Design and modeling of large-scale cross-current multichannel Fischer-Tropsch reactor using channel decomposition and cell-coupling method
DC Field | Value | Language |
---|---|---|
dc.contributor.author | Park, Seongho | - |
dc.contributor.author | Jung, Ikhwan | - |
dc.contributor.author | Lee, Ung | - |
dc.contributor.author | Na, Jonggeol | - |
dc.contributor.author | Kshetrimayum, Krishnadash S. | - |
dc.contributor.author | Lee, Yongkyu | - |
dc.contributor.author | Lee, Chul-Jin | - |
dc.contributor.author | Han, Chonghun | - |
dc.date.accessioned | 2021-08-20T04:40:18Z | - |
dc.date.available | 2021-08-20T04:40:18Z | - |
dc.date.issued | 2015-09 | - |
dc.identifier.issn | 0009-2509 | - |
dc.identifier.issn | 1873-4405 | - |
dc.identifier.uri | https://scholarworks.bwise.kr/cau/handle/2019.sw.cau/48811 | - |
dc.description.abstract | Design and modeling of a micro channel Fischer-Tropsch reactor was considered in this study. A crosscurrent heat-exchange reactor was modeled using a new method, in which all the process and cooling channels are decomposed into a number of unit cells. Each neighboring process and cooling channel unit cells are coupled to set up material and energy balance equations, including heat-transfer equations for the entire reactor domain, which are then solved simultaneously. The model results were compared with the experimental data for a pilot-scale reactor described in the literature, and were found to be in good agreement. Several case studies were performed to see the effect of variables such as catalyst loading ratio, coolant flow rate, and channel layout on design of a reactor with state-of-the-art Fischer-Tropsch catalyst. The developed model could handle more than 5800 process channels, 7500 cooling channels, and 130 layers, with implementation of six complex reaction kinetics. (C) 2015 Published by Elsevier Ltd. | - |
dc.format.extent | 9 | - |
dc.language | 영어 | - |
dc.language.iso | ENG | - |
dc.publisher | PERGAMON-ELSEVIER SCIENCE LTD | - |
dc.title | Design and modeling of large-scale cross-current multichannel Fischer-Tropsch reactor using channel decomposition and cell-coupling method | - |
dc.type | Article | - |
dc.identifier.doi | 10.1016/j.ces.2015.05.057 | - |
dc.identifier.bibliographicCitation | CHEMICAL ENGINEERING SCIENCE, v.134, pp 448 - 456 | - |
dc.description.isOpenAccess | N | - |
dc.identifier.wosid | 000359029200042 | - |
dc.identifier.scopusid | 2-s2.0-84930933857 | - |
dc.citation.endPage | 456 | - |
dc.citation.startPage | 448 | - |
dc.citation.title | CHEMICAL ENGINEERING SCIENCE | - |
dc.citation.volume | 134 | - |
dc.type.docType | Article | - |
dc.publisher.location | 영국 | - |
dc.subject.keywordAuthor | Fischer-Tropsch | - |
dc.subject.keywordAuthor | Micro channel reactor | - |
dc.subject.keywordAuthor | Reactor design | - |
dc.subject.keywordAuthor | Distributed parameter model | - |
dc.subject.keywordAuthor | Gas-to-liquid process | - |
dc.subject.keywordPlus | CATALYST | - |
dc.subject.keywordPlus | METHANE | - |
dc.subject.keywordPlus | STEAM | - |
dc.relation.journalResearchArea | Engineering | - |
dc.relation.journalWebOfScienceCategory | Engineering, Chemical | - |
dc.description.journalRegisteredClass | sci | - |
dc.description.journalRegisteredClass | scie | - |
dc.description.journalRegisteredClass | scopus | - |
Items in ScholarWorks are protected by copyright, with all rights reserved, unless otherwise indicated.
84, Heukseok-ro, Dongjak-gu, Seoul, Republic of Korea (06974)02-820-6194
COPYRIGHT 2019 Chung-Ang University All Rights Reserved.
Certain data included herein are derived from the © Web of Science of Clarivate Analytics. All rights reserved.
You may not copy or re-distribute this material in whole or in part without the prior written consent of Clarivate Analytics.