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OSE571 Ocean Plant Design
Safety design and API RP 14C
Korea Advanced Institute ofScience and Technology
Daejun CHANG ([email protected])
Division of Ocean System Engineering
Design Procedure and Key deliverablesDesign Procedure and Key deliverables
Design Basis (Philosophy)
Concept Consolidation
Process Flow DiagramProcess Simulation
Equipment SpecificationEquipment Design
System Description
Production Availability ?
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Process Operation and Control Philosophy
P&ID
Layout
HAZOPRisk AssessmentSafety Studies
Caution: Not universally applicable
Hazards and Safety SystemsHazards and Safety Systems
Accident Controlling Protection(F&G Detection, ESD, Depressurization, Alarm)
Accident Mitigating Protection(Active/Passive Fire Protection, Fire/Blast Walls)
Emergency Response(Escape Route, TR, Evacuation Means, Rescue Equipment, Emergency Power)
Potential Accident:
Accident:Fire/Explosion
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Inherent Safety Design(Layout, Inventory, Leak, Ignition)
Basic Process Control(P, T, F, Surge, Back Pressure)
Preventive Protection(Structural & Machinery Integrity, Relief, PSV)
Potential Accident:Gas Leak
Layered Structure of Safety Systems against Fire and Explosion
P&ID (W11)
Process Operation and Control Philosophy (W9)
System Description (W4)
Workflow for Process ControlWorkflow for Process Control
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Field Implementation
Logic Diagram
Functional Design Specification (W11)
API RP 14CAPI RP 14C
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Not restricted to platform topside design.
Topside design for floating installations (FPSO, FSRU, FLNG) conforms to this.
API RP 14CAPI RP 14C
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This document presents recommendations for designing, installing, and testing a basic surface safety system on an offshore production platform.
This recommended practice illustrates how system analysis
1.2 SCOPE1.2 SCOPE
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methods can be used to determine safety requirements to protect any process component.
Overview of Safety SystemsOverview of Safety Systems
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2. SAFETY DEVICE SYMBOLS2. SAFETY DEVICE SYMBOLS
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Safety Device SymbolsSafety Device Symbols
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3.1 PURPOSE AND OBJECTIVES The technical content of this recommended practice establishes a
firm basis for designing documenting a production platform safety system for a process composed of components and systems normally used offshore.
3. INTRODUCTION TO SAFETY ANALYSIS AND SYSTEM DESIGN3. INTRODUCTION TO SAFETY ANALYSIS AND SYSTEM DESIGN
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Moreover, it establishes guidelines for analyzing components or systems that are new or significantly different from those covered in this document.
3.2 SAFETY FLOW CHART Hazards, their propagation, and intervention of safety devices Overall objectives
1. Prevent a release of hydrocarbons2. Shut in the process to stop the flow of hydrocarbons to a leak3. Treat hydrocarbon escaping from the process.
3. INTRODUCTION TO SAFETY ANALYSIS AND SYSTEM DESIGN3. INTRODUCTION TO SAFETY ANALYSIS AND SYSTEM DESIGN
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3. Treat hydrocarbon escaping from the process.4. Prevent ignition5. Shut in the process in the event of a fire.6. Prevent undesirable events causing the additional release
3.4 PREMISES FOR BASIC ANALYSIS AND DESIGNa. Accordance with good engineering practicesb. Two levels of protectionc. Activation order of the two: primary and secondaryd. Proven systems analysis techniques to determine the minimum
safety requirements for a process component.e. All process equipment and functions are incorporated into the
3. INTRODUCTION TO SAFETY ANALYSIS AND SYSTEM DESIGN3. INTRODUCTION TO SAFETY ANALYSIS AND SYSTEM DESIGN
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e. All process equipment and functions are incorporated into the safety system.
f. Safe components + logical integration the entire facility will be protected.
g. The analysis procedure should provide a standard method to develop a safety system and provide supporting documentation.
4.2.1 Undesirable Events4.2.1.1 Overpressure4.2.1.2 Leak4.2.1.3 Liquid Overflow4.2.1.4 Gas Blowby: gas flow through the liquid line
4. PROTECTION CONCEPTS AND SAFETY ANALYSIS4. PROTECTION CONCEPTS AND SAFETY ANALYSIS
Protection Concept
1. Cause
2. Effect and Detectable Abnormal Condition
3. Primary Protection
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4.2.1.5 Under Pressure4.2.1.6 Excess Temperature4.2.1.7 Direct Ignition Sources4.2.1.8 Excess Combustible Vapors in the Firing Chambers
3. Primary Protection
4. Secondary Protection
5. Location of Safety Devices
Example: Undesirable Events - Overpressure Cause
- Inlet: input source, overflow, gas blow-by- Outlet: flow rate control failure, restrictions, blockage- Body: thermal expansion
Effect
4. PROTECTION CONCEPTS AND SAFETY ANALYSIS4. PROTECTION CONCEPTS AND SAFETY ANALYSIS
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Effect- High pressure- Hydrocarbons leak- Rupture
Protection 1: PSH - inflow, heat, fuel shut off
Protection 2: PSV
4.3 SAFETY ANALYSIS Analyzing the process and establishing design criteria for an
integrated safety system covering the entire platform process SAT: Safety Analysis Table SFC: Safety Analysis Checklist
4. PROTECTION CONCEPTS AND SAFETY ANALYSIS4. PROTECTION CONCEPTS AND SAFETY ANALYSIS
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SAFE: Safety Analysis Function Evaluation Chart Completion of the SAFE chart provides a means of verifying the
design logic of the basic safety system. Implemented into the shutdown logic (Cause and Effect Chart)
Level 1 APS Abandon platform
Level 2 ESD I Emergency shutdown (total)
Level 3 ESD II Emergency shutdown (partial)
Shutdown LogicShutdown Logic
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Level 3 ESD II Emergency shutdown (partial)
Level 4 PSD Process shutdown (total)
Level 5 PSD Process shutdown (partial)
Shut DHSVAuto Depressurisation
Timer-based disconnectionFire&gas detectionPA, ESD/PSD, radioEmergency generator/UPS
DisconnectionMain generatorNon-critical non-EXequipment
APS
ESD I
Manual
Manual
Input
Gas detection Non hazardous area
Fire&gas detectionHazardous area
Standardizing
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Start Emergency generator
equipment
Shut fuel gas supply
Activation of DHSV (fire in riser/ well area)Riser ESDVDepressurisation
ESD II
PSD
Manual
Low pressurehydraulic system
Low pressure Instrument air
High lev flare k.o drum
Tube rupture in cooler
Hazardous area
Recommended Safety DevicesRecommended Safety DevicesA.1 Wellheads and Flow Lines
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UndesirableEvent
Cause Detectable Abnormal Condition at Component
Overpressure Blocked or restricted lineDownstream choke pluggedHydrate plugUpstream flow control failureChanging well conditions
High pressure
A.1 Wellheads and Flow Lines
Safety Analysis Table (SAT)Safety Analysis Table (SAT)
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Changing well conditionsClosed outlet valve
Leak DeteriorationErosionCorrosionImpact damageVibration
Low pressure
a. High Pressure Sensor (PSH)1. PSH installed.2. Flow line segment has a maximum allowable working pressure greater than maximum
shut in pressure and is protected by a PSH on a downstream flow line segment.
b. Low Pressure Sensor (PSL)1. PSL installed.2. Flow line segment is between the well and the first choking device and is less than 10
feet(3m) in length or in the case of an underwater installation, reasonably close to that
Safety Analysis Checklist (SAC)Safety Analysis Checklist (SAC)A.1 Wellheads and Flow Lines
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distance.
c. Pressure Safety Valve (PSV)1. PSV installed.2. . . .
d. Flow Safety Valve (FSV)1. FSV installed.2. . . ..
Wellheads and Flow lines Wellhead Injection line Header Pressure vessel Atmospheric vessel Fired and Exhaust heated component
More Examples in Appendix AMore Examples in Appendix A
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Fired and Exhaust heated component Pump Compressor Pipeline Heat exchanger(Shell-Tube)
Check the examples before drawing your P&ID
Safety Analysis Function Evaluation Chart (SAFE)Safety Analysis Function Evaluation Chart (SAFE)
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Cause
Effect
Cause and Effect ChartCause and Effect Chart
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