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IF YOU DO NOT RECEIVE ANY MATERIAL MESSAGE FROM US, WE ASK YOU TO SUBMIT THIS APPLICATION AND NOT TO THE FIRST TIME OF THE PRIORITY PERIOD OF THE PRIVATE PATENT OFFICE

机译:如果您没有收到我们的任何材料信息,我们请您提交此申请,并且不要在私人专利局优先期的第一时间提交

摘要

A process for the production of terephthalic acid from p-xylene and methanol by way of the dimethyl terephthalate obtained by oxidation, in the liquid phase with atmospheric oxygen in the presence of dissolved heavy metal compounds as the catalyst, of a mixture of p-xylene and a fraction containing predominantly methyl p-toluate, which fraction is recycled into the oxidation, to obtain an oxidation product containing primarily p-toluic acid and monomethyl terephthalate at a temperature of 140 DEG -170 DEG C. and under a pressure of 4-8 bar; by esterification of the oxidation product in a reactor with liquid and subsequently vaporized methanol brought to an elevated pressure, at a temperature of 220 DEG -280 DEG C. and under a pressure of 20-25 bar to obtain a raw ester containing primarily methyl p-toluate and dimethyl terephthalate; by withdrawing the raw ester fraction and a methanol-containing vapor fraction from the esterification reactor; by distillatory separation of the raw ester into a methyl p-toluate fraction and a fraction rich in terephthalic aldehyde methyl ester, which fractions are recycled into the oxidation, a raw dimethyl terephthalate fraction, and a residual fraction; and by hydrolysis of the raw dimethyl terephthalate fraction with water, obtaining the thus-formed terephthalic acid and separation of a methanol-water mixture. In this process, the methanol-containing vapor fraction and the methanol-water mixture are separated by rectification under elevated pressure and elevated temperature into a methanol-rich head fraction and an aqueous sump phase, the methanol formed at the head of the rectification stage is withdrawn in vapor phase under elevated pressure, and esterification of the oxidation product is conducted with the methanol-containing vapor brought by compression to esterification pressure and esterification temperature.
机译:一种由对二甲苯和甲醇生产对苯二甲酸的方法,该对苯二甲酸是通过在溶解的重金属化合物作为催化剂存在下,在大气中用氧在液相中用大气氧氧化对二甲苯的混合物而得到的对苯二甲酸二甲酯制成的。以及主要包含对甲苯甲酸甲酯的馏分,该馏分再循环到氧化中,以在140℃至170℃的温度和4℃的压力下获得主要包含对甲苯甲酸和对苯二甲酸单甲酯的氧化产物。 8巴;通过在反应器中用液体,然后将汽化的甲醇在220℃-280℃的温度和20-25巴的压力下用液体酯化并随后将其汽化的甲醇酯化,以得到主要含有甲基对苯二甲酸的粗酯。 -甲苯酸酯和对苯二甲酸二甲酯;通过从酯化反应器中取出粗酯馏分和含甲醇的蒸气馏分;通过将粗酯蒸馏分离为对甲苯甲酸甲酯馏分和富含对苯二甲酸醛甲酯的馏分,将该馏分再循环至氧化反应中,将粗对苯二甲酸二甲酯馏分和残余馏分回收。通过用水将粗对苯二甲酸二甲酯级分水解,得到如此形成的对苯二甲酸,并分离出甲醇-水混合物。在该方法中,通过在高压和高温下的精馏将含甲醇的蒸气馏分和甲醇-水混合物分离为富甲醇的塔顶馏分和水底液相,在精馏阶段的塔顶形成的甲醇为在高压下以蒸气相抽出,然后通过压缩至酯化压力和酯化温度而使含甲醇的蒸气进行氧化产物的酯化。

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