lifecycle ots: using simulation models from engineering
TRANSCRIPT
© Inprocess
Lifecycle OTS: Using Simulation Models from Engineering Design to Plant Operations
Leonardo Carpio
✓ OTS Lifecycle dynamic modelling
1. Process Design & Control Validation
2. Integration and Control narrative
verification
3. Procedures Verification & Early Senior
CRO´s Training
4. ICSS Database Checkout
5. Operator Training System
6. OTS Support operations
Page 2
Agenda
© Inprocess 3
What could go wrong in an FPSO?
Picture © bp p.l.c.
PROCESS DESIGN
• Recycle valve sizing• Hot Gas Bypass req.• Compressor driver
constraint• GT constraint• Set points consistency
among process areas• Trip value settings
OPERATINGPROCEDURES
• Transition conditions• Not feasible in real• Excessive flaring• Not safe Emergency
procedures
CONTROL NARRATIVES
• Modules interaction• Wrong parameters for
loops, alarms, timing• SIS definition
ICSS CODE• Wrong Tags, Units,
Ranges, modules…• Errors in sequences• Wrong loops tuning• Alarms overload• SIS implementation
HUMAN ERROR
• Insufficient quality training• Unseen abnormalities• Lack of monitoring,
diagnose and operation support tools
SHORT TERM IMPACTCauses spurious trips, equipment damages and delays in start-up in the
order of 10-20 days
LONG TERM IMPACTCompromise the production
along the whole FPSO life
LONG TERM IMPACTDecrease the %uptime along the
whole FPSO life
Basic Engineering (FEED)
Detailed Engineering
(EPC)
Commissioning & Start-up
Operations & Maintenance
Simulation Lifecycle and Digitalization
Inherently Safer Design
Operational Excellence
© by inprocess 4
Simulation and Process Lifecycle flowchart
Dynamic Model built
Additional equipment,
ICSS/UCP Control
Narrative, CEMs, interlocks
Model
Adjust
Engineering Study
ICSS HMI Emulated with
Inprocess Instructor Station
Process Trainers
ICSS HMI
displays
ICSS
Database
Control Logic
ICSS Checkout
Model
Connectivity
Instructor Station, Training Scenarios,
Additional ICSS Consoles
Direct-Connect OTS
Model from
engineering Studies
Plant Data
Engineering Data
Analysis of
critical units
Control Narrative and
Procedure Verification
Early CRO Training
-Knowledge
Transfer
ICSS Virtual
Commissioning
OTS ready
Training
Support
Operations with
Digital Twin
OTS
Maintenance
Blue boxes indicate the areas included in thescope of the Dynamic Simulation Study
Page 5
Stg 1: Process Design & Control Validation
GAS INJECTION COMPRESSIONDEHYDRATION & TEG
REGENERATION
HP FLASH GAS COMPRESSION
HHPSEPARATION
HPSEPARATION
PRODUCED WATER & SEA WATER
DSS→
Main focus is on the critical units (compressors or areas where significant control interactions are foreseen) in order to verify the operability and safety of the plant. Any early stage finding can be handled easily, to achieve: the best solution with minimum design modifications at minimum costs.
Blue boxes indicate the areas included in thescope of the Dynamic Simulation Study
Page 6
Stg 2: OTS model scope
GAS INJECTION COMPRESSIONDEHYDRATION & TEG
REGENERATION
HP FLASH GAS COMPRESSION
NAG SLUG CATCHER
NAG SEPARATION
MP FLASH GAS COMPRESSION
LP FLASH GAS COMPRESSION
MP & LP SEPARATIONCRUDE TRANSFER
HHPSEPARATION
HPSEPARATION
PRODUCED WATER & SEA WATER
DSS→
Green boxes indicate the areas added tothe HYSYS Dynamic model for training
Training→ +
HEATING COOLING
MEDIA
MEG REG.SYSTEM
HP & LP FLARE
FG SYSTEM
The Dynamic model from the DSS will be expanded with new units, the latest control logic implemented and the UCP sequences from the compressor packages.
