EP3325124A1 - Dispositif de séparation de l'eau et de l'huile par application d'air comprimé - Google Patents

Dispositif de séparation de l'eau et de l'huile par application d'air comprimé

Info

Publication number
EP3325124A1
EP3325124A1 EP16766488.7A EP16766488A EP3325124A1 EP 3325124 A1 EP3325124 A1 EP 3325124A1 EP 16766488 A EP16766488 A EP 16766488A EP 3325124 A1 EP3325124 A1 EP 3325124A1
Authority
EP
European Patent Office
Prior art keywords
oil
chamber
water
control air
mixture
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.)
Pending
Application number
EP16766488.7A
Other languages
German (de)
English (en)
Inventor
Herbert Schlensker
Johannes Sinstedten
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Beko Technologies GmbH
Original Assignee
Beko Technologies GmbH
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Beko Technologies GmbH filed Critical Beko Technologies GmbH
Publication of EP3325124A1 publication Critical patent/EP3325124A1/fr
Pending legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/0202—Separation of non-miscible liquids by ab- or adsorption
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/0208—Separation of non-miscible liquids by sedimentation
    • B01D17/0214—Separation of non-miscible liquids by sedimentation with removal of one of the phases
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/02—Separation of non-miscible liquids
    • B01D17/0208—Separation of non-miscible liquids by sedimentation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/08—Thickening liquid suspensions by filtration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B01D17/12—Auxiliary equipment particularly adapted for use with liquid-separating apparatus, e.g. control circuits
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00—Nature of the contaminant
    • C02F2101/30—Organic compounds
    • C02F2101/32—Hydrocarbons, e.g. oil
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2209/00—Controlling or monitoring parameters in water treatment
    • C02F2209/42—Liquid level

Definitions

  • the invention relates to an oil / water separation device for removing oily constituents from an oil / water mixture, comprising a main filter, which is used for separating oil-containing constituents from the oil / water mixture
  • Compressed air compressors used. Compressed air compressors generate compressed air by sucking in and compressing ambient air. The humidity contained in the ambient air falls due to physical reasons and by drying the compressed air as condensate. This condensate is an oil / water mixture is a wastewater, which is mostly due to the entry of lubricants of the
  • Operation of the compressor can count.
  • the bond between water and lubricant is different, ranging from a mixture of oil and water on a dispersion to an emulsion.
  • admissible values for discharge into the waste water channel are of the order of 10-20 mg / l, sometimes even 5 mg / l (oil / condensate).
  • the result is a hazardous waste to be disposed of by waste disposal companies, although more than 99.5% is water from the humidity of the ambient air.
  • Impurities density greater than 1 kg / dm 3
  • free oil fractions density less than 1 kg / dm 3
  • These oil fractions then flow to a collecting container.
  • fine oil droplets are separated from the condensate by an adsorption filter, the adsorption filters often being based on an oleophilic material and activated carbon having a very large internal surface area.
  • an oil / water separator In another embodiment of an oil / water separator, the condensate, together with the free oil fractions, is passed through an adsorption filter, which in turn floats on the condensate surface and which absorbs settling oil fractions (density greater than 1 kg / dm 3 ).
  • an oil / water separator is known, for example, from DE 10 2006 009 542 A1. The construction of this oil / water separator works on the principle of the corresponding water columns, with the extent to which new condensate flows, treated condensate on the apparatus
  • the collected free oils and oil-saturated filters are usually supplied for thermal utilization, but they can also be processed.
  • Highly dispersed or even emulsified condensates are not treatable in these apparatuses and are usually processed by more elaborate methods, e.g. by membrane, evaporation or cleavage method.
  • WO 201 1/104 368 A1 proposes a mechanical separation device for Separation of mucilaginous substances and provide an electric pump, which sucks the condensate through the filter and thus overcomes the flow resistance. Operation takes place in the presence of condensate and is controlled by electronic level detection. Basically, the flow through the filter thus takes place only by means of the pump, which brings the advantages mentioned, but is associated with increased energy costs.
  • the object of the invention is therefore to provide an oil / water separator, which can be operated easily and with little energy.
  • Oil / water mixture can act in particular to the condensate of an air compressor.
  • the device is also suitable for the preparation of similar oil / water mixtures, the terms "oil / water mixture” and “condensate” are used only to describe the invention synonymous.
  • the oil / water separator has a control unit which is adapted to temporarily perform an admission of the oil / water separator with control air through which oil / water mixture can be pressed by means of overpressure through the main filter. If necessary, such a pressurization can be done to push condensate through the filter. There is a need in particular if the flow resistance of the filter has increased.
  • the invention thus provides a device which can be easily operated in a known manner according to the hydrostatic principle in normal operation, but on increasing the flow resistance of the filter is able to overcome this by pressurization and thus to prevent overflow of the apparatus.
  • the device therefore has two modes of operation, between which can be changed.
  • the passage of oil / water mixture through the filter can thus be maintained, even if the flow resistance has increased. This results in longer service life for the separator.
  • This is particularly advantageous if regular maintenance intervals are planned, but a change of the filter elements between the scheduled maintenance appointments should be avoided.
  • the operation of the device can be maintained up to the next maintenance interval.
  • Sensor means for detecting the level of oil / water mixture may be provided in the oil / water separator, which are in communication with the control unit. As the flow resistance of the filter increases, so does the level of condensate in the device.
  • the control unit is then designed to temporarily suspend the application of the oil / water Perform separation device with control air when the sensor means a predetermined level A of oil / water mixture has been detected. This level A represents a maximum level of condensate, if possible not
  • the control unit can assume various evaluation and control functions, and it can also be designed to interact with a user. For example, it may include displays and input means for entering commands.
  • the control unit can also be designed to carry out the admission of the control of the oil / water separation device with control air on the basis of a control command. This can be used in particular in the maintenance of the device to empty a filter when needed. This feature is for example when using interchangeable
  • control unit can also be designed to control the admission of the
  • Shutdown of the control air can flow back condensate and increase the level again until a pressurization is performed again, so that the two modes can also alternate.
  • the working range of the device then lies between levels A and B.
  • the oil / water separator comprises a housing, means for supplying the oil / water mixture in a chamber within this housing and a connection opening for transferring the oil / water mixture from this chamber in the main filter.
  • the control unit is designed to temporarily supply the chamber with control air
  • control air is guided into the chamber within the housing such that the oil / water mixture is forced by means of pressure from the chamber through the connection opening in the main filter.
  • the supply of oil / water mixture is prevented in this chamber.
  • the supply of control air to generate an overpressure in the chamber can be carried out in various ways and with different valves.
  • a supply line for the control air can be provided and means with which other openings of the chamber can be closed in order to be able to build up the overpressure in the chamber above the condensate.
  • Control air inlet for supplying control air in the control air chamber, wherein also a Gemischauslass for discharging the oil / water mixture from the
  • Blend chamber into the chamber within the housing and a control air outlet are provided for discharging the control air from the control air chamber in the chamber of the housing.
  • the mixture inlet of this valve is through
  • control air can be introduced into the chamber of the housing by flowing through the control air chamber into the chamber of the housing.
  • the further inflow of condensate into the chamber of the housing can be prevented by the control air moving the membrane so that it closes the mixture inlet to the membrane valve.
  • the membrane also closes the mixture inlet so that no air can escape through it.
  • the control air outlet of the diaphragm valve preferably has a small opening cross-section than the
  • Control air inlet first builds up pressure quickly within the control air chamber and moves the diaphragm before continuing to build up excess pressure within the chamber of the housing.
  • control air is used with overpressure
  • the overpressure can be suitably selected. Preferably, it is in the order of 0.3-1 bar, but especially at about 0.5 bar. If the oil / water separation device is connected to a compressed air line with a higher pressure, before or even after the supply of the control air to the device, a corresponding
  • Pressure reduction take place. For example, it is possible to reduce the pressure from 7 bar to 0.5 bar or other pressures. An excess pressure of 0.5 bar has been found to be sufficient to overcome typically occurring flow resistances and to push condensate through the filter. An overpressure of this magnitude has the advantage that the oil / water separator so that not as a pressure vessel in terms of
  • the oil / water separation device may comprise, in addition to the basic function of separating oily components in the main filter, further functional elements.
  • the housing of the device has an inlet opening, via which oil / water mixture first into a
  • Pressure relief chamber is feasible within the housing, from which the oil / water mixture is again feasible in the chamber of the housing. From this pressure relief chamber can with the condensate entrained compressed air
  • the lockable valve can be closed, which can also be controlled by the control unit.
  • the pressure relief chamber may be connected to the mixture chamber of the diaphragm valve via the mixture inlet.
  • these free oil components which float on the oil / water mixture in the chamber of the housing, via a collecting discharge from the chamber.
  • the collecting drainage can be connected to a collecting tank. This collection is preferably in the admission of the chamber with control air through the
  • Fig. 1 is a schematic representation of a first embodiment of
  • FIG. 2 is a schematic representation of the oil / water separator according to
  • Fig. 3 at a membrane valve of an oil / water separator at
  • Fig. 4 at a diaphragm valve of an oil / water separator at
  • FIG. 1 first embodiment of a
  • At least the device has a main filter 30, which is designed to prepare oil / water mixture or condensate 1 1 from an air compressor, not shown, by oil-containing components are separated from this condensate. This can be done, for example, by adsorption on a filter material, wherein the main filter 30 preferably comprises a material that can introduce liquids precusively finely dispersed, self-emulsified oils. For example, this oleophilic, melt-spun polymer with distribution-oriented surface compaction and shape, as well as activated carbon in adapted consistency and size for receiving the finest oil droplets and oleophilic, foamed polymer are suitable.
  • the main filter 30 has a housing into which a corresponding adsorption filter material 31 is introduced.
  • the oil / water separator 10 further comprises a control unit 60, with which the functions of the device can be controlled. This can in particular include the evaluation of sensor signals of various detectors, the opening and closing of valves and the detection of periods. Furthermore, the control unit 60 preferably has input means for manually inputting
  • Control unit 60 display means, for example, to display the status of
  • the oil / water separator 10 operates on the hydrostatic principle of the corresponding water columns. This is typically above the
  • Main filter 30, a housing 20 attached which may also be referred to as a head housing due to its arrangement.
  • the housing 20 is connected via a connection opening 23 with the main filter 30.
  • This connection may be fixed, but the main filter 30 may also be at least one interchangeable cartridge filter which is temporarily connected to the housing 20 via an inlet port 32. This can be done in particular via a tight screw connection.
  • condensate can be introduced into the housing 20 via an inlet opening 22.
  • This condensate 1 1 comes in particular from a
  • Compressed air compressor and is to be treated by the oil / water separator 10 by oily components from the condensate 1 1 are removed.
  • the condensate 1 1 flows into the head housing 20 and from there by gravity into the underlying main filter 30.
  • a riser 40 on the treated condensate 1 1 "from the oil / water Separating device 10 can also be connected to outlet pipe 33, so that main filter 30 can be exchanged in total.
  • treated condensate 1 1 leaves "the apparatus at the pure water outlet 42 to the sewer.
  • a collecting outlet 71 may be provided which via a valve 72 in
  • Main filter 30 is supplied, thus takes place a separation of free oil fractions, so that pre-purified condensate 1 1 'reaches the main filter 30.
  • the separation of free oil fractions can also be integrated into a cartridge of the main filter 30.
  • the head housing 20 has in the embodiment of FIG. 1 at least one
  • Chamber 24 in which condensate 1 1 flows and from there the main filter 30 is supplied.
  • This chamber 24 is the main chamber of the head housing 20, which, however, can be supplemented by a second chamber in the form of a
  • Pressure relief chamber 21 In this, the condensate 1 1 is first introduced for a pressure relief.
  • entrained compressed air can be removed from the compressor, said air can escape via an outlet.
  • This relief air outlet 12 can be passed through a filter mat 25 and also be provided with a shut-off valve (not shown).
  • Condensate level within the chamber 24 sets in the steadily free oil fractions 13th discharged and purified condensate 1 1 "via the riser 40 are discharged into a sewer.
  • the flow resistance of the filter 30 may increase. If this takes place, the condensate level within the chamber 24 increases, which can lead to overflow of the device. Furthermore, not only free oil fractions flow into the collecting container 70 at elevated condensate level, but also unpurified condensate.
  • the invention therefore provides that the normal operation of the device 10 is supplemented by a pressure operation in which the condensate 1 1 'can be pressed by an overpressure through the main filter 30, as shown in FIG. This is preferably done by acting on the chamber 24 with control air 14 via a control air line 63.
  • a pressure operation in which the condensate 1 1 'can be pressed by an overpressure through the main filter 30, as shown in FIG.
  • This is preferably done by acting on the chamber 24 with control air 14 via a control air line 63.
  • at least one sensor means 64 is provided, which measures the level of condensate 1 1 '.
  • This sensor means is in connection with the control unit 60, which evaluates the signals of the sensor means 64 and initiates the admission of control air at an increased level.
  • the control unit 60 controls a valve 62 in the control air line 63, with which the supply of control air 14 to the chamber 24 can be regulated.
  • Chamber 14 initiated so that between the chamber 24 and the
  • Outlet nozzle 33 of the main filter 30 sets a pressure difference, through which the condensate 1 1 'is pressed through the filter 30.
  • a corresponding pressure reduction can take place in front of and / or in the valve 62.
  • it can be a reduction in pressure from 7bar to 0.5bar, which can be achieved by throttling.
  • a pressure reduction also take place behind the valve 62, so that it can be realized, for example, by the valve 50.
  • the pressurization requires that the chamber 24 and the connection between the chamber 24 and the main filter 30 are made so tight that at this point no air or at least no appreciable amounts of air can escape.
  • Diaphragm valve 50 comprises two chambers, a control air chamber 52 and a mixture chamber 53. These two chambers are separated by an elastic membrane 54. Via a mixture inlet 55, condensate 1 1 flows from the pressure relief chamber 21 into the mixture chamber 53 of the diaphragm valve 50.
  • FIG. 1 shows how the condensate flows from the mixture chamber 53 into the chamber 24 of the head housing during normal operation of the oil / water separator. This is done via a Gemischauslass 56. To the extent that condensate 1 1 from the
  • Mixing outlet 56 flows into the chamber 24, treated condensate 1 1 "leaves the apparatus at the pure water outlet to the sewer, thereby setting a certain condensate level in the chamber 24.
  • Condensate level on and a level A represents, for example, a critical maximum level, which should not be exceeded. Will about the
  • the control unit 60 opens the valve 62, thus leading control air 14 in the control air chamber 52 of the
  • the sensor means 64 is preferably designed so that only the level of condensate is detected, while free oil fractions and air above the condensate are ignored. It can thus distinguish between condensate and oil or air. The sensor means 64 thus detects the level
  • control air can exit via a control air outlet 57 from the control air chamber 52 and thus enter the chamber 24 of the head housing.
  • the control air outlet 57 preferably has a smaller cross section than the
  • Control air inlet 58 so that can build up within the control air chamber 52 quickly pressure when control air 14 is introduced. By this pressure, the diaphragm 54 moves within the valve 50 to the left in the direction of the mixture inlet 55 and closes it. So no condensate 1 1 flow into the chamber 24 more.
  • the control unit 60 also interrupts the inflow of condensate 1 1 in the pressure relief chamber 21 at the same time. This may in particular be combined with an intermediate collection of the condensate before the oil / water separator 10 or the condensate is fed to another, parallel oil / water separator.
  • control unit 60 By the closure of the mixture inlet 55 by means of the membrane 54, no air can escape from the chamber 24 into the pressure relief chamber 21 in this way.
  • the control unit 60 also closes the valve 72 to the reservoir 70. Further supply of control air 14 in the chamber 24 increases the pressure therein, whereby the condensate 1 1 is pressed through the main filter 30 and the riser 40 to the outlet 42 and thereby cleaned can. Thus, the increased flow resistance of the filter can be overcome and the device can be kept in operation without overflowing.
  • the control air 14 serves only to close the mixture inlet 55 through the membrane 55 and subsequently to the pressure build-up within the chamber 24. This situation is shown in FIG. The condenser level has reached the maximum level A and the membrane 54 closes the mixture inlet 55.
  • FIGS 3 and 4 show the operation of the diaphragm valve 50 in a schematic representation, wherein the two chambers 52 and 53 are visible within a valve housing 51 which by an elastic membrane 54
  • the diaphragm 54 is such that the mixture inlet 55 is open and condensate may flow from the mixture inlet 55 through the mixture chamber 53 and out of the mixture outlet 56. If control air 14 is introduced into the control air inlet 58, builds up within the Control air chamber 52 pressure, by which first the membrane 54 is pressed against the mixture inlet 55, whereby it closes this. The control air exits from the control air outlet 57 and thus builds pressure in the chamber of the
  • the control air 14 can be switched off again by the control unit 60 under different conditions. For example, it can be switched off when the condensate level has reached a lower level B. If the control air 14 is turned off, the membrane 54 returns to its original position (FIG. 1) and releases the mixture inlet 55, so that new condensate 1 1 can flow into the chamber 24. If the condensate level increases again up to level A, a pressurization could take place again, so that there is a steady change between normal operation and pressurization. The level of condensate moves between points A and B.
  • the control air 14 can also be switched off after a predetermined period of time if, for example, empirical values show that the fill level in the chamber 24 has fallen after this time period to a predetermined level which corresponds to the level B.
  • a further pressurization can follow when the level rises again. In this embodiment, therefore, only one level A must be defined and a time control realized.
  • a minimum level C can be defined below which the level of condensate must not fall. This is below the level B and thus below the working range between A and B. If the condensate level despite
  • control unit 60 outputs service messages. This can be done, for example, when a predetermined number of cycles is reached or the duration of a cycle becomes too large.
  • One cycle represents pressurized operation, i. For example, the operation between the levels A and B.
  • a service message can be issued when a
  • Service interval has expired (e.g., 6 months).
  • Operation with pressurization may also be performed for maintenance purposes.
  • a corresponding service command can be input to the control unit 60 by the maintenance personnel, by means of which a control command is generated which effects the described supply of control air 14. So can the
  • Main filter 30 empty and then replaced, if it is a cartridge. For this purpose, the fittings on the inlet pipe 32 and outlet nozzle 33 are released, the main filter 30 is unscrewed and screwed on a fresh filter. If, on the other hand, one were to empty the chamber 24 for this purpose with a pump, condensate could be sucked out of the filter by reflux. This would require a further valve in the region of the connection opening 23.
  • Outlet opening 42 at the oil outlet of the collecting outlet 71 and by the level of the condensate above the filter.
  • valves used in the described embodiments of the invention are merely examples, and these and other valves are also formed by any other types of valves suitable for the particular application.
  • the solenoid valve 72 may also be designed like the diaphragm valve 50.
  • other types of valves such as ball valves, gate valves, hose valves, etc. can be used for both valves.
  • Fig. 5 shows an example of a second embodiment of the invention
  • the control air inlet branches 58 so that a part of the control air can be guided to the valve 50 in order to control this. Further control air is first fed to a restriction 65 before it enters the second chamber 24 in order to increase the pressure there. In this way, a pressure reduction for the control air can take place within the device.
  • valve 50 is preferably configured to reopen when the control air is turned off.
  • the valve can also be controlled by the control unit 60, for example, to effect opening of the valve.
  • the closing of the valve 50 may be triggered by the control unit 60.

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  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Analytical Chemistry (AREA)
  • Water Treatment By Sorption (AREA)
  • Compressor (AREA)
  • Filtration Of Liquid (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

L'invention concerne un dispositif permettant de séparer l'eau et l'huile (10) afin de retirer des constituants contenant de l'huile dans un mélange eau/huile, comprenant un filtre principal (30) destiné à séparer les constituants contenant de l'huile dans un mélange eau/huile. Le mélange eau/huile à traiter est guidé vers le filtre principal (30) et evacué après le passage du mélange à travers le filtre principal (30) hors du dispositif de séparation de l'eau et de l'huile (10), le dispositif de séparation de l'eau et de l'huile (10) étant conçu pour faire circuler ce liquide selon le principe hydrostatique. Le dispositif de séparation de l'eau et de l'huile (10) selon l'invention présente une unité de commande (60) conçue pour faire passer dans le dispositif de séparation de l'eau et de l'huile (10) de l'air un jet temporaire d'air comprimé (14) permettant de pousser le mélange eau/huile par le filtre principal (30) sous l'effet de la surpression.
EP16766488.7A 2015-07-24 2016-07-22 Dispositif de séparation de l'eau et de l'huile par application d'air comprimé Pending EP3325124A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102015112092.5A DE102015112092B4 (de) 2015-07-24 2015-07-24 Öl/Wasser-Trennvorrichtung mit Druckluftbeaufschlagung
PCT/EP2016/067516 WO2017017008A1 (fr) 2015-07-24 2016-07-22 Dispositif de séparation de l'eau et de l'huile par application d'air comprimé

