Formed filter element

• US 9,114,339 B2
• Filed: 09/14/2012
• Issued: 08/25/2015
• Est. Priority Date: 02/23/2007
• Status: Active Grant

• Current Assignee: Donaldson Company Incorporated
• Original Assignee: Donaldson Company Incorporated
• Inventors: Israel, Joseph, Dunn, Eugene F III, Joriman, Jon D, Exley, Jeremy T, Dallas, Andrew
• Primary Examiner(s): Soohoo, Tony G
• Assistant Examiner(s): Keyworth, Peter
• Application Number:
  US13/616,559
• Publication Number:
  US 20130008006A1
• Time in Patent Office: 1,075 Days
• Field of Search: 264/109
• US Class Current: 1/1
• CPC Class Codes: B01D 2239/0216 Bicomponent or multicomponent fibres
• CPC Class Codes: B01D 2239/025 comprising nanofibres apparatus incorporating such gas filtering material see B01D46/546
• CPC Class Codes: B01D 2239/0407 comprising particulate additives, e.g. adsorbents apparatus incorporating gas filtering material B01D46/0036
• CPC Class Codes: B01D 2239/064 The fibres being mixed
• CPC Class Codes: B01D 2239/086 Binders between particles or fibres
• CPC Class Codes: B01D 2239/1225 Fibre length
• CPC Class Codes: B01D 2239/1233 Fibre diameter
• CPC Class Codes: B01D 2239/1241 Particle diameter
• CPC Class Codes: B01D 39/1615 of natural origin
• CPC Class Codes: B01D 39/163 sintered or bonded
• CPC Class Codes: B01D 39/2024 otherwise bonded, e.g. by resins
• CPC Class Codes: B01D 39/2048 otherwise bonded
• CPC Class Codes: B01D 39/2058 the material being particulate
• CPC Class Codes: B01D 39/2062 Bonded, e.g. activated carbon blocks
• CPC Class Codes: B01D 39/2065 the material being fibrous
• CPC Class Codes: B01D 39/2089 otherwise bonded, e.g. by resins
• CPC Class Codes: Y10T 29/49826 Assembling or joining

Abstract

A filter medium for use in filtering a mobile fluid made from at least a bicomponent fiber. Other fibers, particles, or other materials can also be entrained in the filter medium. The filter medium has a substantial thickness compared to filters of the prior art. The fiber length and diameter dimensions are selected to obtain desired filter characteristics including thickness, basis weight, pore size, filtration efficiency, pressure drop, burst strength, and manufacturing efficiency. Further, a multilayer filter medium can be provided with ease. Each layer can have a different composition, pore size, basis weight, and so forth, thus providing the ability to build multiple functionality into the filter media of the invention.

Claims

1. A process of forming a filter element comprising a formed filter medium, the process comprising:

blending an aqueous slurry comprising a bicomponent fiber and a glass fiber;

immersing a perforate support in the aqueous slurry, wherein the perforate support is suitably open to allow the passage of water while depositing fibers onto the perforate support;

applying a vacuum across the perforate support for a period of time sufficient to form a wet layer of fibers on the perforate support;

removing the perforate support having the wet layer formed thereon from the aqueous slurry;

extracting water from the wet layer to form a perforate support having a fibrous filter layer formed thereon; and

heating the perforate support having the fibrous filter layer formed thereon to a temperature sufficient to melt one component of the bicomponent fiber, to form a filter element comprising the perforate support having a formed filter medium disposed thereon, wherein the formed filter medium has a basis weight of at least about 500 grams/meter²;

wherein the process further comprises adding an additive to the aqueous slurry or to the formed filter medium, the additive comprising a surface finish compound, a compound to change the surface energy of one or more fibers, an acid, a base, a fluorocarbon, a flame retardant compound, an antistatic compound, or a combination thereof.

2. The process of claim 1 wherein the fibers are substantially dried during the heating step.

3. The process of claim 1 wherein the formed filter medium comprises about 20 to 95 wt % inclusive of a bicomponent fiber;

and about 80 to 5 wt % inclusive of a glass fiber.

4. The process of claim 3 wherein the glass fiber has a diameter of about 0.1 to 8.0 microns inclusive and aspect ratio of greater than about 1:

100.

5. The process of claim 3 wherein the glass fiber comprises a first glass fiber having a diameter of about 0.1 to 8.0 microns inclusive and a second glass fiber having a fiber diameter of about 8.0 to 13.0 microns inclusive.

6. The process of claim 3 wherein the glass fiber comprises a first glass fiber having a diameter of about 0.1 to 2.0 microns inclusive and a second glass fiber having a fiber diameter of about 2.6 to 8.0 microns inclusive.

7. The process of claim 1 wherein the filter medium after the heating step has a basis weight of up to about 3,000 grams/meter².

8. The process of claim 7 wherein the filter medium after the heating step has a thickness greater than about 5 centimeters basis weight of about 2,500 grams/meter² to about 3,000 grams/meter².

9. The process of claim 1 wherein the bicomponent fiber has a diameter of about 5 to 50 micrometers inclusive and a length of about 0.1 to 20 millimeters inclusive.

10. The process of claim 1 wherein the bicomponent fiber comprises a core material disposed within a sheath material, the core material having a melting point of about 200°

C. to 260°

C. inclusive and the sheath material having a melting point of about 80°

C. to 200°

C. inclusive.

11. The process of claim 10 wherein the bicomponent fiber sheath material comprises a polyolefin, a polyester, a polyvinyl acetate, a polyvinyl chloride, a polyvinyl butyral, an acrylic resin, a polyamide, a polyvinylidene chloride, a polystyrene, a polyvinyl alcohol, a polyurethane, a cellulosic resin, a styrene-butadiene copolymer, an acrylonitrilebutadiene-styrene copolymer, a styrenic block copolymer, a polyisoprene rubber, or a copolymer or a mixture thereof.

12. The process of claim 1, further comprising adding a binder to the slurry.

13. The process of claim 12 wherein the binder is a latex binder, the latex binder comprising an acrylic, an ethylene vinyl acetate, a polyvinyl alcohol, an ethylene vinyl alcohol, a polyvinyl pyrrolidone, a polyvinyl chloride, or a copolymer or a blend thereof.

14. The process of claim 12 wherein the binder is solvent borne, the binder comprising a phenolic resin, a polyvinyl acetate, a polyvinyl alcohol, an acrylic resin, a methacrylic resin, a polyurethane, a polycyanoacrylate, an epoxy, a melamine resin, a polycaprolactone, or a copolymer or blend thereof.

15. The process of claim 1 wherein the aqueous slurry further comprises a thermoplastic fiber, the thermoplastic fiber comprising a polyester, a polyamide, a polypropylene, a copolyetherester, a polyethylene terephthalate, a polybutylene terephthalate, a polyetherketoneketone, a polyetheretherketone, a liquid crystalline polymer, and mixtures thereof.

16. The process of claim 15 wherein the thermoplastic fiber comprises a polyester comprising poly(ethylene terephthalate).

17. The process of claim 1 further comprising adding an antioxidant, a stabilizer, a lubricant, a toughener, a dispersing aid, a surface active agent, an acid, a catalyst, or a mixture thereof to the aqueous slurry.

18. The process of claim 1 further comprising adding an inorganic fiber to the aqueous slurry, the inorganic fiber comprising a carbon, a metal, a metal oxide, or a combination thereof.

19. The process of claim 1 further comprising adding a fiber to the aqueous slurry, the fiber comprising one or more naturally occurring cotton, linen, wool, cellulosic or proteinaceous polymers.

20. The process of claim 1 further comprising adding a particulate to the aqueous slurry, the particulate comprising a metal oxide, a metal, a ceramic, a zeolite, a carbon, an ion exchange resin, a nanotube, or a mixture thereof.

21. The process of claim 20 wherein the particulate comprises activated charcoal.

22. The process of claim 20 wherein the particulate has an average particle size of 3 millimeters or less.

23. The process of claim 1 wherein the additive is added to the formed filter medium by means of dipping the filter medium in a solvent having the additive dispersed therein.

24. The process of claim 1 wherein the additive is added to the formed filter medium by a spraying means.

25. The process of claim 1 wherein a vacuum of 10 to 29 inches Hg is applied for between 2 and 35 seconds.

26. The process of claim 1 wherein the vacuum is maintained for 15 to 30 seconds during extracting after the removing and before the heating.

