IP Library Granted Patent US 10,625,211
Granted Patent B2
US 10,625,211 · App. 16/179,593 · Granted Apr 21, 2020

Method and system for water treatment

Inventors: Gary C. Ganzi (Lexington, MA); Frederick C. Wilkins (Pepperell, MA)
Assignee: Evoqua Water Technologies LLC
B01D61/58A01G25/00B01D61/48C02F1/008C02F1/442C02F1/469C02F1/4693C02F9/00B01D61/027B01D61/44B01D61/46B01D2311/246B01D2311/2649B01D2317/02B01D2317/022B01D2317/08C02F1/441C02F1/444C02F1/4695C02F2103/08C02F2201/46115C02F2209/05C02F2301/08Y02A20/131Y02A20/134
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Quick Facts
Patent No.
US 10,625,211
App. No.
16/179,593
Granted
Apr 21, 2020
Kind
B2
Abstract

Water treatment systems including electrically-driven and pressure-driven separation apparatus configured to produce a first treated water suitable for use as irrigation water and a second treated water suitable for use as potable water from brackish or saline water and methods of operation of same.

Claims (17)

1. A method of treating brackish water to produce irrigation water, the method comprising:

directing water to be treated having a concentration of dissolved salts of between 500 mg/L and 5,000 mg/L to an inlet of an electrodialysis apparatus including one or more monovalent ion selective membranes;

treating the water to be treated in the electrodialysis apparatus to produce a diluate;

directing a first amount of the diluate to an irrigation distribution system and a second amount of the diluate to an inlet of a nanofiltration apparatus;

treating the diluate directed to the inlet of the nanofiltration apparatus in the nanofiltration apparatus to produce a permeate and a retentate; and

combining the retentate with the first amount of the diluate directed to the irrigation distribution system at the irrigation distribution system.

2. The method of claim 1 , further comprising directing at least a portion of the permeate produced in the nanofiltration apparatus to a concentrating compartment of the electrodialysis apparatus.

3. The method of claim 1 , wherein producing the diluate in the electrodialysis apparatus comprises producing treated water having a SAR value of less than about 10.

4. The method of claim 3 , wherein producing the diluate in the electrodialysis apparatus comprises producing treated water having a SAR value of less than about 5.

5. The method of claim 1 , wherein producing the retentate in the nanofiltration apparatus comprises producing treated water having a SAR value of less than the SAR value of the diluate.

6. The method of claim 1 , wherein combining the retentate with the first amount of the diluate directed to the irrigation distribution system comprises producing irrigation water with a SAR value intermediate of a SAR value of the diluate and a SAR value of the retentate.

7. The method of claim 6 , wherein combining the retentate with the first amount of the diluate directed to the irrigation distribution system comprises producing irrigation water with a SAR value of less than about 8 and a total dissolved solids level of greater than about 1,500 ppm.

8. The method of claim 1 , further comprising directing the first amount of the diluate from the electrodialysis apparatus to the irrigation distribution system and directing the second amount of the diluate from electrodialysis apparatus to the nanofiltration apparatus based on one or more parameters of one of the diluate from the electrodialysis apparatus and the retentate from the nanofiltration apparatus.

9. The method of claim 1 , further comprising adjusting one or more operating parameters of the electrodialysis apparatus based on one or more parameters of one of the diluate from the electrodialysis apparatus and the retentate from the nanofiltration apparatus.

10. The method of claim 1 , further comprising removing suspended solids from the water to be treated by pre-filtering the water to be treated prior to directing the water to be treated to the inlet of the electrodialysis apparatus.

11. The method of claim 1 , further comprising directing permeate comprising a total dissolved solids content of less than about 500 ppm, from the permeate outlet of the nanofiltration apparatus to a potable water point of use.

12. The method of claim 1 , further comprising varying an amount of permeate produced in the nanofiltration apparatus directed to the electrodialysis apparatus as concentrate makeup utilizing a diverting system including a valve and a conduit providing direct fluidic communication between the valve and an inlet of a concentrating compartment of the electrodialysis apparatus.

Assignments (3)
RELEASE OF SECURITY INTEREST Recorded May 26, 2023
From: JPMORGAN CHASE BANK N.A., AS COLLATERAL AGENT
To: EVOQUA WATER TECHNOLOGIES LLC; NEPTUNE BENSON, INC.
Reel/Frame 063787/0943 →
SECURITY INTEREST Recorded Apr 7, 2021
From: EVOQUA WATER TECHNOLOGIES LLC; NEPTUNE BENSON, INC.
To: JPMORGAN CHASE BANK, N.A., AS COLLATERAL AGENT
Reel/Frame 055848/0689 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 17, 2018
From: GANZI, GARY C.; WILKINS, FREDERICK C.
To: EVOQUA WATER TECHNOLOGIES LLC
Reel/Frame 047791/0201 →