JP2019203689A - Packaged drink temperature regulator, and heat transfer member - Google Patents

Abstract

To provide a bottled drink temperature regulator capable of adjusting a temperature of a bottled drink such as bottle wine without using ice and iced water.SOLUTION: A wine temperature regulator 100 includes a Peltier unit 120 for adjusting a temperature of bottle wine 1 stored in a bottle storage part 110, and a heat transfer pad 130 arranged between the bottle wine 1 and the Peltier unit 120. The heat transfer pad 130 is constituted of a deformable storage bag, and heat transfer powder and heat transfer liquid stored in the storage bag. The heat transfer powder is metal powder with high heat conductivity, and is composed of for instance, copper powder. The heat transfer liquid is liquid solidified at a temperature higher than a target temperature (for instance, 8°C), and is composed of for instance, pentadecane (solidification temperature:9.9°C). That is, the heat transfer liquid is solidified at a temperature between the target temperature and a use environmental temperature (for instance, 25°C), and is not solidified at the use environmental temperature.SELECTED DRAWING: Figure 1

Description

  INDUSTRIAL APPLICABILITY The present invention relates to a container temperature control device for adjusting the temperature of a beverage (for example, bottled wine) (for example, cooling or cold storage), and heat transfer suitable for use in the container temperature control device. It relates to members.

  2. Description of the Related Art Conventionally, as a wine cooler for cooling and maintaining a bottled wine (hereinafter referred to as “bottle wine”) at a drinking temperature, a bucket-shaped container with ice or ice water is known.

  However, in the wine cooler as described above, since the bottle wine bottle and ice etc. are in direct contact with each other, when the bottle wine is taken out from the wine cooler to be poured into the glass, the water droplets attached to the bottle are wiped off. It was necessary and was to be troublesome.

  In JP 2010-47313 A, since a conventional general wine cooler has water droplets attached to a wine bottle, the bottle is wiped with a towel each time the bottle is taken out of the wine cooler to pour wine into a glass. In view of the need to remove water droplets, a cold storage container with a simple structure, which makes it difficult for water droplets to adhere to the wine bottle and allows the wine bottle label to be visually recognized, which is open at the top consisting of a cylindrical portion and a bottom surface portion. The thing which attached the cold insulating material to the inner wall of this by the fixing means is disclosed.

JP 2010-47313 A

  An object of the present invention is to use a container-containing beverage temperature adjusting device capable of adjusting the temperature of a container-containing beverage such as bottle wine without using ice or ice water, and the use in the container-containing beverage temperature adjusting device. An object of the present invention is to provide a heat transfer member having a suitable high heat conductivity.

  The container-packed beverage temperature control device according to the present invention adjusts the temperature of the container-packed beverage via a heat transfer member that comes into contact with a part of the side surface of the container-packed beverage to be temperature-controlled, and the heat transfer member. And the heat transfer member is composed of a deformable bag, heat transfer powder and heat transfer liquid accommodated in the bag, and the heat transfer liquid is a target. It is a liquid that solidifies at a temperature higher than the temperature.

  In this case, you may make it further provide the urging | biasing part for making the said drink in a container and the said heat-transfer member contact | abut.

  Moreover, in the above case, you may make it the said heat-transfer member contact | abut on the upper part of the said drink with a container. The heat transfer member may be in contact with the entire region from the upper part to the lower part of the beverage in the container, and includes a plurality of the heat transfer members, and the plurality of heat transfer members are contained in the container. You may make it arrange | position at intervals so that the longitudinal direction of a drink may be followed. In this case, you may make it further provide the 2nd heat-transfer member arrange | positioned between the said heat-transfer member and the said temperature control part. Furthermore, in this case, the second heat transfer member may be formed of a metal plate.

  In the above case, before the temperature adjustment of the beverage in the container is started, the heat adjustment member is heated by the temperature adjustment unit to melt the solidified heat transfer liquid. Good.

