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Hydrogenation of carbon dioxide to synthetic natural gas : impact of catalyst bed arrangement 二氧化碳加氢合成天然气:催化剂床安排之影响
| Content Provider | Semantic Scholar |
|---|---|
| Author | Martin, Andreas Türks, Daniel Mena, Hesham Armbruster, Udo |
| Copyright Year | 2016 |
| Abstract | Hydrogenation of carbon dioxide to synthetic natural gas (SNG) might be a future facet of energy storage solutions. This reaction can be run heterogeneously catalyzed at moderate pressure, it proceeds with high carbon dioxide conversions and extremely good SNG selectivity but it is highly exothermic. It can be operated at large scale in different reactor types but also in small units using simple tube reactors for decentralized solutions to turn excess electric power into storable SNG via intermediate hydrogen. In this paper, we describe the impact of catalyst bed arrangement on reaction heat distribution over the reactor as the basis for further simulations to receive the highest yield and productivity. |
| File Format | PDF HTM / HTML |
| Alternate Webpage(s) | https://www.nscj.co.uk/JECM/PDF/3-1-4-Martin.pdf |
| Language | English |
| Access Restriction | Open |
| Content Type | Text |
| Resource Type | Article |