← Back to Patent Explorer
US4066546A Expired / Lapsed US ⏱️ 0.0 years remaining

Continuous filtering process and an apparatus therefor

Assignee: Sekisui Chemical Co Ltd
•
Filing: 1975-10-08
•
Granted: 1978-01-03
•
Expires: 1995-10-08
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A continuous filtering process and apparatus therefor in which a violent turbulence of fluid to be filtered is caused in a filter tank through which the fluid is continuously flowed. The turbulence is caused by rapidly rotating rotators which are arranged in the filter tank so that the surfaces of the rotators face the surfaces of filter media provided in hollow filter disks. A small interval such as three or five millimeters occurs between the rotators and the filter disks. Such violent turbulence of the fluid rapidly disperses concentrated fluid from the surfaces of the filter media so that the clogging of the filter media or the formation of a concentrated polarization layer is substantially prevented. Continuity of the filtering operation is therefore increased even when filter media having very fine perforations therethrough are employed.

Inventors

  • 👤 Jiro Sasaki

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 06:58
CPC Classifications
B; B01; B01D; B01D35/00; B01D35/22; B01D61/00; B01D61/14; B01D61/145; B01D61/147; B01D63/00; B01D63/08; B01D63/082; B01D63/0822; B01D65/00; B01D65/08; B01D2311/00; B01D2311/04; B01D2315/00; B01D2315/02; B01D2321/00; B01D2321/04; B01D2321/20; B01D2321/2008; B01D2321/2016

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 416 words
A continuous filtering process comprising the steps of: a. admixing fluid to be filtered with a predetermined amount of solid particles which can remove free impurities in the fluid by adsorption, absorption, promotion of a decomposition reaction or the like when the particles become in contact with such free impurities; b. permitting said solid particles to remove free impurities in the fluid by adsorption, absorption, promotion of decomposition or the like, c. continuously flowing the fluid to be filtered having been admixed with said solid particles through an inlet of a filter tank having therein i. a plurality of hollow filter disks fixedly arranged with equal intervals therebetween, ii. facing filter media supported on the filter disks, and iii. a plurality of rotators, each rotator being positioned between two adjacent filter disks with small clearances between the surfaces of the rotator and the surfaces of the filter media on the filter disks, d. rotating the rotators continuously with a predetermined speed of rotation to cause a violent turbulence of the fluid to be filtered and thereby causing motion of the solid particles on the surfaces of the filter media, removing a layer of concentrated fluid from the surfaces of the filter media by said violent turbulence of the fluid and by motion of the solid particles, and achieving filtration through the filter media without substantial impurities adhering on the surfaces of the filter media; e. continuously withdrawing filtrate from within the hollow filter disks; f. continuously withdrawing fluid to be filtered from an outlet of the filter tank to an inlet end of an agitation tank having agitation means therein and agitating the fluid within the agitation tank, g. supplying fresh fluid to be filtered to said inlet end of the agitation tank at a rate substantially equal to the rate of withdrawing said filtrate from the filter disks; h. agitating the fluid in the agitation tank; i. continuously withdrawing fluid from an outlet end of the agitation tank, the outlet end of the agitation tank being spaced from the inlet end to provide the fluid within the agitation tank with a stay time and agitation by means of the agitation means whereby the concentration of free impurities in the said fluid is lowered to a concentration that is substantially equal to the concentration of free impurities in the fresh fluid to be filtered; and j. continuously supplying the fluid withdrawn from the outlet end of the agitation tank to the inlet of the filter tank.
Claim 2
Dependent Claim 416 words
A continuous filtering process comprising the steps of: a. admixing fluid to be filtered with a predetermined amount of solid particles which can remove free impurities in the fluid by adsorption, absorption, promotion of a decomposition reaction or the like when the particles become in contact with such free impurities; b. permitting said solid particles to remove free impurities in the fluid by adsorption, absorption, promotion of decomposition or the like, c. continuously flowing the fluid to be filtered having been admixed with said solid particles through an inlet of a filter tank having therein i. a plurality of hollow filter disks fixedly arranged with equal intervals therebetween, ii. facing filter media supported on the filter disks, and iii. a plurality of rotators, each rotator being positioned between two adjacent filter disks with small clearances between the surfaces of the rotator and the surfaces of the filter media on the filter disks, d. rotating the rotators continuously with a predetermined speed of rotation to cause a violent turbulence of the fluid to be filtered and thereby causing motion of the solid particles on the surfaces of the filter media, removing a layer of concentrated fluid from the surfaces of the filter media by said violent turbulence of the fluid and by motion of the solid particles, and achieving filtration through the filter media without substantial impurities adhering on the surfaces of the filter media; e. continuously withdrawing filtrate from within the hollow filter disks; f. continuously withdrawing fluid to be filtered from an outlet of the filter tank to an inlet end of an agitation tank having agitation means therein and agitating the fluid within the agitation tank, g. supplying fresh fluid to be filtered to said inlet end of the agitation tank at a rate substantially equal to the rate of withdrawing said filtrate from the filter disks; h. agitating the fluid in the agitation tank; i. continuously withdrawing fluid from an outlet end of the agitation tank, the outlet end of the agitation tank being spaced from the inlet end to provide the fluid within the agitation tank with a stay time and agitation by means of the agitation means whereby the concentration of free impurities in the said fluid is lowered to a concentration that is substantially equal to the concentration of free impurities in the fresh fluid to be filtered; and j. continuously supplying the fluid withdrawn from the outlet end of the agitation tank to the inlet of the filter tank.
Claim 3
Dependent Claim 353 words
A continuous filtering apparatus comprising: a. a filter tank including a plurality of hollow filter disks fixedly arranged in the tank with equal intervals therebetween and with facing filter media supported on the filter disks, a plurality of rotators positioned between two adjacent filter disks with small clearances between the surfaces of the rotators and the surfaces of the filter media, fluid inlet means and fluid outlet means on the filter tank, and filtrate withdrawing means communicating with the hollow filter disks, said rotators causing a violent turbulency of the fluid to be filtered on the surfaces of the filter media when the rotators are rotated with a predetermined speed of rotation; b. an agitation tank including therein agitation means for agitating fluid, first inlet means at one end of the agitation tank for concentrated fluid to be filtered, second inlet means for fresh fluid to be filtered, and outlet means at another end of the agitation tank for fluid to be filtered; c. a first circulation path means connecting said fluid outlet means of said filter tank to said first inlet means of said agitation tank; d. a fluid supply path means connected to said second inlet means of said agitation tank and including therein pump means for continuously supplying fresh fluid to be filtered to said agitation tank at a predetermined rate; e. a second circulation path means connecting said outlet means of said agitation tank to said fluid inlet means of said filter tank and including therein pump means for continuously pumping fluid to be filtered from said agitation tank to said filter tank; f. solid particle supply means connected to the circulation line formed by said filter tank, said first circulation path means, said agitation tank, and second circulation path means for supplying to said circulation line a predetermined amount of solid particles which can remove free impurities in the fluid to be filtered by adsorption, absorption, promotion of a decomposition reaction or the like; and g. driving means operatively connected to said rotators in the filter tank for continuously rotating the rotators with said predetermined speed of rotation.
Claim 4
Dependent Claim 353 words
A continuous filtering apparatus comprising: a. a filter tank including a plurality of hollow filter disks fixedly arranged in the tank with equal intervals therebetween and with facing filter media supported on the filter disks, a plurality of rotators positioned between two adjacent filter disks with small clearances between the surfaces of the rotators and the surfaces of the filter media, fluid inlet means and fluid outlet means on the filter tank, and filtrate withdrawing means communicating with the hollow filter disks, said rotators causing a violent turbulency of the fluid to be filtered on the surfaces of the filter media when the rotators are rotated with a predetermined speed of rotation; b. an agitation tank including therein agitation means for agitating fluid, first inlet means at one end of the agitation tank for concentrated fluid to be filtered, second inlet means for fresh fluid to be filtered, and outlet means at another end of the agitation tank for fluid to be filtered; c. a first circulation path means connecting said fluid outlet means of said filter tank to said first inlet means of said agitation tank; d. a fluid supply path means connected to said second inlet means of said agitation tank and including therein pump means for continuously supplying fresh fluid to be filtered to said agitation tank at a predetermined rate; e. a second circulation path means connecting said outlet means of said agitation tank to said fluid inlet means of said filter tank and including therein pump means for continuously pumping fluid to be filtered from said agitation tank to said filter tank; f. solid particle supply means connected to the circulation line formed by said filter tank, said first circulation path means, said agitation tank, and second circulation path means for supplying to said circulation line a predetermined amount of solid particles which can remove free impurities in the fluid to be filtered by adsorption, absorption, promotion of a decomposition reaction or the like; and g. driving means operatively connected to said rotators in the filter tank for continuously rotating the rotators with said predetermined speed of rotation.
Claim 5
Dependent Claim 24 words
The continuous filtering apparatus of claim 2 in which said agitation means comprises an air nozzle for jetting compressed air into the agitation tank.

References Cited (Backward Citations)

US3200105A Cited
US3437208A Cited
US3477575A Cited
US3502575A Cited
US3606016A Cited
US3648844A Cited
US3766059A Cited
US3884805A Cited
US3884813A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-01-02 1981-07-04 1982-01-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-01-02 1985-07-04 1986-01-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-01-02 1989-07-04 1990-01-03 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag