Scope: This assessment converts the submitted HAZOP study (1123 rows, 58 nodes) into bowtie format. The submitted study covers 10 of 32 mandatory systems for a complete CCGT asset-level scope (31% mandatory coverage; classification LIMITED). The remaining 22 mandatory systems (of 32 in total) are outside the submitted scope and are not represented in this bowtie package; see §2.3 for the full scope coverage table. Conclusions in this report relate only to the packages studied; a complete asset-level risk picture requires extension of the HAZOP to the excluded scope before operational decisions, lender engagement, or regulatory submission.
Scope Coverage: 10 of 32 mandatory systems -- LIMITED
This Bowtie Risk Assessment evaluated 19 Major Accident Hazard scenarios across Copy_of_Qasim_HAZOP_report_Excel.xlsx (CCGT), developing 19 bowtie diagrams encompassing 47 threat pathways and 50 consequence pathways. A total of 134 prevention barriers and 99 mitigation barriers were identified and assessed against CCPS / EI barrier validity criteria (Effective, Independent, Auditable). The assessment is based on desk review of the source HAZOP (1123 rows, 355 scenarios at S>=3) and carries an evidence confidence cap of 40/100. All outputs require validation by the Process Safety Team.
System-level adequacy ratings combining prevention coverage and mitigation specificity. Priority is set by the worse of the two ratings combined with the system's maximum consequence severity.
| System | Max S | Prev. | Mit. | Prevention Adequacy | Mitigation Adequacy | Overall | Priority |
|---|---|---|---|---|---|---|---|
| LP Steam | S=4 | 8 | 5 | Low | |||
| HRSG LP | S=5 | 8 | 5 | Low | |||
| HRSG Duct Burner | S=5 | 5 | 7 | Low | |||
| Fuel Gas | S=5 | 16 | 7 | Low | |||
| STG Steam | S=4 | 12 | 5 | Low | |||
| STG Lube Oil | S=4 | 5 | 5 | Low | |||
| HRSG HP | S=4 | 12 | 5 | Low | |||
| HRSG Bypass | S=4 | 3 | 5 | Low | |||
| HRH Steam | S=4 | 8 | 5 | Low | |||
| HP Steam | S=4 | 9 | 5 | Low | |||
| CRH Steam | S=4 | 4 | 3 | Low | |||
| Auxiliary Steam | S=4 | 6 | 5 | Low | |||
| ACC | S=4 | 6 | 5 | Low | |||
| STG Seals | S=5 | 8 | 5 | Low | |||
| HRSG IP | S=5 | 6 | 5 | Low | |||
| Generator H2 | S=5 | 5 | 5 | Low | |||
| Feedwater | S=5 | 9 | 4 | Low | |||
| Ammonia/SCR | S=4 | 4 | 6 | High | |||
| Fuel Oil | S=5 | 0 | 7 | Critical |
| # | Recommendation | Type | Scope | Owner | Target |
|---|---|---|---|---|---|
| 1 | Conduct supplementary HAZOP workshop focused on non-hardware barriers (emergency procedures, PTW, competency, SOPs). | Verification | All 19 systems | Process Safety Lead | 90 days |
| 2 | Validate suggested mitigation barriers against actual plant design and installed protection systems. | Verification | All systems with library-seeded mitigation | Process Safety Lead | 60 days |
| 3 | Confirm prevention coverage for unprotected threat pathways -- verify whether barriers exist but were not documented in the HAZOP. | Engineering | 15 threat pathways | I&C Engineering | 60 days |
| 4 | Verify SIL ratings on safety-instrumented functions against IEC 61511 design basis and operational performance records. | Verification | All SIL-credited barriers | I&C Engineering | 120 days |
| 5 | Run a multi-discipline barrier-diversity review (Operations, Maintenance, HSE, I&C) to identify non-hardware barriers that exist at the plant. | Workshop | Cross-cutting (all systems) | HSSE Manager | 90 days |
| 6 | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | Improvement | ACC | Process Safety Lead | 60 days |
| 7 | Extend HAZOP scope to cover the missing mandatory systems: Fuel Gas Receiving Station, Gas Turbine Lubrication System, GT Enclosure Ventilation and Fire Suppression, HRSG Drums (HP/IP/LP) and Downcomer System, Superheater and Reheater, Econ | Improvement | Cross-cutting (all systems) | Process Safety Lead | 60 days |
| 8 | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | Improvement | Auxiliary Steam | Process Safety Lead | 60 days |
Based on this desk-review assessment, risks from 2 of 19 MAH scenarios cannot be confirmed as ALARP until the priority recommendations are addressed. The principal concerns are Ammonia/SCR, Fuel Oil where barrier coverage falls below industry good practice for CCGT facilities. The 25 Critical and 38 Major findings identified in Section 9 represent the minimum actions required before an ALARP demonstration can be completed. A formal ALARP assessment requires site-validated PFD data and operational performance evidence, which are outside the scope of this desk review.
This report converts the HAZOP study for Copy_of_Qasim_HAZOP_report_Excel.xlsx into structured bowtie risk assessment diagrams per CCPS / EI "Bow Ties in Risk Management" (2018). Objectives: (a) classify HAZOP safeguards as prevention or mitigation barriers, (b) identify gaps where barriers are missing or weakened, (c) derive the SCE/SCA register with FARSI performance standards, and (d) produce a Synergi-compatible barrier register for downstream import.
HAZOP source: 1123 rows analysed, 355 scenarios with severity S>=3 (SPEC-XL §5 step 1 filter). Out of scope: electrical protection systems (covered in a separate E-HAZOP study), and equipment with no S>=3 scenarios.
The submitted HAZOP is benchmarked against the Ascendera Reference Scope v1.0 for CCGT (40 reference systems, 32 mandatory). Scope Coverage: 10 of 32 mandatory systems -- LIMITED
Submitted HAZOP covers 10 of 32 mandatory systems for CCGT scope (31% mandatory coverage). Classification: LIMITED. Missing mandatory: Fuel Gas Receiving Station, Gas Turbine Lubrication System, GT Enclosure Ventilation and Fire Suppression, HRSG Drums (HP/IP/LP) and Downcomer System, Superheater and Reheater, Economiser, Steam Turbine Lube, Seal, and Control Oil, Condensate Polishing, Demineralisation Water Treatment, Boiler Water Chemical Dosing, Generator Step-Up Transformer, Unit Auxiliary and Station Service Transformers, HV / EHV Switchyard (AIS or GIS), Medium Voltage Switchgear, Emergency Diesel Generator, Distributed Control System and SCADA, Safety Instrumented System / Emergency Shutdown, Fire and Gas Detection, Special Hazard Fire Suppression, Plant Service Air, Nitrogen Generation and Distribution, HVAC for MCC, Chemical Buildings, Control Room. Conclusions in this report relate only to the packages studied; a complete asset-level risk picture requires extension of the HAZOP to the excluded scope.
| Reference System | Classification | Status | Matched HAZOP Node | Rationale |
|---|---|---|---|---|
| Fuel Gas Heating, Filtration and Let-down | Mandatory | 48. FGS NODE 10 Common condensate tank for fuel gas conditioning area (NET capacity: 5 M3) | Node '48. FGS NODE 10 Common condensate tank for fuel gas conditioning area (NET capacity: 5 M3)' matched 'Fuel Gas Heating, Filtration and Let-down' (fuzzy ratio 100). | |
| Gas Turbine and Enclosure | Mandatory | 28. STG NODE 3 Steam System for HP Steam Turbine | Node '28. STG NODE 3 Steam System for HP Steam Turbine' matched 'Gas Turbine and Enclosure' (fuzzy ratio 78). | |
| Gas Turbine Fuel Manifold, Nozzles, Purge | Mandatory | 13. Fuel Oil System | Node '13. Fuel Oil System' matched 'Gas Turbine Fuel Manifold, Nozzles, Purge' (fuzzy ratio 85). | |
| Steam Turbine | Mandatory | 28. STG NODE 3 Steam System for HP Steam Turbine | Node '28. STG NODE 3 Steam System for HP Steam Turbine' matched 'Steam Turbine' (fuzzy ratio 100). | |
| Condenser (Surface or Air-Cooled) | Mandatory | 30. STG NODE 5 Turbine Sealing System with Gland Condenser | Node '30. STG NODE 5 Turbine Sealing System with Gland Condenser' matched 'Condenser (Surface or Air-Cooled)' (fuzzy ratio 100). | |
| Feedwater System (HP / IP / LP) | Mandatory | 1. HP steam System | Node '1. HP steam System' matched 'Feedwater System (HP / IP / LP)' (fuzzy ratio 75). | |
| Air-Cooled Condenser | Conditional | 56. ACC NODE 1 Steam & Condensate Collection System | Node '56. ACC NODE 1 Steam & Condensate Collection System' matched 'Air-Cooled Condenser' (fuzzy ratio 100). | |
| Auxiliary (Closed-Loop) Cooling Water System | Mandatory | 10. Raw Water System | Node '10. Raw Water System' matched 'Auxiliary (Closed-Loop) Cooling Water System' (fuzzy ratio 86). | |
| Generator, Exciter, Cooling, Seal Oil | Mandatory | 38. STG NODE 13 Generator Shaft Seal System | Node '38. STG NODE 13 Generator Shaft Seal System' matched 'Generator, Exciter, Cooling, Seal Oil' (fuzzy ratio 100). | |
| Plant Fire Water System | Mandatory | 10. Raw Water System | Node '10. Raw Water System' matched 'Plant Fire Water System' (fuzzy ratio 86). | |
| Instrument Air Compression, Drying, Distribution | Mandatory | 32. STG NODE 7 Instrument Air System for STG | Node '32. STG NODE 7 Instrument Air System for STG' matched 'Instrument Air Compression, Drying, Distribution' (fuzzy ratio 100). | |
| Fuel Gas Receiving Station | Mandatory | — | No submitted HAZOP node matched 'Fuel Gas Receiving Station' (best fuzzy ratio 62 below threshold 75). | |
| Gas Turbine Lubrication System | Mandatory | — | No submitted HAZOP node matched 'Gas Turbine Lubrication System' (best fuzzy ratio 65 below threshold 75). | |
| GT Enclosure Ventilation and Fire Suppression | Mandatory | — | No submitted HAZOP node matched 'GT Enclosure Ventilation and Fire Suppression' (best fuzzy ratio 48 below threshold 75). | |
| HRSG Drums (HP/IP/LP) and Downcomer System | Mandatory | — | No submitted HAZOP node matched 'HRSG Drums (HP/IP/LP) and Downcomer System' (best fuzzy ratio 60 below threshold 75). | |
| Superheater and Reheater | Mandatory | — | No submitted HAZOP node matched 'Superheater and Reheater' (best fuzzy ratio 51 below threshold 75). | |
| Economiser | Mandatory | — | No submitted HAZOP node matched 'Economiser' (best fuzzy ratio 42 below threshold 75). | |
| Steam Turbine Lube, Seal, and Control Oil | Mandatory | — | No submitted HAZOP node matched 'Steam Turbine Lube, Seal, and Control Oil' (best fuzzy ratio 65 below threshold 75). | |
| Condensate Polishing | Mandatory | — | No submitted HAZOP node matched 'Condensate Polishing' (best fuzzy ratio 74 below threshold 75). | |
| Demineralisation Water Treatment | Mandatory | — | No submitted HAZOP node matched 'Demineralisation Water Treatment' (best fuzzy ratio 62 below threshold 75). | |
| Boiler Water Chemical Dosing | Mandatory | — | No submitted HAZOP node matched 'Boiler Water Chemical Dosing' (best fuzzy ratio 53 below threshold 75). | |
| Generator Step-Up Transformer | Mandatory | — | No submitted HAZOP node matched 'Generator Step-Up Transformer' (best fuzzy ratio 60 below threshold 75). | |
| Unit Auxiliary and Station Service Transformers | Mandatory | — | No submitted HAZOP node matched 'Unit Auxiliary and Station Service Transformers' (best fuzzy ratio 62 below threshold 75). | |
| HV / EHV Switchyard (AIS or GIS) | Mandatory | — | No submitted HAZOP node matched 'HV / EHV Switchyard (AIS or GIS)' (best fuzzy ratio 0 below threshold 75). | |
| Medium Voltage Switchgear | Mandatory | — | No submitted HAZOP node matched 'Medium Voltage Switchgear' (best fuzzy ratio 0 below threshold 75). | |
| Emergency Diesel Generator | Mandatory | — | No submitted HAZOP node matched 'Emergency Diesel Generator' (best fuzzy ratio 72 below threshold 75). | |
| Distributed Control System and SCADA | Mandatory | — | No submitted HAZOP node matched 'Distributed Control System and SCADA' (best fuzzy ratio 60 below threshold 75). | |
| Safety Instrumented System / Emergency Shutdown | Mandatory | — | No submitted HAZOP node matched 'Safety Instrumented System / Emergency Shutdown' (best fuzzy ratio 57 below threshold 75). | |
| Fire and Gas Detection | Mandatory | — | No submitted HAZOP node matched 'Fire and Gas Detection' (best fuzzy ratio 48 below threshold 75). | |
| Special Hazard Fire Suppression | Mandatory | — | No submitted HAZOP node matched 'Special Hazard Fire Suppression' (best fuzzy ratio 0 below threshold 75). | |
| Plant Service Air | Mandatory | — | No submitted HAZOP node matched 'Plant Service Air' (best fuzzy ratio 59 below threshold 75). | |
| Nitrogen Generation and Distribution | Mandatory | — | No submitted HAZOP node matched 'Nitrogen Generation and Distribution' (best fuzzy ratio 62 below threshold 75). | |
| HVAC for MCC, Chemical Buildings, Control Room | Mandatory | — | No submitted HAZOP node matched 'HVAC for MCC, Chemical Buildings, Control Room' (best fuzzy ratio 42 below threshold 75). | |
| Fuel Oil Receiving, Storage, Transfer | Conditional | — | No submitted HAZOP node matched 'Fuel Oil Receiving, Storage, Transfer' (best fuzzy ratio 70 below threshold 75). | |
| Selective Catalytic Reduction (SCR) | Conditional | — | No submitted HAZOP node matched 'Selective Catalytic Reduction (SCR)' (best fuzzy ratio 0 below threshold 75). | |
| Once-Through Cooling Water Intake and Outfall | Conditional | — | No submitted HAZOP node matched 'Once-Through Cooling Water Intake and Outfall' (best fuzzy ratio 63 below threshold 75). | |
| Wet Mechanical- or Natural-Draft Cooling Tower | Conditional | — | No submitted HAZOP node matched 'Wet Mechanical- or Natural-Draft Cooling Tower' (best fuzzy ratio 70 below threshold 75). | |
| Black Start Capability | Conditional | — | No submitted HAZOP node matched 'Black Start Capability' (best fuzzy ratio 0 below threshold 75). | |
| Burner Management System | Conditional | — | No submitted HAZOP node matched 'Burner Management System' (best fuzzy ratio 44 below threshold 75). | |
| Auxiliary (Startup) Boiler | Conditional | — | No submitted HAZOP node matched 'Auxiliary (Startup) Boiler' (best fuzzy ratio 72 below threshold 75). |
| Standard | Application |
|---|---|
| IEC 61882:2016 | HAZOP study methodology (source data) |
| CCPS / EI Bow Ties in Risk Management (2018) | Bowtie methodology, barrier criteria |
| IEC / ISO 31010:2019 | Risk assessment techniques framework |
| IEC 61511:2016 | SIS requirements for SIL-rated barriers |
| IOGP Report 544 | Barrier standardisation and classification |
| API RP 754 | Process safety performance indicators |
| Energy Institute SCE Performance Standards (2019) | FARSI model for performance standards |
Evidence confidence is capped at 65/100 for any desk-review run. Site verification is a separate, paid activity that is not covered by this report. Every page footer carries the FOR REVIEW -- REQUIRES PROCESS SAFETY TEAM VALIDATION notice.
