CROSS REFERENCE TO RELATED APPLICATIONThis application is based on and claims the benefit of priority from the prior Japanese patent application No. 2001-351720 filed on Nov. 16, 2001; the entire contents of the prior application being incorporated herein by reference.[0001]
BACKGROUND OF THE INVENTION1. Field of the Invention[0002]
The present invention relates to a heat exchanger for conducting heat exchange via a heat transfer member, and more specifically, to the configuration of the heat transfer surface in the heat transfer member of the heat exchanger.[0003]
2. Description of the Related Art[0004]
Thermoelectric power generation apparatus A of a thermo-siphon type shown in FIG. 13, for example, comprises an evaporation unit B in which heat transfer tubes Bb are heated with high-temperature fluid flowing through a duct Ba and vapor is generated by heating a heat medium W stored in a storage unit Bc, and a thermoelectric converter C accommodating a thermoelectric power generation module D comprising a thermoelectric module E, a heat transfer plate (heat-transfer member) F and a water-cooled plate G in a chamber Ca linked to the evaporation unit B.[0005]
Here, the thermoelectric power generation module D is a heat exchanger in the broad sense of the word. In the module D, heat transfer plate F and water-cooled plate G are provided on the high-temperature and low-temperature sides of thermoelectric module E, respectively. When vapor of heat medium W generated in evaporation unit B condenses upon contact with the surface (heat transfer surface) of heat transfer plate F, heat is radiated and the high-temperature side of thermoelectric module E is heated. As a result, power is generated by the operation of a P-type/N-type semiconductor constituting thermoelectric module E, based on the temperature difference between the high-temperature side and low-temperature side of thermoelectric module E that is cooled by water-cooled plate G.[0006]
It is well know that, in the heat transfer with condensation, the heat exchange efficiency of drop condensation is higher than that of film-shaped condensation. For this reason, a coating film Fc made of a material with a very low wettability, that is, a material having no affinity to condensate, such as polyfluoroethylene resin (such as Teflon: trademark), is coated on the surface (heat transfer surface) of heat transfer plate F thereby causing condensate W brought in contact with heat transfer plate F to form drops, as shown in FIG. 14.[0007]
On the other hand, in a heat exchanger in which the temperature of the heat transfer surface of a heat transfer plate is no higher than 0° C., such as a heat exchanger for use in a refrigerator and the like (not shown in the figure), with the object of preventing as much as possible the decrease in heat exchange efficiency due to frost, which originates due to condensation and solidification of water molecules present in the air, a coating film made of a material with low wettability is formed on the heat transfer surface of the heat transfer plate, as in the above-described thermoelectric power generation module D. With this construction, water that has initially condensed upon contact with the heat transfer plate is caused to form drops, thus weakening the frost base of the frost layer and facilitating peeling of the frost from the heat transfer surface of heat transfer plate.[0008]
However, in the structure in which a coating film Fc with low wettability was formed on the flat surface of heat transfer plate F, as in the above-described thermoelectric power generation module (heat exchanger) D as shown in FIG. 14, a contact angle θ of heat medium (condensate) W, which has assumed a drop-like shape, with respect to the heat transfer plate F (coating film Fc) was about 110° at most.[0009]
For this reason, the surface (heat transfer surface) of heat transfer plate F was far from the ideal drop condensation surface and was not sufficient from the standpoint of heat transfer efficiency. Accordingly, in heat exchangers, more significant increase in heat transfer efficiency was desired.[0010]
Further, in heat exchangers for use in cooling apparatuses, even in structures in which a coating film with low wettability was formed on the flat surface (heat transfer surface) of heat transfer plate, the contact angle between condensed water drops and heat transfer plate (coating film) was about 110° at most.[0011]
Therefore, wettability on the surface (heat transfer surface) of heat transfer plate was not sufficiently low, and peeling of the frost from the surface was hindered so that the frost accumulated on the surface (heat transfer surface) of heat transfer plate, thereby causing significant decrease in heat exchange efficiency.[0012]
SUMMARY OF THE INVENTIONWith the foregoing in view, it is an object of the present invention to provide a heat exchanger which makes it possible to attain further increase in heat exchange efficiency.[0013]
According to the present invention, in a heat exchanger for conducting heat exchange via a heat transfer member, the heat transfer member has a heat transfer surface on which a large number of protrusions each having a height and a width of less than 0.01 mm, respectively, are disposed with a pitch of less than 0.01 mm, at least surface of the protrusions being made of a material with low wettability.[0014]
