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Alternative reverse osmosis to purify lactic acid from a fermentation broth

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dc.contributor.author Natnirin Phanthumchinda
dc.contributor.author Tanapawarin Rampai
dc.contributor.author Budsabathip Prasirtsak
dc.contributor.author Sitanan Thitiprasert
dc.contributor.author Somboon Tanasupawat
dc.contributor.author Suttichai Assabumrungrat
dc.contributor.author Nuttha Thongchul
dc.contributor.other Chulalongkorn University. The Institute of Biotechnology and Genetic Engineering
dc.contributor.other Chulalongkorn University. Faculty of Pharmaceutical Sciences
dc.contributor.other Chulalongkorn University. Faculty of Engineering
dc.date.accessioned 2019-06-14T08:31:36Z
dc.date.available 2019-06-14T08:31:36Z
dc.date.issued 2018-04
dc.identifier.citation Chemical Industry and Chemical Engineering Quarterly. vol.24, no.2 (Apr. - Jun, 2018), p.179-190 en_US
dc.identifier.issn 1451-9372 (print)
dc.identifier.issn 2217-7434 (online)
dc.identifier.uri http://cuir.car.chula.ac.th/handle/123456789/62115
dc.description.abstract Brackish water reverse osmosis (BWRO) and seawater reverse osmosis (SWRO) membranes were used in a two-stage reverse osmosis (RO) unit to recover, pre-purify, and pre-concentrate lactic acid. Calcium lactate, sodium lactate, and ammonium lactate were used as model feed solutions. The operating pressure showed a pronounced effect on lactate passage through the first BWRO unit, and the Donnan exclusion effect and hydrogen bonding were responsible for cation rejection. Calcium ions were rejected at the BWRO unit because of low diffusion rate and charge interaction at the surface. However, monovalent ions formed hydrogen bonds with the carbonyl group of the membrane that allowed passage across the membrane. The second SWRO unit was for pre-concentrating lactic acid. A high lactate purity of 99.2% with a total recovery of 50.5% was acquired from calcium lactate feed solution. Lower purity with higher lactate recovery was obtained when the feed solution was sodium lactate and ammonium lactate. When the actual fermentation broth was used in the two-stage RO unit, a slightly lower recovery and purity of lactic acid were obtained. It was claimed that the total ions present in the fermentation broth were responsible for the low efficiency of the two-stage RO unit. en_US
dc.language.iso en en_US
dc.publisher Association of Chemical Engineers of Serbia en_US
dc.relation.uri https://doi.org/10.2298/CICEQ170314030P
dc.relation.uri http://www.doiserbia.nb.rs/Article.aspx?ID=1451-93721700030P
dc.rights Chemical Industry & Chemical Engineering Quarterly en_US
dc.title Alternative reverse osmosis to purify lactic acid from a fermentation broth en_US
dc.type Article en_US
dc.email.author No information provided
dc.email.author No information provided
dc.email.author No information provided
dc.email.author sitanan.t@chula.ac.th
dc.email.author Somboon.T@Chula.ac.th
dc.email.author Suttichai.A@Chula.ac.th
dc.email.author Nuttha.T@Chula.ac.th
dc.subject.keyword lactic acid en_US
dc.subject.keyword fermentation broth en_US
dc.subject.keyword reverse osmosis en_US
dc.subject.keyword Donnan exclusion effect en_US
dc.subject.keyword ionic strength en_US
dc.identifier.DOI 10.2298/CICEQ170314030P


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