  In the above case, the heat transfer powder may be made of metal powder. The heat transfer liquid may be composed of any one of linear hydrocarbon, primary alcohol, linear aldehyde, and linear carboxylic acid.

  In the above case, the amount of the heat transfer liquid added to the heat transfer powder may be 24% by volume or more in volume ratio, or about 28 to 48% by volume in volume ratio. May be.

  Moreover, in the above case, the particle size of the heat transfer powder may be in the range of 0.04 mm to 0.16 mm.

  The heat transfer member according to the present invention is a heat transfer member used for adjusting the temperature of a temperature adjustment object to a target temperature, and is a deformable bag and heat transfer powder accommodated in the bag. And the heat transfer liquid, wherein the heat transfer liquid is a liquid that solidifies at a temperature higher than the target temperature.

  In this case, the heat transfer powder may be made of metal powder. The heat transfer liquid may be composed of any one of linear hydrocarbon, primary alcohol, linear aldehyde, and linear carboxylic acid.

  In the above case, the amount of the heat transfer liquid added to the heat transfer powder may be 24% by volume or more in volume ratio, or about 28 to 48% by volume in volume ratio. May be.

  Moreover, in the above case, the particle size of the heat transfer powder may be in the range of 0.04 mm to 0.16 mm.

  ADVANTAGE OF THE INVENTION According to this invention, without using ice and ice water, the utilization in the container drink temperature control apparatus which can adjust the temperature of container drinks, such as bottle wine, and the said container drink temperature adjustment apparatus A suitable heat transfer member with high thermal conductivity can be provided.

It is a figure for demonstrating the structure of the wine temperature control apparatus by this invention. It is a figure which shows the wine temperature control apparatus 100 of the state which opened the cover part. 3 is a front view for explaining the structure of a Peltier unit 120. FIG. 4 is a left side view for explaining the structure of the Peltier unit 120. FIG. It is a front central cross-sectional view for explaining the structure of the Peltier unit. It is a figure for demonstrating the structure of the thermoelectric conversion module. It is a figure for demonstrating the structure of another wine temperature control apparatus (2nd embodiment) by this invention. It is a figure for demonstrating the structure of another wine temperature control apparatus (3rd embodiment) by this invention. It is the photograph (drawing substitute photograph) which shows the example (Example 2 and Example 5) of the heat-transfer pad used for the cooling test. It is the photograph (drawing substitute photograph) which shows the mode of a cooling test. It is a table | surface which shows the measurement result of each heat-transfer pad. It is a figure for demonstrating the measuring method in the state which inclined the bottle wine by the predetermined angle. It is a table | surface which shows the measurement result in the state which inclined the bottle wine by the predetermined angle.

  Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

  Below, the wine temperature control apparatus as a container drink temperature control apparatus by this invention is demonstrated. The wine temperature adjusting device is for adjusting the temperature of the bottle wine to a predetermined drinking temperature (target temperature). The wine temperature adjusting device is used, for example, to cool bottle wine in a room temperature state to a target temperature and maintain the target temperature. In the following, for the sake of simplicity, the target temperature is determined in advance, but the target temperature may be set by the user (for example, selected from a plurality of predetermined candidates). .

<< First embodiment >>
FIG. 1 is a diagram for explaining a configuration of a wine temperature adjusting apparatus according to the present invention. The figure (a) shows a top view and the figure (b) shows a plan view central cross section. For the sake of simplicity, only the main parts necessary for explaining the present invention are shown in FIG.

  As shown in the figure, a wine temperature control apparatus 100 according to the present invention includes a bottle storage unit 110 for storing a bottle wine 1 to be temperature controlled, and the temperature of the bottle wine 1 stored in the bottle storage unit 110. The Peltier unit 120 for adjusting, the bottle wine 1 accommodated in the bottle accommodating part 110, and the heat-transfer pad 130 arrange | positioned between the Peltier units 120 are provided.

  The bottle accommodating portion 110 is a space for accommodating the bottle wine 1 to be temperature-controlled, and is formed by a main body portion 111 and a cover portion 112 that can be opened and closed in the present embodiment.

  The main body 111 is a main part of the wine temperature adjusting device 100 and includes a Peltier unit 120 therein, as shown in FIG. The heat insulating material 113 is filled.

  The cover portion 112 is attached to the main body portion 111 via a hinge mechanism 114 provided at the lower end portion, and is configured to be rotatable around the axis of the hinge mechanism 114.

  As shown in the figure, a leaf spring 115 is provided inside the cover portion 112.

  The leaf spring 115, together with the cover portion 112, constitutes an urging portion for bringing the bottle wine 1 and the heat transfer pad 130 into contact with each other, and the bottle spring 1 accommodated in the bottle accommodating portion 110 is removed from the Peltier. It is an urging member for urging in the direction of the unit 120 (heat transfer pad 130).

  The Peltier unit 120 is for adjusting (cooling and keeping cold) the temperature of the bottle wine 1 stored in the bottle storage unit 110 (temperature control unit). In the present embodiment, the Peltier unit 120 is connected via the heat transfer pad 130. The temperature of the bottle wine 1 is adjusted. For the sake of simplicity, a simplified display is shown in the figure, but details of the structure of the Peltier unit 120 will be described later.

  For simplicity, although not shown in the figure, the wine temperature adjusting device 100 includes a control unit for controlling the operation of the Peltier unit 120, a fan for cooling the Peltier unit 120 (radiating fins), Further, a power supply unit for supplying power necessary for the operation of the Peltier unit 120 and the like, an operation unit for the user to instruct various operations of the wine temperature adjusting device 100, and the like are further provided.

  The heat transfer pad 130 is in contact with the bottle wine 1 (part of the side surface) accommodated in the bottle accommodating portion 110 and conducts heat between the bottle wine 1 and the Peltier unit 120 (heat transfer member). ). In the present embodiment, the heat transfer pad 130 contacts the bottle wine 1 in the vicinity of the shoulder portion (upper side surface) of the bottle. The heat transfer pad 130 has a substantially rectangular flat plate shape, and is suspended by a fixture (not shown) so as to be parallel to the temperature adjustment surface of the Peltier unit 120. That is, the heat transfer pad 130 is not fixed to the temperature adjustment surface of the Peltier unit 120, and the bottle wine 1 is pressed against the heat transfer pad 130, so that the heat transfer pad 130 comes into close contact with the temperature adjustment surface of the Peltier unit 120.

  The heat transfer pad 130 includes a deformable storage bag, and heat transfer powder and heat transfer liquid stored in the storage bag.

  The storage bag is a bag body that stores the heat transfer powder and the heat transfer liquid, and is made of a material having a suitable strength and flexibility (in this embodiment, a synthetic resin (more specifically, polyethylene)). It is configured.

  The heat transfer powder is a main heat transfer medium together with the heat transfer liquid. The heat transfer powder is a metal powder having a high thermal conductivity, and in this embodiment, the heat transfer powder is composed of copper (Cu) powder.

The heat transfer liquid is a main heat transfer medium along with the heat transfer powder. The heat transfer liquid is a liquid that solidifies at a temperature higher than a target temperature (for example, 8 ° C.), and in the present embodiment, is constituted by paraffin. More specifically, it is composed of pentadecane (C ₁₅ H ₃₂ ) (solidification temperature: 9.9 ° C.) or hexadecane (C ₁₆ H ₃₄ ) (solidification temperature: 18 ° C.). That is, in this embodiment, the heat transfer liquid is at a temperature (a temperature higher than the target temperature and lower than the use environment temperature) between the target temperature (eg, 8 ° C.) and the use environment temperature (eg, 25 ° C.). It will solidify and will not solidify at the ambient temperature (for example, 25 ° C.).