With such a configuration as above, the heat transfer surface of the heat transfer member has very low wettability with an ultralow surface energy.[0015]
Therefore, the heat transfer surface of the heat transfer member that is a condensation heat transfer surface is close to the ideal drop condensation surface, which provides a good heat exchange efficiency.[0016]
Further, when the heat transfer surface of the heat transfer member is a low-temperature heat transfer surface, wettability is extremely low. Therefore, frost assumes a shape of spheres which are easy to peel so that accumulation of frost on the surface of heat transfer plate is suppressed, and hence a good heat exchange efficiency can be obtained.[0017]
Thus, with the heat exchanger in accordance with the present invention, a further increase in heat exchange efficiency can be attained.[0018]
BRIEF DESCRIPTION OF THE DRAWINGSIn the accompanying drawings:[0019]
FIG. 1 is a schematic view illustrating an embodiment of the heat exchanger in accordance with the present invention;[0020]
FIG. 2A is a plan view illustrating a heat transfer member in the heat exchanger shown in FIG. 1;[0021]
FIG. 2B is a sectional side view illustrating the heat transfer member in the heat exchanger shown in FIG. 1;[0022]
FIG. 3A is a schematic view illustrating a process for manufacturing the heat transfer member in the heat exchanger shown in FIG. 1;[0023]
FIG. 3B is a schematic view illustrating a process for manufacturing the heat transfer member in the heat exchanger shown in FIG. 1;[0024]
FIG. 4 is a schematic view illustrating a state in which liquid is brought in contact with the heat transfer member in the heat exchanger shown in FIG. 1;[0025]
FIG. 5 illustrates how an apparent contact angle depends on the fraction of the surface area taken by air portions in the surface with fine peaks and valleys;[0026]
FIG. 6A is a plan view illustrating a modification of the heat transfer member in the heat exchanger shown in FIG. 1;[0027]
FIG. 6B is a cross-sectional view illustrating a modification of the heat transfer member in the heat exchanger shown in FIG. 1;[0028]
FIG. 7A is a plan view illustrating a modification of the heat transfer member in the heat exchanger shown in FIG. 1;[0029]
FIG. 7B is a cross-sectional view illustrating a modification of the heat transfer member in the heat exchanger shown in FIG. 1;[0030]
FIG. 8A is a plan view illustrating a modification of the heat transfer member in the heat exchanger shown in FIG. 1;[0031]
FIG. 8B is a cross-sectional view illustrating a modification of the heat transfer member in the heat exchanger shown in FIG. 1;[0032]
FIG. 9A is a plan view illustrating another embodiment of the heat transfer member;[0033]
FIG. 9B is a sectional side view illustrating another embodiment of the heat transfer member;[0034]
FIG. 10A is a schematic view illustrating a process for the manufacture of the heat transfer member in the heat exchanger shown in FIG. 9;[0035]
FIG. 10B is a schematic view illustrating a process for the manufacture of the heat transfer member in the heat exchanger shown in FIG. 9;[0036]
FIG. 11A is a plan view illustrating still another embodiment of the heat transfer member;[0037]
FIG. 11B is a sectional side view illustrating still another embodiment of the heat transfer member;[0038]
FIG. 12A is a plan view illustrating yet another embodiment of the heat transfer member;[0039]
FIG. 12B is a sectional side view illustrating yet another embodiment of the heat transfer member;[0040]
FIG. 13 is a schematic view illustrating a conventional heat exchanger; and[0041]
FIG. 14 is a sectional view illustrating a heat transfer member in the conventional heat exchanger of FIG. 13[0042]
DESCRIPTION OF THE PREFERRED EMBODIMENTSEmbodiments of the present invention will be described hereinbelow in greater detail with reference to the appended drawings.[0043]
FIG. 1 illustrates an embodiment in which the present invention is employed in a thermoelectric power generator. The[0044]thermoelectric power generator1 comprises anevaporation unit1A and athermoelectric converter1B. In theevaporation unit1A, aheat transfer pipe2bis heated by high-temperature fluid flowing through a duct2aand a heat medium W stored in astorage unit2cbecomes vapor. Thethermoelectric converter1B comprises achamber3clinked to theevaporation unit1A, which accommodates a thermoelectricpower generation module7 comprising athermoelectric module4, a heat transfer plate (heat-transfer member)5, and a water-cooledplate6.
The thermoelectric[0045]power generation module7 is a kind of heat exchanger, wherein heat transfer plate (heat-transfer member)5 is provided on the high-temperature side and water-cooledplate6 is provided low-temperature side ofthermoelectric module4. When vapor of heat medium W generated inevaporation unit1A condenses upon contact with aheat transfer surface5sofheat transfer plate5, heat is radiated so that the high-temperature side ofthermoelectric module4 is heated. With the temperature difference of the high-temperature side ofthermoelectric module4 with the low-temperature side that is cooled by water-cooledplate6, electric power is generated through the operation of a P-type/N-type semiconductor constitutingthermoelectric module4.
As shown in FIG. 1 and FIGS. 2A and 2B, a large number of very fine pins (protrusions)[0046]5aare provided on heat transfer surface (condensation heat transfer surface)5sof heat-transfer plate5.
Each of the[0047]pins5ahas a cylindrical shape of a very small size with a height h and a diameter (width) d being less than 0.01 mm. Thepins5aare arranged to form a lattice with a very small spacing such that a pitch p between theadjacent pins5ais less than 0.01 mm.
Furthermore, the configuration of[0048]pins5ainheat transfer plate5 is such that the entire pins are formed from a material that shows very low wettability with no affinity to condensate, such as a polyfluoroethylene resin (trade name: Teflon). With this structure, at least the surface of the pins is formed from the material with low wettability.
With the structure described above in which a large number of[0049]pins5awith the surface thereof being made of a material having low wettability are provided,heat transfer surface5sofheat transfer member5 is provided with fine peaks and valleys and has very low wettability and ultralow surface energy.
FIGS. 3A and 3B illustrate a process for the fabrication of the[0050]heat transfer member5. In order to fabricate theheat transfer member5, first, as shown in FIG. 3A, asurface layer5B made of a material with low wettability, such as a polyfluoroethylene resin or the like, is formed on the surface of a heattransfer plate base5A made of stainless steel or the like, this layer having a thickness greater than the height h ofpins5a(see FIG. 2B) which are to be formed. Then, as shown in FIG. 3B, a prescribed number ofpins5aare formed by processing the surface layer5bby using microfabrication technology.
Taking into account a heat conductivity and cost, various materials (for example, aluminum and the like) may be employed instead of stainless steel as a material for heat[0051]transfer plate base5A.
Further, various materials (for example, silicone resins and the like) other than the polyfluoroethylene resin may also be employed as the material constituting the[0052]surface layer5B, that is, pins5a,provided that the condition of low wettability is satisfied.
Referring to FIG. 4, when vapor of heat medium W condenses upon contact with[0053]heat transfer surface5sof the above-describedheat transfer plate5, the heat medium (condensate) W assumes drops of almost a spherical shape that are supported by a large number ofpins5a.
Furthermore, as seen from FIG. 4, the contact angle θf of drop-like heat medium (condensate) W with respect to heat[0054]transfer plate5 is much larger than the contact angle θ of heat medium (condensate) W with respect to the conventional heating plate F shown in FIG. 14.
In a surface with ultralow surface energy, the contact angle θf is known to depend on Ag as shown by formula (1) below, where Ag is the fraction of area taken by gas portions in the peak-valley surface.[0055]
cos θf=(1−Ag) cos θ−Ag (1)
Water, freon, Florinate (trademark) or the like can be employed as the heat medium W. However, it goes without saying that the above-described relationship is established for a variety of heating media W.[0056]
FIG. 5 illustrates the relationship between the contact angle θf and Ag. Graph of this figure clearly shows that for the heat medium with a contact angle θ of 110° formed with respect to a plane, the contact angle θf increases to about 130° when Ag is 0.5, and the contact angle θf further increases to 160° when Ag is 0.9.[0057]
In the[0058]heat transfer plate5 according to this embodiment, a large number ofpins5aare formed onheat transfer surface5sso that Ag becomes no less than 0.5, preferably, 0.7-0.9.
For this reason, the contact angle θf of the heat medium (condensate) W that assumed a drop-like shape upon contact with[0059]heat transfer plate5 greatly increases by comparison with the contact angle θ (see FIG. 14) with respect to a flat heat transfer plate. As a result,heat transfer surface5aofheat transfer plate5 becomes close to an ideal drop condensation surface and a good heat exchange efficiency can be obtained.
Furthermore, when the present invention is applied to a heat exchanger for use in a refrigerator or the like, that is, when[0060]heat transfer surface5ainheat transfer member5 shown in FIG. 1 through FIG. 5 is a low-temperature heat transfer surface, the wettability ofheat transfer surface5ainheat transfer member5 is extremely low as described above so that any frost that is present onheat transfer surface5aassumes a spherical shape, which is easy to peel off the surface. As a result, accumulation of the frost onheat transfer plate5 can be effectively prevented and good heat exchange efficiency can be obtained.
