MULTISTAGE FLUID FILTER AND METHOD

Abstract: A fluid filter (10) comprises a plurality of separate filtra­ tion chambers (14-18) with a fluid inlet (12) and a fluid outlet (13). All of the filtration chambers (14-18) are identical and each contain two vertically-spaced doors (28, 29) on one end and two similarly vertically-spaced doors (30, 31) on the other end. In addition, each of the filtration chambers (14-18), includes a trap door through which accumulated particulate matter is discharged. The filtration chambers (14-18) are defined as first and second filtration stages and a cleaning stage. By sequencing the opening and closing of doors (28, 29, 30 and 31) the interconnection between the filtration chambers (14-18) is changed. As particulate mat­ ter is accumulated on the inner surface of a filtration medi­ um (25) the first and second filtration stages and cleaning stages are changed so that each of the chambers (14-18), in turn, serve as all or part of the first filtration stage, second filtration stage and cleaning stage. Accordingly, the filter can operate continuously after a filter layer is accumulated on the filter medium in any one of the filtration chambers without a significant decrease in filtration efficiency.

Description: Technical Field and Background of the Invention This invention relates to a multistage fluid filter for filtering entrained particulate matter from a moving fluid stream and a method for filtering fluids to remove entrained particulate matter. In particular, the application discloses a multistage fluid filter wherein enhanced filtration efficiency is achieved by sequentially redefining filtration zones as entrained particulate matter accumulates on filter media in certain of the filtration chambers. The fluid filter is characterized by having relatively few moving parts and by the ability to be very substantially increased in size and capacity without adversely affecting the filtration efficiency of the filter. Prior art patents disclose the concept of forming a filter medium of enhanced filtration capacity by using a bare filter surface and accumulating on the upstream side of the filter surface a layer of the particulate matter being filtered. It has been learned that such accumulated particulate matter forms a particularly efficient filter of that particular substance. However, the difficulty with such structures is that as the layer of particulate matter accumulates on the filter surface, the resistance to passage of fluid through the accumulating filter media increases as the filtration efficiency increases. At some point, the energy required to force the fluid through the accumulated layer of particulate matter is so great as to render the filter uneconomical both from a capacity and energy consumption standpoint. Prior art patents relating to the above concept (such as EP-A-0 026 069) utilize an endless drum having a filter screen thereon through which fluid is passed. Particulate matter in the fluid accumulates on the upstream side of the drum. The interior and/or exterior of the drum is defined into a prefilter zone in which the filter layer is accumulated to its optimum thickness. Air passing downstream of the filter layer in this zone is recirculated back through the filter to prevent the introduction of less than optimally filtered fluid into the environment. Once the filter layer has reached its optimum thickness, it is passed into a second zone where fluid is passed through the layer of particulate matter for its primary filtration step. Fluid downstream in this zone is exited into the environment. A third doffing zone strips the accumulated particulate matter from the surface of the drum whereupon the bare drum surface moves back into the first filter zone. Such filters represent a large improvement over earlier filters which caused substantial variations in filtration efficiency and energy consumption because of the necessity to periodically strip the layer of particulate matter from the filtration surface. However, the rotating drum-type of filter must be very carefully sealed on its ends and at the line of separation between the various zones. Perfect sealing under such circumstances is difficult since the drum is rotating and a seal must be created against the underside of the rotating drum which is a porous surface. FR-A-2200040 discloses a filtration apparatus in which a series of filter plates is carried on an endless conveyor in a casing, the plates each filling the cross-section of the casing between the conveyor and the wall of the casing. The air stream flows through a plurality of the filter plates which are cleaned on a return run of the conveyor. Again sealing of the moving parts relatively to the stationary casing is difficult. Summary of the Invention Therefore, it is an object of the invention to provide a multistage fluid filter for filtering entrained particulate matter from a moving fluid stream at substantially constant fluid pressure and filtration efficiency during continuous on-line operation. It is another object of the invention to provide a multistage fluid filter which reduces the number of moving parts which must cooperate with the filtration medium. It is another object of the present invention to provide a multistage fluid filter wherein particulate matter is collected on the upstream side of a stationary filter medium and wherein the filtration zones of the filter change in sequence depending on the extent of particulate matter accumulation on the filter medium in any given filtration zone. It is yet a further object of the present invention to provide a method of filtering particulate matter from a moving fluid stream in a multistage fluid filter. These and other objects of the present invention are achieved in the preferred embodiments disclosed below by providing a multistage fluid filter for filtering entrained particulate matter from a moving fluid stream. The filter includes first and second filtration chambers, each filtration chamber having a filtration medium positioned therein from an upstream side to a downstream side thereof. Conduit means are provided for interconnecting the first and second filtration chambers in series for fluid flow from the downstream side of one of the two chambers defined as a first filter stage to the upstream side of the other of the two chambers defined as a second filter stage for two stage filtration of the moving fluid. Fluid is diverted downstream past one of the first or second filtration chambers to define a cleaning stage within the filtration chamber past which fluid flow is diverted. Cleaning means are provided for cleaning particulate matter from the filter medium in the cleaning stage while fluid flow therethrough is diverted. Sequencing means are provided for selectively operating the diverting means to, after cleaning particulate matter from the filter medium in the cleaning stage and, upon an increase in resistance to fluid flow through the first filter stage caused by an increase in thickness and/or density in the layer of particulate matter, redefine the cleaning stage as the first filter stage and the first filter stage as the second stage, successively. The clean filter medium in the first filter stage accumulates particulate matter thereon and the particulate matter in the first filter stage forms a filter of enhanced filtration capacity in the second filter stage. After sufficient particulate matter in the first filter chamber has collected for efficient filtration, the fluid is diverted to bypass the second filtration chamber, at which time the second filtration chamber is cleaned. By redefining each filtration chamber alternately as first and second filter stages, the filter can operate continuously after a filter layer is accumulated on the filter medium in the first and second filtration chambers. In accordance with another embodiment of the invention, a housing having a fluid inlet and a fluid outlet is provided. First, second and third filtration chambers are positioned in the housing. Each of the filtration chambers has a filtration medium thereon from an upstream side to a downstream side thereof. First conduit means are provided for selectably interconnecting any two chambers of the first, second and third filtration chambers in series for fluid flow from the downstream side of one of the two chambers defined as a first filter stage to the upstream side of the other of the two chambers defined as a second filter stage. Second conduit means are provided for selectable interconnecting the fluid inlet in the housing with the upstream side of the filtration chamber defined as the first filter stage, the fluid outlet in the housing with the downstream side of the filtration chamber defined as the second filter stage and for interrupting fluid flow into and out of the third one of the first, second and third filtration chambers to define a cleaning stage. Cleaning means are provided for cleaning particulate matter from the filter medium in the cleaning stage while fluid flow therewith is interrupted. Sequencing means are provided for selectably operating the first and second conduit means to redefine the cleaning stage as the first filter stage, the first filter stage as the second filter stage and the second filter stage as the cleaning stage, successively. The clean filter medium in the first filter stage accumulates particulate matter thereon. The particulate matter in the first filter stage forms a filter of enhanced filtration capacity in the second filter stage. By redefining each filter chamber as first and second filter stages and a cleaning stage, successively, the filter can operate continuously after a filter layer is accumulated on the filter medium in any one of the first, second or third filtration chambers. Brief Description of the Drawings Some of the objects of the invention have been set forth above. Other objects and advantages of the invention will appear as the description of the invention proceeds when taken in conjunction with the following drawings, in which: Figure 1 is a perspective view of a filter according to the present invention; Figure 2 is a top plan view, with parts broken away of a filtration chamber with the filtration medium positioned therein; Figure 3 is a top plan view of a filtration chamber showing the operation of the doors; Figure 4 is a simplified perspective view of a single filtratlon chamber in three sequential phases of operation; Figure 5 is a schematic view with parts rearranged for clarity of the filter shown in Figure 1 and showing the three stages during an initial