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Method for preparing 3,3-dimethyl butyraldehyde

A technology of dimethyl butyraldehyde and dimethyl butyl acetate, which is applied in the field of preparation of 3,3-dimethyl butyraldehyde, can solve the problems of long process, low production safety, expensive raw materials, etc. Mild reaction conditions, high production safety, and the effect of shortening the production process

Inactive Publication Date: 2014-11-05
SHANDONG BENYUE BIOTECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] There are many preparation methods for 3,3-dimethylbutyraldehyde: in CN101311151, ethylene gas is used as raw material for preparation, but ethylene gas has higher requirements in terms of transportation, storage, production equipment, etc., and this preparation method flow It is long and consumes a lot of energy. It needs to be obtained by gasifying 3,3-dimethylbutanol and water at a high temperature above 300°C with an inert gas as a carrier gas, and then catalytic dehydrogenation in the presence of precious metals. The production cost High, production safety is low; In the disclosed method of CN1301247A, use 3,3-dimethyl butyl chloride as raw material, raw material cost price is high, and produce the dimethyl sulfide compound of stench in the production process, to environment The pollution is heavy, and the control of this pollution requires higher production costs, and it is not easy to carry out industrial production; in US5994593, it is prepared by hydrolysis of 1,1-dichloro-3,3-dimethylmethane. The disadvantage of this preparation method is that the raw materials are expensive. It is not suitable for large-scale industrial production; in US5856584, it is prepared by oxidation of 1-chloro-3,3-dimethylbutane. The disadvantage of this method is that it uses iodide as a catalyst, which is expensive and difficult to recycle, and the reaction produces foul-smelling di Methyl sulfide by-products, high processing costs

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Vacuumize the closed reaction kettle to -0.8MPa, first feed nitrogen gas, then vent the nitrogen gas, add 20kg of dichloromethane solvent, add 8.6kg of vinyl acetate dropwise, and feed hydrogen chloride gas to make the pressure inside the kettle reach 0.2MPa. Add 9.3 kg of tert-butyl chloride dropwise within 3 hours, control the temperature at -25°C, and react for 8 hours. After the reaction, excess hydrogen chloride gas is absorbed through the falling film absorber, and then the product is rectified, and dichloride is distilled at 40°C Methane, continue to heat up to 105 ° C to distill 1-chloro-3,3-dimethylbutyl acetate;

[0026] Add 21.6kg of water and 1-chloro-3,3-dimethylbutyl acetate into another reactor, add SO 4 2- / ZrO 2 Solid strong acid catalyst, control the temperature to 120°C to hydrolyze and disproportionate 1-chloro-3,3-dimethylbutyl acetate to obtain a hydrolysis and disproportionation reaction mixture containing 3,3-dimethylbutyraldehyde, and continue...

Embodiment 2

[0028] Vacuumize the closed reactor to -0.9MPa, first feed nitrogen, then vent the nitrogen, add 20kg of dichloromethane solvent, add 15.48kg of vinyl acetate dropwise, and feed hydrogen chloride gas to make the pressure in the kettle reach 0.2MPa, and then Add 18.6 kg of tert-butyl chloride dropwise within 4 hours, control the temperature at -23°C, and react for 9 hours. After the reaction, the excess hydrogen chloride gas is absorbed through the falling film absorber, and then the product is rectified, and dichloride is distilled at 40°C Methane, continue to heat up to 106 ° C to distill 1-chloro-3,3-dimethylbutyl acetate;

[0029] Add 43kg of water and 1-chloro-3,3-dimethylbutyl acetate into another reactor, add S 2 o 8 2- / ZrO 2 Solid strong acid catalyst, control the temperature to 120°C to hydrolyze and disproportionate 1-chloro-3,3-dimethylbutyl acetate to obtain a hydrolysis and disproportionation reaction mixture containing 3,3-dimethylbutyraldehyde, and continue t...

Embodiment 3

[0031] Vacuumize the closed reactor to -0.96MPa, first feed nitrogen, then vent the nitrogen, add 20kg of dichloromethane solvent, add 8.2kg of vinyl acetate dropwise, feed hydrogen chloride gas, so that the pressure in the kettle reaches 0.2MPa, and then Add 9.3 kg of tert-butyl chloride dropwise within 5 hours, control the temperature at -20°C, and react for 10 hours. After the reaction, excess hydrogen chloride gas is absorbed through the falling film absorber, and then the product is rectified, and dichloride is distilled at 40°C. Methane, continue to heat up to 108 ° C to distill 1-chloro-3,3-dimethylbutyl acetate;

[0032] Add 21.6kg of water and 1-chloro-3,3-dimethylbutyl acetate into another reactor, add S 2 o 8 2- / ZrO 2 Solid strong acid catalyst, control the temperature to 120°C to hydrolyze and disproportionate 1-chloro-3,3-dimethylbutyl acetate to obtain a hydrolysis and disproportionation reaction mixture containing 3,3-dimethylbutyraldehyde, and continue to d...

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PUM

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Abstract

The invention relates to a method for preparing 3,3-dimethyl butyraldehyde. The method comprises the following steps: (1) vacuumizing a closed reaction kettle, adding a dichloromethane solvent, dripping vinyl acetate, introducing a catalyst after dripping is ended, and introducing hydrogen chloride gas, so that the pressure reaches 0-1MPa, slowly dripping tert butyl chloride for reacting, removing excessive hydrogen chloride gas after the reaction is ended to obtain a distillation product, raising the temperature and distilling to obtain 1-chloro-3,3-dimethyl butyl acetate; and (2) adding the 1-chloro-3,3-dimethyl butyl acetate and water into the reaction kettle, controlling the temperature to be 120 DEG C, performing hydrolysis disproportionation on the 1-chloro-3,3-dimethyl butyl acetate to obtain a hydrolysis disproportionation reaction mixture containing 3,3-dimethyl butyraldehyde, and distilling and purifying to obtain the 3,3-dimethyl butyraldehyde. According to the method disclosed by the invention, the production cost is low, the production process is shortened, the reaction conditions are mild, the production safety is high, and the preparation method is simple in preparation process, easy to control, high in yield and safe.

Description

technical field [0001] The invention relates to a preparation method of 3,3-dimethylbutyraldehyde. Background technique [0002] Neotame (N-[N-(3,3-dimethylbutyl)-L-α-aspartic acid]-L-phenylalanine-1--methyl ester) in the sweetener is derived from The high-power sweetener developed by Newtrathwaite Company of the United States has the advantages of high sweetness, low calorie, high stability, etc., and is safe and harmless to the human body. It is a kind of non-nutritional strong sweetener with excellent performance. Huge market potential, and 3,3-dimethylbutyraldehyde is an important intermediate of neotame. Due to its high market price, the product price cannot be reduced. Therefore, it is necessary to study an economical and specific method for preparing this intermediate . [0003] There are many preparation methods for 3,3-dimethylbutyraldehyde: in CN101311151, ethylene gas is used as raw material for preparation, but ethylene gas has higher requirements in terms of t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C47/02C07C45/00
CPCC07C67/293C07C45/42
Inventor 陈良
Owner SHANDONG BENYUE BIOTECH
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