CN208642298U - A kind of desulfurization reactor - Google Patents
A kind of desulfurization reactor Download PDFInfo
- Publication number
- CN208642298U CN208642298U CN201821259882.3U CN201821259882U CN208642298U CN 208642298 U CN208642298 U CN 208642298U CN 201821259882 U CN201821259882 U CN 201821259882U CN 208642298 U CN208642298 U CN 208642298U
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- China
- Prior art keywords
- spray assemblies
- tower body
- spraying zone
- desulfurization reactor
- reactor according
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses a kind of desulfurization reactors, including tower body, two groups of spray assemblies, demarcation plate, getter assemblies, the demarcation plate to be horizontally set in the tower body, and the tower body inner cavity is separated into the first spraying zone and the second spraying zone；Two groups of spray assemblies are respectively the first spray assemblies, the second spray assemblies, and first spray assemblies are horizontally set in first spraying zone, and second spray assemblies are horizontally set in second spraying zone；The getter assembly includes aspiration channel, the guide duct for connecting with the aspiration channel and protruding into second spraying zone and the blower being arranged in the aspiration channel being located above first spray assemblies, and the air outlet of the blower is towards the guide duct；The tower body bottom is equipped with smoke inlet and the first leakage fluid dram, top are equipped with outlet flue, and the tower body is equipped with the second leakage fluid dram at the demarcation plate.The desulfurization reactor of the utility model can completely be reacted with the sulfur dioxide gas in flue gas, it is ensured that desulfurization degree.
Description
Technical field
The utility model relates to chemical technology production technical field more particularly to a kind of desulfurization reactors.
Background technique
In existing industrial production, wet desulphurization is a kind of most mature desulfurization method of technology, but in sweetening process,
Flue gas flows from bottom to top, in spray, cannot fully reflect the sulfur dioxide gas in flue gas, lead to a small portion
Sulfur dioxide gas is divided to be emitted into air.
In view of the above shortcomings, the designer, is actively subject to research and innovation, to found a kind of desulfurization reactor, make
It is with more the utility value in industry.
Utility model content
The purpose of this utility model is that propose a kind of desulfurization reactor, can completely with the sulfur dioxide gas in flue gas
Body is reacted.
For this purpose, the utility model uses following technical scheme:
A kind of desulfurization reactor, including tower body, two groups of spray assemblies, demarcation plate, getter assemblies, wherein
The demarcation plate is horizontally set in the tower body, and the tower body inner cavity is separated into the first spraying zone and the second spray
Area；
Two groups of spray assemblies are respectively the first spray assemblies, the second spray assemblies, and first spray assemblies are horizontally set with
In first spraying zone, second spray assemblies are horizontally set in second spraying zone；
The getter assembly includes being located at aspiration channel above first spray assemblies, connecting simultaneously with the aspiration channel
The blower for protruding into the guide duct of second spraying zone and being arranged in the aspiration channel, the air outlet of the blower is described in
Guide duct；
The tower body bottom is equipped with smoke inlet and the first leakage fluid dram, top are equipped with outlet flue, and the tower body is in described point
The second leakage fluid dram is equipped at partition.
Further, bottom is equipped with collecting tank and the air outlet plate above the collecting tank in the tower body, described
Air outlet plate is equipped with multiple exhaust vents, and the smoke inlet is connected with the guiding tube for protruding into the collecting tank.
Further, multiple blenders are equipped in the collecting tank.
Further, first leakage fluid dram is set to the liquid collecting bottom of pond portion, and first leakage fluid dram is equipped with and opens
It closes.
Further, the air outlet plate is the arc to the tower body bottom notch.
Further, the end of the outlet flue is equipped with demister, and is rotatably connected on the inner wall of the outlet flue
Towards the flooding nozzle of the demister.
Further, first spray assemblies and second spray assemblies include inlet tube, multiple settings in institute
State the spray head on inlet tube.
Further, the inner roof wall of the tower body is equipped with guide plate of the inclination towards the outlet flue.
The utility model has the following beneficial effects: the flue gas after being sprayed the first spraying zone using getter assembly is drawn onto second
Spraying zone is sprayed again, and spray can react away completely the sulfur dioxide in flue gas twice, ensures desulfurization effect significantly.
