Conical filter element with funnel directing particles to a trap

Abstract

The invention relates to a filter element (1, 31) for use as a particulate filter in a cooling circuit (100), in particular of an electrochemical energy converter, having a conical grid support structure (3, 33). The filter element features at a first axial end a supply opening (23, 49) for supplying a cooling medium to be filtered into the filter element (1, 31) and the grid support structure (3, 33) carries a filter medium (4, 34). The filter element (1, 31) has axially opposite the supply opening (23, 49) a funnel (16, 40) for axially discharging and collecting particulate impurities, and is closed at second axial end. The conical grid support (3, 33) structure tapers from the first axial end to the second axial end. An arrangement of a fuel cell (102) having a a cooling circuit (100) with the filter element is disclosed.

Claims

1. A conical particulate filter element comprising: a conically shaped grid support structure tapering from a first open end to a second end, and defining an interior space; a filter medium fixedly supported by said conically shaped grid support structure; a collection chamber disposed at, and closing, said second end of said of said conically shaped grid support structure; and a funnel having a solid frustoconical sidewall with openings at either end, is disposed within said interior space and positioned to direct particulate through said funnel and into said collection chamber; wherein a fluid to be filtered is introduced into said interior space through said open end, with particulates above a predetermined size being prevented from passing through said filter medium, and at least some particulates entering said funnel and being directed into said collection chamber.

2. The conical particulate filter element according to claim 1, wherein the filter medium is a screen mesh selected from the group consisting of: a metal mesh or a steel screen mesh.

3. The conical particulate filter element according to claim 2, wherein an average mesh width of the screen mesh is between 70 μm and 120 μm.

4. The conical particulate filter element according to claim 1, wherein the collection chamber is within an end cap or an end cap segment.

5. The conical particulate filter element according to claim 4, wherein the end cap or end cap segment is integrally formed with said conically shaped grid support structure.

6. The conical particulate filter element according to claim 4, wherein the end cap or end cap segment is detachably connected with said conically shaped grid support structure.

7. The conical particulate filter element according to claim 6, wherein the end cap or end cap segment is threadably connected to said conically shaped grid support structure.

8. The conical particulate filter element according to claim 1, wherein the funnel consists of a plastic material.

9. The conical particulate filter element according to claim 1, wherein the funnel includes at least one support member extending downwardly from its radially outer circumferential edge and substantially parallel to a central longitudinal axis of said funnel.

10. The conical particulate filter element according to claim 9, wherein said at least one support member comprises a plurality of support feet spaced apart from each other.

11. The conical particulate filter element according to claim 9, wherein said at least one support member comprises a cylinder.

12. The conical particulate filter element according to claim 11, wherein said cylinder includes at least one return flow opening, which serves to return any fluid flowing into the collection chamber through the funnel back to the interior space, while particles remain in the collecting chamber.

13. The conical particulate filter element according to claim 1, wherein said funnel openings include a first inlet opening having an inlet diameter and a second outlet opening having an outlet diameter; wherein the inlet diameter is at least 20% larger than the outlet diameter.

14. The conical particulate filter element according to claim 1, wherein the screen mesh is encapsulated and/or over-molded with a material of the grid support structure.

Description

BRIEF DESCRIPTION OF DRAWINGS

(1) In the following, the subject of this invention is explained in more detail using several examples of an embodiment and with the aid of the accompanying figures. The examples of an embodiment shown are particularly advantageous, but are not to be understood in a restrictive way of the subject matter of the present invention. Individual features can be transferred to different variants of a filter element that are not displayed. It is shown in:

(2) FIG. 1: a perspective representation of the cooling circuit of an electrochemical energy converter, in particular of a fuel cell;

(3) FIG. 2: a lateral sectional view of a first variant of an embodiment of a filter element according to the invention;

(4) FIG. 3: a perspective view of the filter element with removed flow guidance;

(5) FIG. 4: a perspective sectional view of the filter element with removed flow guidance;

(6) FIG. 5: a perspective sectional view of the filter element with integrated flow guidance;

(7) FIG. 6: a perspective sectional view of the flow guidance;

(8) FIG. 7: a sectional view of a second variant of an embodiment of a filter element according to the invention; and

(9) FIG. 8: a perspective view of the filter element of FIG. 7.

EMBODIMENT(S) OF THE INVENTION

(10) FIG. 1 shows a cooling circuit 100 for cooling an electrochemical energy converter, preferably in the form of a fuel cell 102 or a stack of several fuel cells. Other electrochemical energy converters can also be cooled in this way. The structure of a fuel cell is known per se. It comprises an anode 104 and a cathode 105 separated by an electrolyte, e.g. a semi-permeable membrane. This semi-permeable membrane can be permeable to protons. Energy is generated by a reaction of hydrogen with oxygen.

