CN212818219U - Cyclone separator for organic gas recovery - Google Patents
Cyclone separator for organic gas recovery Download PDFInfo
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- CN212818219U CN212818219U CN202020844424.7U CN202020844424U CN212818219U CN 212818219 U CN212818219 U CN 212818219U CN 202020844424 U CN202020844424 U CN 202020844424U CN 212818219 U CN212818219 U CN 212818219U
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- cyclone
- organic gas
- whirlwind
- barrel
- gas recovery
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Abstract
The utility model relates to an organic gas retrieves and uses cyclone, the novel nipple rectifier comprises a cylindrical shel, barrel upper portion is equipped with the air inlet, and the lower part is equipped with the gas outlet, the middle part inboard of barrel is equipped with interior barrel holder, fixedly connected with inner tube on the interior barrel holder, the upper portion of inner tube is equipped with the baffle, the baffle periphery is equipped with and is annular whirlwind piece seat, evenly be provided with a plurality of air intakes on the whirlwind piece seat, the lower part correspondence of air intake is provided with and is used for the whirlwind piece that leads organic gas and form whirlwind air current. The utility model discloses a suspension among the whirlwind piece separation organic gas, trace suspension pass through the filtration material secondary filter in the whirlwind piece inner tube again, the utility model discloses simple structure, it is with low costs, utilize the whirlwind piece to produce whirlwind and compare the tradition and utilize the shell shape to produce whirlwind during the use, available space is bigger in the barrel, and separation efficiency is higher, and the effect is better, adapts to the automatic continuous operation's the condition.
Description
The technical field is as follows:
the utility model relates to a waste gas recovery technical field especially relates to a cyclone is used in machine gas recovery.
Background art:
in the low-temperature condensation stage of the organic gas recovery device, if a separator is not arranged at the rear end or the structure of the arranged separator is not reasonable, liquid can be brought into the subsequent process along with the airflow, so that the service life of subsequent equipment is reduced, and even the subsequent equipment is damaged. The general casing of traditional separator is the toper, utilizes the separator casing appearance to make the gaseous whirlwind form motion of getting into be gyration in the casing, but in the time of the actual use, this kind of separator structure is complicated, and the cost is higher, and the during operation is because resistance is too big under the carrier effect, generally can only be used for the separation of large granule, and separation efficiency is low, can not reach the anticipated effect of separation.
The utility model has the following contents:
the utility model aims at the defect of prior art, provide a simple structure, it is with low costs, cyclone is used in organic gas recovery that separation efficiency is high.
The utility model discloses a realize through following technical scheme: the cyclone separator for recycling the organic gas comprises a barrel body, wherein an air inlet is formed in the upper portion of the barrel body, an air outlet is formed in the lower portion of the barrel body, an inner barrel frame is arranged on the inner side of the middle of the barrel body, an inner barrel is fixedly connected to the inner barrel frame, a baffle is arranged on the upper portion of the inner barrel, an annular cyclone sheet seat is arranged on the periphery of the baffle, a plurality of air inlets are uniformly formed in the cyclone sheet seat, and cyclone sheets used for guiding the organic gas and forming cyclone airflow are correspondingly arranged on the lower portions of the air inlets.
In the technical scheme, the cyclone sheet is formed by cutting and forming the surface of the cyclone sheet seat and turning the cyclone sheet seat downwards.
In the technical scheme, the cyclone pieces are detachably arranged on the cyclone piece seat.
In the technical scheme, an angle formed by the cyclone pieces and the horizontal plane is 8-15 degrees.
In the technical scheme, the circumferential direction of the lower part of the inner cylinder is provided with the water baffle.
In the technical scheme, the middle part of the cylinder body is provided with a drain valve at the position corresponding to the position of the inner cylinder frame and at the bottom.
In the technical scheme, pressure gauges are arranged at the middle part and the lower part of the cylinder body.
In the above technical scheme, a plurality of guide grooves are arranged on the inner wall surface of the cylinder body.
In the technical scheme, the wall surface of the inner cylinder is provided with a plurality of filtering holes, glass fiber filter paper is placed in the filtering holes, and the outer side of the lower part of the inner cylinder is sealed with the inner wall of the cylinder body through the inner cylinder frame.
