US20020063092A1 - Non-woven depth filter cartridge - Google Patents
Non-woven depth filter cartridge Download PDFInfo
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- US20020063092A1 US20020063092A1 US10/056,715 US5671502A US2002063092A1 US 20020063092 A1 US20020063092 A1 US 20020063092A1 US 5671502 A US5671502 A US 5671502A US 2002063092 A1 US2002063092 A1 US 2002063092A1
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- mass
- filaments
- filter cartridge
- filament
- microns
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- Abandoned
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- 229920000642 polymer Polymers 0.000 claims abstract description 33
- 238000003490 calendering Methods 0.000 claims abstract description 11
- 239000012530 fluid Substances 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 5
- 230000007704 transition Effects 0.000 claims 1
- 238000010924 continuous production Methods 0.000 abstract description 5
- 238000003780 insertion Methods 0.000 abstract description 5
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- 238000009987 spinning Methods 0.000 abstract description 3
- 230000001186 cumulative effect Effects 0.000 abstract 1
- 230000007246 mechanism Effects 0.000 description 20
- 238000001914 filtration Methods 0.000 description 14
- 239000000463 material Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 12
- 239000000835 fiber Substances 0.000 description 9
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 5
- 229920005594 polymer fiber Polymers 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- -1 polypropylenes Polymers 0.000 description 5
- 239000010410 layer Substances 0.000 description 4
- 239000002131 composite material Substances 0.000 description 3
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- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
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- 238000010438 heat treatment Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000012768 molten material Substances 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 1
- 230000003466 anti-cipated effect Effects 0.000 description 1
- 239000012792 core layer Substances 0.000 description 1
- 230000032798 delamination Effects 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 239000012260 resinous material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
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Images
Classifications
-
- D—TEXTILES; PAPER
- D04—BRAIDING; LACE-MAKING; KNITTING; TRIMMINGS; NON-WOVEN FABRICS
- D04H—MAKING TEXTILE FABRICS, e.g. FROM FIBRES OR FILAMENTARY MATERIAL; FABRICS MADE BY SUCH PROCESSES OR APPARATUS, e.g. FELTS, NON-WOVEN FABRICS; COTTON-WOOL; WADDING ; NON-WOVEN FABRICS FROM STAPLE FIBRES, FILAMENTS OR YARNS, BONDED WITH AT LEAST ONE WEB-LIKE MATERIAL DURING THEIR CONSOLIDATION
- D04H3/00—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length
- D04H3/02—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of forming fleeces or layers, e.g. reorientation of yarns or filaments
- D04H3/07—Non-woven fabrics formed wholly or mainly of yarns or like filamentary material of substantial length characterised by the method of forming fleeces or layers, e.g. reorientation of yarns or filaments otherwise than in a plane, e.g. in a tubular way
-
- 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
- B01D29/31—Self-supporting 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
- B01D29/50—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
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
- B01D39/16—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres
- B01D39/1607—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous
- B01D39/1623—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin
- B01D39/163—Other self-supporting filtering material ; Other filtering material of organic material, e.g. synthetic fibres the material being fibrous of synthetic origin sintered or bonded
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2101/00—Types of filters having loose filtering material
- B01D2101/005—Types of filters having loose filtering material with a binder between the individual particles or fibres
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2201/00—Details relating to filtering apparatus
- B01D2201/18—Filters characterised by the openings or pores
- B01D2201/182—Filters characterised by the openings or pores for depth filtration
Definitions
- the present invention relates to the field of fluid filtration, and in particular to depth filters. Specifically, the present invention relates to depth filters formed from non-woven melt-blown polymeric fibers.
- Non-woven melt-blown depth filters are well known and are widely used in fluid filtration applications. Such filters can be formed by extruding softened polymeric materials through an orifice of a nozzle in a stream. Jets of gas (usually air) attenuate the polymer stream to form the fibers, which are directed toward and collected by a rotating mandrel. Fibers continue to build up on the rotating mandrel until a tubular mass of fibers of the desired size and morphology is achieved.
- Jets of gas usually air
- Depth filters of the type described may include a core member to support the fiber mass. Depth filters of this type are typically produced by placing a tubular core member over the mandrel and applying the polymer fibers directly on the core member. This process, however, is discontinuous and requires that a core member be replaced on the mandrel after each depth filter is formed.
- a continuous process for producing a coreless depth filter is also known.
- a coarse core layer of relatively large diameter polymer fibers are initially applied directly onto a spinning mandrel to form an inner cylindrical fiber mass.
- Finer polymer fibers are applied over the inner cylindrical mass to form the depth filter element.
- the fiber mass forming the depth filter element is continuously advanced along and off of the mandrel by a press roller located adjacent to the mandrel.
- the inner fiber mass of such a coreless depth filter provides sufficient structural integrity to support an outer mass of relatively fine polymer fibers and withstand the fluid pressures to which the depth filter is subjected.
- the outer fiber mass of the finer polymer fibers comprises the filtration zone of the depth filter.
- depth filters be capable of filtering very fine particles (e.g., 1 micron) while allowing fluid under pressure to flow through the filter with a minimum drop in pressure.
- Depth filters with an initial pressure drop in the range of 3-4 p.s.i.d. per gallon per minute of liquid flow per ten inch element are known.
- the present invention is directed to a composite polymer filament mass especially suitable for use in constructing a cylindrical depth filter element.
- the composite polymer filament mass is comprised of a first cylindrical mass of very small diameter polymer filaments, i.e., diameters of less than about 1.5 microns.
- An inner cylindrical portion of the first cylindrical mass defines a smooth inner cylindrical surface of the composite filament mass.
- the first cylindrical mass of filaments is surrounded by a second cylindrical mass of polymer filaments having diameters greater than 1.5 microns.
- FIG. 1 is a schematic diagram generally illustrating an apparatus for continuously producing a non-woven depth filter element.
- FIG. 2 is a schematic diagram illustrating the apparatus configuration for continuously producing a depth filter element of the present invention.
- FIG. 2A is an enlarged view of the collection device of the apparatus of FIG. 2.
- FIG. 3 is a cross-sectional view of a depth filter element of the present invention.
- the present invention relates to an improved non-woven depth filter element as well as an apparatus and a method for continuously making such element.
- coreless is used to describe certain depth filter elements. Unless otherwise indicated, the term “coreless” refers to a filter element which is not provided with a separate support core member.
- FIG. 1 generally illustrate an apparatus which is used to continuously manufacture a depth filter element of indefinite length in which the depth filter is comprised of at least two discrete sets of continuous filament material of different diameters or of different materials.
- a depth filter element of indefinite length in which the depth filter is comprised of at least two discrete sets of continuous filament material of different diameters or of different materials.
- One such apparatus suitable for the present invention is disclosed in U.S. Pat. No. 5,340,479, which is fully incorporated herein by reference.
- the preferred embodiment of the apparatus includes a motor driven screw type extruder 10 which is supplied with thermoplastic polymeric material from a source (not shown).
- the particular thermoplastic polymeric material may be any one of a variety of synthetic resinous materials which can produce the filaments used in manufacturing the depth filter element of the present invention.
- the class of polymeric materials known as polypropylenes are preferred, polyesters, Nylon, polyurethanes and other materials may be used as well.
- the polymeric material is heated to a molten state, at which time it is metered and conveyed into a heated delivery line 11 .
- the material is maintained or further heated in the line 11 and is ultimately fed into a common manifold 12 .
- the heated molten polymeric material is then directed by the manifold 12 to filament forming means, which in one embodiment is in the form of two filament delivery systems 14 and 16 .
- Each of the delivery systems 14 and 16 is substantially identical and functions to produce one or more substantially continuous polymeric filaments and to direct the same along a predetermined path toward a collection means as will be described in greater detail below.
- the filament delivery system 14 includes a motor driven gear type positive displacement metering pump 18 which receives molten polymeric material from the manifold 12 and pumps it to heater block 24 .
- the speed of the motor 19 which drives the metering pump 18 , and thus the rate at which the material is metered through the pump 18 is electronically controlled by an appropriate control means 20 .
- Heater block 24 which is independently heated via heating means (not shown) is provided with internal passages which lead to a plurality of nozzles 25 .
- the heating means, and thus the temperature of the polymeric material within heater block 24 is controlled by temperature control 26 .
- Each nozzle 25 includes an orifice, the size of which may be selected as desired to assist in achieving a desired filament size or diameter. The molten material fed to each nozzle 25 exits the orifice in a stream.
- each nozzle 25 Associated with each nozzle 25 are attenuating mechanisms 28 , which comprise a plurality of gas or air jets. Gas flowing out of the attenuating mechanisms 28 function to attenuate the stream of molten material exiting from the nozzles 25 to form polymeric filaments in a manner known in the art.
- the attenuating mechanisms 28 accordingly may be of any design known in the art including that described in U.S. Pat. No. 4,173,443, the disclosure of which is incorporated herein by reference.
- Each of the attenuating mechanisms 28 is associated with a gas heater 29 and gas supply source 31 .
- Gas supply source 31 provides gas via conduit 32 and appropriate valves and regulators to the heater 29 where its temperature is elevated or lowered to the desired temperature via the temperature control 30 .
- the gas is then fed from the heater 29 through conduit 34 to the attenuating mechanisms 28 .
- Attenuating mechanisms 28 may be provided with gas from a common supply source, heater and temperature control, or alternatively, separately controlled gas sources may be employed for each attenuating mechanism 28 .
- the filament delivery system 16 is substantially identical to that of the system 14 described above. Specifically, the system 16 includes a heater block 38 , an independently driven positive displacement metering pump 36 , and motor 39 and motor elements 40 . Heater block 38 is provided with a plurality of nozzles 42 and temperature control 41 . The system 16 is also provided with a plurality of attenuating mechanisms 44 associated with the nozzles 42 . Pressurized gas is passed to each attenuating mechanisms 44 from a gas supply source 45 via conduit 46 , a heater 48 and conduit 49 . Temperature control 50 regulates and controls the temperature produced by heater 48 . The provision of separate filament delivery systems 14 and 16 enables separate control and production of polymeric filaments produced by each system 14 and 16 .
- Each of the delivery systems 14 and 16 is capable of producing a plurality of discrete, continuous filaments 51 and 52 respectively which are directed from the orifices 25 and 42 and attenuating mechanisms 28 and 44 , respectively, toward a filament collection device 54 illustrated in FIG. 1.
- the filament collection device 54 includes a central, rotatable mandrel 55 which extends from a drive motor 58 . Adjacent to the mandrel 55 and spaced therefrom is a press roll member 56 rotatable about the axis 57 .
- the plurality of filaments 51 and 52 are directed in a flared pattern toward the rotating mandrel 55 and collected thereon in a manner known in the art.
- the rotating press roller 56 engages the filaments which have accumulated on the rotating mandrel 55 . As sufficient filaments are built up on the mandrel 55 , the press roller 56 forces the filament mass 59 off the axial end of the mandrel 55 in the direction of the arrow 53 to produce a continuous filament mass 59 of indefinite length.
- the entire filament collection device 54 is known to those skilled in the art and may be similar to that described in U.S. Pat. No. 4,240,864, the disclosure of which is incorporated herein by reference.
- FIG. 1 The apparatus of FIG. 1 has been demonstrated to be adequate for producing coreless depth filters in which filament delivery system 14 is configured to produce polymeric filaments having relatively large diameters (i.e., greater than 15 microns), and filament delivery system 16 is configured to produce polymeric filaments having smaller diameters (i.e., 1-15 microns).