phase of operation; Figures 6-10 illustrate the filter shown in Figure 5 in sequential stages of operation; Figure 11 illustrates a filter similar to that shown in Figure 5 but with an auxiliary fan, with the filter shown in stage 3, cleaning position; and Figures 12-15 illustrate another embodiment of the filter in sequential stages of operation. Description of the Preferred Embodiment Referring now specifically to the drawings, a multistage fluid filter according to the present invention is illustrated in Figure 1 and broadly indicated at reference numeral 10. The fluid filter 10 is contained within a housing structure 11 which is provided with a fluid inlet 12 and a fluid outlet 13. Five separate filtration chambers 14-18, inclusive, are positioned within housing 11. First conduit means 20 is positioned within housing 11, as is a second conduit means 21. Sequencing means, comprising the mechanical apparatus such as solenoids and related hardware for operating filter components is contained within a cabinet 22. The first conduit 20 extends along both sides of filter 10 and communicates one side with the other through an arcuate conduit sequent 20A. The second conduit 21 likewise is positioned on both sides of filter 10. As can be seen in Figure 1, one side of the second conduit communicates with inlet 12 and the other side of conduit 21 communicates with outlet 13. Communication between the two sides of conduit 21 takes place through filter chambers 14-18 in the manner described below. In Figure 2, a filtration chamber is illustrated in a top plan view. Chambers 14-18 are identical in every respect, therefore, the detail in Figure 2 relating to filtration chamber 14 suffices to illustrate the structure of all five chambers. As can be seen, filtration chamber 14 comprises a rectangular enclosed box within which is positioned a trapezoidily shaped filtration medium 25 which comprises a metal frame, on which is positioned, in accordion fashion, a wire screen 26 on which the filtered particulate matter accumulates. The filter medium may comprise a filter fabric instead of the wire screen 26. In the embodiment shown in this application, the wire screen 26 is formed of a 60 x 60 warp/filling mesh. The interior of the filter medium 25 comprises the upstream side through which the particulate-laden air enters, as is shown representationally by the arrow. The remainder of filtration chamber 14 outside of the filtration medium 25 comprises the downstream side of the filtration chamber. Therefore, as particulate-laden air passes through the filtration medium 25 from the upstream to the downstream side, particulate matter is accumulated on the inner surface of the wire mesh 26. Referring now to Figure 4, the construction of each of the filter chambers 14-18 is further illustrated. Again, since all of the filtration chambers 14-18 are identical, the operation will be described with reference to filtration chamber 14. As can be observed from Figure 4, each filtration chamber passes through three successive phases. By referring simultaneously to the illustration of phases I and II, it will be noted that filtration chamber 14 has two vertically-spaced doors 28 and 29. On the other end of filtration chamber 14 are two similarly vertically-spaced doors 30 and 31. Note that doors 28 and 29 communicate with filtration chamber 14 through the upstream side and are therefore used to introduce particulate-laden air into filtration chamber 14. Filtered air is discharged from filtration chamber 14 through doors 30 and 31. Referring now to the phase III illustration in Figure 4, filtration chamber 14 also includes a trap door 33 which encompasses substantially the entire bottom of the filtration chamber. This door is opened during the cleaning stage during which time the entire filtration medium 25 is shaken vigorously with a mechanical shaker to dislodge the accumulated particulate matter on the inner surface of the wire mesh screen 26. Reference is now made to Figures 5-10. The filter 10 has been substantially rearranged in order to illustrate the sequence of operations. Basically, the doors 28, 29 and 30, 31 on each end of each of the filtration zones 14-18 are shown side-by-side rather than on top and bottom as they exist in reality. In addition, the first and second conduits 20 and 21 have been rearranged so that the second conduit 21 is no longer positioned directly above the first conduit 20. Air to be filtered enters the filter 10 through fluid inlet 12 and into the second conduit 21. Note, as in Figure 1, that second conduit 21 is in two segments with one segment on each side of the filtration chambers 14-18. The first conduit 20 extends around filter 10 from one side to the other through a curved segment 20A. Filtration chambers 14 and 15 have been identified with a Roman Numeral I corresponding to phase I in Figure 4. Filtration chambers 16 and 17 have been identified with a Roman Numeral II corresponding with phase II in Figure 4, and filtration zone 18 has been identified with a Roman Numeral III corresponding with the phase III illustration in Figure 4. The purpose of the operation of the filter is to accumulate on the filtration medium 25 in chambers 14 and 15 a matt having an enhanced degree of filtration efficiency. Therefore, by continued