A kind of method for preparing sea breeze aldehyde intermediate
A technology of Haifeng aldehyde and intermediate, applied in the field of preparation of Haifeng aldehyde intermediate, can solve the problems of non-reusable, large amount of waste water, unfavorable environmental protection and the like
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[0015] According to the present invention, there is provided a preparation method of sea breeze aldehyde intermediate, the preparation method comprising the following 3 steps:
[0016] Step 1. Add ethylbenzene, formaldehyde, sulfuric acid aqueous solution and quaternary ammonium salt phase transfer catalyst into the reaction kettle, mix and stir uniformly, wherein the molar ratio of ethylbenzene and formaldehyde is 1:1~2, and the sulfuric acid aqueous solution The mass percentage concentration of the quaternary ammonium salt is 30-95%, and the amount of the quaternary ammonium salt phase transfer catalyst is 0.2-20wt% of ethylbenzene.
[0017] According to the present invention, proton acid sulfuric acid is used as a catalyst for the chloromethylation of ethylbenzene to effectively catalyze the chloromethylation of ethylbenzene. At the same time, sulfuric acid is a large-tonnage chemical product with low price and can reduce production costs.
[0018] The sulfuric acid is used in the...
Embodiment 1
[0052] Add 378g ethylbenzene, 214g paraformaldehyde, 3552g sulfuric acid aqueous solution with a mass percentage concentration of 50% and 57.5g tetrabutylammonium bromide into the reactor, mix and stir well;
[0053] Then the reactor was heated to 50°C, and then hydrogen chloride gas was continuously introduced to perform the chloromethylation reaction. The ventilation rate per hour was such that the molar ratio of hydrogen chloride to ethylbenzene was 0.3:1, and the ventilation was stopped after 12 hours of ventilation;
[0054] The reaction kettle was cooled to 20°C, and then separated at room temperature. The separated aqueous phase was recycled. The organic phase was washed with saturated sodium carbonate solution and saturated brine, and the washed organic phase was distilled under reduced pressure. The fraction of the target product ethyl benzyl chloride is obtained at 70-100°C, and the yield reaches 86%.
[0055] Detected by GC, the content of ethyl benzyl chloride is 96.5%, o...
Embodiment 2
[0057] Add 378g of ethylbenzene, 214g of paraformaldehyde, 2220g of 80% sulfuric acid aqueous solution and 57.5g of tetrabutylammonium bromide into the reactor, mix and stir well;
[0058] Then the reactor was heated to 115°C, and then hydrogen chloride gas was continuously introduced to perform the chloromethylation reaction. The ventilation rate per hour was such that the molar ratio of hydrogen chloride to ethylbenzene was 0.4:1, and the ventilation was stopped after 5 hours of ventilation;
[0059] The reactor was cooled to 25°C, and then separated at room temperature. The separated aqueous phase was recycled. The organic phase was washed twice with saturated sodium carbonate solution and saturated brine, and the washed organic phase was decompressed Distillation to obtain a fraction of the target product ethyl benzyl chloride at 70-100°C, with a yield of 92%.
[0060] According to GC detection, the content of ethyl benzyl chloride is 96.8%, of which the molar ratio of 4-ethyl be...
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