Prakash Bahadur Thapa Memorial University, St. John’s, NL, Canada, A1B 3X5 Corresponding author: Email:
[email protected]; Tel: +1(709) 330-8666
Abstract In this tandem offloading simulation and Risk Bow tie Approach analysis I am taking the three offloading systems evaluated, a base case has been determined with SPM CALM buoy as a primary offloading system and a tandem offloading as a back-up/contingency system. The objective of this tandem offloading study is to simulate the tandem offloading operations under representative met ocean conditions identified from the preliminary operability assessment for the tandem offloading system. Eight representative met ocean cases were selected from the site specific conditions. The vessel particulars and hydrodynamic characteristics were scaled from the established database in SHUTTLE. Time domain simulations were made for tandem offloading operations using MARIN software SHUTTLE. This numerical simulation study on the contingent tandem offloading system to suggest that it is feasible to transfer the cargo under selected representative met ocean cases with up to 3 tugs (1x100 tones BP and 2x60 ton BP).
In no cases considered for this study, the maximum hawser load exceeded 150 ton or 1,471 kN. The specified operating limit on cyclic hawser load, a maximum 100 ton or 981 kN load occurring no more than 5 times/hour, could be achievable by appropriately deploying the tugs.
In most selected cases, 2 tugs (1x 100 ton BP and 1x 60 ton BP) are required to maintain the off take tanker heading and position. These included the cases under the cross wind and current conditions, and cases under beam on wind and current in parallel.
In case of strong wind (15 m/s) from the beam with cross current stern on, three tugs (1x100 ton BP and 2x60 ton BP) were needed to meet the operating criteria.
When metocean conditions are collinear with stern on wind and current, 1x100 ton BP astern pulling tug was required to control the heading and position of the off take tanker.
Only 1x60 ton BP tug or 1x100 ton tug with reduced BP) was needed when all environmental elements action on bow with quartering wind and current on either side of the FPSO .
The SHUTTLE analysis for more metocean conditions stretched beyond the environmental limits, different loading conditions of the FPSO and the off take tankers updating the predefined limiting metocean conditions.
Study on hawser configuration (composition and length) and installation of constant tension winches with an aim to reduce cyclic peak load of the hawser design through numerical simulation.
Assessment of the tug performance in field conditions and installation of constant tension winches better understanding of the tugs’ capability of controlling the off take tanker heading and position through numerical simulation and bridge simulation/physical model test.
Implementation of monitoring, inspection and maintenance programs during operations (Operation).
1.0 INTRODUCTION From the three alternative offloading systems evaluated, a base case has been determined with SPM CALM buoy recommended as a primary offloading system and a tandem offloading as a backup/contingency system. It is expected that the operability of the SPM system is over 95% uptime. The tandem offloading system, however, offers much lower uptime below 60% (mainly due to the strong currents). The operability assessment for tandem offloading was performed by applying predefined operating criteria to time traces of met ocean conditions. Generally the reliability of the offloading operability could be improved by time-domain simulation of the recurring offloading operations over representative met ocean time traces. The objectives of this tandem offloading study are:
Simulate the tandem offloading operations under representative metocean conditions identified from the preliminary operability assessment for the tandem offloading system,
Verify if the limiting metocean conditions identified are acceptable in terms of hawser loads, tanker excursions and tug operations,
Confirm the feasibility of the tandem offloading as a backup/contingency offloading system
Conduct an
initial assessment of the system behaviour under selected representative
environmental conditions
Provide operational guidance to improve the safety of the tandem offloading system.
2.0 Study Basis Data 2.1 Operating Criteria for Tandem Offloading Tandem Offloading Criteria are: Distance Floating production Storage and Offloading (FPSO) tanker: >= 40 m Hawser load:
981 kN /hr 0
Min Heading (deg) 205.01
Max Heading (deg) 205.16
Min Heading (deg) 197.99
Max Heading (deg) 198.64
Within ±60 deg sector Yes
Table 4.6 Results of case 3 with 1x60 tones tug assistance 5.0 Conclusions and recommendations
5.1 General This numerical simulation study on the contingent tandem offloading system suggested that it is feasible to transfer the cargo under selected representative metocean cases with up to 3 tugs (1x100 ton BP and 2x60 ton BP). 5.2 Tug Requirement In most selected cases, 2 tugs (1x 100 ton BP and 1x69 ton BP) are required to maintain the off take tanker heading and position. These included the cases 6 ~ 8 under the cross wind and current conditions, and cases 1 ~ 2 under beam on wind and current in parallel. In case of strong wind (15 m/s) from the beam with cross current stern on (case 5), three tugs were needed to meet the operating criteria.
