Process for filtration of fluids and filter apparatus for performing the process

Patent metadata

Field	Value
Publication number	US-10780378-B2
Application number	US-201113634085-A
Country	US
Kind code	B2
Filing date	Mar 10, 2011
Priority date	Mar 12, 2010
Publication date	Sep 22, 2020
Grant date	Sep 22, 2020

Abstract

The invention relates to a process for filtration of fluids, especially of aqueous media, by means of a backflush filter apparatus consisting of a cylindrical housing, a cylindrical and perforated support body installed coaxially therein, a filter material, a support fabric, and a mobile backflush device present therein, said process enabling improved removal of fine and ultrafine particles, and of particles with greasy or compressible consistency, and allowing higher solid concentrations. The process according to the invention has the steps below. a) Formation of a filtercake in the perforation of the support body; b) deposition of the relatively fine particles or of the particles with greasy or compressible consistency on or in the filtercake; c) backflushing after attainment of the predefined filter loading or of the maximum permissible pressure differential, or when the filtrate volume flow goes below a minimum. A further aspect of the invention is a filter apparatus for performance of the process, characterized in that the filter material consists of a filter fabric with an air permeability of 700-1300 l/m2s at pressure differential 200 Pa.

First claim

What is claimed is:

1. A process for filtration of a fluid stream including particles comprising the steps of:
providing a filtration apparatus which comprises:
a cylindrical housing having an inlet and an outlet;
a cylindrical support body having perforations and being installed coaxially in the cylindrical housing;
a filter material selected from the group consisting of filter fabric having an air permeability of 700-1300l/m 2 s at a pressure differential of 200 Pa and a perforated metal sheet having slot openings, wherein the slot width is 5 to 80 micrometers; and
a movable backwash device, a portion of which sealingly engages an interior surface of said cylindrical housing, disposed within said cylindrical housing;

flowing said fluid stream including particles into said housing inlet to an interior of said cylindrical support body;
forming a support layer of particles on the filter material;
forming a filter cake in the perforations of the support body as inflowing particles from the fluid stream are retained on the support layer; and

backwashing the filter material after attainment of a predefined filter load or a maximum permissible pressure differential, or when a filtrate volume flow drops below a minimum.

2. The process according to claim 1 , further comprising adding a filter aid prior to or during the flowing of said fluid stream.

3. The process according to claim 1 or 2 , wherein dense particles with a grain spectrum from 30-200 micrometers are separated from a backwashing reject by means of a density separating process, and are returned to fluids upstream of the backwash filter apparatus.

4. The process according to claim 3 , further comprising adding dense particles to the fluid stream prior to or during the flowing, separating the dense particles from the reject by means of a density separating process, and returning the dense particles upstream of the backwash filter apparatus.

5. The process according to claim 4 , wherein the dense particles are fine sand, metal powder, or other fine-grained dense powder with a grain spectrum from 30 micrometers to 200 micrometers and a density from 1,500 kg/m 3 to 10,000 kg/m 3 .

6. The process according to claim 5 , wherein the density is from 2,000 kg/m 3 to 8,000 kg/m 3 .

7. The process according to claim 4 , wherein the density separating process includes a hydrocyclone.

8. The process according to claim 1 , wherein after completion of the flowing, forming and backwashing steps, the process further comprises pushing out remaining fluid from an unfiltrate chamber, filtrate chamber, and reject chamber by means of a gas and wherein subsequently any solids are dried and pneumatically discharged by means of the gas.

9. The process according to claim 1 , wherein said fluid is an aqueous media.

10. The process according to claim 1 , wherein the fluids are circulated in a circuit.

11. The process according to claim 1 , wherein the perforations of the support body comprise tapered holes.

12. The process according to claim 1 , wherein the filter material is said perforated metal sheet.

13. The process according to claim 1 , wherein the filter material is said filter fabric and wherein said filter fabric is disposed between said cylindrical support body and a support fabric.

14. A filter apparatus comprising a cylindrical housing having an inlet and an outlet; a cylindrical support body having perforations being installed coaxially in the cylindrical housing; a filter material selected from the group consisting of a filter fabric having an air permeability of 700-1300l/m 2 s at a pressure differential of 200 Pa, and a perforated metal sheet having slot openings, wherein the slot width is 5 to 80 micrometers; and a movable backwash device disposed within said cylindrical housing, wherein said filter material provides for the forming of a support layer of particles on the filter material when a fluid stream comprising particles is filtered in said filter apparatus, wherein said support layer provides for the forming of a filter cake in the perforations of the support body, wherein the filter cake forms on said support layer, and wherein said backwash device is for backwashing the filter material after attainment of a predefined filter load or a maximum permissible pressure differential, or when a filtrate volume flow drops below a minimum.

15. The filter apparatus according to claim 14 , wherein the filter cake formed in the perforations of the support body does not interfere with the backwash device.

16. The filter apparatus according to claim 14 , wherein a sealing prevents a direct flow of the fluid stream into a reject chamber of the apparatus.

17. The filter apparatus according to claim 14 , wherein a clamping device is provided for an even clamping of the filter material onto the support body.

18. The filter apparatus according to claim 14 , wherein the perforations of the support body comprise tapered holes.

19. The filter apparatus according to claim 14 , wherein the filter material is said perforated metal sheet.

20. The filter apparatus according to claim 14 , wherein the filter material is said filter fabric and wherein said filter fabric is disposed between said cylindrical support body and a support fabric.

Assignees

• Strasser Stefan
• Groesswang Roman
• Kneissl Johannes
• Eisl Georg
• Brandt Klaus
• Chemiefaser Lenzing Ag

Inventors

• Strasser Stefan
• Grösswang Roman
• Kneissl Johannes
• Eisl Georg
• Brandt Klaus

Classifications

• B01D37/043

  by flow measuring · CPC title

• B01D29/68 Primary

  with backwash arms, shoes or nozzles · CPC title

• B01D37/046

  by pressure measuring · CPC title

• B01D37/02

  Precoating the filter medium; Addition of filter aids to the liquid being filtered {(devices for feeding reagents C02F1/685 and sub-groups; filter aids)} · CPC title

• B01D29/66 Primary

  by flushing, e.g. counter-current air-bumps · CPC title