

    DLB to be captured in Project

    Procedure

    Timas

    6 Ignition Source

    on DLB

    - Gas Release

    (100mm hole on

    Gas-Gas

    Exchanger) with

    20knots wind

    speed toward

    the DLB

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 8 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Crawler Crane Exhaust Increase risk of

    Fire/Explosion in the event

    of HC release

    5 1 HR The release of HC with 100mm hole is demonstrated to unlikely because:

    1. As per QRA

    2. Process Integrity Management e.g. FLIR

    Camera, rectification of significant TSS Matrix

    Integrity Related Defect. All Integrity related check

    and improvement are included on the GO and NO

    GO Process.

    3. No break of containment the process system

    during SIMOPS

    4. No Heavy Lifting over the process during

    SIMOPS (Most construction activities involved

    small weights - structure lifted in around the

    platform edges west and south

    5. Drop Object Protection is in place for Gas Gas

    Exchanger

    The risk of release of gas has been reduced to

    ALARP, if it would aoccur the severity would be

    less.

    Additional Safguards are:

    1. Crawler Crane is located more than 60 meters

    away

    2. F&G and ESD System on AGX

    3. ERP Procedures

    4. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    5. PM on platform e.g. leaks prevention

    6. Crane Crawler will be shut down upon the

    detection of Gas Release after operation is

    secured.

    4 1 MR

    6 Ignition Source

    on DLB

    - Gas Release

    (100mm hole on

    Gas-Gas

    Exchanger) with

    20knots wind

    speed toward

    the DLB

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 9 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Welding Machines on

    DLB

    Increase risk of

    Fire/Explosion in the event

    of HC release resulting:

    - Personnel injury

    - Asset damage

    5 1 HR The release of HC with 100mm hole is demonstrated to unlikely because:

    1. As per QRA

    2. Process Integrity Management e.g. FLIR

    Camera, rectification of significant TSS Matrix

    Integrity Related Defect. All Integrity related check

    and improvement are included on the GO and NO

    GO Process.

    3. No break of containment the process system

    during SIMOPS

    4. No Heavy Lifting over the process during

    SIMOPS (Most construction activities involved

    small weights - structure lifted in around the

    platform edges west and south

    5. Drop Object Protection is in place for Gas Gas

    Exchanger

    The risk of release of gas has been reduced to

    ALARP, if it would aoccur the severity would be

    less.

    Additional Safguards are:

    1. During SIMOPS, Welding Machines are located

    on DLB are 60m away from the platform.

    2. Standby Persons to disconnect the welding lead

    to Platform and shut down (turn off) the welding

    machines on DLB.

    3. F&G and ESD System on AGX

    4. ERP Procedures

    5. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    6. PM on platform e.g. leaks prevention

    7. Refer to Technical Note for Control of Welding

    Machines Isolation

    8. Portable Gas Detector on the STERN of the

    DLB.

    4 1 MR

    6 Ignition Source

    on DLB

    - Gas Release

    (100mm hole on

    Gas-Gas

    Exchanger) with

    20knots wind

    speed toward

    the DLB

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 10 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Hot Works on DLB Increase risk of

    Fire/Explosion in the event

    of HC release resulting:

    - Personnel Injury

    - Asset Damage

    5 1 HR The release of HC with 100mm hole is demonstrated to unlikely because:

    1. As per QRA

    2. Process Integrity Management e.g. FLIR

    Camera, rectification of significant TSS Matrix

    Integrity Related Defect. All Integrity related check

    and improvement are included on the GO and NO

    GO Process.

    3. No break of containment the process system

    during SIMOPS

    4. No Heavy Lifting over the process during

    SIMOPS (Most construction activities involved

    small weights - structure lifted in around the

    platform edges west and south

    5. Drop Object Protection is in place for Gas Gas

    Exchanger

    The risk of release of gas has been reduced to

    ALARP, if it would aoccur the severity would be

    less.

    Additional Safguards are:

    1. All Hot Works on DLB Deck will be covered by

    PTW

    2. Standby Persons to disconnect the welding lead

    to Platform and shut down (turn off) the welding

    machines on DLB.

    3. F&G and ESD System on AGX

    4 ERP Procedures

    5. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    6. PM on platform e.g. leaks prevention

    7. Portable Gas Detector on STERN of DLB

    4 1 MR

    Fire as Ignition Source

    and its Impact to the

    Safety of the Platform

    Complex

    Increase Risk of Fire on

    Platform (AGX) if there is

    concurrent HC Release

    2 2 LR 1. DLB can be pulled / winched away from the

    Platform (winch speed is approx 60m per

    minute).

    2. F&G System and Fire Fighting System on

    the DLB

    3. ERP

    4. Portable Gas Detector on the STERN of

    the DLB.

    NOTE: based on 10mm hole during the study,

    the dispersion of HC release / gas cloud

    would NOT reach the DLB.

    1 1 LR

    6 Ignition Source

    on DLB

    - Gas Release

    (100mm hole on

    Gas-Gas

    Exchanger) with

    20knots wind

    speed toward

    the DLB

    7 Emergency (Fire)

    on DLB

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 11 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Helicopter Emergency

    on DLB

    Increase Risk of Fire on

    Platform (AGX) if there is

    concurrent HC Release

    2 2 LR 1. DLB can be pulled / winched away from the

    Platform (winch speed is approx 60m per

    minute).

    2. F&G System and Fire Fighting System on

    the DLB

    3. ERP

    4. Portable Gas Detector on the STERN of

    the DLB.

    NOTE: based on 10mm hole during the study,

    the dispersion of HC release / gas cloud

    would NOT reach the DLB.

    1 1 LR

    Failure of Main

    Generator / Black Out

    on DLB

    DLB cannot pull away in

    case required

    3 2 LR 1. Redundancy of Generators

    2. Emergency Power Generator

    3. Fail Safe Brake on the anchor winches

    4. AHT / Tow Tug standby in the field at all

    time

    5. PM System on DLB

    1 1

    Increasing Flaring Rate

    due to Blow Down Event

    Increase Radiant Heat in the

    vicinity of AGX Crane

    NOTE: No Effect anticipated

    to the DLB based on Flare

    Radiation Study

    2 2 LR 1. Radiant Heat Study for AGX shows that it

    is safe for the Crane Operator to be inside the

    Crane Cabin during Full Process Blow Down.

    2. Proximity of DLB Crane Operator is farther

    from the Flare Tip therefore impact of Radiant

    Heat is minimal.

    1 1 LR

    ESD Event Causing

    AGX Process Instability

    Creates changes in Process

    System Pressure,

    Temperature, and Liquid

    Inventory which could lead

    to an increase potential for

    HC release

    2 2 LR 1. Process System is designed to fail safe

    2. Process is continuosly monitored from

    CCR

    3. Process System will be maintained and

    functional with no significant case to operate

    in place during SIMOPS

    4. Contingency Plan in place such that AGX

    Project Team will be asked to leave AGX until

    ESD event has been rectified

    5. COntingency Plan in place such that HOFO

    will communicate potential for escalation to

    DLB such that preparation may made for DLB

    withdrawl from AGX vicinity.

    1 1 LR

    7 Emergency (Fire)

    on DLB

    8 Process Upset

    on AGX

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 12 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    Gas Release Anoa

    Riser

    Fire / Explosion

    Personnel Injury

    5 2 HR 1. Mitigation as per CTO Procedure

    2. F&G System on AGX

    3. ERP Procedures

    4. Platform will inform the DLB in case of F&G

    detection system on platform is activated

    5. DLB can be pulled / winched away to clear

    from platform (winch speed approx 60m per

    minute)

    5 1 HR

    9 Helicopter

    Operation on

    DLB

    Interference with Crane

    Operation

    Helicopter collision with

    Cranes / Crash

    Personnel injury / Lost of life

    4 3 HR 1. Crane Operations on DLB will be shut

    down and/or crane boom would be clear for

    Helicopter Operations

    2. Trained and experienced HLO

    3. Inform Crane Operators of Incoming

    Helicopters

    4. ERP

    3 1 LR

    10 Vessel

    Movement /

    alongside on

    DLB

    Collision with the DLB /

    Platform / Material

    Barge / Anchor Buoy /

    Anchor Wire

    Asset damage

    Personnel injury / Lost of life

    Schedule delay

    4 3 HR 1. Suitable Vessels (Include MWS

    inspection/approval)

    2. Competent Vessel Captain

    3. Slack Anchor Wires if required

    4. Good communication between paties

    involved

    5. Weather limit

    6. Adequate fendering on DLB and vessels

    7. Briefing to all Vessel Captain prior to

    entering 500m zone

    8. High Vis painted Anchor Buoys

    9. Comply with POI Marine Operation

    Procedure

    10. Establish communication with HOFO prior

    to entering 500m Zone and/or Marine

    Supertindent prior to approaching DLB

    2 2 LR

    11 SIMOPS

    Operation

    Between DLB

    Crane and AGX

    Crane

    DLB Crane Boom

    collision with the AGX

    Crane

    Damage asset

    Personnel injury

    Schedule delay

    4 3 HR 1. All Cranes will be under the control of the

    Project (CTR).

    2. Designated Person In Charge for Every Lift

    3. Good illumincation

    4. Procedure control for Cranes Operations

    (SIMOPS)

    5. Detail planning meeting for Crane

    Operations

    3 1 LR

    8 Process Upset

    on AGX

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 13 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    12 Personnel

    Transfer

    Personnel being

    Transferred Fall from

    Height

    Personnel injury / Lost of life 5 3 HR 1. Certified and good condition Crane

    2. Certified and good condition FROG

    3. Certified and good condition rigging

    4. Provision of safety sling

    5. No personnel transfer untill the Vessel will

    be securely moored

    6. Distance of free board between DLB and

    vessel is small

    7. Provision of tag lines

    8. Familiarization for transfer using FROG

    9. Maintain good communicaton among

    parties involved (CO, Bunksman, and

    Riggers).

    10. Weather limit defined for personnel

    transferring using FROG and Crawler Crane

    2 1 LR

    Pool Fire on ANOA

    coming from ANOA 8"

    Riser Pipeline

    Personnel injury / Lost of life

    Impair both ANOA and AGX

    Muster Area

    5 1 HR 1. All personnel shall muster to DLB including

    POI Personnel

    2. Corrosion Monitoring and Pigging Pipeline

    covered by FIMS

    3. PSLL on the pipeline

    4. Daily surface inspection

    5. DLB will be pull / winched away

    5 1 HR

    Condensate on the sea

    due SKIM pile overfilled

    Personnel Injury / Lost of

    Life

    3 1 MR 1. Level Management

    2. Daily surface inspection

    3. DLB will be pull / winched away

    1 1 LR

    5 Verify the certification of the

    storage tank and inspection

    prior to mobilization offshore

    Timas / PNS

    6 Review the N2 handling and

    storage procedure

    Timas / PNS

    N2 Spill Personnel Injury

    Cryogenic

    Embrittlement

    3 3 MR 1. Engineered and certified ISO Storage

    Tanks

    2. Scaffold and bunded area

    3. Use of planks and tarpaulin

    3 2 MR

    3

    13 MAE on

    AGX/ANOA

    MR 1. Engineered and certified ISO Storage

    Tanks

    2. Scaffold and bunded area

    3. Use of planks and tarpaulin

    3 2 MR14 N2 Operation Extreme Temperature

    (minus 160 - minus 200

    C)

    Personnel injury

    Cryogenic

    Embrittlement

    3

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 14 of 15

  • HAZID WORKSHEET

    S L R S L R

    Initial RiskNo Type of Event Potential Hazards Consequences

    Safeguards

    (Existing and Recommended Control

    Measures)

    REC # Recommendation Action PartyResidual Risk

    15 3rd Party Vessel

    / Security

    Collision with the

    Anchor Buoy / Anchor

    Wire

    Personnel Injury

    Asset Damage

    Schedule Delay

    3 2 MR 1. High Vis Anchor Buoy

    2. Standy By Vessels

    3. Radar Watch

    4. Intensity of Marine Activities would deter

    the 3rd Party Vessel to stay away

    5. Liaison Officer onboard of DLB

    3 1 LR

    16 Sabotage Construction Crew

    tempering with Platform

    and DLB system

    Increase risk of incident 3 2 MR 1. Socialization of work to the offshore

    construction team in advance

    2. PTW, JSA, and workpacks

    3. Involve operation team during work pack

    review and execution of the works

    4. Maintain positive working environment,

    provide motivation

    5. Restriction to sensitve areas (security

    measures) e.g. safety / warning signs,

    socialize restricted areas during

    meeting/awareness, Access Control

    6. Maintain adequate supervision / QC

    7. Reward program

    3 1 LR 7 Operation to review the

    existing "security measures"

    and improve as required

    POI

    17 Communication

    between DLB

    and its Support

    Vessels and

    between DLB

    and AGX/ANOA

    Clear Communication

    Method NOT

    established

    Increase risk of

    miscommunication /

    interference leading to

    incident resulting to:

    - Personnel injury

    - Asset damage

    3 2 MR 1. ANOA HSE Induction / Awareness

    2. Various coordination meeting e.g. daily

    planning meeting

    3. Provision of radio communication

    4. English speaking key personnel

    5. Permission to be obtained from HOFO prior

    to entering 500m zone

    6. Permission to be obtained from Marine

    Superintendent for approaching DLB or

    entering the Anchor Pattern

    7. Competent Vessel Captain

    8. Briefing of all support vessels include

    socialization of procedures

    9. Complete GO and No GO Checklist.

    3 1 LR 8 Establish radio

    communication channel for

    all parties to minimize

    interference

    Timas/POI

    HAZID Study for Premier ANOA Phase 4 - AGX Compression Reconfiguration Project N1 Page 15 of 15