← Back to Patent Explorer
US4990260A Expired / Lapsed US ⏱️ 0.0 years remaining

Method and apparatus for removing oxidizable contaminants in water to achieve high purity water for industrial use

Assignee: MAGNUM WATER TECHNOLOGY
•
Filing: 1988-01-28
•
Granted: 1991-02-05
•
Expires: 2008-01-28
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A method and apparatus for removing contaminants in waters used for industrial cleaning. The method and apparatus begins with water which has been purified to level of approximately 18 megaohms resistivity with total inorganic dissolved solids to 1 part per trillion and total organic dissolved carbon contaminants in the range of approximately 100 parts per billion, and purifies it to a level of approximately 18 megaohms resistivity with total inorganic dissolved solids to 1 part per trillion and total organic dissolved carbon contaminants in the range of approximately 10 parts per billion. The method and apparatus includes means for inducing cavitation in the water and irradiating the water with ultraviolet radiation to thereby cause the oxidizable contaminants to be oxidized and therefore removed before the water is used for industrial cleaning.

Inventors

  • 👤 Joseph Pisani

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 23:42
CPC Classifications
C; C02; C02F; C02F1/00; C02F1/34; B; B01; B01J; B01J47/00; B01J47/02; B01J47/04; C02F1/30; C02F1/32; C02F1/20; C02F1/44; C02F1/441; C02F1/42; C02F2001/427; C02F2103/00; C02F2103/02; C02F2103/04; C02F2303/00; C02F2303/04; C02F2305/00; C02F2305/02; C02F2305/023; Y; Y10; Y10S; Y10S210/00; Y10S210/90

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 245 words
A method for removing oxidizable contaminants in recycled water prior to use of the water, wherein the water has been pre-treated to achieve a purity level of approximately 18 megaohms resistivity with dissolved total inorganic solids of 1 part per trillion and dissolved total organic carbon contaminants in the range of approximately 100 parts per billion, comprising: a. inducing cavitation in the water by causing the water to flow through a cavitation critical flow nozzle wherein the hydrodynamic pressure of the water is lower than the vapor pressure of the water causing vapor bubbles to form and then collapse as the pressures equilibrate, imparting a large amplitude shock wave of several hundred atmospheres with local temperatures of many hundred degrees centigrade to thereby create hydroxyl free radicals in the water to act as an oxidizing agent; and b. irradiating the cavitated water containing the hydroxyl free radicals with ultraviolet radiation by causing the cavitated water to flow into an ultraviolet reactor and be irradiated by an ultraviolet lamp; c. whereby the cavitation process which creates the hydroxyl free radicals oxidizes the oxidizable organic contaminants in the water and the irradiation with ultraviolet radiation continues the oxidation process initiated by the hydroxyl free radicals to fully oxidize the oxidizable organic contaminants and thereby decompose the oxidizable organic contaminants contained in the water so that the water is purified to a level of dissolved total organic carbon contaminants in the range of approximately 10 parts per billion.
Claim 2
Independent Claim 245 words
A method for removing oxidizable contaminants in recycled water prior to use of the water, wherein the water has been pre-treated to achieve a purity level of approximately 18 megaohms resistivity with dissolved total inorganic solids of 1 part per trillion and dissolved total organic carbon contaminants in the range of approximately 100 parts per billion, comprising: a. inducing cavitation in the water by causing the water to flow through a cavitation critical flow nozzle wherein the hydrodynamic pressure of the water is lower than the vapor pressure of the water causing vapor bubbles to form and then collapse as the pressures equilibrate, imparting a large amplitude shock wave of several hundred atmospheres with local temperatures of many hundred degrees centigrade to thereby create hydroxyl free radicals in the water to act as an oxidizing agent; and b. irradiating the cavitated water containing the hydroxyl free radicals with ultraviolet radiation by causing the cavitated water to flow into an ultraviolet reactor and be irradiated by an ultraviolet lamp; c. whereby the cavitation process which creates the hydroxyl free radicals oxidizes the oxidizable organic contaminants in the water and the irradiation with ultraviolet radiation continues the oxidation process initiated by the hydroxyl free radicals to fully oxidize the oxidizable organic contaminants and thereby decompose the oxidizable organic contaminants contained in the water so that the water is purified to a level of dissolved total organic carbon contaminants in the range of approximately 10 parts per billion.
Claim 3
Dependent Claim 31 words
The method in accordance with claim 1 further comprising repeating steps a and b until a purity level of dissolved total organic carbon contaminants of 10 parts per billion is achieved.
Claim 4
Dependent Claim 17 words
The method in accordance with claim 1 wherein said ultraviolet lamp has a wavelength of 254 nanometers.
Claim 5
Dependent Claim 17 words
The method in accordance with claim 1 wherein said ultraviolet lamp has a wavelength of 185 nanometers.
Claim 6
Dependent Claim 24 words
The method in accordance with claim 1 further comprising venting carbon dioxide gases from the water while it is being irradiated with ultraviolet radiation.
Claim 7
Dependent Claim 31 words
The method in accordance with claim 1 comprising treating the water with a mixed bed cation-anion exchange means to further purify the water after steps a and b have been performed.
Claim 8
Dependent Claim 35 words
The method in accordance with claim 1 comprising the further steps of: a. degassifying the water to remove excess carbon dioxide; and b. filtering the water to remove particles of 0.2 micron and greater diameter.

References Cited (Backward Citations)

US4280912A Cited
US4296066A Cited
US4273660A Cited
US4544499A Cited
US4296328A Cited
US4428757A Cited
US4698153A Cited
US4764278A Cited
US4842723A Cited
US4808287A Cited
JPH0297687A Cited
JPH0297686A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1994-02-04 1994-08-06 1995-02-05 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1998-02-04 1998-08-06 1999-02-05 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2002-02-04 2002-08-06 2003-02-05 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag