CN215276608U - Multi-channel desulfurizing tower - Google Patents
Multi-channel desulfurizing tower Download PDFInfo
- Publication number
- CN215276608U CN215276608U CN202120249511.2U CN202120249511U CN215276608U CN 215276608 U CN215276608 U CN 215276608U CN 202120249511 U CN202120249511 U CN 202120249511U CN 215276608 U CN215276608 U CN 215276608U
- Authority
- CN
- China
- Prior art keywords
- confluence device
- air inlet
- desulfurizing tower
- confluence
- desulfurization tower
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Treating Waste Gases (AREA)
Abstract
The utility model provides a multi-channel desulfurizing tower, which relates to the technical field of desulfurizing towers and comprises a desulfurizing tower main body for removing sulfides, wherein an air inlet pipe is arranged at an air inlet of the desulfurizing tower main body and is connected with a confluence device for collecting waste gas generated by a plurality of combustion kilns; the confluence device is a component with an inner hollow part for placing a liquid desulfurizer, the air inlet pipe is connected to the top of the confluence device, an air inlet branch pipe for guiding waste gas generated by a single combustion kiln is installed at the top of the confluence device, and one end of the air inlet branch pipe extends into the confluence device and is close to the bottom. The scheme has the advantages of small land occupancy rate and low production cost.
Description
Technical Field
The utility model relates to a technical field of desulfurizing tower especially relates to a multichannel desulfurizing tower.
Background
The desulfurizing tower is used for the flue gas processing apparatus for containing sulphur burning thing, and the sulphur material can produce a large amount of sulfides after burning, and is great to the atmosphere pollution, lets the flue gas that contains sulfides handle through the desulfurizing tower, absorbs the sulfide or produces chemical reaction and reaches the purpose that reduces the sulfide and discharge.
According to the prior art, a combustion kiln can be correspondingly provided with a desulfurizing tower in a production plant area, the distribution of the desulfurizing tower is often related to the distribution of the combustion kiln, and when the combustion kiln is arranged more, the manufacturing cost of enterprises is increased.
SUMMERY OF THE UTILITY MODEL
Aiming at the defects in the prior art, the scheme provides the multi-channel desulfurizing tower which has the function that a plurality of combustion kilns adopt the same desulfurizing tower to carry out desulfurization treatment and has the advantages of small land occupancy rate and reduced production cost.
According to the embodiment of the utility model, the multichannel desulfurizing tower comprises a desulfurizing tower main body for removing sulfide, an air inlet pipe is arranged at the air inlet of the desulfurizing tower main body, and the air inlet pipe is connected with a confluence device for collecting waste gas generated by a plurality of combustion kilns; the confluence device is a component with an inner hollow part for placing a liquid desulfurizer, the air inlet pipe is connected to the top of the confluence device, an air inlet branch pipe for guiding waste gas generated by a single combustion kiln is installed at the top of the confluence device, and one end of the air inlet branch pipe extends into the confluence device and is close to the bottom.
Through above technical scheme, the device that converges can be collected the waste gas of all burning kilns and introduce inside the desulfurizing tower, a plurality of burning kilns use a desulfurizing tower to carry out desulfurization simultaneously, the installation quantity of the desulfurizing tower of reduction, the purchase cost of equipment has been reduced, simultaneously carry out desulfurization treatment to the waste gas that all burning kilns produced through using a desulfurizing tower, compare the traditional structure that adopts a burning kiln to correspond a desulfurizing tower, the land occupation area of desulfurizing tower has been reduced, the cost input of the production that further reduces. The inside splendid attire liquid desulfurizer of confluence device is used for carrying out preliminary desulfurization to waste gas, reuses the desulfurizing tower and carries out further desulfurization, has strengthened the desulfurization effect of device. The end part of the gas inlet branch pipe extends into the bottom position of the confluence device, so that the liquid desulfurizer can be submerged, and when waste gas enters the confluence device, the desulfurization effect of the device can be further enhanced; meanwhile, the liquid desulfurizer can absorb smoke dust particles contained in the waste, so that the possibility that the smoke dust particles enter the desulfurizing tower is reduced, and the pollution to the atmosphere is further reduced.
