Hypochlorous acid and preparation technology for generating epoxypropane by using same
A preparation process and technology of propylene oxide, applied in hypochlorous acid, organic chemistry and other directions, can solve the problem of low concentration of hypochlorous acid, and achieve the effects of high concentration, production cost saving and environmental protection
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Embodiment 1
[0026] A kind of preparation technology of hypochlorous acid in the propylene oxide production process, carries out successively according to following steps:
[0027] 1) Chlorination process: Dilute chlorine gas and saturated sodium chloride alkali solution to 1.5m 3 / h, 0.1m 3 / h is introduced into the bottom of the tubular reactor through a pump, and a chlorination reaction occurs at the bottom of the tubular reactor to generate a hypochlorous acid solution. The temperature of the chlorination reaction is maintained at 10°C, and the pH of the hypochlorous acid solution is 5;
[0028] 2) Chloroalcoholization process: pass propylene into the hypochlorous acid solution to generate a monochloropropanol solution;
[0029] 3) Extraction process: introduce the monochloropropanol solution into the convection tower of the extractor, add the extractant trioctyl phosphate for extraction, the volume ratio of the extractant trioctyl phosphate to the monochloropropanol solution is 1:1, ...
Embodiment 2
[0033] The chlorine in embodiment one, saturated sodium chloride alkaline solution are replaced by volume respectively as 1.6m 3 / h, 0.15m 3 / h, the chlorination reaction temperature is maintained at 20°C, the pH value of the hypochlorous acid solution is 5.5; the extractant is replaced by tributyl phosphate, and the volume ratio of the extractant tributyl phosphate to the monochloropropanol solution is 1:2 , The extraction rate of monochloropropanol solution is 99.5%. The rest of the process and equipment used are the same as those in Embodiment 1, and will not be described again.
Embodiment 3
[0035] Chlorine in embodiment one, saturated sodium chloride alkaline solution are replaced by volume respectively as 1.7m 3 / h, 0.2m 3 / h, the chlorination reaction temperature is maintained at 60°C, the pH value of the hypochlorous acid solution is 6; the extractant is replaced by n-butyl acetate, and the volume ratio of the extractant n-butyl acetate to the monochloropropanol solution is 1:3 , the extraction rate of monochloropropanol solution was 98.1%. The rest of the process and equipment used are the same as those in Embodiment 1, and will not be described again.
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