When metocean conditions are collinear with stern on wind and current (case 4), 1x100 tons BP astern pulling tugs was required to control the heading of position of the offtake tanker. Case 3 represents the metocean condition when all environmental elements action on bow with quartering wind and current on either side of the FPSO. In this case, only 1x60T BP tug was required. 5.3 Hawser Load In no cases selected for this study, the maximum hawser load exceeded 150 ton or 1,471 kN. The specified operating limit on cyclic hawser load could be achieved by appropriately deploying the tugs. It should be noted that an increase of the BP of the astern pulling tug could help reduce the heading difference of two vessels, but also increase the occurrence of excessive cyclic hawser load. Alternatively, it is worthwhile to explore the different composition and length of the hawser to reduce the cyclic load and thereby optimize the tug BP requirement. 5.4 Recommendations The following recommendations for this study on the tandem offloading for FPSO:
Metocean conditions stretched beyond the environmental limits, different loading conditions of the FPSO and the off take tankers – updating the pre-defined limiting metocean conditions.
This study on alternative hawser configuration (composition and length) and installation of constant tension winches with an aim to reduce cyclic peak load of the hawser – design through numerical simulation and physical model test.
Assessment of the tug performance in field conditions and installation of constant tension winches – better understanding of the tugs’ capability of controlling the off take tanker heading and position through numerical simulation and bridge simulation/physical model test.
Monitoring the hawser load, the tanker heading position during any offloading operation to providing better communication to and feedback control of the assisting tugs (Operation), regular inspection and maintenance of the hawser and other mooring equipment. (Operation).
6.0 Bow tie Risk assessment Approach
6.0 Bow Tie Analysis Hazards, Threats and Barriers
Figure 6.1 off take Tanker Approach
HAZARDS
THREATS
BARRIERS AND CONTROLS
Offtake Tanker
Ocean Current Conditions
Berthing Procedure
Wind and Sea Conditions Berthing Procedure
INPUT Current Monitoring Equipment (Redundancy of monitoring equipment requested in MOC 75) INPUT Berthing Tugs Specifications (Set at 120 ton bollard Pull for purpose of review)
Ocean Current operations limit set in Berthing Procedure INPUT (Wave info received from wave buoy) Wind and Wave Monitoring Equipment fitted to FPSO requested in MOC 75
Pilot Training and Competence
Wind and Wave operations limit set in Berthing Procedure
Tanker Loss of Power
Berthing Tugs 2 x 100 %
Pilot Training and Competence Berthing Tugs 2 x 100 %
Offtake Tanker Vetting Process Tanker uncontrolled powered approach
TOP EVENT Berthing Procedures
Loss of Communications with tanker
Lack of training/experience of Pilot or Berthing Tug Crews
Squalls
Duplication of Radio Equipment on tanker and FPSO (Vessel Vetting Process)
Pilot and Tug Crew Selection Process
Secure power Supplies on tanker and FPSO Vessel Vetting process)
Training plans and Competence Assurance System
Pilot Training and Competence
Berthing Procedures
Berthing Tugs 2 x 100 %
Dedicated radio Channels
Tandem Offloading Simulator Training
Weather Radar Surveillance on Tanker, Berthing Tugs, and FPSO Berthing Procedures (Squalls)
Collision between FPSO and Offtake Tanker on approach under pilotage
Figure 6.2 off take Tanker Approach (Continued)
HAZARDS
Offtake Tanker
BARRIERS AND CONTROLS
THREATS
Agreed manning level for operation (Service Level Agreement required for back up Pilot)
Shortage or incapacity of Pilot
Fitness and health checks and monitoring of Pilots’ health
Human Error leading to inappropriate tanker approach
Berthing Procedures (Duties of Pilots FPSO/Tanker Navigation Instrumentation Competence of Pilots Berthing Tugs 2x100%
MOC Differential GPS on FPSO linked to portable DGPS on Offtake Tanker
Towline and/or fixing failures on tug or Off take tanker
Distraction caused by FPSO (ESD, blow-down to flare or other FPSO operation, process upset or emergency situation
TOP EVENT Collision between FPSO and Offtake Tanker on approach under pilotage
Towline Specifications Tug and tanker vetting process (vessels and crews
Towline and fixing inspection and maintenance