Preferably, a valve is arranged on the air inlet branch pipe.
Through above technical scheme, the valve can be used for opening and close the intercommunication situation of air inlet branch pipe and corresponding burning kiln, when wherein there is part burning kiln portion during operation, can close the valve that the burning kiln that does not work corresponds, reduces the possibility that liquid desulfurizer produces the refluence phenomenon because of the pressure differential.
Preferably, the top of the confluence device is provided with a liquid inlet pipe for conveniently introducing a liquid desulfurizer, and the liquid inlet pipe is provided with a control valve; the bottom of the confluence device is provided with an opening for conveniently discharging the liquid desulfurizer, and an end cover for plugging the opening is detachably arranged at the opening.
Through above technical scheme, the feed liquor pipe that sets up at the confluence device top can conveniently add liquid desulfurizer, can dismantle the end cover that sets up in the bottom and can conveniently discharge discarded liquid desulfurizer for the process of changing the desulfurizer is more convenient.
Preferably, a resilient sealing ring is arranged between the end cap and the bus bar.
Through the technical scheme, the sealing ring is used for further enhancing the sealing performance between the end cover and the confluence device and reducing the possibility of leakage of the liquid desulfurizer.
Preferably, the opening is circumferentially provided with a ring groove for mounting the sealing ring.
Through the technical scheme, the sealing ring can be conveniently installed on the annular groove, so that the positioning and the installation of the sealing ring are more accurate.
Preferably, the bottom of the confluence device is arranged obliquely, the liquid inlet pipe is positioned right above the high part of the bottom, and the opening is arranged at the lowest position close to the bottom.
Through above technical scheme, the opening that sets up in the device bottom of converging can conveniently be with the discharge of the sedimentary smog granule in the liquid desulfurizer, and the feed liquor pipe that sets up in the highest position department in bottom can be used for adding new liquid desulfurizer, can also be used for adding the washing liquid, washes out the granular impurity that will adhere to in the device bottom of converging.
Preferably, a transparent observation window is vertically arranged on one side of the confluence device.
Through above technical scheme, the transparent of vertical setting is observed and can be conveniently observed the liquid level height of the inside liquid desulfurizer of converging device, can also be used for observing whether liquid desulfurizer satisfies the state of desulfurization work, and convenient follow-up change is handled.
Compared with the prior art, the utility model discloses one of following beneficial effect has at least:
1. the waste gas of all the combustion kilns can be introduced into the same desulfurizing tower for treatment by utilizing the converging device, so that the purchase cost and the land use cost of equipment are reduced;
2. the utilization inside hollow confluence device can carry out primary desulfurization treatment to waste gas, and then the abandonment is discharged to the desulfurizing tower for secondary desulfurization treatment, has strengthened the desulfurization performance of device.
Drawings
FIG. 1 is a schematic overall structure diagram of an embodiment of the present application;
fig. 2 is an exploded view of the bus bar device.
In the above drawings: 1. a main body of the desulfurizing tower; 11. an air inlet pipe; 2. a confluence device; 21. an opening; 22. an end cap; 23. a seal ring; 24. a ring groove; 3. an intake branch pipe; 31. a valve; 4. a liquid inlet pipe; 41. a control valve; 5. and (6) an observation window.
Detailed Description
The technical solution of the present invention will be further explained with reference to the accompanying drawings and embodiments.
A multi-channel desulfurizing tower, referring to FIG. 1, comprises a desulfurizing tower body 1 for treating sulfide in sulfur-containing exhaust gas and a confluence device 2 for introducing exhaust gas of a plurality of combustion kilns into the desulfurizing tower body 1 simultaneously; the device can reduce the number of the desulfurizing towers, reduce the cost input of production equipment, simultaneously reduce the occupied area and further reduce the cost input.
Referring to fig. 1 and 2, the desulfurization tower main body 1 may be purchased by selecting a suitable model according to the needs of the site. An air inlet pipe 11 is installed at an air inlet of the desulfurizing tower main body 1, and the air inlet pipe 11 can be made of a corrosion-resistant pipeline.
