ASCENDERA
Bridging Capital and Execution

qassim_sample.xlsx
BOWTIE RISK ASSESSMENT

HAZOP-to-Bowtie Conversion -- Desk Review
Document Reference
QASSIM_SAMPLEXLSX_BT-REPORT_R0
Revision
R0 -- Initial Issue
Date
2026-04-26
Facility
qassim_sample.xlsx
Technology
CCGT
Source
HAZOP Study (200 rows, 120 scenarios at S≥3)
Evidence Confidence
40/100 (desk review)
Bowties
1
Gap findings
8
Prepared by
Ascendera Group (for ACWA Power)
Contact
clientaccess@ascenderagroup.sa
Website
www.ascenderagroup.sa
Scope Coverage: 0 of 32 mandatory systems (0%) · LIMITED
FOR REVIEW -- REQUIRES PROCESS SAFETY TEAM VALIDATION

Table of Contents

1. Executive Summary and Asset Risk Profile

Scope: This assessment converts the submitted HAZOP study (200 rows, 1 nodes) into bowtie format. The submitted study covers 0 of 32 mandatory systems for a complete CCGT asset-level scope (0% mandatory coverage; classification LIMITED). The remaining 32 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: 0 of 32 mandatory systems -- LIMITED

1.1 Risk Landscape Overview

This Bowtie Risk Assessment evaluated 1 Major Accident Hazard scenarios across qassim_sample.xlsx (CCGT), developing 1 bowtie diagrams encompassing 1 threat pathways and 1 consequence pathways. A total of 1 prevention barriers and 0 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 (200 rows, 120 scenarios at S>=3) and carries an evidence confidence cap of 40/100. All outputs require validation by the Process Safety Team.

1.2 Barrier Adequacy Summary

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.

SystemMax SPrev.Mit. Prevention AdequacyMitigation Adequacy OverallPriority
Node 1S=510AdequateInadequateInadequateCritical

1.3 Key Findings

  1. 0 of 1 threat pathways (0%) currently have zero prevention barriers. If any of these threats materialises, there is no engineered defence between the initiating event and loss of containment.
  2. 0% of mitigation barriers are generic shared trunk controls (detection, ESD, access restriction, emergency response) rather than consequence-specific protection. The plant's post-release defence posture is weighted toward reactive response rather than targeted consequence reduction.
  3. 0 barriers each appear across 3 or more systems, creating a systemic dependency where degradation of one shared barrier weakens protection across multiple MAH scenarios. The most widely shared barrier is psv: psv set (safeguard 3: relief valve sized for fire case), present in 1 of 1 systems (100%).
  4. The HAZOP safeguard set is dominated by instrumented hardware: 0% Hardware-Active. Only 0 of 1 barriers (0%) are human, procedural or organizational. This reflects HAZOP-methodology bias rather than necessarily inadequate plant protection.
  5. 100% of barriers are assessed as Partially Effective from desk review -- the barrier exists but its reliability or completeness cannot be fully confirmed without site evidence. Lowest-effectiveness system: Node 1 at 0% Effective.

1.4 Priority Recommendations

#RecommendationType ScopeOwnerTarget
1Conduct supplementary HAZOP workshop focused on non-hardware barriers (emergency procedures, PTW, competency, SOPs).VerificationAll 1 systemsProcess Safety Lead90 days
2Validate suggested mitigation barriers against actual plant design and installed protection systems.VerificationAll systems with library-seeded mitigationProcess Safety Lead60 days
3Confirm prevention coverage for unprotected threat pathways -- verify whether barriers exist but were not documented in the HAZOP.Engineering0 threat pathwaysI&C Engineering60 days
4Verify SIL ratings on safety-instrumented functions against IEC 61511 design basis and operational performance records.VerificationAll SIL-credited barriersI&C Engineering120 days
5Run a multi-discipline barrier-diversity review (Operations, Maintenance, HSE, I&C) to identify non-hardware barriers that exist at the plant.WorkshopCross-cutting (all systems)HSSE Manager90 days
6No mitigative barriers identified in HAZOP. All 0 suggested barriers marked for validation.ImprovementNode 1Process Safety Lead60 days
7Single barrier on instrumentation_failure pathway (THR-N-001). Single point of failure on S=5 catastrophic consequence.ImprovementNode 1Process Safety Lead60 days
8Extend HAZOP scope to cover the missing mandatory systems: Fuel Gas Receiving Station, Fuel Gas Heating, Filtration and Let-down, Gas Turbine and Enclosure, Gas Turbine Fuel Manifold, Nozzles, Purge, Gas Turbine Lubrication System, GT EncloImprovementCross-cutting (all systems)Process Safety Lead60 days

1.5 ALARP Position Statement

Based on this desk-review assessment, risks from 1 of 1 MAH scenarios cannot be confirmed as ALARP until the priority recommendations are addressed. The principal concerns are Node 1 where barrier coverage falls below industry good practice for CCGT facilities. The 3 Critical and 5 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.

2. Introduction, Scope and Methodology

2.1 Purpose and Objectives

This report converts the HAZOP study for qassim_sample.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.

2.2 Scope and Battery Limits

HAZOP source: 200 rows analysed, 120 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.

2.3 Scope Completeness Check

The submitted HAZOP is benchmarked against the Ascendera Reference Scope v1.0 for CCGT (40 reference systems, 32 mandatory). Scope Coverage: 0 of 32 mandatory systems -- LIMITED

Submitted HAZOP covers 0 of 32 mandatory systems for CCGT scope (0% mandatory coverage). Classification: LIMITED. Missing mandatory: Fuel Gas Receiving Station, Fuel Gas Heating, Filtration and Let-down, Gas Turbine and Enclosure, Gas Turbine Fuel Manifold, Nozzles, Purge, Gas Turbine Lubrication System, GT Enclosure Ventilation and Fire Suppression, HRSG Drums (HP/IP/LP) and Downcomer System, Superheater and Reheater, Economiser, Steam Turbine, Steam Turbine Lube, Seal, and Control Oil, Condenser (Surface or Air-Cooled), Condensate Polishing, Feedwater System (HP / IP / LP), Demineralisation Water Treatment, Boiler Water Chemical Dosing, Auxiliary (Closed-Loop) Cooling Water System, Generator, Exciter, Cooling, Seal Oil, 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, Plant Fire Water System, Special Hazard Fire Suppression, Instrument Air Compression, Drying, Distribution, 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 SystemClassificationStatus Matched HAZOP NodeRationale
Fuel Gas Receiving StationMandatorymissing—No submitted HAZOP node matched 'Fuel Gas Receiving Station' (best fuzzy ratio 0 below threshold 75).
Fuel Gas Heating, Filtration and Let-downMandatorymissing—No submitted HAZOP node matched 'Fuel Gas Heating, Filtration and Let-down' (best fuzzy ratio 0 below threshold 75).
Gas Turbine and EnclosureMandatorymissing—No submitted HAZOP node matched 'Gas Turbine and Enclosure' (best fuzzy ratio 0 below threshold 75).
Gas Turbine Fuel Manifold, Nozzles, PurgeMandatorymissing—No submitted HAZOP node matched 'Gas Turbine Fuel Manifold, Nozzles, Purge' (best fuzzy ratio 0 below threshold 75).
Gas Turbine Lubrication SystemMandatorymissing—No submitted HAZOP node matched 'Gas Turbine Lubrication System' (best fuzzy ratio 0 below threshold 75).
GT Enclosure Ventilation and Fire SuppressionMandatorymissing—No submitted HAZOP node matched 'GT Enclosure Ventilation and Fire Suppression' (best fuzzy ratio 0 below threshold 75).
HRSG Drums (HP/IP/LP) and Downcomer SystemMandatorymissing—No submitted HAZOP node matched 'HRSG Drums (HP/IP/LP) and Downcomer System' (best fuzzy ratio 0 below threshold 75).
Superheater and ReheaterMandatorymissing—No submitted HAZOP node matched 'Superheater and Reheater' (best fuzzy ratio 0 below threshold 75).
EconomiserMandatorymissing—No submitted HAZOP node matched 'Economiser' (best fuzzy ratio 0 below threshold 75).
Steam TurbineMandatorymissing—No submitted HAZOP node matched 'Steam Turbine' (best fuzzy ratio 0 below threshold 75).
Steam Turbine Lube, Seal, and Control OilMandatorymissing—No submitted HAZOP node matched 'Steam Turbine Lube, Seal, and Control Oil' (best fuzzy ratio 0 below threshold 75).
Condenser (Surface or Air-Cooled)Mandatorymissing—No submitted HAZOP node matched 'Condenser (Surface or Air-Cooled)' (best fuzzy ratio 0 below threshold 75).
Condensate PolishingMandatorymissing—No submitted HAZOP node matched 'Condensate Polishing' (best fuzzy ratio 0 below threshold 75).
Feedwater System (HP / IP / LP)Mandatorymissing—No submitted HAZOP node matched 'Feedwater System (HP / IP / LP)' (best fuzzy ratio 0 below threshold 75).
Demineralisation Water TreatmentMandatorymissing—No submitted HAZOP node matched 'Demineralisation Water Treatment' (best fuzzy ratio 0 below threshold 75).
Boiler Water Chemical DosingMandatorymissing—No submitted HAZOP node matched 'Boiler Water Chemical Dosing' (best fuzzy ratio 0 below threshold 75).
Auxiliary (Closed-Loop) Cooling Water SystemMandatorymissing—No submitted HAZOP node matched 'Auxiliary (Closed-Loop) Cooling Water System' (best fuzzy ratio 0 below threshold 75).
Generator, Exciter, Cooling, Seal OilMandatorymissing—No submitted HAZOP node matched 'Generator, Exciter, Cooling, Seal Oil' (best fuzzy ratio 0 below threshold 75).
Generator Step-Up TransformerMandatorymissing—No submitted HAZOP node matched 'Generator Step-Up Transformer' (best fuzzy ratio 0 below threshold 75).
Unit Auxiliary and Station Service TransformersMandatorymissing—No submitted HAZOP node matched 'Unit Auxiliary and Station Service Transformers' (best fuzzy ratio 0 below threshold 75).
HV / EHV Switchyard (AIS or GIS)Mandatorymissing—No submitted HAZOP node matched 'HV / EHV Switchyard (AIS or GIS)' (best fuzzy ratio 0 below threshold 75).
Medium Voltage SwitchgearMandatorymissing—No submitted HAZOP node matched 'Medium Voltage Switchgear' (best fuzzy ratio 0 below threshold 75).
Emergency Diesel GeneratorMandatorymissing—No submitted HAZOP node matched 'Emergency Diesel Generator' (best fuzzy ratio 0 below threshold 75).
Distributed Control System and SCADAMandatorymissing—No submitted HAZOP node matched 'Distributed Control System and SCADA' (best fuzzy ratio 0 below threshold 75).
Safety Instrumented System / Emergency ShutdownMandatorymissing—No submitted HAZOP node matched 'Safety Instrumented System / Emergency Shutdown' (best fuzzy ratio 0 below threshold 75).
Fire and Gas DetectionMandatorymissing—No submitted HAZOP node matched 'Fire and Gas Detection' (best fuzzy ratio 0 below threshold 75).
Plant Fire Water SystemMandatorymissing—No submitted HAZOP node matched 'Plant Fire Water System' (best fuzzy ratio 0 below threshold 75).
Special Hazard Fire SuppressionMandatorymissing—No submitted HAZOP node matched 'Special Hazard Fire Suppression' (best fuzzy ratio 0 below threshold 75).
Instrument Air Compression, Drying, DistributionMandatorymissing—No submitted HAZOP node matched 'Instrument Air Compression, Drying, Distribution' (best fuzzy ratio 0 below threshold 75).
Plant Service AirMandatorymissing—No submitted HAZOP node matched 'Plant Service Air' (best fuzzy ratio 0 below threshold 75).
Nitrogen Generation and DistributionMandatorymissing—No submitted HAZOP node matched 'Nitrogen Generation and Distribution' (best fuzzy ratio 0 below threshold 75).
HVAC for MCC, Chemical Buildings, Control RoomMandatorymissing—No submitted HAZOP node matched 'HVAC for MCC, Chemical Buildings, Control Room' (best fuzzy ratio 0 below threshold 75).
Fuel Oil Receiving, Storage, TransferConditionalmissing—No submitted HAZOP node matched 'Fuel Oil Receiving, Storage, Transfer' (best fuzzy ratio 0 below threshold 75).
Selective Catalytic Reduction (SCR)Conditionalmissing—No submitted HAZOP node matched 'Selective Catalytic Reduction (SCR)' (best fuzzy ratio 0 below threshold 75).
Once-Through Cooling Water Intake and OutfallConditionalmissing—No submitted HAZOP node matched 'Once-Through Cooling Water Intake and Outfall' (best fuzzy ratio 0 below threshold 75).
Wet Mechanical- or Natural-Draft Cooling TowerConditionalmissing—No submitted HAZOP node matched 'Wet Mechanical- or Natural-Draft Cooling Tower' (best fuzzy ratio 0 below threshold 75).
Air-Cooled CondenserConditionalmissing—No submitted HAZOP node matched 'Air-Cooled Condenser' (best fuzzy ratio 0 below threshold 75).
Black Start CapabilityConditionalmissing—No submitted HAZOP node matched 'Black Start Capability' (best fuzzy ratio 0 below threshold 75).
Burner Management SystemConditionalmissing—No submitted HAZOP node matched 'Burner Management System' (best fuzzy ratio 0 below threshold 75).
Auxiliary (Startup) BoilerConditionalmissing—No submitted HAZOP node matched 'Auxiliary (Startup) Boiler' (best fuzzy ratio 0 below threshold 75).

2.4 Methodology

StandardApplication
IEC 61882:2016HAZOP study methodology (source data)
CCPS / EI Bow Ties in Risk Management (2018)Bowtie methodology, barrier criteria
IEC / ISO 31010:2019Risk assessment techniques framework
IEC 61511:2016SIS requirements for SIL-rated barriers
IOGP Report 544Barrier standardisation and classification
API RP 754Process safety performance indicators
Energy Institute SCE Performance Standards (2019)FARSI model for performance standards

2.5 Confidence Doctrine

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.

3. Facility Description

Facility name: qassim_sample.xlsx
Technology: CCGT
HAZOP source file: /data/output/4d9cf73c-9686-4497-96ab-51c8bc4485e4/input.xlsx
HAZOP rows ingested: 200

3.1 Asset Boundaries

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.

4. Major Accident Hazard Register

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 IDSystemHazardTop EventMax SeverityBowtie Ref
MAH-N-001Node 1Fluid in Node 1Loss of containment of fluid from Node 1S=5 (E)BT-N-001

5. System-Level Bowtie Assessments

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.

5.1 Node 1

Catalogue ref: BT-N-001
Hazard: Fluid in Node 1
Top Event: Loss of containment of fluid from Node 1
Max severity: S=5 | Prev barriers: 1 | Mit barriers: 0 | Gaps: 2

Node 1 has 1 prevention and 0 mitigation barriers. Of these, 1 were traced to HAZOP safeguards while 0 were identified from domain knowledge or engineering standards and require site verification. Defence-in-depth includes 1 barrier type (Hardware - Passive). Barrier effectiveness from desk review: 0% Effective; the remainder are Partially Effective and need site validation.

