OIL/WATER SEPARATOR WITH COMPRESSED AIR CHARGING

Abstract

An oil/water separating device for removing oil-containing constituents from an oil/water mixture, including a main filter which is configured for separating oil-containing constituents from the oil/water mixture, where an oil/water mixture to be purified is supplied to the main filter from a top housing via a condensate line and is removed from the oil/water separating device after passing through the main filter, and the oil/water separating device is configured for supplying and removing these liquids in accordance with the hydrostatic principle, where the top housing is disposed above the main filter, wherein the distance between the top housing and the main filter is selected so as to result in a hydrostatic pressure on the main filter of at least 0.05 bars.

Claims

1. An oil/water separating device for removing oil-containing constituents from an oil/water mixture, comprising a main filter which is configured for separating oil-containing constituents from the oil/water mixture, wherein an oil/water mixture to be purified is supplied to the main filter from a top housing via a condensate line and is removed from the oil/water separating device after passing through the main filter, and the oil/water separating device is configured for supplying and removing these liquids in accordance with the hydrostatic principle, wherein the top housing is disposed above the main filter and the distance between the top housing and the main filter is selected so as to result in a hydrostatic pressure on the main filter of at least 0.05 bars.

2. The oil/water separating device according to claim 1, wherein the distance between the top housing and the main filter is selected so as to result in a hydrostatic pressure on the main filter of 0.1 bars to 0.3 bars.

3. The oil/water separating device according to claim 1, wherein the oil/water separating device further has a control unit which is configured for temporarily charging the oil/water separating device with control air.

4. The oil/water separating device according to claim 3, wherein sensor means for detecting the oil/water mixture filling level are provided in the oil/water separating device, which are connected to the control unit.

5. The oil/water separating device according to claim 4, wherein the control unit is configured for temporarily charging the oil/water separating device with control air if a predetermined oil/water mixture filling level is detected by the sensor means.

6. The oil/water separating device according to claim 3, wherein the control unit is configured to cease charging the oil/water separating device with control air if a predetermined oil/water mixture filling level is detected by the sensor means.

7. The oil/water separating device according to claim 3, wherein the control unit is configured for charging the oil/water separating device with control air because of a control command to the control unit.

8. The oil/water separating device according to claim 3, wherein the supply of the oil/water mixture into the oil/water separating device is stopped during the charging with control air.

9. The oil/water separating device according to claim 3, wherein the oil/water separating device further has means for supplying the oil/water mixture into a chamber within the top housing, and a connecting opening for transferring the oil/water mixture from the chamber into the main filter, and the control unit is configured for temporarily charging the chamber with control air, during which control air is conducted into the chamber within the top housing in such a manner that the oil/water mixture is pushed from the chamber through the connecting opening into the main filter by means of overpressure.

10. The oil/water separating device according to claim 9, wherein the control air and the oil/water mixture are conducted into the chamber of the top housing via a diaphragm valve, wherein the diaphragm valve has a control air chamber and a mixture chamber separated from each other by a diaphragm, and the diaphragm valve has a mixture inlet for supplying the oil/water mixture into the mixture chamber and a control air inlet for supplying control air into the control air chamber, and a mixture outlet for removing the oil/water mixture from the mixture chamber into the chamber of the top housing and a control air outlet for removing the control air from the control air chamber into the chamber of the top housing are provided, wherein the mixture inlet can be closed by means of the diaphragm by charging the control air chamber with control air.

11. The oil/water separating device according to claim 10, wherein the control air outlet of the diaphragm valve has a smaller opening cross section than the control air inlet.

12. The oil/water separating device according to claim 10, wherein the feed of the oil/water mixture to the diaphragm valve can be interrupted by the control unit during the charging of the chamber of the top housing with control air.

13. The oil/water separating device according to claim 1, wherein control air with an overpressure in the order of 0.3-1 bars is used.

14. The oil/water separating device according to claim 9, wherein the top housing has an inlet opening via which the oil/water mixture can be conducted into a pressure relief chamber within the top housing from which the oil/water mixture can be conducted into the chamber of the top housing.

15. The oil/water separating device according to claim 14, wherein the pressure relief chamber is connected to the mixture chamber of the diaphragm valve via the mixture inlet.

