CN208927828U - A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator - Google Patents
A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator Download PDFInfo
- Publication number
- CN208927828U CN208927828U CN201821685622.2U CN201821685622U CN208927828U CN 208927828 U CN208927828 U CN 208927828U CN 201821685622 U CN201821685622 U CN 201821685622U CN 208927828 U CN208927828 U CN 208927828U
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid separation
- membrane module
- separation element
- gas liquid
- 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.)
- Active
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides a kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator, is related to gas and liquid separation technology field.The gas liquid separation element includes supporting layer and membrane module, and membrane module is installed on supporting layer, and supporting layer is set as mesh form, and membrane module includes lyophoby microporous film layers.Gas liquid separation element, gas-liquid separation component and gas-liquid separator provided by the utility model have separation accuracy higher, efficiency also higher advantage.
Description
Technical field
The utility model relates to gas and liquid separation technology fields, in particular to a kind of gas liquid separation element, gas-liquid separation
Component and gas-liquid separator.
Background technique
With the development of industry, people increasingly pay attention to the recycling of utility, with the improvement of living standards,
People are more and more deep to the understanding of environmental protection, therefore for recycling with the resolution element of environmental protection close in industrial production
Obtain within several years the development of high speed.
In the industrial production, many fields need to separate gas with liquid, such as petroleum product field or coal system
Product field etc..Currently, conventional gas-liquid separation mode includes cyclonic separation mode, silk screen mist eliminating mode and fibre conglomerates separation
Mode.Wherein, the liquid that cyclonic separation mode keeps density big using the centrifugal force of gas-liquid rotational flow constantly collides whirlwind point
Separation is realized on bucket wall from device, silk screen mist eliminating mode forms retention using droplet collision contact silk screen and realizes separation, and fiber is poly-
Knot mode is realized the effects of absorption of fine droplet, collision, aggregation using fiber and is separated.But currently used gas-liquid point
It is not high all to there is separation accuracy from mode, the lower problem of filter efficiency.
It is the emphasis of those skilled in the art's concern in view of this, how to solve the above problems.
Utility model content
The purpose of this utility model is to provide a kind of gas liquid separation elements, to solve point of gas-liquid separation in the prior art
It is not high from precision, the lower problem of filter efficiency.
The another object of the utility model is to provide a kind of gas-liquid separation component, to solve gas-liquid separation in the prior art
Separation accuracy it is not high, the lower problem of filter efficiency.
The another object of the utility model is to provide a kind of gas-liquid separator, to solve gas-liquid separation in the prior art
Precision is not high, the lower problem of filter efficiency.
The utility model is realized in this way:
In a first aspect, the utility model embodiment provides a kind of gas liquid separation element, the gas liquid separation element includes
Supporting layer and membrane module, the membrane module are installed on the supporting layer, and the supporting layer is set as mesh form, and the film group
Part includes lyophoby microporous film layers.
Further, the membrane module further includes nonwoven layer, and the lyophoby microporous film layers and the non-woven fabrics level connect
It connects.
Further, the lyophoby microporous film layers include hydrophobic film layer or hydrophobic oleophobic film layer.
Further, the gas liquid separation element further includes membrane module protective layer, the membrane module protective layer and the film
The side far from the supporting layer of component connects.
Further, the shape of the membrane module includes V-type rugosity or L-type rugosity.
Further, the gas liquid separation element further includes fixing layer, the rugosity of the fixing layer and the membrane module
End connection, with the fixation membrane module.
Further, the supporting layer is set as annular, and the membrane module is in the outside of the supporting layer.
Further, the gas liquid separation element further includes sealing ring and capping, and the sealing ring is installed on the support
One end of layer and the membrane module, and the supporting layer, the membrane module are connected by the sealing ring and the capping.
Second aspect, the utility model embodiment additionally provide a kind of gas-liquid separation component, the gas-liquid separation component packet
At least two gas liquid separation elements are included, the gas liquid separation element includes supporting layer and membrane module, and the membrane module is installed on institute
Supporting layer is stated, the supporting layer is set as mesh form, and the membrane module includes lyophoby microporous film layers, at least two gas
Liquid resolution element concatenation is in parallel, and at least two gas liquid separation element connects two-by-two.
The third aspect, the utility model embodiment additionally provide a kind of gas-liquid separator, and the gas-liquid separator includes extremely
A few gas liquid separation element, the gas liquid separation element includes supporting layer and membrane module, and the membrane module is installed on the branch
Layer is supportted, the supporting layer is set as mesh form, and the membrane module includes lyophoby microporous film layers.
Compared with the prior art, the utility model has the following beneficial effects:
The utility model provides a kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator, the gas-liquid point
It include on the outside of supporting layer and membrane module from element, membrane module is installed on supporting layer, and supporting layer is set as mesh form, and membrane module
Including lyophoby microporous film layers.On the one hand, gas is carried out by membrane module since gas liquid separation element provided by the utility model uses
The separation of body and liquid, so precision is higher during separation, efficiency is also higher, on the other hand, using supporting layer to film
Component is supported, so the deformation or damage of membrane module is not easily caused during separating to gas with liquid, from
Precision and efficiency without influencing the gas liquid separation element in use.Also, since supporting layer is set as mesh shape
Shape has separated the gas of liquid and has flowed out from supporting layer mesh, and the liquid being separated then along the surface of film layer from top to bottom
Film layer is left in flowing or rolling, so that entire separation process is more smooth, processing capacity is high.
To enable the above objects, features, and advantages of the utility model to be clearer and more comprehensible, preferred embodiment is cited below particularly, and
Cooperate appended attached drawing, is described in detail below.
Detailed description of the invention
It is practical new below in conjunction with this to keep the objectives, technical solutions, and advantages of the embodiments of the present invention clearer
Attached drawing in type embodiment, the technical scheme in the utility model embodiment is clearly and completely described, it is clear that is retouched
The embodiment stated is the utility model a part of the embodiment, instead of all the embodiments.Usually here in attached drawing description and
The component of the utility model embodiment shown can be arranged and be designed with a variety of different configurations.Therefore, below to attached
The detailed description of the embodiments of the present invention provided in figure is not intended to limit the range of claimed invention,
But it is merely representative of the selected embodiment of the utility model.Based on the embodiments of the present invention, ordinary skill people
Member's every other embodiment obtained without creative efforts, belongs to the model of the utility model protection
It encloses.
Fig. 1 shows the schematic cross-section of membrane module and supporting layer provided by the utility model embodiment.
Fig. 2 shows the structural schematic diagrams of gas liquid separation element provided by the utility model embodiment.
Fig. 3 shows a kind of folded form schematic diagram of membrane module provided by the utility model embodiment.
Fig. 4 shows another folded form schematic diagram of membrane module provided by the utility model embodiment.
Fig. 5 shows the connection schematic diagram of membrane module and fixing layer provided by the utility model embodiment.
Fig. 6 shows the structural schematic diagram of gas-liquid separation component provided by the utility model embodiment.
Icon: 100- gas liquid separation element；110- membrane module；111- lyophoby microporous film layers；112- nonwoven layer；120- branch
Support layer；130- sealing ring；140- capping；150- fixing layer；160- membrane module protective layer；200- gas-liquid separation component.
Specific embodiment
Below in conjunction with attached drawing in the utility model embodiment, the technical scheme in the embodiment of the utility model is carried out clear
Chu is fully described by, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole realities
Apply example.The component of the utility model embodiment being usually described and illustrated herein in the accompanying drawings can be come with a variety of different configurations
Arrangement and design.Therefore, the detailed description of the embodiments of the present invention provided in the accompanying drawings is not intended to limit below
The range of claimed invention, but it is merely representative of the selected embodiment of the utility model.Based on the utility model
Embodiment, those skilled in the art's every other embodiment obtained without making creative work, all
Belong to the range of the utility model protection.
In the description of the present invention, it should also be noted that, unless otherwise clearly defined and limited, term " is set
Set ", " installation ", " connected ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection,
Or it is integrally connected；It can be mechanical connection, be also possible to be electrically connected；It can be directly connected, intermediary can also be passed through
It is indirectly connected, can be the connection inside two elements.For the ordinary skill in the art, it can be managed with concrete condition
Solve the concrete meaning of above-mentioned term in the present invention.
It should also be noted that similar label and letter indicate similar terms in following attached drawing, therefore, once a certain Xiang Yi
It is defined in a attached drawing, does not then need that it is further defined and explained in subsequent attached drawing.