FPSO Operating procedures for Simultaneous Operations and Tandem Loading Operations
Berthing Procedures Tug connection and towing
Berthing Tugs 2x100%
Berthing Procedure Emergency Response
Figure 6.3 off take Tanker Approach Continued Recovery Measures
CONSEQUENCES
Emergency Procedures for Tanker Collision
Structural Damage to FPSO Hull
ESCALATION
Vessels Continues to cause damage after impact (possible damage to risers
Note Riser Protection not designed to withstand energy levels of drifting Offtake Tanker
FPSO Mooring Design FPSO Hull Design
FPSO Double Hull Construction No outboard hydrocarbon tanks
TOP EVENT Collision between FPSO and Offtake taker on approach under pilotage
Emergency Response Procedures (Pollution Incident Control)
Emergency Response Training (Pollution incident Control) Self-Sealing Hose Breakaway Coupling
Fire Fighting Capabilities of FPSO and Tugs
FPSO ESD and Emergency procedures
Tug Assistance and Vessels Engines
Remote Loading ESD controlled by FPSO and Tanker
Emergency Disconnect System and Procedures
Fire
Pollution
Vessels Continues to cause damage after impact (possible damage to risers
Tug Assistance and Vessels Engines Note Riser Protection not designed to withstand energy levels of drifting Offtake Tanker
Escalated explosion due to hydrocarbon leakage from Offtake Tanker
No Explosion Protection on Aft of FPSO to mitigate an escalated event from Offtake Tanker
Figure 6.4 off take tanker Approach Continued Recovery Measures
CONSEQUENCES
Emergency Response procedure
Operating procedure limiting access to aft deck of FPSO during berthing
Loss of life
Personal Injury
SIMOPS Procedure Work in Machinery space during berthing
Loss of Reputation Local
TOP EVENT
ESCALATION
SNEPCO PR Contingency plan
Collision between FPSO and Offtake taken on approach under pilotage
Repair plans and “insurance” spares and equipment
Loss of production
Escalated damage/pollution/loss of asset due to collision
SHELL Group PR Contingency Plan
International Loss of Reputation
Figure 6.5 off take Tanker Moored
BARRIERS AND CONTROLS
THREATS Note Normal Tanker manning not considered adequate for Bonga Tandem loading Operations
HAZARDS
Offtake Tanker Moored to FPSO
Adequate manning of tugs and Offtake Tanker
Tanker and Tug Crew Fatigue during Loading
Mooring Hawser Failure
Hawser
Mooring Tugs 2x 100%
Mooring hawser Specifications
Crew Working Hour Limitations
Adequate Manning for pilot/Loading master
Hawser maintenance and Inspection
Hawser load monitor via Hawser load Monitoring Instrumentation
MOC 75 Differential GPS on FPSO linked to portable DGPS on Offtake Tanker
Accidental Release Release system for hawsers fails in closed position
Loading Procedure
Collision between FPSO and Offtake Tanker whilst moored to FPSO
Mooring Tugs 2x 100%
Human Error FPSO/Tanker Navigation Instrumentation
MOC 75 Differential GPS on FPSO linked to portable DGPS on Offtake Tanker
Competence of Pilots
Berthing Tugs 2x100%
TOP EVENT
Adequate Manning for pilot/Loading master
Figure 6.6 off take Tanker Moored (Continued)
Recovery Measures
CONSEQUENCES
Emergency Procedures for Tanker Collision
Structural Damage to FPSO Hull
ESCALATION
Vessels Continues to cause damage after impact (possible damage to risers
FPSO Mooring Design FPSO Hull Design
FPSO Double Hull Construction No outboard hydrocarbon tanks
TOP EVENT Collision between FPSO and Offtake taker whilst moored to FPSO
Emergency Response Procedures (Pollution Incident Control)
Emergency Response Training (Pollution incident Control) Self-Sealing Hose Breakaway Coupling
Fire Fighting Capabilities of FPSO and Tugs
FPSO ESD and Emergency procedures
Pollution
Vessels Continues to cause damage after impact (possible damage to risers
Tug Assistance and Vessels Engines Note Riser Protection not designed to withstand energy levels of drifting Offtake Tanker
Note Riser Protection not designed to withstand energy levels of drifting Offtake Tanker
Remote Loading ESD controlled by FPSO and Tanker
Emergency Disconnect System and Procedures
Fire
Tug Assistance and Vessels Engines
Escalated explosion due to hydrocarbon leakage from Offtake Tanker
No Explosion Protection on Aft of FPSO to mitigate an escalated event from Offtake Tanker
Figure 6.7 off take Tanker Moored
Recovery Measures
CONSEQUENCES
Emergency Response procedure
Operating procedure limiting access to aft deck of FPSO during berthing
Loss of life
Personal Injury
SIMOPS Procedure Work in Machinery space during berthing
