Method for co-producing epoxypropane and epoxy chloropropane
A technology of epichlorohydrin and propylene oxide, applied in the production of bulk chemicals, organic chemistry, etc., can solve the problems of low-value calcium chloride, insufficient utilization of hydrochloric acid, etc., to improve the utilization rate, improve the utilization value, reduce the The effect of the degree of pollution
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Embodiment 1
[0027] A method for co-production of propylene oxide and epichlorohydrin, comprising the following processing steps:
[0028] 1) Chloroalcoholization reaction: react chlorine gas, propylene and water, the content of chloropropanol produced is about 4%, and the content of hydrochloric acid is about 1.6%;
[0029] 2) Preparation of propylene oxide: After extracting the chloropropanol obtained in step 1) with the extractant, rectify the extractant containing chloropropanol to separate the chloropropanol, and pass the chloropropanol into the saponification tower for further Saponification to produce propylene oxide, the extractant separated by rectification returns to the system to continue extracting chloropropanol;
[0030] 3) Extraction of hydrochloric acid: Extract the solution after extracting chloropropanol in step 2) with a complex extractant to extract hydrochloric acid, wherein the complex extractant is composed of N235, n-hexadecane and tributyl phosphate Mixed in a vol...
Embodiment 2
[0034] The difference with embodiment 1 is:
[0035] 1) The blending agent in the complexing extractant is n-octanol instead of tributyl phosphate in Example 1; the volume ratio of complexing agent, solvent and blending agent is 65:25:10;
[0036] 2) In step 4), the volume ratio of the glycerol passed into the tubular reactor to the complex extractant containing hydrochloric acid is 1:7;
[0037] 3) In step 4), the amount of adipic acid accounts for 1% of the volume amount of glycerol.
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