IP Library Granted Patent US 11,117,813
Granted Patent B1
US 11,117,813 · App. 17/247,986 · Granted Sep 14, 2021

Techniques for managing scale formation in water filtration systems and a reverse osmosis (RO) and nanofiltration (NF) system implementing same

Inventor: Stanton Russel Smith (Waltham, MA)
Assignee: Crosstek Membrane Technology
C02F1/008B01D61/025B01D61/027B01D61/12B01D65/02B01D65/08C02F1/441C02F1/442B01D2311/14B01D2313/18B01D2313/243B01D2321/02B01D2321/16C02F2201/005C02F2209/03C02F2303/16C02F2303/22
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Quick Facts
Patent No.
US 11,117,813
App. No.
17/247,986
Granted
Sep 14, 2021
Kind
B1
Abstract

The present disclosure is directed to filtering technologies that combine elements of continuous and batch NF/RO based on the constraints of the end-user facility to achieve a target balance between, for instance, recovery and power consumption, and to reduce long term operating cost of a plant. A method for extending batch operation into a second induction period with antiscalant injection is also disclosed herein, with the second induction period allowing for yet higher water recovery.

Claims (19)

1. A filter system comprising:

at least one inlet fluidly coupled to at least one feed stream;

at least one filter membrane fluidly coupled to the at least one inlet to receive feed water from the at least one feed stream;

at least one pump to generate a pressure to displace the feed water from the at least one feed stream into the at least one filter membrane and produce an output permeate stream; and

a controller configured to cause a first driving signal to be provided to the at least one pump to cause the generated pressure to produce the output permeate stream at a recovery rate that is substantially equal to a first target recovery rate for a first period of time that is shorter than a period of time when scaling occurs, the first target recovery rate being greater than a maximum non-scaling recovery rate for the at least one filter membrane and less than 100%.

2. The filter system of claim 1 , wherein the controller is further configured to cause a second driving signal to be provided to the at least one pump to cause the generated pressure to produce the output permeate stream at a recovery rate substantially equal to a second target recovery rate during a second period of time.

3. The filter system of claim 2 , wherein the second target recovery rate is equal to or less than a maximum non-scaling recovery rate for the at least one filter, or the second target recovery rate is greater than the maximum non-scaling recovery rate for the at least one filter membrane, or the second target recovery rate is greater than the maximum non-scaling recovery rate for the at least one filter membrane and the first target recovery rate.

4. The filter system of claim 2 , wherein the second driving signal is configured to cause at least a partial flush of the at least one filter membrane, and wherein the second target recovery rate is greater than 0% and less than the maximum non-scaling recovery rate to cause the partial flush of the at least one filter membrane.

5. The filter system of claim 2 , further comprising at least one bleed valve fluidly coupled to the at least one filter membrane to output a first predetermined portion of the feed water of the at least one feed stream as reject water during the second period of time.

6. The filter system of claim 5 , wherein the second target recovery rate is equal to 100%, and wherein the controller is configured to cause the at least one bleed valve to close such that the first predetermined portion of feed water output as reject water is zero percent during the second period of time.

7. The filter system of claim 2 , wherein the second period of time occurs prior to or after the first period of time based on a predetermined sequence of filter operations stored in a memory.

8. The filter system of claim 2 , wherein the second driving signal is further configured to cause one or a plurality of antiscalant doses to be introduced into the at least one filter membrane at a predetermined moment during the second period of time.

9. The filter system of claim 8 , wherein the predetermined moment delineates the second period of time into a first induction period occurring prior to the predetermined moment and a second induction period occurring after the predetermined moment at which antiscalant is introduced, the first induction period being a period of time operating before scaling and/or fouling of the at least one filter membrane occurs, the second induction period being a period of time measured from when the antiscalant is introduced to when scaling and/or fouling of the at least one filter membrane occurs.

10. The filter system of claim 2 , wherein the at least one filter membrane comprises at least first and second filter membranes, each of the first and second filter membranes providing at least a portion of first and second filter stages, respectively.

11. The filter system of claim 10 , further comprising a filter valve arrangement to switchably fluidly couple the first and/or second filter membranes to the at least one feed stream, and wherein the controller is further configured to cause the filter valve arrangement to switchably fluidly couple the first and/or second filter membranes to the at least one feed stream during the first and/or second periods of time.

12. The filter system of claim 1 , wherein the controller is further configured to cause one or a plurality of antiscalant doses to be introduced into the at least one filter membrane at a predetermined moment during the first period of time.

13. The filter system of claim 12 , wherein the predetermined moment delineates the first period of time into a first induction period occurring prior to the predetermined moment and a second induction period occurring after the predetermined moment at which antiscalant is introduced, the first induction period being a period of time operating before scaling and/or fouling of the at least one filter membrane occurs, the second induction period being a period of time measured from when the antiscalant is introduced to when scaling and/or fouling of the at least one filter membrane occurs.

14. The filter system of claim 1 , wherein the at least one filter membrane comprises at least one high-pressure filter membrane with a pressure casing capable of withstanding at least 90 bar of pressure.

15. The filter system of claim 1 , wherein the at least one inlet fluidly couples to a bleed of a filter system such that the at least one feed stream comprises concentrate from the filter system, and/or the at least one inlet fluidly couples to an outlet of a filter system such that the at least one feed stream comprises permeate output by the filter system.

Assignments (3)
NUNC PRO TUNC ASSIGNMENT Recorded May 9, 2025
From: CROSSTEK MEMBRANE TECHNOLOGY LLC; CTX LLC
To: CLEAN H2O TECHNOLOGIES, LLC
Reel/Frame 071077/0522 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 24, 2023
From: CROSSTEK MEMBRANE TECHNOLOGY
To: CTX, LLC
Reel/Frame 062801/0429 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 5, 2021
From: SMITH, STANTON RUSSEL
To: CROSSTEK MEMBRANE TECHNOLOGY
Reel/Frame 054808/0335 →
Cited By (1)
US 12,623,921