16. The oil/water separating device according to claim 9, wherein free oil fractions floating on the oil/water mixture in the chamber of the top housing can be discharged from the chamber via a collective drain.

17. The oil/water separating device according to claim 16, wherein the collective drain can be closed by the control unit during the charging of the chamber with control air.

18. The oil/water separating device according to claim 1, wherein the main filter is formed by at least one filter cartridge that can be temporarily connected to the top housing.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0031] Other advantages, special features and expedient further developments of the disclosure are apparent from the dependent claims and the following presentation of preferred embodiments with reference to the illustrations.

[0032] In the drawings:

[0033] FIG. 1 shows a schematic illustration of a first embodiment of the oil/water separating device according to the disclosure in normal operation;

[0034] FIG. 2 shows a schematic illustration of a second embodiment of the oil/water separating device with compressed air charging according to the disclosure in normal operation;

[0035] FIG. 3 shows a schematic illustration of the oil/water separating device of FIG. 2 when charged with compressed air;

[0036] FIG. 4 shows a diaphragm valve of an oil/water separating device in normal operation;

[0037] FIG. 5 shows a diaphragm valve of an oil/water separating device when charged with compressed air; and

[0038] FIG. 6 shows a schematic illustration of a third embodiment of the oil/water separating device according to the disclosure in normal operation.

DETAILED DESCRIPTION

[0039] The first embodiment of an oil/water separating device 10 according to the disclosure shown schematically in FIG. 1 comprises various components. In this case, the device at least comprises a main filter 30 configured for treating an oil/water mixture or condensate 11 from an air compressor, which is not shown, by oil-containing constituents being separated from this condensate. This may occur by means of adsorption to a filter material, wherein the main filter 30 preferably comprises a material that is capable of separating liquids with finely dispersed, even emulsified, oils so that they are ready for being supplied. For this purpose, oleophilic melt-spun polymer with a distribution-oriented surface compaction and shape and activated carbon with an adapted consistency and size for absorbing extremely fine oil droplets and oleophilic foamed polymer are suitable. The main filter 30 has a main filter housing 80 into which a corresponding adsorption filter material 31 is inserted.

[0040] In the exemplary embodiment shown, the oil/water separating device 10 further comprises a control unit 60 with which the functions of the device can be controlled. In particular, this may include the evaluation of sensor signals of various detectors, the opening and closing of valves and the detection of periods. Preferably, the control unit 60 further has inputting means for manually inputting control commands. Maintenance work on the apparatus, for example, can by carried out through these control commands. The control unit 60 may also comprise display means for displaying the status of the device and/or warning and service notifications.

[0041] The oil/water separating device 10 operates in accordance with the hydrostatic principle of communicating columns. To this end, a top housing 20 is typically attached above the main filter 30. The top housing 20 is connected to the main filter 30 via a connecting opening 23 and a subsequent condensate line 82. The length of the condensate line 82, or the distance between the main filter housing 80 and the main filter 30, determines the hydrostatic pressure with which the condensate is pushed through the main filter 30. In particular, the main filter 30 may be at least one replaceable cartridge filter which is temporarily connected to the top housing 20 via an inlet port 32. In particular, this may be effected by means of a tight screw connection.

[0042] Condensate can be introduced into the top housing 20 via an inlet opening 22. In particular, the condensate 11 originates from an air compressor and is to be treated by the oil/water separating device 10 by oil-containing constituents being removed from the condensate 11. In this case, the condensate 11 flows into the top housing 20 and thence, due to gravity, into the main filter 30 located below it. The main filter 30 is connected via an outlet port 33 to a riser pipe 40 via which treated condensate 11″ exits the oil/water separating device 10. This outlet port 33 may also be connected to the riser pipe 40 via a tight screw connection, so that the main filter 30 is replaceable as a whole. Treated condensate 11″ leaves the apparatus at the pure-water outlet 42 towards the sewer in the same amount as new condensate 11 flows into the top housing 20.

