The purification of fermentatively produced hydrogen using membrane technology: a simulation based on small-scale pilot plant results
Title | The purification of fermentatively produced hydrogen using membrane technology: a simulation based on small-scale pilot plant results |
Publication Type | Journal Article |
Year of Publication | 2016 |
Authors | Lassmann T, Miltner M, Harasek M, Makaruk A, Wukovits W, Friedl A |
Journal | Clean Technologies and Environmental Policy |
Volume | 18 |
Issue | 1 |
Pagination | 315-322 |
ISBN Number | 1618-9558 |
Keywords | Aspen 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. |
URL | https://doi.org/10.1007/s10098-015-0997-7 |
DOI | 10.1007/s10098-015-0997-7 |
Short Title | Clean Technologies and Environmental Policy |