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Gasification furnace for cooperatively producing methane and light tar

A light tar and gasifier technology, applied in the direction of granular/powdered fuel gasification, etc., can solve the problems of reducing the conversion rate of carbonaceous raw materials and the degree of pyrolysis, insufficient pyrolysis reaction, and low output of light tar , to increase contact time and contact surface area, improve gasification efficiency, and increase contact time

Active Publication Date: 2015-09-09
ENN SCI & TECH DEV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, in actual production, the design of the pyrolysis section in the existing gasification furnace does not make full use of the characteristics of catalytic gasification and pyrolysis, so that the carbonaceous raw materials are not in effective contact with the gasification agent in the pyrolysis section, thereby reducing the The conversion rate and pyrolysis degree of carbonaceous raw materials are reduced, resulting in insufficient pyrolysis reaction, resulting in low yield of coal tar, especially light tar with high economic added value.

Method used

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  • Gasification furnace for cooperatively producing methane and light tar
  • Gasification furnace for cooperatively producing methane and light tar
  • Gasification furnace for cooperatively producing methane and light tar

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] The distributed plate fluidized bed gasifier of the present invention is adopted, wherein the diameter ratio of the pyrolysis section Y to the gasification section W is 2, and the height ratio of the pyrolysis section Y to the gasification section W is 0.5. use as figure 2 In the design of the pyrolysis section Y distribution plate shown, the angle of the pyrolysis section Y distribution plate is 45°; the opening rate of the pyrolysis section Y distribution plate is 0.4%, and the aperture is 1mm. The catalytic gasification test was carried out using low-quality lignite with a particle size of less than 2 mm. The catalyst was potassium carbonate with a loading capacity of 10 wt%. The pyrolysis fluidization gas adopts the dry gas at the outlet of the gasifier, and the amount of the pyrolysis fluidization gas is 7% of that at the outlet of the gasifier. The operating pressure of the gasifier is 3.0mpa. During the test, the temperature in each area was monitored and the c...

Embodiment 2

[0041] The distributed plate fluidized bed gasification furnace of the present invention is adopted, wherein the diameter ratio of the pyrolysis section Y to the gasification section W is 2.3, and the height ratio of the pyrolysis section Y to the gasification section W is 0.4. use as image 3 In the design of the pyrolysis distribution plate shown, the angle of the Y distribution plate in the pyrolysis section is 40°; the opening rate of the Y distribution plate in the pyrolysis section is 0.52%, and the aperture is 0.8mm. The catalytic gasification test was carried out using inferior bituminous coal with a particle size of less than 1 mm. The catalyst was potassium carbonate with a loading capacity of 10 wt%. The pyrolysis fluidization gas adopts the dry gas at the outlet of the gasifier, and the amount of the pyrolysis fluidization gas is 8% of the outlet gas of the gasifier. The operating pressure of the gasifier is 3.5mpa. During the test, the temperature in each area wa...

Embodiment 3

[0049] The distributed plate fluidized bed gasification furnace of the present invention is adopted, wherein the diameter ratio of the pyrolysis section Y to the gasification section W is 2.6, and the height ratio of the pyrolysis section Y to the gasification section W is 0.45. use as figure 2 In the design of the pyrolysis distribution plate shown, the angle of the Y distribution plate in the pyrolysis section is 55°; the opening rate of the Y distribution plate in the pyrolysis section is 0.4%, and the aperture is 1.5mm. The catalytic gasification test was carried out using bituminous coal with a particle size of less than 1mm. The catalyst was potassium carbonate with a loading capacity of 10wt%. The pyrolysis fluidization gas adopts the dry gas at the outlet of the gasifier, and the amount of the pyrolysis fluidization gas is 8% of the outlet gas of the gasifier. The pressure is 3.0mpa. During the test, the temperature of each area is monitored and the composition of th...

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Abstract

The invention provides a gasification furnace for cooperatively producing methane and light tar, and belongs to the field of catalytic coal gasification. Under the precondition of guaranteeing the methane yield, the conversion rate and pyrolysis degree of carbon raw material can be improved, and thus the yield of tar, especially light tar, is improved. The gasification furnace comprises a pyrolysis section and a gasification section positioned below the pyrolysis section, wherein the diameter of the pyrolysis section is greater than that of the gasification section; the upper part of the gasification section is embedded in the bottom of the pyrolysis section, and is connected to the inner wall of the pyrolysis section through an inverted cone-shaped pyrolysis section distribution plate; a pyrolysis section air chamber is restricted by the upper part of the gasification section, the inverted cone-shaped pyrolysis section distribution plate and the inner wall of the bottom of the pyrolysis section. The gasification furnace can be used in the gasification technology for cooperatively producing methane and light tar.

Description

technical field [0001] The invention relates to the field of coal catalytic gasification, in particular to a gasifier for co-producing methane and light tar. Background technique [0002] Coal catalytic gasification technology is an important way of clean and efficient utilization of coal. Existing coal catalytic gasifiers include one-stage bed gasifiers, two-stage bed gasifiers and three-stage bed gasifiers. In the above-mentioned gasifiers, catalyst-loaded carbonaceous raw materials are usually used as raw materials. After the carbonaceous raw materials are upgraded in the pyrolysis section in the gasification furnace, they will be mixed with the gasification agent at a certain pressure and temperature in the gasification section. Under the action of the catalyst, the catalytic gasification reaction is carried out to obtain coal tar with high economic value while generating high-concentration methane. [0003] However, in actual production, the design of the pyrolysis se...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10J3/56
Inventor 祖静茹李克忠高占朋
Owner ENN SCI & TECH DEV
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