IP Library Granted Patent US 11,383,179
Granted Patent B2
US 11,383,179 · App. 16/985,020 · Granted Jul 12, 2022

Method and apparatus for desalinating water

Inventors: Bahman Abbasi (Bend, OR); Xiang Zhang (Bend, OR); Mohammed Abbas Elhashimi Khalifa (Corvallis, OR); Deepak Sharma (Corvallis, OR)
Assignee: Oregon State University
B01D1/30B01D1/0035B01D1/14B01D1/16B01D5/006B01D45/16C02F1/043C02F1/10C02F1/14F04F5/18C02F2101/10C02F2103/08C02F2303/10
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Quick Facts
Patent No.
US 11,383,179
App. No.
16/985,020
Granted
Jul 12, 2022
Kind
B2
Abstract

This disclosure concerns a system and a method for removing dissolved solids from liquids. Specific implementations concern desalinating water. The system may comprise a blower, such as a thermal fan/compressor, configured to atomize a solid-bearing liquid to produce a hot, humid gas containing dissolved solids; a gas-solid separator configured to receive hot, humid gas containing entrained dissolved solids from the blower to separate the solids from the humid gas and to transmit the humid gas with solids removed through an exit port; a heater configured to heat the hot, humid gas received from the exit port of the gas-solid separator; and a condenser configured to receive heated humid gas from the heater and to condense solids-free liquid therefrom. The thermal fan/compressor may comprise a plurality of nozzles with outlets positioned adjacent atomization apertures across which a solid-bearing liquid flows and through which gas exiting the nozzles passes.

Claims (48)

1. A desalination system, comprising:

a blower configured to atomize a solid-bearing liquid to produce a hot, humid gas containing dissolved solids, the blower comprising a thermal fan/compressor comprising an inlet face having one or more inlet ports, a plurality of nozzles for receiving a gas from the one or more inlet ports, each nozzle comprising a heat exchange wall, an inlet orifice having a first size, and an outlet orifice having a second size smaller than the inlet orifice, an outlet face having a plurality of atomization apertures across which a solid-bearing liquid can flow and through which gas exiting the nozzles is directed, and a wall separating the inlet face from the outlet face and forming a condensation and heat exchange chamber in which the plurality of nozzles is disposed;

a gas-solid separator configured to receive hot, humid gas containing entrained solids from the blower to separate the solids from the humid gas and to transmit the humid gas with solids removed through an exit port;

a heater configured to heat the hot, humid gas received from the exit port of the gas-solid separator; and

a condenser configured to receive heated humid gas from the heater and to condense solids-free liquid therefrom.

2. The system according to claim 1 wherein the condenser and the heat exchange walls of the plurality of nozzles form a unitary structure.

3. The system according to claim 1 wherein the gas-solid separator is a cyclonic separator.

4. The system according to claim 3 , wherein:

substantially solids-free gas flows from the condenser to a first auxiliary heating element and then to the cyclonic separator to be recycled back to the thermal fan/compressor; or

substantially solids-free gas flows from the cyclonic separator to a second auxiliary heating element to be recycled back to the thermal fan/compressor.

5. The system according to claim 3 further comprising a solids collector in communication with the cyclonic separator and configured to receive solids rejected from the hot, humid gas by the cyclonic separator.

6. The system according to claim 5 wherein the solids collector functions as a heat recuperator and transmits heat from the rejected solids to a liquid flowing to the outlet face of the thermal fan/compressor.

7. The system according to claim 1 wherein the heater is a solar heater.

8. A desalination system, comprising:

a blower configured to atomize a solid-bearing liquid to produce a hot, humid gas containing dissolved solids, the blower comprising a thermal fan/compressor comprising an inlet face having one or more inlet ports, a plurality of nozzles for receiving a gas from the one or more inlet ports, each nozzle comprising a heat exchange wall, an inlet orifice having a first size, and an outlet orifice having a second size smaller than the inlet orifice, an outlet face having a plurality of atomization apertures across which a solid-bearing liquid can flow and through which gas exiting the nozzles is directed, and a wall separating the inlet face from the outlet face and forming a condensation and heat exchange chamber in which the plurality of nozzles is disposed;

a cyclonic gas-solid separator configured to receive hot, humid gas containing entrained solids from the blower to separate the solids from the humid gas and to transmit the humid gas with solids removed through an exit port;

a condenser configured to condense substantially solid-free liquid from the hot, humid gas leaving the gas-solid separator and to supply evaporation heat to the hot, humid gas from the blower;

a gas-liquid separator configured to receive the hot gas and to condense substantially solid-free liquid from the condenser to separate the liquid from the gas; and

a heater configured to supply heat to the heat exchange chamber of the blower.

9. The system according to claim 8 , wherein:

substantially solids-free gas flows from the condenser to an auxiliary heating element and then to the cyclonic separator to be recycled back to the thermal fan/compressor; or

substantially solids-free gas flows from the cyclonic separator to an auxiliary heating element to be recycled back to the thermal fan/compressor.

10. The system according to claim 8 wherein the heater is a solar heater.

11. The system according to claim 8 further comprising a solids collector in communication with the gas-solid separator and configured to receive solids rejected from the hot humid gas by the separator.

12. The system according to claim 8 further comprising a heat recuperator configured to remove heat from the solid-free liquid leaving the gas-liquid separator, and to transmit that heat to an incoming flow of solid-bearing liquid.

13. The system according to claim 12 wherein the gas-liquid separator is fluidly coupled to inlet orifices of the thermal fan/compressor nozzles.

14. The system according to claim 8 , further comprising a bleed stream to heat the solid-free liquid exiting the gas-liquid separator with bleed enthalpy from hot gas leaving a cyclonic separator.

15. A method for desalinating water, comprising:

providing a system according to claim 1 ; and

using the system to desalinate water.

16. The method according to claim 15 , comprising:

supplying a flow of slow-moving dry gas to the blower;

accelerating the dry gas in the blower;

directing the accelerated dry gas through a solid-bearing liquid, thereby atomizing the liquid and forming a hot, humid gas with entrained solids;

supplying the flow of hot, humid gas to the gas-solid separator wherein the entrained solids are separated from the hot, humid gas with entrained solids;

supplying the flow of hot, humid gas from the gas-solid separator to the heater to heat the hot, humid gas; and

supplying the flow of hot, humid gas from the heater to the condenser wherein the substantially solid-free liquid is removed from the gas by condensation.

17. The method according to claim 16 wherein the gas is substantially dry air when it enters the blower.

18. The method according to claim 16 wherein the solid-bearing liquid is saline water, and the substantially solid-free liquid is desalinated water.

19. A method for desalinating water, comprising:

supplying a flow of air to a blower;

the blower comprising a thermal fan/compressor comprising an inlet face having one or more inlet ports, a plurality of nozzles for receiving a gas from the one or more inlet ports, each nozzle comprising a heat exchange wall, an inlet orifice having a first size, and an outlet orifice having a second size smaller than the inlet orifice, an outlet face having a plurality of atomization apertures across which a solid-bearing liquid can flow and through which gas exiting the nozzles is directed, and a wall separating the inlet face from the outlet face and forming a condensation and heat exchange chamber in which the plurality of nozzles is disposed

accelerating the air in the blower;

directing the accelerated air through saline water, thereby atomizing the water and forming a hot, humid gas with entrained solids;

supplying the flow of hot, humid gas with entrained solids to a gas-solid separator, wherein the entrained solids are separated from the hot, humid gas to provide substantially solids-free water;

supplying the flow of hot, humid gas from the gas-solid separator to a condenser to condense substantially solid-free water from the gas; and

supplying the gas and substantially solid-free water mixture from the condenser to a gas-liquid separator to separate gas from the substantially solid free water.

20. The method according to claim 19 wherein the nozzles of the thermal fan/compressor are heated, thereby causing the dry gas to accelerate and flow out of the outlet orifices of the nozzles and through atomization apertures of the outlet face of the thermal fan/compressor, thereby atomizing the solid-bearing water and forming hot, humid gas with entrained solids.

Assignments (2)
CONFIRMATORY LICENSE Recorded Nov 3, 2020
From: OREGON STATE UNIVERSITY
To: UNITED STATES DEPARTMENT OF ENERGY
Reel/Frame 054283/0208 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 26, 2020
From: ABBASI, BAHMAN; ZHANG, XIANG; KHALIFA, MOHAMMED ABBAS ELHASHIMI; SHARMA, DEEPAK
To: OREGON STATE UNIVERSITY
Reel/Frame 054163/0374 →
Continuity (3)
Provisional Application 62968747 · Jan 31, 2020
Provisional Application 62882953 · Aug 5, 2019
Related Publication 20210039008A1 · Feb 11, 2021