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An Effective Iterative Algorithm for Modeling of Multicomponent Gas Separation in a Countercurrent Membrane Permeator | ||
| Gas Processing Journal | ||
| مقاله 4، دوره 2، شماره 1، فروردین 2014، صفحه 19-31 اصل مقاله (676.65 K) | ||
| شناسه دیجیتال (DOI): 10.22108/gpj.2014.20172 | ||
| نویسندگان | ||
| Masoumeh Moheb Shahrestani؛ Amir Rahimi* | ||
| Department of Chemical Engineering, Faculty of Engineering, University of Isfahan, Iran | ||
| چکیده | ||
|  A model is developed for separation of multicomponent gas mixtures in a countercurrent hollow fiber membrane module. While the modelâs solution in countercurrent module usually involves in a time consuming iterative procedure, a proper initial guess is proposed for beginning the calculation and a simple procedure is introduced for correcting the guesses, hereby the CPU time is decreased essentially. The modelâs predictions are compared with the experimental data and a good agreement is achieved. By using data taken from a LAB unit in Isfahan, the proposed model is applied to investigate the feasibility of membrane process for hydrogen separation in this unit. It is revealed that a high hydrogen purity and recovery could be achieved in the permeate stream, while the required area increases at higher stage cut or higher permeate pressure.   | ||
| کلیدواژهها | ||
| Membrane؛ Gas Separation؛ Modeling؛ Hydrogen Separation | ||
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آمار تعداد مشاهده مقاله: 704 تعداد دریافت فایل اصل مقاله: 741 |
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