• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
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    • 专利摘要:
    This separation device (100) comprises: - a separation chamber (102) having an inlet (104) and an outlet (106), - an oil recovery chamber (110) connected to the separation chamber (102) an emitter electrode (121), a collector electrode (122), and an electronic unit (124) connected to the emitter and collector electrodes, during a charge phase: • to carry the emitting electrode (121) to a negative potential, so as to negatively charge drops of oil, and • bring said at least one collector electrode (122) to a zero or positive potential so as to collect negatively charged oil drops. The separation device (100) further comprises a pressure loss generating member (131, 132) in the separation chamber (102). The oil recovery chamber (110) is connected to the downstream portion (102.4) of the separation chamber (102) through a vacuum port (126), so that the oil recovery chamber (110) ) is in depression.
    公开号:FR3026660A1
    申请号:FR1459387
    申请日:2014-10-01
    公开日:2016-04-08
    发明作者:Pascal Guerry；Ludovic Serrurier；Adrien Eustache
    申请人:MGI Coutier SA；
    IPC主号:
    专利说明:

    [0001] The present invention relates to a separation device for separating oil drops from a mixture of gas and oil and from an internal combustion engine. In addition, the present invention relates to a separation process using such a separation device.
    [0002] The present invention applies in particular to the field of the separation of oil and gas in a mixture from an internal combustion engine of a motor vehicle, of the Diesel or gasoline type. By motor vehicle, we mean including passenger vehicles, commercial vehicles or industrial vehicles for example truck type.
    [0003] An internal combustion engine in use produces crankcase gases, which form an aerosol mixture comprising drops of oil suspended in a gas. The drops of oil come from the splashing of the connecting rods and the crankshaft in the oil contained in the oil tank. The gas comes from leaks between cylinders and pistons; these leaks are sometimes referred to as "blowby gas". It is then necessary to separate the oil from the gas to reinject the oil into the internal combustion engine. US2008216660A1 discloses an electrostatic precipitator for separating oil drops from a mixture of gas and oil. The electrofilter of US2008216660A1 comprises a separation chamber, an oil recovery chamber connected to the separation chamber for the oil flow, an emitting electrode, a collector electrode, and an electronic unit supplying the emitting electrode. in the electrofilter of US2008216660A1, when the mixture is rich in oil, the oil captured by the collector electrode accumulates on the collector electrode without being completely evacuated, which leads to a risk of clogging, therefore of failure of the electrostatic precipitator. In addition, the accumulated oil is relatively unloaded on the collector electrode. However, the accumulated electrostatic charges may induce electrical breakdown in the electrostatic precipitator, and thus the decommissioning of the electrostatic precipitator. The present invention is intended in particular to solve, in whole or in part, the problems mentioned above, by providing an effective and compact separation device. For this purpose, the subject of the invention is a separation device for separating oil drops from a mixture comprising gas and oil drops and coming from an internal combustion engine. comprising at least: - a separation chamber having i) an inlet configured for the entry of the mixture into the separation chamber, and ii) an outlet arranged for the gas outlet out of the separation chamber, - a chamber of recovering oil connected to the separation chamber through at least one flow orifice, so that liquid oil can flow from the separation chamber to the oil recovery chamber at through said at least one flow orifice; at least one emitter electrode extending at least partially in the separation chamber; at least one collector electrode extending at least partially in the separation chamber; and one a an electronic unit connected to said at least one emitter electrode and to said at least one collector electrode, the electronic unit being configured for, at least during a charging phase: - bringing said at least one emitter electrode to a negative potential, so said at least one emitting electrode generates at least one electric field adapted to negatively charge drops of oil, and - bringing said at least one collector electrode to a zero or positive potential, so that said at least one collector electrode collects negatively charged drops of oil, the separating device being characterized in that it further comprises at least one pressure loss generating member disposed in the separation chamber so as to delimit an upstream portion and a downstream portion therein. , the pressure loss generating member being configured to generate pressure drops between the upstream portion and the downstream when gas flows between the inlet and the outlet, and in that the oil recovery chamber is connected to the downstream portion via at least one vacuum port, so that the pressure in the oil recovery chamber is lower than the pressure in the upstream part.
    [0004] Since the pressure in the oil recovery chamber is lower than the pressure in the upstream portion, a portion of the gas is sucked by the or each flow orifice, which contributes to the flow of oil through the or each flow port and to the oil recovery chamber. Thus, such a separation device allows an effective evacuation of the oil separated from the mixture, because it maximizes the flow rate of the oil separated from the mixture, while minimizing its size. Indeed, the oil recovery chamber and each flow orifice aspire a large flow of oil. Because of this suction of oil, the risk of clogging of each collector electrode are reduced, so that the risk of electrical breakdown is limited or even avoided, since each collector electrode accumulates less oil and therefore less electrostatic charges.
    [0005] In a motor vehicle, diesel or gasoline type, a separation device according to the invention may for example be integrated in the cylinder head cover or form a component independent of the cylinder head cover. In the present application, the term "to connect" and its derivatives 20 denote in particular the setting in communication of fluid, gas and / or liquid, between at least two zones. In the present application, the term "connect" and its derivatives relate in particular to an electrically conductive connection between at least two components. In the present application, the terms "upstream" and "downstream" refer to the general direction of flow of gas between the inlet and the outlet. The upstream portion extends from the inlet to said at least one loss-generating member. The downstream portion extends from said at least one loss of pressure generating member to the outlet. According to a variant of the invention, the pressure drop generating member is configured to generate a pressure difference of between 5 Pa and 200 Pa between the oil recovery chamber and the upstream portion. According to one embodiment of the invention, said at least one emitter electrode and said at least one collector electrode are at least partially composed of electrically conductive materials, and said at least one emitter electrode and said at least one collector electrode each have a surface state whose arithmetical mean difference Ra is between 0.1 μm and 100 μm. Thus, such emitting and collecting electrodes are relatively smooth, and therefore not very wetting, which favors the spreading of oil drops separated from the mixture on the emitting and collecting electrodes, thus reducing the accumulated oil on the emitting and collecting electrodes. According to a variant of the invention, said at least one emitter electrode and said at least one collector electrode are composed of plastic materials coated with electrically conductive materials. Alternatively to this variant, said at least one emitter electrode and said at least one collector electrode may be totally composed of electrically conductive materials, for example metallic materials. According to a variant of the invention, the electronic unit is configured for, at least during a charging phase, bringing said at least one emitting electrode to a substantially constant negative potential. Thus, such an electronic unit makes it possible to generate an electrostatic field, which maximizes the charge of the drops of oil, and therefore the oil deposition efficiency on each collecting electrode, and therefore the separation efficiency of the separation device. According to one embodiment of the invention, said at least one emitting electrode extends near the input.
    [0006] Thus, the or each emitting electrode can negatively charge drops of oil as soon as the mixture enters the separation chamber, thereby minimizing the size of the separation device. According to a variant of the invention, a distance separating the inlet and the said at least one emitting electrode is between 0% and 30% of the distance separating the inlet and the outlet. The distance between the inlet and the outlet corresponds to the length of the separation chamber. According to one embodiment of the invention, said at least one emitter electrode comprises at least one filiform portion.
    [0007] Thus, such a filiform portion makes it possible to increase the intensity of the electric field for a given electrical voltage, and thus the efficiency of depositing the oil on the collecting electrode. Indeed, a filiform portion produces a significant edge effect, because its section has small dimensions.
    [0008] According to one embodiment of the invention, at least one filiform portion extends in a direction transverse to a direction of flow of the mixture between the inlet and the outlet. Thus, such a filiform portion transverse to the flow of the mixture makes it possible to generate an electric field in a large part of the flow section of the separation chamber. So such a transverse filiform portion can load many drops of oil contained in the mixture. According to a variant of the invention, said at least one filamentary portion extends generally in at least one direction perpendicular to a direction of flow of the mixture between the inlet and the outlet. According to a variant of the invention, the filiform portion is rectilinear. Thus, such a rectilinear filiform portion is simple to install in the separation chamber. Alternatively to this variant, the filiform portion may be curvilinear. Thus, such a curvilinear filamentary portion may be adapted to the geometry of the separation chamber. According to a variant of the invention, each filiform portion has a generally circular profile, whose diameter is less than 1 mm. Thus, such a filiform portion produces a large peak effect, hence an intense electric field. According to a variant of the invention, at least one filiform portion is formed by a wire. According to another variant of the invention, at least one filiform portion is formed by a needle. According to one embodiment of the invention, the separation device comprises at least two emitting electrodes, the filiform portions being arranged substantially parallel to one another. Thus, several emitting electrodes make it possible to produce several electric fields, thus to maximize the charge of the drops of oil and the number of charged drops of oil.
    [0009] According to one embodiment of the invention, the separation device further comprises at least one auxiliary electrode connected to the electronic unit, the electronic unit being configured for, at least during a charging phase, to carry the said at least one auxiliary electrode at a zero or positive potential, said at least one auxiliary electrode being arranged closer to said at least one emitting electrode than said at least one collecting electrode, so that an electric field established between said at least one emitting electrode and said at least one auxiliary electrode is more intense than an electric field established between said at least one emitting electrode and said at least one collecting electrode. Thus, each auxiliary electrode maximizes the electric field through which the oil drops. Indeed, each auxiliary electrode can be placed near the inlet and an emitting electrode, while each collecting electrode should rather be placed near the flow holes so as to accumulate the oil near its outlet to the chamber oil recovery. According to one embodiment of the invention, the separation device comprises at least two auxiliary electrodes formed by auxiliary filiform portions and arranged substantially parallel to each other and to the emitting electrodes, the auxiliary electrodes and the emitting electrodes being arranged in staggered rows. In other words, each auxiliary electrode being located opposite an interval delimited by two consecutive emitting electrodes.
    [0010] Thus, such a staggered arrangement makes it possible to increase the length of travel of the drops of oil in the electric field, therefore their loading time and their charge. Indeed, each electric field generated between an emitter electrode and an auxiliary electrode extends in a direction oblique with respect to the flow direction of the mixture. According to a variant of the invention, the distance between a neighboring auxiliary electrode and a transmitting electrode is between 10% and 30% of the distance between this emitting electrode and the closest collecting electrode. For example, if the distance between a neighboring auxiliary electrode and a transmitting electrode is 5 mm, then the distance between an emitter electrode and the nearest collector electrode may be between 15 mm and 50 mm. Thus, such a distance makes it possible to generate more intense electric fields between emitting and auxiliary electrodes than between emitting and collecting electrodes, which increases the number of charged drops of oil and the charge of each drop of oil before the drops. of oil do not reach near each collecting electrode. According to one embodiment of the invention, said at least one auxiliary electrode is arranged upstream of said at least one emitting electrode. Thus, such an arrangement makes it possible to maximize the collection of oil drops by a collecting electrode. Indeed, the electric field generated between a downstream emitter electrode and an upstream auxiliary electrode induces on each drop of charged oil an electrostatic force opposed to the aeraulic force. So this electric field slows each drop of oil, which facilitates its capture by a collector electrode. In addition, the aeraulic force tends to move each drop of charged oil away from the auxiliary electrode (of opposite or zero charge), which limits or prevents the accumulation of oil on the auxiliary electrode. According to one embodiment of the invention, a flow section of said at least one vacuum port is greater than a flow section of said at least one flow port. Thus, such a vacuum port ensures a sufficient pressure difference between the oil recovery chamber and the separation chamber. Thus such a vacuum port ensures the flow of oil through each flow port. According to a variant of the invention, the ratio between i) a flow section of said at least one vacuum outlet and ii) a flow section of said at least one flow orifice is greater than or equal to 2. Thus, a such a vacuum port maximizes the pressure difference between the oil recovery chamber and the separation chamber. According to one embodiment of the invention, said at least one flow orifice is located in a lower region of the upstream part, for example on the bottom of the upstream part.
    [0011] Thus, such a location allows gravitational oil flow through the flow port, in addition to suction due to the vacuum port. In the present application, the terms "lower" and "upper" refer to the altitude of an element when the separation device is in the service position. According to one embodiment of the invention, said at least one flow orifice is located near or in a respective side wall of the upstream portion. Thus, such a location makes it possible to increase the flow of oil flowing through the flow orifice. Indeed, the speed of the gas, therefore the aeraulic force exerted on each drop of oil, is minimal near the walls (calm zone), which minimizes the risk that a drop of oil is driven by the gas out of the air. flow orifice. According to one embodiment of the invention, the separating device comprises at least two flow orifices respectively disposed on two opposite sides of the upstream part, for example respectively near two opposite side walls of the upstream part. Thus, several flow orifices make it possible to increase the flow of oil flowing to the oil recovery chamber. In the present application, the terms "side" and "lateral" refer to the general direction of gas flow between the inlet and the outlet. According to a variant of this embodiment, the separation device comprises an even number of flow orifices, the flow orifices being arranged in equal numbers on each side of the upstream part. Thus, the profile of the gas velocities in the separation chamber is symmetrical, which allows oil flows with equivalent flow rates through the flow orifices. For example, the separating device may comprise four flow orifices, two flow orifices being arranged on one side of the upstream part and two flow orifices being arranged on the other side of the upstream part.
    [0012] According to a variant of the invention, the separation chamber has an axis of symmetry, the flow orifices being arranged symmetrically on each side of the axis of symmetry. According to one embodiment of the invention, said at least one collecting electrode extends near said at least one flow orifice. Thus, the oil is deposited on each collecting electrode as close to the flow orifices, which facilitates the flow of oil to the oil recovery chamber. According to a variant of the invention, the distance separating a respective flow orifice and a corresponding collector electrode represents between 0% and 5% of the distance separating the inlet and the outlet. According to one embodiment of the invention, the separating device comprises at least two flow orifices and at least two collecting electrodes, each collecting electrode extending near a respective flow orifice. Thus, several collecting electrodes and several flow orifices make it possible to increase the flow of oil flowing towards the oil recovery chamber. According to one embodiment of the invention, said at least one collecting electrode comprises an electrically conductive film, said at least one electrically conductive film at least partially covering a lower surface of the upstream portion. Thus, such an electrically conductive film makes it possible to form an efficient and light collecting electrode. According to a variant of the invention, each of said at least two collecting electrodes is formed by an electrically conductive strip covering a respective portion of the lower surface (or bottom) of the upstream portion of the separation chamber, a portion of each band electrically conductive being arranged near or around a respective flow port. According to an alternative to the previous embodiment, the separation device comprises a single collector electrode. For example, the single collection electrode may completely or partially cover the bottom (or bottom) surface of the upstream portion of the separation chamber. Thus, many drops of oil can be loaded and collected. According to one embodiment of the invention, said at least one collecting electrode comprises: - a peripheral electrically conductive film extending around said at least one flow orifice, and - at least one adjacent electrically conductive film arranged so as to extending the electrically conductive peripheral film and extending substantially vertically when the separating device is in the operating position. Thus, such peripheral and adjacent electrically conductive films make it possible to increase the flow of oil flowing to the oil recovery chamber. Indeed, the peripheral film makes it possible to collect oil around the flow orifice, while the adjacent film allows the gravitation to drive the oil towards the flow orifice. According to one embodiment of the invention, said at least one flow orifice has at least one acute edge comprising an edge having a radius of curvature less than 0.2 mm, and said at least one collecting electrode covers said at least one an acute edge. Thus, such an acute edge produces a peak effect, which makes it possible to generate relatively intense electric fields between the charged drops of oil and the collecting electrode covering the acute edge. According to a variant of the invention, a collecting electrode extends to the inside of a respective flow orifice. In other words, this collecting electrode covers each side of at least one edge of this flow orifice. According to one embodiment of the invention, said at least one acute edge comprises two edges having a radius of curvature of less than 0.2 mm, the two edges being connected by a rounded fillet, for example with a section 30 in the form of circular arc, the rounded fillet having a radius greater than 0.5 mm, preferably greater than 1 mm, said at least one collecting electrode covers the acute edges and the rounded fillet. Thus, such acute edges produce peak effects, which can generate relatively intense electric fields between charged oil drops and the collector electrode covering the acute edges. Likewise, the rounded fillet produces an inverse peak effect, which makes it possible to generate relatively intense electric fields between the charged drops of oil and the collecting electrode covering the rounded fillet.
    [0013] According to one embodiment of the invention, said at least one pressure drop generating member is disposed near a respective flow orifice. Thus, such positioning allows the pressure loss generating member to greatly reduce the gas velocities near each flow orifice. Therefore, this positioning reduces the risks of driving oil drops out of each flow orifice. In addition, the pressure drop generating member delimits a detachment zone near each flow orifice, which promotes the collection of oil drops by a collector electrode.
    [0014] According to a variant of the invention, the distance separating said at least one loss-pressure generating member and a respective flow orifice represents between 0% and 20% of the distance separating the inlet and the outlet. According to a variant of the invention, said at least one member 20 generating pressure drops is contiguous with a respective flow orifice. According to a variant of the invention, said at least one pressure drop generating member is configured to generate singular pressure drops. According to one embodiment of the invention, said at least one loss-generating member is formed by an obstacle. Thus, such an obstacle is easy to implement in the separation chamber and it produces pressure losses that vary little with the flow rate of the gas flow. According to a variant of the invention, said at least one obstacle has a height of between 50% and 100% of the height of the upstream part.
    [0015] According to a variant of the invention, said at least one loss-generating member obstructs between 5% and 30% of the flow section of the separation chamber. According to an alternative to the preceding embodiment, at least one loss-pressure generating member is formed by a curved section. According to another variant of the previous embodiment, at least one pressure loss generating member is formed by a reducing section which has a reduced flow section relative to the inlet. According to one embodiment of the invention, the separation chamber has the overall shape of a parallelepiped, for example a rectangular base, and the oil recovery chamber has the overall shape of a parallelepiped, for example to rectangular base. Thus, such a parallelepiped-shaped separation chamber is easy to implement in a motor compartment. According to one embodiment of the invention, the separation chamber has the overall shape of a cylinder, for example circular base, and the oil recovery chamber has generally the shape of a tube arranged around the separation chamber. Thus, such a cylinder-shaped separation chamber 20 has a gas flow having a uniform velocity profile. According to a variant of this embodiment, the separation device comprises a plurality of emitting electrodes formed by filiform portions arranged substantially parallel to each other and to the axis of the cylinder. Alternatively to the two previous embodiments, the separation chamber has a generally curved shape between the inlet and the outlet. In other words, the separation chamber forms a bend, so that the flow lines of the gas between the inlet and the outlet are bent. According to one embodiment of the invention, the separation device further comprises a transfer member connected to the oil recovery chamber, the transfer member being configured to allow a flow of the liquid oil to the oil recovery chamber. internal combustion engine and to prevent flow of gas from the internal combustion engine to the oil recovery chamber. Thus, such a transfer member makes it possible to keep the oil recovery chamber in a vacuum with respect to the separation chamber, since the transfer member prevents any gas supply coming from the internal combustion engine via the transfer member. to the oil recovery chamber. According to a variant of the invention, the transfer member comprises a siphon and a transfer line configured for an oil transfer to an engine block. Alternatively the transfer member comprises a valve and a transfer line configured for an oil transfer to an engine block. Furthermore, the present invention relates to a separation process, for separating oil drops from a mixture comprising gas and oil drops and from an internal combustion engine, the separation process comprising the steps: - implement a separation device according to the invention, - during a charging phase, control the electronic unit so that: - said at least one emitting electrode generates at least one electric field adapted to negatively charge drops of oil, and said at least one collecting electrode collects negatively charged oil drops, and allowing entry of the mixture into the separation chamber. Thus, such a separation process allows efficient evacuation of the oil separated from the mixture. The embodiments and variants mentioned above may be taken individually or in any technically possible combination. The present invention will be well understood and its advantages will also emerge in the light of the description which follows, given solely by way of nonlimiting example and with reference to the appended drawings, in which: - Figure 1 is a schematic view of perspective of a separation device according to a first embodiment of the invention - - Figure 2 is a schematic perspective view of a separation device according to a second embodiment of the invention - Figure 3 is a schematic perspective view of a separation device according to a third embodiment of the invention - Figure 4 is an enlarged view of detail IV in Figure 3; - Figure 5 is a section along the plane V in Figure 4; FIG. 5 schematically shows electric field lines between emitting electrodes and auxiliary electrodes belonging to the separation device of FIG. 3; - Figure 6 is a schematic perspective view of a separation device according to a fourth embodiment of the invention; FIG. 7 is an enlarged view of detail VII in FIG. 6; - Figure 8 is a view of a portion of Figure 7, on a larger scale and in perspective truncated by the plane VIII in Figure 7; FIG. 9 is a schematic perspective view of a separation device according to a fifth embodiment of the invention; - Figure 10 is a schematic perspective view of a separation device according to a sixth embodiment of the invention; - Figure 11 is a section of a separation device according to a seventh embodiment of the invention; and Fig. 12 is a flowchart illustrating a separation method according to the invention. FIG. 1 illustrates a separation device 100 for separating oil drops 2 from a mixture comprising drops of oil 2 and gas, symbolized by flow lines 4. This mixture is derived from a combustion engine internal not shown. The drops of oil 2 may be globally spherical in shape with a diameter of between 0.1 μm and 100 μm. The separating device 100 comprises a separating chamber 102. The separating chamber 102 generally has the shape of a parallelepiped with a rectangular base. The separation chamber 102 has an inlet 104, which is configured for the entry of the mixture into the separation chamber 102. In addition, the separation chamber 102 has an outlet 106, which is arranged for the gas outlet 4 out of the separation chamber 102. When the separation device 100 is in use, the mixture enters the separation chamber 102 through the inlet 104 and the gas 4 exits the separation chamber 102 through the outlet 106. In addition, the separating device 100 comprises an oil recovery chamber 110. The oil recovery chamber 110 generally has the shape of a parallelepiped with a rectangular base. The oil recovery chamber 110 is connected to the separation chamber 102 through two flow ports 112 and 113. When the separation device 100 is in operation, the liquid oil flows from the separation chamber 102 to the oil recovery chamber 110 through the flow ports 112 and 113. In addition, the separation device 100 comprises an emitter electrode 121 and a collector electrode 122. The emitter electrode 121 is extends completely into the separation chamber 102. Also, the collecting electrode 122 extends completely into the separation chamber 102. The emitting electrode 121 and the collector electrode 122 are composed of plastic materials coated with electrically conductive materials. for example a metal alloy. The emitter electrode 121 and the collector electrode 122 each have a surface state whose arithmetic mean difference Ra is approximately equal to 50 μm. The emitting electrode 121 extends near the input 104. The distance separating the input 104 and the emitting electrode 121 is approximately equal to 15% of the distance separating the input 104 and the output 106. The distance separating the inlet 104 and the outlet 106 corresponds to the length L102 of the separation chamber 102. The emitting electrode 121 comprises a filiform portion which is formed by a straight wire. The transmitting electrode 121 extends generally in a direction Y121 perpendicular to a direction of flow of the mixture between the inlet 104 and the outlet 106. The wire forming the emitting electrode 121 has a circular profile, of which the diameter is approximately equal to 0.8 mm. Thus, such a filiform portion produces a significant peak effect, therefore an intense electric field. The collecting electrode 122 extends around the flow orifice 112 and around the flow orifice 113. The distance between a respective flow orifice 112 or 113 and the collector electrode 122 represents 0% of the distance between the inlet 104 and the outlet 106. The collector electrode 122 comprises an electrically conductive film completely covering the lower surface 103 of the upstream portion 102.4. The separation device 100 further comprises an electronic unit 124 which is connected to the emitter electrode 121 and to the collector electrode 122. The electronic unit 124 is configured for, during a charging phase: emitter 121 at a negative potential, so that the emitter electrode 121 generates at least one electric field E100 adapted to negatively charge drops of oil 2; the negative potential of the emitter electrode 121 can be, for example, between -5 kV and -20 kV, and bring the collector electrode 122 to a zero or positive potential, so that the collector electrode 122 collects drops of oil 2 negatively charged in the electric field E100; the zero or positive potential of the collector electrode 122 may be for example between 0 V and 12 V. The electronic unit 124 is configured for, during a charging phase, to bring the emitting electrode 121 to a negative potential substantially constant, so to generate an electrostatic field. The separating device 100 further comprises two pressure-generating members 131 and 132. The pressure-generating members 131 and 132 are arranged in the separation chamber 102 so as to delimit an upstream portion 102.4 and a downstream portion. 102.6. The upstream portion 102.4 extends from the inlet 104 to the pressure-generating members 131 and 132. The downstream portion 102.6 extends from the pressure-generating members 131 and 132 to the outlet 106. The pressure-generating members 131 and 132 are configured to generate pressure drops between the upstream portion 102.4 and the downstream portion 102.6 when gas 4 flows between the inlet 104 and the outlet 106. Each generating member load losses 131 or 132 is here formed by an obstacle. Each member generating pressure drops 131 or 132 thus produces singular pressure drops. Each pressure-generating member 131 or 132 here obstructs about 20% of the flow section of the separation chamber 102. Thus, the pressure-generating members 131 and 132 make it possible to generate a pressure difference of about 100 Pa between the upstream portion 102.4 and the oil recovery chamber 110. The pressure drop generating member 131 is disposed near the flow orifice 112. The pressure drop generating member 132 is disposed close to of the flow orifice 113. Each member generating pressure drops 131 or 132 has a height equal to 100% of the height of the upstream portion 102.4. Each pressure drop generating member 131 or 132 is contiguous with the respective flow orifice 112 or 113. Thus the distance separating a pressure drop generating member 131 or 132 from the respective flow orifice 112 or 113 here represents 0% of the distance between the input 104 and the output 106.
    [0016] The flow holes 112 are located in a lower region of the upstream portion 102.4. In the example of Figure 1, the flow holes 112 are located on the bottom of the upstream portion 102.4. The oil recovery chamber 110 is disposed below the separation chamber 102. Thus, the oil can flow through the gravitational outlets 112, in addition to the suction due to the above-mentioned pressure difference. Furthermore, the flow orifices 112 and 113 are respectively disposed on two opposite sides of the upstream portion 102.4. In the example of Figure 1, the flow port 112 is located near a side wall of the upstream portion 102.4 and the flow port 113 is located near the opposite side wall. The oil recovery chamber 110 is connected to the downstream portion 102.6 via a vacuum port 126, so that the pressure in the oil recovery chamber 110 is less than the pressure in the oil recovery chamber. upstream part 102.4. The vacuum port 126 is formed at a section of circular section tube. A flow section of the vacuum port 126 is greater than a flow section of each flow port 112 or 113. In the example of Figure 1, the ratio of i) a flow section of the depression 126 and ii) a flow section of each flow orifice 112 or 113 is approximately equal to 10. The separation device 100 further comprises a transfer member 134, which is connected to the oil recovery chamber 110. The transfer member 134 is configured to allow flow of the liquid oil to the internal combustion engine and to prevent flow of the gas 4. The transfer member 134 comprises a siphon 136 and a non-transfer pipe. represented. The transfer line is configured for an oil transfer to a motor block not shown.
    [0017] When the separation device 100 is in use, the electronic unit 124 can carry the emitter electrode 121 at a negative potential (20 kV). The emitting electrode 121 emits negative electric charges when it is polarized (brought to a negative potential).
    [0018] During a charging phase, the electronic unit 124 can carry the collecting electrode 122 at a zero potential (0 V). The collector electrode 122 attracts the negatively charged oil drops because electric fields are established between the collector electrode 122 and each of the charged oil drops. These electric fields exert electrostatic forces on each drop of charged oil. Then, the drops of oil are deposited on the collecting electrode 122, where the flow of gas passing through the flow holes 112 and 113 sucks the liquid oil to the oil recovery chamber 110. Finally, the liquid oil leaves the oil recovery chamber 110 by the transfer member 134. Figure 2 illustrates a separating device 200 according to a second embodiment of the invention. Insofar as the separating device 200 is similar to the separating device 100, the description of the separating device 100 given above in relation with FIG. 1 can be transposed to the separating device 200, with the exception of the notable differences set out below. A component of the separation device 200 which is identical or corresponding, in structure or function, to a component of the separation device 100 has the same numerical reference increased by 100. Thus, a separation chamber 202, an inlet 204, a outlet 206, an oil recovery chamber 210, two flow ports 212 and 213, an emitter electrode 221, an electronic unit 224, a vacuum outlet 226 and pressure loss generating members 231 and 232 defining an upstream portion 202.4 and a downstream portion 202.6 of the separation chamber 202, a transfer member 234 with a siphon 236. The separating device 200 differs from the separating device 100, since it comprises two collecting electrodes 222.1 and 222.2, whereas the separating device 100 comprises a single collecting electrode 122. Each of the collecting electrodes 222.1 and 222.2 is formed by an electrical band ically conductive covering a respective portion of the lower surface of the upstream portion 202.4. A portion of each electrically conductive strip is arranged around a respective flow port 212 or 213. Each of the collecting electrodes 222.1 and 222.2 extends parallel to the direction connecting the inlet 204 and the outlet 206. When the separation 200 is in use, the electronic unit 224 can carry the collecting electrodes 222.1 and 222.2 at different potentials. During a charging phase, the electronic unit 224 can carry the collecting electrodes 222.1 and 222.2 at a zero potential. Then, during a discharge phase, the electronic unit 224 can carry the collecting electrodes 222.1 and 222.2 to a negative potential, for example -10 kV. The charging phase may last longer than the discharge phase. During the discharge phase, the oil drops accumulated on the collecting electrodes 222.1 and 222.2 are discharged and are pushed back by the collecting electrodes 222.1 and 222.2, so that they flow easily through the outlets 212 and 213. In addition, the electronic unit 224 can operate in a delayed manner the charging and discharging phases of the collecting electrodes 222.1 and 222.2, which makes it possible to continue to charge drops of oil with the collecting electrode 222.1 to a zero potential, while drops of oil are discharged when the collecting electrode 222.2 is at a negative potential. Thus, the electronic unit 224 makes it possible to constantly charge drops of oil while effectively evacuating the oil. Figures 3, 4 and 5 illustrate a separation device 300 according to a third embodiment of the invention. Insofar as the separating device 300 is similar to the separating device 200, the description of the separating device 200 given above in relation to FIG. 2 can be transposed to the separating device 300, with the exception of the differences. notables set out below. A component of the separation device 300 which is identical or corresponding, in structure or function, to a component of the separating device 200 has the same increased numeral number of 100. Thus, a separation chamber 302, an inlet 304, is defined. an outlet 306, an oil recovery chamber 310, two flow ports 312 and 313, two collecting electrodes 322.1 and 322.2, an electronic unit 324, a vacuum opening 326 and pressure loss generating members 331 and 332, as well as a transfer member 334.
    [0019] The separation device 300 differs from the separation device 200 because it comprises three emitter electrodes 321, whereas the separation device 200 comprises a single emitter electrode 221. The emitter electrodes 321 are formed by filiform portions arranged substantially parallel to one another. In addition, the separation device 300 differs from the separation device 200 because it comprises two auxiliary electrodes 340. The auxiliary electrodes 340 are connected to the electronic unit 324. The electronic unit 324 is configured for, during a charging phase , bring the auxiliary electrodes 340 to a zero potential. The auxiliary electrodes 340 are arranged closer to the emitting electrodes than the collecting electrodes 322.1 and 322.2, so that an electric field E300 established between the emitting electrodes and the auxiliary electrodes 340 is more intense than an electric field established between the emitting electrodes. 321 and the collecting electrodes 322.1 and 322.2. The auxiliary electrodes 340 are formed by auxiliary filiform portions which are arranged substantially parallel to each other and to the emitter electrodes 321. The auxiliary electrodes 340 are arranged upstream of the emitting electrodes 321.
    [0020] As shown precisely in FIGS. 4 and 5, the auxiliary electrodes 340 and the emitting electrodes 321 are arranged in staggered rows. Each auxiliary electrode 340 is thus located opposite an interval delimited by two consecutive emitting electrodes 321. In use, this staggered arrangement makes it possible to increase the path length of the oil drops 2 in the electric field E300 between each emitting electrode 321 and each auxiliary electrode 340. Thus, the drops of oil 2 undergo a longer charging time. long, so that they are loaded more intensely or in greater numbers. As shown in FIG. 3, the distance 321.340 between an adjacent auxiliary electrode 340 and a transmitting electrode 321 is approximately equal to 10% of the distance 321.322 between this emitter electrode 321 and the closest collector electrode 322.1 or 322.2. Furthermore, the separation device 300 differs from the separation device 200, because the collecting electrodes 322.1 and 322.2 have a three-dimensional geometry, while the collecting electrodes 222.1 and 222.2 have a flat geometry. Indeed, each collecting electrode 322.1 or 322.2 1 comprises i) a peripheral electrically conductive film which extends around a respective flow port 312 or 313, and ii) two adjacent electrically conductive films which are arranged to extend the electrically conductive peripheral film and extend substantially vertically when the separation device 300 is in the service position (Figure 3).
    [0021] Each collecting electrode 322.1 or 322.2 1 is thus formed of three strips which are contiguous on edges and which each extend in a respective plane. The three strips forming the collecting electrode 322.1 respectively follow the shape of the lower surface of the separation chamber 302, a plane side wall and the pressure drop generating member 331. FIG. 6 illustrates a separation device 400 according to a fourth embodiment of the invention. Insofar as the separation device 400 is similar to the separation device 300, the description of the separation device 300 given above in connection with FIGS. 3, 4 and 5 can be transposed to the separation device 400, to the except for the notable differences set out below. A component of the separation device 400 which is identical or corresponding in structure or function to a component of the separation device 300 has the same numerical reference increased by 100. Thus, a separation chamber 402, an inlet 404, a outlet 406, an oil recovery chamber 410, two flow orifices 412 and 413, emitter electrodes 421, an electronic unit 424, a vacuum port 426, auxiliary electrodes 440, and loss generating members. 431 and 432, and a transfer member 434. As shown in Figure 6, the separation device 400 differs from the separation device 300, because the two collecting electrodes 422.1 and 422.2 are shorter than the two collecting electrodes 322.1 and 322.2. The length of each collecting electrode 422.1 or 422.2 represents about 15% of the length of each collecting electrode 322.1 and 322.2, the lengths being measured parallel to the length of the separation chamber 402 (see L102 in FIG. 1). The length of the separation chamber 402 corresponds to the distance separating the entry 104 and the exit 106.
    [0022] Since the collecting electrodes 422.1 and 422.2 are shorter than the collecting electrodes 322.1 and 322.2, all things being equal, the electric fields between the emitting electrodes 421 and the auxiliary electrodes 440 are much more intense than between the emitting electrodes 421 and the collecting electrodes 422.1 and 422.2. This makes it possible to increase the number of charged drops of oil 2 and the charge of each drop of oil 2 before the drops of oil 2 arrive near the collecting electrodes 422.1 and 422.2. On the other hand, as shown in FIGS. 7 and 8, the periphery of each flow orifice 412 or 413 is formed by four acute edges which each comprise two ridges 415 and 416. The ridges 415 and 416 each have a radius of curvature about 0.1 mm. Moreover, as shown in FIG. 8, each collecting electrode 422.1 or 422.1 extends to the inside of a respective flow port 412 or 413. Thus a respective collector electrode 422.1 or 422.2 covers the sharp edges forming the periphery of each flow orifice 412 or 413. Thus, the ridges 415 and 416 produce a peak effect, which makes it possible to generate relatively intense electric fields between the charged oil drops 2 and the respective collecting electrode 422.1 or 422.2. The ridges 415 and 416 are connected by a rounded fillet 417 with an arcuate section. The rounded fillet 417 here has a radius of about 1 mm. Each collecting electrode 422.1 or 422.2 covers the acute edges and the rounded fillet 417. Thus, the rounded fillet 417 produces a reverse peak effect, which allows the generation of relatively intense electric fields between the charged oil drops 2 and the collector electrode 422.1 covering the rounded fillet 417. Figure 9 illustrates a separating device 500 according to a fifth embodiment of the invention. Insofar as the separating device 500 is similar to the separating device 400, the description of the separating device 400 given above in relation to FIG. 6 can be transposed to the separating device 500, with the exception of the differences. notables set out below. A component of the separation device 500 which is identical or corresponding, in structure or function, to a component of the separation device 400 has the same numerical reference increased by 100. Thus, a separation chamber 502, an inlet 504, is defined. an outlet 506, an oil recovery chamber 510, emitter electrodes 521, an electronic unit 524, a vacuum port 526, auxiliary electrodes 540 and charge loss generating members 531 and 532, and a transfer member 534. The separating device 500 differs from the separating device 400 since the separating device 500 has four outlets 512.1, 512.2, 513.1 and 513.2; while the separating device 400 has two outlets 412 and 413. Similarly, the separating device 500 differs from the separating device 400, since the separating device 500 comprises four collecting electrodes 522; while the separating device 400 comprises two collecting electrodes 422.1 and 422.2. Two outlets 512.1 and 512.2 are disposed on one side 20 of the upstream portion and two outlets 513.1 and 513.2 are disposed on the other side of the upstream portion. Since the collecting electrodes 522 extend around the flow orifices 512.1, 512.2, 513.1 and 513.2, two collecting electrodes 522 are arranged on one side of the upstream part and two collecting electrodes 522 are arranged on the other side. side of the upstream part. Like the separating device 400, the separating device 500 comprises an even number of flow orifices and the flow orifices are arranged in equal numbers on each side of the upstream part. On the other hand, in the example of FIG. 9, the separation chamber 502 has an axis of symmetry X500. The outlets 512.1, 512.2, 513.1 and 513.2 are arranged symmetrically on each side of the axis of symmetry X500.
    [0023] In addition, the separation device 500 differs from the separation device 400, because the separation device 500 comprises six pressure loss generating members, while the separation device 400 comprises two loss-generating members 431 and 432. Indeed, the separation device 500 comprises: two primary pressure loss generating members 531 and 532, which are identical to the two pressure loss generating members 431 and 432, plus four secondary loss-generating members 541.1, 10 541.2,542.1 and 542.2. The secondary pressure drop generating members 541.1, 541.2, 542.1 and 542.2 are respectively arranged around the outlets 512.1, 512.2, 513.1 and 513.2. Each of the four secondary pressure drop generating members 541.1, 541.2, 542.1 and 542.2 makes it possible to reduce the gas velocities near the outlets 512.1, 512.2, 513.1 and 513.2; while the two primary pressure drop generating members 531 and 532 rather make it possible to generate a pressure difference between the upstream portion of the separation chamber 502 and the oil recovery chamber 510. When the separation device 500 is in use, the electronic unit 524 can carry the collecting electrodes 522 at different potentials. As described above with reference to FIG. 2, the electronic unit 524 can operate in a delayed manner the charging and discharging phases of the collecting electrodes 522. For example, three collecting electrodes 522 can be brought to a zero potential ( charge phase), while the fourth collector electrode 522 is brought to a negative potential (discharge phase) to repel the charged oil drops to the corresponding flow port 512.1, 512.2, 513.1 or 513.2. Then, the electronic unit 524 discharges the other collecting electrodes 522, each in turn. This makes it possible to continue to charge drops of oil with three collecting electrodes 522, while drops of oil are discharged when the fourth collector electrode 522 is at a negative potential. Thus, the electronic unit 524 makes it possible to constantly load drops of oil while effectively evacuating the oil. Figure 10 illustrates a separation device 600 according to a sixth embodiment of the invention. Insofar as the separation device 600 is similar to the separation device 500, the description of the separation device 500 given above in relation to FIG. 9 can be transposed to the separation device 600, except for the notable differences. set out below. A component of the separation device 600 which is identical or corresponding, in structure or function, to a component of the separation device 500 has the same numerical reference increased by 100. Thus, a separation chamber 602, an inlet 604, a outlet 606, an oil recovery chamber 610, flow orifices 612, 613 and the like, emitter electrodes 621, collecting electrodes 622, an electronics unit 624, a vacuum port 626, auxiliary electrodes 640 and primary and secondary charge loss generating bodies 641 and 642. The separation device 600 further comprises a transfer member (not shown) which is similar, but not its function, to the transfer member 534.
