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Non-noble metal oxide combustion catalyst, and preparation method and use thereof

A technology for burning catalysts and non-precious metals, which is used in catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc. Harsh and other problems, to achieve good catalytic activity and hydrothermal stability, high catalytic activity and hydrothermal stability, beneficial to large-scale production

Inactive Publication Date: 2016-03-09
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] In the Chinese patent (200810110774.4) "a preparation method of a double perovskite methane catalytic combustion catalyst" and the Chinese patent (200810110955.9) "a preparation method of a methane combustion catalyst", the activity of the research is affected by the small specific surface area However, it is limited, the low-temperature catalytic activity is not good, and the process conditions are complicated
Chinese patent (200310118171.6) discloses a preparation method of a metal oxide with a high specific surface area, but the metal oxide is coated on the surface of a carbon carrier by impregnation, but no data on its catalytic combustion performance is given; Chinese patent (2010102686.8) A metal oxide methane combustion catalyst prepared by citric acid complexation method is disclosed. The light-off temperature is higher than 320°C, and the complete conversion temperature is as high as 600°C. This has relatively strict requirements on the material of the reaction equipment, and side reactions will occur , especially for the hydrothermal condition of the combustion process, the stability of the catalyst will be significantly reduced;

Method used

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  • Non-noble metal oxide combustion catalyst, and preparation method and use thereof
  • Non-noble metal oxide combustion catalyst, and preparation method and use thereof
  • Non-noble metal oxide combustion catalyst, and preparation method and use thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0041] Take 15mmol of cobalt nitrate hexahydrate, 1g of polyvinylpyrrolidone (PVP), 80ml of ammonia water (mass concentration is 30%), stir magnetically at room temperature for half an hour, and place this mixture in a 120ml internally agglomerated polytetrafluoroethylene stainless steel for reaction. Seal the kettle and place it in an oven at 80°C for 8h. Then, the reacted sample was subjected to suction filtration, washed with deionized water until neutral, and a filter cake was obtained. The filter cake was placed in an oven at 110 °C and dried for 5 h. The dried sample was placed in a muffle furnace and calcined at 500°C for 2 hours to obtain a combustion catalyst of tricobalt tetroxide, numbered Cat.1.

Embodiment 2

[0043] Take 22.5mmol of cobalt chloride hexahydrate, 60mmol of urea, 0.5000g of cetyl ammonium bromide, add 80ml of deionized water, and stir magnetically at room temperature for half an hour to form a homogeneous solution. Seal it in a tetrafluoroethylene stainless steel reaction kettle, place it in an oven, and keep it at 160°C for 12h. Then, the reacted sample was subjected to suction filtration, washed with deionized water and ethanol until neutral, and a filter cake was obtained. The filter cake was placed in an oven at 80 °C and dried for 8 h. The dried sample was placed in a muffle furnace and calcined at 350°C for 4 hours to obtain a combustion catalyst of tricobalt tetroxide, numbered Cat.2.

Embodiment 3

[0045] Take 20mmol of cobalt sulfate hexahydrate, 60mmol of hexamethylenetetramine, add 1.000g of cetyl ammonium bromide, add 60ml of ethanol, 15ml of deionized water, and stir magnetically at room temperature for half an hour to obtain a uniform solution. Put it in a polytetrafluoroethylene stainless steel reaction kettle with a volume of 120ml and seal it, put it in an oven, and keep it at 120°C for 18h. Then, the reacted sample was subjected to suction filtration, washed with deionized water and absolute ethanol until neutral to obtain a filter cake, which was placed in a vacuum oven at 60° C. and dried for 10 h. Finally, the dried sample was placed in a muffle furnace and calcined at 400°C for 3 hours to obtain a combustion catalyst of tricobalt tetroxide, numbered Cat.3.

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Abstract

The present invention relates to a non-noble metal oxide combustion catalyst and a preparation method and use thereof, and belongs to the technical field of energy utilization and environment protection. The catalyst is iron oxide, cobaltosic oxide, nickel oxide, cupric oxide, vanadium oxide, chrome oxide, manganese dioxide or cerium dioxide prepared according to the following steps: (1) using hydrothermal chemical synthesis to form a precursor of a catalyst; and (b) washing, filtering, shaping, drying and calcinating the obtained precursor of the catalyst, and finally forming a combustion catalyst or coating the precursor of the catalyst on a carrier to form a combustion catalyst. The catalyst prepared by the method can be used in catalytic combustion of methane and other VOC gas, and has the advantages that the synthesis process is simple, the cost is low, the catalytic activity and hydrothermal stability is high, and the light-off temperature and complete combustion temperature of methane are low.

Description

technical field [0001] The invention belongs to the technical field of energy utilization and environmental protection, and in particular relates to a non-noble metal oxide combustion catalyst and its preparation method and application. Background technique [0002] Due to its stable, efficient and clean combustion performance, catalytic combustion is widely used in related industrial processes, such as gas turbines involving catalytic combustion of methane, exhaust gas purification of natural gas fueled vehicles (Catalysis Communications, 2005, 6(5): 329-336.) , coalbed methane treatment process; air purification involving CO catalytic combustion, CO gas sensor and PEMFC fuel cell gas purification (J.Am.Chem.Soc.,2011,133(29):11279-11288.); involving VOCs catalytic combustion VOCs tail gas treatment in petroleum refining and petrochemical, coal processing and conversion processes (Journal of Hazardous Materials, 2004, 109(1-3): 113-139.); [0003] Combustion catalysts have...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/75B01J23/755B01J23/745B01J23/72B01J37/08B01D53/86B01D53/72B01D53/62B01D53/46
Inventor 王树东陈志萍王胜高典楠汪明哲
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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