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US4652379A Expired / Lapsed US ⏱️ 0.0 years remaining

Filtering impurities from liquid using mineral wool fiber material

Assignee: Individual
•
Filing: 1984-05-01
•
Granted: 1987-03-24
•
Expires: 2004-05-01
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Abstract

Abstract This invention is related to a process for filtering gases or liquids for removing liquid or solid impurities and is characterized in that one uses for filtering a fibre material which partly exhibits a layer structure, said fibres along the main part of the total fibre length exhibiting a direction which deviates less than 45° from the direction of a main direction plane of said fibres, said filtering being performed so that the filtered medium is brought to flow away from the filter material through an outflow area in the filter material in which the flow direction is essentially parallel with the direction of the main direction plane of the fibres.

Inventors

  • 👤 Fred Nyberg

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 21:20
CPC Classifications
B; B01; B01D; B01D46/00; B01D46/24; B01D39/00; B01D39/14; B01D39/20; B01D39/2068; B01D39/2082

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 346 words
A process for filtering liquid for removing impurities therefrom which comprises passing said liquid through a filter body of mineral wool fiber material cut from a fiber material web with a thickness of at least 5 cm, of fibers prepared from a melt of fibers with a thickness of essentially from 1 to 20 microns, by depositing said fibers on a surface and bonding the fibers with a binder at a substantial number of points at which the fibers contact each other, said fibers, at least along a main part of a total fiber length, being directed in a direction which deviates less than 45% from a main direction plane formed by said surface, said mineral wool fiber material having a density of from 50 to 150 kg/m 3 and a stiffness, expressed as compressibility under a load of 0.05 kp/cm 2 on an upper surface of a cylinder of said mineral wool fiber material with diameter 100 mm and height 100 mm of at most 40%, in which filtering process the liquid is brought to penetrate into said body of mineral wool fiber material through an inflow surface area comprising a major part of said body of mineral wool fiber material and is removed from said body through an outflow surface area formed by at least one outlet opening nozzle urged against a cut surface of said body of fiber material cut in a direction transverse to a direction of said web, with said nozzle arranged at a distance of at least 1 cm from a peripheral line of said cut surface of said body, the ratio of said inflow surface area to said outflow surface area of said body of fiber material being at least 10, said inflow surface area being at least 90% of the total surface area of said body, said body extending in a direction perpendicular to said outflow surface area at least 5 cm, and passing said liquid through said filter body with a flow speed, calculated on said outflow surface area of said filter body of above 10 meters/hour.
Claim 2
Dependent Claim 346 words
A process for filtering liquid for removing impurities therefrom which comprises passing said liquid through a filter body of mineral wool fiber material cut from a fiber material web with a thickness of at least 5 cm, of fibers prepared from a melt of fibers with a thickness of essentially from 1 to 20 microns, by depositing said fibers on a surface and bonding the fibers with a binder at a substantial number of points at which the fibers contact each other, said fibers, at least along a main part of a total fiber length, being directed in a direction which deviates less than 45% from a main direction plane formed by said surface, said mineral wool fiber material having a density of from 50 to 150 kg/m 3 and a stiffness, expressed as compressibility under a load of 0.05 kp/cm 2 on an upper surface of a cylinder of said mineral wool fiber material with diameter 100 mm and height 100 mm of at most 40%, in which filtering process the liquid is brought to penetrate into said body of mineral wool fiber material through an inflow surface area comprising a major part of said body of mineral wool fiber material and is removed from said body through an outflow surface area formed by at least one outlet opening nozzle urged against a cut surface of said body of fiber material cut in a direction transverse to a direction of said web, with said nozzle arranged at a distance of at least 1 cm from a peripheral line of said cut surface of said body, the ratio of said inflow surface area to said outflow surface area of said body of fiber material being at least 10, said inflow surface area being at least 90% of the total surface area of said body, said body extending in a direction perpendicular to said outflow surface area at least 5 cm, and passing said liquid through said filter body with a flow speed, calculated on said outflow surface area of said filter body of above 10 meters/hour.
Claim 3
Dependent Claim 53 words
A process according to claim 1 in which said filter body of mineral wool fiber material is formed by melting a starting material and spinning to fibers, said filter body of mineral wool filter material comprising 4550% SiO 2 , 10-15% Al 2 O 3 , 10-18% CaO, 6-12% MgO and 6-12% FeO.
Claim 4
Dependent Claim 23 words
A process according to claim 1 in which the ratio of the inflow surface area to the outflow surface area is above 25.
Claim 5
Dependent Claim 52 words
A process according to claim 1 in which said filtering liquid is performed in the presence at least one aluminum compound from the group consisting of complex polynuclear aluminum hydroxide compounds with 2 or more aluminum atoms per molecule and precursors which form said polynuclear aluminum hydroxide compounds when diluted with water.
Claim 6
Dependent Claim 31 words
A process according to claim 1 which comprises filtering a liquid through said mineral wool fiber filter material with a compressibility of at most 10% when measured according to claim 1.
Claim 7
Dependent Claim 16 words
A process according to claim 1 wherein said flow speed is above 20 meters per hour.
Claim 8
Dependent Claim 31 words
A process according to claim 1 wherein said liquid is selected from the group consisting of drinking water, aquaria water, swimming pool water, sewage water, cooling water and hydrocarbon containing products.
Claim 9
Dependent Claim 28 words
A process according to claim 1 wherein said filter body of mineral wool fiber is cut from a web with a thickness of from 5 to 30 cms.

References Cited (Backward Citations)

US2395301A Cited
US3121698A Cited
US3210229A Cited
US3209916A Cited
US3599797A Cited
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US3929666A Cited
US4231878A Cited
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US4058456A Cited
US4238347A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-03-23 1990-09-22 1991-03-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-03-23 1994-09-22 1995-03-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-03-23 1998-09-22 1999-03-24 $7700.00 Window Closed / Lapsed

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