Kinetics Investigation of Carbon Dioxide Hydrate Formation Process in a New Impinging Stream Reactor

被引:5
作者
Bai, Jing [1 ,2 ,3 ]
Xie, Gengbiao [1 ,3 ]
Li, Lingqian [1 ,3 ]
Li, Pan [1 ,2 ,3 ]
Fang, Shuqi [1 ,2 ,3 ]
Chang, Chun [1 ,2 ,3 ]
机构
[1] Zhengzhou Univ, Sch Mech & Power Engn, Zhengzhou 450001, Peoples R China
[2] Henan Ctr Outstanding Overseas Sci, Zhengzhou 450001, Peoples R China
[3] Engn Lab Henan Prov Biorefinery Technol & Equipme, Zhengzhou 450001, Peoples R China
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
carbon dioxide hydrate; impinging stream; CO2 gas consumption; kinetics; NATURAL-GAS HYDRATE; POROUS-MEDIA; METHANE; CO2; COMPOSITE; MIXTURES; CAPTURE;
D O I
10.1515/ijcre-2019-0132
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The absorption of carbon dioxide by hydrates is considered as one of the potential methods for carbon capture and storage. In this work, a new impinging stream reactor was designed to investigate the characteristics of carbon dioxide hydrate formation process. The experiments were carried out at different pressure, temperature and impinging strength. It was shown that the carbon dioxide hydrate formation process could be enhanced by the impinging stream technique. With the increased of impinging strength, both gas consumption and hydration rate were increased. In addition, initial pressure and temperature also had an effect on the carbon dioxide hydrate formation process. Moreover, the kinetics of carbon dioxide hydrate formation was discussed. When the initial pressure was 3.5 MPa and impinging strength was 0.21, the activation energy was 24.74 kJ/mol, which was similar to the experimental data available in the literature.
引用
收藏
页数:15
相关论文
共 39 条
[1]  
[Anonymous], 1996, METHOD PRODUCTION GA
[2]   Phase Equilibria of CO2 Hydrate Formation in Glucoamylase Aqueous Solutions [J].
Bai, Jing ;
Zhang, Lu ;
Li, Jing ;
Liang, Teng-bo ;
Chang, Chun ;
Fang, Shu-qi ;
Han, Xiu-li ;
Liang, Deqing .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2016, 61 (02) :891-895
[3]   Continuous Formation Process of CO2 Gas Hydrate via a Vortex and Impinging Stream Reactor [J].
Bai, Jing ;
Liang, Deqing ;
Li, Dongliang ;
Fan, Shuanshi ;
Du, Jianwei ;
Dai, Xingxue ;
Long, Zhen .
ENERGY & FUELS, 2010, 24 (02) :1207-1212
[4]   Effect of surfactant carbon chain length on hydrate formation kinetics [J].
Daimaru, Takamichi ;
Yamasaki, Akihiro ;
Yanagisawa, Yukio .
JOURNAL OF PETROLEUM SCIENCE AND ENGINEERING, 2007, 56 (1-3) :89-96
[5]  
Elperin I.T., 1961, J. Eng. Phys., V6, P62
[6]   KINETICS OF FORMATION OF METHANE AND ETHANE GAS HYDRATES [J].
ENGLEZOS, P ;
KALOGERAKIS, N ;
DHOLABHAI, PD ;
BISHNOI, PR .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (11) :2647-2658
[7]   KINETICS OF GAS HYDRATE FORMATION FROM MIXTURES OF METHANE AND ETHANE [J].
ENGLEZOS, P ;
KALOGERAKIS, N ;
DHOLABHAI, PD ;
BISHNOI, PR .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (11) :2659-2666
[8]  
Kinias C, 2009, VERFAHREN HERSTELLUN
[9]   Deep sub-seabed disposal of CO2 - The most protective storage [J].
Koide, H ;
Shindo, Y ;
Tazaki, Y ;
Iijima, M ;
Ito, K ;
Kimura, N ;
Omata, K .
ENERGY CONVERSION AND MANAGEMENT, 1997, 38 :S253-S258
[10]   SELF-TRAPPING MECHANISMS OF CARBON-DIOXIDE IN THE AQUIFER DISPOSAL [J].
KOIDE, H ;
TAKAHASHI, M ;
TSUKAMOTO, H ;
SHINDO, Y .
ENERGY CONVERSION AND MANAGEMENT, 1995, 36 (6-9) :505-508