dc.contributor.author | Venvik, Hilde Johnsen | |
dc.contributor.author | Yang, Jia | |
dc.date.accessioned | 2017-05-29T08:44:03Z | |
dc.date.available | 2017-05-29T08:44:03Z | |
dc.date.created | 2017-05-23T12:11:51Z | |
dc.date.issued | 2017 | |
dc.identifier.citation | Catalysis Today. 2017, 285 135-146. | nb_NO |
dc.identifier.issn | 0920-5861 | |
dc.identifier.uri | http://hdl.handle.net/11250/2443657 | |
dc.description.abstract | Synthesis gas production and further conversion via the Fischer-Tropsch, methanol and dimethyl ether (DME) syntheses is currently economic only in the large scale. Compact, modular, and safe technology efficient in smaller scale would enable utilizing smaller natural gas fields, bio-syngas and even off-shore associated gas that otherwise would be flared or re-injected. So-called or microstructured reactors with superior heat and mass transfer properties and scalability by parallelization may offer opportunity for process intensification and different investment risk. Here, we summarize research into the performance of different combinations of catalyst properties and microchannel design.
We find that intensified production of synthesis gas by steam reforming or catalytic partial oxidation remains associated with significant challenges to the reactor design, the catalysis and the materials. With respect to synthesis of methanol, DME or Fischer-Tropsch products, using a microchannel packed-bed with integrated heat exchange, the results are definitely more encouraging, enabling the use of highly active catalysts and severe process conditions without sacrificing on selectivity and stability. | nb_NO |
dc.language.iso | eng | nb_NO |
dc.publisher | Elsevier | nb_NO |
dc.rights | Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal | * |
dc.rights.uri | http://creativecommons.org/licenses/by-nc-nd/4.0/deed.no | * |
dc.title | Catalysis in microstructured reactors - short review on smallscale syngas production and further conversion into methanol, DME and Fischer-Tropsch products | nb_NO |
dc.type | Journal article | nb_NO |
dc.type | Peer reviewed | nb_NO |
dc.description.version | acceptedVersion | nb_NO |
dc.source.pagenumber | 135-146 | nb_NO |
dc.source.volume | 285 | nb_NO |
dc.source.journal | Catalysis Today | nb_NO |
dc.identifier.doi | https://doi.org/10.1016/j.cattod.2017.02.014 | |
dc.identifier.cristin | 1471565 | |
dc.description.localcode | © 2017 Elsevier B.V. All rights reserved. This is the authors' accepted and refereed manuscript to the article. Locked until 01 May 2019 due to copyright restrictions | nb_NO |
cristin.unitcode | 194,66,30,0 | |
cristin.unitname | Institutt for kjemisk prosessteknologi | |
cristin.ispublished | true | |
cristin.fulltext | postprint | |
cristin.qualitycode | 2 | |