Fluid in Node 1 HAZARD: Fluid in Node 1 Instrumentation or control system failure Instrumentation or control system failure THR-N-001 Consequence 3: overpressure leading to rupture Consequence 3: overpressure leading to rupture S=5 CON-N-001 Loss of containment of fluid from Node 1 TOP EVENT Loss of containment of fluid from Node 1 PSV: PSV set (Safeguard 3: relief valve sized for fire case) PSV: PSV set (Safeguard 3: relief val... HW-P THREATS PREVENTION BARRIERS TOP EVENT MITIGATION BARRIERS CONSEQUENCES KEY Threat Top Event Consequence (S4-5) Consequence (S3) Prevention Mitigation Gap (suggested) Effective Partial Impaired Not Assessed
CRITICAL GAP-N-001
No mitigative barriers identified in HAZOP. All 0 suggested barriers marked for validation.
CRITICAL GAP-N-002
Single barrier on instrumentation_failure pathway (THR-N-001). Single point of failure on S=5 catastrophic consequence.

6. Asset Barrier Register

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.

IDSystemBarrierSide CategoryConditionPFDSIL ProvenanceProvenance DetailIndependenceSharedEIA
PB-N-001Node 1PSV: PSV set (Safeguard 3: relief valve sized for fire case)PreventionHardware - PassivePARTIALLY_EFFECTIVEFrom HAZOPVerified rows 4 S=5.Independent1Concern

7. SCE/SCA Register

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 IDTypeSystemBarrier SideMAHCat.Performance Standard Test IntervalOwner
SCE-001SCENode 1PSV: PSV set (Safeguard 3: relief valve sized for fire case)PreventionEAuto-actuate per design intent12 monthsMI Eng

8. Risk Assessment and ALARP Demonstration

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.

8.1 Codes and Standards Compliance

StandardRequirementAddressed by Status
IEC 61511 (Safety Instrumented Systems)SIL-rated SIS for identified safety functionsPressure / temperature alarms, ESD trips, interlocksPartially -- SIL ratings to be confirmed at site
API 521 / EN ISO 4126 (Pressure Relief)PSV / PRV on every pressurised systemPSVs identified on HRSG, Generator H2, Duct BurnerPartially -- PSV sizing not verified
IEC 60079 / BS EN 60079 (Hazardous Areas)Hazardous area classification for flammable / H2Gas detection on Fuel Gas; H2 detection on GeneratorPartially -- area classification not reviewed
NFPA 850 / API 2001 (Fire Protection)Fire detection and suppression for flammable hazardsFire detection on Fuel Oil; deluge on Fuel Gas / Duct BurnerPartially -- coverage and adequacy not confirmed
API 752 (Blast Resistant Structures)Blast-rated control room for VCE scenariosBlast-rated CR identified for Fuel Gas, Duct BurnerAdequate from desk review -- design basis to confirm

8.2 Good Practice Comparison

ElementGood PracticeCurrent Gap
Prevention barriers per threat2-4 independent barriers per threat (CCPS / EI)1.0 avg; 0% with zeroMinor
Barrier type diversity>=2 categories per critical pathway (Tech + Operational)1 categories overall; 0% Hardware-ActiveMinor
Mitigation specificity>=50% consequence-specific mitigation (CCPS / EI event-tree)0% branch / 0% trunkModerate
Human / procedural layers20-40% of barriers are H / P / O0%Significant

8.3 Risk Reduction Measures

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 IDSystemMeasure FeasibilityCostRisk reduction Reasonably practicable?
GAP-N-001Node 1No mitigative barriers identified in HAZOP. All 0 suggested barriers marked for validation.HighLow-MediumSignificantYes -- recommended
GAP-N-002Node 1Single barrier on instrumentation_failure pathway (THR-N-001). Single point of failure on S=5 catastrophic consequence.HighLow-MediumSignificantYes -- recommended
F-SCOPE-001Cross-cutting (all systems)Extend HAZOP scope to cover the missing mandatory systems: Fuel Gas Receiving Station, Fuel Gas Heating, Filtration and Let-down, Gas Turbine and Enclosure, Gas Turbine Fuel Manifold, Nozzles, Purge, Gas Turbine Lubrication System, GT EncloHighLow-MediumSignificantYes -- recommended
F-SYS-001Cross-cutting (all systems)Add human / procedural barriers (emergency procedures, permit-to-work, competency requirements) to the HAZOP.HighLow-MediumModerateYes -- recommended
F-SYS-002Cross-cutting (all systems)Run a multi-discipline barrier-diversity review so each pathway has both technical and operational defences.HighLow-MediumModerateYes -- recommended
F-SYS-003Cross-cutting (all systems)Complete site verification of barrier condition on the high-severity systems listed; upgrade any barrier that cannot be confirmed Effective.HighLow-MediumModerateYes -- recommended
GAP-d945ca894e26Node 1Assess common-cause failure modes for MI Eng-owned barriers on Node 1. Consider diversifying barrier ownership by adding operational or procedural layers.HighLow-MediumModerateYes -- recommended
F-SCOPE-002Cross-cutting (all systems)Re-run the pipeline with --variant set to the plant's actual technology variant, then review the updated scope completeness report.HighLow-MediumModerateYes -- recommended

