Sea water reverse osmosis system to reduce concentrate volume prior to disposal

Patent metadata

Field	Value
Publication number	US-10005681-B2
Application number	US-201715474297-A
Country	US
Kind code	B2
Filing date	Mar 30, 2017
Priority date	Aug 13, 2009
Publication date	Jun 26, 2018
Grant date	Jun 26, 2018

Abstract

The present invention includes systems and methods for treatment of seawater RO system for recovering most of the water (i.e., 85-90%) from the concentrate of a brackish groundwater reverse osmosis treatment system that may use, e.g., a batch method. With proper pH control and antiscalant dosage, the batch-treatment SWRO system of the present invention can be used to recover water from silica-saturated RO concentrate without fouling the membranes. Silica concentrations of over 1,000 mg/L are attainable with relatively minimal pre-treatment of the silica-saturated feed solution.

First claim

The invention claimed is:

1. A method of enhanced recovery from a concentrated feed stream comprising the steps of:
inputting the concentrated feed stream into a feed tank;
measuring a concentrated feed stream saturation resulting from one or more compounds in the concentrated feed stream;
determining an induction time of the concentrated feed stream according to the measured saturation of the concentrated feed from the one or more compounds;
feeding a concentrate from the feed tank to a membrane unit by pumping at a high pressure, wherein the membrane unit comprises one or more reverse osmosis membranes;
passing the concentrate through the one or more reverse osmosis membranes in a batch mode;
collecting a permeate stream from each of the one or more reverse osmosis membranes in a permeate tank; and
flushing each of the one or more reverse osmosis membranes before an expiration of the induction time determined for the concentrate feed stream.

2. The method of claim 1 further comprising:
adding an anti-sealant to the concentrated feed stream.

3. The method of claim 1 , wherein the batch mode further comprises:
halting the feeding of the concentrate from the feed tank to the membrane unit while the flushing of each of the one or reverse osmosis membranes is completed.

4. The method of claim 1 further comprising:
filtering the concentrated feed stream in the feed with a 5μ prefilter and a 1μ prefilter arranged in series between the feed tank and the membrane unit.

5. The method of claim 1 , wherein flushing each of the one or more reverse osmosis membranes further comprises:
flushing the reverse osmosis membranes with at least one of:
the feed concentrate; and
the permeate.

6. The method of claim 1 wherein the concentrated feed stream is saturated with at least one of the following salts:
calcium;
magnesium;
barium; and
strontium.

7. The method of claim 1 , wherein the concentrated feed stream comprises one of:
a concentrate with a total silica concentration exceeding 120 mg/L; and
a calcium sulfate concentration exceeding 2200 mg/L.

8. The method of claim 1 , wherein the one or more reverse osmosis membranes comprises at least one of:
a spiral-wound membrane; and
a hollow-fiber membrane.

9. The method of claim 1 , wherein the one or more reverse osmosis membrane comprises on of:
a polyamide membrane or a cellulose acetate membrane.

10. The method of claim 4 further comprising:
monitoring a temperature of the prefiltered concentrate with a temperature sensor between the 1μ prefilter and the membrane unit;
monitoring a conductivity of the prefiltered concentrate with a conductivity sensor between the 1μ prefilter and the membrane unit;
monitoring a pressure of the prefiltered concentrate with a pressure sensor between the 1μ prefilter and the membrane unit; and
monitoring a pH of the prefiltered concentrate with a pH sensor the 1μ prefilter and the membrane unit.

11. A method of reducing concentration of a silica saturated reverse osmosis concentrate comprising:
inputting a concentrated feed stream into a feed tank;
feeding a concentrate from the feed tank to a 5μ prefilter and a 1μ prefilter arranged in series;
feeding the prefiltered concentrate from the 1μ prefilter to a membrane unit by pumping at a high pressure, wherein the membrane unit comprises a plurality of stages, each of said plurality of stages comprising one or more reverse osmosis membranes arranged in a parallel configuration;
measuring a concentrate saturation of a concentrate after each of the plurality of stages;
determining an induction time of the concentrate after each of the plurality of stages according to the measured saturation of the concentrate;
passing the prefiltered concentrate through the membrane unit in batch mode;
collecting a permeate stream from each of the plurality of stages in a permeate tank; and
flushing each of the plurality of stages before an expiration of the induction time determined for that stage is reached.

12. The method of claim 11 , further comprising:
adding an anti-sealant to the concentrated feed stream.

13. The method of claim 11 , wherein the batch mode further comprises:
halting the feeding of the concentrate from the feed tank to the membrane unit while the flushing of each of the one or more reverse osmosis membranes is completed.

14. The method of claim 11 , wherein a total silica concentration of the concentrated feed stream exceeds 120 mg/L.

15. The method of claim 11 , wherein the one or more osmosis membranes comprises at least one of:
a spiral-wound membrane; and
a hollow-fiber membrane.

16. A water treatment system comprising:
a first water treatment system; and
an enhanced recovery system comprising:
a feed tank for collecting a concentrated feed stream comprising concentrate from the first water treatment system;
a membrane unit comprising at least one reverse osmosis membrane;
a pump for passing the feed water from the feed tank through the membrane unit to separate a permeate and a concentrate;
a computer system, the computer system configured to provide operations comprising:
measuring the concentrated feed stream saturation resulting from one or more compounds in the concentrated feed stream; and
determining an induction time of the concentrated feed stream according to the measured saturation of the concentrated feed stream from the one or more compounds;
a flushing system configured to flush the at least one reverse osmosis membrane before an expiration of the induction time determined for the concentrate; and
permeate tank for collecting the permeate from the enhanced recovery system.

17. The water treatment system of claim 16 wherein the first water treatment system further comprises:
a desalination system for desalinating water, wherein the desalination system provides the concentrated feed stream to the enhanced recovery system.

18. The water treatment system of claim 16 wherein the at least one reverse osmosis membrane comprises at least two semi-permeable reverse osmosis membranes, the at least two semi-permeable reverse osmosis membranes being arranged in a parallel single-stage configuration.

19. The water treatment system of claim 16 further comprising:
a temperature sensor for monitoring a temperature of the concentrate;
a conductivity sensor for monitoring a conductivity of the concentrate;
a pressure sensor for monitoring a pressure of the concentrate; and
a pH sensor for monitoring a pH of the concentrate.

Assignees

• Univ Texas
• Univ Texas

Inventors

• Tarquin Anthony J
• Walker William S
• Delgado Guillermo G

Classifications

• B01D69/08

  Hollow fibre membranes (manufacture of hollow fibres D01D5/24, D01F1/08) · CPC title

• B01D2311/08

  Specific process operations in the concentrate stream · CPC title

• B01D2311/14

  Pressure control · CPC title

• B01D61/022

  Operations & Transport · mapped topic

• C02F2209/40

  Liquid flow rate · CPC title