CN205730738U - Separator-filter - Google Patents
Separator-filter Download PDFInfo
- Publication number
- CN205730738U CN205730738U CN201620377882.8U CN201620377882U CN205730738U CN 205730738 U CN205730738 U CN 205730738U CN 201620377882 U CN201620377882 U CN 201620377882U CN 205730738 U CN205730738 U CN 205730738U
- Authority
- CN
- China
- Prior art keywords
- baffle plate
- breather
- cylinder
- filter
- demarcation strip
- 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 claims description 17
- 230000004888 barrier function Effects 0.000 claims description 15
- 239000010865 sewage Substances 0.000 claims description 9
- 239000012535 impurity Substances 0.000 abstract description 8
- 238000005204 segregation Methods 0.000 abstract description 2
- 239000008187 granular material Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 13
- 238000001914 filtration Methods 0.000 description 8
- 238000000926 separation method Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 4
- 230000006872 improvement Effects 0.000 description 4
- 230000009471 action Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000003570 air Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000003749 cleanliness Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000004531 microgranule Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003129 oil well Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
Landscapes
- Cyclones (AREA)
- Separating Particles In Gases By Inertia (AREA)
Abstract
This utility model relates to a kind of segregation apparatus, is specifically related to a kind of separator-filter, including cylinder and fix the blind flange being connected with barrel port, is sequentially provided with demarcation strip, baffle plate and resolution element in described cylinder；The filter element that is additionally provided with between blind flange and demarcation strip in described cylinder and through baffle plate and the breather of resolution element, described resolution element has oblique teeth groove；Described breather lower end is opening, and upper end is blind end, and breather is positioned at the sidewall on baffle plate top and is provided with through hole；The air inlet that the sidewall of described cylinder is provided with between blind flange and demarcation strip and the air vent between baffle plate and resolution element.The utility model has the advantages that the aqueous water that can efficiently separate in gas and solid impurity granule, to reach to purify further the purpose of gas.
Description
Technical field
This utility model relates to a kind of segregation apparatus, is specifically related to a kind of separator-filter.
Background technology
In separator on existing market, to the gas containing liquid moisture and impurity particle (such as: compressed air, natural gas, coal bed gas, oil well implication, biogas etc.) separating effect is less desirable, and some gases in use need the gas that comparison is pure, existing separator to be unable to reach this requirement.
Utility model content
This utility model is intended to provide the separator-filter that cleaning gas degree after a kind of use is high.
Separator-filter in this programme, including cylinder and fix the blind flange being connected with barrel port, is sequentially provided with demarcation strip, baffle plate and resolution element in described cylinder；The filter element that is additionally provided with between blind flange and demarcation strip in described cylinder and through baffle plate and the breather of resolution element, described resolution element has oblique teeth groove；Described breather lower end is opening, and upper end is blind end, and breather is positioned at the sidewall on baffle plate top and is provided with through hole；The air inlet that the sidewall of described cylinder is provided with between blind flange and demarcation strip and the air vent between baffle plate and resolution element.
The utility model has the advantages that: after gas enters cylinder by air inlet, first the oblique teeth groove from resolution element passes, producing strong rotation with certain flow rate under the guide functions of oblique teeth groove, by centrifugal action, drop and grit that density is bigger are thrown out of.Then the air-flow rotated is upwardly formed secondary vortex flow by breather, can be separated further by small impurity, improves cleaning gas degree.Last gas filters to reach higher cleanliness factor further through filtration core.Therefore the problem that after this utility model can perfectly solve be upwardly formed the triple role of secondary vortex flow and filter element filtering by the cyclonic separation under resolution element effect, breather under to filter, cleaning gas degree is the highest.
As further improvement of the utility model, described baffle plate bottom is provided with the blow-off line connected with between demarcation strip and baffle plate；Described cylinder bottom has sewage draining exit, and described sewage draining exit is provided with female thread, so can be easy to isolated impurity, moisture discharge.
As further improvement of the utility model, described air inlet and exhaust ports are equipped with Pressure gauge, in order to observe pressure and the pressure reduction of air inlet air vent；The lower section of described breather is additionally provided with liquid barrier, and described liquid barrier is provided with scupper, and described scupper is provided with female thread.
As further improvement of the utility model, described liquid barrier is the pyramidal structure to breather projection, and described scupper has junction that is multiple and that be uniformly distributed in liquid barrier and cylinder, it is simple to sewage and impurity are got rid of.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model separator-filter embodiment.
In figure, 1 is Pressure gauge 1, and 2 is the first buffer area, 3 is air inlet, and 4 is oblique teeth groove, and 5 is sewage draining exit, 6 is Chu Wu district, and 7 is liquid barrier, and 8 is breather, 9 is cyclone separation, and 10 is separating plate, and 11 is blow-off line, 12 is the second buffer area, and 13 is filtering area, and 14 is cylinder, 15 is air vent, and 16 is filter element, and 17 is blind flange.
Detailed description of the invention
With detailed description of the invention, this utility model is described in further detail below in conjunction with the accompanying drawings:
According to Fig. 1, a kind of separator-filter, blind flange 17 is connected by bolt is fixing with the port of cylinder 14, demarcation strip, baffle plate, separating plate 10 and liquid barrier 7 it is welded with successively in this cylinder 14, oblique teeth groove 4 is had on separating plate 10, under the guide functions of this oblique teeth groove 4, gas produces strong rotation with certain flow rate, thus produces centrifugal force by liquid moisture, magazins' layout out；This liquid barrier 7 is the pyramidal structure raised up, and liquid barrier 7 is evenly equipped with multiple scupper with the junction of cylinder 14.It it is filtering area 13 between demarcation strip and blind flange 17, demarcation strip and baffle plate time are the second buffer area 12, it is the first buffer area between baffle plate and separating plate 10, is cyclone separation 9 between separating plate 10 and liquid barrier 7, be Chu Wu district 6 between the low side of liquid barrier 7 and cylinder 14.Being additionally provided with filter element 16 and breather 8 in cylinder 14, filter element 16 is positioned at filtering area 13 and fixing with demarcation strip is connected, and breather 8 passes baffle plate and separating plate 10 and is respectively welded with the two；Breather 8 lower end is opening, and upper end is blind end, and breather 8 is positioned at the sidewall of the second buffer area 12 and is provided with through hole.Cylinder 14 bottom has the sewage draining exit 5 connected with Chu Wu district 6, and this sewage draining exit 5 is provided with female thread, it is simple to install blowoff valve.Baffle plate bottom is provided with the blow-off line 11 connected with the second buffer area 12, and this blow-off line 11 is female thread, is not only convenient for installing blowoff valve, is also convenient for the moisture separated and impurity are discharged cylinder 14.The sidewall of cylinder 14 is provided with the air inlet connected with the first buffer area and the air vent 15 connected with filtering area 13.Pressure and pressure reduction for the ease of observing air inlet air vent 15 are respectively equipped with a Pressure gauge 1 at air inlet and air vent 15.
During use, impure gas enters the first buffer area by air inlet, oblique teeth groove 4 along separating plate 10 enters cyclone separation 9 again, now under the guide functions of oblique teeth groove 4, gas produces strong rotation with certain flow rate, cyclone separation 9 it is downwardly into twist again along cylinder 14 inwall, drop and grit that density is bigger are thrown toward cylinder 14 inwall under centrifugal action, and fall to contact with liquid barrier 7 along cylinder 14 inwall under gravity.Rear drop and the impurity sewage draining exit 5 bottom cylinder 14 is discharged.Then, the air-flow rotated shrinks to center flow in cyclone separation 9 by breather 8, and be upwardly formed secondary vortex flow and enter the second buffer area 12, the most isolated minute impurities is filtered further by filter element 16, cleaning gas after filtration is discharged by air vent 15, and the microgranule after filtration is then discharged by blow-off line 11.By blind flange 17 is dismantled i.e. replaceable cartridge 16, it is convenient to change.
Above-described is only embodiment of the present utility model, and in scheme, the known general knowledge such as concrete structure and characteristic too much describes at this.Should be understood that; for a person skilled in the art, on the premise of without departing from this utility model structure, it is also possible to make some deformation and improvement; these also should be considered as protection domain of the present utility model, and these are all without affecting effect and the practical applicability that this utility model is implemented.
Claims (4)
1. separator-filter, it is characterised in that: include cylinder and fix the blind flange being connected with barrel port, in described cylinder, being sequentially provided with demarcation strip, baffle plate and resolution element；The filter element that is additionally provided with between blind flange and demarcation strip in described cylinder and through baffle plate and the breather of resolution element, described resolution element has oblique teeth groove；Described breather lower end is opening, and upper end is blind end, and breather is positioned at the sidewall on baffle plate top and is provided with through hole；The air inlet that the sidewall of described cylinder is provided with between blind flange and demarcation strip and the air vent between baffle plate and resolution element.
Separator-filter the most according to claim 1, it is characterised in that: described baffle plate bottom is provided with the blow-off line connected with between demarcation strip and baffle plate；Described cylinder bottom has sewage draining exit, and described sewage draining exit is provided with female thread.
Separator-filter the most according to claim 1, it is characterised in that: described air inlet and exhaust ports are equipped with Pressure gauge；The lower section of described breather is additionally provided with liquid barrier, and described liquid barrier is provided with scupper, and described scupper is provided with female thread.
Separator-filter the most according to claim 3, it is characterised in that: described liquid barrier is the pyramidal structure to breather projection, and described scupper has junction that is multiple and that be uniformly distributed in liquid barrier and cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620377882.8U CN205730738U (en) | 2016-04-29 | 2016-04-29 | Separator-filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620377882.8U CN205730738U (en) | 2016-04-29 | 2016-04-29 | Separator-filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205730738U true CN205730738U (en) | 2016-11-30 |
Family
ID=57371755
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620377882.8U Expired - Fee Related CN205730738U (en) | 2016-04-29 | 2016-04-29 | Separator-filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205730738U (en) |
-
2016
- 2016-04-29 CN CN201620377882.8U patent/CN205730738U/en not_active Expired - Fee Related
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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: 20161130 |