Facility name: Copy_of_Qasim_HAZOP_report_Excel.xlsx
Technology: CCGT
HAZOP source file: /data/output/b8e28fef-37fc-4c5b-868a-febe49c1beb1/input.xlsx
HAZOP rows ingested: 1123
Asset boundaries follow the systems defined in the source HAZOP. See Section 5 for system-by-system breakdown including hazardous inventory, operating envelope, threat pathways, and barrier coverage. Section 4 lists the Major Accident Hazards this assessment addresses.
The following MAH register summarises every Major Accident Hazard scenario identified at this facility. Each MAH maps to one bowtie diagram in Section 5.
| MAH ID | System | Hazard | Top Event | Max Severity | Bowtie Ref |
|---|---|---|---|---|---|
| MAH-CCGT-AC-001 | ACC | Air cooled condenser | Loss of containment from air-cooled condenser | S=4 (D) | BT-CCGT-AC-001 |
| MAH-CCGT-AX-001 | Auxiliary Steam | Auxiliary steam system for deaerator and tracing | Loss of containment of auxiliary steam | S=4 (D) | BT-CCGT-AX-001 |
| MAH-CCGT-BY-001 | HRSG Bypass | HP/IP/LP bypass valves dumping steam to condenser during trip | Loss of containment from HRSG bypass and casing | S=4 (D) | BT-CCGT-BY-001 |
| MAH-CCGT-DB-001 | HRSG Duct Burner | Natural gas fired duct burner in HRSG | Uncontrolled release from HRSG duct burner | S=5 (E) | BT-CCGT-DB-001 |
| MAH-CCGT-FG-001 | Fuel Gas | Pressurised natural gas in fuel gas supply pipework | Loss of containment of natural gas from fuel gas system | S=5 (E) | BT-CCGT-FG-001 |
| MAH-CCGT-FO-001 | Fuel Oil | Backup fuel oil (HFO / LFO) supply system | Loss of containment of fuel oil | S=5 (E) | BT-CCGT-FO-001 |
| MAH-CCGT-FW-001 | Feedwater | High pressure boiler feedwater | Loss of containment from feedwater system | S=5 (E) | BT-CCGT-FW-001 |
| MAH-CCGT-GH-001 | Generator H2 | Hydrogen cooling gas in generator casing | Uncontrolled release of hydrogen from generator | S=5 (E) | BT-CCGT-GH-001 |
| MAH-CCGT-HI-001 | HRSG IP | IP water/steam in HRSG IP section | Loss of containment from HRSG IP section | S=5 (E) | BT-CCGT-HI-001 |
| MAH-CCGT-HL-001 | HRSG LP | LP water/steam in HRSG LP section | Loss of containment from HRSG LP section | S=5 (E) | BT-CCGT-HL-001 |
| MAH-CCGT-HP-001 | HP Steam | High pressure superheated steam in HP steam header | Loss of containment of HP steam | S=4 (D) | BT-CCGT-HP-001 |
| MAH-CCGT-HR-001 | HRSG HP | HP water/steam in HRSG HP section (economiser, evaporator, superheater) | Loss of containment from HRSG HP section | S=4 (D) | BT-CCGT-HR-001 |
| MAH-CCGT-LP-001 | LP Steam | LP steam header distribution | Loss of containment of LP steam | S=4 (D) | BT-CCGT-LP-001 |
| MAH-CCGT-NH-001 | Ammonia/SCR | Aqueous ammonia (19-25%) for SCR injection | Uncontrolled release of ammonia | S=4 (A) | BT-CCGT-NH-001 |
| MAH-CCGT-SS-001 | STG Steam | HP/IP/LP steam within steam turbine casing | Loss of containment from steam turbine | S=4 (D) | BT-CCGT-SS-001 |
| MAH-CR-001 | CRH Steam | Condensate in CRH Steam | Loss of containment of cold reheat steam | S=4 (D) | BT-CR-001 |
| MAH-HH-001 | HRH Steam | Steam in HRH Steam | Loss of containment of hot reheat steam | S=4 (D) | BT-HH-001 |
| MAH-SL-001 | STG Seals | Hydrogen in STG Seals | Loss of containment from turbine shaft seals | S=5 (E) | BT-SL-001 |
| MAH-LO-001 | STG Lube Oil | Lube oil in STG Lube Oil | Loss of containment of lube oil from ST system | S=4 (D) | BT-LO-001 |
One sub-section per system. Each contains the system description, the hazard, the bowtie SVG, the barrier register, and the gap findings specific to that system.
Catalogue ref: BT-CCGT-AC-001
Hazard: Air cooled condenser
Top Event: Loss of containment from air-cooled condenser
Max severity: S=4 | Prev barriers: 6 | Mit barriers: 5 |
Gaps: 2
ACC has 6 prevention and 5 mitigation barriers. Of these, 6 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 1 of 2 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 3 barrier types (Hardware - Active, Organizational, Procedural). Barrier effectiveness from desk review: 64% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-AX-001
Hazard: Auxiliary steam system for deaerator and tracing
Top Event: Loss of containment of auxiliary steam
Max severity: S=4 | Prev barriers: 6 | Mit barriers: 5 |
Gaps: 2
Auxiliary Steam has 6 prevention and 5 mitigation barriers. Of these, 6 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 1 of 2 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 3 barrier types (Hardware - Active, Organizational, Procedural). Barrier effectiveness from desk review: 64% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-BY-001
Hazard: HP/IP/LP bypass valves dumping steam to condenser during trip
Top Event: Loss of containment from HRSG bypass and casing
Max severity: S=4 | Prev barriers: 3 | Mit barriers: 5 |
Gaps: 2
HRSG Bypass has 3 prevention and 5 mitigation barriers. Of these, 3 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 1 of 2 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 3 barrier types (Hardware - Active, Organizational, Procedural). Barrier effectiveness from desk review: 50% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-DB-001
Hazard: Natural gas fired duct burner in HRSG
Top Event: Uncontrolled release from HRSG duct burner
Max severity: S=5 | Prev barriers: 5 | Mit barriers: 7 |
Gaps: 2
HRSG Duct Burner has 5 prevention and 7 mitigation barriers. Of these, 5 were traced to HAZOP safeguards while 7 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 2 barrier types (Hardware - Active, Hardware - Passive). Barrier effectiveness from desk review: 58% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 3 consequence-specific barriers parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-FG-001
Hazard: Pressurised natural gas in fuel gas supply pipework
Top Event: Loss of containment of natural gas from fuel gas system
Max severity: S=5 | Prev barriers: 16 | Mit barriers: 7 |
Gaps: 3
Fuel Gas has 16 prevention and 7 mitigation barriers. Of these, 17 were traced to HAZOP safeguards while 6 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 3 barrier types (Hardware - Active, Hardware - Passive, Procedural). Barrier effectiveness from desk review: 70% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-FO-001
Hazard: Backup fuel oil (HFO / LFO) supply system
Top Event: Loss of containment of fuel oil
Max severity: S=5 | Prev barriers: 0 | Mit barriers: 7 |
Gaps: 3
Fuel Oil has 0 prevention and 7 mitigation barriers. Of these, 2 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 3 of 3 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 2 barrier types (Hardware - Active, Hardware - Passive). Barrier effectiveness from desk review: 57% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 3 consequence-specific barriers parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-FW-001
Hazard: High pressure boiler feedwater
Top Event: Loss of containment from feedwater system
Max severity: S=5 | Prev barriers: 9 | Mit barriers: 4 |
Gaps: 1
Feedwater has 9 prevention and 4 mitigation barriers. Of these, 9 were traced to HAZOP safeguards while 4 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 4 barrier types (Hardware - Active, Hardware - Passive, Organizational, Procedural). Barrier effectiveness from desk review: 77% Effective; the remainder are Partially Effective and need site validation.
Catalogue ref: BT-CCGT-GH-001
Hazard: Hydrogen cooling gas in generator casing
Top Event: Uncontrolled release of hydrogen from generator
Max severity: S=5 | Prev barriers: 5 | Mit barriers: 5 |
Gaps: 2
Generator H2 has 5 prevention and 5 mitigation barriers. Of these, 5 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 1 of 3 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 2 barrier types (Hardware - Active, Hardware - Passive). Barrier effectiveness from desk review: 80% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 2 consequence-specific barriers parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-HI-001
Hazard: IP water/steam in HRSG IP section
Top Event: Loss of containment from HRSG IP section
Max severity: S=5 | Prev barriers: 6 | Mit barriers: 5 |
Gaps: 3
HRSG IP has 6 prevention and 5 mitigation barriers. Of these, 6 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 1 of 2 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 4 barrier types (Hardware - Active, Hardware - Passive, Organizational, Procedural). Barrier effectiveness from desk review: 55% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-HL-001
Hazard: LP water/steam in HRSG LP section
Top Event: Loss of containment from HRSG LP section
Max severity: S=5 | Prev barriers: 8 | Mit barriers: 5 |
Gaps: 3
HRSG LP has 8 prevention and 5 mitigation barriers. Of these, 8 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 4 barrier types (Hardware - Active, Hardware - Passive, Organizational, Procedural). Barrier effectiveness from desk review: 54% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-HP-001
Hazard: High pressure superheated steam in HP steam header
Top Event: Loss of containment of HP steam
Max severity: S=4 | Prev barriers: 9 | Mit barriers: 5 |
Gaps: 3
HP Steam has 9 prevention and 5 mitigation barriers. Of these, 9 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 1 of 4 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 4 barrier types (Hardware - Active, Hardware - Passive, Organizational, Procedural). Barrier effectiveness from desk review: 64% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-HR-001
Hazard: HP water/steam in HRSG HP section (economiser, evaporator, superheater)
Top Event: Loss of containment from HRSG HP section
Max severity: S=4 | Prev barriers: 12 | Mit barriers: 5 |
Gaps: 6
HRSG HP has 12 prevention and 5 mitigation barriers. Of these, 12 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 2 of 4 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 4 barrier types (Hardware - Active, Hardware - Passive, Organizational, Procedural). Barrier effectiveness from desk review: 59% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-LP-001
Hazard: LP steam header distribution
Top Event: Loss of containment of LP steam
Max severity: S=4 | Prev barriers: 8 | Mit barriers: 5 |
Gaps: 1
LP Steam has 8 prevention and 5 mitigation barriers. Of these, 8 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 4 barrier types (Hardware - Active, Hardware - Passive, Organizational, Procedural). Barrier effectiveness from desk review: 69% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-NH-001
Hazard: Aqueous ammonia (19-25%) for SCR injection
Top Event: Uncontrolled release of ammonia
Max severity: S=4 | Prev barriers: 4 | Mit barriers: 6 |
Gaps: 3
Ammonia/SCR has 4 prevention and 6 mitigation barriers. Of these, 4 were traced to HAZOP safeguards while 6 were identified from domain knowledge or engineering standards and require site verification. 2 of 3 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 3 barrier types (Hardware - Active, Human - Active, Organizational). Barrier effectiveness from desk review: 50% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CCGT-SS-001
Hazard: HP/IP/LP steam within steam turbine casing
Top Event: Loss of containment from steam turbine
Max severity: S=4 | Prev barriers: 12 | Mit barriers: 5 |
Gaps: 2
STG Steam has 12 prevention and 5 mitigation barriers. Of these, 12 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 1 of 3 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 4 barrier types (Hardware - Active, Human - Active, Organizational, Procedural). Barrier effectiveness from desk review: 76% Effective; the remainder are Partially Effective and need site validation. Mitigation includes 1 consequence-specific barrier parented to individual consequences (event-tree branching).
Catalogue ref: BT-CR-001
Hazard: Condensate in CRH Steam
Top Event: Loss of containment of cold reheat steam
Max severity: S=4 | Prev barriers: 4 | Mit barriers: 3 |
Gaps: 1
CRH Steam has 4 prevention and 3 mitigation barriers. Of these, 4 were traced to HAZOP safeguards while 3 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 3 barrier types (Hardware - Active, Hardware - Passive, Organizational). Barrier effectiveness from desk review: 71% Effective; the remainder are Partially Effective and need site validation.
Catalogue ref: BT-HH-001
Hazard: Steam in HRH Steam
Top Event: Loss of containment of hot reheat steam
Max severity: S=4 | Prev barriers: 8 | Mit barriers: 5 |
Gaps: 1
HRH Steam has 8 prevention and 5 mitigation barriers. Of these, 8 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 3 barrier types (Hardware - Active, Organizational, Procedural). Barrier effectiveness from desk review: 69% Effective; the remainder are Partially Effective and need site validation.
Catalogue ref: BT-SL-001
Hazard: Hydrogen in STG Seals
Top Event: Loss of containment from turbine shaft seals
Max severity: S=5 | Prev barriers: 8 | Mit barriers: 5 |
Gaps: 1
STG Seals has 8 prevention and 5 mitigation barriers. Of these, 8 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 2 barrier types (Hardware - Active, Hardware - Passive). Barrier effectiveness from desk review: 85% Effective; the remainder are Partially Effective and need site validation.
Catalogue ref: BT-LO-001
Hazard: Lube oil in STG Lube Oil
Top Event: Loss of containment of lube oil from ST system
Max severity: S=4 | Prev barriers: 5 | Mit barriers: 5 |
Gaps: 2
STG Lube Oil has 5 prevention and 5 mitigation barriers. Of these, 5 were traced to HAZOP safeguards while 5 were identified from domain knowledge or engineering standards and require site verification. 1 of 2 specific threat pathways carry no prevention barrier -- these are unprotected initiating-event scenarios that need either safeguard documentation in the HAZOP or an engineering review. Defence-in-depth includes 3 barrier types (Hardware - Active, Hardware - Passive, Procedural). Barrier effectiveness from desk review: 80% Effective; the remainder are Partially Effective and need site validation.
Every barrier identified across the assessment, with side, category,
condition, PFD/SIL where known, and provenance tier. Three quality
columns help reviewers scope their verification: Independence
flags barriers that depend on another (e.g. operator response to an
alarm); Shared Count shows how many systems carry the same
barrier title (a high count signals systemic dependency);
EIA Status is the desk-review Effective / Independent / Auditable
validity bucket (Valid / Conditional / Verify / Concern). Cross-references
the WORLD_CLASS.xlsx Bowtie Elements sheet.
| ID | System | Barrier | Side | Category | Condition | PFD | SIL | Provenance | Provenance Detail | Independence | Shared | EIA |
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| PB-AC-019 | ACC | ACC is designed for worst case scenario including opening of LP/IP bypass. | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3634 S=4. | Independent | 1 | Valid | ||
| PB-AC-018 | ACC | FAL-10LCA04-CF101A/B: Flow alarm low (1oo2) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3623 FAL-10LCA04-CF101A/B S=4. Also protects Condensate (FAL-10LCA04-CF101A/B). | Independent | 2 | Valid | ||
| PB-AC-017 | ACC | MOV-10MAJ45-AA075: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3612 MOV-10MAJ45-AA075 S=4. | Independent | 1 | Valid | ||
| PB-AC-016 | ACC | MOV-10LBG45-AA080: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3606 MOV-10LBG45-AA080 S=4. Also protects Auxiliary Steam (MOV-10LBG45-AA080). | Independent | 1 | Valid | ||
| PB-AC-015 | ACC | PAL-10LBG45-CP001: Pressure alarm low (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3595 PAL-10LBG45-CP001 S=4. Also protects Auxiliary Steam (PAL-10LBG45-CP001). | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-AC-014 | ACC | TAH-10MAJ42-CT122: Temperature alarm high (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3578 TAH-10MAJ42-CT122 S=4. | Dependent (alarm-driven) | 1 | Conditional | ||
| MB-AC-001 | ACC | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-AC-003 | ACC | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-AC-004 | ACC | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-AC-002 | ACC | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-AC-005 | ACC | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-AX-004 | Auxiliary Steam | Online sampling of water / steam | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 332 S=4. | Independent | 8 | Valid | ||
| PB-AX-003 | Auxiliary Steam | VALVE-10LBG10-AA406: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 302 VALVE-10LBG10-AA406 S=4. | Independent | 1 | Valid | ||
| PB-AX-002 | Auxiliary Steam | VALVE-10LBC10-AA406: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 298 VALVE-10LBC10-AA406 S=4. | Independent | 1 | Valid | ||
| PB-AX-001 | Auxiliary Steam | MOV-10LBC06-AA402: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 289 MOV-10LBC06-AA402 S=4. | Independent | 1 | Valid | ||
| PB-SL-006-X-AX | Auxiliary Steam | TAH-10MAW82-CT055: Temperature alarm high (056 /057 /058 are available to alert | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2186 TAH-10MAW82-CT055 S=5. Also protects STG Seals (PB-SL-006). | Independent | 1 | Valid | ||
| PB-SL-005-X-AX | Auxiliary Steam | TAL-10MAW82-CT055: Temperature alarm low (056 /057 /058 are available to alert | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2178 TAL-10MAW82-CT055 S=5. Also protects STG Seals (PB-SL-005). | Independent | 1 | Valid | ||
| MB-AX-001 | Auxiliary Steam | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-AX-003 | Auxiliary Steam | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-AX-004 | Auxiliary Steam | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-AX-002 | Auxiliary Steam | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-AX-005 | Auxiliary Steam | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-BY-003 | HRSG Bypass | UPS power backup is available for 24 hours for control system. | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1671 S=4. | Independent | 1 | Valid | ||
| PB-BY-002 | HRSG Bypass | PDAL XYMBR10-CP151/152 | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1628 S=4. | Independent | 1 | Valid | ||
| PB-BY-001 | HRSG Bypass | Operator-controlled flue gas supervision | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1624 S=4. | Independent | 1 | Valid | ||
| MB-BY-001 | HRSG Bypass | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-BY-003 | HRSG Bypass | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-BY-004 | HRSG Bypass | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-BY-002 | HRSG Bypass | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-BY-005 | HRSG Bypass | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-DB-003 | HRSG Duct Burner | PRV-11HHG01-AA003: Pressure relief valve | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 1722 PRV-11HHG01-AA003 S=5. | Independent | 1 | Valid | ||
| PB-DB-005 | HRSG Duct Burner | NRV | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1733 S=5. | Independent | 1 | Valid | ||
| PB-DB-004 | HRSG Duct Burner | FCV-11HHG01-AA101: Flow control valve (control loop regulate downstream flow) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1725 FCV-11HHG01-AA101 S=5. | Independent | 1 | Valid | ||
| PB-DB-001 | HRSG Duct Burner | Instrument interlock: instrument interlock and START standby cooling air fan. | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1718 S=5. | Independent | 1 | Valid | ||
| PB-DB-002 | HRSG Duct Burner | Instrument interlock: instrument interlock and START standby cooling air fan. | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 1718 S=5. | Independent | 1 | Concern | ||
| MB-DB-001 | HRSG Duct Burner | Fire and gas detection system | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per NFPA 72 for detection system design; F&G philosophy per ISA TR84.00.07. Not in HAZOP; requires site validation. Ref: NFPA 72, ISA TR84.00.07. | Independent | 2 | Verify | ||
| MB-DB-002 | HRSG Duct Burner | F&G interlock to ESDV | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 for safety instrumented function; F&G logic per ISA TR84.00.07. Not in HAZOP; requires site validation. Ref: IEC 61511, ISA TR84.00.07. | Independent | 2 | Verify | ||
| MB-DB-007 | HRSG Duct Burner | Site emergency response plan | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS RBPS Element 15 (Emergency Management); site ERP per local regulatory requirements. Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.15, local ERP regulation. | Independent | 4 | Verify | ||
| MB-DB-006 | HRSG Duct Burner | Hazardous area classification (IEC 60079) | Mitigation (trunk) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 3 | Verify | ||
| MB-DB-003 | HRSG Duct Burner | Firewater deluge / water spray system | Mitigation (branch) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per NFPA 15 for water spray fixed systems; coverage per NFPA 850 S6.4 for CCGT. Not in HAZOP; requires site validation. Ref: NFPA 15, NFPA 850 S6.4. | Independent | 2 | Verify | ||
| MB-DB-005 | HRSG Duct Burner | Fireproofing on structural steel (UL 1709) | Mitigation (branch) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 3 | Verify | ||
