Membrane unit for integrated gas separation - membrane bioreactor (GS-MBR) system

0561887 - ÚMCH 2023 RIV HU eng J - Journal Article
Pientka, Zbyněk - Peter, Jakub - Válek, R.
Membrane unit for integrated gas separation - membrane bioreactor (GS-MBR) system.
Hungarian Journal of Industrial Chemistry. Roč. 50, č. 1 (2022), s. 15-22. ISSN 0133-0276
R&D Projects: GA MŠMT(CZ) 8F17005
Institutional support: RVO:61389013
Keywords : polymer membranes * gas separation * hollow fibers
OECD category: Polymer science
Impact factor: 0.2, year: 2022
Method of publishing: Open access
https://hjic.mk.uni-pannon.hu/index.php/hjic/article/view/1156

One of the research directions of renewable energy sources is the production of biohydrogen from the dark fermentation of organic matter. During this fermentation process, since hydrogen is produced along with a complex mixture of other gases and vapors, hydrogen gas requires further purification. One relatively easy solution to this problem might be the utilization of gas separation membrane modules given their low energy consumption, simple operation and ease of upscaling. In this work, hollow fiber (HF) membranes based on polyetherimide (PEI) were developed and tested. HF membranes were spun from a polymer solution of PEI using the wet phase inversion process into a water bath using a pilot-scale spinning device. Gas transport measurements showed that membranes exhibited permeances of between 9.3 and 19.2 GPU with CO2/H2 selectivities within the range of 3.3 - 5.6. Morphology studies showed regular shapes resembling hollow fibers with outer diameters within the range of 250-320 microns, depending on various parameters of the spinning process. The best performing membranes were selected and a morphological analysis carried out. Selected fibers were incorporated into two types of membrane modules. One type was a laboratory-scale membrane mini-module used for preliminary tests, while the other membrane module was designed for the treatment of larger amounts of biohydrogen. Two types of laboratory-scale membrane separation units were constructed. For laboratory use, the low-pressure unit proved more accurate regulation to match the fermenters performance with the separation unit in comparison with the high-pressure one.
Permanent Link: https://hdl.handle.net/11104/0335374