reference to Figure 5, fluid air enters fluid inlet 12 and passes into conduit 21. Doors 28 in filtration chambers 14-18 communicate with conduit 21 immediately downstream of inlet 12. Note in Figure 5 that doors 28 are closed in filtration chambers 16, 17 and 18. Therefore, all of the unfiltered air enters chambers 14 and 15 through open doors 28 and pass from the upstream to the downstream aide of filtration medium 25. As the air passes through filtration medium 25, particulate matter is accumulated on its inner side. As the once filtered air passes through filtration medium 25, it enters the downstream side of filtration chambers 14 and 15 and exits through doors 31. Note that doors 31 enter into conduit 20 and the air is directed through curved segment 20A back around to the upstream side of filtration chambers 14 and 15. Doors 29 which communicate with conduit 20 are closed in chambers 14, 15 and 18 and open in filtration chambers 16 and 17. Therefore, the air which has once been filtered in chambers 14 and 15 now enters the upstream side of chambers 16 and 17 and is filtered once again. In stage II, the filtration achieves a higher efficiency because particulate matter has been allowed to accumulate to a predetermined thickness on the inner walls of filter medium 25, thereby defining a filter medium of enhanced filtration efficiency and capacity. Therefore, the stage II filtration chambers 16 and 17 perform an enhanced filtering operation on the air before it is discharged through open doors 30 into conduit 21 and through fluid outlet 13. During this stage, all of the doors 28, 29, 30 and 31 in filtration chamber 18 are closed. Therefore, phase III comprises a cleaning phase during which door 33 (not shown in Figure 5 but in Figure 4) is opened and a mechanical shaker (not shown) physically dislodges the layer of particulate matter contained on the inner surface of filter medium 25. At a certain point, the thickness of the layer of particulate matter on the inner surface of filtration medium 25 in filtration chambers 16 and 17 (the phase II filtration step) becomes so thick that increased resistance to the flow of air through the layer of particulate matter is encountered. At the same time, the layer of particulate matter on the inner surface of filtration medium 25 in the first stage filter chambers 14 and 15 is just reaching its level of optimum filtering efficiency. At this point, automatic pressure gauge sensing means contained in the sequencing apparatus cabinet 22 open and close doors 28, 29, 30 and 31 so that the filtration zones are redefined as is shown in figure 6. Now, the first filtration zone comprises filtration chambers 14 and 18. This can be observed because doors 28 to these two chambers only are open. Therefore, unfiltered air from fluid inlet 12 into conduit 21 can only enter filtration chambers 14 and 18. Filter medium 25 in filtration chamber 18 is completely bare, having just been shaken and the particulate layer dislodged through door 33. A relatively thin layer of particulate matter is accumulating on the inner surface of the filtration medium 25 in filtration chamber 14. At the same time, the increasing thickness of the layer of particulate matter in filtration chamber 15 means that it can now serve as one of the filtration chambers in the second stage filtration step since the filtration efficiency of the layer of particulate matter is reaching its optimum. Note that doors 29 and 30 in filtration chambers 15 and 16 are open. Therefore, the air which enters filtration chambers 15 and 16 through doors 29 has just passed through filtration chambers 14 and 18 and has therefore been once filtered. The remaining particulate matter is removed in filtration chambers 15 and 16 whereupon the twice filtered fluid exits through doors 30 into conduit 21 and through fluid outlet 13. Chamber 17 now has the greatest accumulation of particulate matter is now defined as the cleaning stage and is cleaned in the manner described above by opening door 33 and shaking the filtration medium 25 to dislodge the layer of particulate matter. As can be seen in Figure 7, the first filter stage now comprises filtration chambers 17 and 18. The filter medium in filtration chamber 17 is bare, having just been doffed as illustrated in Figure 6. The particulate layer in filtration chamber 18 is becoming thicker and is increasing in its filtration efficiency. Chambers 14 and 15 are now defined as the second filter stage, the layer of particulate matter therein having reached its optimum filtration efficiency. At the same time, the layer of particulate matter in filtration chamber 16 has become too thick to efficiently filter and allow the flow of air therethrough. Therefore, it is defined as the cleaning stage and it is cleaned in the manner described above. Referring now to Figure 8, filtration zones 14-18 have once again been redefined. Now, filtration zones 16 and 17 comprise the first filter stage, the filter medium in filtration chamber 16 being bare because of the cleaning stage just completed in Figure 7. Chambers 14 and 18 comprise the second filter stage and filtration chamber 15 is defined as the cleaning stage. Note once again that the sequencing apparatus 22 has rearranged the pattern of opened and closed doors 28-31 so that the