| MB-DB-004 | HRSG Duct Burner | Blast rated control room (API 752) | Mitigation (branch) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 2 | Verify | ||
| PB-FG-023 | Fuel Gas | Stack monitoring | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 2935 S=5. | Independent | 1 | Valid | ||
| PB-FG-042 | Fuel Gas | PAL-00QFB01-CP101A/B: Pressure alarm low (1oo2) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3467 PAL-00QFB01-CP101A/B S=5. | Independent | 1 | Valid | ||
| PB-FG-040 | Fuel Gas | LSL-00EKC10-CL202: Level switch low (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3430 LSL-00EKC10-CL202 S=5. | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-FG-039 | Fuel Gas | BT00EKC10-BT001: alert the operator | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3411 BT00EKC10-BT001 S=5. | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-FG-028 | Fuel Gas | PAL-00EKC50-CP101: Pressure alarm low (00EKC60-CP101 / 00EKC70-CP101 alert the | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3071 PAL-00EKC50-CP101 S=5. | Independent | 1 | Valid | ||
| PB-FG-024 | Fuel Gas | LSH-11EKC30-CL202: Level switch high (A/B (1oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3048 LSH-11EKC30-CL202 S=5. | Independent | 1 | Valid | ||
| PB-FG-029 | Fuel Gas | Condensate transfer pump trip/run monitoring | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 3132 S=5. | Independent | 1 | Concern | ||
| PB-FG-037 | Fuel Gas | TAH-11EKC30-CT001: Temperature alarm high (A/B (1oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3338 TAH-11EKC30-CT001 S=5. | Independent | 1 | Valid | ||
| PB-FG-033 | Fuel Gas | TAL-11EKC30-CT001: Temperature alarm low (A/B (1oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3312 TAL-11EKC30-CT001 S=5. | Independent | 1 | Valid | ||
| PB-FG-032 | Fuel Gas | TAL-11EKC10-CT002: Temperature alarm low (A/B (1oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3304 TAL-11EKC10-CT002 S=5. | Independent | 1 | Valid | ||
| PB-FG-041 | Fuel Gas | VALVE-00EKC10-AA402: Valve position confirmation ON/OFF | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3436 VALVE-00EKC10-AA402 S=5. | Independent | 1 | Valid | ||
| PB-FG-038 | Fuel Gas | VALVE-11EKT20-AA109: Valve position confirmation pneumatic ON/OFF | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3348 VALVE-11EKT20-AA109 S=5. | Independent | 1 | Valid | ||
| PB-FG-036 | Fuel Gas | VALVE-11EKT20-AA113: Pneumatic control valve positioner | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 3326 VALVE-11EKT20-AA113 S=5. | Independent | 1 | Concern | ||
| PB-FG-035 | Fuel Gas | VALVE-11EKT20-AA106: Valve position confirmation pneumatic ON/OFF | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3318 VALVE-11EKT20-AA106 S=5. | Independent | 1 | Valid | ||
| PB-FG-034 | Fuel Gas | VALVE-11EKT20-AA101: Valve position confirmation pneumatic ON/OFF | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3314 VALVE-11EKT20-AA101 S=5. | Independent | 1 | Valid | ||
| PB-FG-031 | Fuel Gas | VALVE-11EKT10-AA111: Pneumatic control valve positioner | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 3287 VALVE-11EKT10-AA111 S=5. | Independent | 1 | Concern | ||
| MB-FG-001 | Fuel Gas | AAH-00EKC10-AI002: Gas detection alarm (20% LEL) | Mitigation (trunk) | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2938 AAH-00EKC10-AI002 S=5. | Independent | 1 | Valid | ||
| MB-FG-002 | Fuel Gas | Fire and gas detection system | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per NFPA 72 for detection system design; F&G philosophy per ISA TR84.00.07. Not in HAZOP; requires site validation. Ref: NFPA 72, ISA TR84.00.07. | Independent | 2 | Verify | ||
| MB-FG-003 | Fuel Gas | F&G interlock to ESDV | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 for safety instrumented function; F&G logic per ISA TR84.00.07. Not in HAZOP; requires site validation. Ref: IEC 61511, ISA TR84.00.07. | Independent | 2 | Verify | ||
| MB-FG-004 | Fuel Gas | Firewater deluge / water spray system | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per NFPA 15 for water spray fixed systems; coverage per NFPA 850 S6.4 for CCGT. Not in HAZOP; requires site validation. Ref: NFPA 15, NFPA 850 S6.4. | Independent | 2 | Verify | ||
| MB-FG-008 | Fuel Gas | Site emergency response plan | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS RBPS Element 15 (Emergency Management); site ERP per local regulatory requirements. Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.15, local ERP regulation. | Independent | 4 | Verify | ||
| MB-FG-006 | Fuel Gas | Fireproofing on structural steel (UL 1709) | Mitigation (trunk) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 3 | Verify | ||
| MB-FG-005 | Fuel Gas | Blast rated control room (API 752) | Mitigation (branch) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 2 | Verify | ||
| MB-FO-001 | Fuel Oil | Gas detection system (from F&G) | Mitigation (trunk) | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 998 MOVS-00EGC03-AA001 S=5. | Independent | 1 | Valid | ||
| MB-FO-006 | Fuel Oil | Spill response kit | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per site environmental management plan; spill kit specification per containment assessment. Not in HAZOP; requires site validation. Ref: ISO 14001, local environmental regulation. | Independent | 1 | Verify | ||
| MB-FO-007 | Fuel Oil | Site emergency response plan | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS RBPS Element 15 (Emergency Management); site ERP per local regulatory requirements. Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.15, local ERP regulation. | Independent | 4 | Verify | ||
| MB-FO-004 | Fuel Oil | Bund containment around tank (API 650) | Mitigation (trunk) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 1 | Verify | ||
| MB-FO-002 | Fuel Oil | Flame / fire detection (from F&G) | Mitigation (branch) | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 998 MOVS-00EGC03-AA001 S=5. | Independent | 1 | Valid | ||
| MB-FO-003 | Fuel Oil | Fire detection in oil area | Mitigation (branch) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per NFPA 72 for fire detection system design. Not in HAZOP; requires site validation. Ref: NFPA 72. | Independent | 1 | Verify | ||
| MB-FO-005 | Fuel Oil | Fire suppression (CO2 / water spray) | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 1 | Verify | ||
| PB-FW-008 | Feedwater | Online sampling of water / steam | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 541 S=5. | Independent | 8 | Valid | ||
| PB-FW-007 | Feedwater | TCV-11LAE05-AA101: Temperature control valve (Confirmed OPEN/CLOSE/Discrepancy | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 532 TCV-11LAE05-AA101 S=5. | Independent | 1 | Valid | ||
| PB-FW-006 | Feedwater | VALVE-11LAE05-AA004: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 508 VALVE-11LAE05-AA004 S=5. | Independent | 1 | Valid | ||
| PB-FW-005 | Feedwater | MOV-11LAB02-AA004: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 500 MOV-11LAB02-AA004 S=5. | Independent | 1 | Valid | ||
| PB-FW-004 | Feedwater | MOV-11LAB02-AA002: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 489 MOV-11LAB02-AA002 S=5. | Independent | 1 | Valid | ||
| PB-FW-003 | Feedwater | VALVE-11LAB02-AA101: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 484 VALVE-11LAB02-AA101 S=5. | Independent | 1 | Valid | ||
| PB-FW-009 | Feedwater | Online SWAS feedwater quality analysis | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 543 S=5. | Independent | 1 | Valid | ||
| PB-FW-002 | Feedwater | PDAH-11LAB02-CP181: Differential pressure alarm high (11LAB03-CP181 alert the | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 454 PDAH-11LAB02-CP181 S=5. | Independent | 1 | Valid | ||
| PB-FW-001 | Feedwater | FAL-11LAB01-CF101A/B: Flow alarm low (1oo2) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 433 FAL-11LAB01-CF101A/B S=5. | Independent | 1 | Valid | ||
| MB-FW-003 | Feedwater | Emergency isolation valve | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 1 | Verify | ||
| MB-FW-004 | Feedwater | Insulation and lagging for personnel protection | Mitigation (trunk) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| MB-FW-001 | Feedwater | Leak detection and area drainage | Mitigation (trunk) | Hardware - Passive | PARTIALLY_EFFECTIVE | Domain knowledge | Per site process safety management system; detection method per fluid and environment. Not in HAZOP; requires site validation. Ref: IEC 61511, site SMS. | Independent | 1 | Verify | ||
| MB-FW-002 | Feedwater | Access restriction to BFP area | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 1 | Verify | ||
| PB-GH-003 | Generator H2 | PSL10MKG21-CP101: alert the operator | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2387 PSL10MKG21-CP101 S=5. Also protects STG Seals (PB-SL-012). | Dependent (alarm-driven) | 2 | Conditional | ||
| PB-GH-002 | Generator H2 | PSH10MKG21-CP102: alert the operator | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2373 PSH10MKG21-CP102 S=5. | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-GH-001 | Generator H2 | PAL-00PGB07-CP101A/B: Pressure alarm low (1oo2) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2362 PAL-00PGB07-CP101A/B S=5. | Independent | 1 | Valid | ||
| PB-GH-005 | Generator H2 | PSV-10MKG42-AA191: release excess pressure above [TBC] BARG to safe location | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 2448 PSV-10MKG42-AA191 S=5. | Independent | 1 | Valid | ||
| PB-GH-004 | Generator H2 | PSV-10MKG10-AA191: 10MKG01-AA191 release excess pressure above 210 BARG to | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 2446 PSV-10MKG10-AA191 S=5. | Independent | 1 | Valid | ||
| MB-GH-001 | Generator H2 | H2-specific catalytic detector | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 60079-29-1 for hydrogen detection; catalytic/electrochemical sensor selection per EN 50073. Not in HAZOP; requires site validation. Ref: IEC 60079-29-1, EN 50073. | Independent | 2 | Verify | ||
| MB-GH-002 | Generator H2 | Ventilation system with gas interlock | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 60079-10-1 for ventilation in hazardous areas; air change rate per ATEX assessment. Not in HAZOP; requires site validation. Ref: IEC 60079-10-1, ATEX directive. | Independent | 2 | Verify | ||
| MB-GH-005 | Generator H2 | Hazardous area classification (IEC 60079) | Mitigation (trunk) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 3 | Verify | ||
| MB-GH-003 | Generator H2 | Explosion relief panels | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 2 | Verify | ||
| MB-GH-004 | Generator H2 | Blast-rated generator building (API 752) | Mitigation (branch) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 2 | Verify | ||
| PB-HI-012 | HRSG IP | NRV-11LBA20-AA201: Non-return valve | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 1390 NRV-11LBA20-AA201 S=5. Also protects HP Steam (NRV-11LBA20-AA201). | Independent | 1 | Valid | ||
| PB-HI-015 | HRSG IP | Online sampling of water / steam | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 1408 S=5. | Independent | 8 | Valid | ||
| PB-HI-013 | HRSG IP | Annual preventive maintenance schedule | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 1396 S=5. | Independent | 3 | Valid | ||
| PB-HI-014 | HRSG IP | VALVE-11HAC30-AA101: Pneumatic control valve positioner | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 1399 VALVE-11HAC30-AA101 S=5. | Independent | 1 | Concern | ||
| PB-HI-011 | HRSG IP | LAH-11HAD20-CL121: Level alarm high (A/B/C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1381 LAH-11HAD20-CL121 S=5. Also protects HRSG HP (LAH-11HAD20-CL121). | Independent | 1 | Valid | ||
| PB-HI-010 | HRSG IP | MOV-11LBB10-AA102: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1371 MOV-11LBB10-AA102 S=5. | Independent | 1 | Valid | ||
| MB-HI-001 | HRSG IP | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-HI-003 | HRSG IP | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-HI-004 | HRSG IP | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-HI-002 | HRSG IP | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-HI-005 | HRSG IP | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-HL-013 | HRSG LP | NRV-11LBA10-AA201: Non-return valve | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 1548 NRV-11LBA10-AA201 S=5. Also protects HP Steam (NRV-11LBA10-AA201). | Independent | 2 | Valid | ||
| PB-HL-017 | HRSG LP | Online sampling of water / steam | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 1573 S=5. | Independent | 8 | Valid | ||
| PB-HL-015 | HRSG LP | Annual preventive maintenance schedule | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 1558 S=5. | Independent | 3 | Valid | ||
| PB-HL-016 | HRSG LP | VALVE-11LAB61-AA102: Pneumatic control valve positioner | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 1564 VALVE-11LAB61-AA102 S=5. Also protects Feedwater (VALVE-11LAB61-AA102). | Independent | 1 | Concern | ||
| PB-HL-014 | HRSG LP | VALVE-11LAB63-AA101: Pneumatic control valve positioner | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 1554 VALVE-11LAB63-AA101 S=5. Also protects Feedwater (VALVE-11LAB63-AA101). | Independent | 2 | Concern | ||
| PB-HL-011 | HRSG LP | PAH-11HAD30-CP121: Pressure alarm high (A/B/C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1543 PAH-11HAD30-CP121 S=5. Also protects HRSG HP (PAH-11HAD30-CP121). | Independent | 1 | Valid | ||
| PB-HL-009 | HRSG LP | PSV-11LBA30-AA191: PSV set (PSV-11HAD30-AA191 and 11HAD30-AA192 | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 1526 PSV-11LBA30-AA191 S=5. Also protects HP Steam (PSV-11LBA30-AA191). | Independent | 1 | Valid | ||
| PB-HL-012 | HRSG LP | PAH-11HAD30-CP121: Pressure alarm high (A/B/C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1543 PAH-11HAD30-CP121 S=5. Also protects HRSG HP (PAH-11HAD30-CP121). | Independent | 1 | Valid | ||
| MB-HL-001 | HRSG LP | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-HL-003 | HRSG LP | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-HL-004 | HRSG LP | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-HL-002 | HRSG LP | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-HL-005 | HRSG LP | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-HP-010 | HP Steam | Online sampling of water / steam | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 72 S=4. | Independent | 8 | Valid | ||
| PB-HP-009 | HP Steam | High alarm with instrument interlock (auto-trip) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 69 S=4. | Independent | 1 | Valid | ||
| PB-HP-006 | HP Steam | FOR10LBA01-AA409: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 56 FOR10LBA01-AA409 S=4. | Independent | 1 | Valid | ||
| PB-HP-005 | HP Steam | VALVE-11LBA02-AA101: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 43 VALVE-11LBA02-AA101 S=4. | Independent | 1 | Valid | ||
| PB-HP-004 | HP Steam | FOR11LBA02-AA001: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 35 FOR11LBA02-AA001 S=4. | Independent | 1 | Valid | ||
| PB-HP-003 | HP Steam | PAH-10LBA03-CP121A/B: Pressure alarm high (1oo2) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 23 PAH-10LBA03-CP121A/B S=4. | Independent | 1 | Valid | ||
| PB-HP-007 | HP Steam | NRV is provided in discharge HP steam line of each HRSG to prevent reverse flow. | Prevention | Hardware - Passive | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 61 S=4. | Independent | 1 | Concern | ||
| PB-HP-008 | HP Steam | NRV is provided in discharge HP steam line of each HRSG to prevent reverse flow. | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 61 S=4. | Independent | 1 | Valid | ||
| PB-HP-002 | HP Steam | MOV: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 7 S=4. | Independent | 2 | Valid | ||
| MB-HP-001 | HP Steam | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-HP-003 | HP Steam | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-HP-004 | HP Steam | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-HP-002 | HP Steam | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-HP-005 | HP Steam | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-HR-015 | HRSG HP | NRV-11LBA10-AA201: Non-return valve | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 1235 NRV-11LBA10-AA201 S=4. Also protects HP Steam (NRV-11LBA10-AA201). | Independent | 2 | Valid | ||
| PB-HR-018 | HRSG HP | Online sampling of water / steam | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 1262 S=4. | Independent | 8 | Valid | ||
| PB-HR-017 | HRSG HP | Annual preventive maintenance schedule | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 1247 S=4. | Independent | 3 | Valid | ||
| PB-HR-014 | HRSG HP | LAH-11HAD10-CL121: Level alarm high (A/B/C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1226 LAH-11HAD10-CL121 S=4. | Independent | 1 | Valid | ||
| PB-HR-012 | HRSG HP | PAH-11HAD10-CP121A/B: Pressure alarm high (C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1223 PAH-11HAD10-CP121A/B S=4. | Independent | 1 | Valid | ||
| PB-HR-011 | HRSG HP | MOV-11LBA10-AA102: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1210 MOV-11LBA10-AA102 S=4. Also protects HP Steam (MOV-11LBA10-AA102). | Independent | 1 | Valid | ||
| PB-HR-016 | HRSG HP | VALVE-11LAB63-AA101: Pneumatic control valve positioner | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 1239 VALVE-11LAB63-AA101 S=4. Also protects Feedwater (VALVE-11LAB63-AA101). | Independent | 2 | Concern | ||
| PB-HR-013 | HRSG HP | PAH-11HAD10-CP121A/B: Pressure alarm high (C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1223 PAH-11HAD10-CP121A/B S=4. | Independent | 1 | Valid | ||
| PB-HR-009 | HRSG HP | VALVE-11LAE10-AA102: Pneumatic control valve positioner | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 1199 VALVE-11LAE10-AA102 S=4. Also protects Feedwater (VALVE-11LAE10-AA102). | Independent | 1 | Concern | ||
| PB-HR-008 | HRSG HP | PDAH-11LAE40-CF181: Differential pressure alarm high (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1189 PDAH-11LAE40-CF181 S=4. Also protects Feedwater (PDAH-11LAE40-CF181). | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-HR-007 | HRSG HP | VALVE-11LAE10-AA104: Pneumatic control valve positioner | Prevention | Hardware - Active | PARTIALLY_EFFECTIVE | From HAZOP | Verified rows 1181 VALVE-11LAE10-AA104 S=4. Also protects Feedwater (VALVE-11LAE10-AA104). | Independent | 1 | Concern | ||
| PB-HR-005 | HRSG HP | PDAH-11LAE10-CP181: Differential pressure alarm high (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1169 PDAH-11LAE10-CP181 S=4. Also protects Feedwater (PDAH-11LAE10-CP181). | Dependent (alarm-driven) | 1 | Conditional | ||
| MB-HR-001 | HRSG HP | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-HR-003 | HRSG HP | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-HR-004 | HRSG HP | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-HR-002 | HRSG HP | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-HR-005 | HRSG HP | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-LP-006 | LP Steam | NRV is provided in discharge LP steam line of each HRSG to prevent reverse flow. | Prevention | Hardware - Passive | EFFECTIVE | From HAZOP | Verified rows 231 S=4. | Independent | 1 | Valid | ||
| PB-LP-008 | LP Steam | Online sampling of water / steam | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 246 S=4. | Independent | 8 | Valid | ||
| PB-LP-007 | LP Steam | LABLE11LBA30-CT121: Temperature elements are avai A/B (1oo2)to generate high | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 243 LABLE11LBA30-CT121 S=4. Also protects HP Steam (LABLE11LBA30-CT121). | Independent | 1 | Valid | ||
| PB-LP-005 | LP Steam | FOR10LBD02-AA405: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 227 FOR10LBD02-AA405 S=4. | Independent | 1 | Valid | ||
| PB-LP-004 | LP Steam | MOV-11LBD01-AA402: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 223 MOV-11LBD01-AA402 S=4. | Independent | 1 | Valid | ||
| PB-LP-001 | LP Steam | MOV-11LBD01-AA001: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 190 MOV-11LBD01-AA001 S=4. | Independent | 1 | Valid | ||
| PB-LP-003 | LP Steam | PCV-11LBD02-AA101: Pressure control valve (Confirmed OPEN/CLOSE/Discrepancy | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 215 PCV-11LBD02-AA101 S=4. | Independent | 1 | Valid | ||
| PB-LP-002 | LP Steam | PAH-10LBD02-CP101A/B: Pressure alarm high (1oo2) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 206 PAH-10LBD02-CP101A/B S=4. | Independent | 1 | Valid | ||
| MB-LP-001 | LP Steam | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-LP-003 | LP Steam | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-LP-004 | LP Steam | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-LP-002 | LP Steam | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-LP-005 | LP Steam | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-NH-001 | Ammonia/SCR | Operator continuous attendance (manual control) | Prevention | Human - Active | EFFECTIVE | From HAZOP | Verified rows 1745 S=4. | Independent | 2 | Valid | ||
| PB-NH-004 | Ammonia/SCR | VALVE-10GHD41-AA102: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1841 VALVE-10GHD41-AA102 S=4. | Independent | 1 | Valid | ||
| PB-NH-003 | Ammonia/SCR | VALVE-10GHD41-AA104: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1833 VALVE-10GHD41-AA104 S=4. | Independent | 1 | Valid | ||
| PB-NH-002 | Ammonia/SCR | VALVE-10GHD41-AA103: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 1830 VALVE-10GHD41-AA103 S=4. | Independent | 1 | Valid | ||
| MB-NH-001 | Ammonia/SCR | Toxic gas detection (NH3) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 60079-29-1 for flammable gas detection; placement per ISA TR84.00.07. Not in HAZOP; requires site validation. Ref: IEC 60079-29-1, ISA TR84.00.07. | Independent | 1 | Verify | ||
| MB-NH-003 | Ammonia/SCR | SCBA availability at unloading bay | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per OSHA 29 CFR 1910.134 respiratory protection; SCBA stations per emergency escape analysis. Not in HAZOP; requires site validation. Ref: OSHA 1910.134, local OHS regulation. | Independent | 1 | Verify | ||
| MB-NH-004 | Ammonia/SCR | Emergency shower and eyewash | Mitigation (trunk) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 1 | Verify | ||
| MB-NH-006 | Ammonia/SCR | Site emergency response plan | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS RBPS Element 15 (Emergency Management); site ERP per local regulatory requirements. Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.15, local ERP regulation. | Independent | 4 | Verify | ||
| MB-NH-005 | Ammonia/SCR | Exclusion zone during transfers | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone radius per consequence modelling or prescriptive rule. Not in HAZOP; requires site validation. Ref: Site SMS, local OHS regulation. | Independent | 1 | Verify | ||
| MB-NH-002 | Ammonia/SCR | Water curtain / spray system | Mitigation (branch) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Vapor Cloud Mitigation; water curtain design for NH3 knockdown. Not in HAZOP; requires site validation. Ref: CCPS vapor cloud mitigation guidelines. | Independent | 1 | Verify | ||
| PB-SS-004 | STG Steam | Operator continuous attendance (manual control) | Prevention | Human - Active | EFFECTIVE | From HAZOP | Verified rows 1917 S=4. | Independent | 2 | Valid | ||
| PB-SS-023 | STG Steam | PCV: Pressure control valve (LCE81-AA001 is available in upstream to regulate | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2110 S=4. | Independent | 1 | Valid | ||
| PB-SS-022 | STG Steam | PCV-10LCE81-AA001: Pressure control valve (Field positioner / Discrepancy | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2100 PCV-10LCE81-AA001 S=4. Also protects LP Steam (PCV-10LCE81-AA001). | Independent | 1 | Valid | ||
| PB-SS-021 | STG Steam | PDAH-10LCE81-CP122: Differential pressure alarm high (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2094 PDAH-10LCE81-CP122 S=4. Also protects LP Steam (PDAH-10LCE81-CP122). | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-SS-020 | STG Steam | TAH-10MAC81-CT053A/B: Temperature alarm high (C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2089 TAH-10MAC81-CT053A/B S=4. Also protects ACC (TAH-10MAC81-CT053A/B). | Independent | 1 | Valid | ||
| PB-SS-019 | STG Steam | FCV: Flow control valve (Field positioner / Discrepancy position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2073 S=4. | Independent | 1 | Valid | ||
| PB-SS-028 | STG Steam | MV10MAL95-AA401: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2220 MV10MAL95-AA401 S=4. | Independent | 1 | Valid | ||
| PB-SS-027 | STG Steam | MV10MAL87-AA401: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2215 MV10MAL87-AA401 S=4. | Independent | 1 | Valid | ||
| PB-SS-026 | STG Steam | MV10MAL82-AA401: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2210 MV10MAL82-AA401 S=4. | Independent | 1 | Valid | ||
| PB-SS-025 | STG Steam | MV10MAL83-AA401: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2205 MV10MAL83-AA401 S=4. | Independent | 1 | Valid | ||
| PB-SS-024 | STG Steam | MV10MAL81-AA401: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2200 MV10MAL81-AA401 S=4. | Independent | 1 | Valid | ||
| PB-SS-018 | STG Steam | MV10MAL86-AA401: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2049 MV10MAL86-AA401 S=4. | Independent | 1 | Valid | ||
| MB-SS-001 | STG Steam | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-SS-003 | STG Steam | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-SS-004 | STG Steam | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-SS-002 | STG Steam | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| MB-SS-005 | STG Steam | Insulation and lagging for personnel protection | Mitigation (branch) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| PB-CR-003 | CRH Steam | VALVE-10LBC01-AA402: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 91 VALVE-10LBC01-AA402 S=4. | Independent | 1 | Valid | ||
| PB-CR-002 | CRH Steam | MOV-12LBC01-AA410: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 87 MOV-12LBC01-AA410 S=4. | Independent | 1 | Valid | ||
| PB-CR-001 | CRH Steam | MOV-11LBC01-AA001: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 80 MOV-11LBC01-AA001 S=4. | Independent | 1 | Valid | ||
| PB-AC-018-X-CD | CRH Steam | FAL-10LCA04-CF101A/B: Flow alarm low (1oo2) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 3623 FAL-10LCA04-CF101A/B S=4. Also protects ACC (PB-AC-018). | Independent | 2 | Valid | ||
| MB-CR-003 | CRH Steam | Insulation and lagging for personnel protection | Mitigation (trunk) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| MB-CR-001 | CRH Steam | Drain routing to safe location | Mitigation (trunk) | Hardware - Passive | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 521 for pressure-relieving and depressuring systems; drain disposal to a safe location per the design basis. Not in HAZOP; requires site validation. Ref: API 521. | Independent | 1 | Verify | ||
| MB-CR-002 | CRH Steam | Access restriction | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 1 | Verify | ||
| PB-HH-006 | HRH Steam | Positive isolation (energy isolation for maintenance) | Prevention | Organizational | EFFECTIVE | From HAZOP | Verified rows 162 S=4. | Independent | 1 | Valid | ||
| PB-HH-008 | HRH Steam | Online sampling of water / steam | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 182 S=4. | Independent | 8 | Valid | ||
