Process for desalination of saline water, especially water, having increased product yield and quality

• US 6,508,936 B1
• Filed: 10/01/1997
• Issued: 01/21/2003
• Est. Priority Date: 10/01/1997
• Status: Expired due to Term

• Current Assignee: Saline Water Conversion Corporation
• Original Assignee: Saline Water Conversion Corporation
• Inventors: Hassan, Ata M.
• Primary Examiner(s): FORTUNA, ANA M
• Application Number:
  US08/941,827
• Time in Patent Office: 1,938 Days
• Field of Search: 210/652, 210/641, 210/180, 210/175, 203/12
• US Class Current: 210/652
• CPC Class Codes: B01D 1/26 Multiple-effect evaporating
• CPC Class Codes: B01D 3/065 Multiple-effect flash distillation (more than two traps)
• CPC Class Codes: B01D 61/029 Multistep processes comprising different kinds of membrane processes selected from reverse osmosis, hyperfiltration or nanofiltration
• CPC Class Codes: C02F 1/04 by distillation or evaporation
• CPC Class Codes: C02F 1/041 by means of vapour compression
• CPC Class Codes: C02F 1/06 Flash evaporation
• CPC Class Codes: C02F 1/441 by reverse osmosis
• CPC Class Codes: C02F 1/442 by nanofiltration
• CPC Class Codes: C02F 2103/08 Seawater, e.g. for desalination
• CPC Class Codes: Y02A 20/124 Water desalination
• CPC Class Codes: Y02A 20/131 Reverse-osmosis

Abstract

A desalination process is disclosed which combining two or more substantially different water treatment processes in a unique manner to desalinate saline water, especially sea water, to produce a high yield of high quality fresh water, including potable water, at an energy consumption equivalent to or less than much less efficient prior art desalination processes. In this process a nanofiltration step is synergistically combined with at least one of sea water reverse osmosis, multistage flash distillation. multieffect distillation of vapor compression distillation to provide an integrated desalination system by which sea water can be efficiently and economically converted to high quality potable water in yields which are at least 70%-80% greater than the yields available from the prior art processes. Typically a process of this invention using the nanofiltration initial step will produce, with respect to sea water feed properties, calcium, magnesium, sulfate and bicarbonate ion content reductions of 63%-94%, pH decreases of about 0.4-0.5 units and total dissolved solids content reductions of 35%-50%.

Claims

1. A desalination process which comprises passing sea water containing a high content of hardness scale forming ionic species, microorganisms or particulate matter or total dissolved solids through a membrane nanofiltration unit to form a first water product having a reduced content of said ionic species, microorganisms, particulate matter or total dissolved solids, and thereafter passing said first water product through a thermal distillation unit to form a second water product of potable quality without salt production.

2. A desalination process as in claim 1 wherein said first water product is passed through at least one of multistage flash distillation, multieffect distillation or vapor compression distillation to form said second water product.

3. A desalination process as in claim 1 wherein said sea water has a cation content on the order of 1.2%-1.7%, an anion content on the order of 2.2%-2.8%, a pH on the order of 7.9-8.2, comparable to a total dissolved solids content on the order of 3.0%-5.0%.

4. A desalination process as in claim 3 further comprising said cation content including 700-2200 ppm of calcium and magnesium cations.

5. A desalination process as in claim 4 wherein, with respect to said sea water properties, calcium, magnesium, sulfate and bicarbonate ion content is reduced on the order of 63%-94%, pH is decreased by about 0.4-0.5 units and total dissolved solids content is reduced by about 35%-50%.

6. A desalination process as in claim 1 wherein said nanofiltration unit is operated at a temperature on the order of 15°

-40°

C. and a pressure on the order of 15-25 bar.

7. A desalination process as in claim 1 wherein said sea water reverse osmosis unit is operated at a temperature on the order of 15°

-40°

C. and a pressure on the order of 15-25 bar.

8. A desalination process as in claim 1 wherein said multistage distillation, multieffect distillation or vapor compression distillation unit is operated at a temperature on the order of up to about 120°

-130°

C.

9. A desalination process as in claim 1 wherein said first water product is divided into a first portion and a second portion, said first portion thereafter being passed through a thermal distillation unit to form a second water product of potable quality without salt production and said second portion thereafter being passed through a sea water reverse osmosis unit to form a second water product of potable quality and a reject water product having increased salinity and reduced hardness, and thereafter passing said reject water product through a thermal distillation unit to form a third water product of potable quality without salt production.

10. A desalination process as in claim 9 wherein said sea water has a cation content on the order of 1.2%-1.7%, an anion content on the order of 2.2%-2.8%, a pH on the order of 7.9-8.2, comparable to a total dissolved solids content on the order of 3.0%-5.0%.

11. A desalination process as in claim 10 further comprising said cation content including 700-2200 ppm of calcium and magnesium cations.

12. A desalination process as in claim 9 wherein said nanofiltration unit is operated at a temperature on the order of 15°

-40°

C. and a pressure on the order of 15-25 bar.

13. A desalination process as in claim 9 wherein said sea water reverse osmosis unit is operated at a temperature on the order of 15°

-40°

C. and a pressure on the order of 15-25 bar.

14. A desalination process as in claim 9 wherein said multistage distillation, multieffect distillation or vapor compression distillation unit is operated at a temperature on the order of up to about 120°

-130°

C.

15. A desalination process as in claim 9 wherein said thermal distillation unit comprises a multistage flash distillation unit, a multieffect distillation unit or a vapor compression distillation unit.