The model will be used to verify the Control Narrative Specifications:
• Control interactions with UCP
• Normal operation
• During non-design conditions
• During specific procedures
• Understanding the limits of the system
• Alarm & Trip limits
• Controller pre-setting
• Verify equipment protection
Page 7
Stg 2 – Operating Procedures (Comprehensive Control Narrative Verification).
Flare Controller Set Points Instrument Ranges &Trip Settings
Calculations & Override Controllers
Selectors & SP strategies
Loops Interactions
Page 8
Phase 3A: Procedures Verification
Early verification of Operating Procedures with timing and transitions conditions
Scope:
- Individual Units
- Overall Start-up process
Combining Expertise’s:
Mix of experienced Engineers / Operators know-how with realistic response of Process Trainer
Operating Procedures are drafted and validated in a closeinteraction between experienced operators and simulation experts
Page 9
Phase 3B: Process Trainer - Early CRO´s Training
Using the Inprocess Instructor Station softwarewith the Process model as simulation engine,an HMI layer is added on top of the Processmodel using the same displays of the ICSScontrol room.
Early CRO´s and Supervisor Training
Knowledge Transfer
• Control Interactions and Issues
• Limits of the system
Training Scope
• ICSS displays familiarization andoperability verification
• Start-up / Shutdown Procedures
• Trip scenarios
• Disturbances and Malfunctions
© by inprocess 10
database checkout – standalone validation - benefitsBenefits of the ICSS Checkout
• Early Database checkout: DCS modules don’t need to befinalised to start its validation.
• Parallel Debugging: Pending on the available licenses(Process model+ DCS), the different modules can be testedin parallel.
• IO signals and transmitters verification: Ranges, Units,Alarm & Trip settings, missing or wrong connections.
• Controllers & Logic:
• Implementation according to the latest controlphilosophy
• Controllability and operability
• SP, PV, OP Ranges and additional functionalities
Phase 4: ICSS Checkout
Dynamic Model
To transmitter
To Controller
Input
IO Block
Controller Output
IO Block
Output
DCS Controller validation cycle
• Sequences ( Compressor, PLC’s, Backwash systems, etc)
• Implemented according to the latest control narrativeand Functional Descriptions
• Sequence/ logic verification
• Transient dynamic verification
• Cause and Effect Matrix: Verification of the DCSimplementation and evaluation of its transient dynamics
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OTS Deployment
Process Plant
Control System
Interface
Process model Dynamics
Process model Dynamics
DCS Emulation
Emulated Controls
Direct-Connect Fully Emulated
Panel Operator Instructor Station & Field Devices
Instructor Station & Field Devices
Emulated Panel Operator
Page 12
Phase 6: OTS Support Operations
Following the lifecycle dynamic modeling approach provides increased added value to the project itself. As it is based on a highly reliablefirst principle model linked with the actual ICSS.
A direct connect OTS based on a first principlemodel allows:
• The evaluation of the operability of the plantunder non design conditions (e.g. Start Upoperations).
• Analysis of alternative control strategies.
• The evaluation of potential plant optimizations(i.e. Debottlenecking studies).
• The evaluation of alternative operating modes.
• The determination of potential limitations inprocess or utility areas.
Process model Dynamics
Speeds-Up procedures (NSD, SU, etc.)
Start-Up date reduced
Flare minimized
Commissioning time reduced
Trips reduced
Safety increased
Plant performance improved
Controllability and operability improvedPHASE 1
Process design and unit control validation
PHASE 2
Integration and control narrative verification
PHASE 3
Procedure verification and process trainer
PHASE 4
ICSS Integration and Checkout
PHASE 5
Operator training system
PHASE 6
OTS Support Operations
Operators: gain confidence and awareness of the plants behavior and interactions
Detects missing equipment or unreachable interlock conditions.Operators have more availability
Any early stage finding can be handled easily, to achieve:• The best solution• with minimum design modifications• At minimum costs.
Lifecycle Dynamic Modeling: Benefits
Final product:Is a valuable tool which can be used for training purposes and as a basis for control logic modifications, optimizations, control tuning, support operations in unforeseen conditions or configurations.
Each phase of the lifecycle approach addresses specific targets , which are aligned with the needs of the project. The model is developed once and refined in successive refined as more detailed information is available.