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Cu/ZrO2 catalyst as well as preparation method and use of Cu/ZrO2 thereof

A catalyst and four-way technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, cyanide reaction preparation, etc., can solve the problem of unsatisfactory catalytic effect of catalyst, difficult control of reduction degree, increase of catalyst cost, etc. Achieve the effects of low raw material prices, easy control of reduction degree, and short preparation time

Inactive Publication Date: 2017-12-08
XIANGTAN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Chinese patent CN101733100A (2009), CN1398850A (2003) and U.S. patent US5292936 (1994), the Cu / ZrO 2 A small amount of nickel, molybdenum, cobalt, vanadium, titanium, etc. are added to the catalyst to form a composite catalyst, which effectively improves the service life of the catalyst. The yield of iminodiacetic acid is about 95%, but adding precious metals increases the cost of the catalyst
[0005] Existing methods for preparing Cu-based catalysts usually start from H 2 Reducing its CuO precursor, this process consumes high energy, takes a long time to reduce, and the degree of reduction is not easy to control, which leads to unsatisfactory catalytic effect of the catalyst

Method used

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  • Cu/ZrO2 catalyst as well as preparation method and use of Cu/ZrO2 thereof
  • Cu/ZrO2 catalyst as well as preparation method and use of Cu/ZrO2 thereof
  • Cu/ZrO2 catalyst as well as preparation method and use of Cu/ZrO2 thereof

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] A Cu / ZrO 2 Catalyst, Cu particles are spherical, with a diameter of 1-4 μm, loaded on sheet-like tetragonal ZrO 2 on the carrier.

[0023] The three valence states of Cu in the catalyst are Cu 0 、Cu + 、Cu 2+ , the molar ratio is 1:0.20~0.35:0.01~0.06.

[0024] A Cu / ZrO 2 Catalyst preparation method:

[0025] (1) Stir and mix the copper salt solution and the zirconium salt solution at a volume ratio of 1:2, slowly add 0.8-1.0mol / L alkali solution dropwise until the pH value of the mixed solution is 11-12, and let it stand for 4-2 After 6 hours, wash and filter with water, put the filter cake in a constant temperature drying oven at 90-110°C and dry it for 10-12 hours, grind it into powder, heat it up to 550°C at 2°C / min, and roast it for 4 hours. After cooling, CuO / ZrO 2 Precursor solid, pulverized to obtain precursor powder;

[0026] (2) Weigh the 10.0gCuO / ZrO 2 The precursor powder was added to 100 mL of 1mol / L NaOH solution, stirred mechanically and heated to...

Embodiment 2~6

[0029] According to the method of embodiment 1, adopt identical preparation method and take the CuO / ZrO of identical weight 2 Precursor powder, just change the amount of hydrazine hydrate to 1mL, 1.5mL, 3mL, 6mL, 12mL respectively, and the prepared catalysts are marked as CZ-1, CZ-1.5, CZ-3, CZ-6, CZ-12. Evaluate using the implementation plan. The catalyst performance evaluation results are shown in Table 1.

[0030] The diethanolamine catalyzed reaction reaction performance result of each catalyst of table 1

[0031]

Embodiment 7

[0033] Weigh the 10.0gCuO / ZrO 2Add the precursor powder to 100mL of 1mol / L NaOH solution, stir mechanically and heat up to 50°C in a water bath, slowly add 1mL of hydrazine hydrate with a mass fraction of 80%, react for 20min, quickly add 200mL of ice water to cool, wash and filter , The filter cake was vacuum-dried at 40° C. for 12 h to prepare the T-20 catalyst. Evaluate using the implementation plan. The performance evaluation results of the catalysts are shown in Table 2.

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Abstract

The invention provides a Cu / ZrO2 catalyst as well as a preparation method and use of the Cu / ZrO2 thereof. According to the preparation method, a Cu / ZrO2 precursor is reduced in alkaline and medium temperature environments by virtue of hydrazine hydrate, the alkaline environment is beneficial to the reducibility of hydrazine hydrate, and the medium temperature environment is beneficial to the acceleration of reduction reaction. By controlling the use amount and reduction time of hydrazine hydrate, the reduction degree of the catalyst is controlled; and by adding ice water, the reduction reaction can be rapidly terminated. According to the preparation method, the Cu / ZrO2 catalyst is prepared in the alkaline and medium temperature environments by virtue of hydrazine hydrate, Cu in the catalyst has three valence states including Cu<0>, Cu<+> and Cu<2+> in a molar ratio of 1 to (0.20-0.35) to (0.01-0.06), and the performance of the catalyst is excellent. The preparation method has the beneficial effects that the time is short, the energy consumption is low, and the reduction degree of the catalyst can be effectively controlled; and the yield of iminodiacetic acid salt prepared from diethanol amine through the catalysis Cu / ZrO2 exceeds 98%, the shortest reaction time is 2.3h, and the Cu / ZrO2 catalyst has good industrial application prospects.

Description

technical field [0001] The invention relates to a copper-based catalyst. Background technique [0002] Iminodiacetic acid prepared by acidification of iminodiacetic acid salt is an important fine chemical raw material, mainly used in the preparation of broad-spectrum insecticide glyphosate. There are two main industrial production routes of glyphosate: glycine route and iminodiacetic acid route. The iminodiacetic acid route is to synthesize iminodiacetic acid first, then react iminodiacetic acid with formaldehyde, phosphorous acid, etc. to form diglyphosate, and then peroxidate diglyphosate to obtain glyphosate. At present, the iminodiacetic acid route is the most advanced method for producing glyphosate in the world, and one of the key points of this route is the preparation of the intermediate product iminodiacetic acid. [0003] Catalysts for the preparation of iminodiacetates from diethanolamine are generally copper-based catalysts. Chinese patent CN101733100A (2009),...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/72B01J35/08B01J37/04B01J37/16C07C227/02C07C229/16
CPCC07C227/02B01J23/72B01J37/04B01J37/16B01J35/40B01J35/51C07C229/16
Inventor 段正康朱宏文尹科张蕾兰小林徐金霞
Owner XIANGTAN UNIV
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