With reference to the accompanying drawing, it elaborates to some embodiments of the utility model.In the absence of conflict, under
The feature in embodiment and embodiment stated can be combined with each other.
First embodiment
Referring to Fig. 1, the utility model embodiment provides a kind of gas liquid separation element 100, the gas liquid separation element 100
Including supporting layer 120, membrane module 110 and membrane module protective layer 160, membrane module 110 is installed on 120 outside of supporting layer, passes through
The supporting layer 120 and membrane module 110 realize the separation to liquid and gas.
Specifically, in the present embodiment, membrane module 110 includes nonwoven layer 112 and lyophoby microporous film layers 111, and lyophoby
Microporous film layers 111 are connect with 112 face of nonwoven layer.Also, lyophoby microporous film layers 111 are a kind of film with lyophoby property, with
Need liquid to be separated that there is height not affinity, i.e., liquid can not pass through the film, but gas can pass through.It is micro- by lyophoby
Hole film layer 111 carries out the separation of liquid and gas, and precision is higher and filter efficiency is also higher, also more extensive using object.
In the present embodiment, lyophoby microporous film layers 111 include hydrophobic film layer or hydrophobic oleophobic film layer, and hydrophobic film layer is for dividing
From water or aqueous solution class I liquid I, hydrophobic oleophobic film then can both separate water or aqueous solution class I liquid I, can also be with Separation of Organic
Class I liquid I separates different organic solvent liquids according to the oleophobic grade and type of hydrophobic oleophobic film layer.
Further, the present embodiment selects hydrophobic oleophobic film layer, also, the present embodiment preferably has hydrophobic oleophobic feature
Microporous teflon membran, further, the present embodiment be preferably to organic solvent have tumbling property feature hydrophobic oleophobic
Microporous teflon membran.It should be noted that micropore described in the present embodiment refers to the hole less than or equal to 20.0 μm, for example,
The aperture of microporous teflon membran can choose 0.05,0.10,0.22,0.45,1.0,3.0,5.0 μm etc. according to requirements
Plurality of specifications, the corresponding retention precision to drop is 0.001,0.005,0.01,0.05,0.1,0.3,0.5 μm, corresponding
99.9999% is more than or equal to the retention efficiency of drop.Of course, in some other embodiments, polytetrafluoroethylene (PTFE) micropore
The aperture of film may be alternatively provided as other values, and the present embodiment does not do any restriction to this.
It should be noted that in the present embodiment, separated gas is generally air, and of course, different industrial circles
Gas composition is different, for example, further include elementary gas (hydrogen, oxygen, nitrogen etc.), petroleum product class gas (hydrocarbon, alcohol, oil etc.),
Coal product class gas (carbon monoxide, carbon dioxide etc.), industrial tail gas (petrochemical industry, pharmaceuticals industry, cleaning industry).
Also, in the present embodiment, since lyophoby microporous film layers 111 are relatively thin, so its intensity is smaller, in order to realize
Support the lyophoby microporous film layers 111, membrane module 110 provided in this embodiment includes non-woven fabrics, with increase filter layer intensity and
Convenient for post-processing.And in the present embodiment, non-woven fabrics includes polyester, polypropylene, polyimides, polyphenylene sulfide, polytetrafluoroethylene (PTFE)
Equal high molecular materials non-woven fabrics.It should be noted that non-woven fabrics plays the role of supporting lyophoby microporous film layers 111, make lyophoby
Microporous film layers 111 become tough, very scrape, and have more practicability.
Also, in order to further play the role of support, gas liquid separation element 100 is provided with supporting layer 120, supporting layer
120 are set as mesh form.Supporting layer 120 can play the role of support to membrane module 110, to overcome air-flow in separation process
To the pressure difference active force that membrane module 110 generates, to greatly improve the practicability and service life of resolution element.Also, liquid
Body (fine droplet) can reside on film surface after the obstruction by lyophoby microporous film layers 111, and subsequent fine droplet merges aggregation
It is tumbled under the effect of gravity from film surface to the lower end of resolution element at big drop, big drop, to realize gas and liquid
Separation.
It should also be noted that, there is aging in use in supporting layer 120 in order to prevent, so in the present embodiment
120 material of supporting layer uses stainless steel.
