Preparation method for halogenohydrin and epoxide
A technology of epoxide and hydroxide, which is applied in separation methods, introduction of hydroxyl and halogen preparation, organic chemistry, etc., can solve problems such as polluting the environment, difficult to handle, and large consumption of water resources
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Embodiment 1
[0095] 1) Haloalcoholization: Add 70wt% concentration of hydrogen peroxide H 2 o 2 , Chlorine (Cl 2 ) and propylene, carry out chlorohydrinization reaction at a temperature of 40 ℃, wherein the hydrogen peroxide H of 70wt% concentration 2 o 2 , Chlorine (Cl 2 ) and propylene flow should make H 2 o 2 with liquid chlorine (Cl 2 ) to propylene in a molar ratio of 1.2:1.6:1. This gives the halohydrin, a mixture of 2-chloropropan-1-ol and 1-chloropropan-2-ol.
Embodiment 2
[0099] 1) Haloalcoholization: add tungstic acid catalyst, 35wt% concentration of hydrogen peroxide H in the tower reactor 2 o 2 , Chlorine (Cl 2 ) and propylene, carry out chlorohydrination reaction at a temperature of 35°C, wherein the mass ratio of tungstic acid catalyst to propylene is 0.05:1, the hydrogen peroxide H of 35wt% concentration 2 o 2 , Chlorine (Cl 2 ) and propylene should be added in such amounts that H 2 o 2 with liquid chlorine (Cl 2 ) to propylene in a molar ratio of 1.5:1.3:1. This gives the halohydrin, a mixture of 2-chloropropan-1-ol and 1-chloropropan-2-ol.
Embodiment 3
[0105] 1) Haloalcoholization: Add 70wt% concentration of hydrogen peroxide H 2 o 2 , Chlorine (Cl 2 ) and propylene, carry out the chloroalcoholization reaction at a temperature of 40°C, and the residence time in the tubular reactor is 35 minutes, wherein the hydrogen peroxide H of 70wt% concentration 2 o 2 , Chlorine (Cl 2 ) and propylene flow should make H 2 o 2 with liquid chlorine (Cl 2 ) to propylene in a molar ratio of 1.2:1.6:1. Halohydrins are obtained, i.e. mixtures of 2-chloropropan-1-ol and 1-chloropropan-2-ol;
[0106] 2) Saponification: Saponifying the haloalcohol obtained in step 1) with sodium hydroxide to obtain an organic phase of propylene oxide and a sodium chloride solution. The saponification reaction is carried out in a steel tower reactor, and the upper part is designed as a sieve tray tower. Steam enters from the bottom of the tower to blow out the crude propylene oxide generated from the top of the tower. The saponification temperature is con...
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