Method for preparation of mixed benzol dimethanoic acid and benzene acetic acid
A technology for mixing xylene and phthalic acid, which is applied in chemical instruments and methods, preparation of organic compounds, preparation of carboxylate, etc., can solve problems such as inability to separate ethylbenzene
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Embodiment 1
[0070] Embodiment 1, the manufacture method of mixed phthalic acid and phenylacetic acid, the technical process is mainly divided into four parts, namely oxidation, phenylacetic acid separation and phenylacetic acid refining, mixed phthalic acid refining, and phthalic anhydride and dimixed phthalic acid separate. According to different product quality requirements and standards, the refining process can be abandoned or simplified.
[0071] (1), oxidation part
[0072] Using mixed xylene as the main raw material, oxygen in compressed air as the auxiliary raw material, acetic acid as the solvent, cobalt acetate and manganese acetate as the catalyst, and hydrobromic acid as the auxiliary catalyst, the oxidation reaction is carried out under relatively mild temperature conditions. Produces mixed phthalic acid (MA) and phenylacetic acid. The "relatively mild temperature conditions" are: a temperature of about 180°C, a pressure of 0.5-2.5Mpa, and a reaction time of 50-180min.
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Embodiment 2
[0092] Embodiment 2 is basically the same as Embodiment 1, but has the following changes:
[0093] The temperature of the oxidation part in step (1) is 100-160° C.;
[0094] In step (2) separation of phenylacetic acid and refining of phenylacetic acid, the method of vacuum distillation is used to separate phenylacetic acid and mixed phthalic acid, so as to reduce the operating temperature of the fluidized bed and avoid the sublimation of phthalic anhydride from entering the phenylacetic acid system;
[0095] In step (3) mixed phthalic acid refining part, hydrogenation reduction refining, mixed phthalic acid (MA) aqueous solution hydrogenation reaction, also can use amorphous nickel as catalyst, carry out in the magnetically stable bed catalytic system. The magnetically stabilized bed technology is used to maintain the suspension, dispersion and relative position stability of the catalyst. In order to increase the reaction residence time, the reaction medium can be designed to...
Embodiment 3
[0096] Embodiment 3 is basically the same as Embodiment 1, but has the following changes:
[0097] The temperature of the oxidation part in step (1) is 190-250° C.;
[0098] Omit the following two steps between the hydroreduction refining step (3)-b and the step (3)-d:
[0099] (3)-c, secondary oxidation refining
[0100] (3)-d, triple oxidation (hydrogen peroxide oxidation) refining.
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