Modeling of stability conditions of natural gas clathrate hydrates using least squares support vector machine approach

被引:35
作者
Ghiasi, Mohammad M. [1 ,2 ]
Yarveicy, Hamidreza [3 ]
Arabloo, Milad [4 ]
Mohammadi, Amir H. [1 ,5 ,6 ]
Behbahani, Reza M. [7 ]
机构
[1] Univ KwaZulu Natal, Sch Engn, Discipline Chem Engn, Howard Coll Campus,King George V Ave, ZA-4041 Durban, South Africa
[2] Natl Iranian Gas Co, South Pars Gas Complex, Asaluyeh, Iran
[3] Tarbiat Modares Univ, Dept Chem Engn, Tehran, Iran
[4] Islamic Azad Univ, Young Researchers & Elites Club, North Tehran Branch, Tehran, Iran
[5] IRGCP, Paris, France
[6] Univ Laval, Fac Sci & Genie, Dept Genie Mines Met & Mat, Quebec City, PQ G1V 0A6, Canada
[7] Petr Univ Technol, Ahwaz Fac Petr Engn, Ahvaz, Iran
关键词
Gas hydrates; Hydrate dissociation temperature; Phase equilibrium; LSSVM algorithm; AQUEOUS ETHYLENE-GLYCOL; CARBON-DIOXIDE; EQUILIBRIUM CONDITIONS; DISSOCIATION PRESSURES; PHASE-EQUILIBRIUM; METHANE HYDRATE; ELECTROLYTE-SOLUTIONS; HYDROGEN-SULFIDE; SODIUM-CHLORIDE; PURE WATER;
D O I
10.1016/j.molliq.2016.09.009
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
This paper concerns a novel computer-based approach namely Least Square version of Support Vector Machine (LSSVM) algorithm to estimate/represent hydrate forming/dissociating conditions of various gases in the presence of pure water or aqueous solutions of salt(s) and/or alcohol(s). To this end, several models have been presented to predict the hydrate dissociating temperature (HDT) of C-1, C-2, C-3, i-C-4, CO2, H2S, N-2, and natural gas mixtures in pure water or additive containing solutions. For modeling purpose, an extensive database comprising more than 3900 experimental data have been gathered from the literate from 1940 to 2013. The collected databank covers wide range of experimental conditions at solid/liquid/vapor or solid/ice/vapor equilibrium of distinct hydrate systems. All the proposed models reproduce the targets with R-2 of greater than 0.97. The predictions of the developed LSSVM models for hydrate systems of C-1, C-2, C-3, i-C-4, CO2, H2S, N-2, and natural gas mixtures are in good agreement with corresponding experimental data with the average absolute relative deviation percent (%AARD) equal to %0.22, %0.33, %0.26, %0.07, %0.47, %0.56, %0.08, and %0.34, respectively. (c) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:1081 / 1092
页数:12
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