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Hydrogenolysis method of cyclohexyl hydroperoxide

A technology of cyclohexyl hydroperoxide and cyclohexane oxidation solution, which is applied in chemical instruments and methods, preparation of carbon-based compounds, preparation of organic compounds, etc., can solve cyclohexyl hydroperoxide decomposition with low selectivity and alkaline wastewater Environmental pollution, catalyst activity reduction and other problems, to achieve the effect of reducing catalyst consumption, less catalyst consumption, increasing conversion rate and

Inactive Publication Date: 2015-02-04
SHANGHAI HONGLU CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the following problems exist in the decomposition process of cyclohexyl hydroperoxide: high production energy consumption, low selectivity of cyclohexyl hydroperoxide decomposition, obvious polycondensation of cyclohexanone, and adding a large amount of alkali in the production, generating a large amount of alkaline wastewater and polluting surroundings
The reaction condition requirement of this method is higher, and the requirement to equipment is also higher; The by-product in the cyclohexane oxidation preparation cyclohexyl hydroperoxide process is easy to be attached on the hydrogenation catalyst surface, causes the activity of catalyst to reduce; Alcohol and ketone The total yield is not high at 92%

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] Under normal pressure, in a three-necked flask with a volume of 1000ml, add 700ml of cyclohexane non-catalytic oxidation solution containing cyclohexyl hydroperoxide and 70ml of desalted water, stir and wash with water at 75°C for 0.25h. Afterwards, the organic phase and the inorganic phase are liquid-liquid separated. Take 500 g of the separated organic phase after washing with water, add 5 g of Pd / Al catalyst with a palladium content of 1% and a particle diameter of 100 um, pass in hydrogen, and react for 0.5 h at a temperature of 95 ° C and a pressure of 0.5 Mpa to hydrogenate the ring Hexyl hydroperoxide; add 10% sodium hydroxide aqueous solution to the reaction liquid after hydrogenation, stir for alkali washing, the temperature of alkali washing is 70°C, and the volume ratio of alkali liquid to reaction liquid is 1:30; The final reaction solution was added with desalted water, stirred and washed with water at a temperature of 70° C., and the ratio of water to the ...

Embodiment 2

[0022] Under normal pressure, add 700ml of cyclohexane non-catalytic oxidation solution containing cyclohexyl hydroperoxide and 20ml of desalted water into a three-necked flask with a volume of 1000ml, stir and wash with water at 80°C for 1 hour. , the liquid-liquid separation of the organic phase and the inorganic phase. Take 500g of the organic phase separated after washing with water, add 2.5g of Pd / Al catalyst with a palladium content of 1% and a particle diameter of 500um, pass in hydrogen, and react for 0.5h at a temperature of 90°C and a pressure of 0.45Mpa, and then hydrolyze Cyclohexyl hydroperoxide; add 15% sodium hydroxide aqueous solution to the reaction liquid after hydrogenation, stir for alkali washing, the temperature of alkali washing is 65°C, and the volume ratio of alkali liquid to reaction liquid is 1:20; The final reaction solution was added with desalted water, stirred and washed with water at a temperature of 65° C., and the ratio of desalted water to th...

Embodiment 3

[0025] Under normal pressure, in a three-necked flask with a volume of 1000ml, add 700ml of cyclohexane non-catalytic oxidation solution containing cyclohexyl hydroperoxide and 50ml of desalted water, stir and wash with water at 65°C for 0.5h, and the washing is completed Afterwards, the organic phase and the inorganic phase are liquid-liquid separated. Take 500g of the organic phase separated after washing with water, add 2g of Pd / Al catalyst with a palladium content of 5% and a particle diameter of 5-6mm, pass in hydrogen, and react for 0.3h at a temperature of 100°C and a pressure of 0.6Mpa, hydrogenation Decompose cyclohexyl hydroperoxide; add 25% sodium hydroxide aqueous solution to the reaction liquid after hydrogenation, stir for alkali washing, the alkali washing temperature is 65°C, and the volume ratio of alkali liquid to reaction liquid is 1:35; Add desalted water to the reaction solution after washing, stir and wash with water, the washing temperature is 60°C, and ...

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PUM

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Abstract

The invention discloses a hydrogenolysis method of cyclohexyl hydroperoxide and belongs to the technical field of organic chemistry. The method comprises the following specific steps: washing a cyclohexane oxidation solution containing cyclohexyl hydroperoxide, isolating an organic phase, adding a Pd / Al catalyst into the organic phase, introducing hydrogen, reacting at the temperature of 50-120 DEG C and at the pressure of 0.1-1.5 MPa for 0.1-3h, filtering the catalyst, carrying out alkali cleaning by adding 5-30 wt% of alkali lye into the reaction liquid with introduced hydrogen, washing with water after alkali cleaning, carrying out liquid separation after water washing, and collecting the organic phase, wherein mass ratio of the catalyst to the organic phase is 1:10-10000 and diameter of the catalyst is 0.01-10mm. The Pd / Al catalyst is used to catalyze hydrogenolysis of cyclohexyl hydroperoxide; reaction condition is mild; selectivity is high; treatment after the reaction is convenient; dosage of the catalyst is low and the catalyst can be recycled; and conversion rate and selectivity are high.

Description

technical field [0001] The invention relates to the technical field of organic chemistry, in particular to a method for hydrolysis of cyclohexyl hydroperoxide. Background technique [0002] At present, most of the KA oil used in the industrial production of adipic acid is prepared by the non-catalytic air oxidation of cyclohexane. The preparation of KA oil by cyclohexane oxidation includes the following steps: 1) Cyclohexane is heated at 160-180°C , the cyclohexane oxidation liquid whose main product is cyclohexyl hydroperoxide is obtained through air non-catalytic oxidation, and contains about 0.5-0.8% acids and esters; 2) cyclohexyl peroxide in the cyclohexane oxidation liquid Hydrogen oxide decomposes into cyclohexanone and cyclohexanol at a certain alkalinity; 3) Distillation to obtain a mixture of cyclohexanone and cyclohexanol, namely KA oil. At present, the following problems exist in the decomposition process of cyclohexyl hydroperoxide: high production energy consu...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C27/04C07C29/132C07C35/08C07C45/53C07C49/403
CPCY02P20/584C07C29/132C07C45/53C07C2601/14C07C35/08C07C49/403
Inventor 余洪勇王敬松孙伟岳远会康传瑞郭园沈巧香杨志强
Owner SHANGHAI HONGLU CHEM TECH
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