CN221062263U - Spray tower for silica gel production - Google Patents
Spray tower for silica gel production Download PDFInfo
- Publication number
- CN221062263U CN221062263U CN202322559436.1U CN202322559436U CN221062263U CN 221062263 U CN221062263 U CN 221062263U CN 202322559436 U CN202322559436 U CN 202322559436U CN 221062263 U CN221062263 U CN 221062263U
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- CN
- China
- Prior art keywords
- silica gel
- atomizing
- heating
- pipe
- pipeline
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- 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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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 55
- 239000000741 silica gel Substances 0.000 title claims abstract description 55
- 229910002027 silica gel Inorganic materials 0.000 title claims abstract description 55
- 239000007921 spray Substances 0.000 title claims abstract description 42
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims abstract description 42
- 238000001035 drying Methods 0.000 claims abstract description 22
- 239000006096 absorbing agent Substances 0.000 claims abstract description 15
- 238000004321 preservation Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 14
- 239000001301 oxygen Substances 0.000 claims description 14
- 229910052760 oxygen Inorganic materials 0.000 claims description 14
- 230000018044 dehydration Effects 0.000 abstract description 6
- 238000006297 dehydration reaction Methods 0.000 abstract description 6
- 238000000889 atomisation Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 17
- 230000000694 effects Effects 0.000 description 3
- 238000007493 shaping process Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000003463 adsorbent Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Silicon Compounds (AREA)
Abstract
The utility model discloses a spray tower for producing silica gel, which relates to the technical field of silica gel production equipment and comprises a main body, wherein a dehydration plate is arranged in the main body, a heating and drying device is arranged below the dehydration plate, a circulating water tank is arranged at the bottom of the heating and drying device, an atomizing device is arranged on one side of the main body, an air inlet pipe is arranged below the atomizing device, a pipeline is arranged on the other side of the main body, a spray header is arranged at one end of the pipeline, and a pump body is arranged below the pipeline. According to the utility model, under the combined action of the air heater, the compressor, the heating pipe, the heat preservation shell, the heat absorber and the air pipe, the spray tower has the function of heating and drying during processing and production of silica gel, so that the phenomenon that the surface of the silica gel is excessively wet due to moisture generated by an atomization device is avoided, the subsequent storage of the silica gel is inconvenient, and the moisture on the surface of the silica gel can be evaporated and removed in a heating mode.
Description
Technical Field
The utility model relates to the technical field of silica gel production equipment, in particular to a spray tower for silica gel production.
Background
Silica gel is porous material with different particle sizes, which is formed by properly dehydrating silicic acid gel, has an open porous structure, a large specific surface area and can adsorb a plurality of substances, is a good drying agent, adsorbent and catalyst carrier, has wide application in many aspects, and a spray tower is common gas treatment equipment, and is used for treating gas by spraying spray liquid with specific components from top to bottom, contacting with the gas and reacting. The following problems exist in the prior art:
1. The existing spray tower for producing silica gel cannot increase the moisture in the spray tower, the production quality of the silica gel is reduced due to excessive drying during processing and production in the tower, and the silica gel is difficult to form and has low practicability;
2. The existing silica gel production spray tower still has a large amount of residual moisture on the surface after the silica gel production and processing, cannot be removed in time, is inconvenient to store, does not have the mode of drying through heating to remove the moisture on the surface, and has lower functionality.
Disclosure of utility model
In order to solve the technical problems, the utility model adopts the following technical scheme:
The utility model provides a silica gel production spray column, includes the main part, the inside of main part is provided with the dehydration board, the below of dehydration board is provided with heating drying device, heating drying device's bottom is provided with the circulating water pond, one side of main part is provided with atomizing device, atomizing device's below is provided with the intake pipe, the opposite side of main part is provided with the pipeline, one end of pipeline is provided with the shower head, the below of pipeline is provided with the pump body; the heating and drying device comprises an air heater, a compressor, a heating pipe, a heat preservation shell, a heat absorber and an air pipe, wherein the compressor is positioned at one side of the air heater, and the heat preservation shell is positioned at the upper end of the compressor; the lower end of the heat preservation shell is fixedly connected with the upper end of the compressor, and one side of the compressor is fixedly connected with one side of the air heater.
The technical scheme of the utility model is further improved as follows: the air pipe is positioned in the heat-insulating shell, the heating pipe is positioned in the air pipe, and the heat absorber is positioned at the upper end of the heating pipe.
The technical scheme of the utility model is further improved as follows: the upper end and the lower end of the air pipe are fixedly connected with the inside of the heat preservation shell, and the lower end of the heat absorber is detachably connected with the upper end of the heating pipe.
The technical scheme of the utility model is further improved as follows: the atomizing device comprises an atomizing cup, a suction nozzle, a face mask, an atomizing humidifier, an air bag and an oxygen humidifier, wherein the suction nozzle is located on one side of the atomizing cup, the face mask is located at the upper end of the atomizing cup, the air bag is located on one side of the face mask, the atomizing humidifier is located on one side of the atomizing cup, and the oxygen humidifier is located at the lower end of the atomizing humidifier.
The technical scheme of the utility model is further improved as follows: one side of suction nozzle passes through connecting hole and one side fixed connection of atomizing cup, one side of atomizing humidifier passes through connecting pipe and one side fixed connection of atomizing cup, the lower extreme of atomizing humidifier and the upper end fixed connection of oxygen humidifier.
The technical scheme of the utility model is further improved as follows: one end of the pipeline is fixedly connected with the upper end of the spray header, and one side of the circulating water tank is fixedly connected with one side of the main body through the pipeline.
By adopting the technical scheme, compared with the prior art, the utility model has the following technical progress:
The utility model provides a spray tower for producing silica gel, which can have the function of heating and drying when the silica gel is processed and produced by the combined action of an air heater, a compressor, a heating pipe, a heat preservation shell, a heat absorber and an air pipe, so that the surface of the silica gel is prevented from being excessively wet due to moisture generated by an atomization device, the surface of the silica gel is inconvenient to store, moisture on the surface of the silica gel can be evaporated and removed in a heating mode, the air in the spray tower can be compressed by the combined action of the compressor and the heat absorber, surrounding hot air is absorbed, the air is heated by the heating pipe, and finally the hot air generated by the operation of the air heater blows the heat from the air pipe to the surface of the silica gel, so that the moisture on the surface of the silica gel can be heated and evaporated, and the drying effect is realized, and the spray tower is very practical and efficient.
The utility model provides a silica gel production spray tower, which can improve the humidity of silica gel in the spray tower under the combined action of an atomizing cup, a suction nozzle, a face mask, an atomizing humidifier, an air bag and an oxygen humidifier, so that the reduction of the production quality of the silica gel caused by excessive drying in the tower is avoided, the silica gel is not easy to form due to the excessive temperature, the gas in the tower is sucked into the atomizing cup through the suction nozzle, the gas in the atomizing cup is converted through the oxygen humidifier and the atomizing humidifier, so that the water molecules in the atomizing cup are increased, the humidity of the gas in the atomizing cup reaches a constant value when the air bag bulges, and the gas in the atomizing cup is discharged into the spray tower through a plurality of leakage holes formed in the surface of the face mask, so that the humidity in the tower is increased, and the silica gel is easier to form.
Drawings
FIG. 1 is a schematic diagram of a silica gel production spray tower according to the present utility model;
Fig. 2 is a schematic structural view of a heating and drying device according to the present utility model;
fig. 3 is a schematic structural view of the atomizing device according to the present utility model.
In the figure: 1. a main body; 2. a spray header; 3. a dewatering plate; 4. a pipe; 5. a pump body; 6. a circulating water tank; 7. an air inlet pipe; 8. a heating and drying device; 81. an air heater; 82. a compressor; 83. heating pipes; 84. a thermal insulation housing; 85. a heat absorber; 86. an air duct; 9. an atomizing device; 91. an atomizing cup; 92. a suction nozzle; 93. a face mask; 94. an atomizing humidifier; 95. an air bag; 96. an oxygen humidifier.
Detailed Description
The utility model is further illustrated by the following examples:
Examples
As shown in fig. 1-3, the utility model provides a spray tower for silica gel production, which comprises a main body 1, wherein a dehydration plate 3 is arranged in the main body 1, a heating and drying device 8 is arranged below the dehydration plate 3, a circulating water tank 6 is arranged at the bottom of the heating and drying device 8, an atomizing device 9 is arranged on one side of the main body 1, an air inlet pipe 7 is arranged below the atomizing device 9, a pipeline 4 is arranged on the other side of the main body 1, a spray header 2 is arranged at one end of the pipeline 4, and a pump body 5 is arranged below the pipeline 4; the heating and drying device 8 comprises a hot air blower 81, a compressor 82, a heating pipe 83, a heat preservation shell 84, a heat absorber 85 and an air pipe 86, wherein the compressor 82 is positioned on one side of the hot air blower 81, and the heat preservation shell 84 is positioned at the upper end of the compressor 82; the lower extreme of heat preservation shell 84 is fixed connection with the upper end of compressor 82, and one side of compressor 82 and one side fixed connection of air heater 81, tuber pipe 86 are located the inside of heat preservation shell 84, and heating pipe 83 is located the inside of tuber pipe 86, and heat absorber 85 is located the upper end of heating pipe 83, and the upper and lower end of tuber pipe 86 and the inside fixed connection of heat preservation shell 84, the lower extreme of heat absorber 85 and the upper end detachable connection of heating pipe 83.
In this embodiment, can make this spray column possess the heating stoving function when producing silica gel processing, avoid the silica gel surface to lead to its surface too moist because of the moisture that atomizing device 9 produced, be inconvenient for follow-up to store it, can evaporate its surperficial moisture through the mode of heating and get rid of, through compressor 82 and absorber 85 combined action under, can compress the inside gas of spray column, and absorb surrounding hot gas, carry out heating treatment through heating pipe 83 to gas, finally blow the heat from tuber pipe 86 to silica gel surface through the hot-blast that the air heater 81 produced work, the moisture of its surface then can be heated and evaporate, thereby realize the effect of stoving, and is very practical high-efficient.
Examples
As shown in fig. 1-3, on the basis of embodiment 1, the present utility model provides a technical solution: preferably, the atomizing device 9 comprises an atomizing cup 91, a suction nozzle 92, a mask 93, an atomizing humidifier 94, an air bag 95 and an oxygen humidifier 96, wherein the suction nozzle 92 is positioned on one side of the atomizing cup 91, the mask 93 is positioned at the upper end of the atomizing cup 91, the air bag 95 is positioned on one side of the mask 93, the atomizing humidifier 94 is positioned on one side of the atomizing cup 91, the oxygen humidifier 96 is positioned at the lower end of the atomizing humidifier 94, one side of the suction nozzle 92 is fixedly connected with one side of the atomizing cup 91 through a connecting hole, one side of the atomizing humidifier 94 is fixedly connected with one side of the atomizing cup 91 through a connecting pipe, and the lower end of the atomizing humidifier 94 is fixedly connected with the upper end of the oxygen humidifier 96.
In this embodiment, can improve the inside moisture of silica gel at the spray column, avoid too dry silica gel production quality decline that leads to in the tower, and because of the too high silica gel difficult shaping that makes of temperature, with the inside gaseous suction atomizing cup 91 of tower inside by suction nozzle 92, and through the oxygen humidifier 96 that is equipped with atomizing humidifier 94 to the inside gaseous conversion of atomizing cup 91, make its inside hydrone increase, indicate when gasbag 95 swell that the inside gaseous humidity of atomizing cup 91 reaches the constant value, at this moment with the inside gaseous discharge to the spray column inside of atomizing cup 91 through a plurality of leak holes that face guard 93 surface was equipped with, then can increase the inside moisture of tower, make the silica gel more easily shaped.
Examples
As shown in fig. 1-3, on the basis of embodiment 1, the present utility model provides a technical solution: preferably, one end of the pipeline 4 is fixedly connected with the upper end of the spray header 2, and one side of the circulating water pool 6 is fixedly connected with one side of the main body 1 through the pipeline 4.
The working principle of the silica gel production spray tower is specifically described below.
When the spray tower is used, as shown in fig. 1-3, the spray tower can have the function of heating and drying during the processing and production of silica gel by the heating and drying device 8, so that the phenomenon that the surface of the silica gel is excessively wet due to moisture generated by the atomizing device 9 is avoided, the surface of the silica gel is inconvenient to store, the moisture on the surface of the silica gel can be evaporated and removed in a heating manner, the gas in the spray tower can be compressed and the surrounding hot gas is absorbed under the combined action of the compressor 82 and the heat absorber 85, the gas is heated by the heating pipe 83, finally the heat is blown to the surface of the silica gel from the air pipe 86 by hot air generated by the operation of the hot air blower 81, the moisture on the surface of the silica gel can be heated and evaporated, and the drying effect is realized, the utility model discloses it is very high-efficient to can improve the inside moisture of silica gel at the spray column by atomizing device 9, avoid the tower to excessively dry and lead to silica gel production quality to descend, and because of the too high shaping that makes silica gel, it is inside with tower internal gas inhalation atomizing cup 91 by suction nozzle 92, and through the oxygen humidifier 96 that is equipped with atomizing humidifier 94 to the inside gas of atomizing cup 91 converts, make its inside hydrone increase, it reaches the constant value to indicate atomizing cup 91 inside gas humidity when gasbag 95 swell, at this moment with atomizing cup 91 inside gas through a plurality of leak holes that face guard 93 surface was equipped with to the inside discharge of spray column, then can increase tower inside moisture, make silica gel more easily shaping.
The foregoing utility model has been generally described in great detail, but it will be apparent to those skilled in the art that modifications and improvements can be made thereto. Accordingly, it is intended to cover modifications or improvements within the spirit of the inventive concepts.
Claims (6)
1. The utility model provides a silica gel production spray column, includes main part (1), its characterized in that: the novel water heater is characterized in that a dewatering plate (3) is arranged inside the main body (1), a heating and drying device (8) is arranged below the dewatering plate (3), a circulating water tank (6) is arranged at the bottom of the heating and drying device (8), an atomizing device (9) is arranged on one side of the main body (1), an air inlet pipe (7) is arranged below the atomizing device (9), a pipeline (4) is arranged on the other side of the main body (1), a spray header (2) is arranged at one end of the pipeline (4), and a pump body (5) is arranged below the pipeline (4);
The heating and drying device (8) comprises an air heater (81), a compressor (82), a heating pipe (83), a heat-preserving shell (84), a heat absorber (85) and an air pipe (86), wherein the compressor (82) is positioned on one side of the air heater (81), and the heat-preserving shell (84) is positioned at the upper end of the compressor (82);
The lower end of the heat preservation shell (84) is fixedly connected with the upper end of the compressor (82), and one side of the compressor (82) is fixedly connected with one side of the air heater (81).
2. A silica gel production spray tower as claimed in claim 1, wherein: the air pipe (86) is positioned in the heat-preserving shell (84), the heating pipe (83) is positioned in the air pipe (86), and the heat absorber (85) is positioned at the upper end of the heating pipe (83).
3. A silica gel production spray tower as claimed in claim 2, wherein: the upper end and the lower end of the air pipe (86) are fixedly connected with the inside of the heat preservation shell (84), and the lower end of the heat absorber (85) is detachably connected with the upper end of the heating pipe (83).
4. A silica gel production spray tower as claimed in claim 1, wherein: the atomizing device (9) comprises an atomizing cup (91), a suction nozzle (92), a mask (93), an atomizing humidifier (94), an air bag (95) and an oxygen humidifier (96), wherein the suction nozzle (92) is located on one side of the atomizing cup (91), the mask (93) is located at the upper end of the atomizing cup (91), the air bag (95) is located on one side of the mask (93), the atomizing humidifier (94) is located on one side of the atomizing cup (91), and the oxygen humidifier (96) is located at the lower end of the atomizing humidifier (94).
5. The silica gel production spray tower of claim 4 wherein: one side of suction nozzle (92) is through connecting hole and one side fixed connection of atomizing cup (91), one side of atomizing humidifier (94) is through connecting pipe and one side fixed connection of atomizing cup (91), the lower extreme of atomizing humidifier (94) is with the upper end fixed connection of oxygen humidifier (96).
6. A silica gel production spray tower as claimed in claim 1, wherein: one end of the pipeline (4) is fixedly connected with the upper end of the spray header (2), and one side of the circulating water pool (6) is fixedly connected with one side of the main body (1) through the pipeline (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322559436.1U CN221062263U (en) | 2023-09-20 | 2023-09-20 | Spray tower for silica gel production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322559436.1U CN221062263U (en) | 2023-09-20 | 2023-09-20 | Spray tower for silica gel production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221062263U true CN221062263U (en) | 2024-06-04 |
Family
ID=91271040
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322559436.1U Active CN221062263U (en) | 2023-09-20 | 2023-09-20 | Spray tower for silica gel production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221062263U (en) |
-
2023
- 2023-09-20 CN CN202322559436.1U patent/CN221062263U/en active Active
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