  In addition, the amount of heat transfer liquid added to the heat transfer powder is such that the presence of both becomes a capillary state (a state where all the gaps between the heat transfer powders are filled with the heat transfer liquid), specifically, The volume ratio is set to be about 35 to 37% by volume.

  FIG. 2 is a diagram showing the wine temperature adjusting device 100 with the cover 112 opened. FIG. 4A shows a state in which the cover 112 is opened to set the bottle wine 1 before the start of cooling, and FIG. 4B shows that the bottle wine 1 is taken out after being cooled to the target temperature. The state which opened the cover part 112 is shown.

  When using the wine temperature adjusting device 100, first, as shown in FIG. 1A, the cover portion 112 is opened and the bottle wine 1 to be temperature adjusted is set, and as shown in FIG. Cooling is started after the section 112 is closed.

  When the bottle wine 1 is set and the cover portion 112 is closed, the bottle wine 1 is urged by the leaf spring 115 and the bottle wine 1 is pressed against the heat transfer pad 130.

  When the bottle wine 1 is pressed against the heat transfer pad 130, the heat transfer pad 130 is appropriately deformed so as to conform to the shape of the bottle wine 1, and the bottle wine 1 and the heat transfer pad 130 are in close contact with each other. The heat conduction efficiency is improved.

  As described above, in the wine temperature adjusting device 100, the shape of the heat transfer pad 130 is adapted to the shape of the bottle wine 1 by pressing the bottle wine 1 (part of the side surface thereof) against the deformable heat transfer pad 130. Therefore, even if the shape and size of the bottle wine 1 are different to some extent, the bottle wine 1 and the heat transfer pad 130 can be brought into close contact with each other.

  Further, as described above, the heat transfer liquid accommodated in the heat transfer pad 130 is solidified at a temperature higher than the target temperature, and thus solidifies in the process of being cooled to the target temperature. Therefore, when the cover 112 is opened after being cooled to the target temperature, the shape of the heat transfer pad 130 remains deformed so as to match the shape of the bottle wine 1 as shown in FIG. , Will be held. Therefore, for example, when the bottle wine 1 is taken out for pouring into the glass and then the same bottle wine 1 is returned to the wine temperature adjusting device 100 again, the close contact state between the bottle wine 1 and the heat transfer pad 130 is maintained. It will be.

  In the wine temperature adjusting apparatus 100, when the cooling of a new bottle wine 1 is started, for example, in response to a user instruction via the operation unit, the control unit first controls the Peltier unit 120 to transmit the bottle wine 1. The heating pad 130 is heated to melt the solidified heat transfer liquid, and then a new bottle of wine 1 is set. In this way, when a new bottle wine 1 is set, the heat transfer pad 130 can be deformed again into a shape that matches the shape of the new bottle wine 1.

  Next, details of the Peltier unit 120 will be described.

  3 to 5 are diagrams for explaining the structure of the Peltier unit 120. 3 shows a front view, FIG. 4 shows a left side view, and FIG. 5 shows a central cross-sectional view of the front view.

  As shown in FIGS. 3 to 5, the Peltier unit 120 includes a heat transfer block 121, heat radiation fins 122, and a case 123. Furthermore, as shown in FIG. 5, a thermoelectric conversion module 124 is sandwiched between the heat transfer block 121 and the heat radiating fins 122.

  The heat transfer block 121 is a heat transfer member that contacts one surface of the thermoelectric conversion module 124 and transfers heat, and is made of, for example, a metal having high thermal conductivity (for example, aluminum). The heat transfer block 121 has a substantially quadrangular prism shape, and the heat transfer pad 130 comes into contact with the upper surface (temperature adjustment surface) 1211 thereof.

  The heat radiating fins 122 are heat transfer members (heat radiating members) that contact (heat radiate) heat by contacting the other surface of the thermoelectric conversion module 124, and are constituted by, for example, a metal having high thermal conductivity (for example, aluminum). Is done. The heat radiating fin 122 includes a rectangular flat plate 1221 and a large number of fins 1222 attached to the bottom surface thereof, and is forcedly cooled by a fan (not shown).

