Dynamic Integrated Model Optimizes Fluid System Startup

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Solution Overview

Problem

The startup time of fluid production and/or injection systems, particularly in complex offshore oil and gas fields, is excessively long due to inefficiencies and unproductive wait times, leading to operational inefficiencies and costly production stoppages.

Innovation Solution

A dynamic integrated model is used to assess and adjust the startup time schedule by integrating a reservoir model with a transient network model, incorporating equipment, field design, and control systems to simulate and optimize startup procedures, identifying potential inefficiencies and providing mitigation strategies based on changing reservoir productivity and facility constraints.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Reliability

If traditional startup procedures are used for complex offshore production systems, then system reliability is maintained through careful sequential operations, but startup time becomes excessively long (5-20+ hours per well)

Engineering Contradiction:
Improvesystem reliabilityVSAvoidstartup time
Core Design Contradiction:
ReliabilityVSLoss of time

Solution Approach 1:

The system performs preliminary actions by pre-calculating optimal startup sequences, pre-positioning equipment states, and preparing control parameters before actual startup begins. The dynamic integrated model predicts required adjustments in advance, allowing the system to execute pre-planned sequences that reduce actual startup time while maintaining reliability through validated procedures.

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The system transitions from static, fixed startup procedures to dynamic, adaptive sequences. The dynamic integrated model continuously adjusts startup parameters based on real-time system state, reservoir conditions, and equipment responses. This allows optimization of each startup event while maintaining safety margins, resolving the contradiction between speed and reliability.

Inventive Principle:
Principle #15Dynamics

2Productivity

If complex integrated modeling is implemented to optimize startup procedures, then startup time and operational efficiency are improved, but system complexity and computational requirements increase

Engineering Contradiction:
Improveoperational efficiencyVSAvoidmodeling system complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The system introduces a dynamic integrated model as an intermediary layer between reservoir data and production control systems. This model acts as a computational mediator that integrates multiple data sources (reservoir models, network models, equipment specifications) and translates them into optimized startup sequences. The intermediary handles the complexity internally while presenting simplified outputs to operators.

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The dynamic integrated model serves multiple functions simultaneously: it integrates diverse data sources, performs predictive simulations, optimizes startup sequences, and provides decision support. This multi-functionality consolidates what would otherwise require multiple separate systems into a single unified platform, managing complexity through consolidation rather than proliferation of components.

Inventive Principle:
Principle #6Universality (Multi-functionality)

Data Source

PatentEP3339565B1Systems and methods for assessing production and/or injection system startup
Publication Date: 2022.08.03 ONESUBSEA IP UK LTD
  • EP3339565B1 patent drawingFigure 1
  • EP3339565B1 patent drawingFigure 2~3
  • EP3339565B1 patent drawingFigure 4~5

AI summary

A method of modeling effects of operational procedures during startup of a fluid production or injection system at a field includes determining initial conditions of the field at a first time based on field measurements of the field. The method also includes simulating startups of the fluid production or injection system based on the initial conditions. The method further includes determining operational procedures for starting up the fluid production or injection system based on the simulated startups. The method also includes determining whether a startup command has been received. The method further includes sending instructions to startup the fluid production or injection system using the operational procedures when the startup command is received.