unfiltered air which enters conduit 21 through fluid inlet 12 first passes through filtration chambers 16 and 17 and then through filtration chambers 14 and 18 before exiting into conduit 20 and out through fluid outlet 13. In Figure 9, filtration chambers 15 and 16 comprise the first filter stage, filtration chambers 17 and 18 comprise the second filter stage and the filtration chamber 14 comprises the cleaning stage. Again, the doors are controlled in such a way as fluid enters first filtration chambers 15 and 16, then filtration chambers 17 and 18 before exiting through fluid outlet 13. During this time, the layer of particulate matter on the filter medium 25 in filtration chamber 14 is being cleaned. When the layer of particulate matter increases beyond optimum thickness in filtration chamber 18, the first and second filtering stages and the cleaning stages are once again redefined, and the arrangement is back to where the operation began in Figure 5. Referring now to Figure 10, the same embodiment as illustrated in Figures 5-9 is shown. Air enters fluid inlet 12 at a pressure of minus 100Kg./M². The suction fan 39 for the filter 10 is positioned downstream of fluid outlet 13. Fan 39 exerts a pressure of minus 200Kg/M². Therefore, the pressure drop from the fluid inlet 12 to the fluid outlet 13 is 100Kg/M². The pressure of the air in conduit 20 is minus 150Kg/M². This reflects the fact that air in conduit 20 has been subject to one drag inducing pass through filter chambers 15 and 16 whereas the air upstream of filtration chambers 15 and 16 must make two drag inducing passes. An alternate arrangement is shown in Figure 11. Here, not only is there a fan 39 positioned downstream of fluid outlet 13 but also an auxiliary fan 40 positioned in the curved segment 20A of conduit 20. As in Figure 10, air enters fluid inlet at a pressure of minus 100Kg/M². Auxiliary fan 40 increases this pressure to minus 150Kg/M² on the downstream side of filtration chambers 15 and 16, and to minus 75Kg/M² on the upstream side of filtration chambers 17 and 18. Filtered air exits through fluid outlet 13 at minus 125Kg/M². To summarize, the clean filter medium in the first filter stage, whichever filter chamber that might be, accumulates particulate matter thereon. The layer of particulate matter in the first filter stage forms a filter of enhanced filtration capacity when redefined as the second filter stage. By redefining each filtration chamber 14-18, successively, as first and second filter stages and a cleaning stage, the filter can operate continuously after a filter layer is accumulated on the filter medium 25 in any of the filtration chambers. In the embodiment described above, a minimum of three filter chambers is required. However, there is no theoretical maximum number of filtration chambers required. The chambers can be ganged together in any suitable arrangement and can be sequenced so that many more than only two filtration stages are defined. In the embodiment disclosed above, air velocity is nominally 18.3 metres per second. The doors are interconnected to open and close simultaneously as is shown in Figure 3. the doors can be operated by conventional electric solenoids or pneumatic cylinders in a manner which is completely conventional and therefore requires no further discussion. Another embodiment of the invention is illustrated in Figures 12-15. The construction of the filter is in most respects identical to that described above. In the embodiment shown in Figures 12-15, only two filter chambers 50 and 51 are provided. However, as with the embodiment shown in Figures 5-11, any number of filter chambers can be used and ganged as desired. Filtration chambers 50 and 51 are provided with a filter medium 52, in a trapezoidal from exactly as described earlier and illustrated in Figures 2 and 4. Air to be filtered enters a conduit 53 through an inlet 54. Air enters filtration chambers 50 and 51 through a door 55 in each. The air passes through the filtration medium 52 from the upstream to the downstream side thereof and exits through a door 57 on the downstream side of the filtration chambers 50 and 51. Doors 56 admit once filtered air from a conduit 60 into filtration chambers 50, 51 and discharge once filtered air into conduit 60 through doors 58 in the downstream side of filtration chambers 50 and 51. Air exits through conduit 53 on the downstream side of filtration chambers 50 and 51 through a fluid outlet 61. In the arrangement shown in Figure 12, filtration chamber 50 is defined as a first filter stage and filtration chamber 51 is defined as a second filter stage. The stages, as previously, are represented by Roman Numerals I and II. Air enters conduit 53 through inlet 54. The air passes into filtration chamber 50 through open door 55 and passes through the filtration medium 52 to the downstream side of filtration chamber 50 and exits through open door 58. Note that no fluid enters directly into filtration chamber 51 from conduit 53. The air which has once been filtered in filtration chamber 50 enters conduit 60 and, because the exit door 63 in the conduit 60 is closed, is passed back around to the upstream side of fil-tration chamber 51 where it enters through open door 56. The air which has already been filtered once in filtration chamber