首页> 外国专利> METHOD OF GAINING AND REINTRODUCING THE OXIDATION CATALYSER IN PROCESS OF PRODUCING THE DIMETHYL TEREPHTALATE IN THE OXIDATION

METHOD OF GAINING AND REINTRODUCING THE OXIDATION CATALYSER IN PROCESS OF PRODUCING THE DIMETHYL TEREPHTALATE IN THE OXIDATION

机译:在氧化过程中生产对苯二甲酸二甲酯的过程中获得和重新引入氧化催化剂的方法

摘要

A process for effecting the recovery and use of a heavy metal oxidation catalyst from a high-boiling distillation residue obtained during the Witten process for the production of dimethyl terephthalate involves the extraction of the high-boiling distillation reside with water or dilute aqueous solution of low molecular weight aliphatic monocarboxylic acids or alcohols and recycling of the extract into the oxidation stage of the Witten process. In the extract the quantitative ratio of the sum of the amount of trimellitic acid and monomethyl ester of trimellitic acid to the amount of heavy metal catalyst is controlled to be at a value of no more than 1.8:1 and in the oxidation stage of the Witten process the catalyst concentration (c), expressed in p.p.m., is represented by the formula: c=44x(a/b)+d wherein a represents the sum of trimellitic acid and monomethyl ester of trimellitic acid, b is the amount of heavy metal oxidation catalyst within the extract, and d is in a range of from 60 to 300 p.p.m.
机译:一种从维滕生产对苯二甲酸二甲酯的过程中获得的高沸点蒸馏残渣中回收和使用重金属氧化催化剂的方法,包括用水或低浓度的稀水溶液萃取高沸点蒸馏残留物。分子量的脂肪族一元羧酸或醇类,并将提取物再循环到维滕工艺的氧化阶段。在提取物中,将偏苯三酸和偏苯三酸单甲酯的总和与重金属催化剂的量的定量比控制为不大于1.8:1,并且在维滕的氧化阶段中式中,催化剂浓度(c)以ppm表示,由下式表示:c = 44x(a / b)+ d其中a表示偏苯三酸和偏苯三酸单甲酯之和,b是重金属的量提取物中的氧化催化剂,d为60-300 ppm

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