期刊文献+

酸性气藏气体偏差系数计算模型 被引量:28

A CALCULATING MODEL FOR GAS DEVIATION COEFFICIENT OF SOUR GAS RESERVOIRS
下载PDF
导出
摘要 应用传统经典状态方程计算酸性气藏天然气混合物物性参数会带来较大偏差,以文献[12]提供的实验室测试数据为基础,采用未校正的DPR模型、HY模型、DAK模型、Sarem模型和HTP模型,以及GXQ校正法和WA校正法,计算了酸性气藏气体偏差系数,并与实验测试值进行对比,评价出酸性气藏气体偏差系数计算模型的适应性。研究结果表明:①酸性气体的偏差系数校正计算模型由于考虑了酸性组分对混合物临界压力和温度的影响,其计算精度普遍高于未校正计算模型;②GXQ校正法是在高压气体混合物规则基础建立的,其计算误差高于WA校正法;③DPR模型和DAK模型结合WA校正方法计算低压酸性混合气体偏差系数较为准确,其次是HY模型,而采用Beggs&Brill模型、Sarem模型和HTP模型误差较大,不适于计算酸性气体的偏差系数。 The application of traditional classical equation of state to calculate the physical property parameters of gas mixture in sour gas reservoir will bring out relatively great deviation.Therefore,taking the laboratory test data provided by ADEL M.Elsharkawy(see ADEL M Elsharkawy,Predicting the properties of sour gases and condensates:Equations of state and empirical correlations'.SPE 74369.prented at the 2002 SPE international petroleum conference and exhibition held in Villaherrmosa,Mexico,2002:10-12)as the foundation,using the uncorrected DPR model,HY model,DAK model,Sarem model and HTP model,as well as the GXQ correction method and the WA correction method,the gas deviation coefficient of sour gas reservoirs has been calculated and compared with experimental test value,and then the adaptability of the calculating model for gas deviation coefficient of sour gas reservoirs has been evaluated.Results show that:①with the consideration of the influence to critical pressure and temperature of the mixture caused by sour components,the calculating result has a higher calculation accuracy than the uncorrected ones;②compared with the WA correction method,the GXQ correction method will result in more errors based on high-pressure gas mixture rules;③using the DPR model,the DAK model,combined with the WA correction method,to calculate low pressure sour mixture deviation factor will produce relatively accurate results,and the HY model comes next.However,the models of Beggs & Brill,Sarem and HTP will cause relatively great errors,which are not suitable for calculating the coefficient deviation of sour gas.
出处 《天然气工业》 EI CAS CSCD 北大核心 2008年第4期89-92,共4页 Natural Gas Industry
基金 国家自然科学基金项目(编号:50774062) CNPC石油科技中青年创新基金(编号:06E1016)的资助
关键词 气藏 酸性气体 状态方程 偏差系数 数学模型 校正 gas reservoir,sour gas,state equation,deviation factor,mathematical model,correction
  • 相关文献

参考文献13

二级参考文献21

  • 1陈元千.确定酸性天然气偏差系数的方法[J].试采技术,1989,10(2):1-5. 被引量:9
  • 2韩洪升.天然气压缩因子计算方法的评价[J].油气储运,1994,13(1):13-18. 被引量:21
  • 3刘志军,李桂芹.用SHBWR方程计算石油气的压缩因子[J].压缩机技术,1996(1):21-23. 被引量:4
  • 4李仕伦.天然气工程[M].北京:石油工业出版社,2000..
  • 5[1]Standing M B and Katz D L. Density of natural gases [J]. Transaction of AIME, 1942,146:140-149.
  • 6[2]Dranchuk P M and Quon D. A general solution of the equation describing steady state turbulent compressible flow in circular conduits [J]. Journal of Canada Petroleum Technology, 1965, (Summer):60-65.
  • 7[3]Papay J. A Termelestechnologial Perameterek Valtozaisa a Gazeleplemuvelese Soran [M]. OGIL Mus Tud Kuzl, Budapest, 1968.
  • 8[4]Brill J P and Beggs H D. Two Phase Flow in Pipes [M]. Intercompressibility Course, University of Tulsa, 1974.
  • 9[5]Gopal V N. Gas Z-factor equation developed for computer [J]. Oil & Gas Journal, 1977, 75(August): 8-13.
  • 10[6]Redlich O and Kwong J NS. The thermodynamics of solutions-V. An equation of station fugacity of gaseous solutions [J ]. Chemistry Review, 1949, 44:233 - 244.

共引文献92

同被引文献219

引证文献28

二级引证文献105

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部