Measurement and Correlation of Solubility Data for CO2 in NaHCO3 Aqueous Solution

被引:36
作者
Han, Xiaoying [1 ,2 ]
Yu, Zhihui [1 ]
Qu, Jingkui [1 ]
Qi, Tao [1 ]
Guo, Wei [3 ]
Zhang, Guoqing [4 ]
机构
[1] Chinese Acad Sci, Key Lab Green Proc & Engn, Inst Proc Engn, Beijing 100190, Peoples R China
[2] Chinese Acad Sci, Grad Univ, Beijing 100049, Peoples R China
[3] Beijing Univ Chem Technol, Coll Chem Engn, Beijing 100029, Peoples R China
[4] Sichuan Anxian YinHe Construct & Chem Grp Co Ltd, Chengtu 0816, Sichuan, Peoples R China
关键词
CARBON-DIOXIDE; MOLECULAR THERMODYNAMICS; OSMOTIC COEFFICIENTS; SODIUM-CHLORIDE; HENRY CONSTANTS; IMPROVED MODEL; PURE WATER; PREDICTION; ELECTROLYTES; TEMPERATURES;
D O I
10.1021/je1011168
中图分类号
O414.1 [热力学];
学科分类号
摘要
To investigate the influence of NaHCO3 on the CO2, absorption in aqueous solution, the solubility of CO2 in NaHCO3 aqueous solutions [(0, 0.05, 0.1, 0.5, and 1.0) mol.kg(-1)] was measured in the temperature range from (313 to 333) K with pressure range from (0.3 to 2.0) MPa by employing a new designed batch apparatus. The results showed that the solubility data for CO2 in NaHCO3 aqueous solutions agreed well with Henry's law, and the Henry constant appeared to be a function of temperature and the concentration of NaHCO3. Two thermodynamic models were proposed for correlating the experimental data, that is, the modified Setschenow and Peng-Robinson (PR)-Duan equations. It was proved that the models fitted well in with the experimental data, and the average relative deviations were (4.06 and 3.90) %, respectively. In addition, the Henry constant in pure water can be basically predicted at a certain temperature range. The influence of NaHCO3 on the solubility of CO2 is interpreted by "salting-out effect" which is usual for the salt-containing solutions.
引用
收藏
页码:1213 / 1219
页数:7
相关论文
共 56 条
[11]   An improved model calculating CO2 solubility in pure water and aqueous NaCl solutions from 273 to 533 K and from 0 to 2000 bar [J].
Duan, ZH ;
Sun, R .
CHEMICAL GEOLOGY, 2003, 193 (3-4) :257-271
[12]   AN EQUATION OF STATE FOR THE CH4-CO2-H2O SYSTEM .1. PURE SYSTEMS FROM 0-DEGREES-C TO 1000-DEGREES-C AND 0 TO 8000 BAR [J].
DUAN, ZH ;
MOLLER, N ;
WEARE, JH .
GEOCHIMICA ET COSMOCHIMICA ACTA, 1992, 56 (07) :2605-2617
[13]   Accurate thermodynamic model for the calculation of H2S solubility in pure water and brines [J].
Duan, Zhenhao ;
Sun, Rui ;
Liu, Rong ;
Zhu, Chen .
ENERGY & FUELS, 2007, 21 (04) :2056-2065
[14]  
FERRENTINOA G, 2009, J SUPERCRIT FLUID, V1, P1
[15]   Solubilities of methane, nitrogen, carbon dioxide, and a natural gas mixture in aqueous sodium bicarbonate solutions under high pressure and elevated temperature [J].
Gao, J ;
Zheng, DQ ;
Guo, TM .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1997, 42 (01) :69-73
[16]  
Gehrig M., 1980, PhD thesis
[17]   Semiempirical correlation for Henry's constants over large temperature ranges [J].
Harvey, AH .
AICHE JOURNAL, 1996, 42 (05) :1491-1494
[18]   MOLECULAR THERMODYNAMICS OF GAS SOLUBILITY [J].
HU, Y ;
XU, YN ;
PRAUSNITZ, J .
FLUID PHASE EQUILIBRIA, 1985, 23 (01) :15-40
[19]   MOLECULAR THERMODYNAMICS OF FLUID MIXTURES CONTAINING MOLECULES DIFFERING IN SIZE AND POTENTIAL-ENERGY [J].
HU, Y ;
LUDECKE, D ;
PRAUSNITZ, J .
FLUID PHASE EQUILIBRIA, 1984, 17 (02) :217-241
[20]   THERMODYNAMICS OF ASSOCIATED SOLUTIONS - HENRY CONSTANTS FOR NONPOLAR SOLUTES IN WATER [J].
HU, Y ;
AZEVEDO, E ;
LUDECKE, D ;
PRAUSNITZ, J .
FLUID PHASE EQUILIBRIA, 1984, 17 (03) :303-321