A method for calculating the liquid density for the CO2-H2O-NaCl system under CO2 storage condition

被引:34
作者
Li, Dedong [1 ]
Graupner, Bastian J. [1 ]
Bauer, Sebastian [1 ]
机构
[1] Univ Kiel, Inst Geosci, Geohydromodelling Grp, D-24118 Kiel, Germany
来源
10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES | 2011年 / 4卷
关键词
CO2; OpenGeoSys; CCS; saline aquifers; liquid density; AQUEOUS NACL SOLUTIONS; CARBON-DIOXIDE; METHANE RECOVERY; IMPROVED MODEL; PURE WATER; 647; K; SOLUBILITY; SEQUESTRATION; PRESSURES;
D O I
10.1016/j.egypro.2011.02.317
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A liquid density model for the H2O-CO2-NaCl ternary system is established, based on previous methods (Duan et al. Energy & Fuels 2008, 22, 1666-1674), and combined with a recent density model for H2O-NaCl binary solution (Mao and Duan. The Journal of Chemical Thermodynamics 2008, 40, 1046-1063). The applicable range of the model is 273-573 K, 0.001-1000 bar and 0-6 mol/kg NaCl concentration as well as CO2 concentrations from 0 up to saturated conditions. The model is accurate and its total error is within 0.5%. The applicable range totally covers conditions for geological storage of CO2. Therefore it is suited for simulation studies of CO2 geological storage, especially for fluid convection processes due to density differences. In order to facilitate the model application, a Matlab((c)) program is provided which can be downloaded from our web page. Three examples are presented to demonstrate the model application. The first one is the calculation of pure water density varying with pressure at different temperature conditions. Second application is on the fluid density calculation under different CO2 saturations which is relevant for convection process simulation. The last application shows the total pressure change caused by temperature changes under isometric conditions. (C) 2011 Published by Elsevier Ltd.
引用
收藏
页码:3817 / 3824
页数:8
相关论文
共 25 条
[1]   Scale formation in desalination plants: effect of carbon dioxide solubility [J].
Al-Anezi, Khalid ;
Hilal, Nidal .
DESALINATION, 2007, 204 (1-3) :385-402
[2]   Viscosity of aqueous NaCl solutions with dissolved CO2 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, 2004, 49 (05) :1328-1332
[3]   The simulator TOUGH2/EWASG for modelling geothermal reservoirs with brines and non-condensible gas [J].
Battistelli, A ;
Calore, C ;
Pruess, K .
GEOTHERMICS, 1997, 26 (04) :437-464
[4]  
Deo M.D., 1993, SPE Advanced Technology Series, V1, P142
[5]   An improved model for the calculation of CO2 solubility in aqueous solutions containing Na+, K+, Ca2+, Mg2+, Cl-, and SO42- [J].
Duan, ZH ;
Sun, R ;
Zhu, C ;
Chou, IM .
MARINE CHEMISTRY, 2006, 98 (2-4) :131-139
[6]   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
[7]   Densities of the CO2-H2O and CO2-H2P-NaCl systems up to 647 K and 100 MPa [J].
Duan, Zhenhao ;
Hu, Jiawen ;
Li, Dedong ;
Mao, Shide .
ENERGY & FUELS, 2008, 22 (03) :1666-1674
[8]   SEQUESTRATION OF CO2 IN THE DEEP OCEAN BY SHALLOW INJECTION [J].
HAUGAN, PM ;
DRANGE, H .
NATURE, 1992, 357 (6376) :318-320
[9]   PVTx properties of the CO2-H2O and CO2-H2O-NaCl systems below 647 K:: Assessment of experimental data and thermodynamic models [J].
Hu, Jiawen ;
Duan, Zhenhao ;
Zhu, Chen ;
Chou, I-Ming .
CHEMICAL GEOLOGY, 2007, 238 (3-4) :249-267
[10]   A process-oriented approach to computing multi-field problems in porous media [J].
Kolditz, O ;
Bauer, S .
JOURNAL OF HYDROINFORMATICS, 2004, 6 (03) :225-244