CN218421927U - Gemini spraying tower - Google Patents
Gemini spraying tower Download PDFInfo
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- CN218421927U CN218421927U CN202122452895.0U CN202122452895U CN218421927U CN 218421927 U CN218421927 U CN 218421927U CN 202122452895 U CN202122452895 U CN 202122452895U CN 218421927 U CN218421927 U CN 218421927U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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Abstract
The utility model provides a twin spray tower, including the main tower, and the recovery tower that sets up with the main tower symmetry, the main tower is the same with the tower body structure of recovery tower, the main tower includes the tower body, tower body left side wall from the top down is equipped with access hole N2 in proper order, access hole N3, air inlet N4a, overflow mouth N5, filler N6, drain N7, the right wall from the top down of tower body is equipped with circulation liquid import N10 in proper order, air inlet N4a, level gauge mouth N9b, level gauge mouth N9a, circulation liquid export N8, the circulation liquid import N10 of main tower is linked together through the circulation liquid export N8 of first circulating pipe with the recovery tower, circulation liquid export N8 of main tower be linked together through the circulation liquid import N10 of second circulating pipe with the recovery tower, the gas vent N1 of main tower links to each other through blast pipe and the N4a of recovery tower air inlet. The beneficial effects of the utility model are that through taking two tower structures, water circulation in two towers all the time realizes that the temperature is roughly balanced in two towers, reduces the influence that waste gas and particle raw materials reaction caused, improves processingquality.
Description
Technical Field
The utility model belongs to the technical field of chemical industry equipment, especially, relate to a Gemini spray tower.
Background
The spray tower is also called as a spray tower. The absorption tower is provided with no filler or access board but with a nozzle. The liquid enters from the top of the tower and is sprayed into a fog shape or a raindrop shape through a nozzle; gas enters from the lower part of the tower and is closely contacted with the mist or raindrop-shaped liquid for mass transfer, so that the easily soluble components in the gas are absorbed. Waste gas generated in the reaction tower is generally discharged through the exhaust hole, and the generated heat is wasted; if the pigment is directly introduced into the reaction tower for use, the pigment can react with the granular pigment, and the product quality is influenced.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a Gemini spray tower, its waste heat that make full use of waste gas has, the make full use of energy improves product quality, is particularly suitable for being used for producing various particle pigment.
The technical scheme of the utility model is that: a twin spray tower comprises a main tower and a recovery tower which is symmetrically arranged with the main tower, the main tower and the recovery tower have the same tower body structure,
the main tower comprises a tower body, an exhaust port N1 is arranged at the top end of the tower body, a maintenance port N2, a maintenance port N3, an air inlet N4a, an overflow port N5, a water filling port N6 and a sewage draining port N7 are sequentially arranged on the left wall of the tower body from top to bottom, a circulating liquid inlet N10, an air inlet N4a, a liquid level meter port N9b, a liquid level meter port N9a and a circulating liquid outlet N8 are sequentially arranged on the right wall of the tower body from top to bottom, a lower manhole N11 is arranged at the lower end of the front side of the tower body,
a remote temperature measuring port T3 and a local temperature measuring port G3 are respectively arranged at the position of a circulating liquid inlet N10, a remote temperature measuring port T2 and a local temperature measuring port G2 are arranged in the right wall of the tower body and are flush with the access port N3, the access port N3 is arranged below the first grating and the liquid collecting ring, the air inlet N4a and the air inlet N4b are arranged below the second grating and are arranged symmetrically left and right, a remote temperature measuring port T1 and a local temperature measuring port G1 are arranged on the right wall of the tower body between the liquid level meter port N9b and the liquid level meter port N9a,
the recycling tower is characterized in that a circulating liquid inlet N10 of the main tower is communicated with a circulating liquid outlet N8 of the recycling tower through a first circulating pipe, the circulating liquid outlet N8 of the main tower is communicated with the circulating liquid inlet N10 of the recycling tower through a second circulating pipe, a first water pump and a first switch valve are arranged on the first circulating pipe, a second water pump and a second switch valve are arranged on the second circulating pipe, an air outlet N1 of the main tower is connected with an air inlet N4a of the recycling tower through an exhaust pipe, an air pump and a third switch valve are arranged on the exhaust pipe, a spiral heat dissipation pipeline is arranged in the recycling tower, and the spiral heat dissipation pipeline is connected with the air outlet N1 of the recycling tower.
Preferably, the service opening N2 is on the same horizontal line as the circulating liquid inlet N10.
Preferably, the bottom end of the main tower is provided with a base, and the bottom end of the recovery tower is provided with a recovery seat.
Preferably, the outer walls of the main tower and the recovery tower are both provided with heat insulation cotton.
The utility model has the advantages and positive effects be: by adopting the technical scheme, the water circulation in the two towers is always realized by adopting the double-tower structure, so that the water temperature in the two towers is approximately balanced, the influence caused by the reaction of waste gas and particle raw materials is reduced, and the processing quality is improved.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
In the figure:
| 1. main tower | 2. Recovery tower | 3. First grid |
| 4. Second grid | 5. First circulation pipe | 6. Second circulation pipe |
| 7. And (4) exhausting the gas. |
Detailed Description
As shown in figure 1, the technical proposal of the utility model is a twin spray tower, which comprises a main tower 1 and a recovery tower 2 symmetrically arranged with the main tower 1, the main tower 1 and the recovery tower 2 have the same tower body structure,
the main tower 1 comprises a tower body, an exhaust port N1 is arranged at the top end of the tower body, a maintenance port N2, a maintenance port N3, an air inlet N4a, an overflow port N5, a water filling port N6 and a sewage discharge port N7 are sequentially arranged on the left wall of the tower body from top to bottom, a circulating liquid inlet N10, an air inlet N4b, a liquid level meter port N9a and a circulating liquid outlet N8 are sequentially arranged on the right wall of the tower body from top to bottom, a lower manhole N11 is arranged at the lower end of the front side of the tower body,
a remote temperature measuring port T3 and a local temperature measuring port G3 are respectively arranged at the position of a circulating liquid inlet N10, a remote temperature measuring port T2 and a local temperature measuring port G2 are arranged in the right wall of the tower body and are flush with the access port N3, the access port N3 is arranged below the first grating 3 and the liquid collecting ring, the air inlet N4a and the air inlet N4b are arranged below the second grating 4 and are arranged in bilateral symmetry, a remote temperature measuring port T1 and a local temperature measuring port G1 are arranged on the right wall of the tower body between the liquid level meter port N9b and the liquid level meter port N9a,
the recycling tower is characterized in that a circulating liquid inlet N10 of a main tower 1 is communicated with a circulating liquid outlet N8 of a recycling tower 2 through a first circulating pipe 5, the circulating liquid outlet N8 of the main tower 1 is communicated with the circulating liquid inlet N10 of the recycling tower 2 through a second circulating pipe 6, a first water pump and a first switch valve are arranged on the first circulating pipe 5, a second water pump and a second switch valve are arranged on the second circulating pipe 6, an exhaust port N1 of the main tower 1 is connected with an air inlet N4a of the recycling tower through an exhaust pipe 7, an air pump and a third switch valve are arranged on the exhaust pipe 7, a spiral heat dissipation pipeline is arranged in the recycling tower 2 and is connected with the exhaust port N1 of the recycling tower 2, the internal structure of the main tower 1 is the same as that of an existing spraying tower, the reaction principle of the spraying tower is the same as that of the existing spraying tower, the internal structure of the recycling tower 2 is provided with the spiral heat dissipation pipeline communicated with the spiral heat dissipation pipeline, other spaces store water sources, and the rest of the recycling tower are closed when the rest of the surplus openings are left openings.
In this embodiment, the access opening N2 and the circulating liquid inlet N10 are on the same horizontal line.
In this embodiment, the bottom end of the main tower 1 is provided with a base, and the bottom end of the recovery tower 2 is provided with a recovery base.
In this embodiment, the outer walls of the main tower 1 and the recovery tower 2 are both provided with heat insulation cotton.
The working process and principle of the example are as follows: during the use, the waste gas that produces the reaction of main tower 1 enters into recovery tower 2 through blast pipe 7 in, flow the in-process in the spiral heat dissipation pipeline, the realization is with the effect on the heat transfer of waste gas to recovery tower 2 internal water, then with the water in the recovery tower 2 along first circulating pipe 5 enter into main tower 1 in, simultaneously in main tower 1 the lower water of temperature let in to recovery tower 2 in continue the heat transfer can, analogize in proper order, realize main tower 1 and recovery tower 2 internal circulation heat transfer, water temperature is roughly balanced in two towers, accomplish recovery tower 2 and carry out thermal conversion, reduce the waste of the energy, and the quality of processing is improved.
While one embodiment of the present invention has been described in detail, the description is only a preferred embodiment of the present invention, and should not be considered as limiting the scope of the present invention. The equivalent changes and improvements made according to the application scope of the present invention should be still included in the patent coverage of the present invention.
Claims (4)
1. A Gemini spray tower is characterized in that: comprises a main tower and a recovery tower which is symmetrically arranged with the main tower, the main tower and the recovery tower have the same tower body structure,
the main tower comprises a tower body, an exhaust port N1 is arranged at the top end of the tower body, a maintenance port N2, a maintenance port N3, an air inlet N4a, an overflow port N5, a water filling port N6 and a sewage draining port N7 are sequentially arranged on the left wall of the tower body from top to bottom, a circulating liquid inlet N10, an air inlet N4a, a liquid level meter port N9b, a liquid level meter port N9a and a circulating liquid outlet N8 are sequentially arranged on the right wall of the tower body from top to bottom, a lower manhole N11 is arranged at the lower end of the front side of the tower body,
a remote temperature measuring port T3 and an in-situ temperature measuring port G3 are respectively arranged at the circulating liquid inlet N10, a remote temperature measuring port T2 and an in-situ temperature measuring port G2 are arranged in the right wall of the tower body and are flush with the access port N3, the access port N3 is arranged below the first grating and the liquid collecting ring, the air inlet N4a and the air inlet N4b are arranged below the second grating and are arranged in bilateral symmetry, a remote temperature measuring port T1 and an in-situ temperature measuring port G1 are arranged on the right wall of the tower body between the liquid level meter port N9b and the liquid level meter port N9a,
the circulation liquid import N10 of main tower be linked together through the circulation liquid export N8 of first circulating pipe with the recovery tower, the circulation liquid export N8 of main tower be linked together through the circulation liquid import N10 of second circulating pipe with the recovery tower, be equipped with first water pump and first ooff valve on the first circulating pipe, be equipped with second water pump and second ooff valve on the second circulating pipe, gas vent N1 of main tower links to each other through the air inlet N4a of blast pipe with the recovery tower, is equipped with air pump and third ooff valve on the blast pipe, the recovery tower in be equipped with spiral heat dissipation pipeline, and spiral heat dissipation pipeline links to each other with gas vent N1 of recovery tower.
2. A twin spray tower as defined in claim 1 in which: the access hole N2 and the circulating liquid inlet N10 are on the same horizontal line.
3. A twin spray tower as defined in claim 1 in which: the bottom of the main tower is provided with a base, and the bottom of the recovery tower is provided with a recovery base.
4. A twin spray tower as defined in claim 1 in which: the outer walls of the main tower and the recovery tower are both provided with heat insulation cotton.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122452895.0U CN218421927U (en) | 2021-10-12 | 2021-10-12 | Gemini spraying tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122452895.0U CN218421927U (en) | 2021-10-12 | 2021-10-12 | Gemini spraying tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218421927U true CN218421927U (en) | 2023-02-03 |
Family
ID=85079642
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122452895.0U Active CN218421927U (en) | 2021-10-12 | 2021-10-12 | Gemini spraying tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218421927U (en) |
-
2021
- 2021-10-12 CN CN202122452895.0U patent/CN218421927U/en active Active
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