Further, in the present embodiment, referring to Fig. 2, supporting layer 120 is set as annular, membrane module 110 is in supporting layer
120 outside sets a cylindrical shape for entire supporting layer 120, enable gas and liquid simultaneously along supporting layer 120 from film
Surrounding input outside component protection layer 160, then gas, liquid are contacted with lyophoby microporous film layers 111, and gas passes through film and branch
It supports layer 120 to flow out from the center of resolution element, and the detention of liquid envelope and flows from above to below or roll along film layer and leave
Film layer is flowed out from the mesh of membrane module protective layer 160, the separation of gas and liquid is realized, so that separation in actual use
It is more efficient.Of course, in some other embodiments, supporting layer 120 can also be other shapes, for example, an arcuate structure
Or a planar structure, the present embodiment do not do any restriction to this.It should be noted that in the present embodiment, a is indicated without dividing
From gas and liquid flow direction, b indicate separation after liquid flow direction, c indicate separation after gas flow direction.
Further, in order to enable gas to be after isolation easier to be controlled, in the present embodiment, gas-liquid separation group
Part 200 further includes sealing ring 130 and capping 140, and sealing ring 130 is installed on one end of supporting layer 120, and supporting layer 120 passes through
Sealing ring 130 is connect with capping 140.After will cover 140 and cover tightly, gas can not be flowed along the end, and only towards supporting layer
It flows in the direction of 120 other end.
It should be noted that gas liquid separation element 100 provided in this embodiment can be made to become by setting capping 140
Independent completed element is used alone, but it is also possible to which processing number is continuously improved by the in parallel of same precision filter element
Amount, the concatenation by concatenating especially different filtering accuracy elements are continuously improved processing accuracy, pass through same precision filter element
The concatenation of in parallel and different filtering accuracy elements forms the processing system of optimization.Identical or different lyophoby can be used by multiple
The gas liquid separation element 100 of microporous film layers 111 carries out in parallel or concatenation, so that the effect of gas-liquid separation is more preferable.Also, work as
When needing to be concatenated multiple gas liquid separation elements 100, the capping 140 of one of gas liquid separation element 100 need to only be torn open
It is lower, it is easy to operate.
It should also be noted that, in the present embodiment, it, need to be by film when membrane module 110 and supporting layer 120 to be attached
Component 110 is folded.In a first aspect, the area of the film of hydrophobic film layer can be increased by way of folding, be conducive to improve
The efficiency of gas-liquid separation component 200.Second aspect carries out membrane module 110 to fold the use intensity that can also improve film, even if
Film is changed as solid shape from plane configuration, so that the use intensity of film be made to increase.The third aspect carries out membrane module 110
The angle that can also change Liquid Flow direction and membrane plane is folded, by reducing the angle in Liquid Flow direction and membrane plane, is subtracted
The blocking possibility of few film, so that the anticlogging performance enhancement of membrane module 110 in use.
Further, refering to Fig. 3 and Fig. 4, in the present embodiment, the folded form of membrane module 110 is V-type rugosity or L
Type rugosity, wherein V-type rugosity is suitble to such as 40mm or less small size fold height, and L-type rugosity is suitble to such as 40mm or more
Large scale fold height.By using film folded form, make separated contact surfaces product of the gas liquid separation element 100 in unit volume
Loading close to maximum value, further, since film is to big by separation liquid repulsive force, liquid is on film surface in rolling shape
State, therefore the separative efficiency of gas liquid separation element 100 greatly improves under ad eundem.
It should be noted that referring to Fig. 5, the opening size of the folding in order to guarantee membrane module 110 is uniformly arranged,
In the present embodiment, liquid resolution element further includes fixing layer 150, and fixing layer 150 and the end of the rugosity of membrane module 110 connect
It connects, to fix membrane module 110.Further, the present embodiment uses thermoset elastic binder (such as polyurethane) by fixing layer 150
It is fixed with membrane module 110 according to the size of space of regulation.
It should also be noted that, in the present embodiment, the foldable number that membrane module 110 is folded is according to supporting layer
The diameter of 120 cylinders surrounded determines that the broken number optimized if diameter is 350mm is 102 foldings.
To sum up, the working principle of gas liquid separation element provided in this embodiment is such that separate in gas and liquid
Cheng Zhong, gas passes through membrane module under the promotion of pressure, and liquid can then reside on film surface, and subsequent fine droplet merges aggregation
It is tumbled under the effect of gravity from film surface to the lower end of resolution element at big drop, big drop, to realize gas and liquid
Separation.
Second embodiment
Referring to Fig. 6, the utility model embodiment additionally provides a kind of gas-liquid separation component 200, the gas-liquid separation component
200 include at least two gas liquid separation elements 100 as in the first embodiment, at least two gas liquid separation element 100 string
Parallel connection is connect, and at least two gas liquid separation elements 100 connect two-by-two.
It should be noted that the performance of the membrane module 110 of at least two gas liquid separation element 100 is identical.Also,
Concatenation described in the present embodiment is to connect one end of two neighboring gas liquid separation element 100, to make entire gas-liquid separation group
The length of part 200 increases, and its essence is one kind to be connected in parallel form for such tandem, to increase the effect of gas-liquid separation
Energy.
Further, gas-liquid separation component 200 described in the present embodiment can be using simultaneously when handling biggish gas-liquid quantity
The mode of connection installation improves the processing capacity of separator, such as 3,5,7,9 or more gas-liquid separation components 200 are connected in parallel on one
It rises, is formed by processing capacity and is improved in proportion with the increase of quantity.It on the other hand, can will not in order to improve the efficiency of separation
Separation assembly with separation accuracy is together in series, for example, the first order use retention precision for 0.5 μm, retention efficiency be 99.9%
Separation assembly, the second level use retention precision for 0.005 μm, retention efficiency be 99.9999% separation assembly, such two fraction
Combination from component had not only improved the efficiency of separation but also had shared isolated load, kept entire separation process more reliable, more economical.
3rd embodiment
The utility model embodiment additionally provides a kind of gas-liquid separator, which includes at least one such as first
Gas liquid separation element 100 described in embodiment.It simultaneously include the metal with necessary inlet and outlet, control instrument and pipeline valve
Shell.Further, metal shell requires to need to design for isolated object, quantity, result.
In conclusion the utility model provides a kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator,
The gas liquid separation element includes on the outside of supporting layer and membrane module, and membrane module is installed on supporting layer, and supporting layer is set as mesh form,
And membrane module includes lyophoby microporous film layers.On the one hand, pass through film group since gas liquid separation element provided by the utility model uses
Part carries out the separation of gas and liquid, so precision is higher during separation, efficiency is also higher, on the other hand, utilizes branch
Support layer is supported membrane module, so not easily causing the deformation of membrane module during separating to gas with liquid
Or damage, so that the precision and efficiency of the gas liquid separation element will not be influenced in use.Also, since supporting layer is arranged
For mesh form, the gas for having separated liquid is flowed out from supporting layer mesh, and the liquid being separated is then along the surface of film layer
It flows from above to below or rolls and leave film layer, so that entire separation process is more smooth, processing capacity is high.
In the description of the present invention, it should be noted that term " first ", " second ", " third " etc. are only used for area
Divide description, is not understood to indicate or imply relative importance.The above is only the preferred embodiment of the present invention and
, be not intended to limit the utility model, for those skilled in the art, the utility model can have it is various change and
Variation.Within the spirit and principle of the utility model, any modification, equivalent substitution, improvement and etc. done, should be included in
Within the protection scope of the utility model.
Claims (10)
1. a kind of gas liquid separation element, which is characterized in that the gas liquid separation element includes supporting layer and membrane module, the film group
Part is installed on the supporting layer, and the supporting layer is set as mesh form, and the membrane module includes lyophoby microporous film layers.
2. gas liquid separation element as described in claim 1, which is characterized in that the membrane module further includes nonwoven layer, described
Lyophoby microporous film layers are connect with the non-woven fabrics level.
3. gas liquid separation element as claimed in claim 2, which is characterized in that the lyophoby microporous film layers include hydrophobic film layer or
Hydrophobic oleophobic film layer.
4. gas liquid separation element as described in claim 1, which is characterized in that the gas liquid separation element further includes that membrane module is protected
Sheath, the membrane module protective layer are connect with the side far from the supporting layer of the membrane module.