- a depth filter element produced thereby has a tubular configuration with an innermost cylindrical zone of relatively large polymeric filaments which defines a support for an outer cylindrical zone of the smaller polymeric filaments which form a filtration zone of the depth filter.
- the present invention is directed to an novel apparatus configuration and method for continuously producing an improved depth filter for use with a core member.
- the improved depth filter of the present invention is generally characterized by an inner cylindrical mass of very small diameter polymeric filaments (i.e., 0.5-1.5 microns), a calendered (i.e. smooth) inner cylindrical surface and an outer cylindrical mass of coarser, large diameter polymeric filaments (i.e., 4-10 microns or greater). While cored depth filters having a filtration zone near the core are known in the art, production of such filters is discontinuous and requires that the relatively fine polymeric filaments comprising the filtration zone to be deposited directly on a core member supported by a mandrel.
- the improved apparatus configuration and process of the present invention overcomes the limitations of such a discontinuous depth filter production process by enabling a continuous process whereby very small diameter polymeric filaments (0.5-1.5 microns) are directly applied to and collected on a mandrel of a filament collection device, such as filament collection device 54 shown in FIG. 1, with larger diameter polymeric filaments thereafter applied over the small filament mass.
- a calendered inner cylindrical surface of the depth filter comprised of a portion of the mass of very small polymeric filaments, results from this process, which allows for an easy, post-production insertion of a core member known in the art.
- the process of the present invention therefore enables a continuous production of a depth filter element independent of a core member to be used with the depth filter.
- FIG. 2 is a schematic diagram illustrating the apparatus of FIG. 1 configured for continuously producing a depth filter element of the present invention.
- four filament producing devices 100 , 102 , 104 , and 106 are employed, each of which comprises a nozzle and an attenuating mechanism, such as nozzle 25 and attenuating mechanism 28 of FIG. 1.
- Filament producing devices 100 , 102 , 104 , and 106 are longitudinally aligned along a common axis 108 which is parallel with mandrel 110 .
- each filament producing device 100 , 102 , 104 , and 106 includes an orifice which defines an axis 112 that is perpendicular to axis 108 and mandrel 110 .
- Axis 112 generally corresponds to the flow axis of molten polymer exiting the nozzle orifice.
- filament producing devices 100 , 102 , 104 , 106 are located approximately 30 inches from mandrel 110 .
- the attenuating mechanism of filament producing device 100 is oriented to produce gas streams which are generally aligned and parallel with axis 112 . This orientation results in a flared filament pattern 114 being directed toward mandrel 110 .
- Filament pattern 114 is comprised of polymer filaments having very small diameters of between about 0.5 micron to about 1.5 microns.
- polymer filaments of filament pattern 114 were produced in the depth filter of the instant invention by passing polypropylene heated to a temperature of 420° C. to about 425° C. through a nozzle having an orifice size of about 0.011 inch at a rate of about 3.8 pounds per hour and passing a heated gas at a temperature of 400° C. at a rate of 11 cubic feet per minute over the molten polymer stream exiting the nozzle orifice. It will be appreciated that a person skilled in the art can readily determine other parameter combinations suitable to form very fine filaments of between about 0.5 microns to about 1.5 microns, and that the parameters necessary to form such very fine filaments will vary according to the particular polymer material used.
- the attenuating mechanism of filament producing device 102 is oriented to produce gas streams which are directed at an angle, relative to axis 112 of device 102 , away from filament pattern 114 .
- a flared filament pattern 116 is produced which substantially avoids overlapping with filament pattern 114 .
- the objective of this configuration is to allow polymeric filaments from device 100 to accumulate and form a mass on mandrel 110 with minimal mixing of polymeric filaments from device 102 .
- the attenuating mechanism of device 102 is oriented to produce gas streams away from filament pattern 114 at an angle of between about 30° to about 40° relative to axis 112 of device 102 .
- the polymer filaments of filament pattern 116 have diameters of between about 4 microns to about 8 microns.
- the filaments of pattern 116 were produced by passing polypropylene heated to a temperature of 420° C. to about 425° C. through a nozzle having an orifice size of about 0.011 inch at a rate of about 3.8 pounds per hour and passing a gas at ambient temperature at a rate of 11 cubic feet per minute over the molten polymer stream exiting the nozzle orifice.
- the attenuating mechanism is oriented to produce gas streams at an angle directed toward filament pattern 116 to produce a filament pattern 118 which substantially overlaps with filament pattern 116 .
- the attenuating mechanism of device 104 is oriented to produce gas streams at an angle of between about 5° to about 10° relative to axis 112 of device 104 .
- the polymer filaments of filament pattern 118 have diameters of between about 6 microns to about 10 microns.
- the filaments of pattern 118 were produced by passing polypropylene heated to a temperature of 390° C. through a nozzle having an orifice size of about 0.011 inch at a rate of about 5.1 pounds per hour and passing a gas at ambient temperature at a rate of 11 cubic feet per minute over the molten polymer stream exiting the nozzle orifice.
- the attenuating mechanism of device 106 is oriented to produce a gas stream angled toward filament pattern 118 . In a preferred embodiment, this orientation results in a gas stream directed at an angle of between about 10° to about 20° relative to axis 112 of device 106 .
- device 106 produces filament pattern 120 , which substantially overlaps filament pattern 118 .
- the polymer filaments of filament pattern 120 have diameters of between about 6 microns to about 10 microns.
- the filaments of pattern 120 were produced by passing polypropylene heated to a temperature of about 390° C. through a nozzle having an orifice size of about 0.016 inch at a rate of about 5.1 pounds per hour and passing a gas at ambient temperature at a rate of 16 cubic feet per minute over the molten polymer stream exiting the nozzle orifice.
- filament producing device 100 is oriented such that filament pattern 114 is generally centered on nip 122 of press roller 124 .
- filament pattern 114 has a width of about 6 to 8 inches at mandrel 110 .
- Filament pattern 116 is intended to be substantially separate from filament pattern 114 , with sufficient overlap or intermingling of each pattern, however, to prevent separation or delamination of the filament mass formed. Filament pattern 114 therefore accumulates on mandrel 110 as a generally homogenous filter mass.
- Filament patterns 116 , 118 and 120 are intended to substantially overlap, which results in a relatively heterogenous filament mass being applied over the filament mass produced by filament pattern 114 .
- FIG. 2A which is an enlarged view of the collection device of FIG. 2, an accumulated mass of filaments 114 a and 114 b from filament pattern 114 are produced on opposite sides of nip 122 of press roller 124 .
- press roller 124 is oriented at an angle relative to mandrel 110 with nip 122 in contact with mandrel 110 .
- outer surface 123 of press roller 124 is angularly displaced by about 3° relative to mandrel 110 .
- sufficient filaments from filament pattern 116 are intermixed with those of filament mass 114 b that the filament mass 114 a is drawn past nip 122 as the collective filament mass 126 is moved along mandrel 110 in the direction indicated by arrow 128 .
- the filaments from filament mass 114 a are drawn past nip 122 , they are compressed between nip 122 and mandrel 110 to form a dense layer of the very small diameter filaments produced in filament pattern 114 . Because of the small diameter of these filaments, the filaments are able to sufficiently cool in the time it takes for them to accumulate and pass by nip 122 .
- a filament mass of the present invention may be formed in any desirable lengths and subsequently cut to any desirable size to form discrete depth filter elements.
- the method of the present invention demonstrates a way of continuously producing at an advantageous rate a filament mass suitable for making a depth filter element having an inner filtration zone comprised of very fine filaments and an outer filtration zone comprised of larger filaments, and which produces a smooth inner cylindrical surface that allows for subsequent easy insertion of a core member.
- FIG. 3 illustrates a cross-sectional view of the filament mass 126 produced by the present invention.
- filament mass 126 is comprised of an inner cylindrical calendered layer 130 , which is contiguous with an inner filtration zone 132 comprised of a relatively homogenous zone of very fine polymer filaments have diameters of less than about 1.5 microns, and generally in a range of between about 0.5 micron and 1.5 microns.
- Calendered layer 130 results from the compression of filaments having the same morphology and size as those found in filtration zone 132 .
- calendered layer has a thickness of about 5 mils which defines a smooth inner cylindrical surface 134 of filament mass 126 .
- Filament mass 126 is further comprised of an outer filtration zone 136 formed by a heterogenous filament mass having intermixed filaments having diameters ranging in size from about 4 microns to about 10 microns. In one embodiment, filament mass 126 has a mass of 110 grams per ten inch section.
- Depth filter elements formed in the manner described relative to FIGS. 1, 2 and 2 A and having the characteristics described relative to FIG. 3 have demonstrated excellent particle filtration and fluid throughput capabilities.
- the depth filter of the present invention has demonstrated to be 99.9% effective at removing 1 micron particles.
- the depth filter element of the present invention allows fluid throughput with a minimal drop in fluid pressure across the filter (e.g. pressure drops of about 1.5 p.s.i.d. per gallon per minute of liquid flow per ten inch element).
Abstract
A new non-woven depth filter cartridge is formed by insertion of a core into filter mass formed in a continuous process. A mass of very fine diameter polymer filaments is overlaid by mass of larger diameter polymer filaments. The filaments are continuously accumulated on a spinning mandrel and advanced along and off of the mandrel by a press roller. An inner cylindrical surface of the cumulative filament mass forming the depth filter element is calendered, which facilitates insertion of a core member.
Description
- This application claims priority from U.S. patent application Ser. No. 09/296,070, filed on Apr. 21, 1999, for “Non-Woven Depth Filter Element” by Thomas M. Aune, et al., now pending; and U.S. patent application Ser. No. 09/550,814, filed on Apr. 18, 2000 for “Method of Producing a Non-Woven Depth Filter Element” by Thomas M. Aune, et al., now pending.
- The present invention relates to the field of fluid filtration, and in particular to depth filters. Specifically, the present invention relates to depth filters formed from non-woven melt-blown polymeric fibers.
- Non-woven melt-blown depth filters are well known and are widely used in fluid filtration applications. Such filters can be formed by extruding softened polymeric materials through an orifice of a nozzle in a stream. Jets of gas (usually air) attenuate the polymer stream to form the fibers, which are directed toward and collected by a rotating mandrel. Fibers continue to build up on the rotating mandrel until a tubular mass of fibers of the desired size and morphology is achieved.
- Depth filters of the type described may include a core member to support the fiber mass. Depth filters of this type are typically produced by placing a tubular core member over the mandrel and applying the polymer fibers directly on the core member. This process, however, is discontinuous and requires that a core member be replaced on the mandrel after each depth filter is formed.
- A continuous process for producing a coreless depth filter is also known. According to this process, a coarse core layer of relatively large diameter polymer fibers are initially applied directly onto a spinning mandrel to form an inner cylindrical fiber mass. Finer polymer fibers are applied over the inner cylindrical mass to form the depth filter element. The fiber mass forming the depth filter element is continuously advanced along and off of the mandrel by a press roller located adjacent to the mandrel. The inner fiber mass of such a coreless depth filter provides sufficient structural integrity to support an outer mass of relatively fine polymer fibers and withstand the fluid pressures to which the depth filter is subjected. The outer fiber mass of the finer polymer fibers, on the other hand, comprises the filtration zone of the depth filter.
- Under some circumstances, it is desirable that depth filters be capable of filtering very fine particles (e.g., 1 micron) while allowing fluid under pressure to flow through the filter with a minimum drop in pressure. Depth filters with an initial pressure drop in the range of 3-4 p.s.i.d. per gallon per minute of liquid flow per ten inch element are known.
- There continues to be a need in the art for a method of continuously producing a depth filter element for use with a core member which yields a suitable depth filter capable of filtering particles 1 micron or less with a minimum pressure drop.
