Gas solubility measurement and modeling for the nitrogen plus water system from 274.18 K to 363.02 K

被引:67
作者
Chapoy, A
Mohammadi, AH
Tohidi, B
Richon, D
机构
[1] Ecole Natl Super Mines, Ctr Energet, CENERG TEP, F-77305 Fontainebleau, France
[2] Heriot Watt Univ, Inst Petr Engn, Ctr Gas Hydrate Res, Edinburgh EH14 4AS, Midlothian, Scotland
关键词
D O I
10.1021/je049869d
中图分类号
O414.1 [热力学];
学科分类号
摘要
New experimental solubility data of N-2 in water are reported over a wide temperature range from (274.18 to 363.02) K and pressures up to 7.16 MPa. A static-analytic apparatus, taking advantage of a pneumatic capillary sampler, is used for fluid sampling. The experimental data generated in this work are compared with those reported in the open literature with good agreement. The Valderrama modification of the Patel-Teja equation of state combined with nondensity-dependent mixing rules is used for modeling the gas-liquid equilibrium. The solubility data generated in this work are used for tuning the binary interaction parameters between nitrogen and water. The model predictions are compared with independent experimental data on nitrogen solubility in water as well as water content of the gas phase. The results are in good agreement, demonstrating reliability of the technique and the thermodynamic approach used in this work.
引用
收藏
页码:1110 / 1115
页数:6
相关论文
共 34 条
[1]  
ALTHAUS K, 1999, FORTSCHR BERICHTE VD, V3, P350
[2]   PREDICTION OF VL AND VLL EQUILIBRIA OF MIXTURES CONTAINING PETROLEUM RESERVOIR FLUIDS AND METHANOL WITH A CUBIC EOS [J].
AVLONITIS, D ;
DANESH, A ;
TODD, AC .
FLUID PHASE EQUILIBRIA, 1994, 94 :181-216
[3]  
Avlonitis D., 1988, MULTIPHASE EQUILIBRI
[4]  
AVLONITIS D, 1992, THESIS HERIOTWATT U
[5]   The concentration of water vapor in compressed hydrogen, nitrogen and a mixture of these gases in the presence of condensed water [J].
Bartlett, EP .
JOURNAL OF THE AMERICAN CHEMICAL SOCIETY, 1927, 49 :65-78
[6]  
BUKACEK RF, 1955, RES B, V8
[7]   Solubility measurement and modeling of water in the gas phase of the methane/water binary system at temperatures from 283.08 to 318.12 K and pressures up to 34.5 MPa [J].
Chapoy, A ;
Coquelet, C ;
Richon, D .
FLUID PHASE EQUILIBRIA, 2003, 214 (01) :101-117
[8]   Measurement of the water solubility in the gas phase of the ethane plus water binary system near hydrate forming conditions [J].
Chapoy, A ;
Coquelet, C ;
Richon, D .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2003, 48 (04) :957-966
[9]  
CHAPOY A, 2004, IN PRESS FLUID PHASE
[10]  
Danesh A., 1998, PVT PHASE BEHAV PETR