FILTER MODULES FOR IMPROVED MEDIA UTILIZATION AND USE IN GENERALLY CYLINDRICAL HOUSING

• US 20110073551A1
• Filed: 03/26/2010
• Published: 03/31/2011
• Est. Priority Date: 09/20/2006
• Status: Abandoned Application

• Current Assignee: Omnipure Filter Company, Inc.
• Original Assignee: Omnipure Filter Company, Inc.
• Inventors: SAASKI, BRUCE D., REID, ROGER P.
• Application Number:
  US12/748,372
• Publication Number:
  US 20110073551A1
• Time in Patent Office: Days
• US Class Current: 210/800
• CPC Class Codes: B01D 2201/043 Filter tubes connected to plates
• CPC Class Codes: B01D 2201/46 Several filtrate discharge conduits each connected to one filter element or group of filter elements
• CPC Class Codes: B01D 2239/0407 comprising particulate additives, e.g. adsorbents apparatus incorporating gas filtering material B01D46/0036
• CPC Class Codes: B01D 2239/086 Binders between particles or fibres
• CPC Class Codes: B01D 2239/125 Size distribution
• CPC Class Codes: B01D 29/33 arranged for inward flow filtration
• CPC Class Codes: B01D 29/35 arranged for outward flow filtration
• CPC Class Codes: B01D 29/52 in parallel connection
• CPC Class Codes: B01D 39/2062 Bonded, e.g. activated carbon blocks
• CPC Class Codes: B01D 39/2065 the material being fibrous

Abstract

Filter modules for use in a water dispenser, carafe, or other gravity-flow water filtration and dispensing unit are self-supporting, rigid and porous, and are adapted in size and shape to substantially fill a generally-cylindrical housing. The filter modules are molded forms of high-porosity compositions, so that they are consistent in performance and “non-dusting” compared to the unpredictable arrangements, positions, and performance of loose activated carbon particles. Filter modules may include activated carbon, zeolitic, resins, metal-scavengers, and/or other water filtration/treatment media granules/powders, for example, bound into a solid profile form by thermoplastic and/or other polymeric binders. Low melt index, or very low melt index, binders are preferred to maximize exposure of the activated carbon surface area. Thin walls of media surround the preferred single core/bore of each module, to preferably form generally D-shaped or triangular modules, wherein multiple modules of the same shape may be attached side-by-side to a housing plate/member, to substantially fill the housing, with the modules close together but spaced to allow water flow between and all around the modules.

Claims

1. A filter comprising multiple porous filter block modules and a housing, each of said modules comprising filter media walls surrounding and defining a bore for receiving fluid, and each of said modules being connected to a portion of said housing to retain and seal the bore in fluid communication with a fluid inlet of the housing;

each module having an internal surface defined by said bore and reachable by inlet fluid to be filtered, wherein fluid directed to the internal surface flows through said filter media walls for filtration and exits the module at external surfaces of the module;

wherein the filter is characterized by;

having only two of said modules, wherein each of said two modules has an axial length and a radial dimension perpendicular to said axial length, and each of said two modules is D-shaped in radial cross-section substantially all along the axial length of the module, and wherein said bore is D-shaped all along the axial length of the bore;

wherein each of the two modules is made of materials selected from the group consisting of activated carbon powder, activated carbon granules, lead removal additive, arsenic removal additive, and at least one binder, and said at least one binder has a melt index of less than or equal to 0.1 g/min melt index by ASTM D1238 or DIN 53735 at 190 degrees C. and 15 kilograms.

2. A filter as in claim 1 wherein the inlet fluid is water, and wherein said two modules remove lead from said water to a level less than 10 ppb total of soluble and particulate lead by means of said water flowing through said filter media walls under gravity-flow.

3. A filter as in claim 1, each of said modules being made only of said at least one binder, activated carbon, and lead removal media, wherein said activated carbon has a size distribution equal to D10 of 10-30 microns, D50 of 70-100 microns, and D90 of 170-200 microns.

4. A filter as in claim 1, wherein said two modules are provided in a generally-cylindrical housing cup and are fixed to a radial lid that covers a top end of said housing cup, the two modules being spaced apart in said housing all along their axial lengths.

5. A filter as in claim 4, wherein said lid comprises outer depending walls that surround an outer perimeter of a top end of each of said modules.

6. A filter as in claim 5, wherein said lid comprises inner depending walls that are received in said bore of each module.

7. A filter as in claim 6, wherein said outer surface of each of the two modules is tapered to be smaller at a bottom end than at a top end of each module.

8. A filter as in claim 4, wherein the modules are each made of 30-50 wt-% binder, 28-52 wt-% activated carbon, and 18-22 wt-% lead removal media, wherein the total of said binder, activated carbon, and lead removal media is 100 wt-% of each filter module.

9. A filter block as in claim 8, wherein said binder is selected from the group consisting of:

thermoplastic binder, thereto-set binder, polyolefins, polyethylene, polyvinyl halides, polyvinyl esters, polyvinyl ethers, polyvinyl sulfates, polyvinyl phosphates, polyvinyl amines, polyamides, polyimides, polyoxidiazoles, polytriazols, polycarbodiimides, polysulfones, polycarbonates, polyethers, polyarylene oxides, polyesters, polyarylates, phenol-formaldehyde resins, melamine-formaldehyde resins, formaldehydeureas, ethyl-vinyl acetate copolymers, co-polymers and block interpolymers thereof, and derivatives and combinations thereof.