(11) The oxygen can be provided by an air inlet 111, e.g. as pure oxygen or as ambient air, or by a liquid medium, e.g. water. The oxygen or air can be moistened with water, for example, before it is fed into the fuel cell 102. To increase the humidity of the gas introduced, e.g. air or oxygen, the cooling circuit features a humidifier 103, which increases the air humidity before introducing it into the fuel cell 102.

(12) In addition to the air inlet 111, the fuel cell 102 features also an inlet for fuel 106, in particular hydrogen. Furthermore, the fuel cell 102 features a supply line 114 for a coolant, e.g. deionized water. The supply line 111 is part of the cooling circuit 100.

(13) The fuel cell 102 features also a discharge line 112 for exhaust gas or exhaust air and a discharge line 115 for the coolant from the fuel cell 102. The discharge line features a three-way valve 113. Depending on the circuit of the three-way valve 113, the coolant can be supplied to a heat exchanger 108 or to a bypass line 107 bypassing the heat exchanger 108. Furthermore, a cooling tank 109 can be provided on the discharge line 115 for the expansion of the coolant, which compensates for temperature-related pressure fluctuations of the coolant. A coolant pump 110 increases the coolant pressure before it is introduced into the fuel cell 102.

(14) The above-mentioned example of an embodiment of a fuel cell 102 and an associated cooling circuit 100 is only to be understood as an example. A hydrocarbon such as alcohols, e.g. methanol or ethanol, can also be used as fuel instead of hydrogen.

(15) A filter element 101, which filters out particulate impurities from the coolant, especially during commissioning or after refilling with coolant, is disposed on the supply line of the coolant to the fuel cell.

(16) Current filter elements used for the application often include a filter medium for depth filtration allowing the dirt contained in the fluid to be filtered out of the coolant or coolant liquid. As a result, the dirt adheres firmly both inside and on the surface of the medium to the fibers located there and thus reduces the free cross-section of the medium above a certain amount of dirt, so that less flow cross-section is available for the volume flow and the pressure loss of the cooling medium due to the filter element increases over the course of time the filter element is in operation.

(17) The filter element according to the invention, for example in the variants of an embodiment of FIGS. 2 to 6 and FIGS. 7 to 8, feature a clearly lower pressure loss over the operating time.

(18) FIGS. 2 to 8 show a first variant of an embodiment of a filter element 1 according to the invention which is arranged in a pipe 2. Pipe 2 has a terminal protrusion 20 for connection to filter element 1. In addition, the pipe 2 features a pipe connection 21 for connecting the pipe 2 to a process line of a cooling circuit, e.g. the cooling circuit 100 of FIG. 1. The connection can be made, for example, by slipping a hose over it and then fastening it using hose clamps.

(19) The filter element 1 features a grid support structure 3 with a cone-shaped course along its longitudinal axis A. The grid support structure 3 defines several grid windows 14 in which the filter medium 4 is disposed. The filter medium 4 is a screen mesh for separating particulate impurities in an interior space 10 of the filter element 1, which is limited by the grid support structure 3.

(20) The grid support structure 3 features an end cap segment 8 closed to the exterior side of the filter element, which is an integral part of the grid support structure 3 in FIGS. 2 to 6. However, it is possible and advantageous to return the cooling medium towards the interior space 10.

(21) The grid support structure 3 features annular struts 5, which extend transversely, in particular vertically, to the longitudinal axis A, and which decrease in ring diameter in the course of the longitudinal axis A towards the end cap segment 8. The annular struts 5 are connected to each other by longitudinal struts 15 and form a circumferential surface with a conical course.

(22) Opposite the closed-wall end cap segment 8, the filter element 1 features at the end a union 7 with a supply opening 23 for connection to a process line of the aforementioned cooling circuit and for supplying coolant to filter element 1. This union 7 extends from an annular closed-wall pipe segment 22. This pipe segment 22 features an annular circumferential projection 6 to the stop and to the circumferential mould closure with the protrusion 20 of pipe 2. The projection 6 can be connected, e.g. by welding, to the protrusion 20 of the pipe 2 in a circumferential material-locking manner.

(23) Between the end cap segment 8 and the pipe segment 22 are disposed the grid windows 14 with the filter medium 4. The end cap segment 8 features stop surfaces 12 for the stop of a flow guidance 9 inserted in the end cap segment 8.

(24) This flow guidance 9 is shown in detail in FIG. 6. It can preferably be disposed detachably in the end cap segment 8. It features a funnel 16 with a funnel axis extending coaxially to the longitudinal axis A of the grid support structure. The funnel features a larger first funnel opening 17 and a smaller second funnel opening 18. The funnel 16 together with the end cap segment 8 defines a collecting chamber 13 to receive the filtered particulate impurities.

(25) The larger funnel opening 17 is disposed in an inlet area of the end cap segment 8 and the smaller funnel opening 18 leads into the collecting chamber 13.

