Plantwide control of an oil production network

被引:10
作者
Jahanshahi, Esmaeil [1 ]
Krishnamoorthy, Dinesh [1 ]
Codas, Andres [2 ]
Foss, Bjarne [2 ]
Skogestad, Sigurd [1 ]
机构
[1] Norwegian Univ Sci & Technol NTNU, Dept Chem Engn, NO-7491 Trondheim, Norway
[2] Norwegian Univ Sci & Technol NTNU, Dept Engn Cybernet, NO-7034 Trondheim, Norway
关键词
Oil production; Plant-wide control; Self-optimizing control; Unstable systems; REAL-TIME OPTIMIZATION; MULTIPHASE FLOW; DESIGN; STABILIZATION; PRESSURE; FIELDS;
D O I
10.1016/j.compchemeng.2020.106765
中图分类号
TP39 [计算机的应用];
学科分类号
081203 ; 0835 ;
摘要
In this paper, we consider Real-Time Optimization (RTO) and control of an oil production system. We follow a systematic plantwide control procedure. The process consists of two gas-lift oil wells connected to a pipeline-riser system, and a separator at the topside platform. When the gas injection rates are low, the desired steady flow regime may become unstable and change to slug flow due to the casing-heading phenomenon. Therefore, a regulatory control layer is required to stabilize the desired two-phase flow regime. To this end, we propose a new control structure using two pressure measurements, one at the well-head and one at the annulus. For the optimization layer, we compare the performance of nonlinear Economic Model Predictive Control (EMPC), dynamic Feedback-RTO (FRTO) and Self-Optimizing Control (SOC). Based on dynamic simulations using the realistic OLGA simulator, we find that SOC is the most practical approach. (C) 2020 The Authors. Published by Elsevier Ltd.
引用
收藏
页数:14
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