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Sulfur dioxide flue gas absorption system and method for treating sulfur dioxide flue gas

A sulfur dioxide and absorption system technology, applied in chemical instruments and methods, gas treatment, separation methods, etc., can solve the problems of insufficient reaction between flue gas and lime slurry, unsteady exhaust gas concentration, and difficulty in guaranteeing occupational hygiene, etc. Sedimentation and scaling, reducing the scaling in the tower, reducing the effect of the cross-sectional area in the tower

Inactive Publication Date: 2018-04-13
HUNAN CHENZHOU MINING CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the production practice of this traditional sulfur dioxide absorption process shows that the original process has the following problems: ① Tail gas SO 2 Concentration cannot be reached stably
②The utilization rate of fine lime is low
Tower cleaning requires a lot of labor, the working environment is poor, and occupational hygiene is difficult to guarantee
The main reason is that it adopts internal circulation absorption, the oxygen content of flue gas is low, SO 2 The reaction between flue gas and lime slurry is insufficient, and the generated calcium sulfite is unstable; in order to reduce the exhaust gas control index, the pH value of the discharged lime slurry can only be increased to a high level, resulting in low lime utilization. If the pH value of lime slurry is too high, it will inevitably increase the consumption of fine lime
The lime slurry is circulated in the tower, and the lime slurry discharged outside is overflow, causing a large amount of lime residue to stay in the desulfurization tower system

Method used

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  • Sulfur dioxide flue gas absorption system and method for treating sulfur dioxide flue gas
  • Sulfur dioxide flue gas absorption system and method for treating sulfur dioxide flue gas

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Embodiment 1

[0028] The fine lime powder is made into lime slurry in the pulping tank (the concentration of CaO is above 80%, the particle size is 200 mesh, and the concentration of lime slurry is controlled at about 7%), and it enters the raw slurry tank by gravity. The lime slurry in the raw slurry tank is pumped into the secondary absorption tower by a 55kw slurry pump for spray absorption. After absorption, it flows back to the raw slurry tank and then overflows into the circulating slurry tank. The lime slurry in the circulating slurry tank is pumped into the primary absorption tower through a 55kw slurry pump, and flows into the circulating slurry tank after being absorbed; absorbing SO 2 The final slurry is discharged through the slag discharge pump and enters the tailings system.

[0029] The slag discharge process is that when the pH value in the circulating lime slurry tank reaches the set value (generally set at about 6), the slag discharge pump is turned on for slag discharge, ...

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Abstract

The invention discloses a sulfur dioxide flue gas absorption system and a method for treating sulfur dioxide flue gas. The sulfur dioxide flue gas enters a primary absorption tower from the top of theprimary absorption tower, is sequentially sprayed and absorbed by the primary absorption tower and a secondary absorption tower and then is discharged from the lower portion of the secondary absorption tower. Besides, fresh lime slurry is intermittently fed into a raw slurry tank and overflows into a slurry circulating tank, the lime slurry in the raw slurry tank is pumped into the top of the secondary absorption tower from an external circulating pipeline under the action of a slurry pump to spray and absorb the sulfur dioxide flue gas in the tower, and then the lime slurry automatically flows and returns to the raw slurry tank. The lime slurry in the slurry circulating tank is pumped into the top of the primary absorption tower from the external circulating pipeline under the action ofthe slurry pump to spray and absorb the sulfur dioxide flue gas in the tower, and then the lime slurry automatically flows and returns to the slurry circulating tank. The removal rate of sulfur dioxide can reach 99% or more after treatment of the two absorption towers, absorption stability is good, national environmental protection emission indexes are met, the use rate of refined lime can be increased, usage of the lime is reduced, and cost is saved.

Description

technical field [0001] The invention relates to a sulfur dioxide flue gas absorption system, in particular to a treatment method for sulfur dioxide flue gas produced in the fire antimony smelting process by using the sulfur dioxide flue gas absorption system; it belongs to the field of environmental protection. Background technique [0002] In the industrial production of antimony smelting, antimony sulfide ore is added to coke, iron ore, and limestone to rough-smelt antimony concentrate through blast furnace pyrometallurgy to produce antimony oxygen and noble antimony while producing sulfur dioxide flue gas. With the country's emphasis on environmental protection, sulfur dioxide flue gas must reach 400mg / m 3 the following. However, the existing technology is difficult to meet the emission requirements of sulfur dioxide flue gas, or when meeting the emission requirements of sulfur dioxide flue gas, the cost of investment is high, which is not conducive to the improvement of...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/80B01D53/50B01D53/73
CPCB01D53/80B01D53/502B01D53/504B01D53/73B01D2251/404B01D2258/0283
Inventor 王亲雄
Owner HUNAN CHENZHOU MINING CO LTD
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