Hydrogen production from biogas reforming and the effect of H2S on CH4 conversion |
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| Affiliation: | 1. Department of Biosystems Engineering, Auburn University, AL, USA;2. Department of Biological and Agricultural Engineering, University of Arkansas, Fayetteville, AR, USA;1. Department of Chemical Engineering, Indian Institute of Technology Hyderabad, Andhra Pradesh 502205, India;2. Department of Metallurgical and Materials Engineering, Indian Institute of Technology Madras, Chennai 600036, Tamil Nadu, India;3. Department of Chemical Engineering, Indian Institute of Technology Madras, Chennai 600036, Tamil Nadu, India;4. Institute for Chemical Technology and Polymer Chemistry, Karlsruhe Institute of Technology, Engesserstr. 20, 76131 Karlsruhe, Germany;1. Department of Chemical Engineering, Faculty of Engineering, Burapha University, Chonburi 20131, Thailand;2. Department of Chemical Engineering, Faculty of Engineering, Srinakharinwirot University, Nakorn Nayok 26120, Thailand;3. School of Chemical Engineering, Faculty of Engineering, King Mongkut''s Institute of Technology Ladkrabang, Bangkok 10520, Thailand;4. Computational Process Engineering Research Unit, Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok 10330, Thailand;1. Advanced Technology Research Laboratories, Nippon Steel Corporation, 20-1 Shintomi, Futtsu, Chiba 293-8511, Japan;2. Research Center for Synchrotron Light Applications, Kyushu University, 6-1 Kasuga-koen, Kasuga, Fukuoka 816-8580, Japan;3. Department of Energy and Material Sciences, Faculty of Engineering Sciences, Kyushu University, 6-1 Kasuga-koen, Kasuga, Fukuoka 816-8580, Japan |
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| Abstract: | Biogas produced during anaerobic decomposition of plant and animal wastes consists of high concentrations of methane (CH4), carbon dioxide (CO2) and traces of hydrogen sulfide (H2S). The primary focus of this research was on investigating the effect of a major impurity (i.e., H2S) on a commercial methane reforming catalyst during hydrogen production. The effect of temperature on CH4 and CO2 conversions was studied at three temperatures (650, 750 and 850 °C) during catalytic biogas reforming. The experimental CH4 and CO2 conversions thus obtained were found to follow a trend similar to the simulated conversions predicted using ASPEN plus. The gas compositions at thermodynamic equilibrium were estimated as a function of temperature to understand the intermediate reactions taking place during biogas dry reforming. The exit gas concentrations as a function of temperature during catalytic reforming also followed a trend similar to that predicted by the model. Finally, catalytic reforming experiments were carried out using three different H2S concentrations (0.5, 1.0 and 1.5 mol%). The study found that even with the introduction of small amount of H2S (0.5 mol%), the CH4 and CO2 conversions dropped to about 20% each as compared to 65% and 85%, respectively in the absence of H2S. |
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| Keywords: | Biogas reforming Hydrogen sulfide Hydrogen selectivity Catalytic poisoning |
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