CN220802585U - Decarburization tower with high decarburization efficiency - Google Patents
Decarburization tower with high decarburization efficiency Download PDFInfo
- Publication number
- CN220802585U CN220802585U CN202321772606.8U CN202321772606U CN220802585U CN 220802585 U CN220802585 U CN 220802585U CN 202321772606 U CN202321772606 U CN 202321772606U CN 220802585 U CN220802585 U CN 220802585U
- Authority
- CN
- China
- Prior art keywords
- tower body
- tower
- water
- decarburization
- outlet pipe
- 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.)
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- 238000005261 decarburization Methods 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- 239000000945 filler Substances 0.000 claims abstract description 22
- 230000007423 decrease Effects 0.000 claims description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 40
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 20
- 239000001569 carbon dioxide Substances 0.000 abstract description 10
- 239000011347 resin Substances 0.000 abstract description 7
- 229920005989 resin Polymers 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000007921 spray Substances 0.000 abstract description 3
- 230000002265 prevention Effects 0.000 abstract 1
- 238000012856 packing Methods 0.000 description 12
- 150000001768 cations Chemical class 0.000 description 7
- 150000001450 anions Chemical class 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000002585 base Substances 0.000 description 4
- 238000005262 decarbonization Methods 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000026676 system process Effects 0.000 description 1
Landscapes
- Gas Separation By Absorption (AREA)
Abstract
The utility model discloses a decarburization tower with high decarburization efficiency, which comprises a tower body, wherein the tower body is cylindrical, a filler area is arranged in the middle of the tower body, the filler area comprises a grid support plate fixedly connected with the tower wall of the tower body, a plurality of fillers are placed on the grid support plate, an air outlet pipe is arranged at the top of the tower body, a spray pipe is arranged between the air outlet pipe and the filler area, one end of the spray pipe is connected with a water inlet pipe, a descending pipeline is arranged below the filler area of the tower body, an air inlet pipe inserted from one side outside the tower body is arranged in the descending pipeline, the air inlet pipe is connected with a fan, a water outlet pipe is connected with a water seal device, and the water outlet pipe is blocked by the water seal device to play a role of wind prevention and leakage, so that the air inlet can only pass through the filler area from bottom to top, the content of carbon dioxide can be effectively reduced, the exchange capacity of negative resin can be improved, and the production cost can be reduced.
Description
Technical Field
The utility model relates to the technical field of decarburization towers, in particular to a decarburization tower with high decarburization efficiency.
Background
The current ion exchange system process is: cation exchanger- & gt decarburization tower- & gt intermediate water tank- & gt anion exchanger. The decarburization tower has the following functions: the effluent of the cation bed contains a large amount of bicarbonate HCO 3-which combines with H+ in the water to form carbonic acid H2CO3. The carbon dioxide remover is used for removing CO2 gas in the water of the positive bed so as to reduce heavy carbonate radicals entering the water of the negative bed. When raw water passes through the cation resin, cations in the water are adsorbed, H+ carried by the resin is replaced into the water, so that the water is acidic, when the PH is less than 4, the water almost exists in a carbon dioxide gas form, and if the PH is not removed, the carbon dioxide gas reacts with the anion resin, so that the exchange capacity of the anion resin is shortened, the working period is shortened, and the water production cost is increased.
The working principle of the existing decarbonization tower is that according to henry's law, in a certain volume of solution, the dissolved gas content is in direct proportion to the partial pressure of the gas on the liquid level, when a decarbonization fan blows air into the tower, packing is filled in the tower to increase the contact area between the water of a cation bed and the air, when the water of the cation bed flows downwards from the tower, and in the process of the air flowing upwards from the bottom, the partial pressure of CO2 gas in the air is far smaller than the partial pressure of CO2 in the water of the cation bed, so that the CO2 gas in the water escapes.
In the prior art, a part of air after the air enters the fan easily flows out from the water outlet, and the effect of carrying carbon dioxide cannot be achieved, so that the working efficiency of the decarburization tower is reduced.
Disclosure of utility model
In order to solve the technical problems, the utility model relates to a decarburization tower with high decarburization efficiency, which has a simple and reliable structure, effectively solves the technical problems, is suitable for popularization and use, and is realized by the following technical scheme:
The utility model provides a decarbonization tower with high decarbonization efficiency, includes the tower body, the tower body is cylindrically, the middle part of tower body is equipped with the district of packing, the district of packing includes the grid backup pad with tower body tower wall fixed connection, a plurality of packing has been placed in the grid backup pad, the top of tower body is equipped with the outlet duct, the tower body is equipped with the shower between outlet duct and the district of packing, the inlet tube is connected to the one end of shower, a plurality of spouts of shower are towards the district of packing, the tower body is equipped with down the pipeline in the below of packing district, be equipped with from the air-supply line of tower body outside one side male in the pipeline of falling, the air-supply line is connected with the fan, the below of down the pipeline is connected with the outlet pipe, the outlet pipe links to each other with water seal device.
The above-mentioned scheme is based on and is a preferable scheme of the above-mentioned scheme: the filler is a multi-surface hollow sphere.
The above-mentioned scheme is based on and is a preferable scheme of the above-mentioned scheme: the descending pipeline is in a truncated cone shape with a large upper part and a small lower part.
The above-mentioned scheme is based on and is a preferable scheme of the above-mentioned scheme: the water seal device comprises a water tank, the bottom plate of the tower body is fixedly connected with the top of the water tank, the water outlet pipe is positioned in the water tank, and an overflow pipe is arranged on one side of the upper part of the water tank.
The above-mentioned scheme is based on and is a preferable scheme of the above-mentioned scheme: the air blower is fixedly arranged on the base, and the lower part of the base is fixedly connected with the two sliding blocks.
Compared with the prior art, the utility model has the following outstanding and beneficial technical effects: the water sealing device is used for sealing the water outlet pipe to prevent wind leakage, so that the air inlet can only take out carbon dioxide from bottom to top through the filler area, the content of carbon dioxide can be effectively reduced, the exchange capacity of the anion resin can be improved, the use amount of liquid alkali can be reduced, and the production cost is reduced.
Drawings
FIG. 1 is a schematic diagram of an overall device connection structure;
FIG. 2 is a schematic diagram of a fan installation.
Detailed Description
In order to make the objects, technical solutions and advantages of the present utility model more apparent, the technical solutions in the embodiments will be clearly and completely described with reference to the drawings in the embodiments, however, the following detailed description and the embodiments are only for illustrative purposes and not limiting the utility model.
In the description of the present utility model, it should be understood that the terms "longitudinal," "transverse," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like indicate orientations or positional relationships based on the orientation or positional relationships shown in fig. 1, merely for convenience in describing the present utility model, and do not indicate or imply that the device or element being referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the utility model.
In the description of the present application, the terms "first," "second," and the like are used for descriptive purposes only and are not to be construed as indicating or implying relative importance or implicitly indicating the number of technical features indicated.
In the prior art, a part of wind easily flows out from a water outlet after the wind enters a fan 8, and the effect of carrying carbon dioxide is not achieved, so that the working efficiency of a decarburization tower is reduced, and in order to solve the technical problems, as shown in fig. 1-2, the utility model relates to a decarburization tower with high decarburization efficiency, which comprises a tower body 1, wherein the tower body 1 is cylindrical, a filler area 2 is arranged in the middle of the tower body 1, the filler area 2 comprises a grid supporting plate 3 fixedly connected with the tower wall of the tower body 1, a plurality of fillers are arranged on the grid supporting plate 3, and the fillers are preferably polyhedral hollow spheres, and the polyhedral hollow spheres have the advantages of high gas speed, more blades, small resistance, large specific surface area and the like, and can fully solve the gas-liquid exchange, effectively disperse water into a linear shape, a film shape or a water drop shape, so that the contact area of water and air is increased, the separation path of CO2 from water is shortened, and the resistance is reduced, and the separation speed of CO2 from water is increased.
The top of tower body 1 is equipped with outlet duct 4, tower body 1 is equipped with shower 5 between outlet duct 4 and packing district 2, the inlet tube is connected to shower 5's one end, shower 5's a plurality of spouts are towards packing district 2, tower body 1 is equipped with down pipeline 6 in packing district 2's below, down pipeline 6 is the round platform shape of big-end-up preferably, can make top-down inflow liquid export downwards fast, and the toper structure avoids producing ponding in the inner wall, be equipped with the air-supply line 7 of inserting from tower body 1 outside one side in the down pipeline 6, air-supply line 7 is connected with fan 8, and fan 8 is preferably centrifugal fan 8, can carry out the air inlet of high-efficient and stable, down pipeline 6's below is connected with outlet pipe 9, outlet pipe 9 links to each other with water seal arrangement. Further, the water seal device comprises a water tank 10, the bottom plate of the tower body 1 is fixedly connected with the top of the water tank 10, the water outlet pipe 9 is positioned inside the water tank 10, an overflow pipe 11 is arranged on one side of the upper part of the water tank 10, and the hydrostatic pressure with a certain height is utilized to resist the pressure change in the water outlet pipe 9 in a water seal mode, so that the gas in the pipe is prevented from moving downwards.
Further, still include base 12, guide rail 13, slider 14, two guide rail 13 symmetry sets up at water tank 10 top, every guide rail 13 and a slider 14 sliding connection, fan 8 fixed mounting is on base 12, the below and the two slider 14 fixed connection of base 12, the air outlet and the air-supply line 7 of fan 8 pass through bolt piece and dismantle fixed connection, can clean air-supply line 7 and the inside pipe wall of decline pipeline 6 after fan 8 and air-supply line 7 split, can follow guide rail 13 direction after the cleaning is accomplished and remove fan 8 and make its air outlet and air-supply line 7 laminating contact after again according to the bolt piece, the cooperation of guide rail and slider is convenient for fan 8's location installation, the later maintenance of being convenient for.
When the device works, anode effluent enters from the upper part, is sprayed down through the spray pipe 5, is discharged into the water tank 10 from the lower part after passing through the packing layer, and air for removing CO2 is sent in from one side of the downcomer through the fan 8 and is discharged from the top together with the removed CO2 after passing through the packing layer. In the carbon remover, water flowing down from above is dispersed into many small water streams, water drops or films due to the blocking effect of the filler, and is fully contacted with air. Since the amount of CO2 in air is small and its partial pressure is about 0.03% of atmospheric pressure, when air and water come into contact, CO2 in water is separated out and carried away by air and discharged into the atmosphere. The water sealing device is used for sealing the water outlet pipe 9 to play a role in preventing wind leakage, so that the air inlet can only carry out carbon dioxide from bottom to top through the filler area 2, the content of carbon dioxide can be effectively reduced, the exchange capacity of anion resin can be improved, the use amount of liquid alkali can be reduced, and the production cost is reduced.
It should be noted that technical features such as fans, fillers, etc. related to the present application should be considered as the prior art, and specific structures, working principles, and control modes and spatial arrangements possibly related to the technical features should be selected conventionally in the art, and should not be considered as the points of the present application, where the present application is not further specifically developed.
The above embodiments are only preferred embodiments of the present utility model, and are not intended to limit the scope of the present utility model in this way, therefore: equivalent changes in structure, shape and principle of the present utility model should be covered by the protection scope of the present utility model.
Claims (2)
1. A decarburization tower with high decarburization efficiency is characterized in that: the tower body is cylindrical, the middle part of tower body is equipped with the filler district, the filler district includes the grid backup pad with tower body tower wall fixed connection, a plurality of fillers have been placed in the grid backup pad, the top of tower body is equipped with the outlet duct, the tower body is equipped with the shower between outlet duct and filler district, the inlet tube is connected to one end of shower, a plurality of spouts of shower are towards the filler district, the tower body is equipped with the decline pipeline in the below in filler district, be equipped with from the external one side male air-supply line of tower in the decline pipeline, the air-supply line is connected with the fan, the below of decline pipeline is connected with the outlet pipe, the outlet pipe is connected with water seal arrangement, the decline pipeline is big-end-up's round platform shape, water seal arrangement includes the water tank, the bottom plate and the water tank top fixed connection of tower body, the outlet pipe is located inside the water tank, the overflow pipe has still including base, guide rail, slider, two the guide rail symmetry sets up at the water tank top, every guide rail and a sliding connection, two fixed mounting are connected with the base below the slider.
2. The decarburization tower having a high decarburization efficiency as recited in claim 1, wherein: the filler is a multi-surface hollow sphere.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202321772606.8U CN220802585U (en) | 2023-07-06 | 2023-07-06 | Decarburization tower with high decarburization efficiency |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202321772606.8U CN220802585U (en) | 2023-07-06 | 2023-07-06 | Decarburization tower with high decarburization efficiency |
Publications (1)
Publication Number | Publication Date |
---|---|
CN220802585U true CN220802585U (en) | 2024-04-19 |
Family
ID=90710376
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202321772606.8U Active CN220802585U (en) | 2023-07-06 | 2023-07-06 | Decarburization tower with high decarburization efficiency |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN220802585U (en) |
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2023
- 2023-07-06 CN CN202321772606.8U patent/CN220802585U/en active Active
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