This application claims priority under 35 U.S.C. §119 to European Patent Application No. 1 3170378.7 filed in Europe on Jun. 4, 2013, the entire content of which is hereby incorporated by reference in its entirety.
This disclosure relates to an apparatus with an evaporator for receiving a heat load from one or more electric components in order to provide adequate cooling for the components.
Closed electric cabinets, such as cabinets containing drives controlling the operation of electric motors, can employ cooling devices for ensuring that heat generated by the electric components do not raise the temperature inside the cabinets to a level where damage may occur.
These known cooling devices can include heat sinks or heat exchangers receiving heat loads from the electric components, and via which a cooling air flow passes for dissipating the heat load to the surrounding environment. Such known cooling devices can include metal pieces without any kind of fluid circulation, or of devices with fluid circulation and which employ a pump for generating the fluid circulation.
There also exists more efficient apparatuses for cooling electric components, such as thermosyphons, capable of circulating a cooling fluid without a need for a pump. It would be desirable to utilize such apparatuses in older electric cabinets which have originally been manufactured to include known heat sinks or heat exchangers.
Such more efficient apparatuses, however, can have shape and dimensions in question. Due to the shape and dimensions these more efficient known apparatuses cannot be utilized to the extent otherwise possible.
An apparatus is disclosed comprising: an evaporator with a first surface for receiving a heat load from one or more electric components; tubes having internal longitudinal walls dividing the tubes into channels, wherein the tubes partly penetrate into the evaporator for providing evaporator channels which are embedded into the evaporator; and condenser channels which are located outside of the evaporator: connecting parts at first and second ends of the tubes for passing fluid from the evaporator channels into the condenser channels and for passing fluid from the condenser channels into the evaporator channels, the connecting parts having hollow sections located within the tubes, each hollow section connecting the channels of a tube to each other in a vicinity of an end of the tube in order to allow fluid to flow between the channels of the tube via the hollow section; and fins extending between the condenser channels of adjacent tubes.
In the following, embodiments of the present invention will be described in closer detail by way of example and with reference to the attached drawings, in which:
The present disclosure provides an apparatus where the shape and dimensions of the apparatus can place less restrictions on installations where the apparatus can be utilized.
The use of connecting parts including hollow sections located within the tubes, which hollow sections connect the channels of a tube to each other in the vicinity of an end of the tube, makes it possible to obtain efficient circulation between evaporator channels and condenser channels without a need for a large fluid distribution element at the ends of the tubes. Therefore the shape and dimensions of the apparatus may be selected more freely than previously.
The
One or more tubes 4 with internal longitudinal walls 5 penetrate partly into the second surface 22 of the evaporator 2 such that at least one channel of the penetrating tubes can be embedded in the base plate 2 to form an evaporator channel 6. Fluid located in this evaporator channel 6 (or evaporator channels 6) receives the heat load 3 via the base plate. Due to temperature rise and evaporation, the fluid will flow upwards in the evaporator channel 6 in the illustrated example.
A hollow section 8 within each tube 4, in other words an end section of the tube where no internal walls are present, connects the channels 6 and 7 of each tube to each other in a first end 10 of the tubes 4 in order to allow fluid to flow between the channels 6 and 7 of the tubes 4.
The channels located outside the evaporator 2 are condenser channels 7. The fluid which has entered the condenser channels 7 will be cooled while moving towards the second end 11 of the tubes 4. The cooling may be accomplished by transfer of heat from the fluid through the walls of the condenser channels 7 to the surrounding air.
A hollow section 9 within each tube 4, in other words an end section of the tube where no internal walls are present, connects the channels 7 and 6 of each tube to each other in the second end 11 of the tubes 4 in order to allow fluid to flow between the channels 7 and 6 of the tubes 4. Consequently, the cooled fluid is returned from the condenser channels 7 to the evaporator channels 6 for a new cycle. In practice, the returning fluid has condensed into a liquid state.