The confluence device 2 is a hollow shell-shaped component, and the confluence device 2 is used for converging all waste gas generated by the combustion kiln and is also used for containing a liquid desulfurizer for primary desulfurization treatment; here, a rectangular parallelepiped member is formed with its bottom inclined, and one end of the intake pipe 11 communicates with the desulfurizing tower body 1 and the other end is connected to the top of the confluence device 2 and communicates with the inside of the confluence device 2.
Install the branch pipe 3 that admits air that is used for a plurality of waste gases of introducing single burning kiln production respectively at the top of converging device 2, adopt three branch pipe 3 here, the one end of branch pipe 3 stretches into the bottom position department of converging device 2, when introducing the waste gas that produces in every burning kiln to converging device 2, can be so that waste gas and liquid desulfurizer's reaction is better, the desulfurization effect of reinforcing device.
The intake branch pipe 3 is also provided with a valve 31, and when one or more combustion kilns do not work, the valve 31 is closed, so that the possibility of generating backflow of the liquid desulfurizer in the confluence device 2 can be reduced.
The top of the confluence device 2 is provided with a liquid inlet pipe 4 for adding the liquid desulfurizer, the liquid inlet pipe 4 is positioned at the position opposite to the highest position of the bottom, the liquid inlet pipe 4 is provided with a control valve 41, and when the liquid desulfurizer is not added, the control valve 41 is closed, so that the possibility that the waste gas in the confluence device 2 directly enters the atmosphere is reduced.
An opening 21 for discharging waste liquid desulfurizer is arranged on the confluence device 2, the opening 21 is positioned at the lowest position close to the bottom of the confluence device 2, an end cover 22 for closing the opening 21 is detachably arranged at the opening 21, the end cover 22 is a flat-plate-shaped member, the end cover 22 is fixed on the confluence device 2 by bolts, an elastic sealing ring 23 is arranged between the confluence device 2 and the end cover 22, and the sealing ring 23 can be made of corrosion-resistant rubber; to facilitate the installation of the sealing ring 23, a ring groove 24 is provided at the opening 21 around the circumference thereof, and the sealing ring 23 is installed in the ring groove 24.
When the liquid desulfurizer in the confluence device 2 needs to be replaced, the bottom surface arranged obliquely can conveniently discharge the smoke and dust absorbed by the liquid desulfurizer, the practicability of the device is improved, and the pollution to the atmosphere is reduced.
A transparent observation window 5 is vertically embedded in one side of the confluence device 2, and the transparent observation window 5 can be made of glass. The transparent observation window 5 is used for observing the liquid level height and the desulfurization quality of the liquid desulfurizing agent contained in the confluence device 2.
The application discloses multichannel desulfurizing tower's implementation principle does: install and debug the device, add liquid desulfurizer in the inside of converging device 2, make inlet branch 3 be located the tip submergence in converging device 2 in the liquid desulfurizer, connect inlet branch 3 respectively on the blast pipe of each burning kiln, waste gas that the burning kiln produced converges to the inside of converging device 2 through inlet branch 3, reentrant to desulfurizing tower main part 1 in, when the waste gas in inlet branch 3 converges, carry out primary desulfurization through liquid desulfurizer and handle, carry out secondary desulfurization through desulfurizing tower main part 1 again. The device can reduce the investment of production cost and improve the desulfurization effect of the device.
Finally, although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that the present invention can be modified or replaced by other means without departing from the spirit and scope of the present invention, which should be construed as limited only by the appended claims.
Claims (7)
1. A multi-channel desulfurization tower comprising a desulfurization tower main body (1) for removing sulfide, characterized in that: an air inlet pipe (11) is installed at an air inlet of the desulfurizing tower main body (1), and the air inlet pipe (11) is connected with a confluence device (2) for collecting waste gas generated by a plurality of combustion kilns; the utility model discloses a flue gas desulfurization device, including confluence device (2), intake pipe (11), branch pipe (3) that admits air, confluence device (2) is the component that an inside cavity is used for placing liquid desulfurizer, the top at confluence device (2) is connected in intake pipe (11), the top of confluence device (2) is installed and is used for guiding the waste gas that single burning kiln produced, the one end of branch pipe (3) stretches into in confluence device (2) and is close to bottom position department.
