CO2 solubility in formation water under sequestration conditions

被引:38
作者
Ahmadi, Pezhman [1 ]
Chapoy, Antonin [1 ,2 ]
机构
[1] Heriot Watt Univ, Inst Petr Engn, Hydrates Flow Assurance & Phase Equilibria Res Gr, Edinburgh EH14 4AS, Midlothian, Scotland
[2] Mines ParisTech, CTP Ctr Thermodynam Proc, 35 Rue St Honore, F-77305 Fontainebleau, France
关键词
CO2; solubility; Water; NaCI; Experimental measurement; Thermodynamic modelling; CARBON-DIOXIDE SOLUBILITY; AQUEOUS NACL SOLUTIONS; PHASE-EQUILIBRIA; PLUS WATER; LIQUID-EQUILIBRIA; HIGH-TEMPERATURES; SODIUM-CHLORIDE; GAS SOLUBILITY; PURE WATER; 423.15; K;
D O I
10.1016/j.fluid.2018.02.002
中图分类号
O414.1 [热力学];
学科分类号
摘要
A high pressure experimental setup was used to measure the solubility of CO2 in an aqueous solution of different salts (salinity: similar to 80000 ppm) at temperatures from (300-424) K and pressures up to 41 MPa. To ensure the validity of the experimental results and procedures, CO2 solubilities in deionised water were measured at the same pressure and temperature conditions. For both cases, experimental results were compared against predictions of the simplified cubic plus association equation of state (sCPA-EoS) [1] and Duan model [2]. Furthermore, the measured solubilities in deionised water were compared with literature experimental data. The average absolute deviation (%AAD) of all the measured solubilities in the mixed salts aqueous solution in comparison with predictions of the sCPA-EoS and Duan model were found to be 6.88% and 4.04%, respectively. A similar comparison was also performed for the measured CO2 solubilities in deionised water. The average absolute deviation between experimental results and predictions of the sCPA-EoS and Duan model were calculated to be 7.74% and 4.19%, respectively. The percentage average expanded uncertainty (with 95% level of confidence, k = 2) for measurements conducted in deionised water and mixed salt aqueous solution were found to be 1.20% and 1.57%, respectively. (C) 2018 Elsevier B.V. All rights reserved.
引用
收藏
页码:80 / 90
页数:11
相关论文
共 66 条
[1]   Solubility of carbon dioxide in water under incipient clathrate formation conditions [J].
Anderson, GK .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2002, 47 (02) :219-222
[2]   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
[3]   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
[4]  
Bartholomk E., 1956, CHEM-ING-TECH, V289, P706
[5]   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
[6]   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
[7]   Clathrate hydrate equilibria in mixed monoethylene glycol and electrolyte aqueous solutions [J].
Chapoy, Antonin ;
Mazloum, Saeid ;
Burgass, Rod ;
Haghighi, Hooman ;
Tohidi, Bahman .
JOURNAL OF CHEMICAL THERMODYNAMICS, 2012, 48 :7-12
[8]  
Chladni E. F. F., 1787, ENTDECKUNGEN FIBER T
[9]   Solubility of hydrocarbons and CO2 mixtures in water under high pressure [J].
Dhima, A ;
de Hemptinne, JC ;
Jose, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (08) :3144-3161
[10]  
Drummond, 1981, BOILING MIXING HYDRO