| PB-HH-007 | HRH Steam | LABLE11LBB10-CT123: Temperature elements are avai A/B/C to generate high | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 179 LABLE11LBB10-CT123 S=4. | Independent | 1 | Valid | ||
| PB-HH-003 | HRH Steam | PAH-10LBB01-CP121A/B: Pressure alarm high (1oo2)and PAL-10LBB01-CP122 is | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 134 PAH-10LBB01-CP121A/B S=4. | Independent | 1 | Valid | ||
| PB-HH-001 | HRH Steam | FAL-11LBB10-CF121A/B: Flow alarm low (1oo2) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 113 FAL-11LBB10-CF121A/B S=4. | Independent | 1 | Valid | ||
| PB-HH-005 | HRH Steam | FOR10LBB01-AA412: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 157 FOR10LBB01-AA412 S=4. | Independent | 1 | Valid | ||
| PB-HH-004 | HRH Steam | VALVE-11LBB01-AA101: Valve position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 144 VALVE-11LBB01-AA101 S=4. | Independent | 1 | Valid | ||
| PB-HH-002 | HRH Steam | MOV: Motor operated isolation valve | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 118 S=4. | Independent | 2 | Valid | ||
| MB-HH-001 | HRH Steam | Steam leak detection and alarm | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 61511 SIF design for steam leak scenarios; detector placement per OEM recommendation. Not in HAZOP; requires site validation. Ref: IEC 61511, OEM O&M manual. | Independent | 10 | Verify | ||
| MB-HH-003 | HRH Steam | Emergency isolation (remote operated) | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per API 6D valve specification and IEC 61511 SIS design for remote-operated ESD. Not in HAZOP; requires site validation. Ref: API 6D, IEC 61511. | Independent | 10 | Verify | ||
| MB-HH-005 | HRH Steam | Insulation and lagging for personnel protection | Mitigation (trunk) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 12 | Verify | ||
| MB-HH-004 | HRH Steam | Emergency operating procedures | Mitigation (trunk) | Procedural | PARTIALLY_EFFECTIVE | Domain knowledge | Per CCPS Guidelines for Risk Based Process Safety, Element 10 (Operating Procedures). Not in HAZOP; requires site validation. Ref: CCPS RBPS Ch.10, ISO 45001 S8.1. | Independent | 10 | Verify | ||
| MB-HH-002 | HRH Steam | Access restriction and exclusion zones | Mitigation (trunk) | Organizational | PARTIALLY_EFFECTIVE | Domain knowledge | Per site safety management system; exclusion zone policy for MAH areas. Not in HAZOP; requires site validation. Ref: ISO 45001 S8.1, site SMS. | Independent | 10 | Verify | ||
| PB-SL-014 | STG Seals | LAH-10MKW01-CL101: Level alarm high (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2521 LAH-10MKW01-CL101 S=5. | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-SL-013 | STG Seals | ECTOR10MKW21-BZ001: SODE will overflow to liquid det and alert the operator | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2518 ECTOR10MKW21-BZ001 S=5. | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-SL-012 | STG Seals | PSL10MKG21-CP101: alert the operator | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2513 PSL10MKG21-CP101 S=5. Also protects Generator H2 (PSL10MKG21-CP101). | Dependent (alarm-driven) | 2 | Conditional | ||
| PB-SL-011 | STG Seals | Pump discharge line is designed for pump shut-off head. | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2503 S=5. | Independent | 1 | Valid | ||
| PB-SL-010 | STG Seals | FAL-10MKW06-CF001: Flow alarm low (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2488 FAL-10MKW06-CF001 S=5. | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-SL-009 | STG Seals | PDAH-10MKW10-CP001: Differential pressure alarm high (A/B (1oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2485 PDAH-10MKW10-CP001 S=5. | Independent | 1 | Valid | ||
| PB-SL-004 | STG Seals | Auto start of standby Gland condenser blower on tripping of duty blower. | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2149 S=5. | Independent | 1 | Valid | ||
| PB-SL-002 | STG Seals | PCV: Pressure control valve (Field positioner / Discrepancy position feedback | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2126 S=5. | Independent | 1 | Valid | ||
| MB-SL-001 | STG Seals | H2-specific catalytic detector | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 60079-29-1 for hydrogen detection; catalytic/electrochemical sensor selection per EN 50073. Not in HAZOP; requires site validation. Ref: IEC 60079-29-1, EN 50073. | Independent | 2 | Verify | ||
| MB-SL-002 | STG Seals | Ventilation system with gas interlock | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per IEC 60079-10-1 for ventilation in hazardous areas; air change rate per ATEX assessment. Not in HAZOP; requires site validation. Ref: IEC 60079-10-1, ATEX directive. | Independent | 2 | Verify | ||
| MB-SL-003 | STG Seals | Explosion relief panels | Mitigation (trunk) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 2 | Verify | ||
| MB-SL-004 | STG Seals | Blast-rated generator building (API 752) | Mitigation (trunk) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 2 | Verify | ||
| MB-SL-005 | STG Seals | Hazardous area classification (IEC 60079) | Mitigation (trunk) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 3 | Verify | ||
| PB-LO-005 | STG Lube Oil | Turn around PM schedule is available | Prevention | Procedural | EFFECTIVE | From HAZOP | Verified rows 2359 S=4. | Independent | 1 | Valid | ||
| PB-LO-004 | STG Lube Oil | TAH-10MAV95-CT122: Temperature alarm high (A/B (1oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2340 TAH-10MAV95-CT122 S=4. | Independent | 1 | Valid | ||
| PB-LO-003 | STG Lube Oil | PAH-10MAV95-CP125: Pressure alarm high (A/B/C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2328 PAH-10MAV95-CP125 S=4. | Independent | 1 | Valid | ||
| PB-LO-002 | STG Lube Oil | PDAH-10MAV93-CP181: Differential pressure alarm high (alert the operator) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2308 PDAH-10MAV93-CP181 S=4. | Dependent (alarm-driven) | 1 | Conditional | ||
| PB-LO-001 | STG Lube Oil | PAL-10MAV95-CP125: Pressure alarm low (A/B/C (2oo) | Prevention | Hardware - Active | EFFECTIVE | From HAZOP | Verified rows 2302 PAL-10MAV95-CP125 S=4. | Independent | 1 | Valid | ||
| MB-LO-001 | STG Lube Oil | Oil mist detection | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per OEM recommendation for turbine enclosure; oil mist concentration alarm per machine protection. Not in HAZOP; requires site validation. Ref: OEM O&M manual, API 670. | Independent | 1 | Verify | ||
| MB-LO-002 | STG Lube Oil | CO2 / clean agent fire suppression | Mitigation (trunk) | Hardware - Active | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 1 | Verify | ||
| MB-LO-004 | STG Lube Oil | Flame detection near hot surfaces | Mitigation (trunk) | Hardware - Active | PARTIALLY_EFFECTIVE | Domain knowledge | Per NFPA 72 for flame detector selection; UV/IR technology per EN 54-10. Not in HAZOP; requires site validation. Ref: NFPA 72, EN 54-10. | Independent | 1 | Verify | ||
| MB-LO-003 | STG Lube Oil | Drip trays and bund containment | Mitigation (trunk) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 1 | Verify | ||
| MB-LO-005 | STG Lube Oil | Fireproofing on structural steel (UL 1709) | Mitigation (trunk) | Hardware - Passive | EFFECTIVE | Engineering standard | Design basis per industry standard referenced in title. Not a HAZOP safeguard. | Independent | 3 | Verify |
Safety Critical Elements (SCE, hardware) and Safety Critical Activities
(SCA, human / procedural). Performance standards follow the Energy Institute
FARSI model (Functionality, Availability, Reliability, Survivability, plus
Test Interval). Cross-references WORLD_CLASS.xlsx SCE Register.
| SCE ID | Type | System | Barrier | Side | MAH | Cat. | Performance Standard | Test Interval | Owner |
|---|---|---|---|---|---|---|---|---|---|
| SCE-001 | SCE | ACC | ACC is designed for worst case scenario including opening of LP/IP bypass. | Prevention | MAH-CCGT-AC-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-002 | SCE | ACC | FAL-10LCA04-CF101A/B: Flow alarm low (1oo2) | Prevention | MAH-CCGT-AC-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-003 | SCE | ACC | MOV-10MAJ45-AA075: Motor operated isolation valve | Prevention | MAH-CCGT-AC-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-004 | SCE | ACC | MOV-10LBG45-AA080: Motor operated isolation valve | Prevention | MAH-CCGT-AC-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-005 | SCE | ACC | PAL-10LBG45-CP001: Pressure alarm low (alert the operator) | Prevention | MAH-CCGT-AC-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-006 | SCE | ACC | TAH-10MAJ42-CT122: Temperature alarm high (alert the operator) | Prevention | MAH-CCGT-AC-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-007 | SCE | HRSG Bypass | UPS power backup is available for 24 hours for control system. | Prevention | MAH-CCGT-BY-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-008 | SCE | HRSG Bypass | PDAL XYMBR10-CP151/152 | Prevention | MAH-CCGT-BY-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-009 | SCE | HRSG Bypass | Operator-controlled flue gas supervision | Prevention | MAH-CCGT-BY-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-010 | SCE | HRSG Bypass | Insulation and lagging for personnel protection | Mitigation | MAH-CCGT-BY-001 | A | Reduce consequence severity | 12 months | I&C Eng |
| SCE-011 | SCE | HRSG Duct Burner | PRV-11HHG01-AA003: Pressure relief valve | Prevention | MAH-CCGT-DB-001 | E | Auto-actuate per design intent | 12 months | MI Eng |
| SCE-012 | SCE | HRSG Duct Burner | NRV | Prevention | MAH-CCGT-DB-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-013 | SCE | HRSG Duct Burner | FCV-11HHG01-AA101: Flow control valve (control loop regulate downstream flow) | Prevention | MAH-CCGT-DB-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-014 | SCE | HRSG Duct Burner | Instrument interlock: instrument interlock and START standby cooling air fan. | Prevention | MAH-CCGT-DB-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-015 | SCE | HRSG Duct Burner | Instrument interlock: instrument interlock and START standby cooling air fan. | Prevention | MAH-CCGT-DB-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-016 | SCE | HRSG Duct Burner | Firewater deluge / water spray system | Mitigation | MAH-CCGT-DB-001 | E | Reduce consequence severity | 12 months | HSSE |
| SCE-017 | SCE | HRSG Duct Burner | Fireproofing on structural steel (UL 1709) | Mitigation | MAH-CCGT-DB-001 | E | Reduce consequence severity | 12 months | Project Eng |
| SCE-018 | SCE | HRSG Duct Burner | Blast rated control room (API 752) | Mitigation | MAH-CCGT-DB-001 | E | Reduce consequence severity | 12 months | Project Eng |
| SCA-001 | SCA | Fuel Gas | Stack monitoring | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | Operations |
| SCE-019 | SCE | Fuel Gas | PAL-00QFB01-CP101A/B: Pressure alarm low (1oo2) | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-020 | SCE | Fuel Gas | LSL-00EKC10-CL202: Level switch low (alert the operator) | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-021 | SCE | Fuel Gas | BT00EKC10-BT001: alert the operator | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-022 | SCE | Fuel Gas | PAL-00EKC50-CP101: Pressure alarm low (00EKC60-CP101 / 00EKC70-CP101 alert the | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-023 | SCE | Fuel Gas | LSH-11EKC30-CL202: Level switch high (A/B (1oo) | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-024 | SCE | Fuel Gas | Condensate transfer pump trip/run monitoring | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-025 | SCE | Fuel Gas | TAH-11EKC30-CT001: Temperature alarm high (A/B (1oo) | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-026 | SCE | Fuel Gas | TAL-11EKC30-CT001: Temperature alarm low (A/B (1oo) | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-027 | SCE | Fuel Gas | TAL-11EKC10-CT002: Temperature alarm low (A/B (1oo) | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-028 | SCE | Fuel Gas | VALVE-00EKC10-AA402: Valve position confirmation ON/OFF | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-029 | SCE | Fuel Gas | VALVE-11EKT20-AA109: Valve position confirmation pneumatic ON/OFF | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-030 | SCE | Fuel Gas | VALVE-11EKT20-AA113: Pneumatic control valve positioner | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-031 | SCE | Fuel Gas | VALVE-11EKT20-AA106: Valve position confirmation pneumatic ON/OFF | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-032 | SCE | Fuel Gas | VALVE-11EKT20-AA101: Valve position confirmation pneumatic ON/OFF | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-033 | SCE | Fuel Gas | VALVE-11EKT10-AA111: Pneumatic control valve positioner | Prevention | MAH-CCGT-FG-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-034 | SCE | Fuel Gas | Blast rated control room (API 752) | Mitigation | MAH-CCGT-FG-001 | E | Reduce consequence severity | 12 months | Project Eng |
| SCE-035 | SCE | Fuel Oil | Flame / fire detection (from F&G) | Mitigation | MAH-CCGT-FO-001 | E | Reduce consequence severity | 12 months | HSSE |
| SCE-036 | SCE | Fuel Oil | Fire detection in oil area | Mitigation | MAH-CCGT-FO-001 | E | Reduce consequence severity | 12 months | HSSE |
| SCE-037 | SCE | Fuel Oil | Fire suppression (CO2 / water spray) | Mitigation | MAH-CCGT-FO-001 | E | Reduce consequence severity | 12 months | I&C Eng |
| SCE-038 | SCE | Generator H2 | PSL10MKG21-CP101: alert the operator | Prevention | MAH-CCGT-GH-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-039 | SCE | Generator H2 | PSH10MKG21-CP102: alert the operator | Prevention | MAH-CCGT-GH-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-040 | SCE | Generator H2 | PAL-00PGB07-CP101A/B: Pressure alarm low (1oo2) | Prevention | MAH-CCGT-GH-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-041 | SCE | Generator H2 | PSV-10MKG42-AA191: release excess pressure above [TBC] BARG to safe location | Prevention | MAH-CCGT-GH-001 | E | Auto-actuate per design intent | 12 months | MI Eng |