2. A multi-channel desulfurization tower in accordance with claim 1, wherein: and a valve (31) is arranged on the air inlet branch pipe (3).
3. A multi-channel desulfurization tower in accordance with claim 2, wherein: a liquid inlet pipe (4) for conveniently introducing a liquid desulfurizer is arranged at the top of the confluence device (2), and a control valve (41) is arranged on the liquid inlet pipe (4); the bottom of the confluence device (2) is provided with an opening (21) for conveniently discharging the liquid desulfurizer, and an end cover (22) for plugging the opening (21) is detachably mounted at the opening (21).
4. A multi-channel desulfurization tower in accordance with claim 3, wherein: an elastic sealing ring (23) is arranged between the end cover (22) and the confluence device (2).
5. A multi-channel desulfurization tower in accordance with claim 4, wherein: and a ring groove (24) for mounting a sealing ring (23) is formed in the circumferential direction of the opening (21).
6. A multi-channel desulfurization tower in accordance with claim 5, wherein: the bottom of the confluence device (2) is obliquely arranged, the liquid inlet pipe (4) is positioned right above the high part of the bottom, and the opening (21) is arranged at the position close to the lowest position of the bottom.
7. A multi-channel desulfurization tower in accordance with claim 1, wherein: one side of the confluence device (2) is vertically provided with a transparent observation window (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120249511.2U CN215276608U (en) | 2021-01-27 | 2021-01-27 | Multi-channel desulfurizing tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202120249511.2U CN215276608U (en) | 2021-01-27 | 2021-01-27 | Multi-channel desulfurizing tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215276608U true CN215276608U (en) | 2021-12-24 |
Family
ID=79530592
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202120249511.2U Active CN215276608U (en) | 2021-01-27 | 2021-01-27 | Multi-channel desulfurizing tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN215276608U (en) |
-
2021
- 2021-01-27 CN CN202120249511.2U patent/CN215276608U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107596798B (en) | Pre-dedusting, desulfurizing and denitrating integrated treatment device and method | |
| CN204933118U (en) | A kind of gas sampling treating apparatus with measuring ability | |
| CN105013259A (en) | Waste gas collection and treatment device with detection function | |
| CN2640584Y (en) | Integrated equipment for desulfurizing and discharging smoke | |
| CN215276608U (en) | Multi-channel desulfurizing tower | |
| CN206597446U (en) | A kind of wet type desulfurizing reaction unit | |
| CN206131026U (en) | Industrial boiler flue gas processing system | |
| CN204469519U (en) | A kind of flue gas desulfurization denitration dust-removing integrated device | |
| CN216062697U (en) | Inside and outside bucket self-loopa airlift wet flue gas desulfurization device | |
| CN213824090U (en) | High-efficient denitrification facility of cement kiln waste gas | |
| CN205650012U (en) | Desulfurization dust removal reduction machine | |
| CN211522105U (en) | Device for collecting smoke dust of coke oven | |
| CN209968067U (en) | Turbulent flow mixed type sintering machine flue gas dry desulfurization device | |
| CN208473958U (en) | A kind of automobile exhaust gas processing apparatus | |
| CN205412528U (en) | Novel high -efficient desulfurization dust remover | |
| CN206577587U (en) | Sulfurous gas liquid phase regenerating desulfurization integral system | |
| CN216005777U (en) | Radial tower device for converting organic sulfur in blast furnace gas | |
| CN217163715U (en) | Poisonous gas processing apparatus of coal mine production | |
| CN221085182U (en) | Desulfurizing tank | |
| CN212142067U (en) | Brickmaking waste gas treatment system | |
| CN203061041U (en) | Liquefied gas mercaptan removing tail gas treatment device | |
| CN206138991U (en) | Compound flue gas desulphurization device | |
| CN218981070U (en) | Desulfurization and mercury removal waste gas treatment device | |
| CN210905621U (en) | Flue gas pretreatment system for desulfurization and denitrification | |
| CN209475957U (en) | A kind of Rapid Circulation formula gas sweetening unit |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |