Classifications

• • 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
  • B01D29/01—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 flat filtering elements
  • B01D29/05—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 flat filtering elements supported
  • B01D29/07—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 flat filtering elements supported with corrugated, folded or wound filtering 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
  • B01D2201/00—Details relating to filtering apparatus
  • B01D2201/12—Pleated filters
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01D—SEPARATION
  • B01D2201/00—Details relating to filtering apparatus
  • B01D2201/29—Filter cartridge constructions
  • B01D2201/291—End caps
  • B01D2201/295—End caps with projections extending in a radial outward direction, e.g. for use as a guide, spacing means

Definitions

• This disclosure pertains to a fuel water separator and particulate filter designed to provide high water and particulate removal efficiency.
• the disclosure of this application in particular relates to the disclosures of U.S. Application No. 12/820,784, filed on June 22, 2010, and entitled “TWO STAGE WATER SEPARA TOR AND PARTICULATE FILTER," and U.S. Application No. 12/820,791 , filed on June 22, 2010, and entitled “MODULAR FILTER ELEMENTS FOR USE IN A FILTER-IN-FILTER
• Fluid filters are widely known and used in various filtration systems and applications, for instance where there is a need for particle and/or fluid separation from a working fluid in a protected system.
• foe! filtration systems for engines are well known and can employ fluid filters that are aimed at water and particle separation from the fuel .
• Filter cartridges in some of these filters have one filter element with media configured to coalesce water, and have another filter element thai has media configured to further filter the fuel and separate the coalesced water from the fuel ,
• the filter elements are arranged in a concentric filter within a filter configuration., where an outer filter element surrounds an inner filter element.
• a filter that has improved fuel water separation over the life of the fi lter.
• the filter is a two stage configuration, for example a concentric filter within a filter configuration., with the first or outer stage being configured primarily to coalesce water from, die fuel or other fluid with which the filter is used, and the second or inner stage being configured to separate coalesced water from the fluid and also remove fine solid contaminants from the fluid.
• the filter is preferably configured for use wiih fuel, such as ultra low sulfur diesel (UI.SD) or hiodiesel, but the concepts of the filter described herein could be employed with any type of fluid requiring water separation from the fluid, for example hydraulic fluid, oil or lubrication fluid, air, and the like.
• IFTs inierfaciai tensions
• the filter can be made from all polymeric materials.
• the two stages of the filter, including the media and endcaps can be made of thermoplastic material Cs) to facilitate disposal of the filter such as by recycling or incineration.
• thermoplastic material Cs thermoplastic material
• the use of all poly meric (for example thermoplastic) media layers allows better bonding of adjacent media layers to each other.
• polymeric media provides better chemical resistance/compatibility compared to media formed from other non-polymeric material
• certain media properties for example pore size and pore size distribution, are better controlled using polymeric media.
• the filter will primarily be described as a two stage configuration, the first stage could be used by itself in a single stage configurati on, used in combination with different second stage designs, or used in combination with two or more additional stages.
• the second stage could be used b itself in a single stage configuration, used in combination with different first stage designs, or used in combination with two or more additional stages.
• a coalescing fluid filter in one embodiment, includes a pleated cylinder of polymeric media configured to coalesce water that is in fluid.
• the pleated cylinder of polymeric media has pleat valleys and downstream pleat tips, and release sites at or adjacent the downstream pleat tips.
• the pleated cylinder of media has opposite ends that are fixed to endcaps, for example using an adhesive, embedding the ends in the endcaps which are preferably made of polymeric (for example thermoplastic) material, using mechanical fasteners, or using other suitable fixation techniques.
• the pleated cylinder can have a single layer or a plurality of layers of media.
• the release sites can be located at. for example, junctures of the downstream pleat tips and a non-pleated cylinder of polymeric (for example thermoplastic) media, or
• the distance between the inner tips of the pleated cylinder and the non-pleated cylinder is such that there is no significant gap or separation between the two.
• the pleat tips of the pleated cylinder can be fixed to or not fixed to the outer surface of the non-pleated cylinder.
• a support cylinder for supporting the media can be disposed between the pleat tips and the non-pleated cylinder, or disposed within and surrounded by the non-pleated cylinder.
• a first stage is di posed upstream of second stage with a. gap therebetween.
• the first and second stages can be in a filter in filter arrangement:, with the first stage being an outer stage and the second stage being an inner stage.
• the outer stage includes a pleated cylinder of polymeric (for example thermoplastic) .media configured to coalesce water that is in a fluid.
• the pleated cylinder has pleat valleys and downstream pleat tips, and release sites at the downstream pleat tips.
• the inner stage includes a non-pleated cylinder of polymeric (for example thermoplastic) media surrounding a multi-layer pleated cylinder of polymeric (for example thermoplastic) media, and the inner stage is configured to separate coalesced, water from the fluid and remove fine solid contaminants from the fluid.
• polymeric for example thermoplastic
• the inner stage is configured to separate coalesced, water from the fluid and remove fine solid contaminants from the fluid.
• the outer stage and the inner stage may be fixed to endcaps.
• the endcaps may be separate so that the outer stage includes endcaps attached to opposite ends thereof and the inner stage includes endcaps attached to opposite ends thereof.
• the outer stage and the inner stage may share one or both endcaps, whereby single, common endcap is attached to one end of each of the outer stage and the inner stage, and a. single, common endcap is attached to the opposite end of each of the outer stage and the inner stage.
• Figure 1 is an exploded view of one embodiment of a two stage filter described herein.
• Figure 2 is a cross-sectional view of the two stage filter of Figure i in an assembled state.
• Figure 3 is an exploded view of another embodiment of a two stage filter that can employ the concepts described herein.
• Figure 4 is an exploded view of the first or outer stage of the two stage filter of Figures 1 and 2.
• Figure 5 is an exploded view of the second or inner stage of the two stage filter of Figures 1 and 2.
• Figures 6A-6C show different configurations of the media layers of the .first stage.
• Figure 7 shows an exemplary configuration of the media layers of the second stage.
• Figure 8 shows an example of an outer stage with slits, holes or apertures formed in the downstream pleat tips to form release sites.
• a two stage filter configuration with a first stage that is configured primarily to coalesce water from a fluid with which the filter is used, and a second stage that is configured to separate coalesced water from the fluid and also remove fine solid
• the fluid initially flows through the first stage followed by flowing through the second stage.
• the filter will primarily be described as having a two stage configuration, the first stage could be used by itself in a single stage configuration, used in combination with different second stage designs than those described herein, or used in combination with two or more additional staaes.
• the second stage coul d be used by itself in a single stage configuration, used in
• the filter is preferably configured for use with fuel, preferably diesel fuel such as ULSD, biodiesel or other fuels having low IFTs, to filter the fuel pri r to reaching an engine where the foe! is combusted.
• fuel preferably diesel fuel such as ULSD, biodiesel or other fuels having low IFTs
• ULSD ULSD
• biodiesel or other fuels having low IFTs to filter the fuel pri r to reaching an engine where the foe! is combusted.
• the concepts of the filter described herein could be employed with any type of fluid requiring water separation from the fluid, for example hydraulic fluid, oil or lubrication fluid, air, and the like.
• Figures 1 and 2 illustrate an example of a two stage filter 10 having a first, upstream stage i2 that is configured primarily to coalesce water from the fluid, and a second stage 14 downstream from the first stage 12 that is configured to separate coalesced water from the fluid and also remove fine solid contaminants from the fluid.
• the filter 10 is a filter in filter construction configured for outside-in flow, with the first stage 12 being an outer coal seer stage and the second stage 14 being an inner separator stage, with the outer stage surrounding the inner stage with a gap 16 therebetween.
• the filter 10 is configured to be disposed within a filter housing with the housing then being secured to a filter head.
• An example of this ty pe of filter housing and attachment to a head employed with a single stage filter is described in ' U.S. Patent Application Publication No. 2007/0267338.
• An endcap 18 is connected to a first or upper end of the first stage 12 and an end cap 20 is connected to a second or l were end of the first stage.
• the endcaps 18, 20 are made of polymeric material, for example thermoplastic material, and the ends of the first stage media are suitably fixed to the endcaps, for example using an adhesive, embedding the ends of the media in the endcaps, or other suitable fixation techniques.
• the endcaps 18, 20 can be made of non -polymeric material, for example metal, with the ends of the media fixed to the metal endcaps using a potting materia! know hi the art.
