CN208839267U - Liquid separator - Google Patents
Liquid separator Download PDFInfo
- Publication number
- CN208839267U CN208839267U CN201821137802.7U CN201821137802U CN208839267U CN 208839267 U CN208839267 U CN 208839267U CN 201821137802 U CN201821137802 U CN 201821137802U CN 208839267 U CN208839267 U CN 208839267U
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- Prior art keywords
- reservoir
- liquid
- filter cell
- container
- liquid separator
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- 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.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/20—Combinations of devices covered by groups B01D45/00 and B01D46/00
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0027—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions
- B01D46/003—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions including coalescing means for the separation of liquid
- B01D46/0031—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with additional separating or treating functions including coalescing means for the separation of liquid with collecting, draining means
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
- Degasification And Air Bubble Elimination (AREA)
Abstract
The utility model designs a kind of liquid separator, it is with container, container limits space, filter cell is arranged so that gas-liquid mixture has to pass through filter cell after entering container via entrance and before it can leave container via outlet in space, the reservoir that the liquid discharge tube collected in reservoir is attached to filter cell can be discharged, reservoir is provided with equipment, once the liquid level in equipment reservoir falls below specified level and is shut off discharge pipe, liquid separator is provided with separator, its side wall from container extends around outlet and including the base wall with entrance opening, the chamber of filter cell is wherein attached with by separator, a part of the side wall of base wall and container limits, it extends from base wall around entrance opening, and all features above are arranged so that in separator The exit region with outlet connection is limited between filter cell.It therefore, will be so that gas will not be removed when liquid is less.
Description
Technical field
The utility model relates to a kind of liquid separators for being provided with this filter cell.
More specifically, the utility model is intended to the liquid in separating liquid/gas mixtures.
Background technique
In liquid-spraying type machine (such as compressor or expanding machine), the gas of compression or expansion will contain a certain amount of liquid
Body, such as oil or water.
Therefore, liquid separator can be installed after the liquid-spraying type machine to separate liquid with gas.
In general, this liquid separator includes container, the container has for the entrance of gas-liquid mixture and for transporting
The outlet for gas of walking that treated, wherein the container defines space, and is wherein provided with filter in the space
Element, the filter cell extend around the outlet.
Entrance is preferably arranged at the position tangent with the side wall of container, so that gas-liquid mixture follows spiral shell in a reservoir
Revolve shape track, thus allow occur the first separation phase, in first separation phase centrifugal force cause in mixture compared with
The liquid particles of weight finally flow downward against the side wall of container and then along the side wall.However, it's not necessary.
It is not precluded within the pipe or separator that setting extends around filter cell between the side wall of container and filter cell,
To limit entrance area between the side wall and pipe of container, the first separation phase will occur in the entrance area.
If there is the pipe, then gas-liquid mixture will be forced to surround the endwall flow of pipe, to change direction and court
To output flow.
In this way it is possible to which another separation phase occurs, flowed up because heavier liquid particles will not turn to,
But it will continue to flow downward.
Isolated next stage occurs to flow through filter before leaving liquid separator by outlet in gas-liquid mixture
At the time of element.
Finally, when gas-liquid mixture passes through filter cell, in most cases, most light and the smallest liquid particles
Therefore it is removed from gas by filter cell.
In the inside of filter cell, the droplet formation of liquid and the bottom for flowing to filter cell.
Drop is collected and is carried away by means of the point of discharge pipe towards lower pressure at the bottom.
Isolated liquid is typically collected in the reservoir in the container of liquid separator, and this occupies liquid point
From the space in device, then which cannot load other liquid separator components (such as filter cell).
In traditional filter cell, the nozzle in discharge pipe will determine discharge amount (discharge).
If discharge amount is too low, filter cell will become to be saturated with liquid, and the separation in filter cell will not
It is optimal, and therefore big quantity of fluid will leave filter cell via outlet, so as to cause resulting all disadvantages.
This is why the size of discharge amount and therefore nozzle is chosen to ensure have in all cases
Enough discharges.
This means that bulk gas is unnecessarily transported, especially when filter cell separates seldom liquid, because for
As the discharge rate of gas-liquid mixture is low or because the liquid in gas-liquid mixture is seldom.
This is likely to result in loss.
For this reason, some known liquid separators are provided with a kind of equipment, once in the equipment reservoir
Liquid level drop to specified level or just completely close discharge pipe lower than specified level.By opening these equipment, once the storage
Storage is filled on specific above-mentioned level, then is only transported some isolated liquid in reservoir.
Disadvantage of this is that reservoirs to be always filled with a certain amount of isolated liquid, this has been determined in liquid separator
Space needed for reservoir.
Utility model content
The purpose of the utility model is to provide the solutions of at least one of aforementioned and/or other shortcomings.This is practical
Novel also aim to keeps liquid separator usually as compact as possible, and does not have to transport unnecessary excess gas together with isolated liquid
Body, but still realize the maximum separation of liquid and gas-liquid mixture.
Purpose involved in the utility model is a kind of liquid separator, and the liquid separator has container, the appearance
Device has the entrance for gas-liquid mixture and the outlet for gas of transporting that treated,
Wherein, the container limits space,
Wherein, filter cell is arranged so that gas-liquid mixture after entering container via entrance in the space
And filter cell is had to pass through before it can leave container by outlet,
Wherein, it is provided with reservoir, is collected in the reservoir by the liquid of filter cell separation,
Wherein, discharge pipe is connected to the reservoir, and the discharge pipe can transport the liquid collected in reservoir, and
And
Wherein, reservoir is provided with equipment, once the liquid level in the equipment reservoir drops to specified level or is lower than
Specified level is shut off discharge pipe,
It is characterized in that, the liquid separator is provided with separator (screen), side wall of the separator from container
Extend around above-mentioned outlet, and including the base wall with entrance opening,
Wherein, the chamber is limited by a part of the side wall of separator, base wall and container,
Wherein, it is attached with above-mentioned filter cell in the chamber being thusly-formed, the filter cell is from described
Base wall extends around the entrance opening, and all features above are arranged so that in the separator and the filter
Exit region is limited between element, the exit region is connect with said outlet.
One advantage is isolated liquid and gas barrier by using reservoir, and is collected in specific position (i.e.
Reservoir) in.
It is also provided with and closes setting for discharge pipe when the liquid level in reservoir drops to specified level or lower than specified level
It is standby.This means that can only transport liquid, gas can't be transported.
" closing discharge pipe " is understood to mean that no liquid will be allowed and is discharged from reservoir by discharge pipe.
One advantage is (usually to be separated in any liquid when the liquid in reservoir is seldom and collect it
Before be initially separated process in the case where), discharge pipe can be with temporary close, so that in this case without gas or gas-liquid mixed
Object is carried away.
In principle, the position that the liquid of removal is actually pulled away is not important the utility model.
The liquid of removal can for example be brought to injection-tube, so that liquid be allowed to refill in machine.
The utility model is also applied for all types of gas-liquid mixtures, in other words, does not have to the type of gas or liquid
It is restricted.
The utility model applies also for all types of pressure, and is therefore also applied for compressor and vacuum machine.
When the separator extended around outlet is arranged in liquid separator, the gas-liquid mixed of container is entered via entrance
Object must follow the track of spiral shape or whirlwind shape first before reaching filter cell, thereby promote liquid and gas-liquid
Mixture separation.It is heavier in centrifugal forces affect gas-liquid mixture when gas-liquid mixture follows this spiral track
Drop under the action of, these drops of liquid are actually collided with the side wall of container and then along the side wall towards container
Flows can take out the drop from container at the bottom.
Separator is provided with base wall, is combined to be formed using a part of the base wall and separator and the side wall of container
Compact chamber.The base wall of the chamber provides mechanical support for the filter cell being inserted.
The formation of this compact chamber has other advantage, i.e., the described chamber includes for for isolated liquid
The potentially integrated space of reservoir.
In a preferred embodiment, the form for flap valve or valve being made for closing the above equipment of discharge pipe.
Flap valve or valve can be that machine automatization operates or can be automatically controlled.
In addition, flap valve or valve can provide power or flap valve by gravity, spring, magnetic force or valve can be by electronically
Power is provided.
In a preferred embodiment, similar float is made in the equipment, and the discharge that the float can close in reservoir is opened
Mouthful, device is provided with so that float to be maintained to the position above outlet opening.
" outlet opening " is understood to mean that the opening in reservoir, and the outlet opening is connect with discharge pipe.
One advantage of this embodiment is not need peripheral operation or active operation.
In fact, float can be made into so that once the liquid level in reservoir is too low, float will just close outlet opening,
It is further discharged so that not having liquid, and any gas is made to be impossible to escape.
The device that float is maintained to the position above outlet opening will ensure that float cannot be " free everywhere in reservoir
Ground " floating, but will remain in a position, once so that the liquid level in reservoir declines, float will just close outlet opening.
In an actual embodiment, reservoir is made into individual reservoir, and the reservoir uses connecting tube and filtering
The connection of device element.The individual reservoir can be arranged in the external container of liquid separator, to save the space in container.
In the actual embodiment of substitution, reservoir is integrated in filter cell or one of filter cell
Point.
In the preferred embodiment of the utility model, discharge pipe is provided with the nozzle positioned at reservoir downstream, is divided with adjusting
From liquid from the discharge amount in reservoir.
In the preferred embodiment of liquid separator according to the present utility model, base wall is provided with multiple entrance openings,
Multiple filter cells in chamber extend around the entrance opening.
In this way, the increase of filter surfaces is realized for the chamber of identical size, this leads to liquid and gas-liquid
The isolated increase of mixture, without space needed for increasing liquid separator.In other words, this liquid separator ensure that
The separation of increased liquid.Thus the increased discharge of isolated liquid can be carried away in an efficient way via discharge pipe.
Detailed description of the invention
In order to preferably show the feature of the utility model, below with reference to the accompanying drawings by means of example without any restrictions
Ground describes the preferred embodiment of liquid separator according to the present utility model, in which:
Fig. 1 schematically shows known liquid separator；
Fig. 2 shows liquid separators according to the present utility model；
Fig. 3 illustrates in greater detail the part indicated in Fig. 2 with F3；
Fig. 4 shows the modification of Fig. 3；
Fig. 5 schematically shows the alternate embodiment of liquid separator according to the present utility model.
Specific embodiment
The liquid separator 1 schematically shown in Fig. 1 includes container, and the container has entering for gas-liquid mixture
Mouthful and for gas of transporting that treated outlet.
Container 2 defines that space 5, the space 5 are closed at top 6 with lid 7.The lid 7 can with or cannot
It is dismantled from container 2.It can also be not provided with individual lid 7.
Filter cell 8 is provided in space 5, the filter cell 8 extends around outlet 4 in this case,
So that having to pass through filter before it can leave container 2 via outlet 4 via the gas-liquid mixture that entrance 3 enters container 2
Element 8.
Filter cell 8 is provided with reservoir 9, is collected in the reservoir 9 by the isolated liquid of filter cell 8
In.
In the example shown, reservoir 9 is made into individual reservoir 9, it means that it is point of filter cell 8
From component or separate section.
Individual reservoir 9 is connect using connecting tube 10 with filter cell 8, wherein the connecting tube 10 will be used for by by
The isolated liquid of filter cell 8 is discharged towards reservoir 9.
Discharge pipe 11 leaves the reservoir 9 and leads to outside, and thus the discharge pipe 11 is used for the liquid in reservoir 9
Body is discharged to the outside.
In Fig. 1, reservoir 9 is located in the container 2 of liquid separator 1.
However, be not necessarily such case, Fig. 5 is shown and liquid separator 1 identical in Fig. 1, but reservoir 9
It is arranged in the outside of said vesse 2.
For this purpose, connecting tube 10 is made to longer, and the side wall 12 of container 2 is passed through before entering reservoir 9.Certainly
Connecting tube 10 is not excluded for across lid 7 or the base portion by container 2.
The operation of liquid separator 1 is very simple, and as described below.
Gas-liquid mixture for being handled enters the container 2 of liquid separator 1 via entrance 3.
Entrance is arranged at tangent position, so that gas-liquid mixture follows the track of whirlwind shape in container 2.Centrifugation
Power causes to occur to separate for the first time, because heavier liquid particles are thrown to the inside of the side wall 12 of container 2 and are collected in
It the bottom of container 2 and is removed.
Then, gas-liquid mixture passes through filter cell 8.Here further separation phase will occur.
Isolated liquid particles will flow down over filter cell 8, and will will finally be collected in via connecting tube 10
In reservoir 9.
Liquid can be transported from reservoir 9 via discharge pipe 11 to another position.
Nozzle 13 in discharge pipe 11 can limit the maximum emission of liquid, make it possible to achieve more stable liquid row
It puts.
The liquid separator 1 being not excluded in Fig. 1 is provided with separator, and the separator extends from lid 7 and around filtering
Device element 8 extends.
In other words, separator is located in the region between the side wall 12 and filter cell 8 of container 2.
The separator combines the space between the side wall 12 and separator of container 2 with the entrance being arranged at tangency location
In cause cyclonic separation.
Tubulose can be made in separator.
Fig. 2 shows liquid separators according to the present utility model.
Liquid separator 1 in Fig. 2 is provided with separator 20, and the separator 20 surrounds above-mentioned outlet 4 from aforementioned lid 7
Extend, and including the base wall 21 with entrance opening 22, middle chamber 23 is limited by separator 20, base wall 21 and lid 7
Fixed, wherein being attached with above-mentioned filter cell 8 in the chamber 23 being thusly-formed, the filter cell 8 is enclosed from base wall 21
Extend around entrance opening 22, all features above are arranged so as to limit outlet area between separator 20 and filter cell 8
Domain 24, the exit region 24 are connect with said outlet 4.
It note that the liquid separator of type in liquid separator and Fig. 1 to Fig. 4 for type in Fig. 5, gas-liquid is mixed
It closes object and has to pass through filter after entering container 2 via entrance 3 and before it can leave container 2 via outlet 4
Element 8.
In this case, although not necessarily, base wall 21 is provided with multiple entrance openings 22, and in chamber 23
The middle multiple filter cells 8 of setting, all filter cells 8 extend around entrance opening 22.
In the case, there are two filter cells 8, but can also have 3,4,6,8 etc..
In this case, there are a reservoirs 9, wherein all liq quilt isolated by all filter cells 8
It collects in the reservoir 9.
The exact position for taking out liquid is not important for the utility model.
It is also possible that each filter cell 8 is provided with the reservoir 9 of oneself.
Reservoir 9 can be individual reservoir, as shown in Figure 2 but it is also possible to be integrated reservoir 9.
Reservoir 9 can be for example integrated in afore-mentioned bottom wall 21.
The operation of liquid separator in Fig. 2 is similar to the operation of the liquid separator in Fig. 1.
Separator 20 will be first about via the gas-liquid mixture that entrance 3 enters container 2 to advance along the track of whirlwind shape.
Thus the first separation phase will occur.
Then, gas-liquid mixture will change direction, so as to flow through filtering via the entrance opening 22 in base wall 21
Device element 8, to eventually enter into exit region 24, to leave container 2 via outlet 4.
Second separation phase occurs during the direction of gas-liquid mixture changes, and third separation phase is in gas-liquid mixed
Generation when filter cell 8 is crossed in logistics.
It will be collected via the connecting tube 10 in reservoir 9 by the isolated liquid of filter cell 8.
Although in all examples being illustrated above, filter cell 8 is located in container 2, this is for the utility model
It is not required.
Fig. 3 and 4 illustrates in greater detail the connection of reservoir 9 and discharge pipe 11 in Fig. 1 and 2.
Reservoir 9 is provided with equipment 14, once liquid level of the equipment 14 in reservoir 9 drops to specified level
Or discharge pipe 11 is shut off when lower than specified level, so that never removing gas in this way.
" closing discharge pipe 11 " is understood to mean that no liquid can leave reservoir 9 via discharge pipe 11.
The form of flap valve or valve can be made in the equipment 14.
However, in the cases of figs. 3 and 4, float 15 is made in these equipment 14, the float 15 can close reservoir 9
In outlet opening 16, be provided with device 17 so that float 15 to be maintained to the position of the top of outlet opening 16.
Float 15 will be swum on relevant liquid, and once liquid level drops to specified level or is lower than specified level
Outlet opening 16 is closed, and therefore closes discharge pipe 11.Once liquid level is more than the level, outlet opening 16 will not be closed.
In Fig. 3, a kind of perforation retainer 18 is made in device 17, and the perforation retainer 18 is attached at outlet opening 16
On, and float 15 is located in the perforation retainer 18.
Obviously, when the liquid level in reservoir 9 rises or falls, float 15 will be correspondingly upper and lower in perforation retainer 18
It is mobile.
Although float 15 is spherical in shape, it is apparent that the utility model is without being limited thereto.
In Fig. 4, a kind of lever arm 19 is made in device 17, and the lever arm 19 is connected with float 15, and and filter
Element 8, base wall 21, separator 20 or reservoir 9 edge in any be connected.
In this case, connection is hinged, but not necessarily so.
Embodiment in Fig. 3 is also equipped with nozzle 13 as shown in figure 1, and the embodiment in Fig. 4 is not provided with the nozzle.
However, this can also be just the opposite.
Furthermore, however not excluded that the embodiment in Fig. 2 is provided with the equipment 14 for closing discharge pipe 11.This equipment 14 can
In the form of flap valve or valve is made, or the form (such as shown in Figures 3 and 4) of float 15 is made.
Fig. 5, which shows filter cell 8 according to the present utility model and is arranged in 2 downstream of container of liquid separator 1, to be shown
Example.
In this case, the container 2 in liquid separator 1 occurs for above-mentioned first separation phase and the second separation phase
In, the container 2 is equipped with such as the separator 20 in Fig. 5.
Gas-liquid mixture will leave container 2 via outlet 4, and be guided towards filter cell 8.
Similar with Fig. 1 and Fig. 2, which is provided with individual reservoir 9, collects in the reservoir 9
Isolated liquid.This is closely similar with previously described embodiment.
As shown in figure 5, reservoir 9 can be located at the outside of said vesse.
In addition, nozzle 13 is not present in discharge pipe 11.However, it is not excluded that discharge pipe 11 is provided with this nozzle 13.
In terms of other, the operation of the liquid separator in Fig. 5 is identical as the operation of the liquid separator in Fig. 2.
It being not precluded, reservoir 9 is provided with equipment 14, once liquid level of the equipment 14 in reservoir 9 drops to
Specified level is shut off discharge pipe 11 lower than specified level.
As shown in Figure 3 and Figure 4, reservoir is also provided with float 15.
The utility model is never limited to the embodiment for describing and being shown in the accompanying drawings as example, but can be with various shapes
Formula and size realize liquid separator according to the present utility model without departing from the scope of the utility model.
Claims (9)
1. a kind of liquid separator, the liquid separator has container (2), and the container has entering for gas-liquid mixture
Mouthful (3) and outlet (4) for gas of transporting that treated,
Wherein, the container (2) limits space (5),
Wherein, filter cell (8) is arranged so that gas-liquid mixture is entering appearance via entrance (3) in the space (5)
Filter cell (8) are had to pass through after device (2) and before it can leave container (2) via outlet (4),
Wherein, the filter cell (8) is provided with reservoir (9), is collected by the liquid that the filter cell (8) separate
In the reservoir,
Wherein, discharge pipe (11) is attached to the reservoir (9), and collection can be discharged in the reservoir (9) in the discharge pipe
In liquid, and
Wherein, the reservoir (9) is provided with equipment (14), and liquid level of the equipment once in the reservoir (9) drops to
Specified level is shut off the discharge pipe (11) lower than specified level,
It is characterized in that, the liquid separator (1) is provided with separator (20), the separator is from the container (2)
Side wall (12) extends around above-mentioned outlet (4), and including the base wall (21) with entrance opening (22),
Wherein, chamber (23) by the separator (20), the base wall (21) and the container (2) the side wall (12)
A part limits,
Wherein, it is attached with above-mentioned filter cell (8) in the chamber (23) being thusly-formed, the filter cell is from institute
Base wall (21) are stated to extend around the entrance opening (22), and features above be arranged so that in the separator (20) and
Exit region (24) are limited between the filter cell (8), the exit region is connect with said outlet (4).
2. liquid separator according to claim 1, which is characterized in that flap valve or valve is made in aforementioned device (14).
3. liquid separator according to claim 1, which is characterized in that the equipment (14) is made float (15), described
Float can close the outlet opening (16) in the reservoir (9), be provided with device (17) to protect the float (15)
Hold the position above the outlet opening (16).
4. the liquid separator according to any one of preceding claims 1 to 3, which is characterized in that reservoir (9) system
At individual reservoir (9), the reservoir is connect using connecting tube (10) with the filter cell (8).
5. the liquid separator according to any one of preceding claims 1 to 3, which is characterized in that reservoir (9) collection
At in the filter cell (8) or forming a part of the filter cell.
6. the liquid separator according to any one of preceding claims 1 to 3, which is characterized in that the discharge pipe (11)
It is provided with the nozzle (13) positioned at the reservoir (9) downstream.
7. the liquid separator according to any one of preceding claims 1 to 3, which is characterized in that reservoir (9) position
In the inside of aforesaid receptacle (2).
8. the liquid separator according to any one of preceding claims 1 to 3, which is characterized in that reservoir (9) position
In the outside of aforesaid receptacle (2).
9. the liquid separator according to any one of preceding claims 1 to 3, which is characterized in that the base wall (21)
It is provided with multiple entrance openings (22), and is provided with multiple filter cells (8) in the chamber (23), each mistake
Filter element surrounds the entrance opening (22) extension.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| BE2017/5510A BE1025405B1 (en) | 2017-07-18 | 2017-07-18 | FILTER ELEMENT AND LIQUID SEPARATOR WITH SUCH FILTER ELEMENT |
| BEBE2017/5510 | 2017-07-18 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208839267U true CN208839267U (en) | 2019-05-10 |
Family
ID=59569089
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810786948.2A Active CN109260872B (en) | 2017-07-18 | 2018-07-18 | Liquid separator |
| CN201821137802.7U Active CN208839267U (en) | 2017-07-18 | 2018-07-18 | Liquid separator |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810786948.2A Active CN109260872B (en) | 2017-07-18 | 2018-07-18 | Liquid separator |
Country Status (3)
| Country | Link |
|---|---|
| CN (2) | CN109260872B (en) |
| BE (1) | BE1025405B1 (en) |
| WO (1) | WO2019016651A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109260872A (en) * | 2017-07-18 | 2019-01-25 | 阿特拉斯·科普柯空气动力股份有限公司 | Liquid separator |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114901380A (en) * | 2019-10-28 | 2022-08-12 | 悦马塑料技术有限公司 | Liquid separator |
Family Cites Families (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3217162A1 (en) * | 1982-05-07 | 1983-11-10 | Volkswagenwerk Ag | Device for the removal of water from the fuel system of an internal combustion engine |
| ATE24120T1 (en) * | 1983-04-08 | 1986-12-15 | Cash Eng Co Pty Ltd | FLOODED COMPRESSOR SEPARATORS. |
| DE3906550A1 (en) * | 1989-03-02 | 1990-09-06 | Bosch Gmbh Robert | LIQUID FILTER |
| JPH1057737A (en) * | 1996-08-20 | 1998-03-03 | Kawasaki Heavy Ind Ltd | Method for recovering mist contained in gas and device therefor |
| DE10106950A1 (en) * | 2001-02-15 | 2002-09-05 | Bosch Gmbh Robert | Filter element for fuels |
| CN100406098C (en) * | 2002-12-06 | 2008-07-30 | 唐纳森公司 | Inlet baffle arrangement for gas/liquid separation, apparatus, and methods |
| WO2006078787A2 (en) * | 2005-01-19 | 2006-07-27 | Donaldson Company, Inc. | Inlet baffle arrangement with perforated vortex finder for gas/ liquid separation |
| BE1018543A3 (en) * | 2009-04-27 | 2011-03-01 | Atlas Copco Airpower Nv | LIQUID SEPARATOR. |
| BR112017008882B1 (en) * | 2014-10-29 | 2021-12-28 | Atlas Copco Airpower, Naamloze Vennootschap | OIL SEPARATOR |
| CN105779022B (en) * | 2016-03-10 | 2018-09-18 | 中国神华能源股份有限公司 | Cyclone separator and gas-liquid solid separation system |
| CN206103606U (en) * | 2016-08-31 | 2017-04-19 | 江苏明浩新能源发展有限公司 | Double entry vapour and liquid separator |
| BE1025405B1 (en) * | 2017-07-18 | 2019-02-18 | Atlas Copco Airpower Naamloze Vennootschap | FILTER ELEMENT AND LIQUID SEPARATOR WITH SUCH FILTER ELEMENT |
-
2017
- 2017-07-18 BE BE2017/5510A patent/BE1025405B1/en active IP Right Grant
-
2018
- 2018-07-12 WO PCT/IB2018/055148 patent/WO2019016651A1/en active Application Filing
- 2018-07-18 CN CN201810786948.2A patent/CN109260872B/en active Active
- 2018-07-18 CN CN201821137802.7U patent/CN208839267U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109260872A (en) * | 2017-07-18 | 2019-01-25 | 阿特拉斯·科普柯空气动力股份有限公司 | Liquid separator |
Also Published As
| Publication number | Publication date |
|---|---|
| BE1025405A1 (en) | 2019-02-11 |
| CN109260872B (en) | 2022-03-15 |
| WO2019016651A1 (en) | 2019-01-24 |
| BE1025405B1 (en) | 2019-02-18 |
| CN109260872A (en) | 2019-01-25 |
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