Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Method for catalytically oxidizing cyclohexane

A cyclohexane and catalyst technology, applied in the field of catalytic oxidation of cyclohexane, can solve the problems of low conversion rate of cyclohexane, poor selectivity, clogging, etc., and achieves the effects of good regeneration performance, easy control, and increased diffusion speed.

Active Publication Date: 2011-06-01
CHINA PETROLEUM & CHEM CORP +1
View PDF2 Cites 23 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, some by-products will react with cobalt ions to form slag, which will be deposited on the inner wall of the equipment pipeline and cause blockage
[0007] In the research report of using ordinary titanium silicon molecular sieve as catalyst and hydrogen peroxide as oxidant to prepare cyclohexanone by oxidation of cyclohexane, the conversion rate of cyclohexane is low and the selectivity is poor.

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Weigh 4g of hollow titanium-silicon molecular sieve HTS and put it in a 250ml three-neck glass bottle, and then add 0.74mol (80ml) cyclohexane and 0.6mol 28% (80ml) hydrogen peroxide to the container successively. The three-neck glass bottle was placed in a constant temperature oil bath with a temperature controlled at 80°C, and the oil bath was placed on a temperature-controlled magnetic stirrer. Start the magnetic stirring and start the reaction.

[0031] After reacting for 6 hours, the conversion rate of cyclohexane was 9.6%, and the selectivity of cyclohexanone and cyclohexanol reached 86.1%.

Embodiment 2

[0033] Weigh 4g of hollow titanium-silicon molecular sieve HTS and put it in a 250ml three-necked glass bottle, and then add 100ml of tert-butanol, 0.19mol of cyclohexane (about 20ml) and 0.15mol of 28% (together 20ml) hydrogen peroxide into the container in sequence. The three-neck glass bottle was placed in a constant temperature oil bath with a temperature controlled at 70°C, and the oil bath was placed on a temperature-controlled magnetic stirrer. Start the magnetic stirring and start the reaction.

[0034] After reacting for 6 hours, the conversion rate of cyclohexane was 9.1%, and the selectivity of cyclohexanone and cyclohexanol reached 82.6%.

Embodiment 3

[0039] Weigh 4g of hollow titanium-silicon molecular sieve HTS and put it in a 250ml three-necked glass bottle, and then add 100ml of tert-butanol, 0.19mol of cyclohexane (about 20ml) and 0.15mol of 28% (together 20ml) hydrogen peroxide into the container in sequence. The three-neck glass bottle was placed in a constant temperature oil bath with a temperature controlled at 80°C, and the oil bath was placed on a temperature-controlled magnetic stirrer. Start the magnetic stirring and start the reaction.

[0040] After reacting for 6 hours, the conversion rate of cyclohexane was 17.9%, and the selectivity of cyclohexanone and cyclohexanol reached 82.6%.

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
lengthaaaaaaaaaa
adsorption capacityaaaaaaaaaa
lengthaaaaaaaaaa
Login to View More

Abstract

The invention discloses a method for catalytically oxidizing cyclohexane, which is characterized in that cyclohexane, hydrogen peroxide and a catalyst are in contact for reacting, the mol ratio of the cyclohexane to the hydrogen peroxide is 0.5-8, the concentration of the catalyst in a reaction system is 0.005-0.1g / min, the reaction temperature is 40-150 DEG C, the catalyst is a titanium-silicon molecular sieve with an MFI structure, a hysteresis loop exits between an adsorption isotherm and a desorption isotherm of low-temperature nitrogen absorption of the molecular sieve, a crystalline grain is a single hollow crystalline grain or an aggregated crystalline grain formed by the aggregation of a plurality of hollow crystalline grains, the radial length of the cavity part of the hollow crystalline grains is 5-300nm, and the benzene adsorption capacity of the sample of the molecular sieve, measured under the conditions that the absorption time is 1h, the temperature is 25 DEG C and P / P0 is equal to 0.10, is at least 70mg / g. The method has the advantages of high selectivity of a target product and environment protection.

Description

technical field [0001] The invention relates to a method for catalytically oxidizing cyclohexane with titanium-silicon molecular sieve as catalyst and hydrogen peroxide as oxidant. Background technique [0002] Cyclohexanone and cyclohexanol are important chemical raw materials, widely used in the industries of fiber, synthetic rubber, industrial coating, medicine, pesticide and organic solvent. Especially due to the rapid development of the polyamide industry, the demand for cyclohexanone and cyclohexanol as intermediates for the preparation of nylon 6 and nylon 66 is more than 1 million tons per year all over the world. There are three main production process routes of cyclohexanone: cyclohexane liquid-phase oxidation method, phenol hydrogenation method and benzene partial hydrogenation method, among which cyclohexane oxidation method is the main process of industrial production of cyclohexanone, accounting for more than 90% , but the process is also considered to be one ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): C07C49/403C07C35/08C07C27/16C07C45/28C07C29/48B01J29/89
Inventor 林民刘郁东朱斌史春风汝迎春
Owner CHINA PETROLEUM & CHEM CORP
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products