• the endcap I S includes a central opening 22 defined by a sleeve 23 that forms a fluid outlet passageway for fluid that has been filtered by the filter 10.
• An elastornerie gasket 25 surrounds the sleeve 23 for sealing engagement with the filter head when the .filter and filter housing are installed.
• the endcap 20 includes an opening 24 that allows insertion of the second stage 14 within the fi rst stage 12 during assembly of the filter.
• an endcap 26 is connected to a first or upper end of the second stage 14 and an endcap 28 i s connected to a second or lower end of the second stage.
• the endcaps 26, 28 are also made of polymeric material, for example thermoplastic material, and the ends of the second stage media are suitably fixed to the endcaps, for example using an adhesive, embedding the ends of the media in the endcaps. or other suitable fixation techniques.
• the endcaps 26, 28 are made of non- polymeric material, for example metal, with the ends of the media fixed to the metal endcaps using a potting material known in the art.
• the endcap 26 includes a central opening 30 (see Figures 1, 2 and 5) that allows the endcap 26 to slide over and onto a cylindrical tube 32 (see Figure 2) extending downwardly from the endcap 1.8 and forming a part of the central opening 22,
• the endcap 28 is generally closed to prevent flow of fuel through the endcap 28.
• the first stage 12 and the second stage 1 can be connected together using any suitable connection technique.
• An example of a suitable connection technique is
• Figures I and 2 illustrate that the endcaps I S, 20 of the first stage 12 are separate from the endcaps 26, 28 of the second stage 14.
• the first stage 12 and the second stage 14 may share common endcaps, whereby a single, common endcap Is attached to the first or upper ends of the first stage and the second stage, and a single, common endcap is attached to the second or lower ends of the first stage and the second stage.
• An example of a fi rst stage and a second stage sharing common endcaps can be found in U.S. Patent Applicati n Publication No. 2007/0289915.
• FIG 3 is an exploded view of another embodiment of a two stage filter 40 configured as a filter in .filter construction for out side-in flow, that can employ the inventive concepts described herein, with a first stage 42 being an outer coaiescer stage and a second stage 44 being an inner separator stage, with the outer stage surrounding the inner stage with a gap therebetween.
• the filter media of the first stage 42 and the filter media of the second stage 44 are connected to endcaps 46, 48 and 51 , 53, respectively., in the same manner as described above for the endcaps 18, 20, 26, 28, although a common endcap can be used at each end as well.
• the filter 40 is configured to be installed over standpipe within a filter housing. Further details on this general type of two stage filter construction are disclosed in U.S. Patent Application Publication No. 2009/0065425,
• Fitiures 4 and 5 illustrate details of the first or outer coaiescer stage 12 and the second or inner separator stage 14 of the filter 10, respectively.
• the stages 42, 44 of the filter 40 are configured substantially the same as the stages 12. 14, except for the endcaps, and will not be separately described.
• the first or outer coalesce* " stage 12 includes a pleated cviirider 50 of polymeric media that when assembled surrounds a non-pleated cy linder 52 of polymeric media.
• the second or inner separator stage 14 includes a non-pleated cylinder 54 of polymeric media that when assembled surrounds a pleated cylinder 56 of polymeric media.
• the pleated media 50 includes inner (i ,e. downstream) pleat tips 60 that in use are positioiied closely adjacent to the outer surface of the cylinder 52 such that there is no significant gap or separation between the two.
• the inner pleat tips 60 are in intimate contact with the outer surface of the cylinder 52.
• the inner pleat tips 60 may or may not be attached or fixed to the outer surface of the cylinder 52, but are positioned closely adjacent to, for example in contact with, the cylinder.
• Figure 6 A shows a cross-sectional view of one embodiment of the first stage 12 with the thickness of the layers being exaggerated for clarity.
• the thickness of the layers being exaggerated for clarity.
• downstream pleat tips 60 of the pleated media 50 are in direct, inti mate contact with the outer surface of the non-pleated media. 52, with the tips 60 being optionally fixed, or not fixed, to the outer surface.
• the embodiment in Figure 6.4 does not utilize a center tube, screen, cage or other supporting structure for the media of the first stage 12. in this case, the non-pleated media 52 and/or the pleated media 50 would he stiff enough to act as its own supporting structure.
• Figure 6B shows another embodiment of the first stage, where a center tube, screen, cage, spring or other support cylinder structure 70 for the media of the first stage 12 is located downstream of and adjacent to the non-pleated media cylinder 52.
• the support structure 70 if used, can be formed from a polymeric material, for example thermoplastic material, and is provided with openings to allow fluid to flow through the first stage to the second stage.
• the optional support structure 70 is used to prevent the inner non-pleated media 52 from collapsing under the flow and pressure drop of the fluid, ideally, however, the pleated 50 and non-pleated media 52 together provide sufficient strength and stiffness rendering use of the support structure 70 unnecessary.
• the non-pleated media 52 may be affixed to the support structure 70 only at the endcaps because there is no need to bond it elsewhere due to the fluid pressure during use. Nonetheless, the non-pleated media 52 can be fixed to the support structure 70 at any locations one finds suitable.
• Figure 6C shows another embodiment of the first stage, where the support structure 70 is located between, adjacent to, and touches both the upstream pleated media 50 and the downstream non-pleated media 52.
• the suppor structure 70 provides support to the pleated media 50, whose inner pleat tips 60 are in intimate contact with it, while the non-pleated media. 52 is located inside and downstream of, and in intimate contact with, the support structure 70.
• the non-pleated media 52 may be thermally welded to or injection molded with the polymeric support staicture 70 to affix it to the support structure.
• the numerals 1-5 indicate, in order from upstream to downstream in the direction of fluid flow, the different layers of media of one example of the pleated media 50.
• the media layers of the pleated media 50 are made of polymeric materials, for example thermoplastic .materials.
• the pleated media 50 can include three l ayers of polymeric, fibrous filter media. (1 -3), one layer of polymeric nanofiber media (4), and. a final layer (5) of polymeric, fibrous media.
• the non-pleated media 52 is a single layer of polymeri c, fibrous medi formed as a tube and placed inside the pl eated media 50 with its upstream face either in direct contact with the pleaied media via the pleat tips 60 or in indirect contact with the pleated media 50 via the intermediary support structure 70.
• the axial lengths L .i (see Figure 2) of the layers of the pleated media 50, the non-pleated media 52, and the support structure (if used) are the same, with the ends of each embedded into the endcaps 18, 20 or potted in an adhesi ve, e.g.,
• polyurethane or otherwise attached to the endcaps in a manner to prevent bypass of unfiltered fluid around the media.
• Figures 6A-6C show five layers for the pleated media 50, and one layer for the non-pleated media 52, more or less layers may be used for the pleated media 50 and the non-pleated media 52 depending, for example, on the requirements of the application and coalescer desi g n.
• the function and design constraints for each layer of the first ' or coalescer stage 12 and how and when they are used will now be described.
• examples of each layer are described in Table 1 for three different media combinations, referred to as Coalescer X, Y, and Z. It is noteworthy that these three media
• the media combinations, materials and properties listed in Table I are exemplary only, and reflect combinations, materials and properties that the inventors believe, at the time of filing thi s application, would provide adequate performance results with respect to high pressure common rail diesel fuel systems running on ULSD or biodiesel Further research may reveal suitable media combinations, materials and material properties other than those listed in Table L both with respect to high pressure common rail diesel fuel systems running on ULSD or biodiesel and with, respect to oilier types of fluids on other types of systems.
• thermoplastic materials such as polyamide, polybutylene terephihalaie, and polyethylene terephthalate
• the media layers are not limited to these specific thermoplastic materials.
• Other thermoplastic materials could be used.
• the media layers are not limited to thermoplastic materials.
• Other polymeric materials could be used for the media layers including, but not. limited to, thermosetting plastics.
• gsm is defined as grams per square meter and cfm is defined as cubic feet per minute; thickness is measured from upstream to downstream relative to the primary direction of fluid flow through the media layers.
• Coalescer X includes at least 6 media layers, and an optional supporting structure can be used. Layers 1-5 form the pleated media 50 and layer 6 forms the non-pleated cylinder 52. Coalescer X may be referred to as a velocity change coalescer (see for example PCX Publication o WO 2010/042706) for use in a filter-in- filter design.
• Layer 1 functions as a prefilter and reduces the pressure drop across the outer stage 12.
• Layer 1 is more open (e.g. has a higher porosity, larger pore size, larger mean fiber diameter, higher Frasier permeability, and/or lower contaminant removal efficiency) than Layer 2.
• Layer 2 functions to capture fine emulsified droplets, for example water droplets in ULSD fuel.
• Layer 2 is tighter (e.g. having a lower porosity, smaller pore size, smaller mean fiber diameter, lower Frasier permeability, and/or higher contaminant removal efficiency) than Layer 3.
• Layer 3 functions to reduce the fluid velocity within the layer and provide a space for droplets captured in Layer 2 to drain to, accumulate and coalesce.
• the physical properties of Layer 3 are such that the fluid velocity in this layer is less than in Layer 4.
• Layer 3 is more open (e.g. has a higher porosity, larger pore size, larger mean fiber diameter, higher Frasier permeability, and/or lower contaminant removal efficiency) than Layer 4.
• Layer 4 functions to capture droplets that were not captured by the previous layers, especially the finer droplets, and to serve as a semi -permeable barrier to the passage of captured droplets.
• the semi-permeable barrier function causes droplets to concentrate and accumulate in Layer 3, giving them more time and greater probability for coalescence to occur.
• Layer 4 also gives rise to localized increased fluid velocity and a transient increase in drop surface area, which further enhances coalescence.
• the .fluid velocity in Layer 4 is higher than m Layer 5.
• Layer 4 is tighter (e.g. has a lower porosity, smaller pore size, smaller mean fiber diameter, lower Frasier permeability, and/or higher contaminant removal efficiency) than Layer 5.
• Layer 4 can be, for example, a thermoplastic nanofiber filter media with fibers having a diameter of less than about 1 urn, which helps achieve the very high water removal efficiency requirements for modern high pressure common rail dieseS fuel systems running on ULSD or hiodiesel.
• Layer 4 can be formed using an e!ectrob!owing process, but can be formed using other suitable processes.
• Layer 4 can also have a maximum to mean pore size ratio of less than about 3, and more preferably less than about 2.
• Layer 5 functions to create a lower velocity environment for the coalesced drops formed in the previous layers to collect in and drain through prior to release.
• Layer 5 is more ope (e.g. has a higher porosity, larger pore size, larger mean fiber diameter, higher Frasier permeability, and/or lower contaminant removal efficiency) than Layer 4.
• La er 6 i.e. the non-pleated cylinder 52
• Layer 6 is more open (e.g. has a higher porosity, larger pore size, larger mean fiber diameter, higher Frasier permeability, and/or lower contaminant removal efficiency) than Layer 5.
• Layer 6 also provides structural support for the first stage I 2 as discussed above for Figure 6A, eliminating the need for a separate support structure.
• Coalescer Y may he referred to as a single layer surface coalescer (see U.S. Patent Application Serial No. 61/ 1 78,738 filed on May 15, 2009 and U.S. Patent Application Serial No. 12/780,392 filed on Ma 14, 2010) for use in a fil term-filter design.
• the first layer functions to provide a semi-permeable barrier to the passage of fine emulsified droplets, forcing them to concentrate at its upstream surface. In this manner, droplets have time and a suitable environment for coalescence and drop growth to occur.
• Layer 4 is a relatively tight layer with characteristics comparable to Layer 4 in Coalescer X or even tighter.
• Layer 4 relies on sieving to prevent passage of tine droplets, and in this example can be a thermoplastic nanofiber filter media with fibers having a diameter of less than about I pro, a mean pore size smaller than the mean drop size of the influent droplets and can have a maximum to mean pore size ratio of less than about 3, and preferably less than about 2.
• Layer 4 can be formed using an
• electroblowing process but can be formed using other suitable processes.
• Layer 5 is optional and provides structural support for Layer 4, if required, and serves as a drainage path for coalesced drops forced through Layer 4.
• Layer 5 also connects Layer 4 to the release Layer 6 (i.e. non-pleated cylinder 52).
• Layer 5 creates a lower velocity environment for the coalesced drops to collect in and drain through prior to release.
• Layer 5 (if used) is more open than Layer 4 and is structurally stronger, to provide support to Layer 4 and facilitate processing of the filter media.
