Process for preparing 2,3,5-trimethyl p-benzoquinone by means of catalytic oxidation
A catalytic oxidation and trimethylation technology, applied in the preparation of oxidized quinone, organic chemistry, etc., can solve the problems of low oxygen utilization rate, few industrial practical applications, and low production efficiency
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[0022] According to above narration, the present invention proposes the preparation method of a set of 2,3,5-trimethyl-p-benzoquinone matched with the preparation technology of 2,3,5-trimethyl-p-benzoquinone of the present invention, now In conjunction with the preparation process of the above-mentioned 2,3,5-trimethyl-p-benzoquinone to understand the idea of the preparation method of 2,3,5-trimethyl-p-benzoquinone, see figure 2 . The preparation technology of this 2,3,5-trimethyl-p-benzoquinone comprises the following steps:
[0023] S1: Turn on the temperature control device and raise all reactors and pipelines to the specified temperature.
[0024]S2: Turn on the supergravity reactor 7 and the stirred tank reactor 2, and adjust to the required speed.
[0025] S3: Open the gas pipeline and the liquid pipeline, the gas enters the stirred tank reactor 2 after passing through the supergravity reactor 7, and finally discharges from the condensation device 9; the liquid circ...
Embodiment 1
[0034] Embodiment 1: Effect experiment of supergravity level
[0035] The reaction temperature is 73°C, the volume fraction of the water phase in the liquid phase is 0.83, the rotation speed of the stirred tank reactor is 600rpm, the concentration of 2,3,6-trimethylphenol in the oil phase is the same as that of CuCl in the water phase 2 The concentration ratio is 1:2, the above refers to the molar concentration ratio, CuCl 2 The concentration of the aqueous solution is 1mol / L, the gas-liquid volume flow ratio is 2.6, and the result of reaction for 10 minutes is as follows:
[0036] Hypergravity level (g)
[0037] The above results show that, compared with using the stirred tank reactor alone, the yield of 2,3,5-trimethyl-p-benzoquinone can be increased by about 10% after adding the high gravity reactor.
Embodiment 2
[0038] Example 2: Gas volume influence experiment
[0039] The reaction temperature is 75°C, the volume fraction of the water phase in the liquid phase is 0.83, the rotation speed of the stirred tank reactor is 600rpm, the supergravity level of the supergravity reactor is 270g, the liquid flow rate is 20L / h, and 2,3,6-trimethanone in the oil phase Base phenol concentration and CuCl in aqueous phase 2 The concentration ratio is 1:2, the above refers to the molar concentration ratio, CuCl 2 The concentration of the aqueous solution is 1mol / L, and the result of reacting for 10 minutes is as follows:
[0040]
[0041]
[0042] The above results show that, compared with using the stirred tank reactor alone, the yield of 2,3,5-trimethyl-p-benzoquinone can be increased by about 9-13% after adding the high gravity reactor.
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