  The case 123 covers the periphery (side) of the thermoelectric conversion module 124 sandwiched between the heat transfer block 121 and the heat radiating fins 122 to form a sealed space. For example, the heat conductivity is low, It is composed of a synthetic resin (for example, polyphenylene sulfide) that has water resistance and low gas permeability. The case 123 covers the side wall part 1231 extending along the side surface of the heat transfer block 121 and a part of the upper surface of the heat radiation fin 122 (rectangular flat plate 1221) so as to cover most of the side surface of the heat transfer block 121. , And an overhanging portion 1232 extending outward along the upper surface of the radiating fin 122, and is formed so that the cross section is substantially L-shaped. For example, the case 123 is formed by insert molding so as to be integrated with the heat transfer block 121, and the overhanging portion 1232 is fixed (screwed) to the radiating fin 122.

  As shown in FIG. 4, a set of tab terminals 125 for supplying a direct current to the thermoelectric conversion module 124 is provided on one side of the overhanging portion 1232 of the case 123. The tab terminal 125 and the thermoelectric conversion module 124 (the metal electrode thereof) are connected by a lead wire 126.

  FIG. 6 is a diagram for explaining the structure of the thermoelectric conversion module 124.

  As shown in the figure, the thermoelectric conversion module 124 includes a plurality of π-type thermoelectric elements 610 (one end of an n-type semiconductor element 611 and a p-type semiconductor element 612 joined by a metal electrode 613) arranged in a plate shape. The plurality of π-type thermoelectric elements 610 are electrically connected in series and thermally in parallel by metal electrodes 620. In the example shown in the figure, when a direct current is passed in the direction of the arrow (the direction from the n side of the π-type thermoelectric element to the p side), heat is absorbed on the upper surface side (np junction side of the π-type thermoelectric element). Then, heat is released on the bottom side. On the other hand, when the direction of the current is reversed, heat is radiated on the upper surface side and heat is absorbed on the bottom surface side. In general, an insulating substrate 630 (for example, a ceramic substrate) is bonded to the upper surface and the bottom surface, respectively, to form a heat absorption surface and a heat dissipation surface. In the figure, the insulating substrate on the upper surface side is omitted.

  Since the Peltier unit 120 has the above configuration, the heat transfer pad 130 (and the bottle wine 1) is controlled by controlling the amount and direction of the current supplied to the Peltier unit 120 (thermoelectric conversion module 124). It is possible to adjust the temperature.

<< Second Embodiment >>
Next, another wine temperature adjusting device (second embodiment) according to the present invention will be described.

  Below, only the part which is fundamentally different from 1st embodiment mentioned above is demonstrated. Constituent elements similar to those of the first embodiment are denoted by the same reference numerals, and detailed description thereof is omitted.

  FIG. 7 is a diagram for explaining the configuration of another wine temperature adjusting device (second embodiment) according to the present invention. The figure (a) shows a top view and the figure (b) shows a plan view central cross section.

  As shown in the figure, a second wine temperature adjusting device 200 according to the present invention includes a bottle storage unit 110 for storing a bottle wine 1 to be temperature controlled, and a bottle wine 1 stored in the bottle storage unit 110. The Peltier unit 120 for cooling the bottle, the bottle wine 1 accommodated in the bottle accommodating part 110, and the heat transfer pad 230 and the heat transfer plate 240 disposed between the Peltier unit 120 are provided.

  In the present embodiment, the Peltier unit 120 adjusts the temperature of the bottle wine 1 via the heat transfer plate 240 and the heat transfer pad 230.

  The heat transfer plate 240 is disposed between the Peltier unit 120 and the heat transfer pad 230 and conducts heat between the Peltier unit 120 and the heat transfer pad 220 (heat transfer member). In the embodiment, it is configured by a thin (for example, 5 mm thick) metal plate (more specifically, a copper plate). The heat transfer plate 240 is fixed (screwed) to the heat transfer block 121 of the Peltier unit 120.

  The heat transfer pad 230 is in contact with the bottle wine 1 (part of the side) accommodated in the bottle accommodating portion 110 and conducts heat between the bottle wine 1 and the heat transfer plate 240 (heat transfer). Member). The heat transfer pad 230 has the same components (accommodating bag, heat transfer powder, and heat transfer liquid) as the heat transfer pad 130 in the first embodiment, and the difference between them is only the shape and size. That is, the heat transfer pad 130 in the first embodiment is in contact with the bottle wine 1 in the vicinity of the shoulder of the bottle, whereas the heat transfer pad 230 in the second embodiment is generally a vertically long rectangle. It has a flat plate shape and abuts the bottle wine 1 over the entire region from the shoulder to the lower end of the bottle. The heat transfer pad 230 is suspended by a fixture (not shown) so as to be parallel to the heat transfer plate 240. That is, the heat transfer pad 230 is not fixed to the heat transfer plate 240, and the bottle wine 1 is pressed against the heat transfer pad 230, thereby being brought into close contact with the heat transfer plate 240.

  Since the heat transfer pad 230 in the second embodiment has the above-described configuration, the temperature can be adjusted efficiently even for bottled wine with a small amount of wine inside (a state in which the liquid level is lowered). It is like that. That is, as the wine inside the bottle is swallowed, the liquid level of the wine gradually decreases. The bottle wine in such a state is set in the wine temperature adjusting device 100 of the first embodiment. In this case, if the liquid level of the wine inside the bottle falls below the portion where the heat transfer pad 130 is in contact, the temperature adjustment efficiency (cooling efficiency) of the wine inside the bottle will be reduced. On the other hand, in the wine temperature control apparatus 200 of the second embodiment, the heat transfer pad 230 abuts over the entire region from the shoulder portion to the lower end portion of the bottle, so that high temperature control efficiency (cooling) is required until the wine inside the bottle is completely consumed. Efficiency).

<< 3rd embodiment >>
Next, still another wine temperature adjusting device (third embodiment) according to the present invention will be described.

  Below, only the part which is fundamentally different from 1st and 2nd embodiment mentioned above is demonstrated. The same components as those in the first and second embodiments are denoted by the same reference numerals, and detailed description thereof is omitted.

  FIG. 8 is a view for explaining the configuration of still another wine temperature adjusting apparatus (third embodiment) according to the present invention. The figure (a) shows a top view and the figure (b) shows a plan view central cross section.

  As shown in the figure, the third wine temperature adjusting device 300 according to the present invention has a configuration substantially similar to the second wine temperature adjusting device 200 described above, and the difference between the two is that the heat transfer pad is different. Only the difference in configuration.

  That is, the heat transfer pad in the second embodiment is configured by one large heat transfer pad 230, but the heat transfer pad in the third embodiment is configured by a plurality of small heat transfer pads 331 to 336. .

  The plurality of heat transfer pads 331 to 336 are arranged at intervals in the vertical direction (vertical direction in FIG. 5B), and the bottle wine 1 accommodated in the bottle accommodating portion 110 (part of the side surface thereof) And heat conduction between the bottle wine 1 and the heat transfer plate 240 (heat transfer member). Each heat-transfer pad 331-336 has the same component (a storage bag, heat-transfer powder, and heat-transfer liquid) as the heat-transfer pad 222 in 2nd embodiment, and both differ only in a shape and a magnitude | size. It is. That is, the heat transfer pad in the second embodiment covers a range from the shoulder portion to the lower end portion of the bottle by one heat transfer pad 230, whereas the heat transfer pad in the third embodiment is The range from the shoulder portion to the lower end portion of the bottle is covered with a plurality of heat transfer pads 331 to 336 arranged at intervals along the longitudinal direction of the bottle wine 1.

