CN218740362U - Stepped stripping tower plate - Google Patents
Stepped stripping tower plate Download PDFInfo
- Publication number
- CN218740362U CN218740362U CN202223176345.1U CN202223176345U CN218740362U CN 218740362 U CN218740362 U CN 218740362U CN 202223176345 U CN202223176345 U CN 202223176345U CN 218740362 U CN218740362 U CN 218740362U
- Authority
- CN
- China
- Prior art keywords
- tower
- plate
- tower plate
- plate component
- component
- 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
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a stepped stripping tower plate, which comprises a first tower plate component, a second tower plate component, a feeding baffle, a middle baffle and a tower plate overflow plate component, wherein one end of the first tower plate component is connected with the inner end part of an outer cylinder of a stripping tower, the other end of the first tower plate component is connected with the second tower plate component, and the first tower plate component and the second tower plate component transversely penetrate through the inner end part of the outer cylinder of the stripping tower; the feeding baffle is vertically arranged at the side end of the first tower plate assembly, and the middle baffle is vertically arranged between the first tower plate assembly and the second tower plate assembly; through with the cascaded installation of first column plate subassembly and second column plate subassembly in this application, and first column plate subassembly is higher than the second column plate subassembly, and the first column plate subassembly and the second column plate subassembly of cascaded installation are passed simultaneously from bottom to top to gas in the tower, are favorable to reducing column plate gas-liquid resistance, advance simultaneously to the installation of baffle, well baffle and column plate overflow board subassembly, have prevented crossing of foam.
Description
Technical Field
The utility model relates to a relevant technical field of chemical industry equipment, concretely relates to cascaded blow-off column plate.
Background
Current typical gas stripping equipment:
1. packed tower
The blowing-off device is a device with higher efficiency, but the waste water is relatively dirty and easy to block, and the requirement on the distributor is high, so that the blowing-off device is not suitable for the working condition with small liquid load.
2. Conventional plate tower
When the liquid and gas are small, the fluid distribution on the tower plate is not ideal, and the blowing efficiency is seriously influenced by the short circuit phenomenon.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a cascaded column plate that blows off to solve the current problem of proposing in the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme: a stepped stripping tower plate comprises a first tower plate component, a second tower plate component, a feeding baffle, a middle baffle and a tower plate overflow plate component, wherein one end of the first tower plate component is connected with the inner end part of an outer barrel of a stripping tower, the other end of the first tower plate component is connected with the second tower plate component, and the first tower plate component and the second tower plate component transversely penetrate through the inner end part of the outer barrel of the stripping tower;
the feeding baffle is vertically arranged at the side end part of the first tower plate component, the middle baffle is vertically arranged between the first tower plate component and the second tower plate component, and a tower plate overflow plate component is also vertically arranged at the other side of the second tower plate component;
the first tower plate component and the second tower plate component are installed in a stepped mode, and the first tower plate component is higher than the second tower plate component.
Preferably, the tray overflow plate assembly consists of a vertical plate and an inclined plate, and the vertical plate and the inclined plate are fixedly connected.
Preferably, the first tray assembly and the second tray assembly adopt vertical sieve plates.
Compared with the prior art, the beneficial effects of the utility model are that: through with the cascaded installation of first column plate subassembly and second column plate subassembly in this application, and first column plate subassembly is higher than the second column plate subassembly, and the first column plate subassembly and the second column plate subassembly of cascaded installation are passed simultaneously from bottom to top to gas in the tower, are favorable to reducing column plate gas-liquid resistance, advance simultaneously to the installation of baffle, well baffle and column plate overflow board subassembly, have prevented crossing of foam.
Drawings
FIG. 1 is a cross-sectional view of the present invention;
fig. 2 is a top view of the present invention.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative efforts all belong to the protection scope of the present invention.
