CN207203662U - A kind of freezing type drier spiral type gas-water separator - Google Patents
A kind of freezing type drier spiral type gas-water separator Download PDFInfo
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- CN207203662U CN207203662U CN201721198089.2U CN201721198089U CN207203662U CN 207203662 U CN207203662 U CN 207203662U CN 201721198089 U CN201721198089 U CN 201721198089U CN 207203662 U CN207203662 U CN 207203662U
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- housing
- type drier
- freezing type
- separation
- inner barrel
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Abstract
The utility model discloses a kind of freezing type drier spiral type gas-water separator, it is related to freezing type drier technical field, the utility model includes housing, housing sidewall upper end is connected with air inlet pipe, housing sidewall lower end is provided with separation and covered, separation, which covers, offers some osculums, housing bottom offers discharge outlet, discharge outlet is connected with drainpipe, enclosure interior is provided with inner barrel, and inner cylinder external surface is fixed with helical baffle, and inner cylinder intracoelomic cavity submits mistake and is fixed with some baffle plates, baffle plate lower surface is provided with some burrs, and inner barrel upper end is connected with escape pipe；The utility model carries out first time separation using centrifugal force and gravity, strengthen separating effect by the guide functions of helical baffle, the most of drop separation carried secretly in compressed gas is gone out, it is folded to again by separating lid into inner barrel, by the baffle plate with burr, passes through continuous collision process, continue the drop in compressed air and the separation of liquid foam, it is compact-sized, good separating effect, separative efficiency height.
Description
Technical field
Freezing type drier technical field is the utility model is related to, more particularly to a kind of freezing type drier spiral shell
Rotating moisture trap.
Background technology
Freezing type drier has used physical principle, and the moisture in compressed air is refrigerated to below dew point, is allowed to from sky
The dried-air drier separated out in gas, the source of the gas treatment element belonged in pneumatic system.Freezing type drier generally include compressor,
Condenser, choke valve, evaporator and moisture trap.At present, common moisture trap include baffle-type moisture trap and
Cyclone type gas-water separator, baffle-type moisture trap is simple in construction, and manufacture is simple, and still, its gas-water separation effect is not as rotation
The separating effect of wind formula moisture trap.
Existing baffle-type moisture trap and cyclone type gas-water separator can meet that the gas-water separation under general operating mode will
Ask, still, the operating mode higher to gas-water separation effect requirements, especially there is the work that higher position reason requires to the less drop of diameter
Condition, its separating effect is not satisfactory, can not remove the liquid foam being mingled with gas.If also continue to use existing baffle-type gas
Separator or cyclone type gas-water separator, excessive moisture will be brought to downstream process link by air-flow, cause in downstream links
Require that degree of drying high humidity of media is excessive and even produce failure, it is necessary to frequently change the medium, larger safety be present
Hidden danger.
Utility model content
The purpose of this utility model is：In order to solve existing baffle-type moisture trap or cyclone type gas-water separator
Separating effect is undesirable, it is impossible to removes liquid foam, the problem of larger potential safety hazard to downstream links be present, the utility model provides
A kind of freezing type drier spiral type gas-water separator.
The utility model specifically uses following technical scheme to achieve these goals：
A kind of freezing type drier spiral type gas-water separator, including housing, the housing sidewall upper end are connected with air inlet
Pipe, the air inlet tube axis direction and housing sidewall face are tangent, and the housing sidewall lower end is provided with separation and covered, and the separation lid will
Housing cavity is divided into two parts up and down, and separation, which covers, offers some osculums, and the housing bottom offers discharge outlet, described
Discharge outlet is connected with drainpipe, and enclosure interior is provided with inner barrel, and the inner cylinder external surface is fixed with helical baffle, under inner barrel
End opens, and inner cylinder intracoelomic cavity submits mistake and is fixed with some baffle plates, and the baffle plate lower surface is provided with some burrs, on the inner barrel
End is connected with escape pipe, and the escape pipe is extended to outside housing；Compressed gas carries out spiral shell after entering housing along housing tangential direction
Rotation motion, first time separation is carried out using centrifugal force and gravity, strengthens separating effect by the guide functions of helical baffle, will
The most of drop separation carried secretly in compressed gas is gone out, then is folded to by separating lid into inner barrel, by the gear with burr
Plate, by continuous collision process, continue the drop in compressed air and the separation of liquid foam, compact-sized, good separating effect, point
From efficiency high.
Preferably, the air inlet pipe is shaped as rhombus or pentagon；The bootable compressed gas into housing cavity
Body downwards are moved, and to reduce resistance, improve separative efficiency.
Preferably, the separation lid is the cambered surface being bent upwards, and the osculum, which is evenly distributed on, separates lid periphery；
Quickly the drop of centrifugation is expelled directly out, from osculum after being assembled by the drop or liquid foam of baffle plate separation by separation lid
Discharge, the velocity of discharge of accelerating liquid, it can also effectively stop the aqueous vapor that housing bottom escapes.