The utility model has the advantages that: the utility model discloses a suspension among the whirlwind piece separation organic gas, trace suspension pass through the filtration material secondary filter in the whirlwind piece inner tube again, the utility model discloses simple structure, it is with low costs, utilize the whirlwind piece to produce whirlwind and compare the tradition and utilize the shell shape to produce whirlwind during the use, available space is bigger in the barrel, and separation efficiency is higher, and the effect is better, adapts to the automatic continuous operation's the condition.
Description of the drawings:
fig. 1 is a schematic front sectional view of the present invention;
fig. 2 is a schematic top view of a cyclone sheet according to the present invention;
the reference numbers are as follows: a cylinder 100; an inner barrel frame 110; an air inlet 120; an air outlet 130; a blowoff valve 140; a pressure gauge 150; an inner barrel 200; a baffle 210; a cyclone sheet holder 220; a water guard plate 230; the cyclone sheet 300.
The specific implementation mode is as follows:
the following detailed description of the preferred embodiments of the present invention will be provided in conjunction with the accompanying drawings, so that the advantages and features of the present invention can be more easily understood by those skilled in the art, and the protection scope of the present invention can be clearly and clearly defined.
As shown in fig. 1 and 2, a cyclone separator for recycling organic gas includes a cylinder 100, an air inlet 120 is disposed at an upper portion of the cylinder 100, an air outlet 130 is disposed at a lower portion of the cylinder 100, an inner cylinder frame 110 is disposed at an inner side of a middle portion of the cylinder 100, an inner cylinder 200 is fixedly connected to the inner cylinder frame 110, a baffle 210 is disposed at an upper portion of the inner cylinder 200, an annular cyclone sheet seat 220 is disposed at an outer periphery of the baffle 210, a plurality of air inlets 221 are uniformly disposed on the cyclone sheet seat 220, and cyclone sheets 300 for guiding the organic gas and forming cyclone airflow are correspondingly disposed at lower portions of the air inlets 221.
The cyclone sheet 300 is formed by cutting and folding down the surface of the cyclone sheet holder 220.
The cyclone pieces 300 are detachably mounted on the cyclone piece holder 220.
The angle between the cyclone 300 and the horizontal plane is 8-15 degrees, so that the organic gas can flow between the cylinder 100 and the inner cylinder 200 in a cyclone manner.
The circumference of the lower part of the inner cylinder 200 is provided with the water baffle 230, liquid in the middle of practical use can be condensed on the outer wall of the inner cylinder 200, and the water baffle 230 can effectively avoid splashing when the liquid falls down, so that secondary pollution is caused.
As shown in fig. 1, a drain valve 140 is provided at the middle and bottom of the drum 100 at a position corresponding to the inner frame 110.
The inner wall surface of the cylinder 100 is provided with a plurality of flow guide grooves, so that the flow direction of the internal gas can be better guided.
The wall surface of the inner cylinder 200 is provided with a plurality of filtering holes, glass fiber filter paper is placed in the filtering holes, the organic gas reaches the inner side of the inner cylinder 200 after passing through the filtering holes, the organic gas is secondarily filtered by the filter paper in the passing process, and the dried gas is discharged from the exhaust port 130 at the lower part.
In actual operation, the ratio of the gas flow to the area of the cyclone 300 is 20-30.
The utility model discloses when using: organic gas enters the cylinder 100 from the gas inlet 120, firstly passes through the cyclone pieces 300, the cyclone pieces 300 are cut and bent at regular intervals, gaps are formed after bending, the organic gas starts to rotate after passing through the gaps and collides with the inner cylinder 200 and the cylinder wall, and separated liquid flows into the bottom of the cylinder 100 and is discharged by the drain valve 140 after being stored to a certain amount.
Through the process, qualified dry gas flows out of the high-efficiency cyclone separator and enters the next treatment process.
In addition, in the description of the embodiments of the present invention, unless otherwise explicitly specified or limited, the terms "mounted," "connected," "disposed," "provided," and the like are to be construed broadly and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", "side", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed in a specific orientation, and be operated, and thus, should not be construed as limiting the present invention.
Finally, it should be noted that: the above embodiments are only specific embodiments of the present invention, and are not intended to limit the technical solution of the present invention, and the protection scope of the present invention is not limited thereto, although the present invention is described in detail with reference to the foregoing embodiments, those skilled in the art should understand that: those skilled in the art can still modify or easily conceive of changes in the technical solutions described in the foregoing embodiments or make equivalent substitutions for some technical features within the technical scope of the present disclosure; such modifications, changes or substitutions do not substantially depart from the spirit and scope of the embodiments of the present invention, and are intended to be included within the scope of the present invention. Therefore, the protection scope of the present invention shall be subject to the protection scope of the claims.
