IP Library › Granted Patent US 11,473,817
Granted Patent B2
US 11,473,817 · App. 16/589,578 · Granted Oct 18, 2022

Method to change fluid temperature using a thermally driven control unit

Inventors: Gong Zhou (Panama City, FL); Aly H. Shaaban (Panama City, FL)
Assignee: Applied Research Associates, Inc.
F25B15/02F25B27/02Y02A30/27Y02A30/274Y02B30/62
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Quick Facts
Patent No.
US 11,473,817
App. No.
16/589,578
Granted
Oct 18, 2022
Kind
B2
Abstract

Systems and methods are provided for changing the temperature of an environment using a thermally driven system. At least one solute and a solvent are selected such that the mixture of each solute and the solvent produce a negative enthalpy change for heating and a positive enthalpy change for cooling. In some embodiments, a plurality of pumps move the solute and the solvent, and a mixture thereof, among the various components of the present invention. A liquid loop may be coupled with a mixing heat exchanger and an air handler to provide a warm or cool supply air. Further, a process for cooling or heating air using enthalpy change of a solution associated with the dissolution of a solute in a solvent at relatively constant atmospheric pressure, and separation of the solute from the solvent for re-use in the process is disclosed.

Claims (61)

1. A method for changing a temperature of a fluid using a thermally-driven system comprising a mixing heat exchanger, an evaporator column, a condenser, a solute, and a solvent, the method comprising the steps of:

mixing the solute and the solvent to form a binary mixture in the mixing heat exchanger to generate an enthalpy change of solution within the mixing heat exchanger,

wherein the enthalpy change of solution from the mixing of the solute and the solvent within the mixing heat exchanger changes the temperature of the fluid;

after mixing the solute and solvent, separating the solute and the solvent by heating the binary mixture in the evaporator column to vaporize the solute,

wherein a boiling point of the solute is lower than a boiling point of the solvent;

after evaporating the binary mixture, condensing the solute into a liquid state in the condenser; and

after condensing the solute into a liquid state, supplying the solute and the solvent to the mixing heat exchanger,

wherein the solute and the solvent are supplied to the mixing heat exchanger in a liquid state.

2. The method of claim 1 ,

wherein the solute is a first solute and the thermally-driven system further comprises a second solute,

wherein the boiling point of the second solute is lower than the boiling point of the solvent,

wherein the first solute produces an endothermic reaction when mixed with the solvent thereby cooling the fluid,

wherein the second solute produces an exothermic reaction when mixed with the solvent thereby heating the fluid.

3. The method of claim 2 , wherein the condenser is a first condenser that condenses the first solute and the thermally-driven system further comprises:

a second condenser that condenses the second solute;

a plurality of control valves,

wherein a first control valve of the plurality of control valves directs the first solute to the first condenser,

wherein a second control valve of the plurality of control valves directs the second solute to the second condenser;

a plurality of pumps,

wherein a first pump of the plurality of pumps is associated with the first condenser,

wherein a second pump of the plurality of pumps is associated with the second condenser.

4. The method of claim 1 , wherein the fluid is a working fluid within an air handler.

5. The method of claim 4 , wherein the condenser is housed within the air handler to supplement heating of air within the air handler.

6. The method of claim 1 , wherein the binary mixture is heated in the evaporator column using waste heat.

7. The method of claim 1 ,

wherein the thermally-driven system further comprises a liquid loop,

wherein the liquid loop is supported within the mixing heat exchanger, and

wherein the fluid is cycled through the liquid loop.

8. The method of claim 1 , wherein the solute and solvent are selected so that the respective boiling point of the solute is at least 10° C. lower than the boiling point of the solvent.

9. A method for cooling a fluid using a thermally-driven system comprising a mixing heat exchanger, an evaporator column, a condenser, a solute, and a solvent, the method comprising the steps of:

mixing the solute and the solvent to form a binary mixture in the mixing heat exchanger to create a positive enthalpy change of solution,

wherein the enthalpy change of solution from the mixing of the solute and the solvent cools the fluid;

after mixing the solute and solvent, separating the solute and the solvent by heating the binary mixture in the evaporator column to vaporize the solute,

wherein the solute and the solvent are selected so that a boiling point of the solute is lower than a boiling point of the solvent;

after evaporating the binary mixture, condensing the solute into a liquid state in the condenser; and

after condensing the solute into a liquid state, supplying the solute and the solvent to the mixing heat exchanger,

wherein the solute and the solvent are supplied to the mixing heat exchanger in a liquid state.

10. The method of claim 9 , wherein the fluid is a working fluid within an air handler.

11. The method of claim 10 , wherein the condenser is housed within the air handler to supplement heating of air within the air handler.

12. The method of claim 9 , wherein the binary mixture is heated in the evaporator column using waste heat.

13. The method of claim 9 ,

wherein the thermally driven system further comprises a liquid loop,

wherein the liquid loop is supported within the mixing heat exchanger, and

wherein the fluid is cycled through the liquid loop.

14. The method of claim 9 , wherein the solute and solvent are selected so that the respective boiling point of the solute is at least 10° C. lower than the boiling point of the solvent.

15. A method for heating a fluid using a thermally-driven system comprising a mixing heat exchanger, an evaporator column, a condenser, a solute, and a solvent, the method comprising the steps of:

mixing the solute and the solvent to form a binary mixture in the mixing heat exchanger to create a negative enthalpy change of solution,

wherein the enthalpy change of solution from the mixing of the solute and the solvent heats the fluid;

after mixing the solute and solvent, separating the solute and the solvent by heating the binary mixture in the evaporator column to vaporize the solute,

wherein the solute and the solvent are selected so that a boiling point of the solute is lower than a boiling point of the solvent;

after evaporating the binary mixture, condensing the solute into a liquid state in the condenser; and

after condensing the solute into a liquid state, supplying the solute and the solvent to the mixing heat exchanger,

wherein the solute and the solvent are supplied to the mixing heat exchanger in a liquid state.

16. The method of claim 15 , wherein the fluid is a working fluid within an air handler.

17. The method of claim 16 , wherein the condenser is housed within the air handler to supplement heating of air within the air handler.

18. The method of claim 15 , wherein the binary mixture is heated in the evaporator column using waste heat.

19. The method of claim 15 ,

wherein the thermally-driven system further comprises a liquid loop,

wherein the liquid loop is supported within the mixing heat exchanger, and

wherein the fluid is cycled through the liquid loop.

20. The method of claim 15 , wherein the solute and solvent are selected so that the respective boiling point of the solute is at least 10° C. lower than the boiling point of the solvent.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 1, 2019
From: ZHOU, GONG; SHAABAN, ALY H.
To: APPLIED RESEARCH ASSOCIATES, INC.
Reel/Frame 050585/0824 →
Continuity (3)
Division 14811502 · Jul 28, 2015
Provisional Application 62030120 · Jul 29, 2014
Related Publication 20200033031A1 · Jan 30, 2020
Cited By (1)
US 12,207,650