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Standing wave design of carousel ion-exchange processes for the removal of zinc ions from a protein mixture

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dc.contributor.authorMun, Sung yong-
dc.contributor.authorChin, Chim-
dc.contributor.authorXie, Yi-
dc.contributor.authorWang, Nien-Hwa Linda-
dc.date.accessioned2022-12-21T12:13:01Z-
dc.date.available2022-12-21T12:13:01Z-
dc.date.created2022-08-26-
dc.date.issued2006-01-
dc.identifier.issn0888-5885-
dc.identifier.urihttps://scholarworks.bwise.kr/hanyang/handle/2021.sw.hanyang/181879-
dc.description.abstractChelex 100 is a highly effective adsorbent for the separation of metal ions from proteins for three reasons: (i) it has a high affinity for metal ions; (ii) proteins with molecular weight of 1000 or higher are excluded from the particle pores; and (iii) it also allows high flow rates, because it can withstand a pressure drop up to 100 psi. In this study, a carousel process based on Chelex 100 has been developed for the removal of Zn ions from protein in a buffer solution. The intrinsic parameters for the carousel design were estimated from a series of single-column experiments, which showed that Chelex 100 has a high selectivity for Zn ions in I N acetic acid and it can be effectively regenerated using 0.1 N HCl. The exchange mechanisms between Zn2+ and H+ on Chelex 100 were studied and considered in rate model simulations. The effective zinc isotherm was determined to be unfavorable in 1 N acetic acid. A design method based on the standing wave analysis for unfavorable isotherm systems has been developed in this study to ensure high product purity and high yield in carousel ion-exchange processes. Computer simulations and several laboratory-scale carousel experiments showed that the design method and the proposed carousel process can achieve high product purity (100%) and high product yield (> 99%). Compared to a batch size-exclusion chromatography process described previously [Xie et al., Biotechnol. Prog. 2002, 18, 1332], a three-zone carousel process that was based on Chelex 100 has more than 600 times the throughput per bed volume, requires only 63% of the mobile phase, and has a smaller residence time (by a factor of 50).-
dc.language영어-
dc.language.isoen-
dc.publisherAMER CHEMICAL SOC-
dc.titleStanding wave design of carousel ion-exchange processes for the removal of zinc ions from a protein mixture-
dc.typeArticle-
dc.contributor.affiliatedAuthorMun, Sung yong-
dc.identifier.doi10.1021/ie050427k-
dc.identifier.scopusid2-s2.0-30444450692-
dc.identifier.wosid000234315400036-
dc.identifier.bibliographicCitationINDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, v.45, no.1, pp.316 - 329-
dc.relation.isPartOfINDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH-
dc.citation.titleINDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH-
dc.citation.volume45-
dc.citation.number1-
dc.citation.startPage316-
dc.citation.endPage329-
dc.type.rimsART-
dc.type.docTypeArticle-
dc.description.journalClass1-
dc.description.isOpenAccessN-
dc.description.journalRegisteredClassscie-
dc.description.journalRegisteredClassscopus-
dc.relation.journalResearchAreaEngineering-
dc.relation.journalWebOfScienceCategoryEngineering, Chemical-
dc.subject.keywordPlusSIMULATED MOVING-BED-
dc.subject.keywordPlusMASS-ACTION EQUILIBRIA-
dc.subject.keywordPlusCOUNTERCURRENT OPERATION-
dc.subject.keywordPlusINSULIN PURIFICATION-
dc.subject.keywordPlusADSORPTION PROCESSES-
dc.subject.keywordPlusLINEAR-SYSTEMS-
dc.subject.keywordPlusGROWTH-FACTOR-
dc.subject.keywordPlusCHROMATOGRAPHY-
dc.subject.keywordPlusACID-
dc.subject.keywordPlusBINDING-
dc.identifier.urlhttps://pubs.acs.org/doi/10.1021/ie050427k-
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