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Method of purifying calcium carbide furnace gas

A technology of calcium carbide furnace gas and calcium carbide furnace, which is applied in the direction of combustible gas purification, combustible gas purification/transformation, gas dust removal, etc. The effect of low water consumption, reduced floor space and investment, and cost reduction

Active Publication Date: 2009-04-29
CHINA TIANCHEN ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] 2. When the temperature of the furnace gas is ≤225°C, the tar in the furnace gas reaches the freezing point and precipitates, causing the pipe to stick to coke and the diameter of the pipe gradually becomes smaller, which affects the furnace gas transportation
[0011] The above two wet purification methods use water directly to lower the temperature of the furnace gas from 600 to 800°C to normal temperature, and perform dust removal and tar removal treatment. Although the furnace gas can be purified, the furnace gas mainly relies on turbid circulating water to cool down. , the temperature difference is relatively large, and the water consumption is relatively large

Method used

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  • Method of purifying calcium carbide furnace gas

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Embodiment 1

[0018] A method for purifying calcium carbide furnace gas, comprising the following steps: (1) dissolving the tar-containing 150~600mg / Nm from the calcium carbide furnace 3 , Dust 100~150g / Nm 3 After the high-temperature furnace gas passes through the dust removal system, the temperature drops to 225°C (dry dust removal). The dust removal system consists of a secondary cyclone dust collector, a fan, and a three-stage bag filter. The high-temperature furnace gas passes through the secondary cyclone dust collector, Fan, three-stage bag filter; (2) The cooled furnace gas is boosted to 10KPaG by a high-temperature fan, and sent to a water washing tower for washing, so that the temperature of the furnace gas drops to 20°C, the tar content drops to 1-100ppm, and the dust content Reduced to 1~5mg / Nm 3 (wet purification); (3) The furnace gas washed from the water washing tower passes through the water seal in front of the gas cabinet, the spiral wet gas cabinet, and the water seal be...

Embodiment 2

[0021] A method for purifying calcium carbide furnace gas, comprising the following steps: (1) dissolving the tar-containing 150~600mg / Nm from the calcium carbide furnace 3 , Dust 100~150g / Nm 3 After the high-temperature furnace gas passes through the dust removal system, the temperature drops to 260°C. The dust removal system is composed of a secondary cyclone dust collector, a fan, and a third-stage bag filter. The high-temperature furnace gas passes through the secondary cyclone dust collector, fan, and third-stage dust collector in turn. Bag dust collector; (2) The cooled furnace gas is boosted to 25KPaG by a high-temperature fan, and sent to a water washing tower for washing, so that the temperature of the furnace gas is reduced to 50°C, the tar content is reduced to 1-100ppm, and the dust content is reduced to 1-100ppm 5mg / Nm 3 (3) The furnace gas washed from the water washing tower will pass through the water seal before the gas holder, the spiral wet type gas holder, ...

Embodiment 3

[0023] A method for purifying calcium carbide furnace gas, comprising the following steps: (1) dissolving the tar-containing 150~600mg / Nm from the calcium carbide furnace 3 , Dust 100~150g / Nm 3 After the high-temperature furnace gas passes through the dust removal system, the temperature drops to 240°C, and the dust removal system adopts a conventional dust removal system; (2) The cooled furnace gas is boosted to 20KPaG by a high-temperature fan, and sent to a water washing tower for washing, so that the furnace gas The temperature drops to 35°C, the tar content drops to 1-100ppm, and the dust content drops to 1-5mg / Nm 3 (3) The furnace gas washed from the water washing tower will pass through the water seal before the gas holder, the spiral wet type gas holder, and the water seal after the gas holder in turn to make purified calcium carbide furnace gas. According to the length of the distance, the purified calcium carbide furnace gas is sent to the user after being boosted b...

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Abstract

The invention discloses a purifying method of calcium carbide furnace gas, which comprises the following steps: (1) leading high temperature furnace gas with 150-600mg / Nm3 oil tar and 100-150g / Nm3 from calcium carbide furnace through dust pelletizing system; lowing the temperature at 225-260deg.c; (2) leading to high temperature fan; boosting pressure at 10-25KPaG; washing in water scrubber; lowing furnace temperature at 20-50 deg.c; lowing oil tar content to 1-100ppm; lowing dust content to 1-5mg / Nm3; (3)leading furnace gas from water scrubber through air collector front water-sealing, screw-type dish gas holder and air collector back water-sealing; getting the product. This can low accommodation area and investment.

Description

technical field [0001] The invention relates to a method for purifying calcium carbide furnace gas. Background technique [0002] Coke and lime, the raw materials produced by calcium carbide, produce calcium carbide under the action of resistance arc heat, and also produce a large amount of furnace gas. The furnace gas temperature from the calcium carbide furnace is about 600-800°C, and the instantaneous maximum temperature can reach 1000°C, with high calorific value. It can be used as fuel for charcoal drying hot blast stoves, gas-fired lime kilns, power plants, boilers and other equipment. It enables energy recovery and reuse, realizes circular economy, and increases product added value. [0003] Calcium carbide furnace gas contains 70-90% CO, H 2 5~7%, O 2 0.2~0.6%, CO 2 2~5%, CH 4 0~5%, N 2 1~4%, tar 150~600mg / Nm 3 , Dust 100~150g / Nm 3 . It has the characteristics of high temperature, flammability, explosion, dust stickiness and blockage. [0004] Gas-fired li...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10K1/02C10K1/10
Inventor 孔祥武汤明伟李树华石晶张春丽郭曼波李勇
Owner CHINA TIANCHEN ENG
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