THERMAL EXCHANGING DEVICE
A thermal exchanging device is provided to exchange heat with a hot heat source and a cold heat source. The thermal exchanging device includes a vacuum chamber, a working material capable of being excited magnetically, and a working fluid capable of undergoing a transition between two phase flows of liquid and vapor. The working fluid is provided in the chamber to communicate with the working material. When the working material is magnetically excited, the working fluid is configured to exchange heat with the cold heat source. Otherwise, the working fluid is configured to absorb heat from the hot heat source.
This Application claims priority from U.S. provisional application No. 61/245,441, filed on Sep. 24, 2009, the entirety of which is incorporated by reference herein.
BACKGROUND1. Field of the Invention
The present invention is in the technical field of a thermal exchanging device, more particularly to a magnetically driven thermal exchanging device utilizing a magneto-caloric material (MCM) to generate a two-phase flow of liquid and vapor by means of magnetization and demagnetization mechanism.
2. Description of the Related Art
A conventional thermal exchanging device that utilizes the magneto-calorific properties of certain materials, such as Gadolinium or certain alloys, has the particularity of heating up when a magnetic field is applied (magnetization process) and of cooling to a temperature lower than the initial temperature following the diminishing effect of the magnetic field (demagnetization process). For instance, when the magneto-calorific material (MCM) is magnetized, the magnetic moment of the MCM becomes aligned causing a rearrangement of the atoms to thereby generate heat from the MCM. On the other hand, when the MCM is demagnetized, the magnetic moment of the MCM becomes randomized causing a disorder of the atoms to thereby absorb heat from outside of the MCM.
As shown in
It is to be noted that the operating efficiency of the thermal exchanging device is primarily determined by the amount of heat transfer between the MCM and the fluid. Thus, in order to optimize the operating efficiency of the thermal exchanging device, two contributing factors are considered significant: MCM's surface area and fluid flow rate. As such, the optimization can be achieved either by dispensing a large amount of fluid through the surface of the MCM, or by increasing the surface area of the MCM. However, as the surface area of the MCM increases, the surface area of gaps or the pores of the MCM decreases, thereby limiting the amount of fluid to pass therethrough. As a result, a higher driving force is required to force the fluid through the MCM, which in turn requires a stronger pump to achieve this task. Consequently, the coefficient of performance (COP) of the thermal exchanging device is reduced.
SUMMARYThe present invention overcomes the aforementioned disadvantages by offering a magnetically driven thermal exchanging device that is simple in design while having an efficient and reliable performance.
A thermal exchanging device is provided to exchange heat with a heat source. The heat source has hot and cold sources. The thermal exchanging device includes a vacuum chamber, a working material capable of being excited magnetically, and a working fluid capable of undergoing a transition between two phase flows of liquid and vapor. The working fluid is provided in the chamber to communicate with the working material. When the working material is magnetically excited, the working fluid is configured to exchange heat with the cold heat source. Otherwise, the working fluid is configured to absorb heat from the hot heat source.
The invention can be more fully understood by reading the subsequent detailed description and examples with references made to the accompanying drawings, wherein:
Referring to
The magnetic-generating source 26 is selected from one of a permanent magnet, a Halbach magnet, and an electrical conductive coil magnetic set. In this preferred embodiment, the electrical conductive coil magnetic set is a superconductor coil, and the working material 22 is a porous magneto-caloric material made of gadolinium and the grain size of the porous magneto-caloric material which is between 50 to 150 micrometers. The porous magneto-caloric material is provided with more than one Curie temperature. When the working material 22 is near its Curie temperature, the magnetic state of the working material 22 will change between ferromagnetism and paramagnetism so as to cause a change of the magnetic entropy of the working material 22. Further, the porous magneto-caloric material is selected from one of a powder shape and a wire mesh shape. In this preferred embodiment, the magneto-caloric material is a bulk material with thin slits provided therethrough and/or has a plurality of stacked plates with gaps spaced therebetween. The working fluid 25 is characterized by having more than one boiling point temperature. In this preferred embodiment, the working fluid is water.
The working material 22 can be magnetically excited by the magnetic-generating source 26. When the working material 22 is magnetically excited, the working fluid 25 operates to exchange heat with the cold heat source Q2. Similarly, when the working material 22 is not magnetically excited, the working fluid 25 operates to absorb heat from the hot heat source Q1. The heating unit 24 is disposed on an outer surface of the chamber 21 and operable to exchange heat with the external heat source Q. The working material 22 is surrounded by the wick structure 23 in the chamber 21 so as to facilitate flowing of the working fluid 25 and the working material 22 in the chamber 21 by means of, for example, capillary action. The wick structure 23 also has a portion 231 in thermal contact with the heating unit 24. Additionally, as shown in
Since the working fluid 25 is encapsulated in the vacuum chamber 21, a portion of the working fluid 25 vaporizes to a higher vapor stream so as to fill up a portion of the empty space of the chamber 21. The vaporization process will stop when the vapor pressure reaches to the working fluid's 25 saturation point. At this moment, the vapor and liquid phases are in equilibrium with each other until the temperature of the working fluid 25 changes again. Contrarily, when the temperature of the working material 22 decreases to result in cooling the working fluid 25, the working fluid 25 condenses to a lower vapor pressure stream.
Referring to
Referring to
Reference is now made to
Referring to
The present invention operates in a fundamentally the same manner as the refrigeration. It should be noted that, in other embodiments of the present invention, the thermal exchanging device can be used in conjunction in other applications, such as in cooling or heating devices for operating as a power-conversion device. In addition, it is to be noted that the chamber 21, 31, 41, or 51 is kept airtight in a vacuum manner so that the internal pressure of the chamber 21, 31, 41, or 51 is lower than the atmosphere (atm) pressure, which results in decreasing the boiling point of the working fluid 25, 35, 45, or 55 inside the chamber accordingly. As a consequence of this phenomenon, the working fluid 25, 35, 45, or 55 can be more convenient to undergo the two-phase transition.
As described from the foregoing, the advanced design of the thermal exchanging device according to the present invention provides a high efficiency, high speed and low cost solution with operational advantages explained below:
1. The convection coefficient (h) for heat transfer using a two-phase flow of liquid and vapor is about 5˜50 times higher than that of a pure liquid. Also, the heat absorption for vaporizing one gram of water is 574 Calorie (2400 Joule), whereas the heat absorption for raising one centigrade degree of one gram of water is one Calorie (4.184 Joule). By comparison, the heat absorption for evaporating the two-phase flow fluid is 500 times higher than raising one-centigrade degree of the water. Therefore, the two-phase flow can absorb or expel a greater amount of heat than that of the traditional forced-liquid flow used on the thermal exchanging device. As a result, the two-phase flow phenomena can increase the speed at which the working fluid and the working material exchange heat.
2. The wick structure, based on the principle of capillary action, can transport the working fluid and the working material seamlessly through the chamber. In effect, by virtue of the capillary action, less energy is required to draw the working fluid across the chamber, compared to the conventional forced-liquid flow of the working fluid. Consequently, the operating efficiency of the thermal exchanging device is much higher than that that of the conventional thermal exchanging device.
Although the invention has been described with reference to specific embodiments, this description is not meant to be construed in a limiting sense. Various modifications of the disclosed embodiments, as well as alternative embodiments, will be apparent to persons skilled in the art. It is, therefore, contemplated that the appended claims will cover all modifications that fall within the true scope of the invention.
Claims
1. A thermal exchanging device, comprising:
- a vacuum chamber;
- a working material capable of being excited magnetically; and
- a working fluid capable of undergoing a transition between two phase flows of liquid and vapor, the working fluid being provided in the chamber to communicate with the working material;
- wherein when the working material is magnetically excited, the working fluid is configured to exchange heat with a relative cold heat source; and
- wherein otherwise, the working fluid is configured to exchange heat with a relative hot heat source.
2. The thermal exchanging device as claimed in claim 1, further comprising a magnetic-generating source to excite the working material.
3. The thermal exchanging device as claimed in claim 1, further comprising a wick structure surrounding the working material in the chamber to facilitate flowing of the working fluid and the working material in the chamber.
4. The thermal exchanging device as claimed in claim 3, further comprising a heating unit disposed on outer surface of the chamber and operable to exchange heat between the wick structure and the heat sources.
5. The thermal exchanging device as claimed in claim 4, further comprising a thermal controlling unit having a switch switchable between a first position and a second position for controlling the flow direction of heat exchange between the heating unit and the heat sources, the first position being defined by a heat generation stage where heat is exchanged between the heating unit and the cold heat source, the second position being defined by a heat absorption stage where heat is exchanged between the heating unit and the hot heat source.
6. The thermal exchanging device as claimed in claim 5, wherein the thermal controlling unit further comprises a first port in contact with the heating unit, a second port in contact with the hot heat source, and a third port in contact with the cold heat source, one of the first and second positions is defined by selectively bridging the first port to one of the second and third ports.
7. The thermal exchanging device as claimed in claim 6, wherein the switch is adapted to bridge the first and second ports upon demagnetization of the working material.
8. The thermal exchanging device as claimed in claim 6, wherein the switch is adapted to bridge the first and third ports upon magnetization of the working material.
9. The thermal exchanging device as claimed in claim 3, further comprising:
- two heating units opposite to each other and respectively in thermally contact with the hot and cold heat sources;
- a support member provided in the chamber to separate the chamber into two portions, and
- an activation unit having one valve provided on the support member and operable to selectively close one of the two portions of the chamber.
10. The thermal exchanging device as claimed in claim 9, further comprising two valves close to the two portions of the chamber respectively.
11. The thermal exchanging device as claimed in claim 3, further comprising:
- two heating units oppositing to each other and respectively in contacting with the hot and cold heat sources; and
- an activation unit having two valves respectively provided on opposite sides of the working material.
12. The thermal exchanging device as claimed in claim 1, wherein the working material is a porous magneto-caloric material with more than one Curie temperature, and the porous magneto-caloric material is a powder shape or a wire mesh shape.
13. The thermal exchanging device as claimed in claim 1, wherein the working material includes a plurality of stacked plates with gaps spaced therebetween.
14. The thermal exchanging device as claimed in claim 1, wherein the working material is a bulk material with holes disposed therethrough.
15. The thermal exchanging device as claimed in claim 1, wherein the working material is a bulk material with thin slits provided therethrough.
16. The thermal exchanging device as claimed in claim 1, wherein the working fluid is water.
17. The thermal exchanging device as claimed in claim 1, wherein the working fluid has more than one boiling point temperature.
Type: Application
Filed: Sep 23, 2010
Publication Date: Mar 24, 2011
Inventor: Shao-Hsiung CHANG (Taoyuan Hsien)
Application Number: 12/888,924
International Classification: F25B 21/00 (20060101); F28D 15/00 (20060101);