Abstract
Conceptual process simulations and optimization are essential in the design, operation and
troubleshooting stages of a membrane-based gas separation system. Despite this, there are few
mathematicalmodels/tools associated with a hollow fiber membrane module available in a commercial
process simulator. A mathematical model dealing with the hollow fiber module characteristics that can
be included within a commercial process simulator is needed to examine the performance and
economics of a gas separation system. In this study, a hollow fiber membrane modelwas incorporated in
Aspen HYSYS as a user defined unit operation for the study of carbon dioxide separation from methane.
The hollow fibermembrane model was validated experimentally. The study of a double stage membrane
module with a permeate recycle, which was proposed to be the optimal configuration in previous
studies, was extended to consider the effects of the module characteristics (such as the fiber length,
radius of the fiber bundle, diameter of the fibers, and porosity) on the process performance and
economics. The gas processing cost (GPC) increased with increasing fiber length and bundle radius, and
decreased with increasing outer diameter of the fibers and porosity. At the same time, the separation
efficiency (product quality) was also dependent on these module parameters. Therefore, the tradeoff for
the hollow fiber membrane module characteristics needs to be determined based on the minimum GPC
with respect to the desired product purity
Original language | English |
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Pages (from-to) | - |
Journal | Journal of Industrial and Engineering Chemistry |
DOIs | |
Publication status | Published - 5 Jun 2014 |
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Faizan Ahmad
- SCEDT Engineering - Associate Professor of Research
- Centre for Sustainable Engineering
Person: Academic