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PVT筒中气液两相非平衡过程的数值模拟
引用本文:梁平,田园,任东兴,岳从海,唐柯.PVT筒中气液两相非平衡过程的数值模拟[J].西南石油大学学报(社会科学版),2010,29(4):148-150.
作者姓名:梁平  田园  任东兴  岳从海  唐柯
作者单位:1.重庆科技学院石油工程学院,重庆 大坪 400042; 2.塔里木油田开发事业部,新疆 库尔勒 841000;3.四川石油管理局川东开发公司,重庆 江北 400020; 4.中国航油重庆公司,重庆 渝北 410020
摘    要:目前国内外多采用平衡后各组分逸度系数相等的平衡判据来描述两相中各个组分的分配情况,但该法无法进行两相由非平衡初始状态达到平衡状态这一非平衡热力学过程的研究。针对这一问题,提出了引入扩散方程来描述液相和气相各个组分由接触到稳定过程的方法,建立了描述两相非平衡态扩散过程的数学模型,提出了分阶段求解模型的求解算法,并运用该法对PVT筒中气液两相系统由接触到稳定过程的状态进行了分析,得出系统全程压力变化规律及平衡状态下随高度变化的甲烷浓度分布规律。计算结果与实验数据对比验证了该方法的可行性,从而为非平衡态相变问题的分析提供了新的思路。

关 键 词:两相    非平衡过程    数值模拟    PVT筒    分离变量法

THE NUMERICAL SIMULATION OF THE TWO PHASES NONEQUILIBRIUM THERMODYNAMIC PROCESS IN PVT CELL
LIANG Ping,TIAN Yuan,REN Dong-xing,YUE Cong-hai,TANG Ke.THE NUMERICAL SIMULATION OF THE TWO PHASES NONEQUILIBRIUM THERMODYNAMIC PROCESS IN PVT CELL[J].Journal of Southwest Petroleum University(Social Sciences Edition),2010,29(4):148-150.
Authors:LIANG Ping  TIAN Yuan  REN Dong-xing  YUE Cong-hai  TANG Ke
Institution:1.Petroleum Engineering Institute,Chongqing University of Science and Technology,Daping Chongqing 400042,China;2.Development Department,Tarim Oilfield Company,CNPC,Korla Xinjiang 841000,China;3.CNPC Sichuan Pertroleum East Sichuan Development Complany,Jiangbei Chongqing 400020,China;4.CNAF Chongqing Branch,Yubei Chongqing 410020,China
Abstract:The currently used methods for determining the thermodynamic equilibrium of the mixed two phases substances is to judge the equality of the coefficient of each component in two phases,and with this analysis,each component mole fraction can be got at the equilibrium state.But this method can not be used in analyzing the process from the initial two phases nonequilibrium state to the final equilibrium state.To address this issue,diffusion equation to describe various gas and liquid components from exposure to the stabilization process is introduced in this paper,a mathematical model to describe the two phases nonequilibrium diffusion process established.By using the method,a gasliquid two phases system that changes from contact to steady status in the PVTcanister is analyzed.The whole process pressure change rule of the system is obtained.The methane concentration distributing rule that changes with altitude in the balance state got,too.The results compared with the experimental data proved the feasibility of the method,thus the nonequilibrium phase transition analysis of the issue gives a new train of thought.
Keywords:two phases                                                                                                                        nonequilibrium process                                                                                                                        numerical simulation                                                                                                                        PVT cell                                                                                                                        separation of variables 
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