Preferably, the housing lower end is reclinate cambered surface；The fluid zone of concentration can be formed, is effectively collected point
From obtained liquid, and there is bigger saturation than reverse taper shape.
Preferably, the inner barrel is fixed on the top of housing；Ensure that compressed air enters after housing along housing
Spiral inner wall flows, and avoids producing unnecessary pressure drop, ensures higher separative efficiency.
Preferably, the drainpipe is connected with liquid seal device, long-term to keep housing bottom to leave a small amount of liquid water, is formed
Fluid-tight；Effectively avoid compressed air from being escaped from drainpipe, produce gas leak phenomenon, lower air-treatment amount.
Preferably, the housing upper end is provided with cap, and the cap is connected with shell flange；It is easy to disassemble, it is beneficial to
In the future to the maintenance of equipment.
Preferably, the edge of the helical baffle is close to housing sidewall inner surface；Compressed gas to entering housing
There are more preferable guide functions, make full use of centrifugal force preferably to be separated, ensure more preferable separating effect.
Preferably, the outer of the baffle plate tilts down setting；Relatively expressed beneficial to by the drop separated by baffle plate
Collection gets up, and accelerates collection process, avoids being mixed into again in compressed gas and reducing separating effect.
The beneficial effects of the utility model are as follows：
The utility model is compact-sized, is centrifuged with reference to gravity and two kinds of separate modes are separated with baffle plate, by compressed air
In drop and liquid foam efficiently separate, good separating effect, separative efficiency is high, while effectively avoids compressing stomata leakage, further
Ensure higher air-treatment amount, the unnecessary water velocity of discharge is fast, and structure is reliable, can keep preferable working condition for a long time.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Reference：1- housings, 2- air inlet pipe, 3- drainpipes, 4- separation lids, 5- inner barrels, 6- helical baffles, 7- gears
Plate, 8- escape pipes.
Embodiment
In order to which those skilled in the art are better understood from the utility model, below in conjunction with the accompanying drawings with following examples to this
Utility model is described in further detail.
Embodiment 1
As shown in figure 1, the present embodiment provides a kind of freezing type drier spiral type gas-water separator, including housing 1, institute
State the sidewall upper of housing 1 and be connected with air inlet pipe 2, the axis direction of air inlet pipe 2 and the side wall of housing 1 are tangent, the side wall of housing 1
Lower end is provided with separation lid 4, and the inner chamber of housing 1 is divided into two parts up and down by the separation lid 4, is separated and is offered some drainings on lid 4
Hole, the bottom of housing 1 offer discharge outlet, and the discharge outlet is connected with drainpipe 3, and the inside of housing 1 is provided with inner barrel 5, described
The outer surface of inner barrel 5 is fixed with helical baffle 6, and the lower end of inner barrel 5 is opened, and staggeredly some gears are fixed with the inner chamber of inner barrel 5
Plate 7, the lower surface of baffle plate 7 are provided with some burrs, and the upper end of inner barrel 5 is connected with escape pipe 8, and the escape pipe 8 extends to
Outside housing 1.
The operation principle of the present embodiment：Compressed gas enters housing from air inlet pipe 2, under the guide functions of helical baffle 6,
Screw is carried out, then is folded to by separating lid 4 into inner barrel, is constantly collided with baffle plate 7, then passes through escape pipe 8
Discharge, during which the drop of separation or liquid foam are discharged by separating the osculum on lid 4 into drainpipe 3.
Compressed gas carries out first time separation using centrifugal force and gravity in the present embodiment, is made by the water conservancy diversion of helical baffle
For strengthening separating effect, the most of drop separation carried secretly in compressed gas is gone out, then is folded to by separating lid in entrance
Cylinder, by the baffle plate with burr, by continuous collision process, continue the drop in compressed air and the separation of liquid foam, knot
Structure is compact, good separating effect, and separative efficiency is high.
Embodiment 2
As shown in figure 1, further optimize on the basis of the freezing type drier moisture trap described in embodiment 1,
The air inlet pipe 2 is shaped as rhombus or pentagon, and the bootable compressed gas downwards into the inner chamber of housing 1 are moved, with
Just resistance is reduced, improves separative efficiency.
Embodiment 3
As shown in figure 1, further optimize on the basis of the freezing type drier moisture trap described in embodiment 1,
The separation lid 4 is the cambered surface being bent upwards, and the osculum is evenly distributed on separation lid 4 periphery, quickly by centrifugation
Drop is expelled directly out, the drop or liquid foam separated by baffle plate 7 by separate lid 4 assemble after from osculum discharge, accelerating liquid
The velocity of discharge, can also effectively stop the bottom of housing 1 effusion aqueous vapor.
Embodiment 4
As shown in figure 1, further optimize on the basis of the freezing type drier moisture trap described in embodiment 1,
The lower end of housing 1 is reclinate cambered surface, can form the fluid zone of concentration, effectively collects isolated liquid, and compare
Reverse taper shape has bigger saturation.
Embodiment 5
As shown in figure 1, further optimize on the basis of the freezing type drier moisture trap described in embodiment 1,
The inner barrel 5 is fixed on the top of housing 1, ensures that compressed air flows after entering housing 1 along the spiral inner wall of housing 1, keeps away
Exempt to produce unnecessary pressure drop, ensure higher separative efficiency.
Embodiment 6
As shown in figure 1, further optimize on the basis of the freezing type drier moisture trap described in embodiment 1,
The drainpipe 3 is connected with liquid seal device, long-term to keep the bottom of housing 1 to leave a small amount of liquid water, forms fluid-tight, effectively avoids compressing
Air escapes from drainpipe 3, produces gas leak phenomenon, lowers air-treatment amount.
Embodiment 7
As shown in figure 1, further optimize on the basis of the freezing type drier moisture trap described in embodiment 1,
The upper end of housing 1 is provided with cap, and the cap is connected with the flange of housing 1, easy to disassemble, beneficial to the maintenance to equipment in the future.
Embodiment 8
As shown in figure 1, further optimize on the basis of the freezing type drier moisture trap described in embodiment 1,
There are more preferable guide functions at the edge of the helical baffle 6 close to the side wall inner surfaces of housing 1, to the compressed gas for entering housing 1,
Make full use of centrifugal force preferably to be separated, ensure more preferable separating effect.
Embodiment 9
As shown in figure 1, further optimize on the basis of the freezing type drier moisture trap described in embodiment 1,
The outer of the baffle plate 7 tilts down setting, comparatively fast collects beneficial to by the drop separated by baffle plate 7, accelerates to be collected into
Journey, avoid being mixed into again in compressed gas and reducing separating effect.
It is described above, preferred embodiment only of the present utility model, not limiting the utility model, the utility model
Scope of patent protection be defined by claims, it is every to be equal with what specification of the present utility model and accompanying drawing content were made
Structure change, similarly it should be included in the scope of protection of the utility model.
Claims (9)
1. a kind of freezing type drier spiral type gas-water separator, including housing (1), it is characterised in that：Housing (1) side
Wall upper end is connected with air inlet pipe (2), and air inlet pipe (2) axis direction and housing (1) side wall are tangent, housing (1) side wall
Lower end is provided with separation lid (4), and housing (1) inner chamber is divided into two parts up and down, offered on separation lid (4) by the separation lid (4)
Some osculums, housing (1) bottom offer discharge outlet, and the discharge outlet is connected with drainpipe (3), set inside housing (1)
There is inner barrel (5), inner barrel (5) outer surface is fixed with helical baffle (6), and the lower end of inner barrel (5) opens, inner barrel
(5) some baffle plates (7) are fixed with staggeredly on inner chamber, baffle plate (7) lower surface is provided with some burrs, on the inner barrel (5)
End is connected with escape pipe (8), and the escape pipe (8) extends to housing (1) outside.
2. freezing type drier moisture trap according to claim 1, it is characterised in that：The air inlet pipe (2)
It is shaped as rhombus or pentagon.
3. freezing type drier moisture trap according to claim 1, it is characterised in that：(4) are covered in the separation
The cambered surface being bent upwards, the osculum are evenly distributed on separation lid (4) periphery.
4. freezing type drier moisture trap according to claim 1, it is characterised in that：Housing (1) lower end
For reclinate cambered surface.
5. freezing type drier moisture trap according to claim 1, it is characterised in that：The inner barrel (5) is solid
It is scheduled on the top of housing (1).
6. freezing type drier moisture trap according to claim 1, it is characterised in that：The drainpipe (3) is even
There is liquid seal device, keep housing (1) bottom to leave a small amount of liquid water for a long time, form fluid-tight.
7. freezing type drier moisture trap according to claim 1, it is characterised in that：Housing (1) upper end
Provided with cap, the cap is connected with housing (1) flange.
8. freezing type drier moisture trap according to claim 1, it is characterised in that：The helical baffle (6)
Edge close to housing (1) side wall inner surfaces.