| SCE-042 | SCE | Generator H2 | PSV-10MKG10-AA191: 10MKG01-AA191 release excess pressure above 210 BARG to | Prevention | MAH-CCGT-GH-001 | E | Auto-actuate per design intent | 12 months | MI Eng |
| SCE-043 | SCE | Generator H2 | Explosion relief panels | Mitigation | MAH-CCGT-GH-001 | E | Reduce consequence severity | 12 months | I&C Eng |
| SCE-044 | SCE | Generator H2 | Blast-rated generator building (API 752) | Mitigation | MAH-CCGT-GH-001 | E | Reduce consequence severity | 12 months | Project Eng |
| SCE-045 | SCE | HRSG IP | NRV-11LBA20-AA201: Non-return valve | Prevention | MAH-CCGT-HI-001 | E | Auto-actuate per design intent | 12 months | MI Eng |
| SCA-002 | SCA | HRSG IP | Online sampling of water / steam | Prevention | MAH-CCGT-HI-001 | E | Auto-actuate per design intent | 12 months | Operations |
| SCA-003 | SCA | HRSG IP | Annual preventive maintenance schedule | Prevention | MAH-CCGT-HI-001 | E | Auto-actuate per design intent | 12 months | Operations |
| SCE-046 | SCE | HRSG IP | VALVE-11HAC30-AA101: Pneumatic control valve positioner | Prevention | MAH-CCGT-HI-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-047 | SCE | HRSG IP | LAH-11HAD20-CL121: Level alarm high (A/B/C (2oo) | Prevention | MAH-CCGT-HI-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-048 | SCE | HRSG IP | MOV-11LBB10-AA102: Motor operated isolation valve | Prevention | MAH-CCGT-HI-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-049 | SCE | HRSG IP | Insulation and lagging for personnel protection | Mitigation | MAH-CCGT-HI-001 | D | Reduce consequence severity | 12 months | I&C Eng |
| SCE-050 | SCE | HRSG LP | NRV-11LBA10-AA201: Non-return valve | Prevention | MAH-CCGT-HL-001 | E | Auto-actuate per design intent | 12 months | MI Eng |
| SCA-004 | SCA | HRSG LP | Online sampling of water / steam | Prevention | MAH-CCGT-HL-001 | E | Auto-actuate per design intent | 12 months | Operations |
| SCA-005 | SCA | HRSG LP | Annual preventive maintenance schedule | Prevention | MAH-CCGT-HL-001 | E | Auto-actuate per design intent | 12 months | Operations |
| SCE-051 | SCE | HRSG LP | VALVE-11LAB61-AA102: Pneumatic control valve positioner | Prevention | MAH-CCGT-HL-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-052 | SCE | HRSG LP | VALVE-11LAB63-AA101: Pneumatic control valve positioner | Prevention | MAH-CCGT-HL-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-053 | SCE | HRSG LP | PAH-11HAD30-CP121: Pressure alarm high (A/B/C (2oo) | Prevention | MAH-CCGT-HL-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-054 | SCE | HRSG LP | PSV-11LBA30-AA191: PSV set (PSV-11HAD30-AA191 and 11HAD30-AA192 | Prevention | MAH-CCGT-HL-001 | E | Auto-actuate per design intent | 12 months | MI Eng |
| SCE-055 | SCE | HRSG LP | PAH-11HAD30-CP121: Pressure alarm high (A/B/C (2oo) | Prevention | MAH-CCGT-HL-001 | E | Auto-actuate per design intent | 12 months | I&C Eng |
| SCA-006 | SCA | HP Steam | Online sampling of water / steam | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | Operations |
| SCE-056 | SCE | HP Steam | High alarm with instrument interlock (auto-trip) | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-057 | SCE | HP Steam | FOR10LBA01-AA409: Valve position feedback | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-058 | SCE | HP Steam | VALVE-11LBA02-AA101: Valve position feedback | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-059 | SCE | HP Steam | FOR11LBA02-AA001: Valve position feedback | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-060 | SCE | HP Steam | PAH-10LBA03-CP121A/B: Pressure alarm high (1oo2) | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-061 | SCE | HP Steam | NRV is provided in discharge HP steam line of each HRSG to prevent reverse flow. | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | MI Eng |
| SCE-062 | SCE | HP Steam | NRV is provided in discharge HP steam line of each HRSG to prevent reverse flow. | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | MI Eng |
| SCE-063 | SCE | HP Steam | MOV: Motor operated isolation valve | Prevention | MAH-CCGT-HP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-064 | SCE | HP Steam | Insulation and lagging for personnel protection | Mitigation | MAH-CCGT-HP-001 | A | Reduce consequence severity | 12 months | I&C Eng |
| SCE-065 | SCE | HRSG HP | NRV-11LBA10-AA201: Non-return valve | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | MI Eng |
| SCA-007 | SCA | HRSG HP | Online sampling of water / steam | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | Operations |
| SCA-008 | SCA | HRSG HP | Annual preventive maintenance schedule | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | Operations |
| SCE-066 | SCE | HRSG HP | LAH-11HAD10-CL121: Level alarm high (A/B/C (2oo) | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-067 | SCE | HRSG HP | PAH-11HAD10-CP121A/B: Pressure alarm high (C (2oo) | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-068 | SCE | HRSG HP | MOV-11LBA10-AA102: Motor operated isolation valve | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-069 | SCE | HRSG HP | VALVE-11LAB63-AA101: Pneumatic control valve positioner | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-070 | SCE | HRSG HP | PAH-11HAD10-CP121A/B: Pressure alarm high (C (2oo) | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-071 | SCE | HRSG HP | VALVE-11LAE10-AA102: Pneumatic control valve positioner | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-072 | SCE | HRSG HP | PDAH-11LAE40-CF181: Differential pressure alarm high (alert the operator) | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-073 | SCE | HRSG HP | VALVE-11LAE10-AA104: Pneumatic control valve positioner | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-074 | SCE | HRSG HP | PDAH-11LAE10-CP181: Differential pressure alarm high (alert the operator) | Prevention | MAH-CCGT-HR-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-075 | SCE | HRSG HP | Insulation and lagging for personnel protection | Mitigation | MAH-CCGT-HR-001 | D | Reduce consequence severity | 12 months | I&C Eng |
| SCE-076 | SCE | LP Steam | NRV is provided in discharge LP steam line of each HRSG to prevent reverse flow. | Prevention | MAH-CCGT-LP-001 | D | Auto-actuate per design intent | 12 months | MI Eng |
| SCA-009 | SCA | LP Steam | Online sampling of water / steam | Prevention | MAH-CCGT-LP-001 | D | Auto-actuate per design intent | 12 months | Operations |
| SCE-077 | SCE | LP Steam | LABLE11LBA30-CT121: Temperature elements are avai A/B (1oo2)to generate high | Prevention | MAH-CCGT-LP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-078 | SCE | LP Steam | FOR10LBD02-AA405: Valve position feedback | Prevention | MAH-CCGT-LP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-079 | SCE | LP Steam | MOV-11LBD01-AA402: Motor operated isolation valve | Prevention | MAH-CCGT-LP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-080 | SCE | LP Steam | MOV-11LBD01-AA001: Motor operated isolation valve | Prevention | MAH-CCGT-LP-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCA-010 | SCA | Ammonia/SCR | Operator continuous attendance (manual control) | Prevention | MAH-CCGT-NH-001 | A | Auto-actuate per design intent | 12 months | Operations |
| SCE-081 | SCE | Ammonia/SCR | VALVE-10GHD41-AA102: Valve position feedback | Prevention | MAH-CCGT-NH-001 | A | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-082 | SCE | Ammonia/SCR | VALVE-10GHD41-AA104: Valve position feedback | Prevention | MAH-CCGT-NH-001 | A | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-083 | SCE | Ammonia/SCR | VALVE-10GHD41-AA103: Valve position feedback | Prevention | MAH-CCGT-NH-001 | A | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-084 | SCE | Ammonia/SCR | Water curtain / spray system | Mitigation | MAH-CCGT-NH-001 | A | Reduce consequence severity | 12 months | HSSE |
| SCA-011 | SCA | STG Steam | Operator continuous attendance (manual control) | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | Operations |
| SCE-085 | SCE | STG Steam | PCV: Pressure control valve (LCE81-AA001 is available in upstream to regulate | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-086 | SCE | STG Steam | PCV-10LCE81-AA001: Pressure control valve (Field positioner / Discrepancy | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-087 | SCE | STG Steam | PDAH-10LCE81-CP122: Differential pressure alarm high (alert the operator) | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-088 | SCE | STG Steam | TAH-10MAC81-CT053A/B: Temperature alarm high (C (2oo) | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-089 | SCE | STG Steam | FCV: Flow control valve (Field positioner / Discrepancy position feedback | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-090 | SCE | STG Steam | MV10MAL95-AA401: Valve position feedback | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-091 | SCE | STG Steam | MV10MAL87-AA401: Valve position feedback | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-092 | SCE | STG Steam | MV10MAL82-AA401: Valve position feedback | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-093 | SCE | STG Steam | MV10MAL83-AA401: Valve position feedback | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-094 | SCE | STG Steam | MV10MAL81-AA401: Valve position feedback | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-095 | SCE | STG Steam | MV10MAL86-AA401: Valve position feedback | Prevention | MAH-CCGT-SS-001 | D | Auto-actuate per design intent | 12 months | I&C Eng |
| SCE-096 | SCE | STG Steam | Insulation and lagging for personnel protection | Mitigation | MAH-CCGT-SS-001 | A | Reduce consequence severity | 12 months | I&C Eng |
| SCE-097 | SCE | CRH Steam | VALVE-10LBC01-AA402: Valve position feedback | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-098 | SCE | CRH Steam | MOV-12LBC01-AA410: Motor operated isolation valve | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-099 | SCE | CRH Steam | MOV-11LBC01-AA001: Motor operated isolation valve | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-100 | SCE | CRH Steam | FAL-10LCA04-CF101A/B: Flow alarm low (1oo2) | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCA-012 | SCA | HRH Steam | Positive isolation (energy isolation for maintenance) | Prevention | D | Auto-actuate per design intent | 12 months | HSSE | |
| SCA-013 | SCA | HRH Steam | Online sampling of water / steam | Prevention | D | Auto-actuate per design intent | 12 months | Operations | |
| SCE-101 | SCE | HRH Steam | LABLE11LBB10-CT123: Temperature elements are avai A/B/C to generate high | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-102 | SCE | HRH Steam | PAH-10LBB01-CP121A/B: Pressure alarm high (1oo2)and PAL-10LBB01-CP122 is | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-103 | SCE | HRH Steam | FAL-11LBB10-CF121A/B: Flow alarm low (1oo2) | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-104 | SCE | HRH Steam | FOR10LBB01-AA412: Valve position feedback | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-105 | SCE | HRH Steam | VALVE-11LBB01-AA101: Valve position feedback | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-106 | SCE | HRH Steam | MOV: Motor operated isolation valve | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-107 | SCE | STG Seals | LAH-10MKW01-CL101: Level alarm high (alert the operator) | Prevention | E | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-108 | SCE | STG Seals | ECTOR10MKW21-BZ001: SODE will overflow to liquid det and alert the operator | Prevention | E | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-109 | SCE | STG Seals | PSL10MKG21-CP101: alert the operator | Prevention | E | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-110 | SCE | STG Seals | Pump discharge line is designed for pump shut-off head. | Prevention | E | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-111 | SCE | STG Seals | FAL-10MKW06-CF001: Flow alarm low (alert the operator) | Prevention | E | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-112 | SCE | STG Seals | PDAH-10MKW10-CP001: Differential pressure alarm high (A/B (1oo) | Prevention | E | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-113 | SCE | STG Seals | Auto start of standby Gland condenser blower on tripping of duty blower. | Prevention | E | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-114 | SCE | STG Seals | PCV: Pressure control valve (Field positioner / Discrepancy position feedback | Prevention | E | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCA-014 | SCA | STG Lube Oil | Turn around PM schedule is available | Prevention | D | Auto-actuate per design intent | 12 months | Operations | |
| SCE-115 | SCE | STG Lube Oil | TAH-10MAV95-CT122: Temperature alarm high (A/B (1oo) | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-116 | SCE | STG Lube Oil | PAH-10MAV95-CP125: Pressure alarm high (A/B/C (2oo) | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-117 | SCE | STG Lube Oil | PDAH-10MAV93-CP181: Differential pressure alarm high (alert the operator) | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng | |
| SCE-118 | SCE | STG Lube Oil | PAL-10MAV95-CP125: Pressure alarm low (A/B/C (2oo) | Prevention | D | Auto-actuate per design intent | 12 months | I&C Eng |
This section follows the four-step qualitative ALARP demonstration structure from HSE UK SPC / Permissioning / 37 -- codes-and-standards compliance, good-practice comparison, risk-reduction measures register, and an explicit ALARP conclusion statement.
