Experimental and modeling study on controlling factor of methane hydrate formation in silica gels

被引:35
作者
Zhang, Yu
Li, Xiao-Sen [1 ]
Chen, Zhao-Yang
Xia, Zhi-Ming
Wang, Yi
Li, Gang
机构
[1] Chinese Acad Sci, Guangzhou Inst Energy Convers, Guangzhou 510640, Guangdong, Peoples R China
基金
中国国家自然科学基金; 国家重点研发计划;
关键词
Methane hydrate; Formation; Silica gels; Pore size; Controlling factor; GAS HYDRATE; CARBON-DIOXIDE; POROUS-MEDIA; PHASE-EQUILIBRIUM; ACTIVE CARBONS; PORE SIZES; FLUE-GAS; CO2; RECOVERY; BEHAVIOR;
D O I
10.1016/j.apenergy.2018.05.059
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
In order to study the mechanism of methane hydrate formation in porous media, the formation experiments of methane hydrate in porous media at the constant pressure were performed in the temperature range of 274.15-276.15 K and the pressure range of 5-8 MPa. The silica gels with the average pore diameters of 129.5, 179.6, and 332 angstrom were used as the porous media for the experiments. The experimental results indicate that the final gas consumption increases with the increase of the formation pressure and the decrease of the formation temperature. Based on the shrinking core model, the reaction-controlled kinetic model and the diffusion-controlled kinetic model for hydrate formation in silica gels were built, respectively. The reaction-controlled kinetic model well fits the kinetic data in 129.5 angstrom and 179.6 angstrom silica gels, and the diffusion-controlled model well fits the kinetic data in 332 angstrom silica gels with a relatively high regression coefficient (R-2 > 0.99). The formation rate of the methane hydrate is controlled by the gas diffusion process in 129.5 angstrom and 179.6 angstrom silica gels, and is controlled by the reaction process in 332 angstrom silica gels.
引用
收藏
页码:827 / 834
页数:8
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