Integrated pyrolysis and gasification device for seed coal and integrated pyrolysis and gasification method for seed coal

A technology for pyrolysis gasification and seed coal, applied in the field of coal chemical industry, can solve the problems of low thermal efficiency and cold gas efficiency in the gasification process, difficult recovery and utilization of solid sensible heat, increased investment in air separation plants, etc., so as to improve energy conversion. Efficiency, efficient coupling, effect of increasing productivity

Inactive Publication Date: 2020-02-11
王树宽
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] At present, although fast pyrolysis can produce high value-added gas, the semi-coke produced has a large amount of sensible heat, and the recovery and utilization of solid sensible heat is very difficult, and the heat recovery efficiency is low, and the investment in recovery equipment is large; Chilling treatment after high-temperature dust removal not only wastes a lot of waste heat, but also consumes a lot of water and power during the cooling process
[0005] The conventional gasification process is to burn part of the raw material to generate the heat required for gasification, so as to ensure the continuous operation of the gasification process, and the partially burned fuel becomes carbon dioxide, resulting in low thermal efficiency and cold gas efficiency of the gasification process
Moreover, the traditional gasification process needs to obtain high calorific value coal gas. The gasification process requires pure oxygen as the gasification agent, which greatly increases the investment of the air separation plant, and the operation process requires a large amount of electric energy, which greatly increases the operating cost and the rate of return. Greatly reduced

Method used

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  • Integrated pyrolysis and gasification device for seed coal and integrated pyrolysis and gasification method for seed coal

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Experimental program
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Effect test

Embodiment 1

[0045] see figure 1 , the seed coal integrated pyrolysis gasification device in this embodiment includes a raw material bin 1, a reaction bin 2, an ash buffer bin 4, and a semi-coke buffer bin 5; wherein,

[0046]The raw material bin 1 is used for storing and unloading materials; it is fixed on the top of the reaction bin 2, and the top of the raw material bin 1 is provided with a coal inlet, and its bottom is connected with the top coal inlet of the reaction bin 2 through a pipeline.

[0047] The reaction bin 2 is used to pyrolyze and gasify the seed coal in the raw material bin 1. Its shape is a circular cylinder, and its inner cavity is divided into a pyrolysis area 201, a gasification area 202, and a coke discharge area 203. The pyrolysis area 201 Arranged above the gasification zone 202 and the coke discharge zone 203, a raw coal gas outlet is opened on the cylinder wall of the pyrolysis zone 201, and a gas guide 204 is installed above the pyrolysis zone 201, and the gas ...

Embodiment 2

[0054] see figure 2 with 3 , the seed coal integrated pyrolysis gasification device in this embodiment includes a raw material bin 1, a reaction bin 2, an ash buffer bin 4, and a semi-coke buffer bin 5; wherein,

[0055] The raw material bin 1 is used for storing and unloading materials; it is fixed on the top of the reaction bin 2, and the top of the raw material bin 1 is provided with a coal inlet, and its bottom is connected with the top coal inlet of the reaction bin 2 through a pipeline.

[0056] The reaction chamber 2 is used to pyrolyze and gasify the seed coal in the raw material warehouse 1. Its shape is a square cylinder, and its inner cavity is divided into a pyrolysis area 201, a gasification area 202 and a coke discharge area 203. The pyrolysis area 201 is arranged Above the gasification zone 202 and the coke discharge zone 203, a raw coal gas outlet is opened on the cylinder wall of the pyrolysis zone 201, and a gas exporter 204 is installed above the pyrolysis...

Embodiment 3

[0067] The difference from Embodiment 1 is that no heat exchange fluid channel 6 is arranged on the outer wall of the coke discharge area 203 in this embodiment, and a heat exchange jacket 11 is arranged on the outer wall of the semi-coke buffer bin 5 below the coke discharge area 203, Deoxygenated water is filled in the heat exchange jacket 11 to further reduce the temperature of the semi-coke and complete the primary cooling of the semi-coke.

[0068] Spraying mechanism 12 and coke pushing mechanism 13 can also be arranged at the bottom of semi-coke buffer storehouse 5, spray water to semi-coke through spraying mechanism 12, realize secondary cooling of semi-coke, can effectively prevent gas from leaking out of coke pushing mechanism 13 at the same time, The coke pushing mechanism 13 further pushes the semi-coke after spray cooling to ensure the smooth discharge of the coke. Further, in order to ensure the effect of gasification and pyrolysis, the semi-coke flux ratio of the...

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Abstract

The invention provides an integrated pyrolysis and gasification device for seed coal and an integrated pyrolysis and gasification method for seed coal. The integrated pyrolysis and gasification devicecomprises a raw material bin and a reaction bin, wherein the raw material bin is used for storing and discharging seed coal; the reaction bin is used for pyrolyzing and gasifying the seed coal in theraw material bin; an inner cavity of the reaction bin is divided into a pyrolysis area, a gasification area and a coke discharging area; the gasification area and the coke discharging area are arranged below the pyrolysis area in parallel; the seed coal in the raw material bin is pyrolyzed to generate semicoke in the pyrolysis area by utilizing high-temperature synthesis gas generated by gasification as a heat carrier; a part of the semicoke enters the coke discharging area and is discharged as a semicoke product; and the other part of the semicoke enters the gasification area and is gasified, and generated high-temperature water gas and pyrolyzed raw gas are discharged after being filtered and purified by utilizing the seed coal in the rising process from bottom to top. According to theintegrated pyrolysis and gasification technology in the invention, fuel consumption needed by a coal pyrolysis process is reduced, the energy utilization efficiency of a system is improved, the utilization way of semicoke is widened, and the targets of high efficiency and low consumption in the coal chemical industry are achieved.

Description

technical field [0001] The application belongs to the technical field of coal chemical industry, and in particular relates to an integrated pyrolysis gasification device and method for seed coal. Background technique [0002] Based on the status quo of my country's energy supply and consumption structure, the status of coal as the main energy source in China will not undergo a fundamental change. At present, my country's direct combustion-based utilization of coal resources basically only utilizes the combustion properties of coal, resulting in waste of resources for useful components in coal molecules and serious environmental pollution problems. Therefore, it is a problem that my country's coal chemical industry must solve at present to develop a variety of technologies coupled, capable of cascade utilization of coal resources, and clean and efficient coal conversion and utilization technologies. [0003] According to the structure and physical and chemical properties of ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10J3/66C10J3/62C10J3/72
CPCC10J3/62C10J3/66C10J3/721C10J2300/0936
Inventor 王树宽
Owner 王树宽
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