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Method and device for utilizing high value through pyrolysis and gasification of coal

A technology for pyrolysis gas and coal gasification, which is used in the gasification of granular/powdered fuels, mitigation of combined combustion, and the manufacture of combustible gases. Coal C, H structure resources and other issues

Active Publication Date: 2010-07-21
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The "circulating fluidized bed thermoelectricity tar polygeneration device and its method" (CN 1978591A) proposed by Zhejiang University combines a fluidized bed retort furnace and a circulating fluidized bed combustion furnace, and utilizes the circulating hot ash of the circulating fluidized bed to achieve The pyrolysis of coal produces pyrolysis oil, pyrolysis gas and semi-coke, and the produced semi-coke is transported to the circulating fluidized bed combustion furnace for combustion to heat water and generate electricity, although this method can extract pyrolysis by pyrolysis oil, but a large amount of semi-coke is burned, and the C and H structure resources in coal cannot be fully utilized
The "circulating fluidized bed boiler high-temperature ash pyrolysis coal-to-oil device" (CN 200996006Y) proposed by Shandong University sends part of the high-temperature circulating ash into the pyrolysis reactor to be mixed with coal by setting a spiral ash collector under the cyclone separator. The powder is mixed and pyrolyzed, and the mixture of semi-coke and circulating ash produced by pyrolysis is transported by the screw conveyor under the pyrolysis reactor to the circulating fluidized bed boiler for combustion. This technology uses baffles in the pyrolysis reactor To realize the mixing of coal ash and coal powder, it is difficult to ensure the uniform mixing of coal ash and coal powder, and the screw used for ash collection must be able to withstand high temperature, which makes it difficult to scale up and run the technology for a long time
[0005] In short, the existing high-value comprehensive utilization technologies of coal mainly combine pyrolysis and combustion of coal, and most of them are aimed at pulverized coal, and the processing consumption of coal is relatively high
In the process of raw coal production and grading preparation of granular coal, a large amount of crushed coal with a wide particle size distribution below 25mm will be produced. Most of these coals are used for boiler combustion, and it is difficult to obtain high-value and efficient utilization.

Method used

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  • Method and device for utilizing high value through pyrolysis and gasification of coal

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Embodiment 1

[0083] The dilute-phase conveying bed and dense-phase fluidized bed in this embodiment are a coal pyrolysis gasification process system coupled up and down, such as figure 1 As shown, it includes: feed system 1, dense-phase fluidized bed 2, dilute-phase conveying bed 3, separation equipment (cyclone separator 4 and pyrolysis oil separator 6), return valve 7 and down riser 5.

[0084] In this process flow, the raw coal is fed from the lower part of the dilute-phase conveying bed 3 through the first feeding system 1, and the large-sized coal with a particle size of 3-25 mm in the raw coal enters the dense phase below the dilute-phase conveying bed 3 downwards. In the fluidized bed 2, partial combustion and gasification occurs under the action of one or more gases of air, oxygen, water vapor, oxygen-containing carbon dioxide and methane fed into the dense-phase fluidized bed air chamber 10, relying on Part of the heat generated by coal combustion is gasified in the range of 500-1...

Embodiment 2

[0086] The dilute-phase conveying bed and the dense-phase fluidized bed in this embodiment are coal pyrolysis and gasification process systems coupled left and right, such as figure 2 Shown, comprise: feed system (the first feed system 1 and the second feed system 17), dense-phase fluidized bed 2, dilute-phase conveying bed 3, separation equipment (cyclone separator 4 and heat produced during low temperature Oil separation separator 6), distribution valve 13 and down riser 5.

[0087] In this process flow, the raw coal is fed into the dense-phase fluidized bed 2 through the first feed system 1, and the hot ash and / or The incompletely gasified semi-coke is mixed and fluidized and heated, and pyrolyzed in the temperature range of 300-1100°C, and the pyrolysis gas products (including pyrolysis gas and pyrolysis oil (pyrolysis temperature lower than 800°C) will be produced)) from the upper part of the dense-phase fluidized bed 2 into the pyrolysis oil separator 6 to be separated...

Embodiment 3

[0091] In this embodiment, a coal pyrolysis gasification process system that uses a dilute-phase conveying bed that further burns out ash and a dense-phase fluidized bed is coupled up and down, such as image 3 As shown, it includes: feed system 1, dense-phase fluidized bed 2, dilute-phase conveying bed 3, separation equipment (cyclone separator 4 and pyrolysis oil separator 6), return valve 7, down riser 5, ash The slag burns out the fluidized bed 11 and the solid slag removal device 20 .

[0092] In this process flow, the raw coal is fed from the lower part of the dilute-phase conveying bed 3 through the first feeding system 1, and the large-sized coal with a particle size of 3-25 mm in the raw coal enters the dense phase below the dilute-phase conveying bed 3 downwards. In the fluidized bed 2, partial combustion and gasification occurs under the action of one or more gases of air, oxygen, water vapor, oxygen-containing carbon dioxide and methane fed into the dense-phase flu...

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Abstract

The invention relates to a method and a device for utilizing high value through pyrolysis and gasification of coal. The pyrolysis and gasification processes of the coal are separated in a mode of coupling a dilute phase conveying bed and a dense phase fluidized bed; and the coal is partially or wholly pyrolyzed before gasification, and co-production of pyrolysis gas, gasification generated gas and pyrolysis oil is realized. The dilute phase conveying bed and the dense phase fluidized bed can be coupled in two modes, namely upper-lower coupling and left-right coupling, and are applied to treating the coal in wide particle diameter distribution. High-value organic structures in the coal can be extracted before the gasification of the coal, and the utilization value of the coal is improved.

Description

technical field [0001] The invention belongs to the technical field of high-value comprehensive utilization of coal and energy quality improvement and high-efficiency, high-clean energy, and relates to a method and a device suitable for high-value utilization of pyrolysis gasification of coal with wide particle size. Background technique [0002] my country is poor in oil and natural gas resources, but relatively rich in coal resources. In my country's primary energy consumption structure, coal consumption accounts for about 68.7% of the total energy consumption structure. The existing coal utilization methods are mainly combustion, gasification, liquefaction and pyrolysis, among which combustion is the main utilization mode of coal, and its coal consumption accounts for about 80% of the total coal consumption. Coal contains a large amount of C and H chemical structure resources. On the one hand, direct combustion has low utilization efficiency and serious pollution. On the...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10J3/66C10J3/56C10G1/00
CPCY02E20/18
Inventor 董利许光文汪印宋文立高士秋纪文峰
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI
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