Modelling of gas to hydrate conversion for promoting CO2 capture processes in the oil and gas industry

被引:14
作者
Baghban, Alireza [1 ]
Bahadori, Mohammad [2 ]
Kashiwao, Tomoaki [3 ]
Bahadori, Alireza [4 ]
机构
[1] Petr Univ Technol, Ahwaz Fac Petr Engn, Dept Gas Engn, Ahvaz, Iran
[2] Griffith Univ, Griffith Sch Environm, Nathan Campus, Nathan, Qld 4111, Australia
[3] Natl Inst Technol, Dept Elect & Control Engn, Niihama, Japan
[4] So Cross Univ, Sch Environm Sci & Engn, Lismore, NSW 2480, Australia
关键词
Semiclathrate hydrate; CO2; TBAC; TBAB; promoter; particle swarm optimization algorithm; least square support vector machine; BUTYL AMMONIUM-CHLORIDE; PLUS CARBON-DIOXIDE; PHASE-EQUILIBRIUM; METHANE; WATER; SYSTEMS; PREDICTION; ENERGY; QSPR; N-2;
D O I
10.1080/10916466.2016.1156126
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 this contribution, equilibrium conditions of clathrate hydrates containing mixtures of carbon dioxide and tetra-n butylammonium bromide and tetra-n butylammonium chloride are modeled by a combination of particle swarm optimization algorithm with least square support vector machine intelligent approach. The evaluation of aforementioned model has been conducted by statistical analyses between experimental and predicted values. The obtained results show excellent performance of proposed model.
引用
收藏
页码:642 / 651
页数:10
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