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A red brick powder-supported nickel catalyst for cracking and reforming of biomass tar and its preparation method

A technology for tar cracking and red brick powder is applied in the field of red brick powder-supported nickel catalyst and preparation, and can solve the problems of complicated preparation process, expensive nickel-based catalyst and the like

Active Publication Date: 2021-04-23
HUAIYIN INSTITUTE OF TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the catalyst prepared by loading nickel with these substances has good tar removal effect, it will be rapidly deactivated under high temperature conditions. Expensive and complex preparation process

Method used

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  • A red brick powder-supported nickel catalyst for cracking and reforming of biomass tar and its preparation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035]This example uses the red brick powder manufactured by Huaan Industry and Trade Co., Ltd. in Xintai City, Shandong Province as the catalyst carrier, including the following steps: sieving the collected red brick powder, and taking the red brick powder with a particle size of 200 to 400 mesh as the catalyst Carrier, put the selected red brick powder into ultra-pure water and rinse continuously until the cleaning solution is free of turbidity, dry the red brick powder with impurities removed in a temperature environment of 110°C for 12 hours, and immerse 20g of the dried red brick powder in the containing 0.02 mol nickel nitrate solution for 12 hours, then the red brick powder soaked in the nickel nitrate solution was dried for 12 hours at a temperature of 110°C, and the dried red brick powder loaded with nickel nitrate was placed in a protective gas atmosphere at a temperature of 500°C Under heating for 10min. The catalyst prepared by the above method has a specific surfa...

Embodiment 2

[0039] This example uses the red brick powder manufactured by Huaan Industry and Trade Co., Ltd. in Xintai City, Shandong Province as the catalyst carrier, including the following steps: sieving the collected red brick powder, and taking the red brick powder with a particle size of 200 to 400 mesh as the catalyst Carrier, put the selected red brick powder into ultra-pure water and rinse continuously until the cleaning solution is free of turbidity, dry the red brick powder with impurities removed in a temperature environment of 110°C for 12 hours, and immerse 20g of the dried red brick powder in the containing 0.04 mol nickel nitrate solution for 12 hours, then the red brick powder soaked in the nickel nitrate solution was dried for 12 hours at a temperature of 110°C, and the dried red brick powder loaded with nickel nitrate was placed in a protective gas atmosphere at a temperature of 500°C Under heating for 10min. The catalyst prepared by the above method has a specific surf...

Embodiment 3

[0043] This example uses the red brick powder manufactured by Huaan Industry and Trade Co., Ltd. in Xintai City, Shandong Province as the catalyst carrier, including the following steps: sieving the collected red brick powder, and taking the red brick powder with a particle size of 200 to 400 mesh as the catalyst Carrier, put the selected red brick powder into ultra-pure water and rinse continuously until the cleaning solution is free of turbidity, dry the red brick powder with impurities removed in a temperature environment of 110°C for 12 hours, and immerse 20g of the dried red brick powder in the containing 0.06 mol nickel nitrate solution for 12 hours, then the red brick powder soaked in the nickel nitrate solution was dried for 12 hours at a temperature of 110°C, and the dried red brick powder loaded with nickel nitrate was placed in a protective gas atmosphere at a temperature of 500°C Under heating for 10min. The catalyst prepared by the above method has a specific surf...

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Abstract

A method for preparing a red brick powder-supported nickel catalyst for pyrolysis and reforming of biomass tar, comprising the following steps: 1) using red brick powder as a raw material and sieving it; 2) removing the surface of the sieved red brick powder Impurities; 3) Dry the red brick powder that removes impurities; 4) Soak the dried red brick powder in nickel nitrate solution, and ensure that all raw materials are immersed in nickel nitrate solution; 5) After soaking in nickel nitrate solution 6) heating the dried red brick powder impregnated with nickel nitrate in an electric heating furnace under the atmosphere of protective gas, so as to obtain the red brick powder supported nickel catalyst. Known by above-mentioned method, a kind of red brick powder loaded nickel catalyst and preparation method for cracking and reforming of biomass tar, have obtained the red brick powder loaded nickel catalyst with efficient biomass tar cracking and reforming, is the effective catalyst of biomass tar. Removal provides a new way.

Description

technical field [0001] The invention relates to the field of catalytic utilization of biomass resources, in particular to a red brick powder-supported nickel catalyst for cracking and reforming of biomass tar and a preparation method thereof. Background technique [0002] The excessive exploitation and use of traditional fossil energy has made the problems of energy shortage and environmental pollution more and more serious. Developing and searching for new alternative energy sources has become one of the major problems to be solved urgently in human society. Biomass energy is considered to be the most important alternative energy source in the future because of its abundant reserves, low pollution and renewable characteristics. [0003] Pyrolysis or gasification of biomass as raw material to obtain synthesis gas (H 2 +CO) is an important chemical raw material. Syngas can be used to synthesize a variety of chemical products, such as synthetic ammonia, hydrocarbon refining ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/78C10G11/04C10G11/02C01B3/26
CPCB01J23/002B01J23/78B01J2523/00C01B3/26C10G11/02C10G11/04B01J2523/13B01J2523/22B01J2523/31B01J2523/41B01J2523/842B01J2523/847
Inventor 董庆李相前张金峰周佳时号仲娃
Owner HUAIYIN INSTITUTE OF TECHNOLOGY