    [0024] The separation device 600 differs from the separation device 500, because the separation chamber 602 has the overall shape of a circular cylinder, while the separation chamber 502 has the overall shape of a parallelepiped. Likewise, the separation device 600 differs from the separation device 500, since the oil recovery chamber 610 generally has the shape of a circular tube disposed around the separation chamber 602, whereas the recovery chamber of oil 510 has the overall shape of a parallelepiped arranged under the separation chamber 502. In addition, the separation device 600 differs from the separation device 500, since the emitting electrodes 621 and the auxiliary electrodes 640, formed by filiform portions, are arranged substantially parallel to each other and to the axis of the cylinder defining the separation chamber 602, thus substantially parallel to the flow direction of the mixture between the inlet 604 and the outlet 606. On the contrary, the emitting electrodes 521 and the Auxiliary electrodes 540 extend perpendicular to the flow direction of the mixture between the inlet 504 and the outlet 506. even the separation device 500, the separation device 600 has four flow orifices, two of which are visible in Figure 10 with the references 612 and 613 and two of which are not shown. The two flow orifices are situated respectively opposite the flow orifices 612 and 613 with respect to the axis of the cylinder forming the separation chamber 602. Moreover, the mixture is introduced into the separation device 600. by a 90 degree elbow. Figure 11 illustrates a separation device 700 according to a sixth embodiment of the invention. Insofar as the separating device 700 is similar to the separating device 600, the description of the separating device 400 given above in relation with FIG. 10 can be transposed to the separating device 700, except for the differences. notables set out below. A component of the separating device 700 which is identical or corresponding in structure or function to a component of the separating device 600 bears the same increased numeral number of 100. Thus, a separation chamber 702, an inlet 704, is defined. an outlet 706, an oil recovery chamber 710, an electronic unit 724, a vacuum port 726, a primary pressure drop generating member 731, and a transfer member 734. As shown in FIG. 9, the separation device 700 differs from the separation device 600 because the separation device 700 comprises a single emitter electrode 721 formed by a wire extending all the way through the separation chamber 702 and which is collinear with the axis of the cylinder forming the separation chamber 702, because the separation device 700 comprises a single collecting electrode 722, since the separation device 700 comprises a a single flow orifice 712, which has an annular shape, since the separating device 700 comprises a single pressure-loss generating member 731, which has an annular shape, and since the separating device 700 does not comprise any auxiliary electrode 740.
    [0025] FIG. 12 illustrates a separation process 1000 for separating oil drops 2 from a mixture comprising gas 4 and drops of oil 2 coming from an internal combustion engine. The separation method 1000 comprises the steps of: - 1002) implementing a separation device according to one of the embodiments described above, - 1004) during a charging phase, controlling the electronic unit so that: - 1006) the or each emitter electrode generates at least one electric field adapted to negatively charge drops of oil, and - 1008) the or each collector electrode collects negatively charged oil drops, and - 1010) allow entry mixing in the separation chamber. Of course, the present invention is not limited to the particular embodiments described in the present patent application, nor to embodiments within the scope of those skilled in the art. Other embodiments may be envisaged without departing from the scope of the invention, from any element equivalent to an element indicated in the present patent application.
    权利要求:
    Claims (25)
    [0001]
    REVENDICATIONS1. Separating device (100; 200; 300; 400; 500; 600; 700) for separating oil droplets (2) from a mixture comprising gas (4) and drops of oil (2) and derived from an internal combustion engine, the separation device (100 - 700) comprising at least: - a separation chamber (102 - 702) having i) an inlet (104 - 704) configured for the entry of the mixture into the separation chamber (102 - 702), and ii) an outlet (106 - 706) arranged for the outlet (106 - 706) of the gas out of the separation chamber (102 - 702), - an oil recovery chamber (110 - 710) connected to the separation chamber (102 - 702) via at least one flow port (112, 113 - 712) so that liquid oil can flow from the separation chamber (102 - 702) to the oil recovery chamber (110 - 710) through the at least one flow orifice (112, 113 - 712), - at least one emitting electrode (121 -721). ) extends at least partially in the separation chamber (102 - 702), - at least one collecting electrode (122 - 722) extending at least partially in the separation chamber (102 - 702), and - an electronic unit (124). - 724) connected to said at least one emitter electrode (121 -721) and said at least one collector electrode (122 - 722), the electronic unit (124 - 724) being configured for, at least during a charging phase - bringing said at least one emitter electrode (121 -721) to a negative potential, so that said at least one emitting electrode (121 -721) generates at least one electric field (E100; E300) adapted to negatively charge oil drops (2), and - bringing said at least one collector electrode (122 - 722) to a null or positive potential, so that said at least one collector electrode (122 - 722) collecting droplets of oil (2) negatively charged, the separating device (100-700) being characterized in that it furthermore comprises at least one pressure loss generating member (131, 132-231) arranged in the chamber of separation (102 - 702) so as to delimit an upstream portion (102.4; 202.4) and a downstream portion (102.4; 202.4), the pressure drop generating member (131, 132 - 731) being configured to generate losses between the upstream portion (102.4; 202.4) and the downstream portion (102.4; 202.4) when gas flows between the inlet (104 - 704) and the outlet (106 - 706), and that the chamber oil recovery (110 -710) is connected to the downstream part (102.4; 202.4) via at least s a vacuum port (126 - 726), so that the pressure in the oil recovery chamber (110-710) is lower than the pressure in the upstream portion (102.4; 202.4).
    [0002]
    The separation device (100-700) according to claim 1, wherein said at least one emitting electrode (121 -721) and said at least one collector electrode (122-722) are at least partially composed of electrically conductive materials, and wherein said at least one emitter electrode (121 -721) and said at least one collector electrode (122-722) each have a surface state whose arithmetic average deviation Ra is between 0.1 μm and 100 μm.
    [0003]
    The separation device (100-500) according to any one of the preceding claims, wherein said at least one emitting electrode (121-521) extends near the input (104-504).
    [0004]
    4. Separation device (100-700) according to any one of the preceding claims, wherein said at least one emitting electrode (121 -721) comprises at least one filiform portion.
    [0005]
    Separating device (100 - 500) according to claim 4, wherein at least one filiform portion extends in a direction transverse to a direction of flow of the mixture between the inlet (104 - 504) and the outlet ( 106 - 506).
    [0006]
    6. separating device (100 - 700) according to any one of claims 4 to 5, comprising at least two emitter electrodes (321 - 621), the filiform portions being arranged substantially parallel to each other.
    [0007]
    The separation device (300 - 600) according to any one of the preceding claims, further comprising at least one auxiliary electrode (340 - 640) connected to the electronic unit (324 - 624), the electronic unit (324). - 624) being configured for, at least during a charging phase, bringing said at least one auxiliary electrode (340 - 640) to a zero or positive potential, said at least one auxiliary electrode (340 - 640) being arranged closer to said at least one emitter electrode (321 - 621) as said at least one collector electrode (322 - 622), so that an electric field established between said at least one emitter electrode (321 -621) and said at least one electrode auxiliary (340 - 640) is more intense than an electric field established between said at least one emitter electrode (321 - 621) and said at least one collector electrode (322 - 622).
    [0008]
    8. Separating device (300 - 500) according to claims 6 and 7, comprising at least two auxiliary electrodes (340-540) formed by auxiliary filiform portions and arranged substantially parallel to each other and to the emitting electrodes (321 -521), the auxiliary electrodes (340-540) and the emitting electrodes (321-521) being staggered.
    [0009]
    9. separation device (300 - 600) according to any one of claims 7 to 8, wherein said at least one auxiliary electrode (340 - 640) is arranged upstream of said at least one emitting electrode (321 -621) .
    [0010]
    The separation device (100-700) according to any one of the preceding claims, wherein a flow section of said at least one vacuum port (126-726) is greater than a flow section of said at least one port of flow (112, 113 - 712).
    [0011]
    The separation device (100-700) according to any one of the preceding claims, wherein said at least one flow orifice (112, 113 -712) is located in a lower region of the upstream portion (102.4; 202.4 ), for example on the bottom of the upstream part (102.4; 202.4).
    [0012]
    The separation device (100-700) according to any one of the preceding claims, wherein said at least one flow orifice (112, 113-712) is located near or in a respective side wall of the upstream portion. (102.4, 202.4).
    [0013]
    13. separating device (100 -700) according to any one of the preceding claims, comprising at least two outlets (112, 113 -612, 613) respectively disposed on two opposite sides of the upstream portion (102.4; 202.4 ), for example respectively close to two opposite side walls of the upstream portion (102.4; 202.4).
    [0014]
    The separation device (100-700) according to any one of the preceding claims, wherein said at least one collection electrode (122-722) extends near said at least one flow port (112, 113 - 712). ).
    [0015]
    15. separating device (100 - 700) according to claims 13 and 14, comprising at least two outlets (112, 113 -612, 613) and at least two collecting electrodes (222.1, 222.2 - 522), each electrode collector (122 - 722) extending near a respective flow port (112, 113-712).
    [0016]
    The separation device (100-700) according to any of the preceding claims, wherein said at least one electrodecollector (122-722) comprises an electrically conductive film, said at least one electrically conductive film at least partially covering a surface lower portion of the upstream portion (102.4; 202.4).
    [0017]
    The separation device (100 - 700) according to one of claims 14 to 15 and claim 16, wherein said at least one collecting electrode (122 -722) comprises: - a peripheral electrically conductive film extending around said at least one flow orifice (112, 113 - 712), and - at least one adjacent electrically conductive film arranged to extend the peripheral electrically conductive film and to extend substantially vertically when the separation device (100- 700) is in the service position.
    [0018]
    The separation device (400) according to any one of the preceding claims, wherein said at least one flow orifice (412, 413) has at least one acute edge including an edge (415, 416) having a radius of curvature less than 0.2 mm, and wherein said at least one collecting electrode (422) covers said at least one acute edge.
    [0019]
    The separation device (400) according to claim 18, wherein said at least one acute edge comprises two ridges (415, 416) having a radius of curvature of less than 0.2 mm, both ridges (415, 416) being connected by a rounded fillet (417), for example with an arcuate section, the rounded fillet (417) having a radius greater than 0.5 mm, preferably greater than 1 mm, said at least one collecting electrode (422) covers acute edges and rounded fillet (417).
    [0020]
    Separating device (100-700) according to any of the preceding claims, wherein said at least one pressure drop generating member (131, 132-731) is disposed near a respective flow orifice ( 112, 113-712).
    [0021]
    21. separating device (100 -700) according to any one of the preceding claims, wherein said at least one loss-generating member (131, 132 - 731) is formed by an obstacle.
    [0022]
    22. separating device (100 - 500) according to any one of the preceding claims, wherein the separation chamber (102 - 502) has the overall shape of a parallelepiped, for example rectangular base, and wherein the chamber oil recovery (110 - 510) has generally the shape of a parallelepiped, for example rectangular base.
    [0023]
    The separating device (600 - 700) according to any one of claims 1 to 21, wherein the separation chamber (602 - 702) has the overall shape of a cylinder, for example a circular base, and wherein the oil recovery chamber (610 - 710) is generally in the form of a tube disposed around the separation chamber (602 - 702).
    [0024]
    24. Separation device (100 - 500) according to any one of the preceding claims, further comprising a transfer member (134-534) connected to the oil recovery chamber (110-710), the transfer (134-534) being configured to allow flow of the liquid oil to the internal combustion engine and to prevent flow of gas from the internal combustion engine to the oil recovery chamber (110-710).
    [0025]
    25. Separation process (1000), for separating oil drops from a mixture comprising gas and oil drops and coming from an internal combustion engine, the separation process (1000) comprising the steps of: - (1002) implement a separation device (100 - 700) according to any one of the preceding claims, - (1004) during a charging phase, control the electronic unit so that: - (1006) said at least one emitting electrode generates at least one electric field adapted to negatively charge drops of oil, and - (1008) said at least one collector electrode collects negatively charged oil drops, and - (1010) allow the entry of the mixing in the separation chamber.
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    优先权:
    申请号 | 申请日 | 专利标题
    FR1459387A|FR3026660B1|2014-10-01|2014-10-01|DEVICE FOR SEPARATING OIL DROPS IN A GAS AND OIL MIXTURE AND SEPARATION METHOD USING SUCH A SEPARATION DEVICE|FR1459387A| FR3026660B1|2014-10-01|2014-10-01|DEVICE FOR SEPARATING OIL DROPS IN A GAS AND OIL MIXTURE AND SEPARATION METHOD USING SUCH A SEPARATION DEVICE|
    JP2015195869A| JP6611541B2|2014-10-01|2015-10-01|Equipment for separating oil droplets in a gas oil mixture|
    US14/872,677| US9901933B2|2014-10-01|2015-10-01|Device for separating oil drops in a mixture of gas and oil and a separation method implementing such a separator device|
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