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dc.contributor.author문성용-
dc.date.accessioned2019-11-21T01:28:10Z-
dc.date.available2019-11-21T01:28:10Z-
dc.date.issued2017-03-
dc.identifier.citationJOURNAL OF CHROMATOGRAPHY A, v. 1491, page. 75-86en_US
dc.identifier.issn0021-9673-
dc.identifier.issn1873-3778-
dc.identifier.urihttps://www.sciencedirect.com/science/article/pii/S0021967317302789?via%3Dihub-
dc.identifier.urihttps://repository.hanyang.ac.kr/handle/20.500.11754/113014-
dc.description.abstractThe production of fumaric acid through a biotechnological pathway has grown in importance because of its potential value in related industries. This has sparked an interest in developing an economically efficient process for separation of fumaric acid (product of interest) from acetic acid (by-product). This study aimed to develop a simulated moving bed (SMB) chromatographic process for such separation in a systematic way. As a first step for this work, commercially available adsorbents were screened for their applicability to the considered separation, which revealed that an Amberchrom-CG71C resin had a sufficient potential to become an adsorbent of the targeted SMB. Using this adsorbent, the intrinsic parameters of fumaric and acetic acids were determined and then applied to optimizing the SMB process under consideration. The optimized SMB process was tested experimentally, from which the yield of fumaric-acid product was found to become lower than expected in the design. An investigation about the reason for such problem revealed that it was attributed to a fronting phenomenon occurring in the solute band of fumaric acid. To resolve this issue, the extent of the fronting was evaluated quantitatively using an experimental axial dispersion coefficient for fumaric acid, which was then considered in the design of the SMB of interest. The SMB experimental results showed that the SMB design based on the consideration of the fumaric-acid fronting could guarantee the attainment of both high purity (>99%) and high yield (>99%) for fumaric-acid product under the desorbent consumption of 2.6 and the throughput of 0.36L/L/h. (C) 2017 Elsevier B.V. All rights reserved.en_US
dc.description.sponsorshipThis research was supported by Basic Science Research Program through the National Research Foundation of Korea (NRF) funded by the Ministry of Science, ICT and Future Planning (grant number NRF-2015R1A2A2A01003455). Also, it was partially supported by the Advanced Biomass R&D Center (ABC) of Global Frontier Project funded by the Ministry of Science, ICT and Future Planning (ABC-2010-0029728).en_US
dc.language.isoen_USen_US
dc.publisherELSEVIER SCIENCE BVen_US
dc.subjectSTANDING-WAVE DESIGNen_US
dc.subjectMULTIOBJECTIVE OPTIMIZATIONen_US
dc.subjectSMB CHROMATOGRAPHYen_US
dc.subjectGENETIC ALGORITHMen_US
dc.subjectTERNARY MIXTURESen_US
dc.subjectSTRATEGIESen_US
dc.subjectHYDROLYZATEen_US
dc.subjectBIOMASSen_US
dc.subjectSYSTEMSen_US
dc.titleDesign of simulated moving bed for separation of fumaric acid with a little fronting phenomenonen_US
dc.typeArticleen_US
dc.relation.volume1491-
dc.identifier.doi10.1016/j.chroma.2017.02.040-
dc.relation.page75-86-
dc.relation.journalJOURNAL OF CHROMATOGRAPHY A-
dc.contributor.googleauthorChoi, Jae-Hwan-
dc.contributor.googleauthorKang, Mun-Seok-
dc.contributor.googleauthorLee, Chung-gi-
dc.contributor.googleauthorWang, Nien-Hwa Linda-
dc.contributor.googleauthorMun, Sungyong-
dc.relation.code2017003444-
dc.sector.campusS-
dc.sector.daehakCOLLEGE OF ENGINEERING[S]-
dc.sector.departmentDEPARTMENT OF CHEMICAL ENGINEERING-
dc.identifier.pidmunsy-
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COLLEGE OF ENGINEERING[S](공과대학) > CHEMICAL ENGINEERING(화학공학과) > Articles
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