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Method for realizing dehydration of 2-picoline through coupling of extraction and rectification

A coupling technology of methyl pyridine and rectification, applied in the direction of organic chemistry, etc., can solve the problems such as the inability to recycle the lye, the inability to discharge the alkali water directly, and the limited ability of benzene to carry water, and achieve high product recovery rate and low production cost. , the effect of high volatility

Inactive Publication Date: 2017-05-31
山东海昆化工技术有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The dehydration and refining process of 2-picoline commonly used in industry is mainly the alkali-adding stratification method, which realizes the stratification of 2-picoline and water by changing the acidity and alkalinity of the solution, thereby preparing high-purity 2-picoline However, this method has obvious defects: after adding lye, each ton of industrial raw materials needs to stand still for 10-15 hours, and the product purity is not high, the generated lye cannot be directly discharged, and the lye cannot be recycled, so the economy is poor
It is also reported that benzene is used as an entrainer to destroy the azeotropic mixture of 2-picoline and water through its low-boiling azeotrope with water, so as to realize azeotropic distillation and dehydration. However, benzene, as a toxic chemical Reagents are dangerous in actual operation, and the ability of benzene to carry water is limited; in addition, technical means such as barium oxide, calcium oxide, calcium hydride, lithium aluminum hydride, metal sodium, 5A molecular sieve or membrane separation can also be used Dehydration, but it is not suitable when the water content is high and the treatment capacity is large, the operation is relatively cumbersome and other impurities may be introduced

Method used

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  • Method for realizing dehydration of 2-picoline through coupling of extraction and rectification
  • Method for realizing dehydration of 2-picoline through coupling of extraction and rectification

Examples

Experimental program
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Effect test

Embodiment 1

[0024] This example was carried out in batch mode. First weigh 100 mass parts of 2-picoline and mix 150 mass parts of water as the 2-picoline solution to be dehydrated, then add 800 mass parts of dichloromethane to prepare a mixed solution, and place the mixed solution in In the separatory funnel, seal it with a glass stopper, shake the separatory funnel to mix the materials evenly, then let it stand for 2 hours, you can see obvious stratification, wherein the upper layer is the water phase, and the lower layer contains 2-picoline and The organic phase of dichloromethane was separated to obtain an aqueous phase and an organic phase. It was found by measurement that the aqueous phase was 170 parts by mass, and the organic phase was 880 parts by mass, and the first extraction was completed.

[0025] By testing, the mass percentage of 2-picoline in the water phase is 11.1%. The water phase after the first extraction is mixed with 190 parts by mass of dichloromethane, and dichloro...

Embodiment 2

[0030] The difference between this example and Example 1 is that both the sample and the dichloromethane are fed continuously. Wherein in the mixed solution of 2-picoline and water, the mass percentage composition of 2-picoline is 50%, the feed flow rate is 200kg / h, and the feed flow rate of extractant dichloromethane is 1000kg / h , After the two are mixed evenly by the mixer, they enter the phase separator for static phase separation, ensuring that the residence time of the material in the phase separator is 55min, and the aqueous phase and the organic phase can be continuously extracted. The produced water phase flow rate is 106.4kg / h, and the organic phase flow rate is 1093.6kg / h.

[0031] The aqueous phase obtained by phase separation for the first time is mixed with methylene chloride at a flow rate of 100kg / h, and then phase-separated, the aqueous phase flow rate is 99.8 kg / h, and its composition is measured to know that the mass fraction of water is 99.5%. The mass frac...

Embodiment 3

[0034] The difference between this embodiment and Example two is: in the mixed solution of 2-picoline and water, the mass percentage of 2-picoline is 10%, the feed flow rate is 200kg / h, and the extraction agent The feed flow rate of dichloromethane is 160kg / h. After the two are mixed evenly by the mixer, they enter the phase separator for phase separation, ensuring that the residence time of the material in the phase separator is 30min, and the aqueous phase and organic phase can be continuously extracted. Mutually. The produced aqueous phase flow rate is 185.3 kg / h, and the organic phase flow rate is 174.7 kg / h.

[0035] The water phase obtained by phase separation for the first time is mixed with methylene chloride at a flow rate of 50kg / h, and then separated again, the flow rate of the water phase is 180.6 kg / h, and the mass fraction of water obtained by measuring its composition is 99.6%. The mass fraction of 2-picoline is 0.34%, and the mass fraction of dichloromethane i...

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Abstract

The invention discloses a method for realizing dehydration of 2-picoline through coupling of extraction and rectification, and belongs to the technical field of refinement of organic high molecular compounds. The method is characterized by comprising the following steps: (1) performing mixing: mixing dichloromethane with a to-be-dehydrated 2-picoline solution so as to obtain mixed liquor, wherein the mass ratio of the dichloromethane to the 2-picoline in the mixed liquor is (6-10) to 1; (2) performing extraction and phase separation: placing the mixed liquor in a phase separator for phase separation so as to obtain an aqueous phase and an organic phase and complete extraction once; (3) performing extraction and phase separation once again: detecting the aqueous phase obtained in the step (2), if the 2-picoline is greater than or equal to 1% by mass of the aqueous phase, adding the dichloromethane to the aqueous phase, and when the mass ratio of the dichloromethane to the 2-picoline is (6-10) to 1, executing the step (2) and the step (3); and (4) performing rectification: performing rectification on the organic phase obtained in the step (2) and the step (3), extracting an extraction agent at upper parts, and extracting 2-picoline at lower parts. The dehydration method has the advantages of good separation effects, low production cost, low energy consumption and the like.

Description

technical field [0001] The invention belongs to the technical field of purifying organic polymer compounds, and in particular relates to a method for realizing the dehydration of 2-picoline by coupling extraction and rectification. Background technique [0002] 2-Methylpyridine is an important chemical intermediate and an important raw material for the synthesis of medicines and dyes. At present, a large amount of 2-picoline is used to synthesize 2-vinylpyridine, and 2-vinylpyridine is used to produce butylpyridine latex, which is the skeleton material of rubber products such as tires and conveyor belts. my country's annual demand is tens of thousands of tons and year by year increase, but currently domestic butylpyridine latex mainly relies on imports. [0003] The process of synthesizing 2-vinylpyridine with 2-picoline is as follows: 2-picoline and paraformaldehyde are catalytically added in liquid phase under high pressure or normal pressure to synthesize 2-hydroxyethylpy...

Claims

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Application Information

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IPC IPC(8): C07D213/16
CPCC07D213/16
Inventor 吕灵娟白鹏刘顺江
Owner 山东海昆化工技术有限公司
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