(26) Support members 11, which extend parallel to the funnel axis at the edge of the funnel 16, relative to its radially outer circumferential edge, and which are preferably connected to the funnel 16 in a material-locking manner, are disposed on the funnel 16. In FIGS. 2 to 6, the support members 11 are designed as support feet spaced apart from each other. The gaps 19 between the support feet also serve as backflush openings for the medium to flow out of the collecting chamber 13 while the particles remain in the collecting chamber 13. The support members 11 rest on the stop surfaces 12.

(27) The funnel serves as separation 16 between the collecting chamber 13 for particles or dirt and the actual filter medium 4. This funnel allows the particles arriving in the fluid to enter the collecting chamber in its funnel center and at the same time prevents the particles from being flushed back towards the filter medium 4.

(28) FIGS. 7 and 8 feature a second variant of an embodiment of a filter element 31 according to the invention. It is clamped between two pipes 51 and 52, which are connected to each other via a flange connection 54. The flange connection 54 features a first sealing ring 53 for radial sealing. Terminally, i.e. at an opposite end to the flange connection 54, one pipe flange 55, 56 is disposed at each pipe 51, 52 for the connection to a process line.

(29) The filter element 31 itself can be designed in three parts, comprising a grid support structure 33 with a longitudinal axis A with circumferential struts 35, which are connected to each other by longitudinal struts and define a circumferential surface as well as an interior space 41 enclosed by it. In the grid windows of the grid support structure or along the circumferential surface, a filter medium 34, in particular a screen mesh, is disposed.

(30) Terminally, the grid support structure 33 features a closed-wall pipe segment 37 with an annular circumferential projection 36. This projection can feature an annular groove to accommodate a sealing ring for the radial seal, as shown in FIGS. 7 and 8.

(31) The grid support structure 33 is terminally open on one side and features on the other side an interface 32 to an end cap 38, which is detachably disposed on the grid support structure 33. The interface 32 is in this case a screw thread. The end cap, in conjunction with the grid support structure 33, forms a collecting chamber 43 for particles.

(32) Between the grid support structure 33 and the end cap 38 a flow guide component 39 is disposed, in particular clamped or screwed.

(33) In analogy to FIGS. 2 to 6, this flow guidance also features a funnel 40, which enables dirt to be discharged towards the collecting chamber.

(34) The grid support structure 33 features a supply opening 49 into the filter element 31 and a discharge opening at the transition to the flow guidance 39. Preferably, the diameter of the supply opening 49 is at least twice as large as the diameter of the discharge opening 50.

(35) The funnel 40 features a circumferential cylindrical support member 42 at the edge, which can support itself on a stop surface 46 of the end cap 38 against axial displacement in the mounted state.

(36) The support member 42 features return flow openings 43 at the edge, which serve to return the medium flowing in through the funnel 40, while the particles remain in the collecting chamber 43. Accordingly, the return flow openings 43 should be advantageously at least smaller than the inflow opening of the funnel 40.

(37) In FIGS. 2 to 8, the funnel 16, 40 features an inwardly rounded shape, which has additional fluidic advantages.

(38) The funnel 16, 40 shown in FIGS. 2 to 8 can, for example, feature an inlet diameter of 35-45 mm and an outlet diameter of 20-30 mm for the exit into the collecting chamber 13, 43. The inlet diameter is particularly preferably to be at least 20%, preferably at least 25% larger than the outlet diameter.

(39) The internal diameter of the end cap or end cap segment can be between 40-50 mm. It is advantageously at least 30% larger than the outlet diameter.

(40) The length of the filter element 1, 31 can preferably be between 100 mm and 230 mm, preferably between 130 mm and 200 mm.

(41) The supply opening 49 into the filter element 31 and in analogy also the supply opening 23 for the filter element 1 can preferably feature a diameter between 14 and 20 mm, preferably between 15 and 18 mm.

(42) The filter medium 4, 34 can be particularly preferably designed as screen mesh, preferably made of stainless steel, e.g. high-grade steel. The average mesh width of the filter medium, in particular of the screen mesh, can preferably be more than 70 μm, in particular between 80 and 150 μm, in particular between 100 and 120 μm.

(43) FIGS. 2 to 8 show only two preferred design variants of an embodiment. It is also conceivable that the funnel is part of the filter medium 4, 34, which can be inserted as a separate component of the filter element into the grid support structure.

(44) The filter elements shown in FIGS. 2 to 8 each provide a collecting chamber 13, 43 for the dirt which is located outside the flow cross-section and thus does not restrict it. Thus, more dirt can be filtered out than with a conventional filter medium. An increase in pressure during operation does not occur or occurs only to a very small extent.

(45) This means that a relatively large dirt capacity can be made available in a smaller installation space with relatively little filtration area. In addition, the mesh used as screen mesh without depth filtration offers an advantage in pressure loss for the high volume flows that can occur in a cooling circuit of an electrochemical energy converter, for example in the 250 l/min range.

(46) The conical shape of the filter is also advantageous for the dirt particles. They slide along the mesh and then are flushed into the collecting chamber, in addition to the particles that have already reached it directly.