Hydrate-based gas separation model considering hydrate structure transformation

被引:0
|
作者
Gao, Jingbo [1 ]
Sun, Qiang [1 ]
Wu, Yuehan [1 ]
Luo, Jia [1 ]
Wang, Yiwei [2 ]
Zhen, Xu [2 ]
Liu, Zengqi [2 ]
Guo, Xuqiang [2 ]
机构
[1] China Univ Petr, State Key Lab Heavy Oil Proc, Beijing 102249, Peoples R China
[2] China Univ Petr Beijing Karamay, State Key Lab Heavy Oil Proc, Karamay 834000, Peoples R China
关键词
Hydrate; Gas separation; Hydrate structure transformation; Model; Muti-phase equilibrium calculation; METHANE; PROPANE; ETHANE;
D O I
10.1016/j.ces.2024.120424
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The study introduces a pioneering model for hydrate-based gas separation technology, which enhances the prediction method for the coexistence of multiple structure hydrates. The calculated results demonstrate strong agreement with 96 sets of experimental data, exhibiting a lower average relative deviation of 8.00 % compared to the traditional model ' s average relative deviation of 60.00 %. Furthermore, it offers a comprehensive discussion on the composition of hydrate structures in (H 2 + CH 4 + C 2 H 6 + C 3 H 8 ) during gas - water-hydrate equilibrium, providing a more precise depiction of hydrate structure evolution. Additional gas-hydrate equilibrium experiments were conducted for the (H 2 + CH 4 + C 2 H 6 + C 3 H 8 ) system to optimize the model parameters. The fitting goodness of the hydrate structure transformation formula ( n I i- S i formula) is enhanced from 0.9162 to 0.9816.
引用
收藏
页数:6
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