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油气水分离设备仿真与应用 被引量:2

Simulation and Application of Oil-gas-water Separator
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摘要 为建立海上油田集输系统仿真流程,以三相分离器为例对油气水分离设备进行仿真。在已知分离器结构尺寸、处理液性质、处理量以及操作条件的基础上,将理论计算法与人工神经网络法相结合,预测三相分离器出口原油含水率;建立油、气、水流量及出口温度数学模型,并利用Matlab与C++Builder语言开发仿真软件。由软件模拟仿真可得到油、气、水流量,出口原油含水率、温度及能流图。经现场应用测试,仿真结果满足工程允许误差要求。利用该仿真软件可快速、高效的得到不同工况下设备出口运行参数及能耗情况,进而优选运行工况,实现集输系统节能降耗,具有一定工程应用价值。 To establish the offshore oil field gathering and transportation system simulation flow,the simulation of separation equipment was given by taking the three-phase separator as an example.Based on the structure dimensions,the properties of liquids,the capacity and the operating conditions,the water content was obtained by combining theory calculation with artificial neural network method.The mathematical model of temperature and the flow rate of gas,water and oil were put forward.The simulation software was presented which be programmed using MATLAB and C + + Builder.The simulation results include the water content,the temperature,the energy flow chart and the flow rate of gas,water and oil.According to field tests,the error of result data meets the demand.Applying the model in the simulation of system,the process parameters and the energy consumption can be found rapidly and efficiently.The energy consumption can be reduced by optimizing the process parameter.Therefore,this study has certain engineering application value.
出处 《流体机械》 CSCD 北大核心 2011年第10期45-49,共5页 Fluid Machinery
基金 "十二.五"国家科技重大专项:海上油田生产运行管理智能决策支持技术研究(2011ZX05024-002-009)
关键词 海上油田集输系统 三相分离器 数学模型 仿真 offshore oil field gathering and transportation system three-phase separator mathematical model simulation
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  • 1Maston L Powers. Analysis of Gravity Separation in Free-water Knockouts[ J]. SPE18205,1990:52-58.
  • 2Rehm S J, ShaughnessyIII R J, Natco C-E. Enhanced Oil-Water Separation-The Performax Coalescer [ J ]. SPE11562,1983 : 165-170.
  • 3杨晓帆,陈廷槐.人工神经网络固有的优点和缺点[J].计算机科学,1994,21(2):23-26. 被引量:72
  • 4Mahmoud M. E1-Halwagi, Srinivas B K, Russell F. Dunn. Synthesis of Optimal Heat-Induced Separation Networks[ J]. Chemical Engineering Science, 1995, 50(1) : 81-97.

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