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Double-bed gasification unit and method

A technology for a gasification device and a gasification furnace, which is applied in the field of gasification, can solve the problem that the calorific value of gas is difficult to greatly increase, and achieve the effects of reducing the amount of pollutants, improving the quality of gas, and reducing damage

Pending Publication Date: 2017-08-22
SHENWU TECH GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0003] At present, the traditional twin-bed gasification technology generally sends the pyrolysis gas generated after pyrolysis directly into the gasifier to be cracked and gasified again at high temperature, so as to obtain synthetic gas or water gas with lower impurities and higher calorific value. This type of technology is relatively simple, with high thermal efficiency and high cold gas efficiency, but it directly converts substances with high calorific value such as hydrocarbons or low-boiling aromatic ring substances in the pyrolysis gas into hydrogen and Substances such as carbon monoxide reduce the content of organic substances with high calorific value in the gas, making it difficult to greatly increase the calorific value of the gas

Method used

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  • Double-bed gasification unit and method

Examples

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Embodiment 1

[0046] In this example, the 10t / h circulating fluidized bed-moving bed double-bed low-rank coal gasification is taken as a specific example to illustrate this patent in detail.

[0047] Wherein, the present embodiment uses air and water vapor as the gasification agent, and the device used in the present embodiment is as figure 2 As shown, it mainly includes: pyrolysis furnace 1, gasification furnace 2, pyrolysis gas condensation separator 3 and synthetic gas cooler 4.

[0048] The pyrolysis furnace 1 is a moving bed pyrolysis furnace, and its coal inlet is connected with the coal supply system; its semi-coke outlet is connected with the gasification furnace 21 of the gasification furnace 2 through the inclined leg of the return material; Its heat carrier inlet is connected with the material leg of the separator 22 of the gasifier 2 ; its pyrolysis gas outlet is connected with the pyrolysis gas inlet of the pyrolysis gas condensation separator 3 .

[0049] The gasification fu...

Embodiment 2

[0061] In this example, a 10 t / h fluidized bed-rotary bed twin-bed low-rank coal gasification in which the gasification agent is a mixture of air and steam is taken as a specific example. Wherein, in this embodiment, oxygen-enriched carbon dioxide gas and water vapor are used as gasification agents.

[0062] image 3 It is a schematic diagram of the twin-bed gasification device of the rotary bed pyrolysis furnace of the present invention, as image 3 As shown, the twin-bed gasification device in this embodiment mainly includes: a pyrolysis furnace 1 , a gasification furnace 2 , a pyrolysis gas condensation separator 3 and a synthetic gas cooler 4 .

[0063] Wherein, the pyrolysis furnace 1 is a rotary bed pyrolysis furnace, and its coal inlet is connected to the coal supply system; its semi-coke outlet is connected to the semi-coke inlet of the gasification furnace 21 of the gasifier 2; The gas outlet is connected to the gas pipe network system; the pyrolysis gas outlet is c...

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Abstract

The invention relates to a double-bed gasification device, which includes: a pyrolysis furnace, a gasification furnace and a pyrolysis gas condensation separator, and re-adds the difficult-to-use low-quality tar produced by pyrolysis into the high-temperature gasification furnace to generate synthetic gas Or water gas, and reduce the tar component in the generated synthetic gas or water gas, improve the gas quality, reduce the amount of pollutants in the gas, and reduce the difficulty of subsequent gas treatment. At the same time, after the pyrolysis gas is cooled and liquefied, only the liquefied tar enters the gasifier again for re-gasification, and the pyrolysis coal gas of hydrocarbon-rich substances that cannot be gasified no longer participates in the gasification but directly interacts with the generated The mixed gas and water gas are mixed to form a mixture, thereby reducing the damage to the hydrocarbons in the pyrolysis gas, and these hydrocarbon-rich substances are transferred to the mixed gas, which greatly improves the calorific value and quality of the gas.

Description

technical field [0001] The invention belongs to the technical field of gasification, and in particular relates to a double-bed gasification device and method. Background technique [0002] The twin-bed gasification technology generally pyrolyzes the solid fuel first, and then sends the pyrolysis product into the gasifier for gasification to obtain synthetic gas or water gas, which can effectively reduce the content of impurities such as tar in the produced synthetic gas. It improves the gas quality, reduces the emission of pollutants such as phenol water, and increases the calorific value of the produced synthetic gas. It is a very important gasification technology, especially suitable for the low-quality tar produced by low-rank coal pyrolysis. In difficult-to-use working conditions, low-quality tar can be effectively gasified and reused. [0003] At present, the traditional twin-bed gasification technology generally sends the pyrolysis gas produced after pyrolysis directl...

Claims

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Application Information

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IPC IPC(8): C10J3/56C10J3/72C10J3/76C10J3/84C10B47/30C10B49/06C10B53/04
CPCC10J3/56C10B47/30C10B49/06C10B53/04C10J3/721C10J3/76C10J3/84C10J2300/093C10J2300/0959C10J2300/0976C10J2300/1215C10J2300/1807
Inventor 刘周恩李少雨苏二强吴黎阳余海鹏黄伟郑庆庆史东军史雪君吴道洪
Owner SHENWU TECH GRP CO LTD
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