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dc.contributor.authorChebbi, Rachid
dc.contributor.authorAl-Amoodi, Nahla S.
dc.contributor.authorAbdel-Jabbar, Nabil
dc.contributor.authorHusseini, Ghaleb
dc.contributor.authorAl Mazroui, Khamis A.
dc.date.accessioned2021-01-26T08:50:41Z
dc.date.available2021-01-26T08:50:41Z
dc.date.issued2010
dc.identifier.citationS. 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.en_US
dc.identifier.issn0263-8762
dc.identifier.urihttp://hdl.handle.net/11073/21283
dc.description.abstractEthane 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.en_US
dc.language.isoen_USen_US
dc.publisherElsevieren_US
dc.relation.urihttps://doi.org/10.1016/j.cherd.2009.11.003en_US
dc.subjectNatural gas liquids (NGL)en_US
dc.subjectEthaneen_US
dc.subjectRecoveryen_US
dc.subjectOptimizationen_US
dc.subjectTurboexpanderen_US
dc.subjectSimulationen_US
dc.titleOptimum ethane recovery in conventional turboexpander processen_US
dc.typePeer-Revieweden_US
dc.typeArticleen_US
dc.typePostprinten_US
dc.identifier.doi10.1016/j.cherd.2009.11.003


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