High strength, high capacity filter media and structure

• US 7,985,344 B2
• Filed: 11/20/2007
• Issued: 07/26/2011
• Est. Priority Date: 11/05/2004
• Status: Active Grant

• Current Assignee: Donaldson Company Incorporated
• Original Assignee: Donaldson Company Incorporated
• Inventors: Dema, Keh B., Olson, Linda M.
• Primary Examiner(s): CLEMENTE, ROBERT ARTHUR
• Application Number:
  US11/986,377
• Publication Number:
  US 20080073296A1
• Time in Patent Office: 1,344 Days
• Field of Search: 210/767, 210/504, 210/505, 210/506, 210/508, 210/509
• US Class Current: 210/767
• CPC Class Codes: B01D 27/06 with corrugated, folded or wound material
• CPC Class Codes: B01D 39/163 sintered or bonded
• CPC Class Codes: B01D 39/2024 otherwise bonded, e.g. by resins

Abstract

In the filtration of fluid materials, the removal of particulate from the moving stream requires substantial pressure to maintain flow and substantial capacity for removing particulate. The filters of the invention are rugged, high wet strength materials having a basis weight, permeability and efficiency suitable to obtain substantial reduction in particulate loading from liquid streams without plugging or mechanical failure. In particular, the filters of the invention permit the removal of substantial proportions of particulate from non-aqueous streams including lubricant oils, hydraulic fluids and other contaminated streams.

Claims

1. A method of filtering a non-aqueous liquid comprising a fuel, a lubricant, a hydraulic fluid, or a brake fluid, the method consisting essentially of:

passing the non-aqueous liquid with a particulate load through a filter medium comprising a layer comprising 5 to 50 wt % of a bicomponent binder fiber, about 50 to 95 wt % of a glass fiber, and about 0.5 to 25 wt % of a binder resin, the layer having a basis weight of about 30 to 250 g-m<sup>−

2</sup>, the layer having a permeability of 10 to 50 ft-min<sup>−

1</sup>, a wet bursting strength of about 5 lb-in<sup>−

2</sup> to 30 lb-in<sup>−

2</sup>; and

removing the particulate load.

2. The method of claim 1 wherein the medium comprises a first layer comprising a loading layer having a basis weight of about 25 to 75 g-m⁻

2 and a second layer comprising an efficiency layer having a basis weight of about 50 to 150 g-m<sup>−

2</sup>, wherein the loading layer comprises about 1 to 25% of a bicomponent binder fiber and about 70 to 90 w % of a glass fiber, and the efficiency layer comprises about 5 to 25 wt % of a bicomonent binder fiber and about 50 to 95 wt % of a glass fiber.

3. The method of claim 2 wherein the glass fiber comprises a blend of two or more glass fiber sources that differ by average diameter.

4. The method of claim 2 wherein the glass fiber comprises a blend of three or more glass fiber sources that differ by average diameter.

5. The medium of claim 2 wherein the glass fiber comprises a blend of a first fiber having a diameter of less than 0.5 microns and a second glass fiber having diameter of greater than 5 microns.

6. The method of claim 1 wherein the medium comprising a wet bursting strength of about 10 lb-in⁻

2 to 30 lb-in<sup>−

2</sup>.

7. The method of claim 1 wherein the medium comprises a mean flow pore size of about 2 to about 10 micrometers.