Optimal design of a gas-to-liquids process with a staged Fischer-Tropsch reactor

Rafiee, Ahmad ORCID: https://orcid.org/0000-0002-4750-8536 and Panahi, Mehdi 2016. Optimal design of a gas-to-liquids process with a staged Fischer-Tropsch reactor. Chemical Engineering & Technology 39 (10) , pp. 1778-1784. 10.1002/ceat.201600040

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Abstract

The optimal design of a natural gas-to-liquid hydrocarbons (GTL) process with a multistage cobalt-based Fischer-Tropsch reactor and interstage product separation is considered. The objective function is to maximize the wax (C21+) production rate at the end of the reactor path. Sectioning of the Fischer-Tropsch reactor increases the chain growth probability inside the reactor which results in a higher production of wax. The carbon efficiency of the two-stage reactor is distinctly higher than that of the single-stage reactor.

Item Type:	Article
Date Type:	Publication
Status:	Published
Schools:	Schools > Engineering
Subjects:	T Technology > TJ Mechanical engineering and machinery
Publisher:	Wiley-Blackwell
ISSN:	0930-7516
Date of Acceptance:	20 May 2016
Last Modified:	21 Oct 2022 07:46
URI:	https://orca.cardiff.ac.uk/id/eprint/100715

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