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<dublin_core schema="dc">
<dcvalue element="contributor" qualifier="author">An,&#x20;Jinjoo</dcvalue>
<dcvalue element="contributor" qualifier="author">Na,&#x20;Jonggeol</dcvalue>
<dcvalue element="contributor" qualifier="author">Lee,&#x20;Ung</dcvalue>
<dcvalue element="contributor" qualifier="author">Han,&#x20;Chonghun</dcvalue>
<dcvalue element="date" qualifier="accessioned">2024-01-19T23:34:02Z</dcvalue>
<dcvalue element="date" qualifier="available">2024-01-19T23:34:02Z</dcvalue>
<dcvalue element="date" qualifier="created">2021-09-03</dcvalue>
<dcvalue element="date" qualifier="issued">2018-01</dcvalue>
<dcvalue element="identifier" qualifier="issn">0263-8762</dcvalue>
<dcvalue element="identifier" qualifier="uri">https:&#x2F;&#x2F;pubs.kist.re.kr&#x2F;handle&#x2F;201004&#x2F;121856</dcvalue>
<dcvalue element="description" qualifier="abstract">A&#x20;comprehensive&#x20;optimal&#x20;design&#x20;for&#x20;the&#x20;CO2&#x20;dehydration&#x20;process&#x20;created&#x20;by&#x20;decomposition&#x20;based&#x20;superstructure&#x20;optimization&#x20;is&#x20;proposed.&#x20;To&#x20;reach&#x20;the&#x20;most&#x20;economical&#x20;process&#x20;configuration,&#x20;the&#x20;superstructure&#x20;model&#x20;has&#x20;been&#x20;developed&#x20;including&#x20;binary&#x20;interaction&#x20;parameter&#x20;regression&#x20;of&#x20;the&#x20;NRTL-RK&#x20;thermodynamic&#x20;model,&#x20;unit&#x20;operation&#x20;modeling,&#x20;and&#x20;identification&#x20;of&#x20;the&#x20;connectivity&#x20;of&#x20;each&#x20;of&#x20;the&#x20;unit&#x20;operations&#x20;in&#x20;the&#x20;superstructure.&#x20;The&#x20;superstructure&#x20;imbeds&#x20;30,720&#x20;possible&#x20;process&#x20;alternatives&#x20;and&#x20;unit&#x20;operation&#x20;options.&#x20;To&#x20;simplify&#x20;the&#x20;optimization&#x20;problem,&#x20;the&#x20;process&#x20;simulation&#x20;was&#x20;explicitly&#x20;carried&#x20;out&#x20;in&#x20;a&#x20;sequential&#x20;process&#x20;simulator,&#x20;and&#x20;the&#x20;constrained&#x20;optimization&#x20;problem&#x20;was&#x20;solved&#x20;externally&#x20;using&#x20;a&#x20;genetic&#x20;algorithm&#x20;and&#x20;an&#x20;Aspen&#x20;Plus-MATLAB&#x20;interface.&#x20;The&#x20;optimal&#x20;process&#x20;includes&#x20;a&#x20;five-stage&#x20;contactor,&#x20;a&#x20;nine-stage&#x20;still&#x20;column&#x20;(with&#x20;the&#x20;feed&#x20;stream&#x20;entering&#x20;at&#x20;the&#x20;seventh&#x20;stage),&#x20;a&#x20;lean&#x2F;rich&#x20;solvent&#x20;heat&#x20;exchanger,&#x20;and&#x20;a&#x20;cold&#x20;rich&#x20;solvent&#x20;split&#x20;flow&#x20;fed&#x20;to&#x20;the&#x20;first&#x20;stage&#x20;of&#x20;still&#x20;column.&#x20;The&#x20;total&#x20;annualized&#x20;cost&#x20;of&#x20;the&#x20;optimum&#x20;process&#x20;is&#x20;6.70&#x20;M$&#x2F;year,&#x20;which&#x20;corresponds&#x20;to&#x20;the&#x20;specific&#x20;annualized&#x20;cost&#x20;of&#x20;1.88&#x20;$&#x2F;tCO(2).&#x20;As&#x20;part&#x20;of&#x20;the&#x20;process&#x20;optimization,&#x20;a&#x20;Monte&#x20;Carlo&#x20;simulation&#x20;was&#x20;performed&#x20;to&#x20;analyze&#x20;the&#x20;sensitivity&#x20;of&#x20;utility&#x20;cost&#x20;volatility;&#x20;the&#x20;refrigerant&#x20;and&#x20;steam&#x20;present&#x20;the&#x20;most&#x20;influential&#x20;utility&#x20;costs.&#x20;(C)&#x20;2017&#x20;Institution&#x20;of&#x20;Chemical&#x20;Engineers.&#x20;Published&#x20;by&#x20;Elsevier&#x20;B.V.&#x20;All&#x20;rights&#x20;reserved.</dcvalue>
<dcvalue element="language" qualifier="none">English</dcvalue>
