Catalyst for biomass tar cracking and preparation method thereof

A technology for tar cracking and biomass, applied in the field of biomass tar cracking catalyst and its preparation, can solve problems such as reducing process energy consumption and production cost, and achieve the effects of reducing process energy consumption and production cost and high gasification efficiency

Inactive Publication Date: 2018-02-06
桂林市漓江机电制造有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] According to the catalyst for cracking biomass tar and its preparation method provided by the present invention, a biomass synthesis gas catalyst is prepared by compounding biological semi-coke, metal oxides and auxiliary components for microwave pyrolysis gasification of biomass, solving the problem of metal Catalyst deactivation problems such as separation and aggregation of oxides and auxiliary components, coking and ca

Method used

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  • Catalyst for biomass tar cracking and preparation method thereof
  • Catalyst for biomass tar cracking and preparation method thereof

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Embodiment 1

[0014] A catalyst for cracking biomass tar, comprising the following components by weight: 60 parts by weight of semi-coke for biomass, 20 parts by weight of tar, 20 parts by weight of chromium oxide green, 15 parts by weight of copper oxide, cesium hydroxide 10 parts by weight, 8 parts by weight of lithium hydroxide, 8 parts by weight of barium hydroxide, 6 parts by weight of rubidium hydroxide, 5 parts by weight of manganese dioxide, 1 part by weight of nickel oxide, and 1 part by weight of sodium oxide , The alumina binder is 15 parts by weight.

Embodiment 2

[0016] A catalyst for cracking biomass tar, comprising the following components by weight: 75 parts by weight of semi-coke for biomass, 30 parts by weight of tar, 23 parts by weight of chromium oxide green, 16 parts by weight of copper oxide, cesium hydroxide 13 parts by weight, 10 parts by weight of lithium hydroxide, 10 parts by weight of barium hydroxide, 8 parts by weight of rubidium hydroxide, 7 parts by weight of manganese dioxide, 2 parts by weight of nickel oxide, and 2 parts by weight of sodium oxide , The alumina binder is 20 parts by weight.

Embodiment 3

[0018] A catalyst for cracking biomass tar, comprising the following components by weight: 90 parts by weight of semi-coke for biomass, 40 parts by weight of tar, 26 parts by weight of chromium oxide green, 18 parts by weight of copper oxide, cesium hydroxide 16 parts by weight, 12 parts by weight of lithium hydroxide, 13 parts by weight of barium hydroxide, 10 parts by weight of rubidium hydroxide, 8 parts by weight of manganese dioxide, 3 parts by weight of nickel oxide, and 3 parts by weight of sodium oxide , The alumina binder is 25 parts by weight.

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Abstract

The invention relates to a catalyst for biomass tar cracking and a preparation method thereof. The catalyst is prepared from biomass semicoke, tar, chromium oxide green, copper oxide, cesium hydroxide, lithium hydroxide, barium hydroxide, rubidium hydroxide, manganese dioxide, nickel oxide, sodium oxide, and alumina binder. The invention solves the problem of catalyst inactivation, such as separation and aggregation of metal oxides and auxiliary components and coking and carbon deposition, and realizes the recycling of biological semicoke catalysts, using the biomass pyrolysis catalyst to assist microwaves to pyrolyze and gasify biomass can obtain a high gasification efficiency and high-quality synthetic gas product under low temperature, exogenous gas, such as vapor, is not introduced forconsumption into the whole process, and therefore the energy consumption and production cost of the process are remarkably reduced.

Description

technical field [0001] The invention belongs to the technical field of energy saving and environmental protection, and in particular relates to a catalyst for cracking biomass tar and a preparation method thereof. Background technique [0002] Biomass pyrolysis liquefaction is to directly pyrolyze biomass under the conditions of medium temperature (500-650°C), high heating rate (104-105°C / s) and extremely short gas residence time (<2s). Cooling allows intermediate liquid product molecules to condense before further fragmentation to gas, resulting in high yields of biomass liquid oils. However, the common problem of existing biomass cracking technology is that the catalyst is difficult to recycle and reuse, and in order to improve H2 / CO, a large amount of water vapor is consumed, energy consumption and gas consumption are increased, and the process economy is not high. Contents of the invention [0003] In view of the problems existing in the prior art, the invention pr...

Claims

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Application Information

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IPC IPC(8): B01J31/32C10B53/00C10G1/00
CPCB01J31/32C10B53/00C10G1/00C10G2300/1011
Inventor 方杰敏
Owner 桂林市漓江机电制造有限公司
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