10. A method of gravity-flow water filtration comprising:

providing a filter comprising a housing and multiple porous filter block modules inside said housing, each of said modules comprising filter media walls surrounding and defining a bore in each of said modules for receiving fluid, and said modules being connected to a lid of said housing, wherein the filter is characterized by;

comprising only two of said modules, wherein each of said two modules has an axial length and a radial dimension perpendicular to said axial length, each bore of each module is D-shaped in radial cross-section, each module outer surface is D-shaped in radial cross-section, and the modules are spaced apart so that they are adapted to allow fluid flow between them;

the filter modules being made of materials selected from the group consisting of activated carbon powder, activated carbon granules, lead removal additive, arsenic removal additive, and at least one binder, and said at least one binder has a melt index of less than or equal to 0.1 g/min melt index by ASTM D1238 or DIN 53735 at 190 degrees C. and 15 kilograms; and

the method is further characterized by;

directing water to the bores of the two modules so that the water flows through said filter media walls only under gravity flow to exit the filter modules at external surfaces of said modules; and

wherein said gravity flow of the water through the filer media walls removes lead from said water to a level less than 10 ppb total of soluble and particulate lead.

11. A method as in claim 10, wherein the modules are made only of said at least one binder, activated carbon, and lead removal media, wherein said activated carbon has a size distribution equal to D10 of 10-30 microns, D50 of 70-100 microns, and D90 of 170-200 microns.

12. A method as in claim 11, wherein at least one of said modules further comprises an elongated, axially-extending rib-brace between the two D-shaped modules.

13. A method as in claim 12, wherein:

the bores of the two modules extend generally parallel to each other, and said rib-brace also extends generally parallel to the bores;

the outer surface of each of the two modules is tapered to be smaller at a bottom end than at a top end of each module, and wherein said rib-brace is tapered to be smaller at its bottom end than at its top end, and the internal surface formed by said bores are tapered so that each bore has an overall smaller diameter at the bottom of the bore compared to the top of the bore.

14. A method as in claim 13, wherein each module is made of 30-50 wt-% binder, 28-52 wt-% activated carbon, and 18-22 wt-% lead removal media, wherein the total of said binder, activated carbon, and lead removal media is 100 wt-% of each module.

15. A filter comprising multiple porous filter block modules and a housing, each of said modules comprising filter media walls surrounding and defining a bore for receiving fluid, and each of said modules being connected to a portion of said housing to retain and seal the bore in fluid communication with a fluid inlet of the housing;

each module having an internal surface defined by said bore and reachable by inlet fluid to be filtered, wherein fluid directed to the internal surface flows through said filter media walls for filtration and exits the module at external surfaces of the module;

wherein the filter is characterized by;

having only four of said modules, wherein each of said four modules has an axial length and a generally triangular in radial cross-section substantially all along the axial length of the module, and wherein said bore is generally triangular all along the axial length of the bore;

wherein each of the four modules is made of materials selected from the group consisting of activated carbon powder, activated carbon granules, lead removal additive, arsenic removal additive, and at least one binder, and said at least one binder has a melt index of less than or equal to 0.1 g/min melt index by ASTM D1238 or DIN 53735 at 190 degrees C. and 15 kilograms.

16. A filter as in claim 15 wherein the inlet fluid is water, and wherein said four modules remove lead from said water to a level less than 10 ppb total of soluble and particulate lead by means of said water flowing through said filter media walls under gravity-flow.

17. A filter as in claim 15, wherein the modules are made only of said at least one binder, activated carbon, and lead removal media, wherein said activated carbon has a size distribution equal to D10 of 10-30 microns, D50 of 70-100 microns, and D90 of 170-200 microns.

18. A filter as in claim 15, wherein said four modules are provided in a generally-cylindrical housing cup and are fixed to a radial lid that covers a top end of said housing cup, the four modules being spaced apart in said housing all along their axial lengths.

19. A filter as in claim 18, wherein said lid comprises outer depending walls that surround an outer perimeter of a top end of each of said modules.

20. A filter as in claim 19, wherein said lid comprises inner depending walls that are received in said bore of each module.

21. A filter as in claim 20, wherein said outer surface of each of the four modules is tapered to be smaller at a bottom end than at a top end of each module.

22. A filter as in claim 18, said modules being made of 30-50 wt-% binder, 28-52 wt-% activated carbon, and 18-22 wt-% lead removal media, wherein the total of said binder, activated carbon, and lead removal media is 100 wt-% of each module.

23. A filter block as in claim 22, wherein said binder is selected from the group consisting of:

thermoplastic binder, thermo-set binder, polyolefins, polyethylene, polyvinyl halides, polyvinyl esters, polyvinyl ethers, polyvinyl sulfates, polyvinyl phosphates, polyvinyl amines, polyamides, polyimides, polyoxidiazoles, polytriazols, polycarbodiimides, polysulfones, polycarbonates, polyethers, polyarylene oxides, polyesters, polyarylates, phenol-formaldehyde resins, melamine-formaldehyde resins, formaldehydeureas, ethyl-vinyl acetate copolymers, co-polymers and block interpolymers thereof, and derivatives and combinations thereof.