CN204429063U - The large working area compact gas-liquid separation device of freezing type drier - Google Patents
The large working area compact gas-liquid separation device of freezing type drier Download PDFInfo
- Publication number
- CN204429063U CN204429063U CN201520037137.4U CN201520037137U CN204429063U CN 204429063 U CN204429063 U CN 204429063U CN 201520037137 U CN201520037137 U CN 201520037137U CN 204429063 U CN204429063 U CN 204429063U
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- Prior art keywords
- flange
- nozzle
- filter screen
- liquid separation
- separation device
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Abstract
The utility model discloses a kind of large working area compact gas-liquid separation device of freezing type drier, comprise nozzle, the front end of described nozzle is provided with Conic nozzle, Conic nozzle is evenly distributed with bullport, the edge of described Conic nozzle is provided with the first flange, and the front end of described Conic nozzle is also provided with the first flange; One end of spray tail is provided with outwardly taper sheath, and the edge of described taper sheath is provided with flange, and flange outer rim is connected with the second flange; One end of described spray tail is also provided with the second flange, is provided with pod apertures between the sidewall of the second flange and described spray tail; Described nozzle and described spray tail, by the first flange and the second Flange joint, accompany the first filter screen between described first flange and the second flange.The utility model compact conformation, can be installed on the admission line of air compressor machine with the form of flange; Its filter screen is in tilted layout, and working face is larger; Uniform stream can also be guided to be distributed in whole screen surface, guarantee disintegrate-quality, raising air-flow pass through efficiency simultaneously.
Description
Technical field
The utility model relates to freezing type drier technical field, particularly relates to the gas-liquid separation device of freezing type drier.
Background technology
Freezing type drier is primarily of refrigeration system, heat-exchange system, carbonated drink piece-rate system and corresponding electric control system four part composition.Saturated compressed air is in cooling procedure, a large amount of condensation water can be gathered in heat exchanger, also there is a large amount of more tiny water droplet water smoke to be suspended in compressed air and enter precool heat exchanger device, after these water droplet water smokes enter precooling regenerator, along with a part " double evaporation-cooling " of carrying out for heat exchange returns gas phase, moisture increase in finished product gas is made to cause dew point to rise, the aqueous water that another part has little time to evaporate then enters user pipe with air-flow, make to occur aqueous water in the gas equipment of downstream, the quality of product certainly will be affected like this.In order to make the aqueous water condensed in heat transfer process well separate from finished product gas, thus ensure the quality of finished product gas, it is required for arranging water separator, is an obligato vitals in freezing type drier.
Existing gas-liquid separation device mainly relies on filter screen to be separated, and the working face of filter screen is larger, and in the unit interval, the air of process is more, and thus efficiency is higher; But working face is larger, volume is larger, gas-liquid separation device is caused to install and inconvenient maintenance.
Utility model content
The applicant restricts by working face for the gas-liquid separation device in existing freezing type drier, the problem that volume is large, installation and maintenance are inconvenient, carry out linguistic term, a kind of large working area compact gas-liquid separation device of freezing type drier is provided, its compact conformation, can be installed on the admission line of air compressor machine with the form of flange; Its filter screen is in tilted layout, and working face is larger; Uniform stream can also be guided to be distributed in whole screen surface, guarantee disintegrate-quality, raising air-flow pass through efficiency simultaneously.
The technical solution of the utility model is as follows:
A large working area compact gas-liquid separation device for freezing type drier, the front end of nozzle is provided with Conic nozzle, and Conic nozzle is evenly distributed with bullport, and the edge of Conic nozzle is provided with the first flange, and the front end of Conic nozzle is also provided with the first flange; One end of spray tail is provided with outwardly taper sheath, and the edge of taper sheath is provided with flange, and flange outer rim is connected with the second flange; One end of spray tail is also provided with the second flange, is provided with pod apertures between the sidewall of the second flange and spray tail; Nozzle and spray tail, by the first flange and the second Flange joint, accompany the first filter screen between the first flange and the second flange.
Further improvement as technique scheme:
The tail end of described nozzle is provided with the first adpting flange, the air inlet Flange joint on the first adpting flange and air inlet; The other end of spray tail is provided with the second adpting flange, the gas outlet Flange joint on the second adpting flange and gas outlet.
The front end of described Conic nozzle is provided with flaring turbulent hole, and the first flange is located at the periphery in turbulent hole; Described second flange is provided with the through hole corresponding with turbulent hole; The second filter screen is connected with between described second adpting flange and gas outlet flange.
Annular gasket is provided with between described first filter screen and the first flange.
The beneficial effects of the utility model are:
1, the utility model compact conformation, filter screen working face are larger: compared to existing technology, filter screen is directly arranged in the technical scheme in pipeline, although external diameter of the present utility model is larger than the diameter of common admission line 1 to 2 times, the work area of filter screen is large 8 to 13 times.
The uniform stream of air inlet can be delivered to the surface of the first filter screen everywhere by the bullport 2, described Conic nozzle arranged, and avoids certain part by filter screen in air flow collection, causes filter screen unbalance stress, disintegrate-quality not high.
3, air-flow enters from the small bore end in turbulent hole, due to turbulent hole flue, thus forms negative pressure at the large nose end in turbulent hole; The air entering spray tail inner chamber from described pod apertures affects formation turbulent flow in described inner chamber by this; Being formed of turbulent flow is beneficial to and is separated moisture in air and oil droplet, thus the other end of spray tail is provided with the second filter screen, can be separated moisture remaining in air and oil droplet further, improve separating effect.
4, the utility model is connected with existing admission line by the flange at two ends, and upgrade cost is little; Simultaneously due to compact conformation, radial distance is shorter, less on the impact of other devices, thus can directly upgrade in existing equipment.
Accompanying drawing explanation
Fig. 1 is front sectional view of the present utility model.
Fig. 2 is the revolved sectional view in A-A cross section in Fig. 1.
In figure: 1, air inlet; 11, air inlet flange; 2, nozzle; 21, the first adpting flange; 22, Conic nozzle; 23, bullport; 24, turbulent hole; 25, the first flange; 26, the first flange; 3, annular gasket; 4, the first filter screen; 5, tail is sprayed; 51, the second flange; 52, taper sheath; 53, inner chamber; 54, the second adpting flange; 55, pod apertures; 56, through hole; 57, the second flange; 58, flange; 6, the second filter screen; 7, gas outlet; 71, gas outlet flange.
Detailed description of the invention
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described.
As shown in Figure 1 and Figure 2, the utility model comprises nozzle 2, and the front end of nozzle 2 is provided with Conic nozzle 22, Conic nozzle 22 is evenly distributed with bullport 23, and bullport 23 is vertical with the outer surface of Conic nozzle 22; The edge of Conic nozzle 22 is provided with the first flange 25, and the front end of Conic nozzle 22 is also provided with the first flange 26; One end of spray tail 5 is provided with outwardly taper sheath 52, and the edge of taper sheath 52 is provided with flange 58, and flange 58 outer rim is connected with the second flange 51; One end of spray tail 5 is also provided with between the second flange 57, second flange 57 and the sidewall spraying tail 5 and is provided with pod apertures 55; Nozzle 2 is connected with the second flange 51 by the first flange 25 with spray tail 5; The first filter screen 4 is accompanied between first flange 25 and the second flange 51, annular gasket 3 is provided with between first filter screen 4 and the first flange 25, first filter screen 4 is by annular gasket 3, first flange 26, thus and form certain gap between the outer surface of Conic nozzle 22, make the air-flow of injection in bootstrap hole 23 more uniformly can be distributed to the surface of the first filter screen 4.
As preferred embodiment, the front end of Conic nozzle 22 is provided with the periphery that flaring turbulent hole 24, first flange 26 is located at turbulent hole 24; Second flange 57 is provided with the through hole 56 corresponding with turbulent hole 24; Air-flow enters from the small bore end in turbulent hole 24, due to turbulent hole 24 flue, thus forms negative pressure at the large nose end in turbulent hole 24; The air entering spray tail 5 inner chamber 53 from pod apertures 55 affects formation turbulent flow in inner chamber 53 by this; Being formed of turbulent flow is beneficial to and is separated moisture in air and oil droplet, thus between the second adpting flange 54 and gas outlet flange 71, is connected with the second filter screen 6, to be separated moisture remaining in air and oil droplet further, promotes separating effect.
