CO2 solubility in multi-component brines containing NaCl, KCl, CaCl2 and MgCl2 at 297 K and 1-14 MPa

被引:44
作者
Jacob, Ruth [1 ]
Saylor, Beverly Z. [1 ]
机构
[1] Case Western Reserve Univ, Dept Earth Environm & Planetary Sci, Cleveland, OH 44106 USA
关键词
Carbon dioxide; Geologic sequestration; CO2; solubility; Multi-component brine; CARBON-DIOXIDE-WATER; AQUEOUS-SOLUTIONS; HIGH-PRESSURE; GEOLOGICAL SEQUESTRATION; MUTUAL SOLUBILITIES; LIQUID-EQUILIBRIUM; HIGH-TEMPERATURES; CO2-H2O MIXTURES; PHASE-EQUILIBRIA; SITE SELECTION;
D O I
10.1016/j.chemgeo.2016.01.013
中图分类号
P3 [地球物理学]; P59 [地球化学];
学科分类号
0708 ; 070902 ;
摘要
Carbon capture and storage (CCS) is a strategy to reduce greenhouse gas emissions by capturing CO2 from point sources and injecting it into deep saline formations. Over time, the injected CO2 dissolves into the saline pore waters forming an aqueous solution that is both a negatively buoyant fluid (sinks) and geologically reactive. Deep saline aquifers are geochemically complex and experimental studies have several gaps in solubility measurements for the multi-component brines that are needed to model the fate and reaction of CO2. New experimental data are presented here for three of the most common salts found in potential carbon storage locations, NaCl, KCl and MgCl2, as well as multi-salt brines including these salts and CaCl2. These experimental data are compared with available literature data and models used to predict CO2 solubility in single-and multi-component brines. Comparison of the experimental data with the models indicates that the reactor does work in the range of temperature, pressure and salinity presented here and that available models can accurately predict the solubility of CO2 in various salt solutions. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:86 / 95
页数:10
相关论文
共 60 条
[1]   Densities of Aqueous MgCl2(aq), CaCl2(aq), KI(aq), NaCl(aq), KCl(aq), AlCl3(aq), and (0.964 NaCl+00136 KCl)(aq) at Temperatures Between (283 and 472) K, Pressures up to 68.5 MPa, and Molalities up to 6 mol.kg-1 [J].
Al Ghafri, Saif ;
Maitland, Geoffrey C. ;
Trusler, J. P. Martin .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2012, 57 (04) :1288-1304
[2]  
[Anonymous], 2011, Annual Energy Review
[3]  
[Anonymous], 2014, CONTRIBUTION WORKING
[4]  
[Anonymous], 2014, The Global Status of CCS: 2014
[5]   Sequestration of CO2 in geological media:: criteria and approach for site selection in response to climate change [J].
Bachu, S .
ENERGY CONVERSION AND MANAGEMENT, 2000, 41 (09) :953-970
[6]   Sequestration of CO2 in geological media in response to climate change:: road map for site selection using the transform of the geological space into the CO2 phase space [J].
Bachu, S .
ENERGY CONVERSION AND MANAGEMENT, 2002, 43 (01) :87-102
[7]   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
[8]   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
[9]   Experimental and modelling study of the solubility of CO2 in various CaCl2 solutions at different temperatures and pressures [J].
Bastami, Alireza ;
Allahgholi, Mohammad ;
Pourafshary, Peyman .
PETROLEUM SCIENCE, 2014, 11 (04) :569-577
[10]  
BREEN KJ, 1985, 844314 USGS