The purification of fermentatively produced hydrogen using membrane technology: a simulation based on small-scale pilot plant results

  • Posted on: 6 June 2018
  • By: mmiltner
TitleThe purification of fermentatively produced hydrogen using membrane technology: a simulation based on small-scale pilot plant results
Publication TypeJournal Article
Year of Publication2016
AuthorsLassmann T, Miltner M, Harasek M, Makaruk A, Wukovits W, Friedl A
JournalClean Technologies and Environmental Policy
Volume18
Issue1
Pagination315-322
ISBN Number1618-9558
KeywordsAspen custom modeler, Aspen plus, Gas permeation, Hydrogen purification, Membrane separation, Simulation
Abstract

Hydrogen is known as one of the most promising energy carriers of the future. Its production in a sustainable manner is therefore an important step towards a competitive alternative to fossil energy sources. Dark fermentation is such a sustainable pathway, as hydrogen is produced via biotechnological conversion of biomass. But, the resulting hydrogen-rich gas from fermentation still needs to be upgraded, which can be done via membrane technology. In this work, an innovative small-scale process was developed, membrane modules were assembled and tested, and the purification method was simulatively investigated. The laboratory tests with pure gases showed that the utilized commercially available H2-selective membranes have an ideal H2/CO2-selectivity of 3.3, at the respective process conditions. When applying gas mixtures, the H2/CO2-selectivity was reduced. To further investigate the purification method, an Aspen Plus® gas permeation simulation model was used. The single-stage model was evaluated and it reflected the results from field and laboratory tests well. Furthermore, three different multi-stage setups were developed, simulated, and analyzed. The utilization of H2-selective material in a two-stage process resulted in a specific energy demand of 0.400 kWh/Nm3H2, but achieved no sufficient hydrogen purity. Compared to that, the use of CO2-selective membranes demanded only 0.296 kWh/Nm3H2. The recycle to feed ratio, as well as the H2-puriy of 95.5 vol% in the product was also in favor of the CO2-selective membranes compared to the commercially available H2-selective material.

URLhttps://doi.org/10.1007/s10098-015-0997-7
DOI10.1007/s10098-015-0997-7
Short TitleClean Technologies and Environmental Policy