As preferred embodiment, the maximum outside diameter of the utility model (not comprising the first flange 25 and the second flange 51) controls 2 times to 3 times of the diameter in air inlet pipe 1, so that installation of the present utility model; With this understanding, the work area of the first filter screen 4 is about 10 times of the second filter screen 6 work area.
Mounting means of the present utility model is as follows: the tail end of nozzle 2 is provided with the first adpting flange 21, first adpting flange 21 and is connected with the air inlet flange 11 on air inlet 1; The other end of spray tail 5 is provided with the second adpting flange 54, second adpting flange 54 and is connected with the gas outlet flange 71 on gas outlet 7.
Above illustrated embodiment is better embodiment of the present utility model, only be used for conveniently the utility model being described, not any pro forma restriction is done to the utility model, have in any art and usually know the knowledgeable, if do not depart from the utility model carry in the scope of technical characteristic, utilize the utility model disclose the Equivalent embodiments changed or modify in the done local of technology contents, and do not depart from technical characteristic content of the present utility model, all still belong in the scope of the utility model technical characteristic.
Claims (4)
1. the large working area compact gas-liquid separation device of a freezing type drier, it is characterized in that: the front end of nozzle (2) is provided with Conic nozzle (22), Conic nozzle (22) is evenly distributed with bullport (23), the edge of Conic nozzle (22) is provided with the first flange (25), and the front end of Conic nozzle (22) is also provided with the first flange (26); One end of spray tail (5) is provided with outwardly taper sheath (52), and the edge of taper sheath (52) is provided with flange (58), and flange (58) outer rim is connected with the second flange (51); One end of spray tail (5) is also provided with the second flange (57), is provided with pod apertures (55) between the sidewall of the second flange (57) and spray tail (5); Nozzle (2) is connected with the second flange (51) by the first flange (25) with spray tail (5), accompanies the first filter screen (4) between the first flange (25) and the second flange (51).
2. the large working area compact gas-liquid separation device of freezing type drier as claimed in claim 1, it is characterized in that: the tail end of described nozzle (2) is provided with the first adpting flange (21), the first adpting flange (21) is connected with the air inlet flange (11) on air inlet (1); The other end of spray tail (5) is provided with the second adpting flange (54), and the second adpting flange (54) is connected with the gas outlet flange (71) on gas outlet (7).
3. the large working area compact gas-liquid separation device of freezing type drier as claimed in claim 2, it is characterized in that: the front end of described Conic nozzle (22) is provided with flaring turbulent hole (24), and the first flange (26) is located at the periphery of turbulent hole (24); Described second flange (57) is provided with the through hole (56) corresponding with turbulent hole (24); The second filter screen (6) is connected with between described second adpting flange (54) and gas outlet flange (71).
4. the large working area compact gas-liquid separation device of freezing type drier as claimed in claim 1, is characterized in that: be provided with annular gasket (3) between described first filter screen (4) and the first flange (25).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520037137.4U CN204429063U (en) | 2015-01-19 | 2015-01-19 | The large working area compact gas-liquid separation device of freezing type drier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520037137.4U CN204429063U (en) | 2015-01-19 | 2015-01-19 | The large working area compact gas-liquid separation device of freezing type drier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204429063U true CN204429063U (en) | 2015-07-01 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520037137.4U Expired - Fee Related CN204429063U (en) | 2015-01-19 | 2015-01-19 | The large working area compact gas-liquid separation device of freezing type drier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204429063U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107504362A (en) * | 2017-07-19 | 2017-12-22 | 东方电气(广州)重型机器有限公司 | A kind of steam-water separation equipment |
| CN109453640A (en) * | 2018-12-27 | 2019-03-12 | 河南海力特机电制造有限公司 | Heavy pressure fine spray desulfurization cooling spray head |
-
2015
- 2015-01-19 CN CN201520037137.4U patent/CN204429063U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107504362A (en) * | 2017-07-19 | 2017-12-22 | 东方电气(广州)重型机器有限公司 | A kind of steam-water separation equipment |
| CN107504362B (en) * | 2017-07-19 | 2019-10-11 | 东方电气(广州)重型机器有限公司 | A kind of steam-water separation equipment |
| CN109453640A (en) * | 2018-12-27 | 2019-03-12 | 河南海力特机电制造有限公司 | Heavy pressure fine spray desulfurization cooling spray head |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150701 Termination date: 20170119 |