Desalination method and system using compressed air energy systems

• US 20070295673A1
• Filed: 03/30/2007
• Published: 12/27/2007
• Est. Priority Date: 04/05/2006
• Status: Active Grant

• Current Assignee: Ben Enis, Paul Lieberman
• Original Assignee: Ben Enis, Paul Lieberman
• Inventors: Lieberman, Paul, Enis, Ben
• Granted Patent: US 8,863,547 B2
• Time in Patent Office: Days
• US Class Current: 210/766
• CPC Class Codes: C02F 1/10 by direct contact with a particulate solid or with a fluid, as a heat transfer medium
• CPC Class Codes: C02F 1/12 Spray evaporation
• CPC Class Codes: C02F 1/22 by freezing
• CPC Class Codes: C02F 2103/08 Seawater, e.g. for desalination
• CPC Class Codes: C02F 2209/02 Temperature
• CPC Class Codes: C02F 2209/03 Pressure
• CPC Class Codes: C02F 2303/16 Regeneration of sorbents, filters
• CPC Class Codes: C02F 2303/26 Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles
• CPC Class Codes: Y02A 20/124 Water desalination
• CPC Class Codes: Y02W 10/37 using solar energy

Abstract

The invention relates to a desalination method and system that uses freeze crystallization technology that incorporates the use of compressed air energy as the source for freezing temperatures. When compressed air is released by a turbo expander, chilled air is produced as a by-product, wherein the chilled air is introduced into a crystallization chamber. Also injected into the chamber is a spray cloud of seawater droplets, which has been pre-chilled by heat exchange with the cold chamber walls, and which is then circulated and exposed to the chilled air in the chamber. The sizes of the droplets can vary, but are preferably predetermined, along with the relative temperatures, flows and speeds of the spray and chilled air, such that when the droplets are circulated within the chilled air, and settle at the bottom of the chamber, they are deposited at slightly above the eutectic temperature. This way, the ice/snow mass that forms at the bottom of the chamber will consist of frozen ice crystals, and a residue of salt water brine, which can runoff from the mass, either from the sides, or through any voids or channels that may form within the mass.

Claims

1. A system for desalinating seawater comprising:

a compressor for compressing air;

an expander for expanding compressed air to co-generate chilled air;

a chamber, with at least one nozzle through which the seawater can be sprayed into the chamber, and into which the chilled air from the expander can be introduced, wherein the exposure of the seawater to the chilled air enables ice particles consisting of pure water to be formed in the chamber;

a device that helps remove the ice particles from the chamber, thereby helping to separate the pure water in the ice particles from the impurities in the seawater.

2. The system of claim 1, wherein the system comprises at least one of the following:

1) a storage tank is provided to enable the compressed air to be stored therein, and wherein the expander is adapted to release and expand the compressed air inside said tank, to produce chilled air;

2) an electrical generator is provided which is adapted to produce electricity as the compressed air is being released by the expander, wherein the chilled air is produced as a by-product of producing electricity;

3) a surge tank, wherein, as the compressed air is expanded by the expander, the energy produced thereby is used to drive a second compressor that produces additional compressed air energy that can be introduced into the surge tank;

4) at least one heat exchanger for helping to reduce the temperature of the compressed air before it is expanded by the expander;

or

5) at least one common shaft between the compressor and expander which allows them to operate in association with each other.

3. The system of claim 1, wherein the temperature of the chilled air introduced into the chamber is below the eutectic temperature for the seawater, and wherein the ice particles are allowed to deposit at the bottom of the chamber in the form of a mass, wherein the temperature of the mass at the bottom of the chamber is above the eutectic temperature for the seawater.

4. The system of claim 3, wherein the temperature of the chilled air is between minus 135 degrees F. and 175 degrees F., and the temperature of the mass of ice particles is above minus 6.2 degrees F., such that a liquid brine consisting of the impurities in the seawater can runoff from the mass.

5. The system of claim 1, wherein the system comprises at least one of the following:

1) the system is adapted such that the seawater can be sprayed down into the chamber from above, and the chilled air can be introduced such that it flows upward inside the chamber;

2) the system is adapted such that the seawater can be sprayed down into the chamber from above, and the chilled air can be introduced such that it flows downward inside the chamber in the same direction as the seawater.

6. The system of claim 1, wherein chilled air is introduced at a temperature between minus 135 degrees F. and 175 degrees F.

