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Device and method for wet-process deacidification

A kind of equipment and deacidification technology, which is applied in the field of economical wet deacidification equipment and high efficiency, to avoid high-salt wastewater, low raw material cost, and reduce operating cost

Pending Publication Date: 2019-10-11
光大绿色环保管理(深圳)有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] In recent years, with the rapid development of the environmental protection industry, many companies are actively entering the field of hazardous solid waste disposal. At present, my country's hazardous solid waste is mainly disposed of by incineration technology. As the country's environmental supervision becomes more and more strict, the incineration process It is particularly important to meet the emission standards of flue gas. Generally, hazardous solid waste materials have high content of Cl and S elements, and these elements produce a large amount of HCl and SO in the incineration process. 2 Equal acidity and wet deacidification for HCl and SO in flue gas 2 Such acid gases have a high removal efficiency, but the traditional wet deacidification process will inevitably produce a large amount of saline wastewater that needs to be treated. The treatment cost and equipment investment of this part of the saline wastewater are in the operation of hazardous waste and equipment investment For this reason, if the generation of saline wastewater can be avoided in the wet deacidification process, the operating cost of hazardous waste disposal will be greatly reduced and the investment in equipment will be reduced to a certain extent.

Method used

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  • Device and method for wet-process deacidification

Examples

Experimental program
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Effect test

Embodiment 1

[0073] A flue gas after dedusting, the main acid gas composition is HCl content of 8000mg / Nm 3 , SO 2 The content is 2000mg / Nm 3 , enter the first washing tower 110, and the circulating liquid is pumped into the first washing tower 110 through the first filter 114 by the first circulating pump 115 to absorb the acid liquid; when the pH of the circulating liquid is lower than 3, the partial circulation in the discharge tower liquid to the acid solution storage tank 113 (spent acid storage tank), and simultaneously open the second circulation pump 116 to replenish industrial water. The acid solution storage tank 113 (spent acid storage tank) is used for sewage treatment or other facilities of the factory such as waste disposal production line for pH adjustment.

[0074] The flue gas washed by the first scrubber 110 enters the second scrubber 120 . The circulating liquid is pumped to the second washing tower 120 through the second filter 121 by the third circulating pump 122 t...

Embodiment 2

[0076] A flue gas after dedusting, the main acid gas composition is HCl content of 8000mg / Nm 3 , SO 2 The content is 12000mg / Nm 3 , enter the first washing tower 110, and the circulating liquid is pumped into the first washing tower 110 through the first filter 114 by the first circulating pump 115 to absorb the acid liquid; when the pH of the circulating liquid is lower than 3, the partial circulation in the discharge tower liquid to the acid solution storage tank 113 (spent acid storage tank), and simultaneously open the second circulation pump 116 to replenish industrial water. The acid solution storage tank 113 (spent acid storage tank) is used for sewage treatment or other facilities of the factory such as waste disposal production line for pH adjustment.

[0077] The flue gas washed by the first scrubber 110 enters the second scrubber 120 . The circulating liquid is pumped to the second washing tower 120 through the second filter 121 by the third circulating pump 122 ...

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Abstract

The invention provides a device and method for wet-process deacidification, and is used for an incineration flue gas cleaning technology. The device comprises a first washing tower and a second washing tower which are communicated by a pipeline. A flue gas after dedusting firstly passes through the first washing tower and enters the second washing tower. The first washing tower internally comprises circulating water. The second washing tower internally comprises circulating saturated Na2CO3 solution. The first washing tower is connected with a sewage treatment device or a waste chemical treatment and production device. After the circulating water in the first washing tower absorbs HCl in the flue gas, a hydrochloric acid is produced. The hydrochloric acid is flowed to the sewage treatmentdevice or the waste chemical treatment and production device, and used for adjusting a pH of solution in the sewage treatment device or the waste chemical treatment and production device. The bottom of the second washing tower is connected with a precipitate centrifugal separation device. The saturated Na2CO3 solution reacts with an acid gas in the flue gas so as to generate salt, and the salt isseparated out in a solid state by the precipitate centrifugal separation device.

Description

technical field [0001] The invention relates to the field of flue gas purification treatment, in particular to an efficient and economical wet deacidification equipment and method. Background technique [0002] In recent years, with the rapid development of the environmental protection industry, many companies are actively entering the field of hazardous solid waste disposal. At present, my country's hazardous solid waste is mainly disposed of by incineration technology. As the country's environmental supervision becomes more and more strict, the incineration process It is particularly important to meet the emission standards of flue gas. Generally, hazardous solid waste materials have high content of Cl and S elements, and these elements produce a large amount of HCl and SO in the incineration process. 2 Equal acidity and wet deacidification for HCl and SO in flue gas 2 Such acid gases have a high removal efficiency, but the traditional wet deacidification process will inev...

Claims

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Application Information

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IPC IPC(8): B01D53/18B01D53/14B01D53/77B01D53/40B01D53/96
CPCB01D53/18B01D53/1456B01D53/1493B01D53/1418B01D53/77B01D53/40B01D53/96B01D2252/103B01D2251/304B01D2251/606B01D2257/2045B01D2257/302B01D2258/0291
Inventor 王曦王云刚朱学理许继云王磊
Owner 光大绿色环保管理(深圳)有限公司
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