Industrial and Engineering Chemistry Research, ( ISI ), Volume (51), No (1), Year (2012-1) , Pages (425-433)

Title : ( A Natural Gas to Liquids Process Model for Optimal Operation )

Authors: Mehdi Panahi , Ahmad Rafiee , Sigurd Skogestad , Magne Hillestad ,

Citation: BibTeX | EndNote

The design and optimization of a natural gas to hydrocarbon liquids (GTL) process is considered, mainly from the view of maximizing the variable income during operation. Autothermal reforming (ATR) is used for synthesis gas production. The kinetic model for FischerTropsch (FT) reactions is the one given by Iglesia et al. for a cobalt-based FT reactor. For the product distribution, three alternative expressions for the chain growth factor α are compared.

Keywords

, natural gas to hydrocarbon liquids (GTL), optimal
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@article{paperid:1045991,
author = {Panahi, Mehdi and Rafiee, Ahmad and Sigurd Skogestad and Magne Hillestad},
title = {A Natural Gas to Liquids Process Model for Optimal Operation},
journal = {Industrial and Engineering Chemistry Research},
year = {2012},
volume = {51},
number = {1},
month = {January},
issn = {0888-5885},
pages = {425--433},
numpages = {8},
keywords = {natural gas to hydrocarbon liquids (GTL); optimal operation},
}

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%0 Journal Article
%T A Natural Gas to Liquids Process Model for Optimal Operation
%A Panahi, Mehdi
%A Rafiee, Ahmad
%A Sigurd Skogestad
%A Magne Hillestad
%J Industrial and Engineering Chemistry Research
%@ 0888-5885
%D 2012

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