Please use this identifier to cite or link to this item: http://nopr.niscair.res.in/handle/123456789/6133
Full metadata record
DC FieldValueLanguage
dc.contributor.authorGadekar, S V-
dc.contributor.authorNaik, R V-
dc.contributor.authorKaul, S N-
dc.date.accessioned2009-10-09T04:26:11Z-
dc.date.available2009-10-09T04:26:11Z-
dc.date.issued2009-10-
dc.identifier.issn0975-1084 (Online); 0022-4456 (Print)-
dc.identifier.urihttp://hdl.handle.net/123456789/6133-
dc.description871-875en_US
dc.description.abstractAcetic acid–water system (AW) poses a challenge in reactive distillation, acetic acid purity and loss of acetic acid in aqueous solutions. Feasible separation of AW has been studied using entrainers but acetic acid loss in lean phase cannot be avoided. This study presents feasible region to operate column with toluene and benzene as entrainer for AW. Liquid -liquid equilibrium data and nature of tie line for ethyl acetate are given priority.en_US
dc.language.isoen_USen_US
dc.publisherCSIRen_US
dc.sourceJSIR Vol.68(10) [October 2009]en_US
dc.subjectAcetic aciden_US
dc.subjectBatch distillationen_US
dc.subjectBenzeneen_US
dc.subjectEntraineren_US
dc.subjectTolueneen_US
dc.titleEntrainer for batch distillation of acetic acid–water systemen_US
dc.typeArticleen_US
Appears in Collections:JSIR Vol.68(10) [October 2009]

Files in This Item:
File Description SizeFormat 
JSIR 68(10) 871-875.pdf588.89 kBAdobe PDFView/Open


Items in NOPR are protected by copyright, with all rights reserved, unless otherwise indicated.