[0043] At the height of the condensate level thus generated within the housing 20, a collective drain 71 may be provided which is connected to a collecting container 70. The valve 72 is, for example, a solenoid valve that can be activated by means of a control unit 60. Free oil fractions 13 that float within the top housing 20 on the condensate 11′ can be removed and collected via this collective drain 71. These free oil fractions have a density <1 kg/dm.sup.3. Thus, a separation of free oil fractions is carried out before the condensate 11 is supplied to the main filter 30, so that pre-purified condensate 11′ arrives at the main filter 30. However, the separation of free oil fractions may also be integrated into a cartridge of the main filter 30.

[0044] A device for separating heavy, sediment-like constituents with a density >1 kg/dm.sup.3 (not shown) may be provided upstream or downstream from the inlet opening 22. It operates according to the principle of gravity separation, so that these constituents deposit on the bottom of the device and do not enter the main filter 30.

[0045] As shown in the Figures, the top housing 20 has at least one chamber 24 into which the condensate 11 flows and is thence supplied to the main filter 30. This chamber 24 constitutes the main chamber of the top housing 20, which may, however, be supplemented with a second chamber in the form of a pressure relief chamber 21. The condensate 11 is at first introduced into the latter, for pressure relief. Entrained compressed air from the compressor can be discharged in this pressure relief chamber 21, wherein this air can escape via an outlet. This relief air outlet 12 may be routed through a filter mat 25 and also be provided with a closable valve (not shown).

[0046] From this pressure relief chamber 21, the condensate 11 arrives in the chamber 24 of the top housing 20, free oil fractions 13 are discharged via the collective drain 71, and the condensate 11′ pre-purified in this manner flows off into the main filter 30. This constitutes the normal operation of the device 10, in which a certain condensate level is generated within the chamber 24, in which free oil fractions 13 are continuously removed, and purified condensate 11″ is discharged into a sewer via a riser pipe 40.

[0047] Due to the hydrostatic pressure produced, the condensate to be purified is pressed into the main filter 30 already with sufficient overpressure.

[0048] Due to a saturation of the upper layers of the filter 30 or the formation of biological slimy layers, however, the flow resistance of the filter 30 may additionally increase even more. If this happens, the condensate level increases within the chamber 24, which may result in the device overflowing. Further, in the case of an elevated condensate level, not only do free oil fractions flow off into the collecting container 70, but also unpurified condensate.

[0049] Although the device 10 can be operated with overpressure already in normal operation, the normal operation of the device 10 can be supplemented with a pressure operation in which the condensate 11′ can be pushed through the main filter 30 by even higher overpressure, as is shown in FIG. 2. This is preferably done by charging the chamber 24 with control air 14 via a control air pipe 63. At least one sensor means 64 measuring the filling level of condensate 11′ is provided in order to detect an elevated condensate level within the chamber 24. This sensor means is connected to the control unit 60 which evaluates the signals of the sensor means 64 and triggers the charging with control air in the event of an elevated filling level. For this purpose, the control unit 60 activates a valve 62 in the control air pipe 63 with which the supply of control air 14 to the chamber 24 can be controlled. The collective drain 71 includes a valve 72. The valve 72 is, for example, a solenoid valve that can be activated by means of a control unit 60.

[0050] Preferably, control air 14 is introduced into the chamber 14 with an overpressure of up to 0.5 bars, so that a pressure difference is generated between the chamber 24 and the outlet port 33 of the main filter 30, by means of which the condensate 11′ is pushed through the filter 30. If the device 10 device is connected to a compressed air pipe with a higher pressure for this purpose, a corresponding pressure reduction may take place upstream of and/or in the valve 62. For example, the pressure may be reduced from 7 bars to 0.5 bars, which may be accomplished by throttling. Alternatively or additionally, a pressure reduction may also take place downstream of the valve 62, so that it may also be realized, for example, by the valve 50.

[0051] The charging with pressure presupposes that the chamber 24 and the connection between the chamber 24 and the main filter 30 are configured to be so tight that no air, or at least no appreciable quantities of air, can escape at this point. It may further be provided that the control unit 60 also seals the valve 72 of the collecting container 70 to be tight with respect to the free oil fractions 13 during the charging with pressure. Furthermore, the supply of new condensate 11 during the charging with pressure is expediently stopped in order also to seal this feed.

[0052] In the exemplary embodiment of FIGS. 2 and 3, a diaphragm valve 50, which is connected to the condensate supply and the control air feed 63, is provided for this purpose within the chamber 24 of the top housing 20. The diaphragm valve 50 comprises two chambers, a control air chamber 52 and a mixture chamber 53. These two chambers are separated from each other by an elastic diaphragm 54. Condensate 11 flows from the pressure relief chamber 21 into the mixture chamber 53 of the diaphragm valve 50 via a mixture inlet 55. FIG. 2 shows how the condensate flows from the mixture chamber 53 into the chamber 24 of the top housing in the normal operation of the oil/water separating device. This takes place via a mixture outlet 56. Treated condensate 11″ leaves the apparatus at the pure-water outlet towards the sewer in the same amount as condensate 11 flows from the mixture outlet 56 into the chamber 24. In the process, a certain condensate level is generated in the chamber 24.

[0053] If the flow resistance of the main filter 30 increases, this condensate level rises and a filling level A constitutes a critical maximum condensate filling level, for example, which should not be exceeded. If this elevated condensate level A is detected by the sensor means 64, the control unit 60 opens the valve 62 and thus conducts control air 14 into the control air chamber 52 of the diaphragm valve 50. In this case, the sensor means 64 is preferably configured in such a way that only the condensate level is detected, whereas free oil fractions and air above the condensate are ignored. Thus, it is capable of differentiating between condensate and oil or air. The sensor means 64 thus detects the filling level of condensate 11′, and not the filling level of free oil fractions 13 above the condensate 11′.

[0054] The control air can escape from the control air chamber 52 via a control air outlet 57 and thus arrive in the chamber 24 of the top housing 20. In this case, the control air outlet 57 preferably has a smaller cross section than the control air inlet 58, so that pressure can be quickly built up in the control air chamber 52 if control air 14 is introduced. Due to this pressure, the diaphragm 54, within the valve 50, moves to the left in the direction of the mixture inlet 55 and seals the latter. Thus, no condensate 11 is able to flow into the chamber 24 any longer. Preferably, the control unit 60 simultaneously also interrupts the feed of condensate 11 into the pressure relief chamber 21. This may be combined, in particular, with an intermediate collection of the condensate upstream of the oil/water separating device 10, or the condensate is supplied to another oil/water separating device connected in parallel.

[0055] By closing the mixture inlet 55 by means of the diaphragm 54, no air can escape from the chamber 24 into the pressure relief chamber 21 via this way, either. Preferably, the control unit 60 also closes the valve 72 to the collecting container 70. By further supplying control air 14 into the chamber 24, the pressure therein rises, whereby the condensate 11 can be pushed through the main filter 30 and the riser pipe 40 towards the outlet 42 and be purified in the process. Thus, the elevated flow resistance of the filter can be overcome and the device can be kept in operation without overflowing. In the process, the control air 14 first serves for closing the mixture inlet 55 by means of the diaphragm 55 and then for building up pressure within the chamber 24. This situation is shown in FIG. 3. The condensate level has reached the maximum filling level A and the diaphragm 54 closes the mixture inlet 55.

[0056] FIGS. 4 and 5 show the mode of operation of the diaphragm valve 50 in a schematic representation, wherein the two chambers 52 and 53 are apparent within a valve housing 51, which are separated from each other by an elastic diaphragm 54. In normal operation (FIG. 4), the diaphragm 54 is positioned such that the mixture inlet 55 is open and condensate is able to flow from the mixture inlet 55 through the mixture chamber 53 and out from the mixture outlet 56. If control air 14 is introduced into the control air inlet 58, pressure builds up within the control air chamber 52, due to which the diaphragm 54 is first pressed against the mixture inlet 55, whereby it seals the latter. The control air exits the control air outlet 57 and thus builds up pressure in the chamber of the top housing 20.

[0057] The control air 14 can be switched off again by the control unit 60 under various conditions. For example, it may be switched off if the condensate level has reached a lower filling level B. If the control air 14 is switched off, the diaphragm 54 returns into its original position (FIG. 2) and unblocks the mixture inlet 55, so that new condensate 11 can flow into the chamber 24. If the condensate level again rises up to the filling level A, a charging with pressure could again take place, so that the normal operation and the charging with pressure are continuously alternated. Thus, the level of the condensate moves between the points A and B.