8.4 ALARP Conclusion

Based on this desk-review assessment, the residual risk from 1 of 1 MAH scenarios cannot be confirmed as ALARP until the 3 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.

9. Findings, Gap Analysis and Improvement Plan

9.1 Cross-Cutting Systemic Findings

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.

MAJOR F-SYS-001 -- Cross-cutting (all systems)
HAZOP methodology gap: the source HAZOP safeguard set is dominated by instrumented hardware barriers (alarms, trips, interlocks, valve position feedback). Of 0 human / procedural / organizational barriers in this assessment only 0 were extracted from HAZOP rows; the rest were added from domain knowledge and engineering standards. Emergency operating procedures, permit-to-work systems, pre-startup safety reviews, shift handover protocols, and management-of-change processes are not documented as HAZOP safeguards. Recommendation: run a supplementary workshop focused on non-hardware barriers so they are captured as HAZOP safeguards rather than tool inferences. Owner: Process Safety Lead. Target: 90 days.
MAJOR F-SYS-002 -- Cross-cutting (all systems)
Defence-in-depth diversity gap: barrier type distribution across the assessment is Hardware-Active 0%, Hardware-Passive 100%, Procedural 0%, Organizational 0%, Human-Active 0%. Barrier ownership is concentrated: MI Eng owns 100% of all barriers; Operations owns 0%. Per CCPS / EI each critical threat pathway should have barriers from at least two of three categories (Technical / Operational / Organizational). Conduct a barrier-diversity review with multi-discipline participation (Operations, Maintenance, HSE, I&C). Owner: HSSE Manager. Target: 90 days.
MAJOR F-SYS-003 -- Cross-cutting (all systems)
Critically low barrier effectiveness on high-severity systems: Node 1 (0% Effective at S=5). Partially Effective barriers cannot be credited at full PFD value in a LOPA -- typical practice is to inflate the failure probability by 2-10x. On systems with Maximum Credible Consequence of S>=4 this represents a genuine residual-risk concern, not a desk-review artefact. Phase 2 site verification must resolve each barrier's condition to Effective or identify the required improvement. Owner: Mechanical Integrity Engineer. Target: 90 days.
CRITICAL F-SCOPE-001 -- Cross-cutting (all systems)
Submitted HAZOP covers 0 of 32 mandatory systems for CCGT scope (0%). Classification: LIMITED.
MAJOR F-SCOPE-002 -- Cross-cutting (all systems)
Variant not declared on CLI; scope benchmark defaulted to natural gas CCGT. A hydrogen-ready, cogeneration, coal, biomass, waste-to-energy, or reciprocating plant has materially different mandatory scope and cannot be assessed accurately against the default.

9.2 System-Specific Findings by Priority

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.

PriorityCountStandard Closure
CRITICAL260 days
MAJOR190 days
MINOR0180 days
Total system-specific3

Systems carrying CRITICAL findings: Node 1.

