西南石油大学学报(自然科学版) ›› 2008, Vol. 29 ›› Issue (4): 148-150.DOI: 10.3863/j.issn.1000-

• 石油与天然气工程 • Previous Articles     Next Articles

THE NUMERICAL SIMULATION OF THE TWO PHASES NONEQUILIBRIUM THERMODYNAMIC PROCESS IN PVT CELL

LIANG Ping1 TIAN Yuan1 REN Dong-xing2 YUE Cong-hai3 TANG Ke4

  

  1. 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
  • Received:1900-01-01 Revised:1900-01-01 Online:2008-08-20 Published:2008-08-20

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.

Key words: two phases, nonequilibrium process, numerical simulation, PVT cell, separation of variables 

CLC Number: