Dichloropropanol catalyst prepared by glycerol method
A technology of dichloropropanol and catalyst, which is applied in the field of catalysts for preparing dichloropropanol by glycerin method, which can solve the problems of high viscosity of glycerin, high reaction energy consumption, serious environmental pollution, etc., and achieve the improvement of industrial production efficiency and the safety of the use process , the effect of shortening the reaction time
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Embodiment approach 1
[0023] Embodiment 1 (tank reaction): each example catalyst and proportioning are respectively by 1,2,3,4,7 examples in the attached table.
[0024]Referring to the method described in Chinese patent CN100999443A, add glycerin and a proportioning amount of catalyst into the reactor, start stirring, heat to 110°C, feed anhydrous HCl gas from the bottom of the reactor, and adjust the pressure and flow of HCl gas so that Glycerol is fully reactive. The water generated in the reaction process, unreacted HCl, and part of dichloropropanol are azeotropically distilled from the top of the reactor, and the rest of dichloropropanol and monochloropropanediol flow out from the bottom of the reactor. The reaction ends when no distillate flows out of the condenser. Excess HCl is discharged from the top of the reactor, condensed, dried with concentrated sulfuric acid, and then re-entered into the reactor for recycling after pressurization.
[0025] After the reaction, the still liquid and t...
Embodiment approach 2
[0026] Embodiment 2 (still adds spray reaction): each example catalyzer and proportioning are respectively by appendix 5,6,8.
[0027] see figure 1 , 2 1. Pass glycerin and a proportioned amount of mixed acid catalyst in the head tank E1 into the reaction kettle E3, heat to 65°C, and continuously feed HCl gas from the steel cylinder E2 to E3, and the speed of HCl feeding should not escape. After reacting for 1 hour, the materials were introduced into the reactor E4 to continue chlorination, the reaction temperature was controlled at 90° C., and HCl was continuously introduced to continue the reaction for 1 hour.
[0028] The material after the primary reaction is introduced into the spray reaction tower E8 equipped with corrugated net packing, and the temperature in the tower is controlled at 110°C. HCl is continuously introduced from E7 to the bottom of the spray reaction tower, and the pressure at the outlet of the HCl gas is adjusted to make glycerin The reaction is compl...
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