CRITICAL F-001 -- Node 1
No mitigative barriers identified in HAZOP. All 0 suggested barriers marked for validation.
CRITICAL F-002 -- Node 1
Single barrier on instrumentation_failure pathway (THR-N-001). Single point of failure on S=5 catastrophic consequence.
MAJOR F-003 -- Node 1
Common-cause failure vulnerability on Node 1: 100% of barriers (1/1) are owned by MI Eng. A systematic failure in that discipline's domain (DCS failure, instrument air loss, staffing gap) would simultaneously degrade the majority of barriers.
Assess common-cause failure modes for MI Eng-owned barriers on Node 1. Consider diversifying barrier ownership by adding operational or procedural layers.

9.3 Common Themes

Cross-finding analysis -- the recurring patterns that emerge when the per-bowtie findings are read together.

Generic mitigation across systems
A small set of mitigation titles appears across many systems (emergency response, access restriction, emergency isolation, insulation and lagging). These were populated from the barrier library, not extracted from the HAZOP. They are appropriate as minimum expectations but mask the absence of system-specific mitigation and create a shared dependency.
Implication: Site verification must confirm these barriers exist as installed systems, not just library expectations.
I&C barrier concentration
0% of all barriers are owned by I&C Engineering, reflecting the HAZOP's focus on instrumented safeguards. This creates common-cause vulnerability -- a DCS failure, loss of instrument air, or loss of UPS would simultaneously degrade the majority of barriers across multiple systems.
Implication: Common-cause failure analysis needed for shared I&C infrastructure (DCS, instrument air, UPS).
Prevention-heavy, mitigation-light
The barrier set is 100% prevention vs 0% mitigation by count, but 0% of mitigation is generic trunk-mounted. Only 0% of mitigation is consequence-specific (fire suppression, blast protection, containment). Defence is strong on preventing loss of containment but weak on managing consequences if prevention fails.
Implication: Process Safety Team should assess consequence-specific mitigation for S>=4 scenarios.
Barrier effectiveness uncertainty
1 of 1 barriers (100%) are Partially Effective from desk review -- they exist in the HAZOP but reliability or completeness cannot be confirmed. Lowest-effectiveness system: Node 1 at 0%. Partially Effective barriers cannot be credited at full PFD value in a LOPA -- the failure probability should be increased by 2-10x.
Implication: Site verification Phase 2 must resolve barrier condition to Effective or identify required improvements.

10. Assessment Confidence and Verification Requirements

10.1 Five-Factor Confidence Framework

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 0% coverage of mandatory reference systems for CCGT.

Hazard identification completeness Medium (weight 25%)

1 MAH scenarios identified from 200 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.

Barrier identification basis Medium (weight 25%)

1 barriers (100%) traced to HAZOP safeguards. 0 (0%) from domain knowledge, 0 (0%) from engineering standards. HAZOP-traced barriers carry highest confidence; library-seeded barriers require site verification.

Barrier effectiveness data Low (weight 20%)

No PFD / SIL data verified against site records. 100% of barriers assessed as Partially Effective. Condition assessment requires maintenance records, test reports and site observation.

Consequence assessment basis Medium (weight 15%)

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.

Degradation factor completeness Low (weight 15%)

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.

10.2 Provenance Breakdown

TierCountDefinition
From HAZOP1Row-level verified with instrument tags
From HAZOP (limited)0Traceable but sparse HAZOP support
Aggregated from HAZOP0Synthesised from multiple HAZOP rows
Derived from HAZOP0Logically inferred from HAZOP data
Engineering standard0Based on industry code or standard
Domain knowledge0Expert knowledge (HAZOP gap)
Suggested0Gap-fill requiring site validation

10.3 Post-Report Verification Plan

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.

11. Conclusions and Forward Look

11.1 Overall Risk Posture

qassim_sample.xlsx's barrier framework provides a foundation of instrumented hardware protection across 1 MAH scenarios. 0 systems are assessed as Adequate or Adequate with Concerns; 0 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.

11.2 Hierarchy of Concerns

Recommended actions sorted by timeframe. Immediate items unblock the ALARP demonstration; systemic items improve future HAZOP and barrier management processes.

Immediate (60 days)

Short-term (90 days)

Medium-term (180 days)

Systemic

11.3 Confidence and Limitations

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).

11.4 Forward Look

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.