Detailed description of the invention
Fig. 1 is the structural schematic diagram for the desulfurization reactor that specific embodiment of the present invention provides.
In figure: 10- tower body, the first spraying zone of 11-, the second spraying zone of 12-, 13- smoke inlet, the first leakage fluid dram of 14-, 15-
Outlet flue, the second leakage fluid dram of 16-, 17- collecting tank, 18- switch, 19- guide plate, the first spray assemblies of 20-, 21- inlet tube,
22- spray head, the second spray assemblies of 30-, 40- demarcation plate, 51- aspiration channel, 52- guide duct, 53- blower, 60- air outlet plate, 61- go out
Air holes, 70- guiding tube, 80- blender, 91- demister, 92- flooding nozzle.
Specific embodiment
Further illustrate the technical solution of the utility model below with reference to the accompanying drawings and specific embodiments.
As shown in Figure 1, the desulfurization reactor of the utility model includes 10, two groups of spray assemblies, demarcation plates 40, air-breathing of tower body
Component.Wherein, demarcation plate 40 is horizontally set in tower body 10, and 10 inner cavity of tower body is separated into the first spraying zone 11 and the second spraying zone
12；Two groups of spray assemblies are respectively the first spray assemblies 20, the second spray assemblies 30, and the first spray assemblies 20 are horizontally set in the first spray
Area 11 is drenched, the second spray assemblies 30 are horizontally set in the second spraying zone 12；Getter assembly includes being located at 20 top of the first spray assemblies
Aspiration channel 51, the guide duct 52 for being connect with aspiration channel 51 and protruding into the second spraying zone 12 and the blower being arranged in aspiration channel 51
53, the air outlet of blower 53 is towards guide duct 52；10 bottom of tower body is equipped with smoke inlet 13 and the first leakage fluid dram 14, top are equipped with
Mouth 15, and tower body 10 is equipped with the second leakage fluid dram 16 at demarcation plate 40.
The utility model can carry out desulfurization twice to flue gas using the first spray assemblies 20 and the second spray assemblies 30, significantly
Improve desulfurization degree；Flue gas after first spraying zone 11 spray can be drawn onto the second spraying zone 12 and be sprayed again by getter assembly
Leaching, and the first leakage fluid dram 14 and the second leakage fluid dram 16 is respectively set in the first spraying zone 11 and the second spraying zone 12, being convenient for will be anti-
Liquid after answering is completely exhausted out.
In order to further increase desulfuration efficiency, the utility model bottom in tower body 10 is equipped with collecting tank 17 and is located at collection
The air outlet plate 60 of 17 top of liquid pool, air outlet plate 60 are equipped with multiple exhaust vents 61, and smoke inlet 13, which is connected with, protrudes into collecting tank 17
Guiding tube 70.The flue gas entered from smoke inlet 13 is first passed into collecting tank 17 and is reacted, and unreacted flue gas is from exhaust vent
61, which exit into the first spraying zone 11, carries out desulfurization.
In order to which unreacted flue gas is discharged from exhaust vent 61, the utility model is equipped with multiple blenders in collecting tank 17
80.By the stirring of blender 80, makes flow of flue gas and be discharged.
In addition, the first leakage fluid dram 14 is set to 17 bottom of collecting tank, and the first leakage fluid dram 14 is equipped with switch 18.
In order to which the liquid for spraying the first spray assemblies 20 enters collecting tank 17 and is discharged, the utility model is by air outlet plate 60
To be taken advantage of a situation into collecting tank 17 convenient for liquid to the arc of 10 bottom notch of tower body.
Furthermore it is also possible to which demister 91 is arranged on the end of outlet flue 15, and direction is set on the inner wall of outlet flue 15
The flooding nozzle 92 of demister 91.The drop that the carrying of the flue gas after desulfurization can be removed using demister 91, utilizes flooding nozzle 92
Demister 92 can be cleaned up.
In order to comprehensively clean demister 91, the utility model rotates the inner wall of flooding nozzle 92 and outlet flue 15
Connection rotates flooding nozzle 92, so as to clean demister 91 from different angles.
Specifically, the first spray assemblies 20 and the second spray assemblies 30 include inlet tube 21, multiple settings in inlet tube
Spray head 22 on 21.
