Modelling of phase equilibria in CH4-C2H6-C3H8-nC4H10-NaCl-H2O systems

被引:14
作者
Li, Jun [1 ]
Zhang, Zhigang [2 ]
Luo, Xiaorong [3 ]
Li, Xiaochun [1 ]
机构
[1] Chinese Acad Sci, Inst Rock & Soil Mech, State Key Lab Geomech & Geotech Engn, Wuhan 430071, Peoples R China
[2] Chinese Acad Sci, Inst Geol & Geophys, Key Lab Earth & Planetary Phys, Beijing 100029, Peoples R China
[3] Chinese Acad Sci, Inst Geol & Geophys, Key Lab Petr Resource Res, Beijing 100029, Peoples R China
基金
中国国家自然科学基金;
关键词
EQUATION-OF-STATE; VAPOR-LIQUID-EQUILIBRIA; ASSOCIATING FLUID THEORY; CALCULATING CO2 SOLUBILITY; AQUEOUS NACL SOLUTIONS; METHANE PLUS WATER; DEW-POINT GAS; PURE WATER; THERMODYNAMIC MODEL; SALT-SOLUTIONS;
D O I
10.1016/j.apgeochem.2015.02.006
中图分类号
P3 [地球物理学]; P59 [地球化学];
学科分类号
0708 ; 070902 ;
摘要
A thermodynamic model is presented for the mutual solubility of CH4-C2H6-C3H8-nC(4)H(10)-brine systems up to high temperature, pressure and salinity. The Peng-Robinson model is used for non-aqueous phase fugacity calculations, and the Pitzer model is used for aqueous phase activity calculations. The model can accurately reproduce the experimental solubilities of CH4, C2H6, C3H8 and nC(4)H(10) in water or NaCl solutions and H2O solubility in the non-aqueous phase. The experimental data of mutual solubility for the CH4-brine subsystem are sufficient for temperatures exceeding 250 degrees C, pressures exceeding 1000 bar and NaCl molalities greater than 6 molal. Compared to the CH4-brine system, the mutual solubility data of C2H6-brine, C3H8-brine and nC(4)H(10)-brine are not sufficient. Based on the comparison with the experimental data of H2O solubility in C2H6-, C3H8-or nC(4)H(10)-rich phases, the model has an excellent capability for the prediction of H2O solubility in hydrocarbon-rich phases, as these experimental data were not used in the modelling. Predictions of hydrocarbon solubility (at temperatures up to 200 degrees C, pressures up to 1000 bar and NaCl molalities greater than 6 molal) were made for the C2H6-brine, C3H8-brine and nC(4)H(10)-brine systems. The predictions suggest that increasing pressure generally increases the hydrocarbon solubility in water or brine, especially in the lower-pressure region. Increasing temperature usually decreases the hydrocarbon solubility at lower temperatures but increases the hydrocarbon solubility at higher temperatures. Increasing water salinity dramatically decreases the hydrocarbon solubility. The experimental solubility data for hydrocarbon mixtures in water are not sufficient or systematic. Comparisons were made between the experimental data and the results of the model calculations. Most of the experimental data can be well predicted by this model with slightly higher discrepancies. More systematic experimental studies are needed to improve the model. (C) 2015 Elsevier Ltd. All rights reserved.
引用
收藏
页码:23 / 36
页数:14
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