Novel desulfurization method for calcination tail gas

A tail gas and calcination technology, applied in separation methods, chemical instruments and methods, and separation of dispersed particles, can solve problems such as unsatisfactory treatment effects of tail gas desulfurization devices, failure to meet national emission standards, and difficulty in recycling and reuse, etc., to achieve increased Recycling and processing value, reducing enterprise investment and operating production costs, and reducing the effect of water mist

Pending Publication Date: 2021-04-09
XIANGYANG LOMON TITANIUM IND CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] With the development of the economy and the ever-changing living environment, people pay more and more attention to environmental protection, and the country pays more and more attention to environmental protection. In the chemical industry, SO in the exhaust gas produced by chemical production 2 It is the focus of national attention, and the treatment effect of traditional tail gas desulfurization devices is not ideal
[0003] In 2019, the annual production capacity of Lomon Group's titanium dioxide will reach 1.01 million tons, and the calcination process is a necessary process for the sulfuric acid method titanium dioxide production process. During the calcination process, the calcination tail gas contains pollutants such as sulfur dioxide, nitrogen oxides, and dust. Therefore, the direct discharge of exhaust gas does not meet the national emission standards, and will pollute the environment.
[0011] 3. The temperature of the sand filter water is not higher than 35°C, and the secondary spraying has no effect on SO 2 The absorption of SO is also relatively limited, so the SO in the tail gas 2 The residual amount is relatively large, and a large amount of sodium chlorite solution with an accelerator needs to be added for absorption. The absorption cost is high, and the absorbed waste liquid has complex components, which is difficult to realize recycling and reuse.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0035] The calcined tail gas desulfurization method of the operating section comprises the following steps:

[0036] (1) The tail gas of the calcination kiln enters the spray tower, and a certain flow rate of waste sulfuric acid is used to spray the tail gas. After spraying, the waste sulfuric acid at the bottom of the tower is directly pumped to the top of the tower for recycling, and the waste sulfuric acid is concentrated. , among which, the negative pressure at the kiln tail of the calcining kiln is maintained at about -100pa, and the spray flow rate of waste sulfuric acid is 50m 3 / h, the waste sulfuric acid circulation spray period is 7 days, part of the waste sulfuric acid after concentration is transported to the thickened acid thickener for settlement and output, and the same amount of new waste sulfuric acid is added into the spray system;

[0037] (2) Use sand filter water to further spray the tail gas to wash away the acid mist carried in the tail gas. The acid spr...

Embodiment 2

[0045] Calcination tail gas desulfurization method, comprising the steps of:

[0046] (1) The tail gas of the calcination kiln enters the spray tower, and a certain flow rate of waste sulfuric acid is used to spray the tail gas. After spraying, the waste sulfuric acid at the bottom of the tower is directly pumped to the top of the tower for recycling, and the waste sulfuric acid is concentrated. , among which, the negative pressure at the kiln tail of the calcining kiln is maintained at about -100pa, and the spray flow rate of waste sulfuric acid is 50m 3 / h, the waste sulfuric acid circulation spray period is 3 days, part of the waste sulfuric acid after thickening is transported to the concentrated acid thickener for settlement and output, and the same amount of new waste sulfuric acid is added into the spray system;

[0047] (2) Use sand filter water to further spray the tail gas to wash away the acid mist carried in the tail gas. The acid spray liquid obtained after sand f...

Embodiment 3

[0051] Calcination tail gas desulfurization method, comprising the steps of:

[0052] (1) The tail gas of the calcination kiln enters the spray tower, and a certain flow rate of waste sulfuric acid is used to spray the tail gas. After spraying, the waste sulfuric acid at the bottom of the tower is directly pumped to the top of the tower for recycling, and the waste sulfuric acid is concentrated. , among which, the negative pressure at the kiln tail of the calcining kiln is maintained at about -100pa, and the spray flow rate of waste sulfuric acid is 50m 3 / h, the cycle spraying period of waste sulfuric acid is 9 days, part of the waste sulfuric acid after thickening is transported to the concentrated acid thickener for settlement and output, and the same amount of new waste sulfuric acid is added into the spray system;

[0053] (2) Use sand filter water to further spray the tail gas to wash away the acid mist carried in the tail gas. The acid spray liquid obtained after sand f...

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PUM

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Abstract

The invention discloses a novel desulfurization method for calcination tail gas, belonging to the technical field of treatment of tail gas produced during titanium dioxide calcination. The novel desulfurization method comprises the following steps: (1) allowing tail gas at the tail of a calcination kiln to enter a spray tower, spraying the tail gas with waste sulfuric acid, directly pumping the waste sulfuric acid which is at the bottom of the tower after spraying to the top of the tower for recycling, and concentrating the waste sulfuric acid; (2) carrying out further spraying operation on the tail gas by using sand filter water, and washing away acid mist carried in the tail gas; and (3) building an alkali liquor cooling tower, subjecting liquid alkali cooled by the alkali liquor cooling tower to circular spraying, reducing the temperature of the tail gas, absorbing SO2 in the tail gas, reducing the temperature of the tail gas to 35 DEG C or below, and discharging the tail gas when the content of SO2 reaches the standard. Due to the adoption of tail gas desulfurization technology, the national policy of energy conservation and emission reduction in China is accorded with, and the survival of enterprises is guaranteed; and SO2 in calcination tail gas is annually saved about 540 t/year, so the surrounding living environment is greatly protected.

Description

technical field [0001] The invention belongs to the technical field of tail gas treatment of titanium dioxide calcination production, and in particular relates to a novel calcination tail gas desulfurization method. Background technique [0002] With the development of the economy and the ever-changing living environment, people pay more and more attention to environmental protection, and the country pays more and more attention to environmental protection. In the chemical industry, SO in the exhaust gas produced by chemical production 2 It is the focus of the country's attention, but the treatment effect of the traditional tail gas desulfurization device is not ideal. [0003] In 2019, the annual production capacity of Lomon Group's titanium dioxide reached 1.01 million tons, and the calcination process is a necessary process for the sulfuric acid method titanium dioxide production process. During the calcination process, the calcination tail gas contains pollutants such as...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/14B01D53/50B01D53/78B01D53/96
CPCB01D53/1481B01D53/1406B01D53/1425B01D53/1493B01D53/502B01D53/78B01D53/96B01D2251/304B01D2251/604B01D2252/10B01D2252/103
Inventor 曾小林卢慧军王国锋鞠浩范双
Owner XIANGYANG LOMON TITANIUM IND CO LTD
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