Device for heat transport with two-phase fluid

• US 10,234,213 B2
• Filed: 02/14/2014
• Issued: 03/19/2019
• Est. Priority Date: 02/14/2013
• Status: Active Grant

• Current Assignee: Euro Heat Pipes SA
• Original Assignee: Euro Heat Pipes SA
• Inventors: Dupont, Vincent
• Primary Examiner(s): Duong, Tho V
• Application Number:
  US14/767,887
• Publication Number:
  US 20150369541A1
• Time in Patent Office: 1,859 Days
• 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: F28D 15/043 forming loops, e.g. capillary pumped loops
• CPC Class Codes: F28D 15/06 Control arrangements therefor
• CPC Class Codes: F28F 2265/12 for preventing overpressure

Abstract

A heat transport device with a diphasic working fluid contained in a general closed circuit, includes an evaporator having a microporous body suitable for providing capillary pumping of liquid phase fluid; a condenser; a tank having an inner space, with a liquid portion and a gas portion; and an inlet/outlet arranged at the liquid portion, wherein the volume of the liquid portion can vary between a minimum volume and a maximum volume. The gas portion of the tank contains the vapor phase of the working fluid, at a first partial pressure, and a noncondensable auxiliary gas at a second partial pressure, wherein the second partial pressure is greater than the first partial pressure, at least when the liquid portion is at the minimum volume thereof.

Claims

1. A device for heat transfer, suited for extracting heat from a hot source and for returning this heat to a cold source via a two-phase working fluid contained in a general closed circuit, comprising:

at least one evaporator, having an inlet and an outlet,

at least one condenser, separate from and away from the evaporator,

a tank with an internal volume , the internal volume including a liquid portion and a gas portion, and at least one inlet/outlet orifice laid out near the liquid portion, where the liquid portion has a volume that can vary between a minimum volume and a maximum volume,

a first connection circuit for the working fluid in vapor phase, connecting the outlet of the evaporator to an inlet of the condenser;

a second connection circuit, for the working fluid in liquid phase, connecting an outlet from the condenser to the tank and to the inlet of the evaporator;

wherein the gas portion from the tank includes the vapor phase of the working fluid with a first partial pressure and a non-condensable auxiliary gas with a second partial pressure, where the second partial pressure is set to obtain a total pressure greater than or equal to a preset minimum operating pressure when the liquid portion in the entire general closed circuit is at the minimum volume, the device having no sensor and no active control, and hence operates in a purely passive operating mode, said device being configured to operate in a temperature range from -50°

C. to +50°

C., wherein;

the internal volume of the tank is fixed and predefined during design for a given application; and

the second partial pressure is at least several times greater than the first partial pressure when the liquid portion is at the minimum volume such that the minimum operating pressure is high enough to allow an instantaneous startup under a significant thermal load without preparation.

2. The device according to claim 1, wherein the non-condensable auxiliary gas is helium.

3. The device according to claim 1, wherein the working fluid is methanol.

4. The device according to claim 1, wherein the total volume of the tank is between 1.3 and 2.5 times said maximum volume of the liquid portion.

5. The device according to claim 1, mainly subject to terrestrial gravity, wherein the inlet/outlet orifice is arranged in an area of a low point of the tank.

6. The device according to claim 1, mainly subject to microgravity, wherein the tank comprises a porous mass laid out at least in an area of the inlet/outlet orifice.

7. The device according to claim 1, wherein the evaporator includes a micro-porous mass adapted for assuring capillary pumping of the liquid phase working fluid.

8. The device according to claim 1, subject mainly to gravity, wherein the evaporator is placed below the condenser and the tank, whereby gravity is used for moving the liquid phase working fluid towards the evaporator.

9. The device according to claim 1, wherein an anti-backflow valve is laid out at the inlet of the evaporator.