CN204911138U - Tubular oxidization regeneration blender - Google Patents
Tubular oxidization regeneration blender Download PDFInfo
- Publication number
- CN204911138U CN204911138U CN201520471258.XU CN201520471258U CN204911138U CN 204911138 U CN204911138 U CN 204911138U CN 201520471258 U CN201520471258 U CN 201520471258U CN 204911138 U CN204911138 U CN 204911138U
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- Prior art keywords
- reaction chamber
- blender
- conversion zone
- inlet pipe
- air inlet
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- Gas Separation By Absorption (AREA)
Abstract
The utility model provides a production efficiency tubular oxidization regeneration blender high, that easily realize, it includes the conversion zone that is equipped with the reaction chamber in it the upper end of conversion zone set up with reaction chamber intercommunication have an inlet, and the lower extreme of conversion zone be provided with with the liquid outlet of reaction chamber intercommunication, and the well upper portion of reaction chamber transversely is provided with the intake pipe, and be provided with the gas vent of some on the pipe wall of intake pipe, the at least tip of intake pipe set up in the outside of conversion zone.
Description
Technical field
The utility model relates to a kind of oxidation regeneration blender, particularly relates to a kind of tubular type oxidation regeneration blender for desulfurization.
Background technology
The use of oxidation regeneration blender in desulphurization plant widely, for the effect that the desulfurization supplier of desulfurizing tower is important, the primary structure of oxidation regeneration blender of the prior art as shown in Figure 1, it mainly comprises desulfuration solution entrance 1, self-priming gas port 2, desulfuration solution outlet 3, the desulfuration solution sent here from solution pump at work enters at a high speed from desulfuration solution entrance 1, liquid produces negative pressure at self-priming gas port 2 place, thus produce oxidation reaction from ambient inlet air and doctor solution in inside, the reduce section of desulfuration solution in mixed regeneration device afterwards, in expanding reach, oxidation generates sulphur foam.The sulphur foam generated after regeneration and lean solution export 3 from desulfuration solution and flow out.There is above-mentioned principle known, in actual use, it is insufficient in use mainly to there is regenerative response in oxidation regeneration blender of the prior art, various losses in production are large, as the loss of thermal loss, catalyst, cause desulfuration efficiency to decline, add operating cost, reduce efficiency, be therefore necessary to be solved the problems referred to above, to adapt to reality need.
Summary of the invention
The purpose of this utility model is to overcome the deficiencies in the prior art, adapts to reality need, provides the tubular type oxidation regeneration blender that a kind of production efficiency is high, be easy to realization.
In order to realize the purpose of this utility model, the technical scheme that the utility model adopts is:
Design a kind of tubular type oxidation regeneration blender, it is characterized in that: it comprises in it conversion zone being provided with reaction chamber, what be communicated with described reaction chamber in the setting of the upper end of described conversion zone has inlet, and is provided with the liquid outlet be communicated with described reaction chamber in the lower end of described conversion zone; And be horizontally arranged with air inlet pipe in the middle and upper part of described reaction chamber, and be provided with the exhaust outlet of some on the tube wall of described air inlet pipe; At least one end of described air inlet pipe is arranged at the outside of described conversion zone.
Further, described exhaust outlet is arranged around described air inlet pipe tube wall.
Further, the both ends of described air inlet pipe are all arranged at the outside of described conversion zone.
Further, the below of the air inlet pipe in described reaction chamber is also provided with the air intake branch of at least one horizontally set, one end of described air intake branch is arranged at the outside of described conversion zone, and the end being arranged at the air intake branch of conversion zone outside is communicated with described air inlet pipe via breather line, and the tube wall of air intake branch in described reaction chamber is also provided with the gas outlet of some.
Further, described gas outlet is arranged around the tube wall of described air intake branch.
Further, the aperture of described steam vent, gas outlet is 1.0-8.0mm.
Further, described air intake branch is at least three, and from top to bottom spaced set in the below of described air inlet pipe.
Further, the air blast that be communicated with corresponding to an end of described air inlet pipe is also comprised.
Further, the reaction chamber of described conversion zone is cylinder-like structure.
Further, be also provided with in the upper end of described conversion zone be communicated with described reaction chamber and purge valve for the pressure in reaction chamber being carried out pressure release.
The beneficial effects of the utility model are:
1. high efficiency can realize sulphur foam by design of the present utility model in use, and not need the liquid to entering to pressurize in use, reduce the input of equipment.
2. the design's novel structure, be easy to realize, and production efficiency is high, can realize high efficiency and work for a long time, meets the needs that enterprise produces.
3. the utility model also has other advantages, will propose in the lump with corresponding structure in an embodiment.
