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Plantwide control of an oil production network
Computers & Chemical Engineering ( IF 3.9 ) Pub Date : 2020-02-08 , DOI: 10.1016/j.compchemeng.2020.106765
Esmaeil Jahanshahi , Dinesh Krishnamoorthy , Andrés Codas , Bjarne Foss , Sigurd Skogestad

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.



中文翻译:

全厂范围内的石油生产网络控制

在本文中,我们考虑了实时优化(RTO)和石油生产系统的控制。我们遵循系统的全厂控制程序。该过程包括两个与管道提升系统相连的气举油井,以及在顶部平台上的一个分离器。当气体注入速率低时,由于套管抬头现象,所需的稳定流态可能变得不稳定并变为团状流。因此,需要调节控制层来稳定所需的两相流态。为此,我们提出了一种使用两种压力测量值的新控制结构,其中一种压力值在井口,另一种压力值在环空。对于优化层,我们比较了非线性经济模型预测控制(EMPC),动态反馈RTO(FRTO)和自优化控制(SOC)的性能。

更新日期:2020-02-10
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