<dcvalue element="publisher" qualifier="none">INST&#x20;CHEMICAL&#x20;ENGINEERS</dcvalue>
<dcvalue element="subject" qualifier="none">POSTCOMBUSTION&#x20;CO2&#x20;CAPTURE</dcvalue>
<dcvalue element="subject" qualifier="none">CHEMICAL&#x20;ABSORPTION</dcvalue>
<dcvalue element="subject" qualifier="none">POWER-PLANTS</dcvalue>
<dcvalue element="subject" qualifier="none">PILOT-PLANT</dcvalue>
<dcvalue element="subject" qualifier="none">ENERGY</dcvalue>
<dcvalue element="subject" qualifier="none">LIQUEFACTION</dcvalue>
<dcvalue element="subject" qualifier="none">PERFORMANCE</dcvalue>
<dcvalue element="subject" qualifier="none">SEPARATION</dcvalue>
<dcvalue element="subject" qualifier="none">FLOW</dcvalue>
<dcvalue element="subject" qualifier="none">MEA</dcvalue>
<dcvalue element="title" qualifier="none">Design&#x20;of&#x20;carbon&#x20;dioxide&#x20;dehydration&#x20;process&#x20;using&#x20;derivative-free&#x20;superstructure&#x20;optimization</dcvalue>
<dcvalue element="type" qualifier="none">Article</dcvalue>
<dcvalue element="identifier" qualifier="doi">10.1016&#x2F;j.cherd.2017.11.028</dcvalue>
<dcvalue element="description" qualifier="journalClass">1</dcvalue>
<dcvalue element="identifier" qualifier="bibliographicCitation">CHEMICAL&#x20;ENGINEERING&#x20;RESEARCH&#x20;&amp;&#x20;DESIGN,&#x20;v.129,&#x20;pp.344&#x20;-&#x20;355</dcvalue>
<dcvalue element="citation" qualifier="title">CHEMICAL&#x20;ENGINEERING&#x20;RESEARCH&#x20;&amp;&#x20;DESIGN</dcvalue>
<dcvalue element="citation" qualifier="volume">129</dcvalue>
<dcvalue element="citation" qualifier="startPage">344</dcvalue>
<dcvalue element="citation" qualifier="endPage">355</dcvalue>
<dcvalue element="description" qualifier="journalRegisteredClass">scie</dcvalue>
<dcvalue element="description" qualifier="journalRegisteredClass">scopus</dcvalue>
<dcvalue element="identifier" qualifier="wosid">000424855100029</dcvalue>
<dcvalue element="identifier" qualifier="scopusid">2-s2.0-85040790833</dcvalue>
<dcvalue element="relation" qualifier="journalWebOfScienceCategory">Engineering,&#x20;Chemical</dcvalue>
<dcvalue element="relation" qualifier="journalResearchArea">Engineering</dcvalue>
<dcvalue element="type" qualifier="docType">Article</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">POSTCOMBUSTION&#x20;CO2&#x20;CAPTURE</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">CHEMICAL&#x20;ABSORPTION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">POWER-PLANTS</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">PILOT-PLANT</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">ENERGY</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">LIQUEFACTION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">PERFORMANCE</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">SEPARATION</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">FLOW</dcvalue>
<dcvalue element="subject" qualifier="keywordPlus">MEA</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">CO2&#x20;dehydration</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">TEG&#x20;absorption</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">Process&#x20;design</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">Superstructure&#x20;optimization</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">Genetic&#x20;algorithm</dcvalue>
<dcvalue element="subject" qualifier="keywordAuthor">Techno-economic&#x20;optimization</dcvalue>
</dublin_core>
