Determination of the upper-quadruple-phase equilibrium region for carbon dioxide and methane mixed gas hydrates

被引:20
作者
Bi, Yin [1 ]
Yang, Tao [1 ]
Guo, Kaihua [1 ]
机构
[1] Sun Yat Sen Univ, Sch Engn, Guangzhou 510275, Guangdong, Peoples R China
关键词
Gas hydrates; CH4-CO2 mixture hydrates; Quadruple-phase equilibrium; LIQUID-VAPOR EQUILIBRIA; REPLACEMENT; SYSTEMS; STORAGE; CH4;
D O I
10.1016/j.petrol.2012.11.019
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
Simultaneous CO2 sequestration and CH4 production has been considered as a possible way to form and restore CO2 hydrates in sediments of natural gas hydrates in seabeds. The phase equilibrium data for the upper-quadruple (H-W-L-V) phase states of CO2-CH4 mixed hydrates are needed for the application of the replacement of CH4 hydrate with CO2. In this paper, the upper-quadruple (Q(2)) phase equilibrium properties of CO2-CH4 mixed hydrates were investigated by using a visual experimental apparatus in the temperature range of 273.16-297.15 K and pressure up to 10 MPa and verified by calculation with thermodynamic models. The coexisting of upper-quadruple phase region was identified in 4.46-8.4 MPa, 283.09-287.9 K and 0-0.225 methane mole fractions. It is found that the range of temperature and pressure for Q(2) phase coexistence increases with the methane concentration until the retrograde of the quadruple phase is reached. The start and end melting points of the CO2-CH4 mixed hydrates in the upper quadruple states were tested in constant volume condition. The tested results had also been compared with the predictions with a combination of the thermodynamic models for the mixed gas hydrate and CO2-CH4 vapor-liquid equilibrium. The existence of the Q(2) phase equilibrium region and its extension are clarified. (C) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:62 / 67
页数:6
相关论文
共 24 条
[1]   HYDRATES OF CARBON-DIOXIDE AND METHANE MIXTURES [J].
ADISASMITO, S ;
FRANK, RJ ;
SLOAN, ED .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1991, 36 (01) :68-71
[2]   Benefits and drawbacks of clathrate hydrates: a review of their areas of interest [J].
Chatti, I ;
Delahaye, A ;
Fournaison, L ;
Petitet, JP .
ENERGY CONVERSION AND MANAGEMENT, 2005, 46 (9-10) :1333-1343
[3]   LIQUID-VAPOR EQUILIBRIA AT 250.00K FOR SYSTEMS CONTAINING METHANE, ETHANE, AND CARBON-DIOXIDE [J].
DAVALOS, J ;
ANDERSON, WR ;
PHELPS, RE ;
KIDNAY, AJ .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1976, 21 (01) :81-84
[4]  
Du Y. H., 1988, J PET CHINA, V3, P82
[5]   In situ methane hydrate dissociation with carbon dioxide sequestration: Current knowledge and issues [J].
Goel, Naval .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2006, 51 (3-4) :169-184
[6]  
Jadhawar P, 2006, NATO SCI S SS IV EAR, V65, P111
[7]  
Jiang C. M., 2010, OIL GAS CHEM ENG CHI, V39, P371
[8]   A GENERALIZED-MODEL FOR PREDICTING EQUILIBRIUM CONDITIONS FOR GAS HYDRATES [J].
JOHN, VT ;
PAPADOPOULOS, KD ;
HOLDER, GD .
AICHE JOURNAL, 1985, 31 (02) :252-259
[9]   Extended law of corresponding states and thermodynamic properties of binary mixtures in and beyond the critical region [J].
Kiselev, SB ;
Rainwater, JC .
FLUID PHASE EQUILIBRIA, 1997, 141 (1-2) :129-154
[10]   Evaluating cubic equations of state for calculation of vapor-liquid equilibrium of CO2 and CO2-mixtures for CO2 capture and storage processes [J].
Li, H. ;
Yan, J. .
APPLIED ENERGY, 2009, 86 (06) :826-836