• Coalescer Y has an additional non-pleated Layer 6 (i .e. non-pleated cylinder 52) downstream of Layer 4 and optional Layer 5 that provides release sites for coalesced drops.
• Layer 6 is more open than optional Layer 5.
• Coalescer Z In the example of Coalescer Z, three or more media layers with an optional support structure are used (see U.S. Patent Application Serial ' No. 61/179,170 filed on May 18, 2009; U. S. Patent Application Serial No. 61/179,939 filed on May 20, 2009; and U.S. Patent Application Serial No. 12/780,392 filed on May 14, 2010.
• Coalescer Z is a more complex surface coalescer than Coalescer Y for use in a filter -in-filter design.
• Layer 3 functions to reduce the pressure drop across the coalescer and serves as a particulate prefilter for the coalescer and to increase its service life.
• Layer 3 is more open than Layer 4 and has a higher capillary pressure (i.e. a more positive capillary pressure) than Layer 4
• layers 1 -5 are pleated.
• the fluid flow profile within the pleats and drag on captured droplets causes them t accumulate in the valleys 62 (downstream direction) of the pleats.
• the inventors have observed that coalesced drops tend to be released from the same active regions or areas on the downstream face of coalescers, while little drop release occurs elsewhere. This suggests that once a drainage path through the media is created, it is repeatedly used.
• preferred drainage paths ending in larger pores are created by the intimate contact of the inner pleat tips of Layer 4 (for Coalescers Y and Z) or Layer 5 (for Coalescer X, as well as Coalescers Y and Z if Layer 5 is included) to the upstream surface of isnpieated Layer 6.
• Layer 4 for Coalescers Y and Z
• Layer 5 for Coalescer X, as well as Coalescers Y and Z if Layer 5 is included
• the pleated media 50 could be as described in the exemplar)' Coalescers X, Y or Z described above, except that Layer 6, i.e. the non- pleated cylinder 52, would be absent.
• This additional embodiment achieves the same fluid flow profile within the pleat and drag on capture drops effects as Coalescers X, Y or Z, to cause droplets and coalesced drops to concentrate in the valleys 62 of the pleats to enhance coalescence.
• drops instead of coalesced drops draining to Layer 6, drops are released from small s!its or holes (i.e. apertures) in the inner pleat tips 60. These apertures could be produced by needle punching or other means and can be on the order of 30-300 p.rn in size. The apertures serve as release points for the coalesced drops.
• Figure 8 illustrates an example of apertures 80 formed in the i nner pleat tips of the pleated media 50.
• An optional layer 82 with relatively large pore size (compared to the media 50), which can be equivalent to the non-pleated cylinder 52 or the support structure 70, can also be present.
• emulsion containing water droplets flows into the pleat at (I ).
• water droplets unable to penetrate the barrier formed by the medi fl w along the media surface to the valley of the pleat.
• water droplets collect in the valley and coalesce into drops.
• pressure drop forces coalesced drops through an aperture 80 in the pleat tip.
• coalesced water drops settle out and/or are carried downstream to the outer, non -pleated cylinder 54 of the second stage 14 where they are separated out and drain
• Figure 7 and Table 2 provide an exemplary configuration of the second or inner separating stage 14,
• the second stage 14 serves to separate coalesced water drops .from the fluid and to remove fine solid contaminants from the fluid.
• the second stage 14 includes ihe outer, non-p!eaied cylinder 54 in intimate coniaci with ihe outer pleat tips of the inner multi-layer pleated cylinder 56.
• the axial lengths L 2 of the non-pleated cylinder 54 and the pleated cylinder 56 are substantially the same, with the ends of the cylinders embedded into the endcaps 26, 28 or potted in an adhesive, for example polyurethane, or otherwise attached to the endcaps in a manner to prevent bypass of until tered fluid around the media.
• the media combinations, materials and properties listed in Table 2 are exemplar) 1 only, and reflect combinations, materials and properties that the inventors beheve, at the time of filing this application, would provide adequate performance results with respect to high pressure common rail diese! fuel systems running on ULSD or biodiesel. Further research may reveal suitable media combinations, materials and material properties other than those listed in Table 2, both with respect to high pressure common rail diesel fuel systems running on ULSD or biodiesel and with respect to other types of fluids on other types of systems.
