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dc.contributor.authorGuan, , Y.
dc.contributor.authorMa, , H.
dc.contributor.authorChen, , W
dc.contributor.authorLi, , M.
dc.contributor.authorQian, Gang
dc.contributor.authorChen, De
dc.contributor.authorZhou, Xinggui
dc.contributor.authorDuan, Xuezhi
dc.date.accessioned2021-02-19T07:44:55Z
dc.date.available2021-02-19T07:44:55Z
dc.date.created2021-01-28T00:06:53Z
dc.date.issued2020
dc.identifier.citationIndustrial & Engineering Chemistry Research. 2020, 59 17408-17416.en_US
dc.identifier.issn0888-5885
dc.identifier.urihttps://hdl.handle.net/11250/2729069
dc.description.abstractMethyl methacrylate (MMA) as a specialty monomer of polymers has motivated industry to develop clean and sustainable technologies for its production. Herein, a comprehensive thermodynamic analysis of MMA production from petroleum-based and coal/biomass-based resources is conducted through the Gibbs free energy minimization method. For the petroleum-based route via oxidative esterification of methacrolein (MAL), the production of MMA is sensitive to the composition of methanol (MeOH) and O2 in the feed, but insensitive to the reaction temperature and pressure. For the coal/biomass-based route via aldol condensation of methyl acetate (MeOAc), a moderate temperature (350–400 °C) and large MeOH/MeOAc ratio (>2) give rise to the efficient production of MMA. Hence, significant improvements in the MMA yield could be achieved by optimizing the reaction conditions, which could almost reach the maximal value theoretically of 1.0 mol from per mole of MAL or MeOAc. This study would shed new light on the thermodynamics of MMA production, which is foundational for the development of new processes at the industrial scale.en_US
dc.language.isoengen_US
dc.publisherAmerican Chemical Societyen_US
dc.titleMethyl Methacrylate Synthesis: Thermodynamic Analysis for Oxidative Esterification of Methacrolein and Aldol Condensation of Methyl Acetateen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionacceptedVersionen_US
dc.source.pagenumber17408-17416en_US
dc.source.volume59en_US
dc.source.journalIndustrial & Engineering Chemistry Researchen_US
dc.identifier.doi10.1016/j.aquatox.2020.105481
dc.identifier.cristin1880843
dc.description.localcodeLocked until 21.5.2021 due to copyright restrictions. This document is the Accepted Manuscript version of a Published Work that appeared in final form in [JournalTitle], copyright © American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see https://doi.org/10.1021/acs.iecr.0c02017en_US
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode2


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