Method and device for heat transfer

• US 10,443,950 B2
• Filed: 02/20/2015
• Issued: 10/15/2019
• Est. Priority Date: 02/25/2014
• Status: Active Grant

• Current Assignee: Alexandr Mikhailovich Derevyagin
• Original Assignee: Alexandr Mikhailovich Derevyagin
• Inventors: Derevyagin, Alexandr Mikhailovich
• Primary Examiner(s): Trpisovsky, Joseph F
• Application Number:
  US15/120,986
• Publication Number:
  US 20160363382A1
• Time in Patent Office: 1,698 Days
• Field of Search: 62119
• CPC Class Codes: F28D 15/025 having non-capillary condensate return means
• CPC Class Codes: F28D 15/0266 with separate evaporating and condensing chambers connected by at least one conduit; Loop-type heat pipes; with multiple or common evaporating or condensing chambers F28D15/043 takes precedence
• CPC Class Codes: F28F 13/06 by affecting the pattern of flow of the heat-exchange media F28F13/003 takes precedence; static flow control means in header boxes F28F9/026
• CPC Class Codes: F28F 2250/08 Fluid driving means, e.g. pumps, fans

Abstract

A method for transferring heat includes: heating an evaporator by a thermal energy source; providing a flow of a mixture of gaseous phases of a first and a second fluid over a steam line into a condenser; providing a flow of the condensed mixture over a liquid line into an accumulation tank; and providing a flow of the condensed mixture from the accumulation tank to the evaporator tank through non-return valves mounted on a return line. The method ensures transferring of a large quantity of thermal energy from a source to a receiver over considerable distances without application of porous capillary materials and additional processes for forced pumping of condensed fluid, regardless of the position of the source and the receiver in the gravity field.

Claims

1. A method for transferring heat, comprising:

heating by a thermal energy source at least one evaporator tank filled with at least two different fluids, where a first fluid is in a gaseous phase and a second fluid is in a liquid phase;

causing by said heating an increase in pressure in the at least one evaporator tank and a transition of the liquid phase of the second fluid into a gaseous phase of the second fluid, which is mixed with the gaseous phase of the first fluid;

under the increased pressure in the at least one evaporator tank, providing a flow of the mixture of the gaseous phases of the first and the second fluid over at least one steam line into at least one condenser, where the gaseous phase of the second fluid is condensed with release of condensation heat to a thermal energy receiver and formation of a liquid phase of the second fluid;

under the increased pressure in the at least one evaporator tank, providing a flow of the condensed liquid phase of the second fluid mixed with the gaseous phase of the first fluid over at least one liquid line into at least one accumulation tank until pressure in the at least one evaporator tank exceeds pressure in the at least one accumulation tank;

once the entire second fluid has transited from the liquid phase to the gaseous phase in the at least one evaporator tank, while condensation of the gaseous phase of the second fluid in the at least one condenser is continuing, reducing pressure in the at least one evaporator tank to a pressure value lower than that in the at least one accumulation tank, thereby ensuring a flow of the condensed liquid phase of the second fluid and the gaseous phase of the first fluid from the at least one accumulation tank to the at least one evaporator tank through at least one non-return valve mounted on at least one return line,

wherein a separator is further provided on the at least one return line to separate the mixture of the gaseous phase of the first fluid medium and the condensed liquid phase of the second fluid leaving the at least one accumulation tank into a flow of the gaseous phase of the first fluid and a flow of the liquid phase of the second fluid and to provide a delay between the arrival time of the gaseous phase of the first fluid and the arrival time of the liquid phase of the second fluid in the at least one evaporator tank, wherein the gaseous phase of the first fluid arrives first, and then the liquid phase of the second fluid arrives.

2. A method according to claim 1, wherein the first fluid is selected from the group consisting of air, nitrogen, helium, hydrogen, carbon dioxide.

3. A method according to claim 1, wherein the second fluid is a refrigerant, alcohols, acetone, water, or mixtures thereof.

4. A method according to claim 1, wherein the at least one steam line has a length from 0.01 m to over 1 km.

5. A method according to claim 1, wherein pressure in the at least one evaporator tank at transition of the liquid phase of the second fluid into a gaseous phase exceeds pressure in the at least one accumulation tank by 5 to 10 atmospheres.

6. A method according to claim 1, wherein the total hydraulic resistance of the at least one steam line, at least one condenser and at least one liquid line is greater than the hydraulic resistance of the at least one return line.

7. A method according to claim 1, wherein at least one non-return valve is mounted on the at least one steam line to prevent a reverse flow of the condensed liquid phase of the second fluid mixed with the gaseous phase of the first fluid from the at least one accumulation tank to the at least one evaporator tank.

8. A method according to claim 7, wherein the at least one non-return valve is mounted on the at least one liquid line to prevent a reverse flow of the condensed liquid phase of the second fluid mixed with the gaseous phase of the first fluid from the at least one accumulation tank to the at least one or more condenser.

9. A method according to claim 1, wherein the at least one steam line, the at least one condenser and the at least one liquid line form an integral pipeline.

10. A device for transferring heat, comprising:

at least one evaporator tank filled with at least two different fluids, where a first fluid is in a gaseous phase and a second fluid is in a liquid phase;

at least one condenser adapted to condense the gaseous phase of the second fluid with release of condensation heat to a thermal energy receiver;

at least one accumulation tank adapted to accumulate the condensed liquid phase of the second fluid and the gaseous phase of the first fluid;

at least one steam line connecting the at least one evaporator tank and the at least one condenser, and providing a flow over the at least one steam line of a mixture of the gaseous phases of the first and second fluids into the at least one condenser under increased pressure caused by heating the at least one evaporator tank until pressure in the at least one evaporator tank exceeds that in the at least one accumulation tank;

at least one liquid line connected with the at least one condenser and providing a flow of the condensed liquid phase of the second fluid mixed with the gaseous phase of the first fluid into the at least one accumulation tank until pressure in the at least one evaporator tank exceeds that in the at least one accumulation tank;

at least one return line having at least one non-return valve mounted thereon to prevent the flow of the fluids from the at least one evaporator tank into the at least one accumulation tank over the at least one return line, wherein the at least one return line provides a flow of the condensed liquid phase of the second fluid and the gaseous phase of the first fluid from the at least one accumulation tank into the at least one evaporator tank once the entire second fluid in the liquid phase in the at least one evaporator tank has transited into a gaseous phase, while condensation of the gaseous phase of the second fluid in the at least one condenser is continuing, and pressure in the at least one evaporator tank is less than that in the at least one accumulation tank,

wherein a separator is further provided on the at least one return line to separate the mixture of the gaseous phase of the first fluid and the condensed liquid phase of the second fluid leaving the at least one accumulation tank into a flow of the gaseous phase of the first fluid and a flow of the liquid phase of the second fluid and to provide a delay between the arrival time of the gaseous phase of the first fluid and the arrival time of the liquid phase of the second fluid in the at least one evaporator tank, wherein the gaseous phase of the first fluid arrives first, and then the liquid phase of the second fluid arrives.

11. A device according to claim 10, wherein the first fluid is selected from the group consisting of air, nitrogen, helium, hydrogen, carbon dioxide.

12. A device according to claim 10, wherein the second fluid is a refrigerant, alcohols, acetone, water, or mixtures thereof.

13. A device according to claim 10, wherein the at least one steam line has a length from 0.01 m to over 1 km.

14. A device according to claim 10, wherein pressure in the at least one evaporator tank at transition of the liquid phase of the second fluid into a gaseous phase is greater than pressure in the at least one accumulation tank by 5 to 10.

15. A device according to claim 10, wherein the total hydraulic resistance of the at least one steam line, the at least one condenser and the at least one liquid line is greater than the hydraulic resistance of the at least one return line.

16. A device according to claim 10, wherein at least one non-return valve is further mounted on the at least one steam line to prevent a reverse flow of the condensed liquid phase of the second fluid mixed with the gaseous phase of the first fluid from the at least one accumulation tank to the at least one evaporator tank over the at least one liquid line through the at least one condenser and the at least one steam line.

17. A device according to claim 16, wherein at least one non-return valve is further mounted on the at least one liquid line to prevent a reverse flow of the condensed liquid phase of the second fluid mixed with gaseous phase of the first fluid from the at least one accumulation tank to the at least one condenser.

18. A device according to claim 10, wherein the at least one accumulation tank is mounted above the at least one evaporator tank.

19. A device according to claim 10, wherein the at least one accumulation tank has an inlet for entrance of the mixture of the gaseous phase of the first fluid and the liquid phase of the second fluid, said inlet being disposed in the upper part of the at least one accumulation tank.

20. A device according to claim 10, wherein the at least one accumulation tank has an outlet in the lower part of the at least one accumulation tank for exit of the mixture of the condensed liquid phase of the second fluid and the gaseous phase of the first fluid from the at least one accumulation tank to the at least one evaporator tank.

21. A device according to claim 10, wherein the at least one steam line, the at least one condenser and the at least one liquid line form an integral pipeline.