  Each of the heat transfer pads 331 to 336 has a generally rectangular flat plate shape, and is suspended by a fixture (not shown) so as to be parallel to the heat transfer plate 240. That is, the heat transfer pads 331 to 336 are not fixed to the heat transfer plate 240, and the bottle wine 1 is pressed against the heat transfer pads 331 to 336, thereby being brought into close contact with the heat transfer plate 240.

  Since the heat transfer pad in the third embodiment has the above-described configuration, as in the second embodiment, the bottle wine in a state where the amount of wine inside the bottle is small (the state where the liquid level is lowered) The temperature can be adjusted efficiently, and a high temperature adjustment efficiency (cooling efficiency) can be obtained until the wine inside the bottle is completely consumed.

  In the figure, the heat transfer pad 331 arranged at the highest position is not in contact with the side surface of the bottle wine 1, but the heat transfer pad 331 is behind the bottle wine 1 shown in the figure. This is to accommodate bottle wines with high (shoulder position is high).

  As described above, in the wine temperature adjusting apparatus described above, the temperature of the bottle wine to be temperature adjusted is adjusted by the Peltier unit and the heat transfer member (heat transfer pad and heat transfer plate). It is possible to adjust the temperature of the bottle wine without using ice or ice water.

  In addition, since a part of the side surface of the bottle wine subject to temperature control and the deformable heat transfer pad are brought into contact with each other, the bottle wine and the heat transfer pad can be brought into close contact with each other efficiently. It is possible to adjust the temperature of the bottle wine.

As mentioned above, although embodiment of this invention has been described, it cannot be overemphasized that embodiment of this invention is not restricted above. For example, in the above-described embodiment, pentadecane or hexadecane is used as the heat transfer liquid, but other linear hydrocarbons (for example, heptadecane (C ₁₇ H ₃₆ ) ( Coagulation temperature: 22 ° C.), octadecane (C ₁₈ H ₃₈ ) (coagulation temperature: 27.1-28.5 ° C.), nonadecane (C ₁₉ H ₄₀ ) (coagulation temperature: 32-34 ° C.)) Alcohol (for example, 1-undecanol (C ₁₁ H ₂₄ O) (coagulation temperature: 19 ° C.), 1-dodecanol (C ₁₂ H ₂₆ O) (coagulation temperature: 24 ° C.), 1-tridecanol (C ₁₃ H ₂₈ O) (Coagulation temperature: 29-34 ° C.) and linear aldehydes (for example, dodecanal (C ₁₂ H ₂₄ O) (coagulation temperature: 12 ° C.), tridecanal (C ₁₃ H ₂₆ O) (coagulation temperature: 14 ° C.) , tetradecanal (C ₁₄ H ₂₈ O) (solidification temperature: 23 ° C.), pen Decanal (C ₁₅ H ₃₀ O) (solidification temperature: 25 ° C.)) and a linear carboxylic acid (e.g., octanoic acid _{(C 8 H 16 O 2)} ( solidification temperature: 16.7 ° C.), nonanoic acid (C ₉ H ₁₈ O ₂ ) (solidification temperature: 11-13 ° C.), decanoic acid (C ₁₀ H ₂₀ O ₂ ) (solidification temperature: 31 ° C.), undecanoic acid (C ₁₁ H ₂₂ O ₂ ) (solidification temperature: 28-31) It is also conceivable to use ° C)). The upper limit of the solidification temperature of the heat transfer liquid that can be used is usually below the operating environment temperature, but before starting cooling, considering that it is heated and melted by a Peltier unit or the like, The temperature is below the temperature at which the Peltier unit can melt.

  Further, in the above-described embodiment, the cover portion 112 is configured to be rotatable about the axis of the hinge mechanism 114, but the cover portion 112 is slid in the horizontal direction (left and right direction in FIG. 2). It is also possible to make it possible to configure. By configuring the cover portion 112 to be slidable in the horizontal direction, it is possible to deal with bottle wines 1 having different sizes (diameters) in a wider range.