Claims (9)
1. A cyclone separator for organic gas recovery is characterized in that: the cyclone gas collector comprises a barrel body (100), wherein an air inlet (120) is formed in the upper portion of the barrel body (100), an air outlet (130) is formed in the lower portion of the barrel body (100), an inner barrel frame (110) is arranged on the inner side of the middle of the barrel body (100), an inner barrel (200) is fixedly connected to the inner barrel frame (110), a baffle (210) is arranged on the upper portion of the inner barrel (200), an annular cyclone sheet seat (220) is arranged on the periphery of the baffle (210), a plurality of air inlets (221) are uniformly formed in the cyclone sheet seat (220), and cyclone sheets (300) used for guiding organic gas and forming cyclone gas flow are correspondingly arranged on the lower portions.
2. The cyclone separator for organic gas recovery according to claim 1, wherein: the cyclone sheet (300) is formed by cutting and forming the surface of the cyclone sheet seat (220) and turning downwards.
3. The cyclone separator for organic gas recovery according to claim 1, wherein: the cyclone piece (300) is detachably arranged on the cyclone piece seat (220).
4. The cyclone separator for organic gas recovery according to claim 1, wherein: the angle between the cyclone piece (300) and the horizontal plane is 8-15 degrees.
5. The cyclone separator for organic gas recovery according to claim 1, wherein: and a water baffle (230) is arranged on the lower part of the inner cylinder (200) in the circumferential direction.
6. The cyclone separator for organic gas recovery according to claim 1, wherein: and a drainage valve (140) is arranged at the position of the middle part of the barrel body (100), which corresponds to the position of the inner barrel frame (110), and the bottom of the barrel body.
7. The cyclone separator for organic gas recovery according to claim 1, wherein: pressure gauges (150) are arranged at the middle part and the lower part of the cylinder body (100).
8. The cyclone separator for organic gas recovery according to claim 1, wherein: the inner wall surface of the cylinder body (100) is provided with a plurality of diversion trenches.
9. The cyclone separator for organic gas recovery according to claim 1, wherein: the wall surface of the inner cylinder (200) is provided with a plurality of filtering holes, glass fiber filter paper is placed in the filtering holes, and the outer side of the lower part of the inner cylinder (200) is sealed with the inner wall of the cylinder body (100) through an inner cylinder frame (110).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020844424.7U CN212818219U (en) | 2020-05-20 | 2020-05-20 | Cyclone separator for organic gas recovery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020844424.7U CN212818219U (en) | 2020-05-20 | 2020-05-20 | Cyclone separator for organic gas recovery |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212818219U true CN212818219U (en) | 2021-03-30 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020844424.7U Active CN212818219U (en) | 2020-05-20 | 2020-05-20 | Cyclone separator for organic gas recovery |
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| Country | Link |
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| CN (1) | CN212818219U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114028876A (en) * | 2021-12-18 | 2022-02-11 | 平湖弘欣热电有限公司 | Low-pressure pulse rotary-spraying bag-type dust collector of circulating fluidized bed boiler |
-
2020
- 2020-05-20 CN CN202020844424.7U patent/CN212818219U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114028876A (en) * | 2021-12-18 | 2022-02-11 | 平湖弘欣热电有限公司 | Low-pressure pulse rotary-spraying bag-type dust collector of circulating fluidized bed boiler |
| CN114028876B (en) * | 2021-12-18 | 2022-07-05 | 平湖弘欣热电有限公司 | Low-pressure pulse rotary spraying cloth bag dust remover for circulating fluidized bed boiler |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder |
Address after: 210000 no.2-1, Yueyuan Road, Hengxi street, Jiangning District, Nanjing City, Jiangsu Province (Jiangning Development Zone) Patentee after: Nanjing Weidun energy environmental protection Co.,Ltd. Address before: 211151 Wangshan Road, Taowu Community, Hengxi Street, Jiangning District, Nanjing City, Jiangsu Province, 2-2 Patentee before: Nanjing Weidun energy environmental protection Co.,Ltd. |
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| CP02 | Change in the address of a patent holder |