[0058] Furthermore, an error notification may be issued on the control unit 60 if the condensate level in the chamber 24 does not reach a lower filling level B, i.e. remains above this level, even during the charging with pressure. This suggests, for example, that the filter 30 is blocked and/or the diaphragm valve 50 is defective.

[0059] The control air 14 may also be switched off after a predefined period, for example, if empirical values show that the filling level in the chamber 24 has dropped to a predefined level corresponding to the level B after this period. Also in this case, another charging with pressure may follow in case of a renewed increase of the level. Thus, in this embodiment, only a level A has to be defined and a timer control has to be realized.

[0060] Furthermore, a minimum filling level C may be defined, beneath which the condensate level must not drop. It lies below the level B and thus below the working range between A and B. If the condensate level drops below this minimum filling level C in spite of the control air being switched off, this suggests that the solenoid valve 62 of the control air 14 is defective, for example, and that control air still flows into the diaphragm valve 50. An error notification may be outputted on the control unit 60 also in this case, because the container could otherwise run out. Thus, the optional point C constitutes an alarm point.

[0061] It may also be provided that the control unit 60 output service notifications. This may take place, for example, if a predefined number of cycles has been reached or the duration of a cycle becomes too long. In this case, the cycle constitutes an operation with a pressure charging, i.e., for example, the operation between the levels A and B. A service notification may also be outputted if a service interval has elapsed (e.g. 6 months).

[0062] An operation with pressure charging may also be carried out for maintenance purposes. For this purpose, a corresponding service command may be inputted by the maintenance personnel into the control unit 60, by means of which a control command is generated that causes the above-described feed of control air 14. Thus, the main filter 30 can be squeezed empty and then replaced if it is a cartridge. For this purpose, the screw connections on the inlet port 32 and the outlet port 33 are unfastened, the main filter 30 is screwed off and a fresh filter is screwed on. If, in contrast, the chamber 24 were pumped empty with a pump for this purpose, condensate could be sucked from the filter due to backflow. This would require another valve in the area of the connecting opening 23.

[0063] The hydraulic levels within the oil/water separating device operating in accordance with the hydrostatic principle must be distinguished from the sensor levels A, B and C. Hydraulic levels are produced on the condensate discharge of the outlet opening 42, at the oil discharge of the collective drain 71 and due to the level of the condensate above the filter.

[0064] The valves used in the above-described exemplary embodiment of the disclosure merely constitute examples, wherein these and other valves are also formed by any other kinds of valve that are suitable for the respective application. For example, the solenoid valve 72 may also be configured like the diaphragm valve 50. Furthermore, other types of valve, such as ball valves, slide gate valves, pinch valves etc. may be used for both valves.

[0065] By way of example, FIG. 6 shows a second embodiment of the oil/water separating device 10′ according to the disclosure in normal operation. The essential components and functions of this oil/water separating device 10′ may correspond to those of the first embodiment according to FIG. 2. However, the valve 50 is not configured as a diaphragm valve with the above-described functions. Rather, another type of valve may be used with which the feed of condensate into the second chamber 24 may be controlled. Condensate 11 still flows from the pressure relief chamber 21 through the valve 50 into the second chamber 24, wherein the valve 50 can be activated, in particular, by the control air if the condensate 11′ reaches the level A. For this purpose, the control air inlet 58 is branched so that a part of the control air can be conducted to the valve 50 in order to activate it. Additional control air is first fed to a throttling means 65 prior to arriving in the second chamber 24 to increase the pressure there. In this way, a pressure reduction for the control air can take place within the device. However, this pressure reduction may also be dispensed with if the control air of the device can already be supplied with the desired pressure or throttling takes place at another location.

[0066] The valve 50 is preferably configured such that it opens again when the control air is switched off. However, the valve may also be capable of being activated by the control unit 60, for example in order to cause the valve to open. It may also be possible to trigger the closing of the valve 50 by means of the control unit 60.