Experimental Measurement of CO2 Solubility in Aqueous NaCl Solution at Temperature from 323.15 to 423.15 K and Pressure of up to 20 MPa

被引:56
作者
Messabeb, Hamdi [1 ]
Contamine, Francois [1 ]
Cezac, Pierre [1 ]
Serin, Jean Paul [1 ]
Gaucher, Eric C. [2 ]
机构
[1] Univ Pau & Pays Adour, Inst Carnot ISIFoR, Lab Therm Energet & Proc LaTEP, Rue Jules Ferry,BP 7511, Pau, France
[2] CSTJF, TOTAL, Ave Larribau, F-64018 Pau, France
关键词
CARBON-DIOXIDE-WATER; PHASE-EQUILIBRIA; PLUS WATER; MUTUAL SOLUBILITIES; LIQUID-EQUILIBRIUM; SODIUM-CHLORIDE; GAS SOLUBILITY; ACETIC-ACID; MIXTURES; BEHAVIOR;
D O I
10.1021/acs.jced.6b00505
中图分类号
O414.1 [热力学];
学科分类号
摘要
Interest in CO2 solubility in brine at high pressure and high temperature has grown in the last few decades. Solubility data are especially important in petroleum geology, carbon capture and geological storage, and geothermal, reservoir engineering. Nevertheless, for,lithe CO2 + NaCl + H2O system there are fewer solubility data available in literature, particularly at high salt molality. A high-pressure experimental device was designed to perform measurements for carbon dioxide solubility in a complex aqueous solution. The apparatus was first validated from. experiment on The CO2-pure water system at 323.15 K by comparison with literature data. Thirty-six new experimental solubility data point were obtained in the pressure range between 5 and 20 MPa at three temperatures (323.15, 373.15, and 423.15 K) and at three molalities of NaCl (1, 3, and 6 moles per kilogram of water) Solubility measurements were obtained by potentiometric titration after sample trapping in a sodium hydroxide solution. The experimental solubility data generated in this work were consistent with literature data, and four original isotherms were obtained at high salinity.
引用
收藏
页码:3573 / 3584
页数:12
相关论文
共 61 条
[1]   High-pressure (vapor plus liquid) equilibrium in binary mixtures of (carbon dioxide plus water or acetic acid) at temperatures from 313 to 353 K [J].
Bamberger, A ;
Sieder, G ;
Maurer, G .
JOURNAL OF SUPERCRITICAL FLUIDS, 2000, 17 (02) :97-110
[2]   Solubility of CO2 in aqueous solutions of NaCl at (30 to 60) °C and (10 to 20) MPa [J].
Bando, S ;
Takemura, F ;
Nishio, M ;
Hihara, E ;
Akai, M .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2003, 48 (03) :576-579
[3]  
BENSON S, 2005, CAMBRIDGE UP UK, V5, P431
[4]   The influence of Na2SO4 on the CO2 solubility in water at high pressure [J].
Bermejo, MD ;
Martín, A ;
Florusse, LJ ;
Peters, CJ ;
Cocero, MJ .
FLUID PHASE EQUILIBRIA, 2005, 238 (02) :220-228
[5]   TERNARY PHASE-EQUILIBRIA FOR ACETIC ACID-WATER MIXTURES WITH SUPERCRITICAL CARBON-DIOXIDE [J].
BRIONES, JA ;
MULLINS, JC ;
THIES, MC ;
KIM, BU .
FLUID PHASE EQUILIBRIA, 1987, 36 :235-246
[6]   Carbon dioxide solubility in aqueous solutions of NaCl: Measurements and modeling with electrolyte equations of state [J].
Carvalho, Pedro J. ;
Pereira, Luis M. C. ;
Goncalves, Neusa P. F. ;
Queimada, Antonio J. ;
Coutinho, Joao A. P. .
FLUID PHASE EQUILIBRIA, 2015, 388 :100-106
[7]   Measurement and modeling of gas solubility and literature review of the properties for the carbon dioxide-water system [J].
Chapoy, A ;
Mohammadi, AH ;
Chareton, A ;
Tohidi, B ;
Richon, D .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (07) :1794-1802
[8]  
Chapoy A, 2005, THESIS
[9]  
Cramer S. D., 1982, REP INVEST US BUR MI, V8706, P1
[10]   Solubility of CO2 in water from -1.5 to 100°C and from 0.1 to 100 MPa:: evaluation of literature data and thermodynamic modelling [J].
Diamond, LW ;
Akinfiev, NN .
FLUID PHASE EQUILIBRIA, 2003, 208 (1-2) :265-290