9. freezing type drier moisture trap according to claim 1, it is characterised in that：Outside the baffle plate (7)
Edge tilts down setting.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721198089.2U CN207203662U (en) | 2017-09-19 | 2017-09-19 | A kind of freezing type drier spiral type gas-water separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721198089.2U CN207203662U (en) | 2017-09-19 | 2017-09-19 | A kind of freezing type drier spiral type gas-water separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207203662U true CN207203662U (en) | 2018-04-10 |
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ID=61821578
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721198089.2U Active CN207203662U (en) | 2017-09-19 | 2017-09-19 | A kind of freezing type drier spiral type gas-water separator |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110118714A (en) * | 2019-05-31 | 2019-08-13 | 江苏蓝创智能科技股份有限公司 | A kind of equipment monitoring oil fume purifier operating status |
| CN111111324A (en) * | 2020-01-20 | 2020-05-08 | 风氢扬科技(杭州)有限公司 | Water-gas separating device |
| CN111569535A (en) * | 2020-05-22 | 2020-08-25 | 重庆开山压缩机有限公司 | But accurate control's dewatering jar |
| CN112221253A (en) * | 2020-11-10 | 2021-01-15 | 天津君宇科技股份有限公司 | Exhaust structure |
| CN113521888A (en) * | 2020-04-17 | 2021-10-22 | 广东美的白色家电技术创新中心有限公司 | Oil separator and compressor assembly |
| CN114105242A (en) * | 2022-01-21 | 2022-03-01 | 东营市赫邦化工有限公司 | Steam-water separator of dechlorination vacuum pump unit |
| CN116116150A (en) * | 2023-04-18 | 2023-05-16 | 德耐尔节能科技（上海）股份有限公司 | Efficient cooler steam-water separation method and device |
| CN116492766A (en) * | 2023-05-04 | 2023-07-28 | 广州奥科维电子有限公司 | Water-steam separation device and use method thereof |
| CN116712783A (en) * | 2023-08-10 | 2023-09-08 | 湖南湾公坡农业科技发展有限公司 | Tea oil spiral propulsion type oil impurity separation equipment and separation method |
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2017
- 2017-09-19 CN CN201721198089.2U patent/CN207203662U/en active Active
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110118714A (en) * | 2019-05-31 | 2019-08-13 | 江苏蓝创智能科技股份有限公司 | A kind of equipment monitoring oil fume purifier operating status |
| CN111111324A (en) * | 2020-01-20 | 2020-05-08 | 风氢扬科技(杭州)有限公司 | Water-gas separating device |
| CN113521888A (en) * | 2020-04-17 | 2021-10-22 | 广东美的白色家电技术创新中心有限公司 | Oil separator and compressor assembly |
| CN111569535A (en) * | 2020-05-22 | 2020-08-25 | 重庆开山压缩机有限公司 | But accurate control's dewatering jar |
| CN112221253A (en) * | 2020-11-10 | 2021-01-15 | 天津君宇科技股份有限公司 | Exhaust structure |
| CN114105242A (en) * | 2022-01-21 | 2022-03-01 | 东营市赫邦化工有限公司 | Steam-water separator of dechlorination vacuum pump unit |
| CN114105242B (en) * | 2022-01-21 | 2022-05-20 | 东营市赫邦化工有限公司 | Steam-water separator of dechlorination vacuum pump unit |
| CN116116150A (en) * | 2023-04-18 | 2023-05-16 | 德耐尔节能科技（上海）股份有限公司 | Efficient cooler steam-water separation method and device |
| CN116492766A (en) * | 2023-05-04 | 2023-07-28 | 广州奥科维电子有限公司 | Water-steam separation device and use method thereof |
| CN116712783A (en) * | 2023-08-10 | 2023-09-08 | 湖南湾公坡农业科技发展有限公司 | Tea oil spiral propulsion type oil impurity separation equipment and separation method |
| CN116712783B (en) * | 2023-08-10 | 2023-10-31 | 湖南湾公坡农业科技发展有限公司 | Tea oil spiral propulsion type oil impurity separation equipment and separation method |
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Legal Events
| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20200116 Address after: 510000 Room 102, building 7, No. 100, Yufeng Road, Nansha District, Guangzhou City, Guangdong Province Patentee after: GUANGZHOU SPEED REFRIGERATION EQUIPMENT Co.,Ltd. Address before: 510000 Guangzhou High-tech Industrial Development Zone Science Avenue 231, 233 Skirt Building B1B2, 1st, 2nd, 3rd and 4th floors Patentee before: BOAO ZONGHENG NETWORK TECHNOLOGY Co.,Ltd. Effective date of registration: 20200116 Address after: 510000 Guangzhou High-tech Industrial Development Zone Science Avenue 231, 233 Skirt Building B1B2, 1st, 2nd, 3rd and 4th floors Patentee after: BOAO ZONGHENG NETWORK TECHNOLOGY Co.,Ltd. Address before: Zhenghualu jinshuiqu 450045 Henan city in Zhengzhou Province, twenty-first Century No. 59 Building No. 13 West community 2 unit 1 No. A2304 Patentee before: HENAN PROVINCE KANG SOURCE BIOTECHNOLOGY LTD. |
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| TR01 | Transfer of patent right |