Accompanying drawing explanation
Fig. 1 is oxidation regeneration blender primary structure schematic diagram in prior art;
Fig. 2 is primary structure schematic diagram of the present utility model;
In figure: the outlet of 1-desulfuration solution entrance, 2-self-priming gas port, 3-desulfuration solution, 4-air inlet pipe, 5-air intake branch, 6-inlet, 7-liquid outlet, 8-purge valve, 9-conversion zone, 10-breather line, 11-reaction chamber.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further illustrated:
Embodiment 1: a kind of tubular type oxidation regeneration blender, see Fig. 2, it comprises in it conversion zone 9 being provided with reaction chamber, as shown in the figure, the reaction chamber 11 of described conversion zone 9 is cylinder-like structure, what be communicated with described reaction chamber 11 in the setting of the upper end of described conversion zone 9 has inlet, and is provided with the liquid outlet 7 be communicated with described reaction chamber 11 in the lower end of described conversion zone, and be horizontally arranged with air inlet pipe 4 in the middle and upper part of described reaction chamber, and be provided with the exhaust outlet of some on the tube wall of described air inlet pipe 4, at least one end of described air inlet pipe 4 is arranged at the outside of described conversion zone, the both ends of the air inlet pipe 4 in the present embodiment are all arranged at the outside of described conversion zone, described exhaust outlet is arranged around described air inlet pipe tube wall, simultaneously, the below of the air inlet pipe 4 in described reaction chamber 11 is also provided with the air intake branch 5 of four horizontally sets, four air intake branches 5 spaced set from top to bottom, and one end of each air intake branch 5 below described air inlet pipe 4 is arranged at the outside of described conversion zone 11, and the end being arranged at the air intake branch 5 of conversion zone outside is communicated with described air inlet pipe via breather line 10, and the tube wall of air intake branch in described reaction chamber is also provided with the gas outlet of some, described gas outlet is arranged around the tube wall of described air intake branch.The aperture of above-described steam vent, gas outlet is 1.0-8.0mm, object to better implement the present invention, and the present embodiment also comprises the air blast that be communicated with corresponding to an end of described air inlet pipe; Simultaneously in order to avoid the pressure in reaction chamber is excessive, the design be also provided with in the upper end of described conversion zone be communicated with described reaction chamber and purge valve 8 for the pressure in reaction chamber being carried out pressure release.
In force, desulfurizing tower enters from inlet 6 from the desulfuration solution flow down, the gas (or compressed air) be blown into air blast is entered in reaction chamber by one end of air inlet pipe and bumps against with desulfuration solution, desulfuration solution is knocked into tiny liquid particles, its desulfuration solution so just can be made with air large area, contact fully, the air intake branch arranged below air inlet pipe can fully contact with doctor solution again, further oxidation reaction, thus oxidation generates more sulphur foam.The sulphur foam generated after regeneration and lean solution flow out from liquid outlet.
What embodiment of the present utility model was announced is preferred embodiment; but be not limited thereto; those of ordinary skill in the art; very easily according to above-described embodiment; understand spirit of the present utility model; and make different amplifications and change, but only otherwise depart from spirit of the present utility model, all in protection domain of the present utility model.
Claims (10)
1. a tubular type oxidation regeneration blender, it is characterized in that: it comprises in it conversion zone being provided with reaction chamber, what be communicated with described reaction chamber in the setting of the upper end of described conversion zone has inlet, and is provided with the liquid outlet be communicated with described reaction chamber in the lower end of described conversion zone; And be horizontally arranged with air inlet pipe in the middle and upper part of described reaction chamber, and be provided with the exhaust outlet of some on the tube wall of described air inlet pipe; At least one end of described air inlet pipe is arranged at the outside of described conversion zone.
2. tubular type oxidation regeneration blender as claimed in claim 1, is characterized in that: described exhaust outlet is arranged around described air inlet pipe tube wall.
3. tubular type oxidation regeneration blender as claimed in claim 1, is characterized in that: the both ends of described air inlet pipe are all arranged at the outside of described conversion zone.
4. tubular type oxidation regeneration blender as claimed in claim 1, it is characterized in that: the below of the air inlet pipe in described reaction chamber is also provided with the air intake branch of at least one horizontally set, one end of described air intake branch is arranged at the outside of described conversion zone, and the end being arranged at the air intake branch of conversion zone outside is communicated with described air inlet pipe via breather line, and the tube wall of air intake branch in described reaction chamber is also provided with the gas outlet of some.
5. tubular type oxidation regeneration blender as claimed in claim 4, is characterized in that: described gas outlet is arranged around the tube wall of described air intake branch.
6. tubular type oxidation regeneration blender as claimed in claim 4, is characterized in that: the aperture of described steam vent, gas outlet is 1.0-8.0mm.
7. tubular type oxidation regeneration blender as claimed in claim 4, is characterized in that: described air intake branch is at least three, and from top to bottom spaced set in the below of described air inlet pipe.
8. tubular type oxidation regeneration blender as claimed in claim 1, is characterized in that: also comprise the air blast that be communicated with corresponding to an end of described air inlet pipe.
9. tubular type oxidation regeneration blender as claimed in claim 1, is characterized in that: the reaction chamber of described conversion zone is cylinder-like structure.
10. tubular type oxidation regeneration blender as claimed in claim 1, is characterized in that: be also provided with in the upper end of described conversion zone be communicated with described reaction chamber and purge valve for the pressure in reaction chamber being carried out pressure release.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520471258.XU CN204911138U (en) | 2015-07-03 | 2015-07-03 | Tubular oxidization regeneration blender |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520471258.XU CN204911138U (en) | 2015-07-03 | 2015-07-03 | Tubular oxidization regeneration blender |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204911138U true CN204911138U (en) | 2015-12-30 |
Family
ID=54960324
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520471258.XU Expired - Fee Related CN204911138U (en) | 2015-07-03 | 2015-07-03 | Tubular oxidization regeneration blender |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204911138U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115445130A (en) * | 2022-08-23 | 2022-12-09 | 国网安徽省电力有限公司电力科学研究院 | Pipe flow mechanism for fire monitor |
-
2015
- 2015-07-03 CN CN201520471258.XU patent/CN204911138U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115445130A (en) * | 2022-08-23 | 2022-12-09 | 国网安徽省电力有限公司电力科学研究院 | Pipe flow mechanism for fire monitor |
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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: 20151230 Termination date: 20180703 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |