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Study On Preparation And Catalytic Performance Of Cu/SO42-/MxOy And Cu/S2O82-/MxOy Catalysts

Posted on:2009-09-20Degree:MasterType:Thesis
Country:ChinaCandidate:H B HuangFull Text:PDF
GTID:2121360245965364Subject:Chemical processes
Abstract/Summary:PDF Full Text Request
Dimethyl carbonate(DMC) is a environmental-friendly green chemistry, the synthesis route of methanol oxidative carbonylation to DMC is in accord with the concept of 21th century green chemistry, at the same time, it is very advantageous in thermodynamics and mature in technics with cheap materials. It has been proved that the industrialized CuCl catalyst possesses the innate defect of deactive easily, serious causticity to equipment and polluting production. Asone of research focus currently, the catalysts of H zeolite loaded CuⅠand CuⅡare low active on the liguid oxidative carbonylation of methanol. Some research indicated that some amount of Br(?)nsted acid sites lies in SO42-/MxOy and S2O82-/MxOy solid (super) acid, but whether can it be applied in soild ion exchange, it is still no any detailed report. In the thesis, the catalytic activity ofCuⅠ/SO42-/MxOy and CuⅠ/S2O82-/MxOy (M=Al, Zn, Fe) catalysts of which solid(super) acids were prepared by impregnating method were evaluated on slurry reactor, as well as solid (super) acids and catalysts were characteristic by XRD, py-FTIR, FTIR, NH3-TPD, H2-TPR, XPS etc. Through experiment research andanalyse, the conclusion shows as below:(1) All of the CuⅠ/SO42-/MxOy and CuⅠ/S2O82-/MxOy (M=Al, Zn, Fe) catalysts with low amount of chloride showed high activation on liquid oxidative carbonylation of methanol to DMC, the catalysts (M=Al, Fe) possessed higher activation than the other(M=Zn); at the same reaction condition, all of the SO42-/MxOy and S2O82-/MxOy loaded CuⅠcatalysts wereproved to be higher active than the traditional CuCl and HY zeolite loaded CuⅠcatalyst.(2) Through the characteristic of py-FTIR and element analyse of XPS surface etching, it is proved that the Br(?)nsted acid sites on solid (super) acid(M=Al, Zn, Fe) can be exchanged by metal ion, and metal ion maintains primary metal valency.(3) The XRD characteristic of solid (super) acids and catalysts shows thatthe structure of solid (super) acids has no obvious change if CuⅠwas loadedunder the rato of WCuCl/Wcarrier≤1:2, part of CuCl exchanges with solid (super)acids, and the other lies in catalyst in the form of monlayer.(4) According to the result of activation evaluation, the optimized heatingtemperature of solid (super) acids is in the range of 500~600℃. At thetemperature metal component can be loaded and exchanged with the greatest extent on solid acid.
Keywords/Search Tags:solid acid, solid ion exchange, copper catalyst, oxidative carbonylation, impregnating method, heterogeneous catalysis
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