Classifications

• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
  • B01D46/52—Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material
  • B01D46/521—Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material using folded, pleated material
  • B01D46/522—Particle separators, e.g. dust precipitators, using filters embodying folded corrugated or wound sheet material using folded, pleated material with specific folds, e.g. having different lengths
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D27/00—Cartridge filters of the throw-away type
  • B01D27/04—Cartridge filters of the throw-away type with cartridges made of a piece of unitary material, e.g. filter paper
  • B01D27/06—Cartridge filters of the throw-away type with cartridges made of a piece of unitary material, e.g. filter paper with corrugated, folded or wound material
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
  • B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
  • B01D29/111—Making filtering elements
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
  • B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
  • B01D29/13—Supported filter elements
  • B01D29/15—Supported filter elements arranged for inward flow filtration
  • B01D29/21—Supported filter elements arranged for inward flow filtration with corrugated, folded or wound sheets
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
  • B01D29/50—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition
  • B01D29/56—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection
  • B01D29/58—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection arranged concentrically or coaxially
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
  • B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
  • B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
  • B01D46/2411—Filter cartridges
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2201/00—Details relating to filtering apparatus
  • B01D2201/04—Supports for the filtering elements
  • B01D2201/0407—Perforated supports on both sides of the filtering element
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2201/00—Details relating to filtering apparatus
  • B01D2201/12—Pleated filters
  • B01D2201/122—Pleated filters with pleats of different length
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2275/00—Filter media structures for filters specially adapted for separating dispersed particles from gases or vapours
  • B01D2275/10—Multiple layers

Definitions

• the present disclosure relates to a fluid filtering device and, more particularly, to a pleated filter element and a method of forming a pleated filter element. Even more particularly, the present disclosure relates to a pleated filter element having a modified W- pleat construction, and a method of forming such a filter element.
• Filtration is the process of separating particles, or contaminants from a fluid (liquid or gas), and can be accomplished by passing the fluid through a porous filter medium that stops or captures the particles while permitting the fluid to pass there through.
• fluid filtering is used extensively in the manufacture of polymer products, medicinal products, mineral and metallurgical processing, petroleum refining, water purification, emissions control, and in beverage and food preparation.
• a surface-type filter medium stops fluid contaminants on its surface.
• examples of surface- type filter media are calendered melt-blown material, cellulose and/or paper, membranes, woven screen, porous metal, and porous non-woven material.
• a depth-type filter medium captures contaminants within the medium, i.e. between an upstream surface and a downstream surface of the medium.
• An example of a depth-type filter medium is a resin bonded filter.
• Pleated surface-type filters typically include relatively thin cellulosic or synthetic filter media that is folded in an accordion-like fashion to produce a plurality of pleats. Each pleat is typically made up of a pair of rectangular panels, with fold lines separating the panels.
• the short sides of the rectangular panels of the pleats usually extend radially outwardly with respect to the axis of the filter element, and thus provide the radial height of the pleats, while the long sides of the rectangular panels of the pleats extend axially between ends of the filter element.
• the maximum number of full pleats i.e., pleats that extend between the inner and outer diameters of the filter element is determined by an inner circumference of the filter element divided by the thickness of the pleats.
• a W-pleat filter element is comparable to a standard pleated filter element in that it includes a plurality of longitudinal pleats disposed in a cylindrical configuration.
• the W- pleat filter element also includes relatively short pleats extending radially inward from the outer periphery of the filter between the pleats of standard height.
• the short pleats are the same height and arise at a uniform frequency about the circumference of the filter, i.e., there is one short pleat between every two full-length pleats. Examples of W-pleat filters can be found in U.S. Patent No. 2,627,350 (1953) to Wicks; U.S. Patent No. 3,002,861 (1962) to Harms; U.S. Patent No.
• W-pleat filters are made using cam-actuated pleating machines that only provide repetitive and uniform pleat patterns, resulting in short pleats of the same height and arising at a uniform frequency.
