发明名称 Transesterification process
摘要 A transesterification process produces a (meth)acrylate ester product from a mixture comprising an alkyl(meth)acrylate reactant, an alcohol reactant, a catalyst, and a polymerization inhibitor, wherein the water content in the reaction zone at the start of the transesterification step is from 0.2 to 1.1 weight percent, based on the weight of the materials in the reaction zone. The mixture is subjected to reaction conditions sufficient to produce a product (meth)acrylate and a product alcohol, which are different than the reactants.
申请公布号 US9394224(B2) 申请公布日期 2016.07.19
申请号 US201314382687 申请日期 2013.02.11
申请人 Rohm and Haas Company 发明人 Flosser David A.;Maillot Philippe P.;Sharma Nawal K.;Ceron Alejandro;Ye Mingyu
分类号 C07C67/02;C07D233/34 主分类号 C07C67/02
代理机构 代理人 Brant Edward L.
主权项 1. A process for producing (meth)acrylate monomers, the process comprising: a) forming a mixture by admixing: a1) reactant alkyl (meth)acrylate; a2) from 10 to 10,000 parts per million by weight, based on the weight of the reactant alkyl (meth)acrylate, of a free radical polymerization inhibitor; and a3) optionally, a reactant alcohol and/or a catalyst: b) if the mixture contains more than 1.1 weight percent water, then dehydrating the mixture so that it contains from 1.0 to 1.1 weight percent water, based on the weight of the mixture; c) adding reactant alcohol and/or catalyst to the mixture, as needed, such that the molar ratio of reactant alcohol to reactant alkyl (meth)acrylate is from 1:1 to 1:20, and such that the catalyst is present in a catalytic amount; d) reacting the reactant alcohol with the reactant alkyl (meth)acrylate in a reaction zone at a temperature of from 70 to 125° C. and a pressure of from 100 mm Hg (13.3 kPa) to 900 mm Hg (120.0 kPa), with the proviso that the water content in the reaction zone at the start of this step is from 1.0 to 1.1 weight percent, based on the weight of the materials in the reaction zone; e) creating a crude product by removing a mixture of alkyl (meth)acrylate and alcohol; f) optionally adding water to enable recycling of the catalyst; g) optionally recycling the reactant alkyl (meth)acrylate; and h) optionally distilling the crude product;wherein the catalyst is selected from the group consisting of dibutyl tin oxide, lithium carbonate, and lithium hydroxide.
地址 Philadelphia PA US