As shown in fig. 1-2, the utility model discloses a stepped stripping tower plate, which comprises a first tower plate component 1, a second tower plate component 2, a feeding baffle 3, a middle baffle 4 and a tower plate overflow plate component 5, wherein one end of the first tower plate component 1 is connected with the inner end of an outer cylinder 6 of a stripping tower, the other end of the first tower plate component 1 is connected with the second tower plate component 2, and the first tower plate component 1 and the second tower plate component 2 transversely penetrate through the inner end of the outer cylinder 6 of the stripping tower;
the feeding baffle 3 is vertically arranged at the side end part of the first tower plate component 1, the middle baffle 4 is vertically arranged between the first tower plate component 1 and the second tower plate component 2, and the other side of the second tower plate component 2 is also vertically provided with a tower plate overflow plate component 5;
the first tower plate assembly 1 and the second tower plate assembly 2 are installed in a stepped mode, and the first tower plate assembly 1 is higher than the second tower plate assembly 2.
The tray overflow plate assembly 5 is composed of a vertical plate 51 and an inclined plate 52, and the vertical plate 51 and the inclined plate 52 are fixedly connected.
The first tower plate component 1 and the second tower plate component 2 both adopt vertical sieve plates. The front end of first column tray subassembly 1 and second column tray subassembly 2 in this application still is provided with middle overflow weir 7, and the rear end of first column tray subassembly 1 and second column tray subassembly 2 is provided with export overflow weir 8, and middle overflow weir 7 and export overflow weir 8 have the effect of keeping on the board liquid layer and making liquid evenly overflow.
Through with the cascaded installation of first column plate subassembly 1 and second column plate subassembly 2 in this application, and first column plate subassembly 1 is higher than second column plate subassembly 2, and the first column plate subassembly 1 and the second column plate subassembly 2 of the cascaded installation are passed simultaneously to gas from bottom to top in the tower, are favorable to reducing column plate gas-liquid resistance, advance simultaneously to baffle 3, well baffle 4 and the installation of column plate overflow plate subassembly 5, have prevented crossing of foam. The position difference between the first tower plate component 1 and the second tower plate component 2 is beneficial to reducing the gas-liquid resistance of the tower plates, and the foam layers are uniform, so that the phenomenon of efficiency reduction caused by the short circuit of tower plate fluid is thoroughly eliminated; meanwhile, after the efficiency of the tower plate is improved, the height of the stripping tower can be effectively reduced.
This structure is dedicated to media with too low liquid-gas ratio and difficult desorption, as follows:
(1) The residual ammonia in the waste liquid is blown off by air and water vapor, the air containing ammonia is blown out to be used as air for boiler combustion, and because the air quantity is very large, the ammonia content in the blown-off air is extremely low, a large amount of steam can be saved, the blowing-off effect is good, and the residual ammonia in the waste water is extremely low.
(2) In the chemical production process, a liquid product is subjected to air stripping and stripping of certain volatile component in a tower by using a heated carrier gas source, the blown gas is subjected to washing (freezing) separation and then circularly enters the blowing-stripping process again, the purity of the carrier is high, no impurity enters the product, and the residual impurity in the product is low.
The utility model discloses the standard part that uses all can purchase from the market, dysmorphism piece all can be customized according to the description with the record of attached drawing, the concrete connected mode of each part all adopts conventional means such as ripe bolt, rivet, welding among the prior art, machinery, part and equipment all adopt among the prior art, conventional model, including circuit connection adopts conventional connected mode among the prior art, and the details are not repeated here, and the content that does not make detailed description in this description belongs to the prior art that expert technical personnel know in this field.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments or portions thereof without departing from the spirit and scope of the invention.
Claims (3)
1. A step-type stripping tower plate is characterized in that: the tower plate component comprises a first tower plate component (1), a second tower plate component (2), a feeding baffle (3), a middle baffle (4) and a tower plate overflow plate component (5), wherein one end of the first tower plate component (1) is connected with the inner end part of an outer barrel (6) of a stripping tower, the other end of the first tower plate component (1) is connected with the second tower plate component (2), and the first tower plate component (1) and the second tower plate component (2) transversely penetrate through the inner end part of the outer barrel (6) of the stripping tower;
the feeding baffle (3) is vertically arranged at the side end part of the first tower plate component (1), the middle baffle (4) is vertically arranged between the first tower plate component (1) and the second tower plate component (2), and the other side of the second tower plate component (2) is also vertically provided with a tower plate overflow plate component (5);
the first tower plate assembly (1) and the second tower plate assembly (2) are installed in a stepped mode, and the first tower plate assembly (1) is higher than the second tower plate assembly (2).
2. The stepped blow-off tray of claim 1, wherein: the tray overflow plate assembly (5) consists of a vertical plate (51) and an inclined plate (52), and the vertical plate (51) and the inclined plate (52) are fixedly connected.
3. The stepped blow-off tray of claim 1, wherein: the first tower plate component (1) and the second tower plate component (2) both adopt vertical sieve plates.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223176345.1U CN218740362U (en) | 2022-11-29 | 2022-11-29 | Stepped stripping tower plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202223176345.1U CN218740362U (en) | 2022-11-29 | 2022-11-29 | Stepped stripping tower plate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218740362U true CN218740362U (en) | 2023-03-28 |
Family
ID=85676476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202223176345.1U Active CN218740362U (en) | 2022-11-29 | 2022-11-29 | Stepped stripping tower plate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218740362U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117185397A (en) * | 2023-09-27 | 2023-12-08 | 山东海思环境工程有限公司 | High ammonia nitrogen industrial wastewater treatment device |
-
2022
- 2022-11-29 CN CN202223176345.1U patent/CN218740362U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN117185397A (en) * | 2023-09-27 | 2023-12-08 | 山东海思环境工程有限公司 | High ammonia nitrogen industrial wastewater treatment device |
| CN117185397B (en) * | 2023-09-27 | 2024-03-29 | 山东海思环境工程有限公司 | High ammonia nitrogen industrial wastewater treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN218740362U (en) | Stepped stripping tower plate | |
| CN102267868A (en) | Industrial production apparatus for trichloroethylene | |
| CN102626558A (en) | Tail gas recovery in polyimide film production process | |
| CN202538412U (en) | Tail gas reclaiming device in polyimide film producing process | |
| CN201762266U (en) | Trichloroethylene industrialized production device | |
| CN201990614U (en) | Continuous dealcoholizing device used for dicapryl phthalate | |
| CN201603410U (en) | Energy-saving continuous alcohol-rectification recovery tower | |
| CN101279179B (en) | Technique for recovering aluminum rolling oil mist | |
| CN201304261Y (en) | Porous three-dimensional gas-liquid contact element | |
| CN213160833U (en) | Pipe cap type grid plate structure | |
| CN211659298U (en) | Deacidification ammonia still | |
| CN108554126A (en) | A kind of continuous rectifying tower exhaust gas purification system | |
| CN204619396U (en) | For the evaporimeter of hydrogen peroxide and the distributor of use thereof | |
| CN204952602U (en) | Fog formula graphite falling liquid film absorber falls | |
| CN212701226U (en) | Effectively improve separator of gaseous recovery efficiency of monomethylamine | |
| CN2581061Y (en) | Gas-liquid parallel flow reactor | |
| CN219290639U (en) | Device for extracting organic solvent from raffinate acid in phosphoric acid production by wet purification | |
| CN219481593U (en) | Rectifying gas-liquid distributor | |
| CN201258248Y (en) | Chlorine gas drying tower | |
| CN210845710U (en) | Gas-liquid separator with double-stage separation function | |
| CN219290638U (en) | Device for concentrating and separating organic solvent from back extraction dilute acid in phosphoric acid production by wet purification | |
| CN217391613U (en) | Decompression tower and environment-friendly glazing agent production facility | |
| CN214654668U (en) | Negative pressure debenzolization tower | |
| CN219757042U (en) | Exhaust steam recovery device | |
| CN220213966U (en) | Energy-saving fractionating tower |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |