Method for assisting thermally-induced changes

Patent metadata

Field	Value
Publication number	US-11198074-B2
Application number	US-201615577013-A
Country	US
Kind code	B2
Filing date	May 27, 2016
Priority date	May 27, 2015
Publication date	Dec 14, 2021
Grant date	Dec 14, 2021

Abstract

Disclosed herein is a method for assisting a thermally-induced change to a nano-sized solute or dispersed-phase in a liquid. The method comprises the step of passing gas bubbles through the liquid, the gas in the gas bubbles having a temperature higher than the bulk temperature of the liquid.

First claim

The invention claimed is:

1. A method for assisting a thermally-induced change to a nano-sized solute or dispersed-phase in a liquid, the method comprising the step of:
passing gas bubbles through the liquid, the gas in the gas bubbles having a temperature higher than the bulk temperature of the liquid and causing the formation of a transient hot surface layer in the liquid around the gas bubbles,
wherein the nano-sized solute or dispersed-phase undergoes a thermally-induced change during the passing of gas bubbles through the liquid,
wherein the thermally-induced change occurs through an interaction between the nano-sized solute or dispersed phase with the transient hot surface layer,
wherein the thermally-induced change is one or more of: (i) a thermally-induced chemical change of the nano-sized solute or dispersed phase, (ii) a thermally-induced chemical reaction of the nano-sized solute or dispersed phase, and (iii) a thermal decomposition of the nano-sized solute or dispersed phase,
wherein the liquid is water or an aqueous solution, the bubbles have a diameter of 0.1 mm to 7 mm, and the gas in the gas bubbles has a relative humidity of less than 50%.

2. The method according to claim 1 , wherein the bulk temperature of the liquid is less than the temperature which would cause the thermally-induced change to the nano-sized solute or dispersed-phase.

3. The method according to claim 1 , wherein the nano-sized solute or dispersed-phase has a diameter of less than 500 nm.

4. The method according to claim 3 , wherein the nano-sized solute or dispersed-phase has a diameter of 0.5 nm to 200 nm.

5. The method according to claim 1 , wherein the bubbles have a diameter of 1 mm to 3 mm.

6. The method according to claim 5 , wherein the bubbles have a diameter of approximately 2 mm.

7. The method according to claim 1 , wherein the nano-sized solute or dispersed-phase is selected from the group consisting of thermally decomposable inorganic solutes, thermally decomposable organic solutes, enzymes, antibiotics and hormones.

8. The method according to claim 7 , wherein the nano-sized solute or dispersed-phase is a thermally decomposable inorganic solute.

9. The method according to claim 8 , wherein the thermally decomposable inorganic solute is an ion of an inorganic salt.

10. The method according to claim 9 , wherein the ion is selected from the group consisting of acetates, persulfates, ammonium, bicarbonates, carbonates and peroxides.

11. The method according to claim 9 , wherein the inorganic salt is NH 4 HCO 3 or K 2 S 2 O 8 .

12. The method according to claim 7 , wherein the nano-sized solute or dispersed-phase is an enzyme.

13. The method according to claim 7 , wherein the nano-sized solute or dispersed-phase is an antibiotic.

14. The method according to claim 7 , wherein the nano-sized solute or dispersed-phase is a hormone.

15. The method according to claim 1 , wherein the liquid is an aqueous solution, and said aqueous solution comprises a bubble coalescence inhibitor.

16. The method according to claim 15 , wherein the bubble coalescence inhibitor is selected from the group consisting of NaCl, CaCl 2 , sucrose, emulsifiers and surfactants.

17. The method according to claim 16 , wherein the bubble coalescence inhibitor is sucrose.

18. The method according to claim 16 , wherein the bubble coalescence inhibitor is a surfactant or an emulsifier.

19. The method according to claim 1 , wherein the gas in the gas bubbles is selected from the group consisting of dry air, humidified air, carbon dioxide, nitrogen, helium, argon and oxygen.

20. The method according to claim 1 , wherein the gas in the gas bubbles has a temperature of less than 600° C.

21. The method according to claim 20 , wherein the gas in the gas bubbles has a temperature of less than 300° C.

22. The method according to claim 1 , wherein the nano-sized solute or dispersed-phase has a diameter of 0.1 nm to 250 nm.

23. The method according to claim 1 , wherein the gas in the gas bubbles has a relative humidity of less than 25%.

Assignees

• Newsouth Innovations Pty Ltd

Inventors

• Pashley Richard
• Xue Xinkai
• Fan Chao
• Ninham Barry
• Shahid Muhammad

Classifications

• B01D1/14

  with heated gases or vapours {or liquids} in contact with the liquid · CPC title

• B01D3/346 Primary

  the gas being used for removing vapours, e.g. transport gas · CPC title

• C02F1/10

  by direct contact with a particulate solid or with a fluid, as a heat transfer medium · CPC title

• C12M1/04

  with gas introduction means · CPC title

• C02F1/02

  by heating (methods of steam generation F22B; preheating boiler feed-water or accumulating preheated boiler feed-water F22D) · CPC title