Chloropropanediol purifying apparatus and production method thereof
A technology of chloroglycerol and production method, applied in the chemical industry, can solve the problems of low conversion rate of raw materials, poor economic benefit, low product yield and the like, and achieve the effects of strong catalytic activity, reduction of by-products, and increase of contact area
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Embodiment 1
[0037] Example 1, such as figure 1 As shown, a chlorinated glycerol purification device comprises a hydrolysis kettle 3, a hydrolyzate head tank 5, an ion exchange column 6, a distillation kettle 7, and a condenser 8 connected through pipelines successively. On the output pipeline of the condenser 8, A front fraction tank 10 and a finished product tank 9 are connected, and the front fraction tank 10 and the finished product tank 9 are respectively connected with a vacuum unit.
[0038] A circulation pipeline is installed between the lower end and the upper end of the hydrolysis kettle 3, and a circulation pump 4 is installed on the circulation pipeline.
[0039] A glass condenser 2 is connected to the circulation pipeline; the liquid inlet pipe of the hydrolyzate head tank 5 communicates with the circulation pipeline.
[0040] The top of the hydrolysis kettle 3 is communicated with an elevated tank 1, and the elevated tank 1 is connected with a hydraulic jet vacuum pump throu...
Embodiment 2
[0059] Example 2, such as figure 1 As shown, a chlorinated glycerol purification device comprises a hydrolysis kettle 3, a hydrolyzate head tank 5, an ion exchange column 6, a distillation kettle 7, and a condenser 8 connected through pipelines successively. On the output pipeline of the condenser 8, A front fraction tank 10 and a finished product tank 9 are connected, and the front fraction tank 10 and the finished product tank 9 are respectively connected with a vacuum unit.
[0060] A circulation pipeline is installed between the lower end and the upper end of the hydrolysis kettle 3, and a circulation pump 4 is installed on the circulation pipeline.
[0061] A glass condenser 2 is connected to the circulation pipeline; the liquid inlet pipe of the hydrolyzate head tank 5 communicates with the circulation pipeline.
[0062] The top of the hydrolysis kettle 3 is communicated with an elevated tank 1, and the elevated tank 1 is connected with a hydraulic jet vacuum pump throu...
Embodiment 3
[0077] Example 3, such as figure 1 As shown, a chlorinated glycerol purification device comprises a hydrolysis kettle 3, a hydrolyzate head tank 5, an ion exchange column 6, a distillation kettle 7, and a condenser 8 connected through pipelines successively. On the output pipeline of the condenser 8, A front fraction tank 10 and a finished product tank 9 are connected, and the front fraction tank 10 and the finished product tank 9 are respectively connected with a vacuum unit.
[0078] A circulation pipeline is installed between the lower end and the upper end of the hydrolysis kettle 3, and a circulation pump 4 is installed on the circulation pipeline.
[0079] A glass condenser 2 is connected to the circulation pipeline; the liquid inlet pipe of the hydrolyzate head tank 5 communicates with the circulation pipeline.
[0080] The top of the hydrolysis kettle 3 is communicated with an elevated tank 1, and the elevated tank 1 is connected with a hydraulic jet vacuum pump throu...
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