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DEPOLYMERIZATION OF POLY(ETHYLENE-TEREPHTHALATE) RESIN UNDER PRESSURE

dc.citation.epage1507en_US
dc.citation.issue6en_US
dc.citation.spage1501en_US
dc.citation.volume42en_US
dc.citation.woscount78
dc.contributor.authorCHEN, JYen_US
dc.contributor.authorOU, CFen_US
dc.contributor.authorHU, YCen_US
dc.contributor.authorLIN, CCen_US
dc.contributor.department應用化學系zh_TW
dc.contributor.departmentDepartment of Applied Chemistryen_US
dc.date.accessioned2014-12-08T15:05:17Z
dc.date.available2014-12-08T15:05:17Z
dc.date.issued1991-03-20en_US
dc.description.abstractThe process of depolymerization of PET resin by EG glycolysis under pressure is investigated. The kinetics of this pressurized depolymerization of PET resin is discussed. It was found that the rate of deploymerization is dependent of temperature, pressure, and concentration ratio of EG to PET. The rate of depolymerization is proportional to the square of EG concentration and faster than that under atmospheric pressure. Glycolyzed products under pressure consist of the PET monomer, BHET, and oligomers, mostly dimer and trimer. An equilibrium between BHET and oligomers is attained quickly soon after the deploymerization step is completed in the case of a higher ratio of EG/PET used. In the case of lower ratio of EG/PET, the final product now consists of molecular weight of oligomers rather than monomer, dimer, and trimer.en_US
dc.identifier.doi10.1002/app.1991.070420603en_US
dc.identifier.issn0021-8995en_US
dc.identifier.journalJOURNAL OF APPLIED POLYMER SCIENCEen_US
dc.identifier.urihttp://dx.doi.org/10.1002/app.1991.070420603en_US
dc.identifier.urihttps://ir.lib.nycu.edu.tw/handle/11536/3832
dc.identifier.wosnumberWOS:A1991EZ41000003
dc.language.isoen_USen_US
dc.titleDEPOLYMERIZATION OF POLY(ETHYLENE-TEREPHTHALATE) RESIN UNDER PRESSUREen_US
dc.typeArticleen_US

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