A kind of industrial preparation system and preparation method of propylene glycol phenyl ether
A technology for propylene glycol phenyl ether and a preparation system, which is applied in the chemical industry and can solve the problems such as difficulty in obtaining raw materials, difficult wastewater treatment, complicated preparation of alkali catalysts and the like
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[0071] Such as figure 2 As shown, the specific examples of the present invention provide the preparation method of the above-mentioned propylene glycol phenyl ether preparation system, and the method comprises the following steps:
[0072] (1) Phenol and propylene oxide are added in the reactor to carry out constant temperature reaction for the first time, add solid basic catalyst after the first constant temperature reaction and carry out the second time constant temperature reaction;
[0073] (2) The material after the second constant temperature reaction is backflushed and extracted with an acid solution, and then phase-separated to obtain an upper organic phase and a lower aqueous phase;
[0074] (3) The upper organic phase obtained in step (2) is subjected to secondary rectification to obtain the product propylene glycol phenyl ether, and the lower aqueous phase obtained in step (2) is subjected to wastewater treatment.
Embodiment 1
[0076] This embodiment provides a kind of preparation system of propylene glycol phenyl ether, and described system comprises reactor 1, acid tower 2, phase separator 3, first rectification tower 4, tower top phase separator 5 and second rectification tower 6, wherein the reaction kettle 1, the acid tower 2 and the phase separator 3 are connected in sequence, the organic phase outlet of the phase separator 3 is connected with the feed port of the first rectification tower 4, and the top material outlet of the first rectification tower 4 is It is connected with the inlet of the top phase separator 5, and the organic phase outlet of the top phase separator 5 is connected with the feed port of the reaction device and the feed port of the second rectifying tower 6.
[0077] Wherein, the acidic tower 2 is filled with acid liquid, the first rectifying tower 4 is a vacuum rectifying tower, and the second rectifying tower 6 is an atmospheric rectifying tower.
Embodiment 2
[0079] In this example, the system described in Example 1 is used to prepare propylene glycol phenyl ether. The solid basic catalyst used in this example is a composition of sodium hydroxide and magnesium hydroxide, wherein the content of sodium hydroxide is 30wt%, and the content of magnesium hydroxide The content of the catalyst is 70wt%; the solid basic catalyst is obtained after ball milling for 5 hours and then screened with a 0.1 mm sieve.
[0080] The preparation method of described propylene glycol phenyl ether comprises the following steps:
[0081] (1) Add 940kg of phenol into the reaction kettle 1, add 1410kg of solid basic catalyst under stirring conditions to carry out the first constant temperature reaction at 30-40°C, react for 1h, and then react under stirring conditions after the first constant temperature reaction Add 1470kg of propylene oxide to the kettle, the solution is yellow at this time, carry out the second constant temperature reaction at 120°C, reac...
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