In addition, being smoothly discharged for the ease of the flue gas after desulfurization, the utility model is equipped on the inner roof wall of tower body 10
Tilt the guide plate 19 towards outlet flue 15.
To sum up, the desulfurization reactor of the utility model can completely be reacted with the sulfur dioxide gas in flue gas,
Desulfurization degree is ensured significantly.
Technical principle of the utility model has been described above with reference to specific embodiments.These descriptions are intended merely to explain this reality
With novel principle, and it cannot be construed to the limitation to scope of protection of the utility model in any way.Based on the explanation herein,
Those skilled in the art, which does not need to pay for creative labor, can associate with other specific implementation modes of this utility model,
These modes are fallen within the protection scope of the utility model.
Claims (8)
1. a kind of desulfurization reactor, which is characterized in that including tower body (10), two groups of spray assemblies, demarcation plate (40), air-breathing group
Part, wherein
The demarcation plate (40) is horizontally set in the tower body (10), and the tower body (10) inner cavity is separated into the first spraying zone (11)
With the second spraying zone (12)；
Two groups of spray assemblies are respectively the first spray assemblies (20), the second spray assemblies (30), first spray assemblies
(20) it is horizontally set in first spraying zone (11), second spray assemblies (30) are horizontally set in second spraying zone (12)；
The getter assembly includes aspiration channel (51) and the aspiration channel being located above first spray assemblies (20)
(51) blower for connecting and protruding into the guide duct (52) of second spraying zone (12) and being arranged in the aspiration channel (51)
(53), the air outlet of the blower (53) is towards the guide duct (52)；
Tower body (10) bottom is equipped with smoke inlet (13) and the first leakage fluid dram (14), top are equipped with outlet flue (15), and described
The second leakage fluid dram (16) are equipped at tower body (10) Yu Suoshu demarcation plate (40).
2. desulfurization reactor according to claim 1, which is characterized in that the interior bottom of the tower body (10) is equipped with collecting tank
(17) and the air outlet plate (60) above the collecting tank (17), the air outlet plate (60) are equipped with multiple exhaust vents
(61), the smoke inlet (13) is connected with the guiding tube (70) for protruding into the collecting tank (17).
3. desulfurization reactor according to claim 2, which is characterized in that be equipped with multiple blenders in the collecting tank (17)
(80)。
4. desulfurization reactor according to claim 2, which is characterized in that first leakage fluid dram (14) is set to the collection
Liquid pool (17) bottom, and first leakage fluid dram (14) is equipped with switch (18).
5. desulfurization reactor according to claim 2, which is characterized in that the air outlet plate (60) is to the tower body (10)
The arc of bottom notch.
6. desulfurization reactor according to claim 1, which is characterized in that the end of the outlet flue (15) is equipped with demisting
Device (91), and the flooding nozzle (92) towards the demister (91) is rotatably connected on the inner wall of the outlet flue (15).
7. desulfurization reactor according to claim 1, which is characterized in that first spray assemblies (20) and described second
Spray assemblies (30) include inlet tube (21), multiple spray heads (22) being arranged on the inlet tube (21).
8. desulfurization reactor according to claim 1, which is characterized in that the inner roof wall of the tower body (10) is equipped with inclination
Towards the guide plate (19) of the outlet flue (15).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821259882.3U CN208642298U (en) | 2018-08-06 | 2018-08-06 | A kind of desulfurization reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821259882.3U CN208642298U (en) | 2018-08-06 | 2018-08-06 | A kind of desulfurization reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208642298U true CN208642298U (en) | 2019-03-26 |
Family
ID=65788280
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821259882.3U Expired - Fee Related CN208642298U (en) | 2018-08-06 | 2018-08-06 | A kind of desulfurization reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208642298U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237686A (en) * | 2019-06-10 | 2019-09-17 | 安徽恒晟重工科技有限公司 | A kind of fume treatment auxiliary |
-
2018
- 2018-08-06 CN CN201821259882.3U patent/CN208642298U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237686A (en) * | 2019-06-10 | 2019-09-17 | 安徽恒晟重工科技有限公司 | A kind of fume treatment auxiliary |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190326 Termination date: 20200806 |
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| CF01 | Termination of patent right due to non-payment of annual fee |