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Device and method for denitrifying flue gas of coking furnace

A desulfurization device and denitrification technology, applied in the field of coke oven flue gas denitrification, can solve the problems of high operating cost and unsatisfactory operating conditions of SCR, and achieve the effects of no waste liquid discharge, little influence of chimney suction, and large thermal gradient

Active Publication Date: 2014-12-10
鹤岗市征楠煤化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The new "Emission Standard of Pollutants for Coking Chemical Industry" implemented on October 1, 2012 has made mandatory regulations on the sulfur and nitrogen oxides in the flue gas emitted from the coking chimney. For the heat recovery coke oven, the flue gas emitted from the chimney Medium SO 2 ≤100mg / m3, NO x ≤200mg / m3, currently there is no reformed coking enterprise, and the flue gas SO from the chimney 2 About 500mg / m3, NO x About 800-1500mg / m3, far exceeding the national standard
The operating temperature of the flue gas in the SCR process is 300-400°C, which is higher than the 260-270°C of the coke oven flue gas. Therefore, although the SCR has high denitrification efficiency, it cannot meet its operating conditions; The operating cost is high, and it is also a heavy burden for the low-profit coking industry

Method used

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  • Device and method for denitrifying flue gas of coking furnace

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0076] A. The coke oven flue gas is cooled three times:

[0077] After the coke oven flue gas at a temperature of 258°C enters the heat exchanger 17 through the induced draft fan 16, it exchanges heat with the purified flue gas from the denitrification tower 9 in the heat exchanger 17. The purified flue gas is heated to a higher temperature, and the coke oven smoke After the gas is cooled once, the temperature drops to 181°C, and then the purified flue gas enters the chimney to be discharged. After cooling, the coke oven flue gas enters the waste heat boiler 8 for heat exchange and cooling with soft water. After the second cooling, the temperature of the coke oven flue gas drops to 82°C , the coke oven flue gas from the waste heat boiler 8 enters the cooling and humidifying tower 1, and the coke oven flue gas is circulated and sprayed with industrial water for three times for cooling through the humidification pump 2, and the temperature of the coke oven flue gas drops to 71°C....

Embodiment 2

[0087] A. The coke oven flue gas is cooled three times:

[0088] After the coke oven flue gas with a temperature of 264°C enters the heat exchanger 17 through the induced draft fan 16, it exchanges heat with the purified flue gas from the denitrification tower 9 in the heat exchanger 17. The purified flue gas is heated to a higher temperature, and the coke oven smoke After the gas is cooled once, the temperature drops to 186°C, and then the purified flue gas enters the chimney to be discharged. After cooling, the coke oven flue gas enters the waste heat boiler 8 for heat exchange and cooling with soft water. After the second cooling, the temperature of the coke oven flue gas drops to 85°C , the coke oven flue gas from the waste heat boiler 8 enters the cooling and humidifying tower 1, and the coke oven flue gas is circulated and sprayed with industrial water for three times for cooling through the humidification pump 2, and the temperature of the coke oven flue gas drops to 74°...

Embodiment 3

[0098] A. The coke oven flue gas is cooled three times:

[0099] After the coke oven flue gas at a temperature of 271°C enters the heat exchanger 17 through the induced draft fan 16, it exchanges heat with the purified flue gas from the denitrification tower 9 in the heat exchanger 17. The purified flue gas is heated and the temperature of the coke oven flue gas After the gas is cooled once, the temperature drops to 189°C, and then the purified flue gas enters the chimney to be discharged. After cooling, the coke oven flue gas enters the waste heat boiler 8 for heat exchange and cooling with soft water. After the second cooling, the temperature of the coke oven flue gas drops to 89°C , the coke oven flue gas from the waste heat boiler 8 enters the cooling and humidifying tower 1, and the coke oven flue gas is circulated and sprayed with industrial water for three times for cooling through the humidification pump 2, and the temperature of the coke oven flue gas drops to 77°C. A...

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Abstract

The invention discloses a device and method for denitrifying flue gas of a coking furnace by using citric acid as a catalyst. The device comprises a cooling device, a desulfurization device and a denitration device. The method for denitrifying flue gas of the coking furnace by using the device comprises the following steps of cooling the flue gas of the coking furnace three times; desulfurizing the flue gas of the coking furnace; carrying out first-stage denitration on the flue gas of the coking furnace; carrying out second-stage denitration on the flue gas of the coking furnace; and discharging the purified flue gas. The method disclosed by the invention is safe, reliable, high in denitration and absorption efficiencies, little in influences to the suction force of a chimney, free of waste liquid discharge and capable of reducing the operation cost at the desulfurization stage; the obtained product does not contain poisonous ammonium sulphate; and the contents of SO2, NO and NO2 in the discharged flue gas are far lower than the national flue gas discharge standard.

Description

[0001] technical field [0002] The invention relates to a coke oven flue gas denitrification device and method, in particular to a coke oven flue gas denitrification device and method using citric acid as a catalyst, and belongs to the field of coke oven flue gas denitrification. Background technique [0003] Since the founding of the People's Republic of my country, China's coking enterprises have been mainly based on extensive development, that is, to increase economic benefits by expanding the scale. There are mandatory regulations, but there is no mandatory standard for the content of nitrogen oxides. With the increasing environmental pollution in recent years, people have begun to pay attention to environmental issues. The new "Emission Standard of Pollutants for Coking Chemical Industry" implemented on October 1, 2012 has made mandatory regulations on the sulfur and nitrogen oxides in the flue gas emitted from the coking chimney. For the heat recovery coke oven, the fl...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/75B01D53/78B01D53/90B01D53/60F27D17/00
CPCY02A50/20Y02P10/25
Inventor 袁磊张超群王为为黄大中
Owner 鹤岗市征楠煤化工有限公司
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