• One problem associated with the W-pleat construction is a less than optimum pleat density and the migration of the shortened pleats towards the axis of the filter. Such migration is undesired because it can cause binding, blockages, increased pressure drops across the filter, reduced filter lives, and damage the filter media.
• a spiral pleat filter element is comparable to a standard pleated filter in that it includes a plurality of longitudinal pleats disposed in a cylindrical configuration. In a spiral pleat filter, however, the ends of the pleats are rolled over to minimize the spacing between adjacent pleat surfaces near an outer diameter of the filter element, such that more filter surface area can be provided in a filter of equal diameter.
• spiral pleated filters can be found in U.S. Patent Nos. 2,395,449, 2,401,222 and 2,420,414 (1946) to Briggs; U.S. Patent No. 2,801,001 (1957) to Bowers; and U.S. Patent Nos. 5,543,047 (1996) and 5,690,765 (1997) to Stoyell et al.
• the spiral pleat and the W-pleat designs provide surface-type filters with increased filter surface area
• the spiral pleat designs do not have the pleat migration problems associated with the W-pleat designs.
• the rolled-over pleats of a spiral pleated filter provide fewer and more difficult to access radial flow paths near the outer diameter of the filter, leading to a greater pressure drop across the filter.
• the rolled-over pleats of a spiral pleated filter provide longer flow paths and, therefore, a greater chance of the flow paths becoming blocked in high load or large particle contaminant applications.
• spiral pleated filters are more difficult to axially insert into a cylindrical cage of a cartridge assembly incorporating the filter element, since the rolled- over pleats have a tendency to straighten out prior to being inserted into the cage. Inserting a spiral pleated filter element into a cage creates drag, which can cause damage to the filter media and can, as a practical matter, limit the axial length of a filter cartridge incorporating a spiral pleated filter element.
• a filter element constructed according to the present disclosure has a plurality of longitudinally extending pleats including outwardly radiating primary pleats and inwardly radiating secondary pleats, with at least one secondary pleat positioned between two adjacent primary pleats.
• Each primary pleat has a predetermined radial height
• each secondary pleat has a radial height that is less than the radial height of each primary pleat and different from the radial height of at least one other secondary pleat.
• a filter element according to the present disclosure has been found to provide improved filter area gains, a greater overall filter density between inner and outer peripheries of the filter element, and an increased number of radial flow paths available at the outer periphery of the filter.
• a filter element according to the present disclosure also provides improved inter-pleat support to reduce the likelihood of pleat migration and binding.
• the filter element is preferably a pleated composite including a filter medium and at least one of an upstream diffusion medium and a downstream diffusion medium.
• the diffusion media provide support to the filter medium, help to efficiently distribute fluid, and ensure that flow channels formed between and within the pleats are not filled and blocked with contaminants.
• the pleated composite of the filter element is heat-set to further reduce the likelihood of pleat migration and binding.
• the present disclosure also provides a cartridge assembly having a cylindrical cage, a cylindrical core coaxially positioned within the cylindrical cage, and a cylindrical filter element, as described above, coaxially positioned between the core and the cage.
• the primary pleats of the filter element each have a predetermined radial height about equal to a difference between an outer radius of the core and an inner radius of the cage.
• a method of forming a filter element according to the present disclosure includes pleating filter medium to form a plurality of longitudinally extending pleats including primary pleats and secondary pleats, wherein at least one secondary pleat is positioned between two adjacent primary pleats, each primary pleat has a predetermined height, and each secondary pleat has a height that is less than the height of each primary pleat and different from the height of at least one other secondary pleat.
• the method further includes cutting the pleated filter medium to a desired length, and forming the cut length of the pleated filter medium into a cylinder such that the primary pleats extend radially outwardly and the secondary pleats extend radially inwardly.
• Fig. 1 is a perspective view of a pleated filter element according to the present disclosure
• Fig. 2 is a perspective view, partially cut-away, of a cartridge assembly including the pleated filter element of Fig. 1 contained between an inner core and an outer cage of the cartridge assembly, wherein a portion of the filter element is shown unwrapped from within the cage;
• Fig. 3 is an enlarged sectional view of the cartridge assembly of Fig. 2; and
• Figs. 3a-3c are sectional views of cartridge assemblies including other examples of pleated filter elements according to the present disclosure.
• a cylindrical cartridge assembly 8 including a pleated filter element 10 constructed according to the present disclosure.
• the cartridge assembly 8 includes a cylindrical inner perforated core 12 coaxially disposed within the filter element, and a cylindrical outer perforated cage 14 coaxially disposed on the filter element.
• the filter element 10 disclosed herein has a "modified" W- pleat construction, which will be described in greater detail hereinbelow.
• Such a filter element 10 has been found to provide filter area gains typical of a spiral pleated filter, with an increase in the number of available radial flow paths of the filter at the outer cage 14.
• such a filter element 10 has been found to provide a greater overall filter density between the inner core 12 and the outer cage 14, with the greater overall filter density improving inter-pleat support to reduce the likelihood of pleat migration and binding.
• a filter element 10 includes a plurality of longitudinally extending pleats "P" and “s” each of which has a pair of pleat legs joined to one another.
• the pleats include outwardly radiating primary pleats "P” and inwardly radiating secondary pleats "si, s 2 , s 3 . . . s ⁇ ", where " ⁇ " is an actual number of secondary pleats, with at least one secondary pleat positioned between two adjacent primary pleats.
• the pleats "P" and “s” are shown spaced apart more than they actually are for purposes of illustration.
• the pleats are positioned closer together so that adjacent pleats touch near the core 12, whereby a greater amount of filter is fit between the core 12 and the cage 14.
• each primary pleat "P” extends to a predetermined height "H”
• the secondary pleats "si, s 2 , s 3 . . . s ⁇ " are each provided with a height "hi,
• each secondary pleat "sj, s 2 , s 3 . . . s ⁇ " also has a radial height "hi, h , h 3 , . . h ⁇ " that is different from the radial height of at least one other secondary pleat.
• each secondary pleat "si, s 2 , s 3 . . . s ⁇ " additionally
• a filter element constructed in accordance with the present disclosure can alternatively be provided with secondary pleats wherein some of the secondary pleats "si, s 2 , s 3 . . . s ⁇ " have equal heights.
• a filter element 10 constructed in accordance with the present disclosure includes
• the theoretical predetermined height of the primary pleats "P” is equal to half a difference between an inner and an outer diameter of the filter element 10.
• the filter element 10, the inner core 12 and the outer cage 14 are sized such that the inner diameter of the filter element is about equal to an outer diameter "d COre " of the core 12, and the outer diameter of the filter element is about equal to an inner diameter "d cage “ of the cage 14.
• the theoretical predetermined height of the primary pleats "P” is preferably equal to about half a difference between the core outer diameter "d core " and the cage inner diameter "d cage “.
• the modified W-pleat design disclosed herein provides a consistent and optimum filter density between the core outer diameter "d CO re” and the cage inner diameter “d cage ".
• a secondary pleat "s” is added for every change in diameter " ⁇ d” between the core outer diameter "d core " and the cage inner diameter “d cage ".
• the change in diameter " ⁇ d” is defined as the diameter change required to increase the circumference by one pleat thickness, and is generally determined by the following equation: t ⁇
• the height "hi, h 2 , h 3 , . . h ⁇ " of each of the secondary pleats "si, s 2 , s 3 . . . S ⁇ ", respectively, can then be determined by the following equations:
• the primary pleats "P" each have a theoretical predetermined height equal to about approximately 0.572 inches, the theoretical number of primary pleats “P” is equal to about sixty-nine (69), and the change in diameter " ⁇ d” is equal to approximately 0.0191 inches.
• the resulting heights "h” of the secondary pleats "s”, and the theoretical number “ ⁇ ” of secondary pleats "s” are provided as follows: Table I Theoretical Height for each Secondary Pleat
• the pleated filter element 10 as calculated and set forth in Table I therefore, has a theoretical total of one hundred and six (106) pleats: sixty-nine (69) primary pleats "P” and thirty-seven (37) secondary pleats "s".
• the aspects of the pleated filter element 10 set forth in Table I are only to be considered as an example, and not a limitation of the present disclosure.
• over twenty more secondary pleats of decreasing heights "h” of between 0.199 and 0.008 inches can be included in Table I.
• secondary pleats "s" having an actual height "h” below a practical minimum height are not included in the filter element.
• the practical minimum height of the pleats is dependent, for example, on the capabilities of the pleating machine used to pleat the filter element, the thickness of the pleats, and the filter material. In the particular example of the pleated filter element of Table I, the practical minimum height is considered to be about 0.200 inches. Accordingly, secondary pleats "s" having an actual height "h" less than 0.200 inches are not considered for inclusion in the filter element.
• the pleated filter element 10 of the present disclosure can be manufactured by a variety of techniques.
• the filter and diffusion media to be pleated may be stored on separate rolls and simultaneously fed to a pleating machine and formed into a composite as the layers are pleated.
• the filter composite is heated so that the filter composite, and in particular, the diffusion media 22, 24 thereof become heat-set.
• the pleated, heat-set filter composite which emerges from the pleating machine is then cut to a prescribed length or prescribed number of pleats as determined by the intended dimensions of the filter element 10.
• the length of pleated filter composite is then formed into a cylindrical shape, and the lengthwise edges of the pleated filter composite are sealed to each other along a seam by conventional means, such as by ultrasonic welding, to retain the pleated filter composite in a cylindrical form.
• the cylindrical inner core 12 may then be axially inserted into the cylindrical filter element 10, the filter element and core axially inserted into the cylindrical outer cage 14, and the end caps 30 attached to the ends of the filter element to form a completed cartridge assembly 8, as shown in Fig. 1.
• a pleating machine having independently actuated pleating blades may be used.
• Karl Rabofsky GmbH of Berlin, Germany
• U.S. Patent Nos. 4,465,213 and 4,465,214 both of which are incorporated herein by reference in their entireties, disclose exemplary servo- actuated pleating machines.
• the Robofsky R178PC pleating machine has been used to provide a pleated filter element according to the present disclosure.
• the program instructs the movement of an upper blade and a lower blade to produce the primary pleats "P" and the secondary pleats "si, s , s 3 . . . s ⁇ " of the filter element 10 as disclosed herein.
• the order of the secondary pleats "s” as calculated in Table I has been mixed to produce the machine instructions of Table II. The mixing of the secondary pleats "s” is done to ensure that the largest number of primary and secondary pleats "P, s" as theoretically calculated in Table I can actually fit into the predetermined dimensions of the cylindrically-shaped filter element 10.
• each of the primary pleats "P" of the pleated filter element 10 set forth in Table I have been provided with an actual height “H” that is less than the theoretical height of the primary pleats "P” to facilitate the axial insertion of the resulting filter element 10 between the core 12 and the cage 14 to form the cartridge assembly 8.
• the actual height "H” of the primary pleats "P” is 0.01 inches less than the theoretical height of 0.572 inches.
• some of the primary pleats "P” may be left out of the filter element 10 to ensure that the filter element 10 will fit between the core 12 and the cage 14. Accordingly, five (5) of the primary pleats "P” have been left out of the machine instructions of Table II, such that an actual number of primary pleats "P” is equal to the theoretical number "N” minus five.
• each of the secondary pleats "s" of the pleated filter element 10 set forth in Table I has been provided with an actual height that is less than the theoretical height "h". In the machine instructions of Table II, therefore, the actual height “h” of each the secondary pleats “s” is 0.01 inches less than the theoretical height “h” shown in Table I.