Publications (1)

Publication Number Publication Date
EP3325124A1 true EP3325124A1 (fr) 2018-05-30

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
EP16766488.7A Pending EP3325124A1 (fr) 2015-07-24 2016-07-22 Dispositif de séparation de l'eau et de l'huile par application d'air comprimé

Country Status (7)

Country Link
US (1) US10722817B2 (fr)
EP (1) EP3325124A1 (fr)
JP (1) JP6860549B2 (fr)
KR (1) KR102113930B1 (fr)
CN (1) CN107921329A (fr)
DE (1) DE102015112092B4 (fr)
WO (1) WO2017017008A1 (fr)

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DE102020133106A1 (de) 2020-12-11 2022-06-15 Beko Technologies Gmbh Filtereinheit und Bodeneinheit einer Öl/Wasser-Trennvorrichtung zum Entfernen ölhaltiger Bestandteile aus einem Öl/Wasser-Gemisch
CN112933664A (zh) * 2021-01-29 2021-06-11 云南电网有限责任公司电力科学研究院 一种变压器油中水分过滤设备及使用方法
CN113244663B (zh) * 2021-06-24 2021-09-17 山东尚能实业有限公司 一种石油化工炼油用油水分离装置
CN115382364B (zh) * 2022-11-01 2023-03-10 杭州嘉隆气体设备有限公司 一种智能化冷冻式压缩空气干燥器及使用方法

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KR102113930B1 (ko) 2020-06-03
DE102015112092B4 (de) 2022-03-10
CN107921329A (zh) 2018-04-17
JP6860549B2 (ja) 2021-04-14
KR20180033191A (ko) 2018-04-02
JP2018525215A (ja) 2018-09-06
US10722817B2 (en) 2020-07-28
DE102015112092A1 (de) 2017-01-26
US20180161698A1 (en) 2018-06-14

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