CN205549970U - Sulfur dioxide's adsorption equipment - Google Patents
Sulfur dioxide's adsorption equipment Download PDFInfo
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- CN205549970U CN205549970U CN201520927848.9U CN201520927848U CN205549970U CN 205549970 U CN205549970 U CN 205549970U CN 201520927848 U CN201520927848 U CN 201520927848U CN 205549970 U CN205549970 U CN 205549970U
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- sulfur dioxide
- variable
- adsorption bed
- pressure adsorption
- post
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses a sulfur dioxide's adsorption equipment, include: the dry post of silica gel, gas mixing ware, pressure swing adsorption bed, tail gas adsorption column, the dry post of silica gel includes the dry post of air silica gel, the dry post of sulfur dioxide silica gel, the dry post of sulfur dioxide silica gel is connected with pressure swing adsorption bed top through the pipeline, the dry post of air silica gel is connected with gas mixing ware, pressure swing adsorption bed bottom through the pipeline, pressure swing adsorption bed bottom is connected with the tail gas adsorption column through the pipeline in addition. The utility model provides a pair of sulfur dioxide's adsorption equipment, when administering the sulfur dioxide pollution, can also concentrated sulfur dioxide. Sulfur dioxide after the concentration can be used to relieving haperacidity, perhaps makes other use to the active carbon can use by recycle and regeneration.
Description
Technical field
The utility model relates to the adsorbent equipment of a kind of sulfur dioxide, belongs to air cleaning facility technical field.
Background technology
Sulfur dioxide is one of topmost atmosphere pollution, and its main source is fossil fuel, such as: coal and the burning from fuel oil such as the gasoline of oil, diesel oil, smelting and the tail gas etc. of sulfuric acid plant of some nonferrous metal sulfide mineral.
Flue gas desulfurization is the maximally efficient He main technological means of control of acid rain in the world and sulfur dioxide pollution.Comparing wet desulphurization to say, it is low that dry desulfurization has investment, the advantages such as equipment is the most perishable.
Utility model content
Purpose: in order to overcome the deficiencies in the prior art, the utility model provides the adsorbent equipment of a kind of sulfur dioxide.
Technical scheme: for solving above-mentioned technical problem, the technical solution adopted in the utility model is:
A kind of adsorbent equipment of sulfur dioxide, including: silica dehydrator post, gas mixer, variable-pressure adsorption bed, tail gas adsorption post, described silica dehydrator post includes air silica dehydrator post, sulfur dioxide silica dehydrator post；Described sulfur dioxide silica dehydrator post is connected with variable-pressure adsorption bed top by pipeline, and described air silica dehydrator post is connected with gas mixer, variable-pressure adsorption bed bottom by pipeline；Described variable-pressure adsorption bed bottom is connected with tail gas adsorption post additionally by pipeline.
Described variable-pressure adsorption bed including first variable-pressure adsorption bed, second variable-pressure adsorption bed, described sulfur dioxide silica dehydrator post, second variable-pressure adsorption bed top variable-pressure adsorption bed by two pipelines and first respectively is connected；Described air silica dehydrator post is connected by two pipelines and gas mixer, first variable-pressure adsorption bed, the second variable-pressure adsorption bed bottom respectively.
Also include that sulfur dioxide recovery bottle, described sulfur dioxide recovery bottle are connected with gas mixer by valve.
Described gas mixer and first variable-pressure adsorption bed, second variable-pressure adsorption bed between be provided with air compressor.
Described first variable-pressure adsorption bed, second is variable-pressure adsorption bed and is provided with vavuum pump between tail gas adsorption post
Preferably, also include gas flow meter, in described pipeline, be provided with multiple gas flow meter.
Beneficial effect: the adsorbent equipment of a kind of sulfur dioxide that the utility model provides, while administering sulfur dioxide pollution, it is also possible to concentrates sulfur dioxide.Sulfur dioxide after concentration can be used for relieving haperacidity, or makees other use, and activated carbon can use with circular regeneration.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with the accompanying drawings the utility model is further described.
