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Raw coke oven gas dedusting device and raw coke oven gas dedusting method

A technology of dust removal device and waste gas, which is used in gas dust removal, gas purification of condensed non-gaseous materials, etc., can solve the problems of filter cake falling off, high temperature corrosion of electrode wires, and tar yield decline.

Active Publication Date: 2013-12-25
SHENMUFUYOU ENERGY TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, there are three methods for dedusting a kind of raw coal gas. The first method is to use a combined cyclone separator, which has low separation efficiency and cannot separate coal dust below 5 μm, and cannot separate a large amount of oil sludge; the second method is electric dust removal. , because the tar-containing raw gas temperature is lower than the tar freezing point and will condense, the electric dust collector needs to be operated at high temperature, the high temperature corrosion of the electrode wire cannot be solved, and the electric dust collector has a large volume, and the tar residence time is too long, and the secondary cracking will be serious. As a result, the yield of tar drops; the third method is automatic backflushing and filtering of ceramic and powder metal tubes. Under high temperature, raw coal gas accumulates carbon on the surface of the tubes to make the pressure difference rise continuously. run

Method used

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Examples

Experimental program
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Embodiment 1

[0026] Taking dusty raw gas with a treatment temperature of 350-600°C and a pressure of 4-10KPa as an example, the dust removal device in this embodiment consists of an independent dust removal unit, see figure 1 , the dust removal unit includes replacement and back blowing gas tank 1, raw gas pipeline 2, raw gas control valve 3, filter 4, replacement gas control valve 5, back blowing gas outlet valve 6, gas cooler 7, bag filter 8 , oil-free gas control valve 9, first T-shaped valve 10, circulating fan 11, heater 12, second T-shaped valve 13, reverse blowing gas inlet valve 14 and purge gas control valve 15 are connected to form.

[0027] The top of the filter 4 of this embodiment is processed with an air inlet and an air outlet, and a tee is installed on the air inlet, and one port of the tee is passed into the raw gas through the raw gas pipeline 2, and the other port is connected to the replacement The replacement gas is introduced into the gas pipeline. A raw gas control v...

Embodiment 2

[0037] In this embodiment, the filter layer 4-3 uses expanded perlite as the filter material, and the thickness of the filter material is 400mm. The expanded perlite is distributed according to the size of the interlayer particles, and the particle size from top to bottom is 6-1.5mm. , the bulk density distribution is 60~800kg / m 3 . The steady flow layer 4-4 is arranged with olivine, with a thickness of 600mm. The olivine is distributed in the order of small up and down big. The particle size from top to bottom is 1-8mm, and the bulk density is 1480-2800kg / m 3 . Johnson net 4-5 adopts high temperature resistant sieve plate type Johnson net 4-5, and its sieve bar interval is 3mm. The grid plates 4-6 are made of high temperature resistant materials, and the grid interval is 20mm. Other components and their connections are the same as in Embodiment 1.

[0038] The method for dedusting the raw coal gas with the above-mentioned device is the same as in Example 1.

Embodiment 3

[0040] In this embodiment, the filter layer 4-3 adopts pumice as the filter material, and the thickness of the filter material is 200mm. 210~360kg / m 3 . The current-stabilizing layer 4-4 is arranged with metal balls with a thickness of 300mm. The metal balls are distributed in the order of large bottom and small top. 3 . Johnson net 4-5 adopts high temperature resistant sieve plate type Johnson net 4-5, and its sieve bar spacing is 7mm. The grid plates 4-6 are made of high temperature resistant materials, and the grid interval is 80mm. Other components and their connections are the same as in Embodiment 1. The method for dedusting the raw coal gas with the above-mentioned device is the same as in Example 1.

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Abstract

The invention relates to a raw coke oven gas dedusting device and a raw coke oven gas dedusting method. The device consists of at least one dedusting unit; each dedusting unit comprises a filter; the filter is respectively communicated with a raw coal oven gas pipeline, a coal oven gas cooler as well as a gas replacement pipeline; the coal gas cooler is communicated with a bag-type deduster; the bag-type deduster and an oil-free gas pipeline are communicated with a circulation fan; the circulation fan is communicated with a coal oven gas heater; a purified gas outlet in the bottom of each filter is communicated with a purified gas emission pipeline; a blowback gas inlet is communicated with a blowback gas pipeline; the blowback gas pipeline and a gas replacement pipeline are communicated with a coal gas heater. The whole device is simple in structure, runs stably, is low in energy consumption, and is high in filtering efficiency; a circulation ash blowing regeneration system is not arranged, bed materials are not required to be circulated, filter materials are prevented from being crushed during the filtering process and the abrasion to equipment is prevented; multiple dedusting devices can be in parallel combination for filtering. According to the method provided by the invention, the operation is simple and convenient, the dedusting efficiency is high, pressure difference is low, energy consumption is low, and the cost is low.

Description

technical field [0001] The invention belongs to the technical field of coal chemical industry for high-temperature dedusting of oily gas, and in particular relates to a dedusting device and a dedusting method for raw coal gas produced in the process of producing coal tar by pyrolysis of pulverized coal. Background technique [0002] In recent years, there have been extensive researches on the production of coal tar by low-temperature pyrolysis of coal at home and abroad, but the raw gas produced during the production process contains a large amount of raw gas containing coke powder, and there has been no breakthrough in dust removal, which seriously restricts this process. industry development. [0003] At present, there are three methods for dedusting a kind of raw coal gas. The first method is to use a combined cyclone separator, which has low separation efficiency and cannot separate coal dust below 5 μm, and cannot separate a large amount of oil sludge; the second method...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10K1/02C10K1/04
Inventor 杨占彪王树宽于广彦万宝良柴宗成贺志宝史宏伟郭生飞
Owner SHENMUFUYOU ENERGY TECH
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