• some of the tallest secondary pleats “s” may be left out of the filter element 10 to ensure that the filter element 10 will fit between the core 12 and the cage 14. Accordingly, the six tallest secondary pleats "si, s 2 , . . . s 6 " have been left out of the machine instructions of Table II. Since secondary pleat "s 6 " has an actual height "h 6 " equal to about 0.504 inches, a predetermined maximum secondary pleat height "h max " has been found empirically in this case to be about 0.504 inches.
• the filter element 10 therefore, is pleated to include an actual number " ⁇ " of
• secondary pleats "s" equal to the theoretical number “ ⁇ ” minus the number “y” of secondary pleats having a height greater than the predetermined maximum secondary pleat height "h max " of about 0.504 inches and less than the practical minimum pleat height of about 0.200 inches.
• the pleat thickness "t" can be increased slightly when calculating the pleats in order to provided fewer pleats.
• the heights "h” of the secondary pleats "s” preferably do not fall below a preferred minimum secondary pleat height "h m j n ", to ensure that the shorter secondary pleats hold their pleated shape and do not blow radially outward of the filter element 10. Accordingly, “h” should be greater than or equal to “h m j n ", in addition to being less than "h max ".
• the minimum secondary pleat height "h m j n " is generally dependent on the pleat thickness and the capabilities of the pleating machine, and may also be dependent on the particular filter and diffusion media incorporated in the filter element.
• a preferred minimum secondary pleat height "h m j drink” has been found to be 0.250 inches. All secondary pleats "s” having a calculated height “h” less than “h m j n " (but greater than the practical minimum pleat height of 0.200 inches) are provided with an actual height equal to "h m j n ".
• the secondary pleats "s 33 , s 34 , s 35 , s 36 and s 37 " for example, each have an actual height "h 33 , h 4 , h 35 , h 36 and h 3 ", respectively, less than the "h m j n " of 0.250 inches, they are each given a height equal to "h m j n " during production of the pleated filter 10, as shown on lines 15, 27, 39, 53 and 63 in Table II.
• the remaining secondary pleats "s 7 , s 8 , . . . s 32 ", as calculated in Table I, are mixed in order and each are positioned between adjacent pairs of primary pleats "P".
• the secondary pleats "s” may be distributed among the primary pleats "P” in a random manner or in a uniform manner to obtain the largest total number of primary and secondary pleats. In the example shown in Table II, the secondary pleats "s” have been randomly mixed.
• the secondary pleats "s” may be distributed among the primary pleats "P” in a uniform manner so that the similar distributions of secondary pleat heights "h” may be repeated every ninety degrees of the filter element 10, for example, or every forty-five degrees.
• a filter element 110 according to the present disclosure can include two secondary pleats "s” between every adjacent pairs of primary pleats "P", as shown in Fig. 3a; a filter element 210 according to the present disclosure can include two secondary pleats "s” between every two adjacent primary pleats "P", as shown in Fig. 3b; and a filter element 310 according to the present disclosure can include one secondary pleat "s” between every two adjacent primary pleats "P", as shown in Fig. 3c.
• a filter element according to the present disclosure can have varying numbers of secondary pleats "s" between adjacent primary pleats "P". Again, many variations of the distribution and arrangement of the secondary pleats "s” with respect to the primary pleats "P" are possible without departing from the spirit and scope of the presently disclosed filter element 10. Referring again to Table II, extra pleats are made at the beginning of the machine instructions, i.e., line 1, and the end of the machine instructions, i.e., line 65, so that a length of the pleated filter composite can be cut at the extra pleats, then formed into a cylindrical shape. Then the cut extra pleats are sealed to each other along a seam by conventional means to retain the pleated filter composite in a cylindrical form.
• Filter elements pleated in accordance with the present disclosure have been found to have a far greater surface area usable for filtration than conventional radial pleated filter elements having the same inner and outer diameters, such as the BetaFine D ® filter manufactured by Cuno, Incorporated of Meriden, CT.
