Effects of additive mixtures (THF/SDS) on carbon dioxide hydrate formation and dissociation in porous media

被引:66
作者
Yang, Mingjun [1 ]
Song, Yongchen [1 ]
Liu, Weiguo [1 ]
Zhao, Jiafei [1 ]
Ruan, Xuke [2 ]
Jiang, Lanlan [1 ]
Li, Qingping [3 ]
机构
[1] Dalian Univ Technol, Minist Educ, Key Lab Ocean Energy Utilizat & Energy Conservat, Dalian 116024, Peoples R China
[2] Chinese Acad Sci, Guangzhou Inst Energy Convers, Key Lab Renewable Energy & Gas Hydrate, Guangzhou 510640, Guangdong, Peoples R China
[3] China Natl Offshore Oil Corp Res Ctr, Beijing 100027, Peoples R China
基金
中国国家自然科学基金;
关键词
CO2; hydrate; Environment; Kinetics; Multiphase flow; Phase equilibria; Porous media; PHASE-EQUILIBRIUM MEASUREMENTS; GAS; CO2; METHANE; SURFACTANT; BROMIDE; CAPTURE; MODEL; N-2;
D O I
10.1016/j.ces.2012.11.026
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The characteristics and stability conditions of carbon dioxide (CO2) hydrate formation are crucial for hydrate-based CO2 capture and storage. The effects of a mixture of additives (THF/SDS) on CO2 hydrate formation and dissociation in porous media have been investigated experimentally using a graphic method. The Gibbs phase rule is used to analyze the experimental p-T curves. Hydrate formation processes can be divided into two cases, depending on the CO2 initial state. The experimental results showed that 1000 mg/L SDS is the best additive and concentration for CO2 hydrate formation among those studied in this investigation due to its shorter induction time and resultantly higher hydrate saturation than those of other concentrations. The presence of 3 mol% THF dramatically decreased the hydrate phase equilibrium pressure. The hydrate equilibrium temperature is 291.55 K in the aqueous phase with 3 mol% THF and 0 mg/L SDS, which is the highest equilibrium temperature at 3.04 MPa observed in this investigation. The experimental results also showed that "pseudo-retrograde" behavior exists at nearly 3.00 MPa with all SDS concentrations. An improved model is used to predict the phase equilibrium conditions for CO2 hydrates in glass beads in the presence of THF, in which the mechanical equilibrium of force between the interfaces in a hydrate-liquid-vapor system is considered. (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:69 / 76
页数:8
相关论文
共 46 条
  • [1] Adeyemo A., 2008, Post combustion capture of carbon dioxide through hydrate formation in silica gel column
  • [2] [Anonymous], 2020, ENERGY TECHNOLOGY PE
  • [3] Sequestration of CO2 in geological media:: criteria and approach for site selection in response to climate change
    Bachu, S
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2000, 41 (09) : 953 - 970
  • [4] Pseudo-retrograde hydrate phenomena at low pressures
    Ballard, AL
    Jager, MD
    Nasrifar, K
    Mooijer-van den Heuvel, MM
    Peters, CJ
    Sloan, ED
    [J]. FLUID PHASE EQUILIBRIA, 2001, 185 (1-2) : 77 - 87
  • [5] Phase equilibrium measurements for semi-clathrate hydrates of the (CO2+N2+tetra-n-butylammonium bromide) aqueous solution systems: Part 2
    Belandria, Veronica
    Mohammadi, Amir H.
    Eslamimanesh, Ali
    Richon, Dominique
    Sanchez-Mora, Maria F.
    Galicia-Luna, Luis A.
    [J]. FLUID PHASE EQUILIBRIA, 2012, 322 : 105 - 112
  • [6] Study of Gas Hydrate Formation in the Carbon Dioxide plus Hydrogen plus Water Systems: Compositional Analysis of the Gas Phase
    Belandria, Veronica
    Eslamimanesh, Ali
    Mohammadi, Amir H.
    Richon, Dominique
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (10) : 6455 - 6459
  • [7] Gas Hydrate Formation in Carbon Dioxide plus Nitrogen plus Water System: Compositional Analysis of Equilibrium Phases
    Belandria, Veronica
    Eslamimanesh, Ali
    Mohammadi, Amir H.
    Richon, Dominique
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (08) : 4722 - 4730
  • [8] Hydrate Equilibrium Conditions of (CH4 + C2H6 + C3H8) Gas Mixtures in Sodium Dodecyl Sulfate Aqueous Solutions
    Chen, Li-Tao
    Sun, Chang-Yu
    Nie, Yun-Qiang
    Sun, Zhan-Song
    Yang, Lan-Ying
    Chen, Guang-Jin
    [J]. JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2009, 54 (05) : 1500 - 1503
  • [9] THE MHV2 MODEL - A UNIFAC-BASED EQUATION OF STATE MODEL FOR PREDICTION OF GAS SOLUBILITY AND VAPOR-LIQUID-EQUILIBRIA AT LOW AND HIGH-PRESSURES
    DAHL, S
    FREDENSLUND, A
    RASMUSSEN, P
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1991, 30 (08) : 1936 - 1945
  • [10] CO2 capture by hydrate crystallization -: A potential solution for gas emission of steelmaking industry
    Duc, Nguyen Hong
    Chauvy, Fabien
    Herri, Jean-Michel
    [J]. ENERGY CONVERSION AND MANAGEMENT, 2007, 48 (04) : 1313 - 1322