- The present invention is directed to a composite polymer filament mass especially suitable for use in constructing a cylindrical depth filter element. In the preferred embodiment, the composite polymer filament mass is comprised of a first cylindrical mass of very small diameter polymer filaments, i.e., diameters of less than about 1.5 microns. An inner cylindrical portion of the first cylindrical mass defines a smooth inner cylindrical surface of the composite filament mass. The first cylindrical mass of filaments is surrounded by a second cylindrical mass of polymer filaments having diameters greater than 1.5 microns.
- FIG. 1 is a schematic diagram generally illustrating an apparatus for continuously producing a non-woven depth filter element.
- FIG. 2 is a schematic diagram illustrating the apparatus configuration for continuously producing a depth filter element of the present invention.
- FIG. 2A is an enlarged view of the collection device of the apparatus of FIG. 2.
- FIG. 3 is a cross-sectional view of a depth filter element of the present invention.
- The present invention relates to an improved non-woven depth filter element as well as an apparatus and a method for continuously making such element. Throughout the specification, the term “coreless” is used to describe certain depth filter elements. Unless otherwise indicated, the term “coreless” refers to a filter element which is not provided with a separate support core member.
- Reference is first made to FIG. 1 to generally illustrate an apparatus which is used to continuously manufacture a depth filter element of indefinite length in which the depth filter is comprised of at least two discrete sets of continuous filament material of different diameters or of different materials. One such apparatus suitable for the present invention is disclosed in U.S. Pat. No. 5,340,479, which is fully incorporated herein by reference. The preferred embodiment of the apparatus includes a motor driven
screw type extruder 10 which is supplied with thermoplastic polymeric material from a source (not shown). The particular thermoplastic polymeric material may be any one of a variety of synthetic resinous materials which can produce the filaments used in manufacturing the depth filter element of the present invention. Although the class of polymeric materials known as polypropylenes are preferred, polyesters, Nylon, polyurethanes and other materials may be used as well. - Within the
extruder 10, the polymeric material is heated to a molten state, at which time it is metered and conveyed into aheated delivery line 11. The material is maintained or further heated in theline 11 and is ultimately fed into acommon manifold 12. The heated molten polymeric material is then directed by themanifold 12 to filament forming means, which in one embodiment is in the form of twofilament delivery systems 14 and 16. Each of thedelivery systems 14 and 16 is substantially identical and functions to produce one or more substantially continuous polymeric filaments and to direct the same along a predetermined path toward a collection means as will be described in greater detail below. - The
filament delivery system 14 includes a motor driven gear type positivedisplacement metering pump 18 which receives molten polymeric material from themanifold 12 and pumps it toheater block 24. The speed of the motor 19 which drives themetering pump 18, and thus the rate at which the material is metered through thepump 18 is electronically controlled by an appropriate control means 20. -
Heater block 24, which is independently heated via heating means (not shown) is provided with internal passages which lead to a plurality ofnozzles 25. The heating means, and thus the temperature of the polymeric material withinheater block 24, is controlled bytemperature control 26. Eachnozzle 25 includes an orifice, the size of which may be selected as desired to assist in achieving a desired filament size or diameter. The molten material fed to eachnozzle 25 exits the orifice in a stream. - Associated with each
nozzle 25 are attenuatingmechanisms 28, which comprise a plurality of gas or air jets. Gas flowing out of theattenuating mechanisms 28 function to attenuate the stream of molten material exiting from thenozzles 25 to form polymeric filaments in a manner known in the art. Theattenuating mechanisms 28 accordingly may be of any design known in the art including that described in U.S. Pat. No. 4,173,443, the disclosure of which is incorporated herein by reference. - Each of the
attenuating mechanisms 28 is associated with agas heater 29 andgas supply source 31.Gas supply source 31 provides gas viaconduit 32 and appropriate valves and regulators to theheater 29 where its temperature is elevated or lowered to the desired temperature via the temperature control 30. The gas is then fed from theheater 29 throughconduit 34 to theattenuating mechanisms 28. Attenuatingmechanisms 28 may be provided with gas from a common supply source, heater and temperature control, or alternatively, separately controlled gas sources may be employed for eachattenuating mechanism 28. - The filament delivery system16 is substantially identical to that of the
system 14 described above. Specifically, the system 16 includes aheater block 38, an independently driven positivedisplacement metering pump 36, and motor 39 andmotor elements 40.Heater block 38 is provided with a plurality ofnozzles 42 andtemperature control 41. The system 16 is also provided with a plurality of attenuatingmechanisms 44 associated with thenozzles 42. Pressurized gas is passed to each attenuatingmechanisms 44 from agas supply source 45 viaconduit 46, aheater 48 andconduit 49.Temperature control 50 regulates and controls the temperature produced byheater 48. The provision of separatefilament delivery systems 14 and 16 enables separate control and production of polymeric filaments produced by eachsystem 14 and 16. - Each of the
delivery systems 14 and 16 is capable of producing a plurality of discrete,continuous filaments orifices mechanisms filament collection device 54 illustrated in FIG. 1. Thefilament collection device 54 includes a central,rotatable mandrel 55 which extends from adrive motor 58. Adjacent to themandrel 55 and spaced therefrom is apress roll member 56 rotatable about theaxis 57. During operation, the plurality offilaments mandrel 55 and collected thereon in a manner known in the art. Therotating press roller 56 engages the filaments which have accumulated on therotating mandrel 55. As sufficient filaments are built up on themandrel 55, thepress roller 56 forces thefilament mass 59 off the axial end of themandrel 55 in the direction of the arrow 53 to produce acontinuous filament mass 59 of indefinite length. The entirefilament collection device 54 is known to those skilled in the art and may be similar to that described in U.S. Pat. No. 4,240,864, the disclosure of which is incorporated herein by reference. - The apparatus of FIG. 1 has been demonstrated to be adequate for producing coreless depth filters in which
filament delivery system 14 is configured to produce polymeric filaments having relatively large diameters (i.e., greater than 15 microns), and filament delivery system 16 is configured to produce polymeric filaments having smaller diameters (i.e., 1-15 microns). A depth filter element produced thereby has a tubular configuration with an innermost cylindrical zone of relatively large polymeric filaments which defines a support for an outer cylindrical zone of the smaller polymeric filaments which form a filtration zone of the depth filter. The present invention, however, is directed to an novel apparatus configuration and method for continuously producing an improved depth filter for use with a core member. - The improved depth filter of the present invention is generally characterized by an inner cylindrical mass of very small diameter polymeric filaments (i.e., 0.5-1.5 microns), a calendered (i.e. smooth) inner cylindrical surface and an outer cylindrical mass of coarser, large diameter polymeric filaments (i.e., 4-10 microns or greater). While cored depth filters having a filtration zone near the core are known in the art, production of such filters is discontinuous and requires that the relatively fine polymeric filaments comprising the filtration zone to be deposited directly on a core member supported by a mandrel. The improved apparatus configuration and process of the present invention overcomes the limitations of such a discontinuous depth filter production process by enabling a continuous process whereby very small diameter polymeric filaments (0.5-1.5 microns) are directly applied to and collected on a mandrel of a filament collection device, such as
filament collection device 54 shown in FIG. 1, with larger diameter polymeric filaments thereafter applied over the small filament mass. A calendered inner cylindrical surface of the depth filter, comprised of a portion of the mass of very small polymeric filaments, results from this process, which allows for an easy, post-production insertion of a core member known in the art. The process of the present invention therefore enables a continuous production of a depth filter element independent of a core member to be used with the depth filter. - For a more complete understanding of the present invention, reference is made to FIG. 2, which is a schematic diagram illustrating the apparatus of FIG. 1 configured for continuously producing a depth filter element of the present invention. As shown in FIG. 2, four
filament producing devices nozzle 25 and attenuatingmechanism 28 of FIG. 1.Filament producing devices mandrel 110. The nozzle of eachfilament producing device axis 112 that is perpendicular to axis 108 andmandrel 110.Axis 112 generally corresponds to the flow axis of molten polymer exiting the nozzle orifice. In one preferred embodiment,filament producing devices mandrel 110. As depicted, the attenuating mechanism of filament producing device 100 is oriented to produce gas streams which are generally aligned and parallel withaxis 112. This orientation results in a flaredfilament pattern 114 being directed towardmandrel 110. -
Filament pattern 114 is comprised of polymer filaments having very small diameters of between about 0.5 micron to about 1.5 microns. As a non-limiting example, polymer filaments offilament pattern 114 were produced in the depth filter of the instant invention by passing polypropylene heated to a temperature of 420° C. to about 425° C. through a nozzle having an orifice size of about 0.011 inch at a rate of about 3.8 pounds per hour and passing a heated gas at a temperature of 400° C. at a rate of 11 cubic feet per minute over the molten polymer stream exiting the nozzle orifice. It will be appreciated that a person skilled in the art can readily determine other parameter combinations suitable to form very fine filaments of between about 0.5 microns to about 1.5 microns, and that the parameters necessary to form such very fine filaments will vary according to the particular polymer material used. - The attenuating mechanism of
filament producing device 102, however, is oriented to produce gas streams which are directed at an angle, relative toaxis 112 ofdevice 102, away fromfilament pattern 114. By orienting the attenuating mechanism ofdevice 102 in this manner, a flaredfilament pattern 116 is produced which substantially avoids overlapping withfilament pattern 114. The objective of this configuration is to allow polymeric filaments from device 100 to accumulate and form a mass onmandrel 110 with minimal mixing of polymeric filaments fromdevice 102. In one preferred embodiment, the attenuating mechanism ofdevice 102 is oriented to produce gas streams away fromfilament pattern 114 at an angle of between about 30° to about 40° relative toaxis 112 ofdevice 102. In the depth filter of the present invention, the polymer filaments offilament pattern 116 have diameters of between about 4 microns to about 8 microns. By way of a non-limiting example, the filaments ofpattern 116 were produced by passing polypropylene heated to a temperature of 420° C. to about 425° C. through a nozzle having an orifice size of about 0.011 inch at a rate of about 3.8 pounds per hour and passing a gas at ambient temperature at a rate of 11 cubic feet per minute over the molten polymer stream exiting the nozzle orifice. - With respect to
device 104, the attenuating mechanism is oriented to produce gas streams at an angle directed towardfilament pattern 116 to produce afilament pattern 118 which substantially overlaps withfilament pattern 116. In one preferred embodiment, the attenuating mechanism ofdevice 104 is oriented to produce gas streams at an angle of between about 5° to about 10° relative toaxis 112 ofdevice 104. In the depth filter of the present invention, the polymer filaments offilament pattern 118 have diameters of between about 6 microns to about 10 microns. By way of a non-limiting example, the filaments ofpattern 118 were produced by passing polypropylene heated to a temperature of 390° C. through a nozzle having an orifice size of about 0.011 inch at a rate of about 5.1 pounds per hour and passing a gas at ambient temperature at a rate of 11 cubic feet per minute over the molten polymer stream exiting the nozzle orifice. - The attenuating mechanism of
device 106 is oriented to produce a gas stream angled towardfilament pattern 118. In a preferred embodiment, this orientation results in a gas stream directed at an angle of between about 10° to about 20° relative toaxis 112 ofdevice 106. In the described configuration,device 106 producesfilament pattern 120, which substantially overlapsfilament pattern 118. In the depth filter of the present invention, the polymer filaments offilament pattern 120 have diameters of between about 6 microns to about 10 microns. By way of a non-limiting example, the filaments ofpattern 120 were produced by passing polypropylene heated to a temperature of about 390° C. through a nozzle having an orifice size of about 0.016 inch at a rate of about 5.1 pounds per hour and passing a gas at ambient temperature at a rate of 16 cubic feet per minute over the molten polymer stream exiting the nozzle orifice. - As further shown in FIG. 2, filament producing device100 is oriented such that