• Table 2 lists various specific ihermoplastic materials such as polyamide, po!ybuty!ene terephthalate, and polyethylene terephthaiate
• the media layers are not limited to these specific thermoplastic materials.
• Other thermoplastic materials could be used.
• the media layers are not limited to thermoplastic materials.
• Other polymeric materials could be used for the media layers including, but not limited to, thermosetti .ng plasti cs.
• the second stage includes at least five layers.
• Layer A i.e. the non-pleated cylinder 54
• Layer A can be, for example, a woven polymeric mesh in the form of a tube that repels the coalesced water drops and allows them to drain freely from the surface.
• Layer A is outside of and in intimate contact with the outer pleat tips 90 of the inner multi-layer pleated cylinder 56.
• the inventors currently believe that the mesh opening of Layer A should be less than 100 p.m and preferably less than 50 pm for ULSD and biodiesel applications. However, further research may reveal other suitable mesh opening sizes.
• the pleated layers (Layers B-E, i.e. pleated cylinder 56) function to capture solid contaminants and drops not removed by upstream layers.
• the first of these pleated layers, Layers B and C in Figure 7 and Table 2 are transitional layers which reduce pressure drop, provide further removal of drops and droplets, and reduce solids from collecting on the following nanotiber filtration layer, Layer D.
• Layers B and C have properties similar to Layers 1 and 2 in the outer stage 12. Layer B also facilitates manufacturing and processing.
• the next pleated layer, Layer D functions a a high efficiency filter for fine particles, 4 ⁇ ( ⁇ ) and smaller.
• the layers upstream of Layer D function primarily to remove and separate water drops.
• Layer D functions to protect a downstream system, such as a high pressure common rail fuel injection system, from fine solids.
• Layer D also removes drops that may have passed through the preceding layers.
• Layer D is tighter than any of the other layers of the outer stage 12 or the inner stage 14 and, in one exemplary embodiment, comprises thermoplastic nanofiber filter media with fibers having a diameter of less than 1 urn. At a minimum, Layer D should be as tight as Layer 4 of the outer stage 12.
• Layer E functions to provide support for the preceding layers without significantly increasing the pressure drop.
• Layer E is a relatively open media with sufficient strength and stiffness to support the upstream layers of the inner stage 14 under conditions of use and enhance processability of the media of the inner stage 14.
• Tables i and 2 above list, the various media layers as being made from specific thermoplastic materials.
• the endcaps and the support structure 70 are also described as being made from thermoplastic materials.
• the performance ad vantages of the filter described herein can be obtained if some of the components are not thermoplastic, but are made of other polymeric materials or in some circumstances non-polymeric materials.
• one or more of the media layers of the outer stage 1.2 and/or the inner stage 14 can be made from polymeric materials other than
• thermoplastic materials can be formed of material other than thermoplastic, for example metal or other polymeric material such as thermoset plasties.
• the support structure 70 can be made of materials other than thermoplastic, for example other polymeric materials, metal or other materials known in the art.
• Suitable polymeric material that can be used for the various elements of the filter described herein may include, but are not limited to, polyamide material, polyalkylene terephthalate material (e.g., polyethylene terephthaiate material or polybutylene terephthalate material), other polyester material, halocarbon material (e.g., Halar® brand ethylene ch!orotrifluoroethylene (ECTFE), and polyur ethane material.
• polyamide material e.g., polyamide material, polyalkylene terephthalate material (e.g., polyethylene terephthaiate material or polybutylene terephthalate material), other polyester material, halocarbon material (e.g., Halar® brand ethylene ch!orotrifluoroethylene (ECTFE), and polyur ethane material.
• polyalkylene terephthalate material e.g., polyethylene terephthaiate material or polybutylene terephthal
• the pleated media 50 and pleated medi 56 may be formed using any suitable techniques known in the art including, but not limited to, melt-blowing two different l ayers of media one of top of another, by a wet laid process, electrospi.nni.ng,

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Filtering Materials (AREA)
• Filtration Of Liquid (AREA)
• Filtering Of Dispersed Particles In Gases (AREA)
• Separation Using Semi-Permeable Membranes (AREA)

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