Pins[0061]5ain the above-described embodiment had a cylindrical shape as shown in FIGS. 2A and 2B. However, the form ofpins5ais not limited to a cylindrical shape and the pins can be in a variety of shapes such as elliptical cylinder shown in FIGS. 6A and 6B, quadrangular prism shown in FIGS. 7A and 7B, or circular cone shown in FIGS. 8A and 8B.
In[0062]heat transfer plate5 shown in FIGS. 1 through 8, theentire pins5aare formed from a material with low wettability such as a polyfluoroethylene resin or the like. However, because thermal conductivity of polyfluoroethylene resins is lower than that of metals, heat transfer efficiency ofheat transfer plate5 is unavoidably decreased.
FIGS. 9A and 9B illustrate another embodiment of a[0063]heat transfer plate10 designed to increase the heat transfer efficiency. In theheat transfer plate10, a large number of very fine pins (protrusions)10aare provided on aheat transfer surface10s. Thepins10aare in the form of cylinders of a very small size with a height h and diameter (width) d being less than 0.01 mm and are arranged to form a lattice with a very small spacing such that a pitch p between theadjacent pins10ais less than 0.01 mm.
Furthermore, a[0064]film10cmade of a material with a very low wettability because of having no affinity to condensate, such as polyfluoroethylene resin (trademark: Teflon), is formed on the surface ofpins10aformed inheat transfer plate10.
FIGS. 10A and 10B illustrate a process for the fabrication of the[0065]heat transfer member10. In order to fabricate theheat transfer member10, first, as shown in FIG. 10A, a prescribed number ofpins10aare formed by using microfabrication technology such as etching and the like on the surface of a heattransfer plate base10A made of copper or the like.
Then, as shown in FIG. 10B, a[0066]film10cmade of a material with low wettability, such as a polyfluoroethylene resin or the like, is formed by an appropriate coating technique such as painting or deposition on the surface of heattransfer plate base10A, in other words, on the surface ofpins10a.
Taking into account thermal conductivity and cost, various materials other than copper may be employed as the material of heat[0067]transfer plate base5A.
Further, it goes without saying that various materials (for example, silicone resins and the like) other than the polyfluoroethylene resin may be employed for[0068]film10c,provided that the condition of low wettability is satisfied.
With the[0069]heat transfer plate10 of the above-described configuration, because the main bodies ofpins10aare made of a metal material such as copper or the like, heat transfer efficiency can be greatly increased by comparison with that of the heat transfer plate shown in FIGS. 1 through 8, in which the entire pins are formed of a material with low wettability completely.
FIGS. 11A and 11B illustrate a still another embodiment of the present invention in which a[0070]heat transfer plate20 is provided with a large number oflow fins20F. A large number of very small pins (protrusions)20aare provided on asurface20sofheat transfer plate20, including the outer surface of thelow fins20F.
The configuration of those[0071]pins20a,that is, the shape, layout, and manufacturing process thereof are not substantially different from those relating to heattransfer plate5 shown in FIGS. 1 through 8 andheat transfer plate10 shown in FIGS. 9 and 10.
With[0072]heat transfer plate20 of the above-described configuration, heat exchange can be conducted with a very good efficiency due to the enlarged heat transfer surface effect provided bylow fins20F, the surface tension effect of heat medium (condensate), and the condensation heat transfer effect resulting from the presence of a large number ofpins20a.
FIGS. 12A and 12B illustrate yet another embodiment of the present invention in which a[0073]heat transfer plate30 is provided with a large number of plate-shapedfins30F. A large number of very small pins (protrusions)30aare provided on asurface30sofheat transfer plate30, including the outer surface of thosefins30F.
The configuration of those[0074]pins30a,that is, the shape, layout, and manufacturing process thereof are not substantially different from those relating to heattransfer plate5 shown in FIGS. 1 through 8 andheat transfer plate10 shown in FIGS. 9 and 10.
With[0075]heat transfer plate30 of the above-described configuration, heat exchange can be conducted with a very good efficiency due to the enlarged heat transfer surface effect provided bylow fins30F, the surface tension effect of heat medium, and the condensation heat transfer effect resulting from the presence of a large number ofpins30a.
Furthermore, when[0076]heat transfer plate30 of the above-described configuration is used in a heat exchanger, for example, of a refrigerator, providing a large number ofpins30amakes it possible to realize a high-performance low-temperature heat exchanger by effectively preventing frost from accumulating and preventing the increase in ventilation resistance caused by the frost.
In the embodiments described above, the present invention was applied to heat exchangers in thermoelectric power generators or refrigerators. However, it goes without saying that the present invention can be also effectively applied to heat exchangers for use in various apparatuses in a variety of industrial fields, provided that the heat exchangers conduct heat exchange via a heat transfer member.[0077]