filament pattern 114 is generally centered on nip 122 ofpress roller 124. In one embodiment,filament pattern 114 has a width of about 6 to 8 inches atmandrel 110.Filament pattern 116 is intended to be substantially separate fromfilament pattern 114, with sufficient overlap or intermingling of each pattern, however, to prevent separation or delamination of the filament mass formed.Filament pattern 114 therefore accumulates onmandrel 110 as a generally homogenous filter mass.Filament patterns filament pattern 114. - As more completely shown in FIG. 2A, which is an enlarged view of the collection device of FIG. 2, an accumulated mass of
filaments filament pattern 114 are produced on opposite sides of nip 122 ofpress roller 124. In one embodiment,press roller 124 is oriented at an angle relative to mandrel 110 withnip 122 in contact withmandrel 110. As a non-limiting example,outer surface 123 ofpress roller 124 is angularly displaced by about 3° relative tomandrel 110. So configured, sufficient filaments fromfilament pattern 116 are intermixed with those offilament mass 114 b that thefilament mass 114 a is drawn past nip 122 as thecollective filament mass 126 is moved alongmandrel 110 in the direction indicated byarrow 128. As the filaments fromfilament mass 114 a are drawn past nip 122, they are compressed between nip 122 andmandrel 110 to form a dense layer of the very small diameter filaments produced infilament pattern 114. Because of the small diameter of these filaments, the filaments are able to sufficiently cool in the time it takes for them to accumulate and pass by nip 122. As a result, no cross-welding of filaments results asfilament mass 114 a is compressed bynip 122. Furthermore, because of the angular placement ofpress roller 124, compression of filaments incollective filament mass 126 varies along the length ofpress roller 124. This results in a filament mass having a varying density gradient, with the filament density offilament pattern 114 being generally greater than that of the filament mass comprised offilament patterns - It was originally believed that very fine polymer filaments of less than 1.5 microns could not be successfully applied to a collection mechanism employing a spinning mandrel and press roller without roping of the filaments or sticking to the mandrel. It was also not expected that a smooth calendered inner cylindrical surface would result to a filament mass produced from the method of the present invention. Rather, it was anticipated that a continuous process as described would produce a surface defined by fine, fuzzy filaments, which could hamper insertion of a core member. The method of the present invention, however, demonstrates a way of continuously producing at an advantageous rate a filament mass suitable for making a depth filter element having an inner filtration zone comprised of very fine filaments and an outer filtration zone comprised of larger filaments, and which produces a smooth inner cylindrical surface that allows for subsequent easy insertion of a core member.
- FIG. 3 illustrates a cross-sectional view of the
filament mass 126 produced by the present invention. As generally depicted,filament mass 126 is comprised of an inner cylindricalcalendered layer 130, which is contiguous with aninner filtration zone 132 comprised of a relatively homogenous zone of very fine polymer filaments have diameters of less than about 1.5 microns, and generally in a range of between about 0.5 micron and 1.5 microns.Calendered layer 130 results from the compression of filaments having the same morphology and size as those found infiltration zone 132. In one embodiment, calendered layer has a thickness of about 5 mils which defines a smooth innercylindrical surface 134 offilament mass 126.Filament mass 126 is further comprised of anouter filtration zone 136 formed by a heterogenous filament mass having intermixed filaments having diameters ranging in size from about 4 microns to about 10 microns. In one embodiment,filament mass 126 has a mass of 110 grams per ten inch section. - Depth filter elements formed in the manner described relative to FIGS. 1, 2 and2A and having the characteristics described relative to FIG. 3 have demonstrated excellent particle filtration and fluid throughput capabilities. For example, the depth filter of the present invention has demonstrated to be 99.9% effective at removing 1 micron particles. Furthermore, the depth filter element of the present invention allows fluid throughput with a minimal drop in fluid pressure across the filter (e.g. pressure drops of about 1.5 p.s.i.d. per gallon per minute of liquid flow per ten inch element).
- Although the description of the preferred embodiment and method has been quite specific, it is contemplated that various modifications could be made without deviating from the spirit of the present invention. Accordingly, it is intended that the scope of the present invention be dictated by the appended claims rather than by the description of the preferred embodiment.
Claims (16)
1. A non-woven filter cartridge comprising:
a cylindrical core member;
a first cylindrical mass of essentially continuous, intertwined, and thermally bonded polymer filaments adjacent to the core member, the polymer filaments of the first mass having diameters of less than about 1.5 microns;
a second cylindrical mass of essentially continuous, intertwined, and thermally bonded polymer filaments adjacent to the first mass of polymer filaments, the polymer filaments of the second mass having diameters greater than about 1.5 microns;
wherein the filter cartridge has an efficiency in removing 1 micron particles greater than or equal to at least about 99.9%, and wherein a pressure drop across the filter cartridge is less than about 3 pounds per square inch for every gallon per minute of flow through a 10 inch long section of the filter cartridge.
2. The non-woven filter cartridge of claim 1 wherein the filaments of the first mass have diameters less than about 1 micron.
3. The non-woven filter cartridge of claim 1 wherein the filaments of the second mass have diameters ranging from about 4 microns to about 10 microns.
4. The non-woven filter cartridge of claim 1 wherein the pressure drop across the filter cartridge is about 1.5 pounds per square inch for every gallon per minute of flow through the 10 inch section of the filter cartridge.
5. The non-woven filter cartridge of claim 1 wherein the first mass of polymer filaments comprises a first filament zone and a second filament zone, the first filament zone defining a calendered layer having a density of filaments which is substantially greater than that of the second filament zone.
