dc.creatorLEONARDO, Marcelo F.
dc.creatorOLIVEIRA, Eder D.
dc.creatorGIUDICI, Reinaldo
dc.date.accessioned2012-10-19T01:45:12Z
dc.date.accessioned2018-07-04T14:51:01Z
dc.date.available2012-10-19T01:45:12Z
dc.date.available2018-07-04T14:51:01Z
dc.date.created2012-10-19T01:45:12Z
dc.date.issued2010
dc.identifierCHEMICAL ENGINEERING & TECHNOLOGY, v.33, n.11, Special Issue, p.1850-1858, 2010
dc.identifier0930-7516
dc.identifierhttp://producao.usp.br/handle/BDPI/18512
dc.identifier10.1002/ceat.201000250
dc.identifierhttp://dx.doi.org/10.1002/ceat.201000250
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1615307
dc.description.abstractThis work presents a mathematical model for the vinyl acetate and n-butyl acrylate emulsion copolymerization process in batch reactors. The model is able to explain the effects of simultaneous changes in emulsifier concentration, initiator concentration, monomer-to-water ratio, and monomer feed composition on monomer conversion, copolymer composition and, to lesser extent, average particle size evolution histories. The main features of the system, such as the increase in the rate of polymerization as temperature, emulsifier, and initiator concentrations increase are correctly represented by the model. The model accounts for the basic features of the process and may be useful for practical applications, despite its simplicity and a reduced number of adjustable parameters.
dc.languageeng
dc.publisherWILEY-BLACKWELL
dc.relationChemical Engineering & Technology
dc.rightsCopyright WILEY-BLACKWELL
dc.rightsrestrictedAccess
dc.subjectEmulsion copolymerization
dc.subjectMathematical modeling
dc.subjectn-butyl acrylate
dc.subjectVinyl acetate
dc.titleModeling Vinyl Acetate and n-Butyl Acrylate Emulsion Copolymerization Process
dc.typeArtículos de revistas


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