| Standard | Requirement | Addressed by | Status |
|---|---|---|---|
| IEC 61511 (Safety Instrumented Systems) | SIL-rated SIS for identified safety functions | Pressure / temperature alarms, ESD trips, interlocks | Partially -- SIL ratings to be confirmed at site |
| API 521 / EN ISO 4126 (Pressure Relief) | PSV / PRV on every pressurised system | PSVs identified on HRSG, Generator H2, Duct Burner | Partially -- PSV sizing not verified |
| IEC 60079 / BS EN 60079 (Hazardous Areas) | Hazardous area classification for flammable / H2 | Gas detection on Fuel Gas; H2 detection on Generator | Partially -- area classification not reviewed |
| NFPA 850 / API 2001 (Fire Protection) | Fire detection and suppression for flammable hazards | Fire detection on Fuel Oil; deluge on Fuel Gas / Duct Burner | Partially -- coverage and adequacy not confirmed |
| API 752 (Blast Resistant Structures) | Blast-rated control room for VCE scenarios | Blast-rated CR identified for Fuel Gas, Duct Burner | Adequate from desk review -- design basis to confirm |
| Element | Good Practice | Current | Gap |
|---|---|---|---|
| Prevention barriers per threat | 2-4 independent barriers per threat (CCPS / EI) | 2.9 avg; 32% with zero | Significant |
| Barrier type diversity | >=2 categories per critical pathway (Tech + Operational) | 5 categories overall; 73% Hardware-Active | Significant |
| Mitigation specificity | >=50% consequence-specific mitigation (CCPS / EI event-tree) | 19% branch / 81% trunk | Moderate |
| Human / procedural layers | 20-40% of barriers are H / P / O | 17% | Minor |
Generated from the CRITICAL and MAJOR gap findings. All measures are standard industry practice (workshop, verification, walkdown) so feasibility is High and cost is Low to Medium.
| Gap ID | System | Measure | Feasibility | Cost | Risk reduction | Reasonably practicable? |
|---|---|---|---|---|---|---|
| GAP-ANS-001 | ACC | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| F-SCOPE-001 | Cross-cutting (all systems) | Extend HAZOP scope to cover the missing mandatory systems: Fuel Gas Receiving Station, Gas Turbine Lubrication System, GT Enclosure Ventilation and Fire Suppression, HRSG Drums (HP/IP/LP) and Downcomer System, Superheater and Reheater, Econ | High | Low-Medium | Significant | Yes -- recommended |
| GAP-A-001 | Auxiliary Steam | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HNB-001 | HRSG Bypass | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-CSS-001 | CRH Steam | No mitigative barriers identified in HAZOP. All 3 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HND-001 | HRSG Duct Burner | No mitigative barriers identified in HAZOP. All 7 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HND-002 | HRSG Duct Burner | Single barrier on domain_knowledge pathway (THR-DB-002). Single point of failure on S=5 catastrophic consequence. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-FNF-001 | Fuel Gas | Single barrier on from_hazop pathway (THR-FG-002). Single point of failure on S=5 catastrophic consequence. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-FOS-001 | Fuel Oil | Flange and connection leaks on lube oil pipework are caused by vibration-induced bolt relaxation, gasket degradation, and thermal cycling. Standard prevention includes: joint integrity management programme (ASME PCC-1), controlled bolt torq | High | Low-Medium | Significant | Yes -- recommended |
| GAP-FOS-002 | Fuel Oil | Tank overflow during fuel oil delivery is prevented by independent high-level alarms (LAH), high-high level trips (LAHH) with automatic shutoff of the transfer pump or inlet valve, and secondary containment (bund) sized to contain the full | High | Low-Medium | Significant | Yes -- recommended |
| GAP-FOS-003 | Fuel Oil | Pump seal failure on fuel oil transfer or forwarding pumps releases flammable liquid at the pump skid. Standard prevention includes: dual mechanical seals (API Plan 52/54), seal flush systems, bearing temperature and vibration monitoring wi | High | Low-Medium | Significant | Yes -- recommended |
| GAP-F-001 | Feedwater | No mitigative barriers identified in HAZOP. All 4 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-SNH-001 | Generator H2 | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-SNH-002 | Generator H2 | Vacuum system failure in the ACC allows air ingress into the steam space, degrading condenser performance and potentially causing oxygen corrosion of tube internals. This mechanism is typically prevented by vacuum pump redundancy, air eject | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HRS-001 | HRH Steam | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HNI-001 | HRSG IP | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HNI-002 | HRSG IP | Thermal stress during startup/shutdown transitions is a primary damage mechanism for HRSG tubes, headers, and drums. Rapid temperature changes cause differential expansion between thick-walled components (drums, headers) and thin-walled tub | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HNL-001 | HRSG LP | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HS-001 | HP Steam | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HNH-001 | HRSG HP | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-SNL-001 | STG Lube Oil | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-LSS-001 | LP Steam | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-HNA-001 | Ammonia/SCR | No mitigative barriers identified in HAZOP. All 6 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-SNT-001 | STG Seals | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
| GAP-SNB-001 | STG Steam | No mitigative barriers identified in HAZOP. All 5 suggested barriers marked for validation. | High | Low-Medium | Significant | Yes -- recommended |
Based on this desk-review assessment, the residual risk from 2 of 19 MAH scenarios cannot be confirmed as ALARP until the 25 Critical findings are addressed. The principal barriers to an ALARP demonstration are: (a) unconfirmed SIL ratings on safety-instrumented functions; (b) suggested mitigation barriers requiring site verification; and (c) unprotected threat pathways where HAZOP safeguards could not be matched to specific initiating events. A formal ALARP assessment requires site-validated PFD / SIL data, operational performance records, and a reasonably-practicable cost / benefit analysis, which are outside the scope of this desk review.
These findings frame the assessment as a whole. They surface HAZOP methodology gaps and defence-in-depth diversity gaps that affect every system rather than any single MAH scenario.
System-specific findings are listed below in priority order. Standard closure timelines are CRITICAL within 60 days, MAJOR within 90 days, MINOR within 180 days.
| Priority | Count | Standard Closure |
|---|---|---|
| CRITICAL | 24 | 60 days |
| MAJOR | 35 | 90 days |
| MINOR | 20 | 180 days |
| Total system-specific | 79 |
Systems carrying CRITICAL findings: ACC, Ammonia/SCR, Auxiliary Steam, CRH Steam, Feedwater, Fuel Gas, Fuel Oil, Generator H2, HP Steam, HRH Steam, HRSG Bypass, HRSG Duct Burner, HRSG HP, HRSG IP, HRSG LP, LP Steam, STG Lube Oil, STG Seals, STG Steam.
Cross-finding analysis -- the recurring patterns that emerge when the per-bowtie findings are read together.
Confidence in this assessment is decomposed into five weighted factors. Each factor is rated Low (30 points), Medium (55 points) or High (80 points). The weighted overall rolls up to the evidence confidence number reported on the cover.
Weighted overall confidence: 46/100 · Structural confidence: 85% · Evidence confidence cap: 40/100 (non-negotiable for desk reviews per SPEC-XL §19).
Dual confidence cap: confidence is capped at min(desk-review cap 65/100, scope-coverage cap 40/100) = 40/100. Scope cap reflects 31% coverage of mandatory reference systems for CCGT.
19 MAH scenarios identified from 1123 HAZOP rows; 0 systems excluded as non-MAH. Coverage is comprehensive for process systems but does not include electrical protection, GT exhaust / purge, or utility chemical storage.
137 barriers (59%) traced to HAZOP safeguards. 67 (29%) from domain knowledge, 29 (12%) from engineering standards. HAZOP-traced barriers carry highest confidence; library-seeded barriers require site verification.
No PFD / SIL data verified against site records. 33% of barriers assessed as Partially Effective. Condition assessment requires maintenance records, test reports and site observation.
Consequence severity drawn from the HAZOP risk matrix. No QRA, dispersion modelling or fire / explosion consequence analysis performed. Consequence descriptions are credible for CCGT but not independently validated.
Escalation factors and degradation controls not systematically assessed. Common-cause failure analysis not performed. Barrier independence not verified. These require operational data and site walkdown.
| Tier | Count | Definition |
|---|---|---|
| From HAZOP | 137 | Row-level verified with instrument tags |
| From HAZOP (limited) | 0 | Traceable but sparse HAZOP support |
| Aggregated from HAZOP | 0 | Synthesised from multiple HAZOP rows |
| Derived from HAZOP | 0 | Logically inferred from HAZOP data |
| Engineering standard | 29 | Based on industry code or standard |
| Domain knowledge | 67 | Expert knowledge (HAZOP gap) |
| Suggested | 0 | Gap-fill requiring site validation |
Phase 1 (60 days): Process Safety Team validates bowtie groupings, top events and barrier classifications. Phase 2 (90 days): Mechanical Integrity Engineer validates PFD / SIL on all hardware barriers. Phase 3 (120 days): Site walkdown confirms presence and condition of suggested barriers (gap-fill). Phase 4 (180 days): Improvement plan (Section 9) implemented and closed.
Copy_of_Qasim_HAZOP_report_Excel.xlsx's barrier framework provides a foundation of instrumented hardware protection across 19 MAH scenarios. 17 systems are assessed as Adequate or Adequate with Concerns; 1 Require Improvement; 1 Inadequate. The barrier set is strong in prevention (alarm and trip-based protection from HAZOP) but weak in post-release mitigation, non-hardware defence layers, and barrier-independence assurance.
Recommended actions sorted by timeframe. Immediate items unblock the ALARP demonstration; systemic items improve future HAZOP and barrier management processes.
This assessment carries an evidence confidence of 65/100 reflecting its desk-review basis. The three principal limitations are: (a) barrier condition has not been verified by site observation or maintenance records; (b) PFD / SIL data is from design basis, not operational performance; (c) human / procedural barriers were predominantly added from domain knowledge rather than extracted from the HAZOP. These limitations are inherent to desk-review methodology and are addressed in the four-phase verification plan (Section 10.3).
Integrate the SCE / SCA register (Section 7) into the asset's barrier management system (DNV Synergi Life or equivalent) using the WORLD_CLASS.xlsx output. Establish recurring barrier-health reporting against the FARSI performance standards. Re-run this assessment whenever the underlying HAZOP is revised, the process design changes, or following any process safety event at the facility.
Prepared by Ascendera Group (for ACWA Power). FOR REVIEW -- REQUIRES PROCESS SAFETY TEAM VALIDATION.