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Biomass gasification catalytic cracking process and integral gasification catalytic reactor

A catalytic cracking and biomass technology, applied in the field of biomass energy utilization, can solve the problems of gas being burned and easy to block gas pipelines, etc., to avoid sensible heat loss, overcome complex process route problems, and overcome fine carbon particles or flying Difficult to separate gray effect

Inactive Publication Date: 2012-12-05
HUAZHONG NORMAL UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

It overcomes the problem that the existing process method is easy to block the gas pipeline, and the gas produced by the gasification of a large amount of biomass is burned, and at the same time improves the effective component H in the gas. 2

Method used

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  • Biomass gasification catalytic cracking process and integral gasification catalytic reactor
  • Biomass gasification catalytic cracking process and integral gasification catalytic reactor
  • Biomass gasification catalytic cracking process and integral gasification catalytic reactor

Examples

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Effect test

Embodiment 1

[0020]Biomass wood powder is fed into the biomass gasification section 1 of the lower part of the integrated biomass gasification catalytic reactor through the biomass feeding device 7, and the primary gasification agent (air) 4 enters the equal pressure air chamber 2, and then passes through the air distribution The plate 3 enters the biomass gasification section 1, and by controlling the feed rate and the amount of the primary gasification agent 4, when the standard superficial cross-sectional flow velocity of the primary gasification agent in the gasification section is 0.3-0.5m / s, the biomass The temperature of the substance gasification section is controlled at 600-750 for oxidation-reduction reaction to generate flammable gas (referred to as gas) accompanied by the generation of tar, and the generated flammable gas entrains tar and incompletely reacted charcoal Particles flow upwards, through tar catalytic cracking section 8, (cobalt-based composite catalyst is housed in ...

Embodiment 2

[0024] The biomass chaff is fed into the biomass gasification section 1 at the lower part of the integrated biomass gasification catalytic reactor through the biomass feeding device 7, and the primary gasification agent (air) 4 enters the equal pressure air chamber 2, and then passes through the air distribution The plate 3 enters the interior of the biomass gasification section 1, and by controlling the feed rate and the amount of the primary gasification agent 4, the primary gasification agent can be used when the standard superficial cross-sectional flow velocity of the gasification section is 0.3-0.5m / s , under the temperature control of the biomass gasification section, oxidation-reduction reaction occurs at 600-750 ℃, and flammable gas is generated, accompanied by tar formation, and the flammable gas generated entrains tar and incompletely reacted carbon particles to flow upward. After the tar catalytic cracking section 8, under the action of the tar cracking catalyst ...

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Abstract

The invention relates to a biomass gasification catalytic cracking process and an integral gasification catalytic reactor. According to the process, the integral reactor of which the lower part is provided with a biomass gasification section and the upper part is provided with a tar catalytic cracking section is adopted; the biomass gasification section is a fluidized bed, air serving as a primary gasification agent is introduced from the lower part, biomass enters the reactor from the middle-and-lower part to perform oxido-reduction gasification reaction with the gasification agent at the temperature of between 600 and 750 DEG C to generate gas accompanied with tar; the gas accompanied with the tar enters the tar catalytic cracking section on the upper part, the tar catalytic cracking section is a fixed bed into which a tar cracking catalyst is filled, a secondary gasification agent is introduced from the lower lateral part for filling the tar cracking catalyst, and the tar is cracked and converted into small-molecular combustible gas in the tar catalytic cracking section at the catalytic cracking temperature of between 750 and 800 DEG C; and generated ash content is discharged from an ash discharge opening on the lower part of the reactor, and the gas is discharged from a gas outlet on the top of the reactor to enter the next process. By the biomass gasification catalytic cracking process, the problem that the tar is separated from flying ash difficultly in the biomass gasification process is solved, and the gasification efficiency is improved.

Description

technical field [0001] The invention relates to biomass energy utilization technology. It specifically relates to a process and a reactor in which biomass gasification and tar catalytic cracking are carried out in an integrated reactor. technical background [0002] Biomass gasification is one of the most promising methods for large-scale utilization of biomass energy, however, the tar produced during biomass gasification seriously hinders its large-scale application. How to develop a low-tar or no-tar biomass gasification catalytic reactor is the key to solve the above problems. [0003] At present, biomass gasification is divided into two types: fixed bed gasifier reactor and fluidized bed gasifier reactor according to the type of gasifier used, and the fixed bed gasifier reactor is divided into downdraft type and updraft gasifier reactor. There are four types of suction type, horizontal suction type and open heart type; the fluidized bed gasifier reactor is divided into...

Claims

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Application Information

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IPC IPC(8): C10J3/54C10J3/56
Inventor 吴正舜肖少飞陈汉平孙婷婷秦丽刘晓燕
Owner HUAZHONG NORMAL UNIV
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