CN212327851U - Cylinder runner zeolite air-cooled heat sink - Google Patents
Cylinder runner zeolite air-cooled heat sink Download PDFInfo
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- CN212327851U CN212327851U CN202020278018.9U CN202020278018U CN212327851U CN 212327851 U CN212327851 U CN 212327851U CN 202020278018 U CN202020278018 U CN 202020278018U CN 212327851 U CN212327851 U CN 212327851U
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Abstract
A cylinder type rotary wheel zeolite air cooling device relates to the technical field of waste gas treatment, wherein a speed reducing mechanism and rotary wheel zeolite are arranged inside a rotary wheel shell, the speed reducing mechanism is in driving connection with the rotary wheel zeolite, a VOCs waste gas inlet is formed in one side wall of the rotary wheel shell, an adsorption air outlet is connected on one side wall of the rotary wheel shell adjacent to the VOCs waste gas inlet in a through mode, a desorption air inlet is connected on the side wall of the adsorption air outlet in a through mode, the inner end of the desorption air inlet is connected with a desorption air outlet in a through mode through a pipeline, the desorption air outlet is inserted in the rotary wheel shell on the side wall opposite to the VOCs, and a cooling air outlet is inserted in the; the cooling air outlet is connected with the desorption air inlet through a pipeline. Can overcome the defects of low zeolite adsorption rate and high energy consumption in the prior art.
Description
Technical Field
The utility model relates to a waste gas treatment technical field, concretely relates to cylinder runner zeolite forced air cooling heat sink.
Background
In the treatment process of the industrial waste gas VOCs, in the desorption process of the rotating wheel zeolite, the temperature of the zeolite is higher in the process of conversion from high-temperature desorption to adsorption, and the adsorption efficiency of the VOCs waste gas is influenced; the temperature of fresh air for desorption is low, which causes the heating energy consumption to rise.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to prior art's defect and not enough, provide a reasonable in design's cylinder runner zeolite forced air cooling heat sink, can overcome the defect that zeolite adsorption rate is on the low side, the energy consumption is on the high side among the prior art.
In order to achieve the above purpose, the utility model adopts the following technical proposal: the device comprises a VOCs waste gas inlet, an adsorption air outlet, a desorption air inlet, a desorption air outlet, a speed reducing mechanism, runner zeolite, a runner shell and a cooling air outlet; the interior of the rotating wheel shell is provided with a speed reducing mechanism and rotating wheel zeolite, the speed reducing mechanism is in driving connection with the rotating wheel zeolite, one side wall of the rotating wheel shell is provided with a VOCs waste gas inlet, one side wall of the rotating wheel shell, which is adjacent to the VOCs waste gas inlet, is in through connection with an adsorption air outlet, the side wall of the adsorption air outlet is in through connection with a desorption air inlet, the inner end of the desorption air inlet is in through connection with a desorption air outlet through a pipeline, the desorption air outlet is inserted in the rotating wheel shell on one side wall opposite to the VOCs, and a cooling air outlet is inserted in the side; the cooling air outlet is connected with the desorption air inlet through a pipeline.
Furthermore, the cooling air outlet is connected with the electric auxiliary heater through a pipeline, and the electric auxiliary heater is connected with the desorption air inlet through a pipeline.
Furthermore, the connection position of the inner end of the cooling air outlet and the runner zeolite is arranged in a sealing mode.
After the structure is adopted, the beneficial effects of the utility model are that: this embodiment provides a cylinder runner zeolite air-cooled heat sink, can overcome the defect that zeolite adsorption efficiency is on the low side, the energy consumption is on the high side among the prior art.
Description of the drawings:
fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic block diagram of the present invention.
Description of reference numerals:
VOCs waste gas import 1, adsorb air exit 2, desorption income wind gap 3, desorption air outlet 4, reduction gears 5, runner zeolite 6, runner shell 7, cooling air export 8, electricity heat 9 of assisting.
The specific implementation mode is as follows:
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 work belong to the protection scope of the present invention.
As shown in fig. 1 and fig. 2, the following technical solutions are adopted in the present embodiment: the device comprises a VOCs waste gas inlet 1, an adsorption air outlet 2, a desorption air inlet 3, a desorption air outlet 4, a speed reducing mechanism 5, runner zeolite 6, a runner shell 7 and a cooling air outlet 8; a speed reducing mechanism 5 and runner zeolite 6 are arranged in the runner shell 7, the speed reducing mechanism 5 is in drive connection with the runner zeolite 6 (the speed reducing drive connection of the speed reducing mechanism 5 and the runner zeolite 6 is the same as the speed reducing drive principle of the existing runner zeolite), a VOCs waste gas inlet 1 is arranged on one side wall of the runner shell 7, an adsorption air outlet 2 is connected on one side wall of the runner shell 7 adjacent to the VOCs waste gas inlet 1 in a through way, a desorption air inlet 3 is connected on the side wall of the adsorption air outlet 2 in a through way, the inner end of the desorption air inlet 3 is connected with a desorption air outlet 4 in a through way through a pipeline (the pipeline is arranged in the runner zeolite 6), the desorption air outlet 4 is inserted on one side wall of the runner shell 7 opposite, a cooling air outlet 8 is inserted in the side wall, and the connection part of the inner end of the cooling air outlet 8 and the runner zeolite 6 is sealed (the sealing arrangement between the pipeline connection parts is the same as that of a pipeline sealing mechanism in the existing runner zeolite treatment mechanism); the cooling air outlet 8 is connected with the electric auxiliary heater 9 through a pipeline, and the electric auxiliary heater 9 is connected with the desorption air inlet 3 through a pipeline.
The working principle of the specific embodiment is as follows: air-cooled cooling section: extracting gas to be treated by a main process fan connected to a VOCs waste gas inlet 1 to enter a runner shell 7, discharging the adsorbed waste gas through an adsorption air outlet 2, extracting cooling air by using the main process fan after adsorption, sending the cooling air into the runner shell 7 through the VOCs waste gas inlet 1, carrying out air cooling on the desorbed runner zeolite 6, discharging the cooling air from a cooling air outlet 8 after absorbing the runner zeolite 6, and then transferring the cooled runner zeolite 6 to an adsorption process; cooling air for cooling is preheated by the runner zeolite 6, then is pumped by a desorption fan connected at a cooling air outlet 8 and is heated to a required desorption temperature by electric auxiliary heat 9, and is sent into a desorption air inlet 3 for desorption and desorption air.
After adopting above-mentioned structure, this embodiment's beneficial effect is: this embodiment provides a cylinder runner zeolite air-cooled heat sink, can overcome the defect that zeolite adsorption efficiency is on the low side, the energy consumption is on the high side among the prior art.
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. The utility model provides a cylinder runner zeolite air-cooled heat sink which characterized in that: the device comprises a VOCs waste gas inlet (1), an adsorption air outlet (2), a desorption air inlet (3), a desorption air outlet (4), a speed reducing mechanism (5), rotary wheel zeolite (6), a rotary wheel shell (7) and a cooling air outlet (8); a speed reducing mechanism (5) and runner zeolite (6) are arranged inside a runner shell (7), the speed reducing mechanism (5) is in drive connection with the runner zeolite (6), a VOCs waste gas inlet (1) is formed in one side wall of the runner shell (7), an adsorption air outlet (2) is connected to one side wall, adjacent to the VOCs waste gas inlet (1), of the runner shell (7) in a through mode, a desorption air inlet (3) is connected to the side wall of the adsorption air outlet (2) in a through mode, the inner end of the desorption air inlet (3) is connected with a desorption air outlet (4) in a through mode through a pipeline, the desorption air outlet (4) penetrates through one side wall, opposite to the set VOCs, of the runner shell (7), and a cooling air outlet (8) penetrates through the side wall; the cooling air outlet (8) is connected with the desorption air inlet (3) through a pipeline.
2. The air-cooled temperature reduction device with cylindrical rotating wheel zeolite as claimed in claim 1, wherein: the cooling air outlet (8) is connected with the electric auxiliary heater (9) through a pipeline, and the electric auxiliary heater (9) is connected with the desorption air inlet (3) through a pipeline.
3. The air-cooled temperature reduction device with cylindrical rotating wheel zeolite as claimed in claim 1, wherein: the joint of the inner end of the cooling air outlet (8) and the runner zeolite (6) is arranged in a sealing way.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020278018.9U CN212327851U (en) | 2020-03-09 | 2020-03-09 | Cylinder runner zeolite air-cooled heat sink |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020278018.9U CN212327851U (en) | 2020-03-09 | 2020-03-09 | Cylinder runner zeolite air-cooled heat sink |
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| Publication Number | Publication Date |
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| CN212327851U true CN212327851U (en) | 2021-01-12 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202020278018.9U Active CN212327851U (en) | 2020-03-09 | 2020-03-09 | Cylinder runner zeolite air-cooled heat sink |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113842747A (en) * | 2021-10-15 | 2021-12-28 | 扬州绿泉环保工程技术有限公司 | Variable-frequency VOCs zeolite rotary drum adsorption equipment |
| CN117085462A (en) * | 2023-09-04 | 2023-11-21 | 青岛德尔通用环保科技有限公司 | Zeolite roller desorption mechanism and waste gas purifying integrated machine |
-
2020
- 2020-03-09 CN CN202020278018.9U patent/CN212327851U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113842747A (en) * | 2021-10-15 | 2021-12-28 | 扬州绿泉环保工程技术有限公司 | Variable-frequency VOCs zeolite rotary drum adsorption equipment |
| CN117085462A (en) * | 2023-09-04 | 2023-11-21 | 青岛德尔通用环保科技有限公司 | Zeolite roller desorption mechanism and waste gas purifying integrated machine |
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