The invention belongs to the technical field of synthesis of organic compounds, and particularly discloses a
continuous production system and a production method of 1-(4-chlorphenyl)-3-
pyrazole alcohol. The method is used for solving the problems of low production efficiency, high operation cost and danger and large
wastewater discharge of a traditional intermittent
hydrogen peroxide oxidation process. The production
system comprises a
raw material premixing tank, a conveying pump, an air source, an ejector, a reaction unit, a pH adjusting tank, a continuous filter, a
temporary storage tank, a continuous dryer and an
ion resin exchanger, the reaction unit comprises a plurality of static mixing tubular
continuous flow reactors which are connected in series, static mixing elements are arranged in the static mixing tubular
continuous flow reactors, and heat exchange jackets are arranged outside the static mixing tubular
continuous flow reactors; heat exchange jackets or coil pipes are arranged on the outer side walls of the
raw material premixing tank and the pH adjusting tank; and the
ion resin exchanger is provided with a
backwashing port. According to the invention, full-process
continuous production is realized, green and safe preparation is realized, and the production efficiency, the product yield and the product purity are improved.