A method for continuous purification of 2-chloro-5-picoline by rectification-crystallization coupling process
A picoline and process technology, applied in the field of continuous purification of 2-chloro-5-picoline by simple rectification plus crystallization coupling process, can solve the problem of not being able to significantly improve the purity of 2-chloro-5-picoline Purification by rectification method, harsh selection of extractant, etc., to achieve the effect of increasing the difficulty of separation, improving the efficiency of separation and purification, and reducing the difficulty of operation
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Embodiment 1
[0027] Precipitation: The toluene-extracted oil layer was introduced into a desolventization distillation unit at a rate of 1000 g / h, and the content of 2-chloro-5-picoline in the extracted oil layer was 33.45%. Use a stirring device to make the solution have a stable gasification center, control the liquid phase temperature at 60-120°C, keep the vacuum at 5-15kPa, control the gas phase temperature at 20-40°C, and the reflux ratio of 2-3 to extract light component solvents , the output flow rate is 471g / h, and the composition of the solvent is 96.67% toluene and 3.01% dichloroethane. The heavy component is extracted at a certain flow rate, and the coke removal process shows that the content of 2-chloro-5-picoline is 63.2%.
[0028] Decoking: The desolventized material enters the decoking distillation system at a flow rate of 528g / h, and at the same time, the filtered mother liquor from the washing and separation step is added at a certain flow rate. Control the liquid phase t...
Embodiment 2-6
[0035] On the basis of Example 1, change the layer crystallization freezing temperature, sweating heating rate, sweating end point temperature, the obtained results are as follows:
[0036]
Embodiment 7-11
[0038] On the basis of example 5, change suspended crystal residence time, suspended crystal cooling temperature, sweating duration, obtained result is as follows:
[0039]
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