Absorber Model for CO2 Capture by Monoethanolamine

The rate-based steady-state model proposed by Gabrielsen et al. (Gabrielsen, J.; Michelsen, M. L.; Kontogeorgis, G. M.; Stenby, E. H. AIChE J. 2006, 52, 10, 3443−3451) for the design of the CO2−2-amino-2-methyl-propanol absorbers is adopted and improved for the design of the CO2−monoethanolamine abs...

Full description

Saved in:
Bibliographic Details
Published in:Industrial & engineering chemistry research 2010-04, Vol.49 (8), p.3751-3759
Main Authors: Faramarzi, Leila, Kontogeorgis, Georgios M, Michelsen, Michael L, Thomsen, Kaj, Stenby, Erling H
Format: Article
Language:English
Subjects:
Applied sciences
Chemical engineering
Exact sciences and technology
Separations
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by
cites
container_end_page 3759
container_issue 8
container_start_page 3751
container_title Industrial & engineering chemistry research
container_volume 49
creator Faramarzi, Leila
Kontogeorgis, Georgios M
Michelsen, Michael L
Thomsen, Kaj
Stenby, Erling H
description The rate-based steady-state model proposed by Gabrielsen et al. (Gabrielsen, J.; Michelsen, M. L.; Kontogeorgis, G. M.; Stenby, E. H. AIChE J. 2006, 52, 10, 3443−3451) for the design of the CO2−2-amino-2-methyl-propanol absorbers is adopted and improved for the design of the CO2−monoethanolamine absorber. The influence of the application of different mass transfer correlations on the model’s performance is investigated. Analytical expressions for the calculation of the enhancement factor for the second order as well as the pseudo-first-order reaction regime are integrated in the model, and their impact on the model’s prediction is compared. The model has been successfully applied to CO2 absorber packed columns and validated against pilot plant data with good agreement.
doi_str_mv 10.1021/ie901671f
format article
fullrecord <record><control><sourceid>acs_pasca</sourceid><recordid>TN_cdi_pascalfrancis_primary_22630062</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>d145130746</sourcerecordid><originalsourceid>FETCH-LOGICAL-a215t-6be79a20f70cfe641637167e67ebf18aa07690ef6d5881f212b75d495ae3ae793</originalsourceid><addsrcrecordid>eNpFkE1LxDAQhoMouK4e_Ae9eKxO0uajx6X4BSt70XOYtBPs0m1K0j3svzeiKAzMYd53eHgYu-Vwz0Hwh4Ea4Epzf8ZWXAooJdTynK3AGFNKY-Qlu0ppDwBS1vWKiY1LITqKxVvoaSx8iEW7E0WL83KMVLhTPkyBlk-cwoiHYaJrduFxTHTzu9fs4-nxvX0pt7vn13azLVFwuZTKkW5QgNfQeVI1V5XOZJTHeW4QQasGyKs-Y3EvuHBa9nUjkSrM1WrN7n7-zpg6HH3EqRuSneNwwHiyQqgKQIn_HHbJ7sMxTpnKcrDfQuyfkOoL949Qyw</addsrcrecordid><sourcetype>Index Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>Absorber Model for CO2 Capture by Monoethanolamine</title><source>American Chemical Society:Jisc Collections:American Chemical Society Read &amp; Publish Agreement 2022-2024 (Reading list)</source><creator>Faramarzi, Leila ; Kontogeorgis, Georgios M ; Michelsen, Michael L ; Thomsen, Kaj ; Stenby, Erling H</creator><creatorcontrib>Faramarzi, Leila ; Kontogeorgis, Georgios M ; Michelsen, Michael L ; Thomsen, Kaj ; Stenby, Erling H</creatorcontrib><description>The rate-based steady-state model proposed by Gabrielsen et al. (Gabrielsen, J.; Michelsen, M. L.; Kontogeorgis, G. M.; Stenby, E. H. AIChE J. 2006, 52, 10, 3443−3451) for the design of the CO2−2-amino-2-methyl-propanol absorbers is adopted and improved for the design of the CO2−monoethanolamine absorber. The influence of the application of different mass transfer correlations on the model’s performance is investigated. Analytical expressions for the calculation of the enhancement factor for the second order as well as the pseudo-first-order reaction regime are integrated in the model, and their impact on the model’s prediction is compared. The model has been successfully applied to CO2 absorber packed columns and validated against pilot plant data with good agreement.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/ie901671f</identifier><identifier>CODEN: IECRED</identifier><language>eng</language><publisher>Washington, DC: American Chemical Society</publisher><subject>Applied sciences ; Chemical engineering ; Exact sciences and technology ; Separations</subject><ispartof>Industrial &amp; engineering chemistry research, 2010-04, Vol.49 (8), p.3751-3759</ispartof><rights>Copyright © 2010 American Chemical Society</rights><rights>2015 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27901,27902</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&amp;idt=22630062$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Faramarzi, Leila</creatorcontrib><creatorcontrib>Kontogeorgis, Georgios M</creatorcontrib><creatorcontrib>Michelsen, Michael L</creatorcontrib><creatorcontrib>Thomsen, Kaj</creatorcontrib><creatorcontrib>Stenby, Erling H</creatorcontrib><title>Absorber Model for CO2 Capture by Monoethanolamine</title><title>Industrial &amp; engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>The rate-based steady-state model proposed by Gabrielsen et al. (Gabrielsen, J.; Michelsen, M. L.; Kontogeorgis, G. M.; Stenby, E. H. AIChE J. 2006, 52, 10, 3443−3451) for the design of the CO2−2-amino-2-methyl-propanol absorbers is adopted and improved for the design of the CO2−monoethanolamine absorber. The influence of the application of different mass transfer correlations on the model’s performance is investigated. Analytical expressions for the calculation of the enhancement factor for the second order as well as the pseudo-first-order reaction regime are integrated in the model, and their impact on the model’s prediction is compared. The model has been successfully applied to CO2 absorber packed columns and validated against pilot plant data with good agreement.