is filtered a second time in filtration chamber 51. The layer of particulate matter on the upstream side of filter medium 52 and filtration chamber 51 defines a filter medium of enhanced filtration capacity. Once the air has been filtered a second time, it exits the downstream side of filtration chamber 51 through open door 57 into conduit 53 and out fluid outlet 61. Referring now to Figure 13, at the point during the filtration process when the layer of particulate matter on the filtration medium 52 in filtration chamber 51 (filter stage II) reaches a thickness and/or density where filtration efficiency and air passage is reduced, filtration chamber 51 is redefined as a cleaning stage by closing all of its own doors 55 - 58 and opening the lower cleaning door 33 (not shown, but see Figure 4). A mechanical shaker physically removes the layer of particulate matter from the filtration medium 52, leaving a bare wire mesh filter surface. Note that filtration chamber 50 is still defined as the first filter stage, as is indicated by its own open doors 55 and 58. When the layer of particulate matter in filtration chamber 50 reaches an optimum level, doors 55 and 58 in filtration chamber 51 are opened, whereupon filtration chamber 51 begins to serve as a first stage filter. Simultaneously, doors 55 and 58 in filtration chamber 50 are closed and doors 56 and 57 are opened. Therefore, filtration chamber 50 begins operating as a second filter stage. In the configuration shown in Figure 14, air enters through inlet 54 into conduit 53 and passes directly into filtration chamber 51 through open door 55. After leaving a deposit of particulate matter on the upstream side of filtration medium 52, the air exits the downstream end of filtration chamber 51 through open door 58 into conduit 60. The air is carried back around to the upstream side of filtration chamber 50 and enters filtration chamber 50 through open door 56. The twice filtered air exits through open door 57 into conduit 53 and out through fluid outlet 63. In Figure 15, the layer of particulate matter in filtration chamber 50 has accumulated to the point where it must be cleaned. Therefore, it is defined as a cleaning stage and is cleaned in the manner described above while the layer of particulate matter in filtration chamber 51 continues to provide a filtration process to air entering through fluid inlet 54 and exiting through fluid outlet 61. Note that in Figures 13 and 15 the air is subjected to only a single filtration process before exiting through fluid outlet 61. Herein lies the primary distinction between the embodiment shown in Figures 5-11 and that shown in Figures 12-15. Therefore, the filter shown in Figures 12-15 is particularly suitable for situations where filtration standards are not as high but nevertheless where constant filtration at relatively high efficiency is desired. A multi-stage fluid filter and method is described above. The foregoing description of the preferred embodiments of a multi-stage fluid filter and method according to the present invention is provided for the purpose of illustration only and not for the purpose of limitation - the invention being defined by the claims.

Claims: 1. A multistage fluid filter for filtering entrained particular matter from a moving fluid stream at substantially constant fluid pressure and filtration efficiency during continuous on-line operation, said filter comprising: (a) a housing (11) having a fluid inlet (12) and a fluid outlet (13); (b) first, second and third stationary filtration chambers (14 and 15; 16 and 17; 18) positioned in said housing, each having a filtration medium (25) therein from an upstream side to a downstream side thereof and cleaning means for cleaning particulate matter from the filter medium while fluid flow therethrough is interrupted; (c) first conduit means (20) for interconnecting two chambers of said first, second and third filtration chambers in series for fluid flow from the downstream side of one of the two chambers defined as a first filter stage for accumulating particulate matter on the filtration medium thereof, to the upstream side of the other of the two chambers defined as a second filter stage having a previously accumulated layer of particulate matter on the filtration medium thereof; (d) second conduit means (21) for interconnecting the fluid inlet (12) with the upstream side of the filtration chamber defined as the first filter stage and the fluid outlet (13) in the housing with the downstream side of the filtration chamber defined as the second filter stage, characterised in that the first conduit means (20) is adapted for selectably interconnecting any two of the stationary chambers in series, the second conduit means (21) is adapted for selectively interconnecting the fluid inlet (12) and the fluid outlet (13) with the stationary filtration chambers, and being further adapted for interrupting fluid flow into and out of one of the filtration chambers to define a cleaning stage therein; sequencing means (22) for selectably operating the first and second conduit means (20,21) to, after cleaning particulate matter from the filter medium in the cleaning stage and, upon an increase in resistance to fluid flow through the second filter stage caused by an increase in thickness and/or density in the layer of particular matter, re-define the cleaning stage as the first filter stage, the first filter stage as the second filter stage and the second filter stage as the cleaning stage, successively, to permit the filter to operate continuously after a filter layer is accumulated on the filter medium in any of the first, second or third filtration chambers. 2. A multistage fluid filter according to Claim 1, characterised in that the first conduit means (20) includes a first door (29) on the upstream side of each of the first, second and third filtration chambers and a second door (31) on the downstream side of the first, second and third filtration chambers, and the second conduit means (21) includes a first door (28) on the upstream side of each of the first, second and third filtration chambers and a second door (30) on the downstream side of the first, second and third filtration chambers, the sequencing means (22) comprising means for simultaneously opening and closing predetermined ones of said doors to direct fluid flow in a predetermined manner through said housing from the fluid inlet (12) to the fluid outlet (13). 3. A multistage fluid filter according to Claim 1 or Claim 2, characterised in that the cleaning means comprises a trapdoor (33) positioned in gravity feed relation to the filtration medium (25), and means for removing the particulate matter from the filtration medium for gravity flow through said door. 4. A multistage fluid filter according to Claim 2 or Claim 3, so far as it depends from Claim 2, characterised in that the first, second and third filtration chambers comprise identical elongate rectangular metal enclosures, the first and second doors (29,31) of the first conduit means (20) being positioned on opposite ends of the metal enclosure and the first and second doors (28,30) of the second conduit means (21) being positioned respectively adjacent the first and second doors of the first conduit means on opposite sides of said metal enclosure, the trapdoor (33) being positioned in the bottom of the rectangular metal enclosure. 5. A multistage fluid filter according to Claim 4, characterised in that the filter medium (25) comprises a trapezoid-shaped frame having filter fabric or a screen thereon and positioned in the chamber intermediate the upstream and downstream sides thereof with the trapezoid-shaped frame sealingly engaging with the walls of the metal enclosure intermediate the upstream and downstream sides thereof whereby fluid flow through the metal enclosure must be through the filter medium from the upstream to the downstream side thereof. 6. A multistage fluid filter according to Claim 5, characterised in that the frame includes fan-folded sides (26) carrying fan-folded filter medium thereon to increase the surface area through which the fluid can flow. 7. A multistage fluid filter according to Claim 3, or any one of Claims 4 to 6, so far as they depend from claim 3, characterised in that the cleaning means includes a shaker for shaking the frame of the filter medium in that filtration chamber defined as the cleaning stage to dislodge the filtered particulate matter thereon and permit it to drop by gravity feed through the trapdoor (33). 8. A multistage fluid filter for filtering entrained particular matter from a moving fluid stream at substantially constant filtration efficiency during continuous on-line operation, said filter comprising: (a) first and second stationary filtration chambers (50,51), each having a filtration medium (52) therein from an upstream side to a downstream side thereof: (b) conduit means (60) for interconnecting the first and second filtration chambers (50,51) in series for fluid flow from the downstream side of one of the two chambers defined as a first filter stage for accumulating particulate matter on the filtration medium thereof, to the upstream side of the other of the two chambers defined as a second filter stage having a previously accumulated layer of particulate matter on the filtration medium thereof, for two stage filtration of the moving fluid; (c) cleaning means for cleaning particulate matter from the filter medium while fluid flow therethrough is diverted; characterised in that the conduit means (60) is adapted for diverting fluid flow downstream past one of the first or second filtration chambers to define a cleaning stage within the filtration chamber past which the fluid flow is diverted and sequencing means is provided for selectably operating the diverting means to, after cleaning particulate matter from the filter medium in the cleaning stage and, upon an increase in resistance to fluid flow through the first filter stage caused by an increase in thickness and/or density in the layer of particulate matter, re-define the cleaning stage as the first filter stage and the first filter stage as the second filter stage successively, whereby after sufficient particulate matter in the first filter chamber has collected for efficient filtration, the fluid is diverted to by-pass the second filtration chamber at which time the second filtration chamber is cleaned and whereby, by re-defining each filtration chamber alternately as first and second filter stages, the filter can operate continuously after a filter layer is accumulated on the filter medium in the first and second filtration chambers. 