5. gas liquid separation element as described in claim 1, which is characterized in that the shape of the membrane module includes V-type rugosity
Or L-type rugosity.
6. gas liquid separation element as claimed in claim 5, which is characterized in that the gas liquid separation element further includes fixing layer,
The fixing layer is connect with the end of the rugosity of the membrane module, with the fixation membrane module.
7. gas liquid separation element as described in claim 1, which is characterized in that the supporting layer is set as annular, the film group
Part is in the outside of the supporting layer.
8. gas liquid separation element as claimed in claim 7, which is characterized in that the gas liquid separation element further include sealing ring with
Capping, the sealing ring is installed on one end of the supporting layer, and the supporting layer is connected by the sealing ring and the capping
It connects.
9. a kind of gas-liquid separation component, which is characterized in that the gas-liquid separation component includes at least two such as claims 1 to 8
Gas liquid separation element described in any one, at least two gas liquid separation elements concatenation or in parallel, and described at least two
Gas liquid separation element connects two-by-two.
10. a kind of gas-liquid separator, which is characterized in that the gas-liquid separator includes at least one as claim 1 to 8 is any
Gas liquid separation element described in one.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821685622.2U CN208927828U (en) | 2018-10-17 | 2018-10-17 | A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821685622.2U CN208927828U (en) | 2018-10-17 | 2018-10-17 | A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208927828U true CN208927828U (en) | 2019-06-04 |
Family
ID=66724946
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821685622.2U Active CN208927828U (en) | 2018-10-17 | 2018-10-17 | A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208927828U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109126323A (en) * | 2018-10-17 | 2019-01-04 | 苏州名列膜材料有限公司 | A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator |
| CN114644949A (en) * | 2020-12-18 | 2022-06-21 | 中国石油化工股份有限公司 | Natural gas liquid removal equipment and using method thereof |
-
2018
- 2018-10-17 CN CN201821685622.2U patent/CN208927828U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109126323A (en) * | 2018-10-17 | 2019-01-04 | 苏州名列膜材料有限公司 | A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator |
| CN114644949A (en) * | 2020-12-18 | 2022-06-21 | 中国石油化工股份有限公司 | Natural gas liquid removal equipment and using method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Ni et al. | Optimizing geometric parameters in hydrocyclones for enhanced separations: a review and perspective | |
| CN208927828U (en) | A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator | |
| US5454945A (en) | Conical coalescing filter and assembly | |
| US5750024A (en) | Conical coalescing filter | |
| CN109126323A (en) | A kind of gas liquid separation element, gas-liquid separation component and gas-liquid separator | |
| CN109758850B (en) | Gas-liquid coalescent filter element with preseparation function | |
| GB2177019A (en) | Removing liquid aerosols from gases | |
| AU2006236003A1 (en) | A Second-Stage Separator Device for a Vaccuum Cleaner | |
| US3347026A (en) | Fluid separator | |
| RU2013102593A (en) | TWO-STAGE WATER SEPARATOR FOR FUEL AND FILTER FOR SEPARATION OF SOLID PARTICLES | |
| US20180369731A1 (en) | Compact axial flow separator | |
| US20150122720A1 (en) | Water Separating Device, Filter Element of a Fuel Filter and a Fuel Filter | |
| AU665211B2 (en) | Conical coalescing filter | |
| US20130312609A1 (en) | Apparatus and methods for filtration of solid particles and separation of liquid droplets and liquid aerosols from a gas stream | |
| CA2317891A1 (en) | Liquid filter with centrifugal separator | |
| US3519560A (en) | Method and apparatus for removing water from fluids | |
| JP3510250B2 (en) | Conical adsorption filter | |
| JP3747433B2 (en) | Multiple centrifuge for airborne dust control | |
| US20230012037A1 (en) | Apparatus and method for dry cleaning of polluted flue gases | |
| CN203754654U (en) | Diesel or gasoline dehydrator based on micro-nano fiber membrane | |
| CN101732930B (en) | Corrugated plate separating element | |
| US8663353B2 (en) | Selective gas filter | |
| Talavera | Selecting gas/liquid separators | |
| CN106178612A (en) | The polymerization of fine particle that a kind of is carried by medium fluid the device separated with former medium fluid, system and method | |
| CN106964227B (en) | The purification separation device of droplet and particle in a kind of gas |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |