Membrane Unit for Integrated Gas Separation – Membrane Bioreactor (GS-MBR) System

IF 0.5 Q4 ENGINEERING, CHEMICAL Hungarian Journal of Industry and Chemistry Pub Date : 2022-09-27 DOI:10.33927/hjic-2022-04
Z. Pientka, J. Peter, R. Valek
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Abstract

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.
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用于集成气体分离的膜单元-膜生物反应器(GS-MBR)系统
有机物暗发酵制氢是可再生能源的研究方向之一。在这个发酵过程中,由于氢气是与其他气体和蒸汽的复杂混合物一起产生的,因此氢气需要进一步净化。一个相对简单的解决方案可能是利用气体分离膜组件,因为它们能耗低,操作简单,易于升级。本文研究了以聚醚酰亚胺(PEI)为基材的中空纤维(HF)膜。利用中试规模的纺丝装置,从PEI的聚合物溶液中采用湿相转化工艺纺成HF膜。气体输运测量表明,膜的渗透率在9.3 ~ 19.2 GPU之间,CO2/H2选择性在3.3 ~ 5.6之间。形态学研究表明,根据纺丝工艺的不同参数,其外径在250-320微米之间,形状类似于中空纤维。选择了性能最好的膜并进行了形态学分析。选定的纤维被纳入两种类型的膜模块。一种类型是用于初步测试的实验室规模的膜微型模块,而另一种膜模块是为处理大量生物氢而设计的。构建了两种实验室规模的膜分离装置。在实验室使用中,低压装置比高压装置更能准确地调节发酵罐与分离装置的性能。
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来源期刊
自引率
50.00%
发文量
9
审稿时长
6 weeks
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