As it is shown in figure 1, the adsorbent equipment of a kind of sulfur dioxide, sulfur dioxide silica dehydrator post 1 is connected by the variable-pressure adsorption bed top of 2, second variable-pressure adsorption bed 3 of two pipelines and first respectively；Air silica dehydrator post 4 is connected with gas mixer the 5, first variable-pressure adsorption bed bottom of 2, second variable-pressure adsorption bed 3 by two pipelines respectively；The described first variable-pressure adsorption bed bottom of 2, second variable-pressure adsorption bed 3 is connected with tail gas adsorption post 6 additionally by pipeline.Sulfur dioxide recovery bottle 7 is connected with gas mixer 5 by valve.It is provided with air compressor 8 between gas mixer 5 and first variable-pressure adsorption bed 2, second variable-pressure adsorption bed 3.It is provided with vavuum pump 9 between first variable-pressure adsorption bed 2, second variable-pressure adsorption bed 3 and tail gas adsorption post 6.Multiple gas flow meter 10 it is provided with, for measuring the flow of air or sulfur dioxide in described pipeline.
The above is only preferred embodiment of the present utility model; it is noted that, for those skilled in the art; on the premise of without departing from the utility model principle, it is also possible to make some improvements and modifications, these improvements and modifications also should be regarded as protection domain of the present utility model.
Claims (6)
1. the adsorbent equipment of a sulfur dioxide, it is characterised in that: including: silica dehydrator post, gas mixer, variable-pressure adsorption bed, tail gas adsorption post, described silica dehydrator post includes air silica dehydrator post, sulfur dioxide silica dehydrator post；Described sulfur dioxide silica dehydrator post is connected with variable-pressure adsorption bed top by pipeline, and described air silica dehydrator post is connected with gas mixer, variable-pressure adsorption bed bottom by pipeline；Described variable-pressure adsorption bed bottom is connected with tail gas adsorption post additionally by pipeline.
The adsorbent equipment of a kind of sulfur dioxide the most according to claim 1, it is characterized in that: described variable-pressure adsorption bed include first variable-pressure adsorption bed, second variable-pressure adsorption bed, described sulfur dioxide silica dehydrator post, second variable-pressure adsorption bed top variable-pressure adsorption bed by two pipelines and first respectively is connected；Described air silica dehydrator post is connected by two pipelines and gas mixer, first variable-pressure adsorption bed, the second variable-pressure adsorption bed bottom respectively.
The adsorbent equipment of a kind of sulfur dioxide the most according to claim 1, it is characterised in that: also include that sulfur dioxide recovery bottle, described sulfur dioxide recovery bottle are connected with gas mixer by valve.
The adsorbent equipment of a kind of sulfur dioxide the most according to claim 1, it is characterised in that: described gas mixer and first variable-pressure adsorption bed, second variable-pressure adsorption bed between be provided with air compressor.
The adsorbent equipment of a kind of sulfur dioxide the most according to claim 2, it is characterised in that: described first variable-pressure adsorption bed, second is variable-pressure adsorption bed and is provided with vavuum pump between tail gas adsorption post.
The adsorbent equipment of a kind of sulfur dioxide the most according to claim 1, it is characterised in that: also include gas flow meter, in described pipeline, be provided with multiple gas flow meter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520927848.9U CN205549970U (en) | 2015-11-20 | 2015-11-20 | Sulfur dioxide's adsorption equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520927848.9U CN205549970U (en) | 2015-11-20 | 2015-11-20 | Sulfur dioxide's adsorption equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205549970U true CN205549970U (en) | 2016-09-07 |
Family
ID=56823244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520927848.9U Expired - Fee Related CN205549970U (en) | 2015-11-20 | 2015-11-20 | Sulfur dioxide's adsorption equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205549970U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105251313A (en) * | 2015-11-20 | 2016-01-20 | 苏州韵蓝环保科技有限公司 | Adsorption device for sulfur dioxide |
-
2015
- 2015-11-20 CN CN201520927848.9U patent/CN205549970U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105251313A (en) * | 2015-11-20 | 2016-01-20 | 苏州韵蓝环保科技有限公司 | Adsorption device for sulfur dioxide |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160907 Termination date: 20161120 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |