US4276180A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Industrial waste-water reuse by selective silica removal over activated alumina
Assignee: Individual
•
Filing: 1979-11-30
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Granted: 1981-06-30
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Expires: 1999-11-30
Abstract
Abstract Industrial waste-water, particularly cooling water containing water conditioning chemical additives, which heretofore has been discharged to the environment as blowdown because of high silica content, may now be treated for selective silica removal to condition it for reuse in industrial systems. It has been discovered that silica may be effectively and selectively removed from such waste-water streams without the consequential removal of its beneficial chemical conditioning additives by passing such water over activated alumina and thereafter returning it to the system from which it was withdrawn thereby maintaining the silica concentration in the system below its scale formation level.
Inventors
- 👤 Jack V. Matson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 18:06
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/28; C02F1/281; C02F1/58; C02F1/60; C02F2103/00; C02F2103/02; C02F2103/023; Y; Y10; Y10S; Y10S423/00; Y10S423/19
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
139 words
A method for maintaining silica content in a recirculating cooling water system containing water conditioning chemicals selected from the group consisting of sulfates, phosphonates and chromates below a level at which silica scale formation occurs without discharging blowdown from the system with consequential elimination from the system of said water conditioning chemicals or resulting pollution of the environment, comprising the steps of: (a) continuously diverting a portion of the chemically conditioned cooling water from said cooling water system as a side stream; (b) contacting said side stream with activated alumina while said side stream has a pH value of from about 7.0 to about 9.0 to selectively remove silica from said water while leaving the chemical conditioning of the water undisturbed; and (c) then returning said chemically conditioned side stream of reduced silica content to the cooling water system.
Claim 2
Independent Claim
139 words
A method for maintaining silica content in a recirculating cooling water system containing water conditioning chemicals selected from the group consisting of sulfates, phosphonates and chromates below a level at which silica scale formation occurs without discharging blowdown from the system with consequential elimination from the system of said water conditioning chemicals or resulting pollution of the environment, comprising the steps of: (a) continuously diverting a portion of the chemically conditioned cooling water from said cooling water system as a side stream; (b) contacting said side stream with activated alumina while said side stream has a pH value of from about 7.0 to about 9.0 to selectively remove silica from said water while leaving the chemical conditioning of the water undisturbed; and (c) then returning said chemically conditioned side stream of reduced silica content to the cooling water system.
Claim 3
Dependent Claim
18 words
The method of claim 1, wherein the pH of said water is from about 8.0 to about 8.5.
Claim 4
Dependent Claim
12 words
The method of claim 2, wherein the chemically conditioned water contains sulfates.
Claim 5
Dependent Claim
16 words
The method of claim 2, wherein at least some of the water conditioning chemicals are phosphonates.
Claim 6
Dependent Claim
16 words
The method of claim 2, wherein at least some of the water conditioning chemicals are chromates.
Claim 7
Dependent Claim
31 words
The method of claim 2, wherein the silica content of the recirculating cooling water system is maintained below about 160 mg/1 by passing the diverted water stream over said activated alumina.
Claim 8
Dependent Claim
27 words
The method of claim 2, wherein the side stream has a temperature of from about 0° C. to about 50° C. as it contacts the activated alumina.
Claim 9
Dependent Claim
27 words
The method of claim 2, wherein the side stream has a temperature of from about 30° C. to about 50° C. as it contacts the activated alumina.
Claim 10
Dependent Claim
27 words
The process of claim 8 wherein the side stream is contacted with the activated alumina at a residence time of between about 3 to about 10 minutes.
Claim 11
Independent Claim
167 words
A method for maintaining silica concentration in a recirculating cooling water system containing water conditioning chemicals selected from the group consisting of sulfates, phosphonates and chromates below a level at which silica scale formation occurs without discharging blowdown from the system with consequential elimination from the system of said water conditioning chemicals or resulting pollution of the environment, comprising the steps of: (a) continuously diverting a portion of the chemically conditioned cooling water from said cooling water system as a side stream; (b) contacting said side stream with activated alumina at a residence time of from about 5 minutes to about 30 minutes while said side stream has a pH value of from about 8.0 to about 9.0 and a temperature of from about 30° C. to about 50° C. to selectively remove silica from said side stream without otherwise significantly disturbing the chemical conditioning of said side stream; and (c) then returning said chemically conditioned side stream of reduced silica content to the cooling water system.
Claim 12
Independent Claim
167 words
A method for maintaining silica concentration in a recirculating cooling water system containing water conditioning chemicals selected from the group consisting of sulfates, phosphonates and chromates below a level at which silica scale formation occurs without discharging blowdown from the system with consequential elimination from the system of said water conditioning chemicals or resulting pollution of the environment, comprising the steps of: (a) continuously diverting a portion of the chemically conditioned cooling water from said cooling water system as a side stream; (b) contacting said side stream with activated alumina at a residence time of from about 5 minutes to about 30 minutes while said side stream has a pH value of from about 8.0 to about 9.0 and a temperature of from about 30° C. to about 50° C. to selectively remove silica from said side stream without otherwise significantly disturbing the chemical conditioning of said side stream; and (c) then returning said chemically conditioned side stream of reduced silica content to the cooling water system.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-06-29 | 1984-12-29 | 1985-06-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-06-29 | 1988-12-29 | 1989-06-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-06-29 | 1992-12-29 | 1993-06-30 | $7700.00 | Window Closed / Lapsed |