IP Library Granted Patent US 9,637,397
Granted Patent B2
US 9,637,397 · App. 13/283,265 · Granted May 2, 2017

Ion removal using a capacitive deionization system

Inventors: David J. Averbeck (Dousman, WI); Rebecca M. Tallon (Hartland, WI); Brett A. Boedeker (Glendale, WI)
Assignee: Pentair Residential Filtration, LLC
C02F1/008C02F1/4691C02F1/281C02F1/283C02F1/32C02F2201/4611C02F2201/46125C02F2201/46135C02F2201/46145C02F2209/001C02F2209/003C02F2209/005C02F2209/03C02F2209/05C02F2209/40
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Quick Facts
Patent No.
US 9,637,397
App. No.
13/283,265
Filed
Oct 27, 2011
Granted
May 2, 2017
Kind
B2
Art Unit
1756
USPC
204/519
Abstract

Embodiments of the invention provide methods of removing ions from a feed water stream using a flow-through capacitor and a controller for performing the methods. A target value for a water property concentration or a fixed percent removal of a water property concentration to be removed is established for a treated water stream exiting the flow-through capacitor. A feed value for the water property concentration is measured in a feed water stream entering the flow-through capacitor. An amperage of the flow-through capacitor and a flow rate through the flow-through capacitor is controlled to remove ions from the feed water stream to achieve the desired removal of the water property.

Claims (41)

1. A method of removing ions from a feed water stream using a flow-through capacitor having at least a pair of electrodes spaced from one another to accommodate a flow of water and configured to transfer ions between the pair of electrodes and the water, the method comprising:

establishing a target value for a water property concentration for a treated water stream exiting the flow-through capacitor;

measuring a feed value for the water property concentration in a feed water stream entering the flow-through capacitor;

calculating an amount of the water property concentration to be removed from the feed water stream based on the feed value to achieve the target value for the water property concentration in the treated water stream;

controlling an amperage of the flow-through capacitor and a flow rate through the flow-through capacitor to remove ions from the feed water stream to achieve the target value for the water property concentration in the treated water stream; and

wherein an end point of a treatment cycle is established by a comparison of a monitored-current capacity of the flow-through capacitor over the duration of the treatment cycle to a summed-current capacity of the flow-through capacitor that is pre-established.

2. The method of claim 1 wherein the amperage is a function of an amount of ions to be removed from the feed water stream.

3. The method of claim 2 wherein the amount of ions correlates to the amount of the water property concentration to be removed from the feed water stream.

4. The method of claim 2 wherein the amperage is further a function of the flow rate.

5. The method of claim 1 wherein the water property concentration correlates to conductivity and the feed value that is measured is conductivity.

6. The method of claim 1 further comprising limiting the amount of the water property concentration to be removed at a given flow rate based on a voltage limit of the flow-through capacitor.

7. The method of claim 1 wherein the flow rate is based on a system demand for water in a system attached to the flow-through capacitor.

8. The method of claim 7 wherein the system demand is measured by measuring at least one of a water pressure in the system and a tank water level.

9. The method of claim 7 wherein, when the system demand for water exceeds an ability of the flow-through capacitor to remove the amount of the water property concentration from the feed water stream at a particular demand flow rate, the amount of the water property concentration to be removed from the feed water stream is reduced.

10. The method of claim 1 further comprising the step of measuring the water property concentration for the treated water stream exiting the flow-through capacitor and altering control of at least one of the amperage and flow rate if a measured value of the water property concentration is different than the target value.

11. The method of claim 1 further comprising calculating a volume of the feed water stream that can be treated given a summed-current capacity of the flow-through capacitor and establishing a time duration of a treatment cycle based on the summed-current capacity and the flow rate.

12. The method of claim 1 wherein an end point of a treatment cycle is established when a maximum voltage of the flow-through capacitor is reached.

13. The method of claim 1 wherein the flow rate is varied over a time duration of the cycle to inhibit scaling.

14. The method of claim 1 wherein an end point of a treatment cycle is established when a maximum voltage of the flow-through capacitor is reached and the summed-current capacity of the system is adjusted based to be a monitored-current capacity at the maximum voltage.

15. The method of claim 1 wherein an end point of the treatment cycle is established when at least one of a pre-determined volume of the feed water stream has been treated and a duration of the cycle is reached.

16. The method of claim 1 wherein the flow rate has maximum and minimum flow rates.

17. A method of removing ions from a feed water stream using a flow-through capacitor having at least a pair of electrodes spaced from one another to accommodate a flow of water and configured to transfer ions between the pair of electrodes and the water, the method comprising:

establishing a fixed percent removal of a water property concentration to be removed from the feed water stream passing through the flow-through capacitor;

measuring a feed value for the water property concentration in a feed water stream entering the flow-through capacitor; and

controlling an amperage of the flow-through capacitor and a flow rate through the flow-through capacitor to remove ions from the feed water stream to achieve the fixed percent removal of the water property concentration from the feed water stream;

wherein an end point of a treatment cycle is established by a comparison of a monitored-current capacity of the flow-through capacitor over the duration of the treatment cycle to a summed-current capacity of the flow-through capacitor that is pre-established.

18. The method of claim 17 wherein the amperage is a function of an amount of ions to be removed from the feed water stream.

19. The method of claim 18 wherein the amount of ions correlates to the fixed percent removal of the water property concentration to be removed from the feed water stream.

20. The method of claim 18 wherein the amperage is further a function of the flow rate.

21. The method of claim 17 wherein the water property concentration correlates to conductivity and the feed value that is measured is conductivity.

22. The method of claim 17 further comprising limiting an amount of ions to be removed at a given flow rate based on a voltage limit of the flow-through capacitor.

23. The method of claim 17 wherein the flow rate is based on a system demand for water in a system attached to the flow-through capacitor.

24. The method of claim 23 wherein the system demand is measured by measuring at least one of a water pressure in the system and a tank water level.

25. The method of claim 23 wherein, when the system demand for water exceeds an ability of the flow-through capacitor to remove an amount of ions from the feed water stream at a particular demand flow rate, the amount ions to be removed from the feed water stream is reduced.

26. The method of claim 17 further comprising the step of measuring the water property concentration for the treated water stream exiting the flow-through capacitor and altering control of at least one of the amperage and flow rate if a measured removal percent value of the water property concentration is different than the fixed percent removal that is targeted.

27. The method of claim 17 further comprising calculating a volume of the feed water stream that can be treated given a summed-current capacity of the flow-through capacitor and establishing a time duration of a treatment cycle based on the summed-current capacity and the flow rate.

28. The method of claim 17 wherein an end point of a treatment cycle is established when a maximum voltage of the flow-through capacitor is reached.

29. The method of claim 17 wherein the flow rate is varied over a time duration of the cycle to inhibit scaling.

30. The method of claim 17 wherein an end point of a treatment cycle is established when a maximum voltage of the flow-through capacitor is reached and the summed-current capacity of the system is adjusted based to be a monitored-current capacity at the maximum voltage.

31. The method of claim 17 wherein an end point of the treatment cycle is established when at least one of a pre-determined volume of the feed water stream has been treated and a pre-determined duration of the cycle is reached.

32. The method of claim 17 wherein the flow rate has maximum and minimum flow rates.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 10, 2012
From: AVERBECK, DAVID J.; TALLON, REBECCA M.; BOEDEKER, BRETT A.
To: PENTAIR RESIDENTIAL FILTRATION, LLC
Reel/Frame 027511/0030 →
Continuity (1)
Related Publication 20130105323A1 · May 2, 2013