27. The process of claim 1 wherein the heating is accomplished in a through-air drying oven.

28. The process of claim 1 wherein the perforate support is cylindrical, pleated cylindrical, conical, or oval.

29. A process of forming a filtration assembly, the process comprising adding one or more endcaps, housings, or a combination thereof to the filter element made by the process of claim 1.

30. A process of forming a filter element comprising a formed filter medium, the process comprising:

blending an aqueous slurry comprising a glass fiber and a bicomponent fiber comprising a binder component;

immersing a perforate support in the aqueous slurry, wherein the perforate support is suitably open to allow the passage of water while depositing fibers onto the perforate support;

applying a vacuum across the perforate support for a period of time sufficient to form a wet layer of fibers on the perforate support;

removing the perforate support having the wet layer formed thereon from the aqueous slurry;

extracting water from the wet layer to form a perforate support having a fibrous filter layer formed thereon; and

heating the perforate support having the fibrous filter layer formed thereon to a temperature sufficient to melt the binder component of the bicomponent fiber, to form a filter element comprising the perforate support having a formed filter medium disposed thereon;

wherein the formed filter medium has a basis weight of about 500 grams/meter² to 3,000 grams/meter²; and

wherein the filter element does not include a binder other than the binder component of the bicomponent binder fibers.

31. The process of claim 30 further comprising adding an additive to the formed filter medium, the additive comprising a surface finish compound, a compound to change the surface energy of one or more fibers, an acid, a base, a fluorocarbon, a flame retardant compound, a catalyst, an antistatic compound, or a combination thereof.

32. The process of claim 31 wherein the additive is added by means of dipping the filter medium in a solvent having the additive dispersed therein.

33. The process of claim 31 wherein the additive is added by a spraying means.

34. The process of claim 30 further comprising adding an additive to the aqueous slurry, the additive comprising a surface finish compound, a compound to change the surface energy of one or more fibers, an acid, a base, a fluorocarbon, a flame retardant compound, a catalyst, an antistatic compound, or a combination thereof.

35. A process of forming a filter element comprising a formed filter medium, the process comprising:

blending a first aqueous slurry comprising a bicomponent fiber and a glass fiber;

immersing a perforate support in the first aqueous slurry, wherein the perforate support is suitably open to allow the passage of water while depositing fibers onto the perforate support;

applying a vacuum across the perforate support for a period of time sufficient to form a first wet layer of fibers on the perforate support;

removing the perforate support having the first wet layer formed thereon from the aqueous slurry;

vacuum drying the perforate support having the first wet layer formed thereon to form a first dry media layer;

optionally heating the perforate support having the first dry media layer formed thereon to a temperature sufficient to melt one component of the bicomponent fiber;

blending a second aqueous slurry that is different from the first aqueous slurry;

immersing into the second aqueous slurry the perforate support having the first dry media layer, which is optionally heated to melt one component of the bicomponent fiber;

applying a vacuum across the perforate support for a period of time sufficient to form a second wet layer of fibers on the first dry media layer; and

removing the formed filter medium and second wet layer from the aqueous slurry;

vacuum drying the perforate support having the second wet layer formed thereon to form a second dry media layer;

heating the perforate support having the first and second dry media layers formed thereon to a temperature sufficient to melt one component of the bicomponent fiber, to form a filter element comprising the perforate support having a formed filter medium disposed thereon, wherein the formed filter medium has a basis weight of at least about 500 grams/meter².

36. The process of claim 35 further comprising adding an additive to the formed filter medium, the additive comprising a surface finish compound, a compound to change the surface energy of one or more fibers, an acid, a base, a fluorocarbon, a flame retardant compound, an antistatic compound, or a combination thereof.

37. The process of claim 36 wherein the additive is added by means of dipping the filter medium in a solvent having the additive dispersed therein.

38. The process of claim 36 wherein the additive is added by a spraying means.

39. The process of claim 35 further comprising adding an additive to the first and/or the second aqueous slurries, the additive comprising a surface finish compound, a compound to change the surface energy of one or more fibers, an acid, a base, a fluorocarbon, a flame retardant compound, an antistatic compound, or a combination thereof.