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Method for preparing carrier of cyclohexanone catalyst through cyclohexanol dehydrogenation and application

A technology of catalyst carrier and cyclohexanone, which is applied in the direction of catalyst carrier, chemical instrument and method, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problems of low selectivity and low activity, and achieve cyclohexanone The effect of high selectivity, high conversion rate and reasonable pore structure

Inactive Publication Date: 2018-11-02
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although there are many studies on low-temperature cyclohexanol dehydrogenation catalysts, CuO / ZnO catalysts are still widely used in domestic industrial plants. However, compared with copper-silicon catalysts, this catalyst has problems such as low activity and low selectivity.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] In a precipitation tank with stirring, co-precipitate 1M sodium carbonate solution and JA-25 silica sol, at a temperature of 50°C, the pH value of the end point of the precipitation is 10, age at a temperature of 60°C for 30min, and wash , drying, granulation, and tablet molding to obtain a semi-finished carrier. The carrier was roasted at 650°C for 4 hours, and then the carrier was treated in water at 160°C for 1 hour, and then a strong acid was added therein, and the acid concentration was adjusted to 0.5% by weight. %, soaked at 70°C for 2.0 hours, washed, separated, and dried to obtain carrier A. The specific surface area of ​​the carrier is 228.3m 2 / g, the pore volume is 0.35ml / g, and the average pore diameter is 4.7nm.

Embodiment 2

[0020] In a precipitation tank with stirring, co-precipitate 1M sodium carbonate solution and JA-30 type silica sol, at a temperature of 70°C, the pH value of the end point of the precipitation is 9.0, age at a temperature of 70°C for 20min, and wash , drying, granulation, and tablet molding to obtain a semi-finished carrier. The carrier was roasted at 680°C for 5 hours, and then the carrier was treated in water at 180°C for 2 hours, and then a strong acid was added therein to adjust the acid concentration to 1.2% by weight. %, soaked at 80°C for 2 hours, washed, separated, and dried to obtain carrier B. The specific surface area of ​​the carrier is 356..7m 2 / g, the pore volume is 0.42ml / g, and the average pore diameter is 4.6nm.

Embodiment 3

[0022] In a precipitation tank with stirring, co-precipitate 1M nitric acid solution and JN-25 silica sol. At a temperature of 60°C, the pH value of the end point of the precipitation is 6.0, and age at a temperature of 90°C for 10 minutes. After washing, Drying, granulation, and tablet molding to obtain a semi-finished carrier, roast the carrier at 750°C for 3 hours, then treat the carrier in water at 200°C for 4 hours, then add strong acid to it, and adjust the acid concentration to 2% by weight , soaked at 80°C for 2 hours, washed, separated, and dried to obtain carrier C. The specific surface area of ​​the carrier is 456.1m 2 / g, the pore volume is 0.85ml / g, and the average pore diameter is 5.2nm.

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PUM

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Abstract

The invention belongs to the technical field of preparation of catalysts, and provides a method for preparing a carrier of a cyclohexanone catalyst through cyclohexanol gas phase dehydrogenation and application of the carrier in preparation of the catalyst. The prepared catalyst can effectively reduce the generation of a by-product, namely cyclohexene. The catalyst provided by the invention adoptsCu2O / SiO2 as a major component, an active additive is added to improve the acid site of the surface of the catalyst, and the catalyst has the characteristics of high activity and high selectivity.

Description

technical field [0001] The invention belongs to the technical field of catalysts, and in particular relates to a method for preparing a carrier of a catalyst for gas-phase dehydrogenation of cyclohexanol to cyclohexanone, and a catalyst prepared by using the carrier. Background technique [0002] Cyclohexanone is an important organic chemical raw material. The production methods of cyclohexanone mainly include phenol hydrogenation, cyclohexanol dehydrogenation and cyclohexanol oxidation. The dehydrogenation method is widely used in industrial production because of its relatively few by-products, simple operation, and high yield. [0003] The early cyclohexanol dehydrogenation catalyst used in the industry was red iron oxide, which was later replaced by zinc-based catalysts. Due to the high operating temperature of zinc-calcium catalysts, the selectivity of the product cyclohexanone is poor, the energy consumption is large, and the utilization rate of raw materials is not goo...

Claims

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Application Information

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IPC IPC(8): B01J32/00B01J21/08B01J35/10B01J23/72
CPCB01J21/08B01J23/72B01J35/615B01J35/635B01J35/633B01J35/647
Inventor 孙中华张皓殷玉圣袁浩然吴结华
Owner CHINA PETROLEUM & CHEM CORP