Optimum ethane recovery in conventional turboexpander process

Ethane recovery in a conventional turboexpander process is optimized considering different demethanizer pressures and different feeds: a lean gas and a rich one. The design variables are varied, while meeting process constraints, in order to find the optimum conditions achieving the maximum profit....

وصف كامل

محفوظ في:
التفاصيل البيبلوغرافية
المؤلف الرئيسي: Chebbi, Rachid (author)
مؤلفون آخرون: Al-Amoodi, Nahla S. (author), Abdel-Jabbar, Nabil (author), Husseini, Ghaleb (author), Al Mazroui, Khamis A. (author)
التنسيق: article
منشور في: 2010
الموضوعات:
الوصول للمادة أونلاين:http://hdl.handle.net/11073/21283
الوسوم: إضافة وسم
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author Chebbi, Rachid
author2 Al-Amoodi, Nahla S.
Abdel-Jabbar, Nabil
Husseini, Ghaleb
Al Mazroui, Khamis A.
author2_role author
author
author
author
author_facet Chebbi, Rachid
Al-Amoodi, Nahla S.
Abdel-Jabbar, Nabil
Husseini, Ghaleb
Al Mazroui, Khamis A.
author_role author
dc.creator.none.fl_str_mv Chebbi, Rachid
Al-Amoodi, Nahla S.
Abdel-Jabbar, Nabil
Husseini, Ghaleb
Al Mazroui, Khamis A.
dc.date.none.fl_str_mv 2010
2021-01-26T08:50:41Z
2021-01-26T08:50:41Z
dc.format.none.fl_str_mv application/pdf
dc.identifier.none.fl_str_mv S. Al-Amoodi, N.M. Abdel Jabbar, G.A. Husseini, K.A. Al Mazroui, Optimum ethane recovery in conventional turboexpander process, Chemical Engineering Research and Design, Volume 88, Issues 5–6, 2010, Pages 779-787, ISSN 0263-8762, https://doi.org/10.1016/j.cherd.2009.11.003.
0263-8762
http://hdl.handle.net/11073/21283
10.1016/j.cherd.2009.11.003
dc.language.none.fl_str_mv en_US
dc.publisher.none.fl_str_mv Elsevier
dc.relation.none.fl_str_mv https://doi.org/10.1016/j.cherd.2009.11.003
dc.subject.none.fl_str_mv Natural gas liquids (NGL)
Ethane
Recovery
Optimization
Turboexpander
Simulation
dc.title.none.fl_str_mv Optimum ethane recovery in conventional turboexpander process
dc.type.none.fl_str_mv Peer-Reviewed
Postprint
info:eu-repo/semantics/publishedVersion
info:eu-repo/semantics/article
description Ethane recovery in a conventional turboexpander process is optimized considering different demethanizer pressures and different feeds: a lean gas and a rich one. The design variables are varied, while meeting process constraints, in order to find the optimum conditions achieving the maximum profit. The analysis covers the whole process including the refrigeration part, and the entire typical demethanizer pressure range. The optimum ethane recovery is compared with the maximum possible recovery for each value of the demethanizer pressure. Recommendations are given regarding the selection of the level of ethane recovery, along with the demethanizer pressure, and refrigeration recovery system.
format article
id aus_f43a2f1f711af1cf0dfdc31fa0e0ce08
identifier_str_mv S. Al-Amoodi, N.M. Abdel Jabbar, G.A. Husseini, K.A. Al Mazroui, Optimum ethane recovery in conventional turboexpander process, Chemical Engineering Research and Design, Volume 88, Issues 5–6, 2010, Pages 779-787, ISSN 0263-8762, https://doi.org/10.1016/j.cherd.2009.11.003.
0263-8762
10.1016/j.cherd.2009.11.003
language_invalid_str_mv en_US
network_acronym_str aus
network_name_str aus
oai_identifier_str oai:repository.aus.edu:11073/21283
publishDate 2010
publisher.none.fl_str_mv Elsevier
repository.mail.fl_str_mv
repository.name.fl_str_mv
repository_id_str
spelling Optimum ethane recovery in conventional turboexpander processChebbi, RachidAl-Amoodi, Nahla S.Abdel-Jabbar, NabilHusseini, GhalebAl Mazroui, Khamis A.Natural gas liquids (NGL)EthaneRecoveryOptimizationTurboexpanderSimulationEthane recovery in a conventional turboexpander process is optimized considering different demethanizer pressures and different feeds: a lean gas and a rich one. The design variables are varied, while meeting process constraints, in order to find the optimum conditions achieving the maximum profit. The analysis covers the whole process including the refrigeration part, and the entire typical demethanizer pressure range. The optimum ethane recovery is compared with the maximum possible recovery for each value of the demethanizer pressure. Recommendations are given regarding the selection of the level of ethane recovery, along with the demethanizer pressure, and refrigeration recovery system.Elsevier2021-01-26T08:50:41Z2021-01-26T08:50:41Z2010Peer-ReviewedPostprintinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfS. Al-Amoodi, N.M. Abdel Jabbar, G.A. Husseini, K.A. Al Mazroui, Optimum ethane recovery in conventional turboexpander process, Chemical Engineering Research and Design, Volume 88, Issues 5–6, 2010, Pages 779-787, ISSN 0263-8762, https://doi.org/10.1016/j.cherd.2009.11.003.0263-8762http://hdl.handle.net/11073/2128310.1016/j.cherd.2009.11.003en_UShttps://doi.org/10.1016/j.cherd.2009.11.003oai:repository.aus.edu:11073/212832024-08-22T12:04:44Z
spellingShingle Optimum ethane recovery in conventional turboexpander process
Chebbi, Rachid
Natural gas liquids (NGL)
Ethane
Recovery
Optimization
Turboexpander
Simulation
status_str publishedVersion
title Optimum ethane recovery in conventional turboexpander process
title_full Optimum ethane recovery in conventional turboexpander process
title_fullStr Optimum ethane recovery in conventional turboexpander process
title_full_unstemmed Optimum ethane recovery in conventional turboexpander process
title_short Optimum ethane recovery in conventional turboexpander process
title_sort Optimum ethane recovery in conventional turboexpander process
topic Natural gas liquids (NGL)
Ethane
Recovery
Optimization
Turboexpander
Simulation
url http://hdl.handle.net/11073/21283