9. A multistage fluid filter according to Claim 8, characterised in that the conduit means includes a first conduit (53) providing a fluid inlet (54) and a fluid outlet (61), a first door (55) on the upstream side of each of the first and second filtration chambers and a second door (57) on the downstream side of the first and second filtration chambers, the first and second doors providing communication between the first and second filtration chambers and the first conduit and wherein the conduit means further includes a second conduit (60), providing an alternative controlled fluid outlet, a third door (56) on the upstream side of each of the first and second filtration chambers and a fourth door (58) on the downstream side of the first and second filtration chambers the third and fourth doors providing communication between the first and second filtration chambers and the second conduit, and wherein the sequencing means comprises means for simultaneously opening and closing predetermined ones of the doors (55,56,57 and 58) to direct fluid flow in a predetermined manner through the housing from a fluid inlet (54) to either the fluid outlet (61) or the alternative fluid outlet (64). 10. A multistage fluid filter according to Claim 9, characterised in that the cleaning means comprises a trapdoor (33) positioned in gravity feed relation to the filtration medium (52), and means for removing the particulate matter from the filtration medium for gravity flow through the trapdoor. 11. A multistage fluid filter according to Claim 10, characterised in that the cleaning means includes a shaker for shaking the frame of the filter medium (52) in the filtration chamber defined as the cleaning stage to dislodge the filtered particulate matter thereon and permit it to drop by gravity feed through the trapdoor (33). 12. A multistage fluid filter according to any one of claims 10 to 11, characterised in that the first and second filtration chambers comprise identical elongate rectangular metal enclosures, the first and second doors (55 and 57) being positioned on opposite ends of said metal enclosure and the third and fourth doors (56 and 58) being positioned respectively adjacent the first and second doors (55 and 57) on opposite sides of the metal enclosure, and further wherein the trapdoor (33) is positioned in the bottom of the rectangular metal enclosure. 13. A multistage fluid filter according to Claim 12, characterised in that the filter medium comprises a trapezoid-shaped frame having filter fabric or a screen thereon and is positioned in the chamber intermediate the upstream and downstream sides thereof with the trapezoid-shaped frame sealingly engaging the walls of the metal enclosure intermediate the upstream and downstream sides thereof whereby fluid flow through the metal enclosure must be through the filter medium from the upstream to the downstream side thereof. 14. A multistage fluid filter according to Claim 13, characterised in that the frame includes fan-folded sides (26) carrying fan-folded filter medium thereon to increase the surface area through which the fluid can flow. 15. A method for filtering entrained particulate matter from moving fluid stream using a multistage fluid filter as claimed in Claim 1, comprising the steps of: interrupting the fluid flow into and out of the third filtration chamber to define a cleaning stage therein; re-defining the third chamber cleaning stage as the first filter stage, the first chamber as the second filter stage and the second chamber as the cleaning stage, interrupting fluid flow to the cleaning stage; cleaning particulate matter from the filter medium in the cleaning stage while fluid flow therewith is interrupted, and successively redefining the first, second and third chambers as cleaning; first filter and second filter stages upon an increase in resistance to the fluid flow through the second filter stage caused by an increase in thickness and/or density in the layer of the particulate matter. 16. A method for filtering entrained particulate matter from a moving fluid stream using a multistage fluid filter as claimed in Claim 8, comprising the steps of: diverting fluid flow downstream past the first filtration chamber to define a cleaning stage within the first filtration chamber past which fluid flow is diverted; cleaning the particulate matter form the filtration medium in the first filtration chamber; re-defining the first chamber as the first filter stage and the second chamber as the second filter stage; upon the accumulation of sufficient particulate matter in the first filter chamber for efficient filtration diverting the fluid past the second filtration chamber; cleaning the particulate matter from the filtration medium in the second chamber; re-defining each filtration chamber successively as first and second filter stages and cleaning the particulate matter from the filtration medium in the chamber from which fluid flow is diverted whereby the filter is permitted to operate continuously after a filter layer is accumulated on the filter medium in the first and second filtration chambers.

Inventors: NIEDERER, KURT W.
Applicants: AIR FILTERS FOR INDUSTRY LTD.
Application year: 1987
Main classification: B01D46
IPC codes: B01D46