7. The system of claim 1, wherein said at least one nozzle is adapted and configured to produce a centrally focused spray of seawater that tends to keep the droplets that are formed by the spray away from the outer walls of the chamber, and toward the center of the chamber, wherein as the ice particles fall, they tend to land near the center of the chamber, to form an ice mass which allows the seawater to flow down the sides of the ice mass, without being captured within the ice mass formation as it coalesces and freezes.

8. The system of claim 1, wherein the walls of the chamber are adapted with tubes or passages which allow the seawater to be circulated therein, to help regulate the temperature of the walls within the chamber.

9. The system of claim 8, wherein the seawater is passed through the tubes or passages in the chamber walls to help warm up the chamber walls, and in turn, the cold temperature inside the chamber can help pre-chill the seawater as it circulates before being sprayed into the chamber, wherein the seawater that is introduced into the chamber is pre-chilled to less than 40 degrees F.

10. The system of claim 1, wherein the walls of the chamber are adapted with tubes or passages which allow heated air from the compressor to be used to regulate the temperature of the walls within the chamber.

11. The system of claim 10, wherein the heated air is passed through the tubes or passages in the chamber walls to help warm up the chamber walls, wherein the cold temperatures inside the chamber can help pre-chill the heated air as it circulates to the expander.

12. The system of claim 1, wherein the location where the chilled air is introduced into the chamber is above the height that is expected to be reached by an ice mass formation that is formed within the chamber when the ice particles coalesce and freeze together at the bottom of the chamber.

13. The system of claim 1, wherein a heater is provided in connection with the walls of the chamber near where the ice particles accumulate, wherein the walls of the chamber can be heated to prevent the ice particles from freezing on the walls, and/or to allow any ice mass that is produced as the ice particles coalesce and freeze within the chamber to be easily removed.

14. A method of desalinating seawater comprising:

compressing air to produce compressed air energy;

releasing the compressed air with an expander to co-generate chilled air;

introducing the chilled air into a chamber;

spraying the seawater in the form of droplets into the chamber;

exposing the seawater droplets to the chilled air within the chamber, thereby forming ice particles consisting of pure water within the droplets; and

forming a mass with the ice particles within the chamber, thereby helping to separate the pure water in the ice particles from the impurities in the seawater.

15. The method of claim 14, wherein the method comprises at least one of the following:

1) storing the compressed air energy in a storage tank before releasing the compressed air energy;

2) co-producing electricity using a generator, as the compressed air is being released by the expander, wherein the chilled air is produced as a by-product of producing the electricity;

3) using the compressed air energy to drive a supplemental compressor that produces additional compressed air energy that can be introduced into a surge tank;

4) using at least one heat exchanger to reduce the temperature of the compressed air before it is expanded by the expander;

or

5) using at least one common shaft between the compressor and expander to allow them to operate in association with each other.

16. The method of claim 14, wherein introducing the chilled air comprises introducing chilled air at below the eutectic temperature for the seawater, and wherein forming the mass of ice particles comprises keeping the temperature of the mass at the bottom of the chamber above the eutectic temperature for the seawater.

17. The method of claim 16, wherein the temperature of the chilled air is between minus 135 degrees F. and 175 degrees F., and the temperature of the mass of ice particles is above minus 6.2 degrees F., such that a liquid brine consisting of the impurities in the seawater can runoff from the mass.

18. The method of claim 14, comprising at least one of the following steps:

1) spraying the seawater down into the chamber from above, and introducing the chilled air such that it flows upward inside the chamber;

2) spraying the seawater down into the chamber from above, and introducing the chilled air such that it flows downward in the same direction as the seawater being sprayed into the chamber.

19. The method of claim 14, wherein said at least one nozzle is adapted and configured to produce a centrally focused spray of the seawater that tends to keep the droplets that are formed by the spray away from the outer walls of the chamber, and toward the center of the chamber, wherein as the ice particles fall, they tend to land near the center of the chamber, to form an ice mass which allows the seawater to flow down the sides of the ice block, without being captured within the ice mass formation as it coalesces and freezes.

20. The method of claim 14, wherein the method comprises circulating the seawater through at least one tube or passage within the chamber walls to help warm up the chamber walls, and in turn, cause the cold temperature inside the chamber to help pre-chill the seawater before being sprayed into the chamber, wherein the seawater that is introduced into the chamber is pre-chilled to less than 40 degrees F.

21. The method of claim 14, wherein the method comprises circulating heated air from the compressor through at least one tube or passage in the chamber walls to help warm up the chamber walls, wherein the cold temperatures inside the chamber can help pre-chill the heated air as it circulates to the expander.