CN206587508U - A kind of new gas-liquid separator - Google Patents
A kind of new gas-liquid separator Download PDFInfo
- Publication number
- CN206587508U CN206587508U CN201720115620.9U CN201720115620U CN206587508U CN 206587508 U CN206587508 U CN 206587508U CN 201720115620 U CN201720115620 U CN 201720115620U CN 206587508 U CN206587508 U CN 206587508U
- Authority
- CN
- China
- Prior art keywords
- pipe
- medium
- base body
- blow
- erecting bed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 14
- 239000010865 sewage Substances 0.000 claims abstract description 6
- 238000007789 sealing Methods 0.000 claims description 3
- 238000012423 maintenance Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 4
- 239000012535 impurity Substances 0.000 description 7
- 239000003595 mist Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 4
- 230000005484 gravity Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Cyclones (AREA)
Abstract
The utility model discloses a kind of new gas-liquid separator, wherein, the erecting bed that is integrally formed with including base body, on base body, the main cylinder being connected with erecting bed, the first medium pipe and second medium pipe being provided with the erecting bed inside main cylinder, and the blow-off pipe being provided with erecting bed.The sewage draining exit for being provided with and being connected with blow-off pipe on the media outlet for being provided with and being connected with second medium pipe on the medium inlet connected with first medium pipe, base body, base body is provided with base body.Second medium tube inlet end is higher than 36 times of the first medium pipe port of export.The length for being shorter in length than first medium pipe of blow-off pipe.The utility model, which has, to be not easily blocked and is easy to regular maintenance, and the low effect of cost.
Description
Technical field
The utility model is related to mist of oil separation and exhaust apparatus field, and more particularly to a kind of gas refrigeration formula that is applied to is dried
Among machine, mesohigh gas air compressor machine rear portion, the new gas-liquid that the debris such as the water in medium, oil are separated with dielectric gas point
From device.
Background technology
At present, gas-liquid separation device on the market is either intercepted using stop collision effect using filter element filtering net mostly
Filter, it is therefore an objective to impurity is separated with medium.Because above two mode is present, the pressure loss is big, low separation efficiency, and
It is complicated and be unfavorable for daily maintenance.In addition, filter core use time length, it is necessary to regularly replace, increases use cost.
Utility model content
In view of the above problems, the purpose of this utility model is that providing one kind is not easily blocked and is easy to regular maintenance, and into
This low new gas-liquid separator.
To achieve the above object, a kind of new gas-liquid separator that the utility model is provided, wherein, including base body,
The erecting bed that is integrally formed with base body, the main cylinder being connected with erecting bed, it is provided with the erecting bed inside main cylinder
First medium pipe and second medium pipe, and the blow-off pipe being provided with erecting bed.It is provided with base body and first medium Guan Lian
It is provided with the media outlet connected with second medium pipe, base body and is provided with and blow-off pipe on logical medium inlet, base body
The sewage draining exit of connection.Second medium tube inlet end is higher than 3-6 times of the first medium pipe port of export.Blow-off pipe is shorter in length than first Jie
The length of matter pipe.Thus, second medium tube inlet end is higher than 3-6 times of the first medium pipe port of export, it is therefore an objective to ensure air dielectric
Effective travel in main cylinder, and effectively prevent the impurity separated from entering in second medium pipe.In addition, the length of blow-off pipe
Degree is shorter than the length of first medium pipe, that is, blow-off pipe is located at below first medium pipe, and is higher by the main appropriate height in cylinder bottom,
Purpose is to avoid solid impurity from entering in blow-off pipe.
In some embodiments, first medium tube end is provided with turning head.
In some embodiments, blowdown tube end is provided with arc-shaped joint.
In some embodiments, it is provided with sealing ring between erecting bed and main cylinder.
The beneficial effects of the utility model are that have to be not easily blocked and be easy to regular maintenance, and the low effect of cost.Using
When, the air dielectric for being mixed with mist of oil and steam enters from medium inlet, after become owner of through the conveying of first medium pipe in cylinder.This
When, it is at a certain angle using turning head on first medium tube end and main cylinder medial surface shape, it is therefore an objective to ensure air dielectric with
30-60 degree angles are conveyed into main cylinder.Then, air dielectric rotates around main cylinder inwall and risen, in rotary course, air
Mist of oil and steam contained by medium are under the influence of centrifugal force so that be attached in barrel, and suitable under gravity
Main cylinder inwall and flow to main cylinder bottom, most afterwards after blow-off pipe from sewage draining exit.Wherein, blow-off pipe is shorter in length than first medium pipe
Length, that is, blow-off pipe be located at below first medium pipe, and be higher by the main appropriate height in cylinder bottom, efficiently solve conventional gas
The problem of liquid filter bottom blow-down, i.e. solid impurity, block the hidden danger that blowoff valve has low separation efficiency.In addition, first medium
The runner of pipe and second medium pipe is without undergauge, and the pressure loss is small, simple in construction, convenient disassembly, it is not necessary to regular maintenance, no material consumption
Consumption, operating cost is low, and small volume, installation site is unrestricted.It is thereby achieved that be not easily blocked and be easy to regular maintenance, and
The low effect of cost.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model；
Fig. 2 is internal structure schematic diagram of the present utility model；
Fig. 3 is the structural representation of base body and erecting bed.
Embodiment
Utility model is described in further detail below in conjunction with the accompanying drawings.
As Figure 1-3, a kind of new gas-liquid separator, including base body 1, the peace that is integrally formed with base body 1
Dress platform 2, the main cylinder 3 being connected with erecting bed 2, the first medium pipe 4 and second being provided with the erecting bed 2 inside main cylinder 3
Medium tube 5, and the blow-off pipe 6 being provided with erecting bed 2.The medium inlet connected with first medium pipe 4 is provided with base body 1
7, it is provided with base body 1 and is provided with what is connected with blow-off pipe 6 on the media outlet 8 connected with second medium pipe 5, base body 1
Sewage draining exit 9.The arrival end of second medium pipe 5 is higher than 3-6 times of 4 port of export of first medium pipe.Blow-off pipe 6 is shorter in length than first medium
The length of pipe 4.The arrival end of second medium pipe 5 is higher than 3-6 times of 4 port of export of first medium pipe, it is therefore an objective to ensure air dielectric in master
Effective travel in cylinder 3, and effectively prevent the impurity separated from entering in second medium pipe 5.In addition, the length of blow-off pipe 6
Degree is shorter than the length of first medium pipe 4, that is, blow-off pipe 6 is located at the lower section of first medium pipe 4, and it is appropriate to be higher by the main bottom of cylinder 3
Highly, it is therefore an objective to avoid solid impurity from entering in blow-off pipe 6.The end of first medium pipe 4 is provided with turning first 10.The end of blow-off pipe 6
Portion is provided with arc-shaped joint 11.Sealing ring 12 is provided between erecting bed 2 and main cylinder 3.
Using when, the air dielectric for being mixed with mist of oil and steam enters from medium inlet 7, after it is defeated through first medium pipe 4
Send into main cylinder 3.Now, it is at a certain angle using turning head on the end of first medium pipe 4 and the main medial surface shape of cylinder 3, purpose
It is to ensure that air dielectric is conveyed into main cylinder 3 with 30-60 degree angles.Then, air dielectric is in the rotation of the main inwall of cylinder 3
Rise, in rotary course, mist of oil and steam contained by air dielectric are under the influence of centrifugal force so that be attached in barrel
, and the main bottom of cylinder 3 is flowed to along the main inwall of cylinder 3 under gravity, most afterwards after blow-off pipe 6 from sewage draining exit 9.Wherein,
The length for being shorter in length than first medium pipe 4 of blow-off pipe 6, that is, blow-off pipe 6 are located at the lower section of first medium pipe 4, and are higher by master
The appropriate height in 3 bottoms of cylinder, the problem of efficiently solving conventional gas-liquid filter bottom blowdown, i.e. solid impurity block blowoff valve and deposited
In the hidden danger of low separation efficiency.In addition, the runner of first medium pipe 4 and second medium pipe 5 is without undergauge, the pressure loss is small, structure
Simply, convenient disassembly, it is not necessary to regular maintenance, no material consumption consumption, operating cost is low, and small volume, installation site is unrestricted.
Above-described is only some embodiments of the present utility model.For the person of ordinary skill of the art,
On the premise of the utility model creation design is not departed from, various modifications and improvements can be made, these belong to practical new
The protection domain of type.
Claims (4)
1. a kind of new gas-liquid separator, it is characterised in that the erecting bed that is integrally formed with including base body, on base body,
The main cylinder being connected with erecting bed, the first medium pipe and second medium pipe that are provided with the erecting bed inside main cylinder, and
The blow-off pipe that erecting bed is provided with；
The medium inlet connected with first medium pipe is provided with described base body；
The media outlet connected with second medium pipe is provided with described base body；
The sewage draining exit connected with blow-off pipe is provided with described base body；
The length of the second medium pipe is 3-6 times of first medium length of tube；
The length for being shorter in length than first medium pipe of the blow-off pipe.
2. a kind of new gas-liquid separator according to claim 1, it is characterised in that described first medium tube end
It is provided with turning head.
3. a kind of new gas-liquid separator according to claim 2, it is characterised in that described blowdown tube end is set
There is arc-shaped joint.
4. a kind of new gas-liquid separator according to claim 1 or 2 or 3, it is characterised in that described erecting bed with
Sealing ring is provided between main cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720115620.9U CN206587508U (en) | 2017-02-07 | 2017-02-07 | A kind of new gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720115620.9U CN206587508U (en) | 2017-02-07 | 2017-02-07 | A kind of new gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206587508U true CN206587508U (en) | 2017-10-27 |
Family
ID=60128308
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720115620.9U Expired - Fee Related CN206587508U (en) | 2017-02-07 | 2017-02-07 | A kind of new gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206587508U (en) |
-
2017
- 2017-02-07 CN CN201720115620.9U patent/CN206587508U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190109 Address after: 511340 No. 8, Pacific 9 Road, Xintang Town, Zengcheng District, Guangzhou City, Guangdong Province Patentee after: GUANGZHOU JIAMEI MANUFACTURING Co.,Ltd. Address before: 510000 Factory Building No. 115-3-101, Pacific Industrial Zone, Xintang Town, Zengcheng District, Guangzhou, Guangdong Province Patentee before: GUANGZHOU JIAMEI MACHINERY MANUFACTURING Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171027 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |