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A preparation method of a sol-gel catalyst for deep removal of a small amount of hydrogen in industrial CO gas

A technology of sol-gel and catalyst is applied in the field of preparation of sol-gel catalyst to achieve the effects of superior catalytic performance, solving purification problems and simple preparation process

Active Publication Date: 2011-12-21
贵州鑫醇科技发展有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] So far, most of the noble metal catalysts are still prepared by impregnating the active components of the noble metal on the carrier, but the catalyst prepared by this method is not evenly loaded , the amount of precious metals is high, and the active components are easy to agglomerate, which virtually increases the production cost of the entire process

Method used

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  • A preparation method of a sol-gel catalyst for deep removal of a small amount of hydrogen in industrial CO gas
  • A preparation method of a sol-gel catalyst for deep removal of a small amount of hydrogen in industrial CO gas

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example 1

[0022] Weigh 44.8 g of aluminum isopropoxide and grind it into powder with a mortar, put it into a pre-washed and dried beaker, add about 800 g of deionized water, put it in a heat-collecting water bath, and hydrolyze it at 80 °C for 3 h, and the hydrolysis is complete After evaporating the water to dryness, add 55.2 ml of dilute nitric acid (1 mol / L), stir evenly, add about 750 g of deionized water, and seal and age the solution at 80 ℃ for 18 h to obtain a clear sol solution. Dissolve 0.078 g of palladium chloride in 8 ml of dilute hydrochloric acid (1 mol / L) to prepare a chloropalladium acid solution. The chloropalladium acid solution was dropped into the sol, stirred evenly for 1 h, and evaporated at 90 °C for 8 h to get the catalyst precursor. The precursor was put into an oven for two stages of drying at 80 °C and 120 °C, then placed in a muffle furnace for 5 h at 350 °C and cooled to room temperature to obtain the desired dehydrogenation catalyst. Take 10 ml of catalys...

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Abstract

The invention discloses a preparation method of a sol-gel catalyst for deeply removing a little H2 in industrial CO synthetic gas through selective oxidation reaction, and a related process. The method comprises the following steps of: dissolving palladium chloride serving as a palladium source in hydrochloric acid solution with certain concentration, and adding aluminum isopropoxide, water and nitric acid in a certain ratio to form sol at a certain temperature; and gelatinizing the sol at a certain temperature to form gel, and drying and roasting at a certain temperature to obtain the required catalyst. The catalyst prepared by the method has the advantages that: active ingredients are uniformly distributed, the using amount of noble metal palladium salt is reduced, reaction conditions are mild, the phenomena of violent heat release and temperature runaway are avoided, the catalyst has superior performance, the H2 in the industrial CO synthetic gas can be removed to be less than 100ppm, and the requirement on the purity of the CO gas in a carbonyl synthesis process can be effectively met.

Description

technical field [0001] The invention relates to a method for deep removal of a small amount of H in industrial CO gas 2 The preparation method of the sol-gel catalyst and the related process. Background technique [0002] In recent years, the preparation of various bulk chemicals such as methanol, olefins, aromatics, formaldehyde, acetic anhydride, paraformaldehyde, dimethyl ether, ethylene glycol, and mixed alcohols has become a domestic and foreign One of the hotspots of research. [0003] Among them, coal-to-ethylene glycol is an emerging technology in the field of coal chemical industry. Combined with the current situation of my country's lack of oil, less gas and relatively rich coal resources, this technology has significant economic and social benefits. The process route mainly has three reaction steps: (1) Coal-to-water gas is separated by pressure swing adsorption to obtain CO raw material gas; (2) CO catalytic coupling is used to synthesize oxalate; (3) oxalate...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/44C01B31/18C01B32/40
Inventor 姚元根乔路阳周张锋崔国静潘鹏斌林凌覃业燕李兆基
Owner 贵州鑫醇科技发展有限公司
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