Apparatus and process for desalination of water

Patent metadata

Field	Value
Publication number	US-9688548-B2
Application number	US-201314419602-A
Country	US
Kind code	B2
Filing date	Feb 13, 2013
Priority date	Aug 8, 2012
Publication date	Jun 27, 2017
Grant date	Jun 27, 2017

Abstract

A process for desalinating water is disclosed. The process comprises the steps of passing a feed stream of saline solution 2 ′ in a first desalination step through a reverse osmosis membrane desalination plant 3 ′ comprising at least one reverse osmosis desalination unit 4 ′ to form a first product water stream 5 ′ having a reduced salt concentration relative to that of the feed stream of saline solution 2 ′ and a first byproduct stream 6 ′ having an increased salt concentration relative to that of the feed stream of saline solution 2 ′ characterized in that the first byproduct stream 6 ′ is passed in a second desalination step through a suspension crystallization unit 7 to form a second product water stream 8 having a reduced salt concentration relative to that of the first byproduct stream 6 ′ and a second byproduct stream 9 having an increased salt concentration relative to that of the first byproduct stream 6 ′. The invention further relates to an apparatus 1 for carrying out said process. The present invention further relates also to the use of the process or apparatus 1 for the reduction of the volume of the first byproduct stream of a reverse osmosis membrane desalination plant 3 ′, preferably an in-land desalination plant 3 ′, or in a device or plant or process for producing desalinated water, for salt production, for co-production of power and desalinated water, or for air conditioning.

First claim

The invention claimed is:

1. A process for desalinating water comprising the steps of:
passing a feed stream of saline solution in a first desalination step through a reverse osmosis membrane desalination plant comprising at least one reverse osmosis desalination unit to form a first product water stream having a reduced salt concentration relative to that of the feed stream of saline solution and a first byproduct stream having an increased salt concentration relative to that of the feed stream of saline solution,
wherein the first byproduct stream is passed in a second desalination step through a first suspension crystallization unit to form a second product water stream having a reduced salt concentration relative to that of the first byproduct stream and a second byproduct stream having an increased salt concentration relative to that of the first byproduct stream,
wherein the second byproduct stream is passed in a third desalination step through a static crystallization unit to form a third product water stream having a reduced salt concentration relative to that of the second byproduct stream and a third byproduct stream having an increased salt concentration relative to that of the second byproduct stream, and
wherein the salt concentration of the first byproduct stream is between about 3 to about 7 weight %.

2. The process of claim 1 , wherein the first suspension crystallization unit is a multi-stage counter-current crystallization unit.

3. The process of claim 1 , wherein the third product water stream is fed into the first byproduct stream.

4. The process of claim 1 , wherein the first byproduct stream is crystallized in the first suspension crystallization unit at a temperature between about −1 to about −4° C.

5. The process of claim 1 , wherein the first byproduct stream is passed through a first heat exchanger thereby reducing its temperature prior to passing through the first suspension crystallization unit.

6. The process of claim 1 , wherein the temperature of the first byproduct stream is reduced prior to entering the first suspension crystallization unit.

7. The process of claim 6 , wherein the temperature of the first byproduct stream is reduced to a temperature between about 2 and about 20° C.

8. The process of claim 1 , wherein the salt concentration of the second byproduct stream is between about 8 and about 18 weight %.

9. The process of claim 1 , wherein the second byproduct stream is crystallized in the static crystallization unit at a temperature between about −4 to about −13° C.

10. The process of claim 1 , wherein the second byproduct stream is passed through a second heat exchanger thereby reducing its temperature prior to passing through the static crystallization unit.

11. The process of claim 10 , wherein the temperature of the second byproduct stream is reduced to a temperature between about 2 to about 20° C.

12. An apparatus for carrying out a process for desalinating water, the apparatus comprising:
a reverse osmosis membrane desalination plant comprising at least one reverse osmosis desalination unit having an inlet for a feed stream of saline solution, an outlet for a first product water stream, an outlet for a first byproduct stream, wherein the outlet for a first byproduct stream is in fluid communication with an inlet of a first suspension crystallization unit having an outlet for a second product water stream, and an outlet for a second byproduct stream,
the apparatus additionally comprising a static crystallization unit having an inlet in fluid communication with the outlet for the second byproduct stream of the first suspension crystallization unit and an outlet for a third product water stream and an outlet for a third byproduct stream.

13. The apparatus of claim 12 , wherein the first suspension crystallization unit is a multi-stage counter-current crystallization unit.

14. The apparatus of claim 12 , wherein, in use, the feed stream of saline solution in a first desalination step is passed through the reverse osmosis membrane desalination plant to form the first product water stream having a reduced salt concentration relative to that of the feed stream of saline solution and the first byproduct stream having an increased salt concentration relative to that of the feed stream of saline solution,
wherein, in use, the first byproduct stream is passed in a second desalination step through the first suspension crystallization unit to form the second product water stream having a reduced salt concentration relative to that of the first byproduct stream and the second byproduct stream having an increased salt concentration relative to that of the first byproduct stream.

15. The apparatus of claim 12 , further comprising a second heat exchanger installed in line between the outlet for a second byproduct stream and the inlet of the static crystallization unit and wherein the second heat exchanger has an inlet and an outlet, wherein the inlet of the second heat exchanger is in fluid communication with the outlet for a second byproduct stream and the outlet of the second heat exchanger is in fluid communication with the inlet of the static crystallization unit.

16. The apparatus of claim 12 , wherein the outlet for a third product water stream is in fluid communication with the first byproduct stream.

17. The apparatus of claim 12 , additionally comprising a first heat exchanger having an inlet and an outlet, wherein the inlet of the first heat exchanger is in fluid communication with the outlet for a first byproduct stream and the outlet of the first heat exchanger is in fluid communication with the inlet of the first suspension crystallization unit.

18. A method for the reduction of the volume of the first byproduct stream of a reverse osmosis membrane desalination plant, or in a device or plant or process for producing desalinated water, for salt production, for co-production of power and desalinated water, or for air conditioning, the method comprising the steps of:
(I) providing the apparatus of claim 12 ,
(II) introducing a feed stream of saline solution to the inlet of the desalination unit of the apparatus provided in step (I).

19. The method of claim 18 , wherein steps (I) and (II) are performed at an in-land reverse osmosis membrane desalination plant.

Assignees

• Sulzer Chemtech Ag

Inventors

• Dette Severine
• Ahmad Mansour M M
• Stepanski Manfred

Classifications

• C02F2103/08

  Seawater, e.g. for desalination · CPC title

• B01D61/08 Primary

  Apparatus therefor · CPC title

• C02F2209/02

  Temperature · CPC title

• C02F2209/05

  Conductivity or salinity · CPC title

• Y02W10/37

  using solar energy · CPC title