• a filter element 10 pleated according to the present invention has about thirty percent (30%) more surface area than a conventional straight radial pleated filter element.
• a conventional W-pleated filter element has only about twenty percent (20%) more surface area than a conventional straight radial pleated filter element.
• a filter element 10 constructed in accordance with the present disclosure has also been found to provide a greater and more consistent filter density between the inner core 12 and the outer cage 14 of a cartridge assembly 8 than either a conventional W-pleated filter (having a uniform repeating pattern of one half pleat between two pairs of full pleats) or a conventional straight radial pleated filter, as demonstrated here by Table III.
• the theoretical pleat densities for a given pleat thickness "t", core outer diameter “d core " and cage inner diameter "d ca g e " are calculated and compared for a conventional straight pleated filter, a conventional W-pleated filter, and a filter element 10 pleated according to the present disclosure.
• the theoretical pleat densities are equal to the number of actual pleats provided by each filter divided by the maximum number of theoretical pleats that can be provided at each diameter interval "D", where "D” is the difference between "d cag e" and "d cor e” divided by ten.
• the maximum number of theoretical pleats is equal to the diameter at each interval multiplied by ⁇ and divided by the thickness "t" of the pleats.
• a filter element 10 constructed in accordance with the present disclosure provides the greater and more consistent pleat density between the inner core 12 and the outer cage 14, as compared with a conventional straight radial pleated filter and a conventional W-pleated filter.
• the greater and more consistent filter density of the presently disclosed filter element 10 results in improved inter-pleat support and a more even distribution of loads applied to the filter element.
• the greater and more consistent filter density therefore, minimizes pleat migration and binding, and increases the ability of the pleats to retain particles in a pulsating flow system.
• Filter elements pleated in accordance with the present disclosure have been found to provide a greater filter life than conventional straight pleated filter elements, such as the BetaFine-D ® filter. Furthermore, filter elements pleated in accordance with the present disclosure have been found to have advantages over spiral pleated filter elements, such as the PolyPro XL ® filter manufactured by Cuno, Incorporated of Meriden, CT.
• a filter element 10 according to the present disclosure provides filter area and filter density gains similar to a spiral pleated filter element, with an increase in the number of radial flow paths of the filter available at the outer cage 14 of a cartridge assembly 8 containing the filter element 10.
• a filter element 10 according to the present invention is more easily inserted into a cage 14 than a spiral pleated filter element, whose pleats must be rolled over, or "spiraled” before being inserted into the cage.
• the filter element 10 of the present disclosure comprises a pleated composite including a filter medium 20 and at least one of an upstream diffusion medium 22 and a downstream diffusion medium 24, as shown best in Fig. 1.
• upstream and downstream refer to the exterior and interior surfaces of the filter element 10 when the filter is being subjected to radially inward fluid flow, or to interior and exterior surfaces of the filter when the filter element is being subjected to radially outward fluid flow.
• the diffusion media 22, 24 provide support to the filter medium 20 and enable fluid to evenly flow to or from substantially all portions of the surface of the filter medium 20 so that virtually the entire surface area of the filter medium may be effectively used for filtration.
• the filter element 10 comprises a three-layer composite of a filter medium 20, and both an upstream diffusion medium 22 and a downstream diffusion medium 24.
• the filter medium 20 can be selected in accordance with the fluid to be filtered and the desired filtering characteristics.
• the filter medium 20 can be used to filter fluids such as liquids, gases, or mixtures thereof, and may comprise a porous film or a fibrous sheet or mass, or any combination thereof; may have a uniform or graded pore structure and any appropriate effective pore size; may include single or multiple layers; and may be formed from any suitable material, such as a natural material, synthetic polymer, glass, or metal.
• the filter medium is comprised of one or more sheets of non woven thermoplastic micro fibers.
• the non woven thermoplastic micro fibers may be melt blown, spunbond, carded, or hydroentangled, for example.
• the filter medium may be calendered, or compressed, to further modify its porosity.
• the thermoplastic can comprise polypropylene, for example, while for higher temperature applications (i.e., above 180° F) or chemical compatibility with other fluids, the thermoplastic can comprise nylon, polyester or melt-processible fluoropolymer, for example.
• the filter medium 20 may comprise a single layer, or a plurality of layers. Furthermore, it is possible for the filter medium 20 to include two or more layers having different filtering characteristics (e.g., one layer acting as a pre-filter for the second layer).
• the filter medium is preferably provided in sheet form, as opposed to being melt blown directly onto the diffusion medium, for example, such that the sheet can be inspected prior to being incorporated into the filter.
• the use of discrete sheets of depth filter medium has been found to simplify quality control inspection of the filter medium and make the physical properties of each filter cartridge more consistent. Controlling the consistency of the physical properties of the filter medium provides a unique ability to achieve sharp, well-defined, and optimized control over the removal efficiency and dirt capacity of the resulting filter cartridge.
• the diffusion media 22, 24 are preferably distinct from the filter medium 20.
• the upstream and downstream diffusion media 22, 24 can be made of any materials such as a mesh, screen or a porous woven or non- woven sheet.
• Meshes and screens come in various forms. For high temperature applications, a metallic mesh or screen may be employed, while for lower temperature applications, a polymeric mesh may be particularly suitable.
• Polymeric meshes come in the form of woven meshes and extruded meshes, either of which may be employed. Specific examples of suitable extruded polymeric meshes are those available from Nalle Plastics of Austin, TX under the trade names Naltex ® , Zicot ® , and Ultraflo ® . Other examples of suitable extruded polymeric meshes are those available from Applied Extrusion Technologies, Inc.
• a sheet of woven or non- woven fabric may be more suitable for use as the diffusion media 22, 24 since a fabric is usually smoother than a mesh and produces less abrasion of adjoining layers of the filter composite.
• An example of a suitable non- woven fabric for use as a diffusion medium is a polyester non- woven fabric sold under the trade designation Reemay 2011 by Reemay, Inc. of Old Hickory, TN.
• the upstream and downstream diffusion media 22, 24 can be of the same or different construction. Alternatively, the upstream and downstream diffusion media 22, 24 may have different characteristics and these characteristics may be varied to provide a desired effect. For example, where the overall thickness of the filter composite is fixed, the thickness of the upstream diffusion medium 22 may be made greater than the thickness of the downstream diffusion medium 24.
• An example of a pleated filter element 10 constructed according to the present disclosure includes an upstream diffusion medium 22 of Delnet ® extruded polypropylene mesh, and a downstream diffusion medium 24 of Typar T- 135 ® spunbond, non- woven polypropylene, available from Reemay Inc.
• Another example of a pleated filter element 10 constructed according to the present disclosure includes an upstream diffusion medium 22 of Naltex Symmetrical Filtration Netting LWS ® 37-3821 extruded polypropylene mesh, and a downstream diffusion medium 24 of the Typar T-135 ® spunbond, non- woven polypropylene.
• a filter element 10 pleated in accordance with the present disclosure should not always be made to have the most filter area that will fit between a core and a cage of a cartridge assembly.
• Table IV for example, an optimum combination of total filter area and upstream diffusion medium 22 for a filter element 10 pleated in accordance with the present disclosure has been found to depend on the particular type and sizes of contaminants to be filtered.
• Table IV shows the results of single pass tests on various filter elements pleated in accordance with the present disclosure. Each single pass test was performed at a flow rate of three gallons per minute, with water containing between about 0.39 to about 1.0 grams of contaminant per gallon of water. Two standard contaminants were used: 0-150 micron contaminant (ISO COARSE, A.T.D. 12103-1, A4, available from Powder Technologies, Inc. of Bumsville, MN); and 0-10 micron contaminant (A.T.D. nominal 0-10 microns, also available from Powder Technologies, Inc).