In the illustrated position the fluid circulation occurs without a pump due to gravity, the temperature differences and the density differences of the fluid (liquid/vapour) in different parts of the apparatus. In order to ensure efficient circulation of the fluid and to ensure that adequate circulation occurs also when the apparatus is in another position (such as in the horizontal position of
The following formula, for example, can be used to evaluate a suitable diameter:
D=(sigma/(g*(rhol−rhov)))̂0.5,
where sigma is the surface tension, g the acceleration of gravity, rhov the vapor density and rhol the liquid density. This formula gives exemplary values from 1 to 3 mm for R134a (Tetrafluoroethane), R145fa and R1234ze (Tetrafluoropropene), which are exemplary fluids suitable for use in the apparatus illustrated in the Figures.
In order to ensure an even distribution of fluid within the entire apparatus, the apparatus 21 illustrated in
In
The apparatus illustrated in
A plurality of tubes 4 with internal longitudinal walls 5 can be produced. The tubes 4 may be MPE (Multi Port Extruded) tubes which have been manufactured by extruding aluminum, for instance.
The hollow sections 8 and 9 can be produced in the selected end (or both ends) of the tubes 4 by first removing the internal walls 5 from the end of the tube. This can be done by milling with a water jet, for example. After this, the end can be plugged 30 by welding, for example, such that fluid leakage from the hollow sections 8 and 9 to the outside can be avoided.
The tubes 4 are placed into the grooves in the evaporator 2 and attached to the grooves by brazing, for instance. In case a manifold 27 is also produced by drilling through the base plate of the evaporator 2 and the parts of the tubes 4 that penetrate into the evaporator 2, then additional attention should be paid during the brazing to ensure that leak proof interfaces are obtained between the base plate 2 and the tubes 4. The plug 28 may then be welded to close the end of the manifold 27.
In the second embodiment, the tubes 4′ extend through the evaporator 2′. In the illustrated example the evaporator 2′ includes a plurality of elongated spacer elements 31 which are arranged between the tubes 4′ to keep the tubes apart from each other. Therefore, the tubes 4′ partly penetrate into the evaporator 2′ (are located between the spacers of the evaporator), and the channels located in these parts of the tubes 4′ are evaporator channels 6 that are embedded into the evaporator 2′, and the other channels of the tubes are condenser channels 7, located outside of the evaporator 2′.
Similarly, as in the previous embodiment, fins 26 can extend between condenser channels 7 of adjacent tubes 4′. Additionally, secondary spacer elements 32 may be arranged between the condenser channels 7′ of the adjacent tubes at the lower edge of the tubes, as illustrated in
The second embodiment utilizes an alternative way of implementing a manifold 27′. As best seen in
The longitudinal length of the wall element 33 is shorter than the longitudinal length of the plates 34, as best seen in
The plates 34 and the spacer elements 35 arranged between the plates 34 along opposite first edges of the plates 34, together with plug elements 30 (provided by attaching plates by welding, for example) arranged along opposite second edges of the plates 34 together delimit a fluid tight space within the tube 4′. However, naturally a hole for allowing fluid communication via the manifold 27′ may be provided in the tube 4′. The different parts of the tube 4′ may be soldered together, for example.
After production of a sufficient number of tubes 4′, spacer elements 31, secondary space elements 32 and fins 26 may be arranged between such tubes in order to assemble the apparatus 2′ illustrated in
The alternative tube design illustrated in
The spacers 35 and plug elements used in tube 4″ may be similar as explained in connection with tube 4′, and the longitudinal length of the wall element 33′ is shorter than the longitudinal length of the plates 34 in order to produce the hollow sections 8 and 9 at opposite ends of the tube 4″.
It is to be understood that the above description and the accompanying figures are only intended to illustrate exemplary embodiments of the present invention. It will be apparent to a person skilled in the art that the invention can be varied and modified without departing from the scope of the invention.
Thus, it will be appreciated by those skilled in the art that the present invention can be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The presently disclosed embodiments are therefore considered in all respects to be illustrative and not restricted. The scope of the invention is indicated by the appended claims rather than the foregoing description and all changes that come within the meaning and range and equivalence thereof are intended to be embraced therein.
Number | Date | Country | Kind |
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13170378.7 | Jun 2013 | EP | regional |