Loss of Reputation Local
TOP EVENT
ESCALATION
SNEPCO PR Contingency plan
Collision between FPSO and Offtake taker whilst moored to FPSO
Repair plans and “insurance” spares and equipment
Loss of production
Escalated damage/pollution/loss of asset due to collision
SHELL Group PR Contingency Plan
International Loss of Reputation
Figure 6.8 off take Tanker Departing
BARRIERS AND CONTROLS
THREATS
HAZARDS
Offtake Tanker Moored to FPSO
Emergency Disconnect system on FPSO will release Hawser (Can operate even with mooring hawser under tension
Disconnect not possible due to system failure
Tanker
Manoeuvres towardsFPSO in order to Disconnect Mooring Hawser
MOC 75 Differential GPS on FPSO linked to portable DGPS on Offtake Tanker
Emergency Disconnection procedures
FPSO/Tanker Navigation Instrumentation Competence of Pilots Tanker Departure Procedures
TOP EVENT Berthing Tugs 2x100%
Collision between FPSO and Offtake during departure
Figure 8.9 off take Tanker Departing (Continued) Recovery Measures
CONSEQUENCES
Emergency Procedures for Tanker Collision
Structural Damage to FPSO Hull
ESCALATION
Vessels Continues to cause damage after impact (possible damage to risers
FPSO Mooring Design FPSO Hull Design
FPSO Double Hull Construction No outboard hydrocarbon tanks
TOP EVENT Collision between FPSO and Offtake tanker during departure
Emergency Response Procedures (Pollution Incident Control)
Fire Fighting Capabilities of FPSO and Tugs
Pollution
Vessels Continues to cause damage after impact (possible damage to risers
Tug Assistance and Vessels Engines Note Riser Protection not designed to withstand energy levels of drifting Offtake Tanker
Emergency Response Training (Pollution incident Control)
FPSO ESD and Emergency procedures
Tug Assistance and Vessels Engines Note Riser Protection not designed to withstand energy levels of drifting Offtake Tanker
Fire
Escalated explosion due to hydrocarbon leakage from Offtake Tanker
No Explosion Protection on Aft of FPSO to mitigate an escalated event from Offtake Tanker
Figure 6.10 Mooring Hawser Failures
HAZARDS
Mooring Hawser Tension
THREATS
Excessive Loading
BARRIERS AND CONTROLS
Hawser Design Hawser Load Monitoring
Mooring System Operating Procedures
Cyclic Loading Hawser Design
Hawser Replacement Schedules
Crew Training Mooring System Operating Procedures
Degradation
Mechanical Damage
Hawser Maintenance and Inspection
Mooring System Design
Hawser Maintenance and Inspection
Crew Training
TOP EVENT Crude Export Tandem Mooring Failure Manufacturing Defects
Quality Assurance Process
Factory Acceptance Test
Figure 6.11 Mooring Hawser Failures
Recovery Measures
CONSEQUENCES
ESCALATION
Tanker Breakout
TOP EVENT Crude Export Tandem Mooring Failure
Berthing Tugs 2 x 100%
Emergency Procedures
Emergency Procedures Training and Drills
Hose Breakout
See Sheet for Loading Hose Failure Loading Hose Failure (See Loading Hose Failure Sheet)
Collision between Offtake Tanker and FPSO
See Sheeting for Collision During whilst Moored
Figure 6.12 Loading Hose Failure
HAZARDS
Crude Oil Hydrocarbons
THREATS
Mechanical Damage
BARRIERS AND CONTROLS
Hose Design and QA
Hose Inspection and Maintenance Procedures
Hose Pressure Testing Prior to Use
Hose Design
Loading Pump Press Controlled and HP Shut down system (System Designed to API 14C)
Overpressure
Shock Loads as a result of Pressure Surges
Hose Design
Loading Pump Press Controlled and HP Shut down system (System Designed to API 14C) Hose Selfsealing
Excessive Tension
TOP EVENT Manufacturing Defects
Autosubmergence Environmental and Actinic Degradation Seawater and Fatigue Damage
Hose Design
Manufacturer Selection OCIMF
Inspection and Maintenance Procedures
Loading Hose Failure during Loading Operations
Marine Breakaway Coupling
Factory Acceptance Testing Quality Assurance Process
Hose Design Pressure Test
Sabotage
Security Procedures
Inspection and Maintenance
Damage caused by Supply Boats Supply Boat Operating Procedures
Hose Design (Abrasion Resistance)
Pressure Test before Use
Figure 6.13 Loading Hose Failure ESCALATION CONSEQUENCES
Recovery Measures
Pollution
TOP EVENT Crude Export Loading Hose Failure during Loading Operations
Quantity Oil pumped/Quantity Received Reconciliation
Visual Alert form watchman on FPSO/Tug or Offtake Tanker
Emergency Shutdown on Offtake Tanker or FPSO
Emergency Shutdown on Offtake Tanker or FPSO
Loss of Product
Loss of Reputation
Collision between Offtake Tanker and FPSO