A kind of method of producing epichlorohydrin
A technology of epichlorohydrin and chloropropene, which is applied in the direction of organic chemistry, can solve the problems affecting the yield and purity of epichlorohydrin, and achieve the effect of high purity
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Embodiment 1
[0087] At room temperature (25°C) and normal pressure (1 standard atmospheric pressure), after mixing 100 parts by weight of epoxidation reaction mixture with 65 parts by weight of water as the first extractant, it is fed from the lower part of the first extraction tower, and 65 parts by weight of 3-chloropropene (industrial grade, purchased from Baling Petrochemical Co., Ltd., the content of 3-chloropropene is 97% by weight) is added from the top of the first extraction tower as the second extraction agent, so that the two streams Countercurrent contacting is carried out at a temperature of 12°C, and the first extraction phase rich in epichlorohydrin as a heavy liquid phase is obtained from the bottom of the first extraction tower, and the first extraction phase rich in epichlorohydrin as a heavy liquid phase is obtained from the top of the first extraction tower as Methanol-rich first raffinate phase of the light liquid phase.
[0088] The first extraction phase is sent from...
Embodiment 2
[0092] Adopt the same method as Example 1 to separate epichlorohydrin, the difference is that the second extraction phase obtained by the second extraction tower replaces the water used as the first extraction agent in Example 1, wherein the amount of the second extraction phase Same as the consumption of water as the first extractant in Example 1.
[0093] The composition of the obtained second raffinate phase was detected, and the extraction rate of epichlorohydrin and methanol content were calculated, and the results are listed in Table 1.
Embodiment 3
[0102] At room temperature (25°C) and normal pressure (1 standard atmospheric pressure), after mixing 100 parts by weight of the epoxidation reaction mixture with 100 parts by weight of the second extraction phase as the first extractant, it is sent from the lower part of the first extraction tower Into, 50 parts by weight of 3-chloropropene (industrial grade, purchased from Baling Petrochemical Co., Ltd., the content of 3-chloropropene is 97% by weight) is added from the top of the first extraction tower as the second extraction agent, so that The two streams are contacted countercurrently at a temperature of 35° C., and the first extract phase rich in epichlorohydrin as a heavy liquid phase is obtained from the bottom of the first extraction tower. From the tower of the first extraction tower A first methanol-rich raffinate phase was obtained as a light liquid phase.
[0103] The first extraction phase is sent from the lower part of the second extraction tower, and 50 parts ...
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