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Palladium-cobalt alloy catalyst and preparation method and application thereof

A kind of alloy catalyst and catalyst technology, which is applied in the direction of catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problems of poor hydrogenation selectivity and low hydrogenation efficiency of catalysts, and achieve The effect of reducing the amount of precious metals and overall cost, improving utilization efficiency and good stability

Pending Publication Date: 2021-06-18
SHANXI LUAN MINING GRP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Commercial hydrogenation catalysts use 0.3% Pd / Al 2 o 3 , there are disadvantages such as poor catalyst hydrogenation selectivity and low hydrogenation efficiency

Method used

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  • Palladium-cobalt alloy catalyst and preparation method and application thereof
  • Palladium-cobalt alloy catalyst and preparation method and application thereof
  • Palladium-cobalt alloy catalyst and preparation method and application thereof

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Experimental program
Comparison scheme
Effect test

Embodiment approach

[0120] 1. A palladium-cobalt alloy catalyst for preparing hydrogen peroxide by anthraquinone hydrogenation, with mesoporous silica as a carrier, the composition of the catalyst uses Pd x co 1-x / SiO 2 It means that the catalyst is prepared by impregnation method, washed, dried and reduced, and the hydrogenation activity test of 2-ethylanthraquinone is carried out under the condition of reaction temperature 30-60°C and the active components are loaded with metal palladium and cobalt. The content of palladium is 0.1-0.5wt%, and the content of cobalt is 0.1-2wt%.

[0121]2. The carrier is shaped mesoporous silica, the shape of the carrier is spherical, and the pore diameter of the catalyst particles is 2-50 nm.

[0122] 3. The specific surface area of ​​the carrier is 100-350m 2 / g, the pore volume is 0.5-1.5ml / g, and the bulk density is 0.6-1.0g / ml.

[0123] 4. Using hydrogen reduction method.

[0124] 5. First, the acidic palladium and cobalt solution is configured as the ...

Embodiment 1

[0128] (1-1) Weigh SiO with an average particle size of 2 μm 2 Powder 21g, concentrated hydrochloric acid 15ml, SiO 2 The mass fraction of 30%wt alkaline silica sol 126g (where SiO 2 The average particle size is 25nm) and 10ml of methanol are fully mixed, and then 15g of hexamethylenetetramine is added to fully dissolve to obtain a mixed slurry;

[0129] (1-2) Select a nozzle with an aperture of 0.25mm and install it on the jet generator, inject the mixed slurry obtained in step (1-1) into 25# transformer oil at 95°C at a speed of 5m / s, and let it stand After aging for 4 hours, the formed pellets were separated from the oil and dried under vacuum at 80°C for 12 hours. The obtained product was washed to neutrality, then dried at 140°C for 10 hours, and calcined at 550°C for 12 hours to obtain micron-shaped spherical silica particles, namely the carrier;

[0130] (1-3) Weigh 1.6800g PdCl 2 (Palladium content is 59.5%) be dissolved in 10ml deionized water and be made into sol...

Embodiment 2

[0137] (2-1) Weigh SiO with an average particle size of 2 μm 2 Powder 21g, concentrated nitric acid 5ml, SiO 2 The mass fraction of 30%wt alkaline silica sol 126g (where SiO 2 The average particle size is 25nm) and 10ml of ethanol are fully mixed, then add 2g (300 mesh) wollastonite and 15g hexamethylenetetramine, fully dissolve, to obtain a mixed slurry;

[0138] (2-2) Select a nozzle with an aperture of 0.25mm and install it on the jet generator, inject the mixed slurry obtained in (2-1) into 25# transformer oil at 90°C at a speed of 5m / s, and let it stand for aging After 4 hours, the formed pellets were separated from the oil and dried under vacuum at 60°C for 24 hours. The obtained product was washed to neutrality, then dried at 140°C for 10 hours, and calcined at 550°C for 12 hours to obtain micron-shaped spherical silica particles, namely the carrier;

[0139] (2-3) Weigh 2.1657g Pd(NO 3 ) 2 (Palladium content is 46.2%) be dissolved in 10ml deionized water and it is...

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Abstract

The invention discloses a palladium-cobalt alloy catalyst. The palladium-cobalt alloy catalyst comprises a carrier and an active component loaded on the carrier, wherein the carrier comprises silicon dioxide; the active component comprises active elements; and the active elements comprise palladium and cobalt. The invention also provides a preparation method of the catalyst. The palladium element can be better dispersed and fixed by adding cobalt, so the utilization efficiency of palladium is improved, and the dosage of noble metal and the overall cost of the catalyst are obviously reduced; and the palladium-cobalt alloy in the catalyst is in a highly-dispersed nano-state, and relatively good stability can be maintained via relatively strong interaction between the palladium-cobalt alloy and the carrier. The catalyst is applied to preparation of hydrogen peroxide through anthraquinone hydrogenation, and has good economic benefits.

Description

technical field [0001] The application relates to a palladium-cobalt alloy catalyst and its preparation method and application, belonging to the field of chemical catalytic materials. Background technique [0002] Hydrogen peroxide is an important inorganic chemical raw material, which is widely used in the synthesis of inorganic and organic intermediates and other chemicals, textiles, medicine, electronics, food and metallurgical industries. The anthraquinone method is currently the most mature and mainstream process for producing hydrogen peroxide. The technological process of the anthraquinone method mainly includes four processes of hydrogenation, oxidation, extraction and post-treatment, among which the hydrogenation process is the core of the whole process. Commercial hydrogenation catalysts use 0.3% Pd / Al 2 o 3 , there are disadvantages such as poor hydrogenation selectivity of the catalyst and low hydrogenation efficiency. The development of low-cost, high-select...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/89B01J37/02B01J37/18C01B15/023
CPCB01J23/8913B01J37/0201B01J37/0205B01J37/18C01B15/023
Inventor 肖伟王树东郭翔苏宏久赵璐严华姜国良李大卫刘重阳杨晓野刘志
Owner SHANXI LUAN MINING GRP