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A method for temperature control in a sintering flue gas multi-pollutant treatment process

A sintering flue gas and temperature control technology, which is applied in the temperature control of sintering flue gas multi-pollutant treatment process, and in the field of temperature control in flue gas treatment, can solve the problems of large fluctuations in sintering flue gas pollutant components, and achieve outstanding results , reduce consumption and reduce cost

Active Publication Date: 2022-05-03
ZHONGYE-CHANGTIAN INT ENG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Aiming at the problem that the denitrification tower is prone to crystallization in the prior art, the present invention aims at the characteristics of large fluctuations in the components of sintering flue gas pollutants, combines the adsorption rules of different pollutants on the surface of activated carbon, and based on the crystallization temperature curve of ammonium chloride, the current There is a two-stage activated carbon flue gas purification process improvement and optimization, and a control method is formed to finally achieve SO 2 , NO x , Efficient and low-cost removal of HCl

Method used

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  • A method for temperature control in a sintering flue gas multi-pollutant treatment process
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Examples

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Embodiment 1

[0160] A method for temperature control in a sintering flue gas multi-pollutant treatment process, the method comprising the following steps:

[0161] 1) The sintering flue gas enters the denitration tower after being adsorbed and desulfurized by activated carbon in the desulfurization tower, and enters the dechlorination tower after being adsorbed and denitrated by activated carbon in the denitrification tower, and finally discharged from the dechlorination tower;

[0162] 2) Activated carbon circulates among the desorption tower, denitrification tower and desulfurization tower;

[0163] It is characterized in that: a detection device is installed at the entrance of the desulfurization tower to obtain the state data of the sintering flue gas at the entrance of the desulfurization tower; the state data of the sintering flue gas includes the total flow rate of the sintering flue gas and the initial concentration of each gas component in the sintering flue gas, In order to deter...

Embodiment 2

[0165] Repeat Example 1, only to determine the flow rate of the activated carbon to be circulated. Specifically: according to the total flow rate of the sintering flue gas and the content of sulfur dioxide in the sintering flue gas, determine the circulation amount of the activated carbon. According to the adsorption capacity of activated carbon for each gas and the initial concentration of each gas component in the sintering flue gas, the safe temperature range when the sintering flue gas enters the denitrification tower and the dechlorination tower is calculated as follows: detecting the total flow rate of the sintering flue gas, The initial concentration of nitrogen oxides and hydrogen chloride in the sintering flue gas, and calculate the partial pressure of nitrogen oxides and hydrogen chloride at the inlet of the denitrification tower and dechlorination tower according to the adsorption capacity of activated carbon for different gas components; The partial pressure at the ...

Embodiment 3

[0167] Repeat Example 2, only measure the total flow Q of the sintering flue gas at the inlet of the desulfurization tower, the amount of SO in the flue gas 2 Concentration c 1 ,Available:

[0168]

[0169] In the formula, Q is the sintering flue gas flow rate at the inlet of the desulfurization tower, Nm 3 / h. c 1 is the SO in the sintering flue gas at the inlet of the desulfurization tower 2 Concentration, mg / Nm 3 . a 1 Activated carbon for SO 2 Adsorption capacity, mg / kg-AC.

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Abstract

A method for temperature control in a sintering flue gas multi-pollutant treatment process, the method comprising the following steps: 1) The sintering flue gas enters the denitrification tower after being adsorbed and desulfurized by activated carbon in the desulfurization tower, and enters the denitrification tower after being adsorbed and denitrated by activated carbon in the denitrification tower Chlorine tower, finally discharged from the dechlorination tower; 2) Activated carbon circulates between the desorption tower, screening system, denitrification tower and desulfurization tower; a detection device is installed at the entrance of the desulfurization tower to obtain the state data of the sintering flue gas at the entrance of the desulfurization tower; The state data of the sintering flue gas includes the total flow rate of the sintering flue gas and the concentration of each gas component in the sintering flue gas, so as to determine the quality of the circulating activated carbon; according to the adsorption capacity of the activated carbon for each gas and the initial concentration of each gas, calculate the sintering flue gas The temperature range when the gas enters the denitrification tower and dechlorination tower. The invention calculates the temperature range at the denitrification tower in the sintering flue gas multi-pollutant treatment process, effectively prevents the ammonium chloride crystal from blocking the flue gas circulation channel, and reduces the cost.

Description

technical field [0001] The invention relates to a temperature control method in flue gas treatment, in particular to a temperature control method in a sintering flue gas multi-pollutant treatment process, belonging to the field of sintering flue gas treatment. Background technique [0002] Hydrogen chloride is second only to SO in the steel industry 2 , NO x , dust and fluoride are the fifth largest air pollutants. Among them, sintering is the main emission source of hydrogen chloride gas in the iron and steel industry. The chlorine in the sintering process mainly comes from ore, coal fuel and flux, and its emission concentration is mostly 20-60mg / Nm 3 (in one case up to 130mg / Nm 3 above), mainly depends on the total input of chlorine. Generally speaking, for the same ore, coal and flux, the coastal areas are higher than the inland areas, because the concentration of chloride ions in the precipitation in coastal areas is high; Dust, the HCl concentration in the sinterin...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/76B01D53/56
CPCB01D53/76B01D53/56B01D2258/025B01D2258/0283
Inventor 李俊杰魏进超杨峰
Owner ZHONGYE-CHANGTIAN INT ENG CO LTD
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