Method for treatment and reuse of used water streams

Patent metadata

Field	Value
Publication number	US-9617173-B2
Application number	US-201313783496-A
Country	US
Kind code	B2
Filing date	Mar 4, 2013
Priority date	Mar 4, 2013
Publication date	Apr 11, 2017
Grant date	Apr 11, 2017

Abstract

Methods for recovering energy and water from at least one energy-rich process water stream are provided. The methods optionally incorporate the use of filtration, reverse osmosis, ion exchange, water softening, forward osmosis, and membrane distillation. The methods can be used to recover energy and water from blowdown or condensate from a water-containing industrial process, which in certain embodiments may be a boiler system.

First claim

The invention claimed is:

1. A method for improving efficiency of a water-containing industrial process, the method comprising:
feeding energy-rich process water or energy-rich process water filtrate formed by filtering energy-rich process water to a membrane distillation unit, thereby creating a membrane distillate and an energy-rich aqueous liquid;
purifying the energy-rich aqueous liquid using a salinated liquid as a draw stream in a forward osmosis unit, thereby creating a diluted stream;
preliminarily purifying a stream comprising at least one of the energy-rich aqueous liquid and the diluted stream using a technique selected from the group consisting of: reverse osmosis, ion exchange, water softening, and combinations thereof, thereby creating purified water;
feeding the purified water and the membrane distillate into at least one heated thermal industrial water system.

2. The method of claim 1 , wherein the energy-rich process water is discharged from the heated thermal industrial water system.

3. The method of claim 1 , wherein the at least one heated thermal industrial water system is a boiler system, and the purified makeup water stream and the membrane distillate stream are combined into a single stream prior to being fed into the boiler system.

4. The method of claim 1 , wherein the energy-rich process water is a blowdown water from a boiler system.

5. The method of claim 1 , wherein the energy-rich process water is a condensate water from an industrial process selected from the group consisting of a boiler system; food processing; dairy processing; beverage processing; landfill leachate processing; biofuel processing; and combinations thereof.

6. The method of claim 1 , wherein the optional filtering is present and, prior to filtering, the energy-rich process water is treated with a compound selected from the group consisting of a coagulant, a flocculant, an adsorbent, and combinations thereof.

7. The method of claim 1 , wherein the stream being preliminarily purified further comprises raw water.

8. The method of claim 1 , wherein the preliminary purification technique is reverse osmosis.

9. A method for improving efficiency of a water-containing industrial process, the method comprising:
treating energy-rich process water with a compound selected from the group consisting of a flocculant, a coagulant, an adsorbent, and combinations thereof, thereby creating treated energy-rich process water;
feeding the energy-rich process water, the treated energy-rich process water, or energy-rich process water filtrate formed by filtering the energy-rich process water or the treated energy-rich process water to a membrane distillation unit, thereby creating a membrane distillate and an energy-rich aqueous liquid;
purifying the energy-rich aqueous liquid using a salinated liquid as a draw stream in a forward osmosis unit, thereby creating a diluted stream;
preliminarily purifying a stream comprising the diluted stream using a technique selected from the group consisting of: reverse osmosis, ion exchange, water softening, and combinations thereof, thereby creating a purified water;
feeding the purified water and the membrane distillate into at least one heated thermal industrial water system.

10. The method of claim 9 , wherein the filtering is present and utilizes at least one of ultrafiltration, microfiltration, media filtration, and combinations thereof.

11. The method of claim 9 , wherein the stream being purified further comprises raw water.

12. The method of claim 9 , wherein the salinated liquid comprises a reverse osmosis reject stream.

13. The method of claim 9 , wherein the forward osmosis unit is operated in forward osmosis mode.

14. The method of claim 9 , wherein the forward osmosis unit is operated in pressure retarded osmosis mode.

15. The method of claim 9 , wherein the optional filtering is present and, prior to filtering, the energy-rich process water is treated with a compound selected from the group consisting of a coagulant, a flocculant, an adsorbent, and combinations thereof.

16. The method of claim 9 , wherein the preliminary purification technique is reverse osmosis.

17. A method for improving efficiency of a heated thermal industrial water system, the method comprising:
optionally treating energy-rich process water from a boiler system with a compound selected from the group consisting of a flocculant, a coagulant, an adsorbent, and combinations thereof, thereby creating treated energy-rich process water;
filtering energy-rich process water or the treated energy-rich process water, thereby creating an energy-rich process water filtrate;
feeding the energy-rich process water filtrate to a membrane distillation unit, thereby creating a membrane distillate and an energy rich aqueous liquid;
purifying the energy-rich aqueous liquid using a salinated liquid as a draw stream in a forward osmosis unit, thereby creating a diluted stream;
preliminarily purifying raw water and the diluted stream using reverse osmosis, thereby creating a purified water and a reverse osmosis reject stream, wherein the reverse osmosis reject stream is capable of serving as the salinated liquid that is fed into the forward osmosis unit;
feeding the purified water and the membrane distillate into the boiler system.

18. The method of claim 17 , wherein the energy-rich process water is blowdown water from the boiler system.

19. The method of claim 17 , wherein the energy-rich process water or the treated energy-rich process water is filtered using at least one of ultrafiltration, microfiltration, media filtration, and combinations thereof.

20. The method of claim 17 , wherein the energy-rich process water is treated with a compound selected from the group consisting of a coagulant, a flocculant, an adsorbent, and combinations thereof.

Assignees

• Ecolab Usa Inc

Inventors

• Musale Deepak A
• Fowee Roger W

Classifications

• C02F9/00

  Multistage treatment of water, waste water or sewage · CPC title

• C02F1/441

  by reverse osmosis · CPC title

• C02F1/447 Primary

  by membrane distillation (distillation and evaporation without the use of membranes C02F1/04) · CPC title

• C02F1/28

  by sorption (using ion-exchange C02F1/42; sorbent compositions B01J) · CPC title

• C02F1/56

  Macromolecular compounds · CPC title