A kind of nickel-based glucose hydrogenation catalyst and preparation method thereof

A hydrogenation catalyst and glucose technology, which is applied in the direction of catalyst activation/preparation, hydroxyl compound preparation, catalyst protection, etc., can solve the problems of flammability, environmental pollution, and poor stability during storage, transportation, and use, and achieve low cost, The effect of shortening the reaction time and stabilizing performance

Active Publication Date: 2022-02-08
CNOOC TIANJIN CHEM RES & DESIGN INST +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Using ruthenium as a catalyst is the mainstream of sorbitol hydrogenation catalysts in the world today. It is a relatively efficient catalyst, but its price is relatively expensive, which limits its use.
However, the Raney Ni catalyst has problems such as poor stability, flammability during storage, transportation and use, and large environmental pollution during the preparation process.

Method used

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  • A kind of nickel-based glucose hydrogenation catalyst and preparation method thereof
  • A kind of nickel-based glucose hydrogenation catalyst and preparation method thereof
  • A kind of nickel-based glucose hydrogenation catalyst and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Example 1 Weigh 25.30g of zirconium nitrate pentahydrate and dissolve it in deionized water to obtain 500mL solution I, weigh 80.85g of sodium metasilicate nonahydrate, 44.28g of sodium carbonate, and add 50.14g of sodium hydroxide into deionized water to obtain 500mL of solution II, weighed 121.0g of nickel nitrate hexahydrate, 24.3g of cobalt nitrate hexahydrate, and 2.0g of polyethylene glycol were dissolved in deionized water to prepare 1000mL of bottom solution. Turn on the stirring, the speed is 650rpm, and the microwave power is 300W, maintain a certain feed rate of solution I and solution II and add it dropwise to the bottom solution, control the pH value of the reaction to 8.0-9.0, and the co-precipitation reaction ends in about 30 minutes. The reaction slurry was aged for 45 minutes. After the aging, the slurry was filtered and washed with water until neutral to obtain a catalyst precursor filter cake.

[0029] Add the filter cake to 2L of deionized water to ...

Embodiment 2

[0033] Embodiment 2 Nickel oxide and nickel are roughly calculated as nickel

[0034]Weigh 25.30g of zirconium nitrate pentahydrate and dissolve it in deionized water to obtain 500mL solution I. Weigh and weigh 80.85g of sodium metasilicate nonahydrate, 37.75g of sodium carbonate, 71.23g of sodium hydroxide, and 34.0g of hexamethylenetetramine. g was added to deionized water to make 1000mL solution II, weighed 241.0g of nickel nitrate hexahydrate, 18.33g of cobalt nitrate hexahydrate, 5.08g of iron nitrate nonahydrate, and 4.0g of polyethylene glycol were dissolved in deionized water to make the bottom solution 1000mL. Turn on the stirring, the rotation speed is 650rpm, and the microwave power is 420W. Maintain a certain feed rate of solution I and solution II and add it dropwise to the bottom solution. The pH value of the reaction is controlled at 8.0-8.5, and the co-precipitation reaction is completed in about 45 minutes. The slurry was reacted for 1 hour. After the aging,...

Embodiment 3

[0039] Weigh 25.30g of zirconium nitrate pentahydrate and dissolve it in deionized water to obtain 500mL of solution I, weigh 50.21g of sodium metasilicate nonahydrate, 71.23g of sodium hydroxide, and add 249.6g of hexamethylenetetramine into deionized water to prepare To obtain 1000 mL of solution II, weigh 241.0 g of nickel nitrate hexahydrate, 18.33 g of cobalt nitrate hexahydrate, 7.62 g of iron nitrate nonahydrate, and dissolve 4.0 g of polyethylene glycol in deionized water to obtain 1000 mL of bottom solution. Turn on the stirring, the rotation speed is 650rpm, and the microwave power is 420W. Maintain a certain feed rate of solution I and solution II and add them dropwise to the bottom solution. The pH value of the reaction is controlled at 8.0-8.5, and the co-precipitation reaction is completed in about 45 minutes. The reaction slurry was aged for 1 hour. After the aging, the slurry was suction filtered and washed until neutral to obtain a catalyst precursor filter ca...

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Abstract

The invention relates to a nickel-based glucose hydrogenation catalyst and a preparation method thereof. The catalyst is composed of main active components nickel and nickel oxide, additives, silicon oxide and zirconium oxide; the content of the main active component nickel is 3-40wt%, and the content of nickel oxide is 35-72%; the content of the auxiliary agent is 0.1-10wt% %; the silicon oxide content is 10-39wt%, and the rest is zirconia; wherein the auxiliary agent is one or both of cobalt and iron. The invention adopts a microwave-assisted co-precipitation method to synthesize the catalyst precursor slurry, and further crystallizes the slurry, then performs drying, roasting and reduction passivation to obtain a glucose hydrogenation catalyst. The particle size distribution of the catalyst prepared by the invention is uniform, and the average particle size is 7-15 μm. The catalyst is used for the hydrogenation reaction of glucose, has high activity, and is safe to use; the preparation method is simple in operation, good in batch preparation repeatability, and low in cost.

Description

technical field [0001] The invention belongs to the field of catalysts, and in particular relates to a novel nickel-based catalyst for hydrogenation of glucose to sorbitol and a preparation method thereof. Background technique [0002] Sorbitol, also known as sorbitol, is an important raw material for medicine, chemical industry, light industry, and food industry, and is widely used in many fields. At present, the production processes of sorbitol in the world mainly include catalytic hydrogenation, electrolytic oxidation, and fermentation. The main processes of catalytic hydrogenation include kettle-type batch hydrogenation, external circulation batch-type hydrogenation and tubular continuous hydrogenation. The kettle-type intermittent hydrogenation production process is a traditional process for producing sorbitol in my country, and it is also a production process that is currently used more. This process generally uses glucose as a raw material, and sorbitol is prepared b...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/755B01J37/03B01J37/10B01J37/18B01J33/00C07C29/141C07C31/26
CPCB01J23/755B01J37/03B01J37/10B01J37/18B01J33/00C07C29/141C07C31/26
Inventor 刘伟陈永生孙春晖许岩张景成孙彦民宋国良
Owner CNOOC TIANJIN CHEM RES & DESIGN INST
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