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Compound cross-flow liquid-liquid extraction separation method of methylal-methanol azeotropic system

A separation method and composite extractant technology, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problem of difficulty in obtaining high-purity methylal products, long reaction time of calcium chloride method, and unfavorable industrial production and other problems, to achieve the effect of low production cost, high recovery rate and obvious effect

Inactive Publication Date: 2012-11-28
NANJING NORMAL UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The synthetic method of methylal mainly contains dichloromethane method, dimethyl sulfoxide method, calcium chloride method, acid catalysis method, carbon monoxide heterogeneous catalysis and chloramphenicol by-product method, in above-mentioned method, dichloromethane method, two Methyl sulfoxide method and carbon monoxide heterogeneous catalysis are limited because the catalyst is unstable to acid and carbon monoxide or the yield is low; calcium chloride method is not conducive to industrial production because of long reaction time and difficult post-treatment; currently, chlorotoxin is generally used Preparation of methylal by by-product method and acid catalysis method
Regardless of the acid-catalyzed method or the chloramphenicol by-product method, the product after the reaction is a mixture of methylal-methanol, and there are subsequent separation problems. Due to the azeotrope between methylal and methanol, the azeotropic point is 41.85 ° C, and it contains methylal. Aldehyde 91.8%, so it is difficult to obtain high-purity methylal products by ordinary distillation

Method used

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  • Compound cross-flow liquid-liquid extraction separation method of methylal-methanol azeotropic system
  • Compound cross-flow liquid-liquid extraction separation method of methylal-methanol azeotropic system
  • Compound cross-flow liquid-liquid extraction separation method of methylal-methanol azeotropic system

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Embodiment 1

[0015] Embodiment 1, the method for separating methylal and methanol by cross-flow liquid-liquid extraction, with reference to figure 1 The process flow shown and the process parameters shown in Tables 1 and 2, the raw material ① is a mixed solution of methylal and methanol, wherein the mass content of methylal and methanol is 91.8%, 8.2% respectively, the flow rate is 5Kg / h, the solvent ⑨ is the composite extractant after demethanolization, and described composite extractant is glycerol, water, potassium hydroxide mixed solvent, and its mass ratio is 9 / 0.9 / 0.1. The flow rate is 15Kg / h, wherein the S entering the extraction kettle I 1 =7.5Kg / h, the raffinate phase R obtained after stirring for 0.5 hour (stirrer shaft speed 100 rpm) and standing for 1 hour 1 (Stream ②, flow rate 4.6Kg / h) enters extraction kettle II, also enters simultaneously also solvent glycerol S 2 =7.5Kg / h, the raffinate phase R obtained after stirring for 0.5 hour (stirrer shaft speed 100 rpm) and standi...

Embodiment 2

[0023] Embodiment 2 is substantially the same as embodiment 1, but the glycerol in the composite extractant is changed into ethylene glycol.

Embodiment 3

[0024] Embodiment 3 is basically the same as Embodiment 1, but has the following changes:

[0025] Glycerol in the composite extractant is changed to pentaerythritol;

[0026] The mass ratio of extractant to raw material is: 1:1;

[0027] The mass ratio of polyol to water and potassium hydroxide is: 8:0.8:0.09.

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Abstract

The invention relates to a compound cross-flow liquid-liquid extraction separation method of a methylal-methanol azeotropic system. The raw material is a methylal-methanol azeotropic mixture, a compound extracting agent is formed by polylol, water and alkali in a certain proportion, and the raw material and the extracting agent carries out two-stage cross-flow liquid-liquid extraction on a methylal-methanol solution under a certain proportion; after layering separation, raffinate contains methylal with higher purity; extractive phases are the compound extracting agent and methanol; the raffinate contains methylal with higher purity and directly serves as product methylal after being distilled through a treating column; after the extractive phases are distilled by a regenerating column to remove the methanol, the compound extracting agent is recycled. The compound extracting agent of the prioritization scheme is the mixture of glycerine, water and potassium hydroxide, and the mass ratio is 9:0.9:0.1. Compared with the traditional methods, the invention has more obvious methanol removing effect, higher product purity, higher recovery ratio and lower energy consumption. Due to the fact that the compound extracting agent can be recycled in the whole process, the production cost is lower, and the environment cannot be polluted.

Description

technical field [0001] The invention relates to a chemical separation method, in particular to a compound cross-flow liquid-liquid extraction separation method of a methylal-methanol azeotropic system Background technique [0002] Methylal has excellent physical and chemical properties, that is, good solubility, low boiling point, and good compatibility with methanol, and can be widely used in cosmetics, medicines, household products, industrial automotive supplies, insecticides, leather polishes, cleaning agents In the rubber industry, paint, ink and other products, because methylal has good degreasing ability and volatility, it can replace F11 and F113 and chlorinated solvents as a cleaning agent, so it is a substitute for Freon and reduces volatile organic compounds ( VOCs) emissions, environmental protection products that reduce air pollution. The synthetic method of methylal mainly contains dichloromethane method, dimethyl sulfoxide method, calcium chloride method, aci...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C41/58C07C43/303
Inventor 林军顾正桂陈远新冯佳佳吴旋
Owner NANJING NORMAL UNIVERSITY