6. The non-woven filter cartridge of claim 5 wherein the first filament zone is adjacent to the core.
7. The non-woven filter cartridge of claim 6 wherein the calendered layer has a thickness of about 5 mils.
8. The non-woven filter cartridge of claim 7 wherein the second filament zone and the second cylindrical mass are each substantially thicker than about 5 mils.
9. The non-woven filter cartridge of claim 1 further comprising:
a transition region including filaments from the first mass intertwined with filaments from the second mass.
10. The non-woven filter cartridge of claim 1 including a density gradient between the first filament mass and the second filament mass.
11. A non-woven filter cartridge comprising:
a cylindrical core member;
a first cylindrical mass of essentially continuous, intertwined, and thermally bonded polymer filaments positioned over the core member, the first mass of polymer filaments comprised of filaments having a diameter of less than about 1.5 microns, wherein a portion of the first mass of polymer filaments forms a calendered layer positioned adjacent the core member; and
a second cylindrical mass of essentially continuous, intertwined, and thermally bonded polymer filaments disposed over the first mass of polymer filaments, at least some of the polymer filaments in the second mass being intertwined with some of the polymer filaments in the first mass, the second mass of polymer filaments comprised of filaments having a diameter of greater than about 1.5 microns;
wherein the filter cartridge has an efficiency in removing 1 micron particles of at least about 99.9% and wherein a pressure drop across the cartridge is less than about 3 pounds per square inch per gallon per minute of fluid flowing through a 10 inch long section of the filter cartridge.
12. The non-woven cartridge of claim 11 wherein the filaments of the first mass have diameters of between about 0.5 microns and about 1 micron.
13. The non-woven filter cartridge of claim 11 wherein the filaments of the second mass have diameters ranging from about 4 microns to about 10 microns.
14. The non-woven filter cartridge of claim 11 wherein the filaments of the second mass have diameters larger than the diameters of the filaments of the first mass.
15. The non-woven filter cartridge of claim 11 wherein the calendered layer has a thickness of about 5 mils.
16. The non-woven filter cartridge of claim 15 wherein the second cylindrical mass is substantially thicker than about 5 mils.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/056,715 US20020063092A1 (en) | 1999-04-21 | 2002-01-25 | Non-woven depth filter cartridge |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/296,070 US6358417B1 (en) | 1999-04-21 | 1999-04-21 | Non-woven depth filter element |
US10/056,715 US20020063092A1 (en) | 1999-04-21 | 2002-01-25 | Non-woven depth filter cartridge |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US09/296,070 Division US6358417B1 (en) | 1999-04-21 | 1999-04-21 | Non-woven depth filter element |
Publications (1)
Publication Number | Publication Date |
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US20020063092A1 true US20020063092A1 (en) | 2002-05-30 |
Family
ID=23140489
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
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US09/296,070 Expired - Lifetime US6358417B1 (en) | 1999-04-21 | 1999-04-21 | Non-woven depth filter element |
US10/056,715 Abandoned US20020063092A1 (en) | 1999-04-21 | 2002-01-25 | Non-woven depth filter cartridge |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US09/296,070 Expired - Lifetime US6358417B1 (en) | 1999-04-21 | 1999-04-21 | Non-woven depth filter element |
Country Status (6)
Country | Link |
---|---|
US (2) | US6358417B1 (en) |
EP (1) | EP1200170A4 (en) |
JP (1) | JP4721521B2 (en) |
AU (1) | AU4478700A (en) |
CA (1) | CA2370787C (en) |
WO (1) | WO2000062890A1 (en) |
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US20060278574A1 (en) * | 2003-06-06 | 2006-12-14 | Pall Corporation | Fluid treatment element |
CN102374211A (en) * | 2010-08-23 | 2012-03-14 | 贺勍 | Cascade combined type coarse and fine granule grading filter cartridge and combination method thereof |
US11845019B2 (en) * | 2013-11-06 | 2023-12-19 | Bl Technologies, Inc. | Large format melt-blown depth filter cartridge |
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US6358417B1 (en) * | 1999-04-21 | 2002-03-19 | Osmonics, Inc. | Non-woven depth filter element |
WO2003035958A1 (en) * | 2001-10-23 | 2003-05-01 | Osmonics, Inc. | Three-dimensional non-woven media, filter and process |
US20030203694A1 (en) * | 2002-04-26 | 2003-10-30 | Kimberly-Clark Worldwide, Inc. | Coform filter media having increased particle loading capacity |
US8114183B2 (en) * | 2005-09-20 | 2012-02-14 | Cummins Filtration Ip Inc. | Space optimized coalescer |
US7674425B2 (en) * | 2005-11-14 | 2010-03-09 | Fleetguard, Inc. | Variable coalescer |
US7959714B2 (en) | 2007-11-15 | 2011-06-14 | Cummins Filtration Ip, Inc. | Authorized filter servicing and replacement |
US20070062886A1 (en) * | 2005-09-20 | 2007-03-22 | Rego Eric J | Reduced pressure drop coalescer |
US7828869B1 (en) | 2005-09-20 | 2010-11-09 | Cummins Filtration Ip, Inc. | Space-effective filter element |
US8231752B2 (en) * | 2005-11-14 | 2012-07-31 | Cummins Filtration Ip Inc. | Method and apparatus for making filter element, including multi-characteristic filter element |
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Also Published As
Publication number | Publication date |
---|---|
JP2002542009A (en) | 2002-12-10 |
EP1200170A1 (en) | 2002-05-02 |
EP1200170A4 (en) | 2005-01-12 |
AU4478700A (en) | 2000-11-02 |
US6358417B1 (en) | 2002-03-19 |
JP4721521B2 (en) | 2011-07-13 |
CA2370787C (en) | 2012-06-12 |
CA2370787A1 (en) | 2000-10-26 |
WO2000062890A1 (en) | 2000-10-26 |
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