Modeling of nitrogen separation from natural gas through nanoporous carbon membranes

被引:11
|
作者
Al-Rabiah, Abdulrahman A. [1 ]
Ajbar, Abdelhamid M. [1 ]
Soliman, Moustafa A. [1 ,2 ]
Almalki, Fahad A. [3 ]
Abdelaziz, Omar Y. [4 ]
机构
[1] King Saud Univ, Dept Chem Engn, Riyadh 11421, Saudi Arabia
[2] British Univ Egypt, Dept Chem Engn, Cairo 11837, Egypt
[3] King Abdulaziz City Sci & Technol, Riyadh 11442, Saudi Arabia
[4] Cairo Univ, Dept Chem Engn, Giza 12613, Egypt
关键词
Nanoporous carbon membrane; Dusty gas model; Mathematical modeling; Nitrogen removal; Natural gas; Selective surface flow; MOLECULAR-DYNAMICS SIMULATION; DIFFUSION; TRANSPORT; REMOVAL; PERFORMANCE; MIXTURES;
D O I
10.1016/j.jngse.2015.08.040
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
This work presents a theoretical investigation of the use of nanoporous carbon membranes for the separation of nitrogen from natural gas. A mathematical model to predict the performance of the membrane is developed. The model is a combination of the well known dusty gas model, which describes the transfer of multi-components mixture in porous media, together with a surface diffusion model. The model is first validated using the literature results for the separation of hydrogen from hydrocarbons mixture. The model is then applied to the nitrogen-hydrocarbons system. The membrane performance is evaluated in terms of nitrogen recovery, methane loss, nitrogen purity, as well as hydrocarbons compositions in both permeate and retentate sides. The model calculation methods are applied for both co-current and counter-current flow configurations. A parametric study is also carried out to investigate the effects of membrane parameters such as feed and permeate pressures and porosity on the membrane performance. The developed model is general and can be applied to various nanoporous membrane flow patterns. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:1278 / 1284
页数:7
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