Unsaturated acetal preparation method

An unsaturated and acetal technology, which is applied in the field of preparation of high boiling point unsaturated acetal, can solve the problems of increased side reactions, strong corrosion of lithium chloride, high cost, etc., to achieve increased reaction rate, stable process state, and equipment requirements low effect

Active Publication Date: 2014-09-17
WANHUA CHEM GRP CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] 1. Because the consumption of nitric acid is few, the concentration distribution of nitric acid in the reaction tower is difficult to measure;
[0006] 2. Nitric acid will first be enriched at the top of the tower, and then the concentration of nitric acid in the entire reactor will increase, resulting in too high acidity in the bottom of the tower, increased side reactions, and the quantitative maintenance of nitric acid in the entire reaction system is very difficult;
[0007] 3. The decompression operation has high requirements on equipment and process, and the cost is high
Its disadvantages are: the lithium chloride used is highly corrosive and the reaction is carried out under negative pressure conditions, which is not convenient for continuous production and energy saving
[0011] In another patent US5177265A, RHONE POULENC discloses that phosphoric acid is used as a catalyst for condensation reaction, and toluene is added as a solvent to form an azeotrope with water. The reaction temperature is 60-90°C and the pressure is 8000-14000Pa (absolute pressure). The conversion rate of prenaldehyde is 83%, and the yield of acetal is 75.6%. The disadvantage is that after the reaction, the excess acid needs to be neutralized by potassium acetate, sodium acetate, carbonate or hydroxide.
[0012] The existing process for preparing unsaturated acetal is generally carried out under negative pressure conditions, the process control is complicated, and the requirements for equipment are high. At the same time, the temperature of the reactor is high and the energy consumption is large.
Phosphoric acid and lithium chloride are used as catalysts for cumbersome post-treatment. Although nitric acid is used as a catalyst, there are certain advantages, but due to the small amount of use, it is difficult to measure the distribution of nitric acid content in the rectification tower and it is difficult to maintain a constant value.

Method used

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  • Unsaturated acetal preparation method
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  • Unsaturated acetal preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0061] The tower reactor is a rectification tower with an inner diameter of 25mm, a 0.5m Raschig ring filler is installed on the top, and a 0.5m carboxylic acid type acidic ion exchange resin (ion exchange resin produced by Liaoning Dandong Mingzhu Special Resin Co., Ltd.) is installed in the middle. D113), the lower end is filled with Raschig ring packing with a height of 0.5m, and the number of effective trays is 23. A condenser and an oil-water separator are installed on the top of the rectification column. First, cyclohexane is pumped into the gas generator to prepare cyclohexane vapor at 85°C and 115KPa, which is passed into the rectification tower to preheat the reaction system. Prenol and prenyl aldehyde are dosed according to a mass ratio of 2.5:1 (molar ratio is 2.44:1), and mixed uniformly to obtain a reaction liquid. When the temperature at the top of the tower is greater than 82°C, add the reaction liquid to the fixed-bed reactor equipped with carboxylic acid-type...

Embodiment 2

[0063] The above-mentioned carboxylic acid type acidic ion exchange resin filler is changed into heteropolyacid catalyst and repeats above-mentioned experiment, and the content of acetal is 74.62wt% in the extraction liquid of tower still, and prenaldehyde content is 2.08wt%, prenol Content is 20.42wt%, and the content of cyclohexane is 0.84wt%, and other impurity content is 2.04wt%, and this illustrates that the conversion ratio of prenaldehyde is 93.15%, and 3-methyl-2-butene-1-aldehyde The selectivity to di-isopentenyl acetal was 93.04%.

Embodiment 3

[0065] The reaction device is a rectifying tower with an internal diameter of 25mm, a 0.3m Raschig ring filler is installed on the top, and a 1m carboxylic acid type acidic ion-exchange resin (ion-exchange resin D113 produced by Liaoning Dandong Mingzhu Special Resin Co., Ltd.) is installed in the middle. The lower end is filled with Raschig ring packing with a height of 0.2m, and the number of effective trays is 12. The top of the tower is equipped with a condenser and an oil-water separator. First, pump 1,2-dichloroethane into the gas generator to prepare 1,2-dichloroethane vapor at 85°C and 105.19KPa, and pass it into the rectification tower to preheat the reaction system . 2-Methyl-3-buten-2-ol and prenal are dosed according to a mass ratio of 2.5:1 (molar ratio is 2.44:1), and mixed evenly. When the temperature at the top of the tower is higher than 80°C, add the reaction liquid to the fixed-bed reactor equipped with carboxylic acid type acidic ion exchange resin, prehe...

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Abstract

The present invention discloses an unsaturated acetal preparation method. According to the preparation method, an unsaturated alcohol and an unsaturated aldehyde are subjected to a reaction in a pre-reactor to achieve a thermodynamic equilibrium, and then enter a tower type reactor, a water carrying agent is subjected to gasification through a gas generator, and then is subjected to reverse contact with a reaction liquid, and the water generated from the reaction is removed, such that the unsaturated alcohol and the unsaturated aldehyde are subjected to a continuous condensation reaction to prepare the unsaturated acetal. The preparation method has the following characteristics that: the method can be performed under a normal pressure condition, the reaction temperature is constant, low cost synthesis of the unsaturated acetal can be achieved, particularly 3-methyl-2-buten-1-ol and 3-methyl-2-butenal can be adopted as raw materials to synthesize 3-methyl-2-butenal-1 diisopentenyl acetal, wherein the compound is an important intermediate of a synthetic perfume citral.

Description

technical field [0001] The invention relates to a preparation method of unsaturated acetal, in particular to a preparation method of high boiling point unsaturated acetal. Background technique [0002] Unsaturated acetal is an important intermediate in the synthesis of plastics, spices and vitamins, usually using nitric acid, phosphoric acid or lithium chloride as a catalyst, and is produced by reactive distillation under negative pressure conditions. The relevant patents are as follows: [0003] BASF adopts nitric acid (concentration is 1×10 -6 ~1 wt%) is used as a catalyst to carry out the reaction at a reaction pressure of 2-200 mmHg (absolute pressure) and a temperature of 15-100°C. The solution of unsaturated alcohol, unsaturated aldehyde and nitric acid is added to the reaction system from the middle of the tower, the water generated by the reaction is removed through the oil-water separator, the organic phase is refluxed, and the acetal generated by the reaction accu...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C43/303C07C41/56
Inventor 刘英俊张永振崔乐超郑素娟石玉李乐乐黎源华卫琦
Owner WANHUA CHEM GRP CO LTD
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