Experimental Demonstration and Validation of Hydrogen Production Based on Gasification of Lignocellulosic Feedstock
The worldwide production of hydrogen in 2010 was estimated to be approximately 50 Mt/a, mostly based on fossil fuels. By using lignocellulosic feedstock, an environmentally friendly hydrogen production route can be established. A flow sheet simulation for a biomass based hydrogen production plant wa...
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doaj-93a24fd8ea5447fea66092ad59e3ab712020-11-24T21:22:12ZengMDPI AGChemEngineering2305-70842018-12-01246110.3390/chemengineering2040061chemengineering2040061Experimental Demonstration and Validation of Hydrogen Production Based on Gasification of Lignocellulosic FeedstockJürgen Loipersböck0Markus Luisser1Stefan Müller2Hermann Hofbauer3Reinhard Rauch4Syngas processes, BIOENERGY2020+, Wienerstraße 49, 7540 Güssing, AustriaSyngas processes, BIOENERGY2020+, Wienerstraße 49, 7540 Güssing, AustriaInstitute of Chemical Engineering, TU Wien, Getreidemarkt 9/166, 1060 Vienna, AustriaInstitute of Chemical Engineering, TU Wien, Getreidemarkt 9/166, 1060 Vienna, AustriaEngler-Bunte-Institute, Karlsruhe Institute of Technology, Engler-Bunte-Ring 1, 76131 Karlsruhe, GermanyThe worldwide production of hydrogen in 2010 was estimated to be approximately 50 Mt/a, mostly based on fossil fuels. By using lignocellulosic feedstock, an environmentally friendly hydrogen production route can be established. A flow sheet simulation for a biomass based hydrogen production plant was published in a previous work. The plant layout consisted of a dual fluidized bed gasifier including a gas cooler and a dust filter. Subsequently, a water gas shift plant was installed to enhance the hydrogen yield and a biodiesel scrubber was used to remove tars and water from the syngas. CO<sub>2</sub> was removed and the gas was compressed to separate hydrogen in a pressure swing adsorption. A steam reformer was used to reform the hydrocarbon-rich tail gas of the pressure swing adsorption and increase the hydrogen yield. Based on this work, a research facility was erected and the results were validated. These results were used to upscale the research plant to a 10 MW fuel feed scale. A validation of the system showed a chemical efficiency of the system of 60% and an overall efficiency of 55%, which indicates the high potential of this technology.https://www.mdpi.com/2305-7084/2/4/61hydrogenenergy systemcatalysisreformingmodeling |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Jürgen Loipersböck Markus Luisser Stefan Müller Hermann Hofbauer Reinhard Rauch |
spellingShingle |
Jürgen Loipersböck Markus Luisser Stefan Müller Hermann Hofbauer Reinhard Rauch Experimental Demonstration and Validation of Hydrogen Production Based on Gasification of Lignocellulosic Feedstock ChemEngineering hydrogen energy system catalysis reforming modeling |
author_facet |
Jürgen Loipersböck Markus Luisser Stefan Müller Hermann Hofbauer Reinhard Rauch |
author_sort |
Jürgen Loipersböck |
title |
Experimental Demonstration and Validation of Hydrogen Production Based on Gasification of Lignocellulosic Feedstock |
title_short |
Experimental Demonstration and Validation of Hydrogen Production Based on Gasification of Lignocellulosic Feedstock |
title_full |
Experimental Demonstration and Validation of Hydrogen Production Based on Gasification of Lignocellulosic Feedstock |
title_fullStr |
Experimental Demonstration and Validation of Hydrogen Production Based on Gasification of Lignocellulosic Feedstock |
title_full_unstemmed |
Experimental Demonstration and Validation of Hydrogen Production Based on Gasification of Lignocellulosic Feedstock |
title_sort |
experimental demonstration and validation of hydrogen production based on gasification of lignocellulosic feedstock |
publisher |
MDPI AG |
series |
ChemEngineering |
issn |
2305-7084 |
publishDate |
2018-12-01 |
description |
The worldwide production of hydrogen in 2010 was estimated to be approximately 50 Mt/a, mostly based on fossil fuels. By using lignocellulosic feedstock, an environmentally friendly hydrogen production route can be established. A flow sheet simulation for a biomass based hydrogen production plant was published in a previous work. The plant layout consisted of a dual fluidized bed gasifier including a gas cooler and a dust filter. Subsequently, a water gas shift plant was installed to enhance the hydrogen yield and a biodiesel scrubber was used to remove tars and water from the syngas. CO<sub>2</sub> was removed and the gas was compressed to separate hydrogen in a pressure swing adsorption. A steam reformer was used to reform the hydrocarbon-rich tail gas of the pressure swing adsorption and increase the hydrogen yield. Based on this work, a research facility was erected and the results were validated. These results were used to upscale the research plant to a 10 MW fuel feed scale. A validation of the system showed a chemical efficiency of the system of 60% and an overall efficiency of 55%, which indicates the high potential of this technology. |
topic |
hydrogen energy system catalysis reforming modeling |
url |
https://www.mdpi.com/2305-7084/2/4/61 |
work_keys_str_mv |
AT jurgenloipersbock experimentaldemonstrationandvalidationofhydrogenproductionbasedongasificationoflignocellulosicfeedstock AT markusluisser experimentaldemonstrationandvalidationofhydrogenproductionbasedongasificationoflignocellulosicfeedstock AT stefanmuller experimentaldemonstrationandvalidationofhydrogenproductionbasedongasificationoflignocellulosicfeedstock AT hermannhofbauer experimentaldemonstrationandvalidationofhydrogenproductionbasedongasificationoflignocellulosicfeedstock AT reinhardrauch experimentaldemonstrationandvalidationofhydrogenproductionbasedongasificationoflignocellulosicfeedstock |
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