• ISO COARSE A.T.D. 12103-1, A4, available from Powder Technologies, Inc. of Bumsville, MN
• 0-10 micron contaminant A.T.D. nominal 0-10 microns, also available from Powder Technologies, Inc.
• All of the filter elements tested were pleated in accordance with the present disclosure, included a filter medium 20 of non woven thermoplastic micro fibers, a downstream diffusion medium 24 of Typar T-135 ® spunbond, non-woven polypropylene, an outer diameter of about 2.5 inches and a length of about 10 inches.
• the life of a filter for purposes of the tests illustrated in Table IV is defined as the amount of contaminant challenged for the pressure drop across the filter to increase by 20 psid due to contaminant loading in the tested filter.
• a filter element 10 pleated in accordance with the present disclosure having a rating of 0.2 microns and for filtering contaminants of 0-10 microns, preferably will have a filter composite length of at least 9.0 feet and an upstream diffusion layer 22 of 5 mil Delnet ® .
• filter elements 10 pleated in accordance with the present disclosure having ratings of 0.5, 1.0 and 2.5 microns, and for filtering contaminants of 0-150 microns, preferably will each have a filter composite length of not more than about 7.3 feet and an upstream diffusion layer 22 of 20 mil Nalle LWS ® .
• filter elements 10 pleated in accordance with the present disclosure having ratings of 5.0, 10.0, 20.0 and 40.0 to 70.0 microns, and for filtering contaminants of 0-150 microns, preferably will each have a filter composite length of not more than about 7.8 feet and an upstream diffusion layer 22 of 20 mil Nalle LWS ® .
• the cylindrical core 12 of the cartridge assembly 8 supports the inner periphery of the filter element 10 against forces in the radial direction and also helps to give the filter element axial strength and rigidity against bending.
• the core 12 may be of conventional design and may be made of any material having sufficient strength and which is compatible with the fluid being filtered. Openings 26 are formed through the core to permit the passage of fluid between the outside and the center of the core.
• An alternative core would include a splined shaft, or a core that can be removed during manufacturing.
• the outer cage 14 of the cartridge assembly 8 may be of conventional design with openings 28 formed therein for the passage of fluid.
• Alternative cages include expandable mesh sleeve, a porous extruded tube, or a wrap consisting of cord, woven or non- woven material.
• the material of which the cage 14 is made can be selected based on the fluid being filtered and the filtering conditions.
• a cartridge assembly 8 according to the present invention will be equipped with end caps 30 at one or both ends.
• the end caps 30 can be either blind or open end caps, and the material of which they are formed and their shape can be selected in accordance with the filtering conditions and the materials of the members to which the end caps are to be joined.
• the end caps 30 are attached to the filter element 10, but they may also be attached to the core 12 or the cage 14.
• Conventional techniques can be used to attach the end caps 30 to the cartridge assembly 8, such as by use of an epoxy, by thermobonding, or by spin welding.

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• Chemical & Material Sciences (AREA)
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• Geometry (AREA)
• Filtering Of Dispersed Particles In Gases (AREA)
• Filtering Materials (AREA)
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• 2000
  • 2000-01-07 EP EP00903175A patent/EP1140319B1/en not_active Expired - Lifetime
  • 2000-01-07 US US09/479,686 patent/US6315130B1/en not_active Expired - Lifetime
  • 2000-01-07 BR BR0008591-0A patent/BR0008591A/pt not_active Application Discontinuation
  • 2000-01-07 AU AU24960/00A patent/AU765826B2/en not_active Ceased
  • 2000-01-07 DE DE60021055T patent/DE60021055T2/de not_active Expired - Lifetime
  • 2000-01-07 WO PCT/US2000/000438 patent/WO2000040319A1/en not_active Ceased
  • 2000-01-07 JP JP2000592066A patent/JP5042408B2/ja not_active Expired - Fee Related
• 2010
  • 2010-01-15 JP JP2010006704A patent/JP2010110760A/ja active Pending

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