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Exact sciences and technology</subject><subject>Separations</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2010</creationdate><recordtype>article</recordtype><recordid>eNpFkE1LxDAQhoMouK4e_Ae9eKxO0uajx6X4BSt70XOYtBPs0m1K0j3svzeiKAzMYd53eHgYu-Vwz0Hwh4Ea4Epzf8ZWXAooJdTynK3AGFNKY-Qlu0ppDwBS1vWKiY1LITqKxVvoaSx8iEW7E0WL83KMVLhTPkyBlk-cwoiHYaJrduFxTHTzu9fs4-nxvX0pt7vn13azLVFwuZTKkW5QgNfQeVI1V5XOZJTHeW4QQasGyKs-Y3EvuHBa9nUjkSrM1WrN7n7-zpg6HH3EqRuSneNwwHiyQqgKQIn_HHbJ7sMxTpnKcrDfQuyfkOoL949Qyw</recordid><startdate>20100421</startdate><enddate>20100421</enddate><creator>Faramarzi, Leila</creator><creator>Kontogeorgis, Georgios M</creator><creator>Michelsen, Michael L</creator><creator>Thomsen, Kaj</creator><creator>Stenby, Erling H</creator><general>American Chemical Society</general><scope>IQODW</scope></search><sort><creationdate>20100421</creationdate><title>Absorber Model for CO2 Capture by Monoethanolamine</title><author>Faramarzi, Leila ; Kontogeorgis, Georgios M ; Michelsen, Michael L ; Thomsen, Kaj ; Stenby, Erling H</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a215t-6be79a20f70cfe641637167e67ebf18aa07690ef6d5881f212b75d495ae3ae793</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2010</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Exact sciences and technology</topic><topic>Separations</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Faramarzi, Leila</creatorcontrib><creatorcontrib>Kontogeorgis, Georgios M</creatorcontrib><creatorcontrib>Michelsen, Michael L</creatorcontrib><creatorcontrib>Thomsen, Kaj</creatorcontrib><creatorcontrib>Stenby, Erling H</creatorcontrib><collection>Pascal-Francis</collection><jtitle>Industrial &amp; engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Faramarzi, Leila</au><au>Kontogeorgis, Georgios M</au><au>Michelsen, Michael L</au><au>Thomsen, Kaj</au><au>Stenby, Erling H</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Absorber Model for CO2 Capture by Monoethanolamine</atitle><jtitle>Industrial &amp; engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2010-04-21</date><risdate>2010</risdate><volume>49</volume><issue>8</issue><spage>3751</spage><epage>3759</epage><pages>3751-3759</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><coden>IECRED</coden><abstract>The rate-based steady-state model proposed by Gabrielsen et al. (Gabrielsen, J.; Michelsen, M. L.; Kontogeorgis, G. M.; Stenby, E. H. AIChE J. 2006, 52, 10, 3443−3451) for the design of the CO2−2-amino-2-methyl-propanol absorbers is adopted and improved for the design of the CO2−monoethanolamine absorber. The influence of the application of different mass transfer correlations on the model’s performance is investigated. Analytical expressions for the calculation of the enhancement factor for the second order as well as the pseudo-first-order reaction regime are integrated in the model, and their impact on the model’s prediction is compared. The model has been successfully applied to CO2 absorber packed columns and validated against pilot plant data with good agreement.</abstract><cop>Washington, DC</cop><pub>American Chemical Society</pub><doi>10.1021/ie901671f</doi><tpages>9</tpages></addata></record>
fulltext fulltext
identifier ISSN: 0888-5885
ispartof Industrial & engineering chemistry research, 2010-04, Vol.49 (8), p.3751-3759
issn 0888-5885
1520-5045
language eng
recordid cdi_pascalfrancis_primary_22630062
source American Chemical Society:Jisc Collections:American Chemical Society Read & Publish Agreement 2022-2024 (Reading list)
subjects Applied sciences
Chemical engineering
Exact sciences and technology
Separations
title Absorber Model for CO2 Capture by Monoethanolamine
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-06T19%3A58%3A13IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-acs_pasca&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Absorber%20Model%20for%20CO2%20Capture%20by%20Monoethanolamine&rft.jtitle=Industrial%20&%20engineering%20chemistry%20research&rft.au=Faramarzi,%20Leila&rft.date=2010-04-21&rft.volume=49&rft.issue=8&rft.spage=3751&rft.epage=3759&rft.pages=3751-3759&rft.issn=0888-5885&rft.eissn=1520-5045&rft.coden=IECRED&rft_id=info:doi/10.1021/ie901671f&rft_dat=%3Cacs_pasca%3Ed145130746%3C/acs_pasca%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-a215t-6be79a20f70cfe641637167e67ebf18aa07690ef6d5881f212b75d495ae3ae793%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true