ELECTROLYTIC SANITIZATION OF WATER

• US 20100276294A1
• Filed: 05/25/2010
• Published: 11/04/2010
• Est. Priority Date: 03/28/2003
• Status: Abandoned Application

• Current Assignee: John M. Lambie
• Original Assignee: John M. Lambie
• Inventors: Lambie, John M.
• Application Number:
  US12/787,060
• Publication Number:
  US 20100276294A1
• Time in Patent Office: Days
• US Class Current: 205/335
• CPC Class Codes: C02F 1/4674 with halogen or compound of halogens, e.g. chlorine, bromine
• CPC Class Codes: C02F 1/70 by reduction C02F1/4676 takes precedence
• CPC Class Codes: C02F 1/727 using pure oxygen or oxygen rich gas
• CPC Class Codes: C02F 2001/46133 characterised by the material
• CPC Class Codes: C02F 2001/4619 only cathodic or alkaline water, e.g. for reducing
• CPC Class Codes: C02F 2103/007 Contaminated open waterways, rivers, lakes or ponds
• CPC Class Codes: C02F 2209/003 Downstream control, i.e. outlet monitoring, e.g. to check the treating agents, such as halogens or ozone, leaving the process
• CPC Class Codes: C02F 2209/005 Processes using a programmable logic controller [PLC]
• CPC Class Codes: C02F 2209/11 Turbidity
• CPC Class Codes: C02F 2209/29 Chlorine compounds
• CPC Class Codes: C02F 2303/04 Disinfection

Abstract

A method for sanitizing water comprises flowing the water without added electrolyte between opposing first and second electrodes arranged in an electrolysis cell, the water forming a continuous flow that contacts both electrodes simultaneously before exiting the electrolysis cell. The method further comprises biasing the first and second electrodes with respect to each other in response to a relative amount of a bioinhibitory agent in the water exiting the electrolysis cell.

Claims

1. A method for sanitizing water, comprising:

flowing the water without added electrolyte between opposing first and second electrodes arranged in an electrolysis cell, the water forming a continuous flow that contacts both electrodes simultaneously before exiting the electrolysis cell; and

biasing the first and second electrodes with respect to each other in response to a relative amount of a bioinhibitory agent in the water exiting the electrolysis cell.

2. The method of claim 1, wherein the bioinhibitory agent comprises one or more of chlorine, hypochlorite ion, and hypochlorous acid.

3. The method of claim 2, wherein the one or more of chlorine, hypochlorite ion, and hypochlorous acid derives from an oxidation of substantially adventitious chloride ion in the water.

4. The method of claim 1, wherein the bioinhibitory agent comprises oxygen.

5. The method of claim 1, wherein the bioinhibitory agent comprises hydrogen.

6. The method of claim 1 further comprising reading a sensor responsive to the relative amount of the bioinhibitory agent in the water exiting the electrolysis cell.

7. The method of claim 1, wherein biasing the first and second electrodes with respect to each other comprises controlling a current density of the first or second electrode.

8. The method of claim 7, wherein controlling the current density comprises reducing the current density when the relative amount of the bioinhibitory agent increases and increasing the current density when the relative amount of the bioinhibitory agent decreases.

9. The method of claim 1, wherein flowing the water comprises adjusting a pressure of the flowing water, and wherein the pressure is adjusted in response to the relative amount of the bioinhibitory agent.

10. The method of claim 9, wherein adjusting the pressure of the flowing water comprises increasing the pressure as a relative amount of dissolved oxygen in the water exiting the electrolysis cell decreases, and decreasing the pressure as the relative amount of dissolved oxygen increases.

11. The method of claim 1, wherein flowing the water comprises adjusting a flow rate of the flowing water, and wherein the flow rate is adjusted in response to the relative amount of the bioinhibitory agent in the water exiting the electrolysis cell.

12. The method of claim 1 further comprising separating entrained gas bubbles from the water exiting the electrolysis cell.

13. The method of claim 1 further comprising reducing a relative amount of one or more ions in the water exiting the electrolysis cell.

14. A water-treatment system for sanitizing water, comprising:

opposing first and second electrodes arranged in an electrolysis cell and configured to admit a first flow of water therebetween, the first flow forming a continuous flow that contacts both electrodes simultaneously;

a gas-liquid separator arranged downstream of the electrolysis cell and configured to discharge a second flow of water and a third flow of gas;

a sensor responsive to a relative amount of a bioinhibitory agent in the second flow; and

an electronic control system operatively coupled to the sensor and configured to bias the first and second electrodes with respect to each other in response to an output of the sensor.

15. The water-treatment system of claim 14, wherein the first electrode is a dimensionally stable, oxidation-inert anode.

16. The water-treatment system of claim 14, wherein the first electrode comprises one or more of bismuth and titanium dioxide.

17. The water-treatment system of claim 14, wherein the second electrode is a stainless-steel cathode.

18. The water-treatment system of claim 14, wherein the first and second electrodes are separated by between 0.020 and 0.080 inches.

19. The water-treatment system of claim 14 further comprising a finisher arranged downstream of the separator and configured to reduce a relative amount of an undesired chemical species the second flow.

20. A water-treatment system for sanitizing water, comprising:

opposing first and second electrodes arranged in an electrolysis cell, separated by between 0.020 and 0.080 inches, and configured to admit a first flow of water therebetween, the first flow forming a continuous flow that contacts both electrodes simultaneously;

a gas-liquid separator arranged downstream of the electrolysis cell and configured to discharge a second flow of water and a third flow of gas;

a finisher arranged downstream of the separator and configured to reduce a relative amount of an undesired chemical species in the second flow;

a sensor responsive to a relative amount of a bioinhibitory agent in the second flow; and

an electronic control system operatively coupled to the sensor and configured to bias the first and second electrodes with respect to each other in response to an output of the sensor.