  In the above-described embodiment, the bottle storage unit 110 is configured to store the bottle wine 1 to be temperature controlled in a vertical state (the standing state), but the bottle wine 1 to be temperature controlled. It is also conceivable that the storage device is accommodated in a state where it is inclined at a predetermined angle (a state in which it is laid).

  In the above-described embodiment, metal powder is used as the heat transfer powder, but it is also conceivable to use powders of other materials (for example, ceramic powder).

  Moreover, although the case where the temperature of bottle wine was adjusted was demonstrated in embodiment mentioned above, of course, this invention can also be utilized for the adjustment of the temperature of canned wine or other beverages contained in containers.

  Moreover, although embodiment mentioned above demonstrated the case where a heat-transfer pad was utilized for the temperature adjustment of a drink, the heat-transfer pad by this invention adjusts the temperature of liquids other than a drink, and things other than a container-containing drink. It can be used for this purpose.

  Next, the Example of the heat-transfer pad used in the container drink temperature control apparatus by this invention is described.

  First, a plurality of types of heat transfer pads containing heat transfer powders (copper powders) having different particle sizes were produced as follows.

Example 1
75 g of copper powder (manufactured by DOWA Electronics Co., Ltd.) with a particle size of 3 μm (0.003 mm) indicated by the manufacturer is weighed using an electronic scale (TANITA Corporation, KD-321), and a plastic bag with a chuck (produced by Co., Ltd.) The product was transferred into a Nihon Pack (registered trademark) GP B-4) (hereinafter referred to as “B-4 polybag”). Next, pentadecane (C ₁₅ H ₃₂ ) (manufactured by Wako Pure Chemical Industries, Ltd., Wako Special Grade) is added dropwise using a pipette (Gilson Co., P1000), 0.5 ml at a time, while slowly acclimating, and copper powder is added. After the liquid level was confirmed visually on the surface, 0.5 ml was further added. Air bubbles in the prepared heat transfer pad were sufficiently removed by vibration or the like, and sealed with the air in the bag removed as much as possible to obtain a final heat transfer pad (see FIG. 9).

  The total amount of pentadecane injected was 8 ml. On the other hand, when the bulk volume of 75 g of the copper powder was measured using a 50 ml graduated cylinder, it was 22.5 ml. Therefore, in this case, the amount of heat transfer liquid (pentadecane) added to the heat transfer powder (copper powder) is approximately 36 (= (8 / 22.5) × 100) in volume ratio (ratio to the bulk volume of the heat transfer powder). It becomes capacity%.

Example 2
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-designated particle size of 0.07 mm was weighed using the electronic scale and transferred into a B-4 plastic bag. Thereafter, a heat transfer pad (right side of FIG. 9) was produced in the same manner as in Example 1 described above.

  The total amount of pentadecane injected was 5 ml. On the other hand, when the bulk volume of 75 g of the copper powder was measured using a 50 ml graduated cylinder, it was 14 ml. Therefore, in this case, the amount of the heat transfer liquid (pentadecane) added to the heat transfer powder (copper powder) is about 36 (= (5/14) × 100) volume% in volume ratio.

Example 3
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer's designated particle size of 0.1 mm was weighed using the electronic balance and transferred into a B-4 plastic bag. Thereafter, a heat transfer pad was produced in the same manner as in Example 1 described above.

  The total amount of pentadecane injected was 5 ml. On the other hand, when the bulk volume of 75 g of the copper powder was measured using a 50 ml graduated cylinder, it was 13.5 ml. Therefore, in this case, the amount of heat transfer liquid (pentadecane) added to the heat transfer powder (copper powder) is about 37 (= (5 / 13.5) × 100) volume% in volume ratio.

Example 4
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a particle size of 0.2 mm indicated by the manufacturer was weighed using the electronic scale and transferred into a B-4 plastic bag. Thereafter, a heat transfer pad was produced in the same manner as in Example 1 described above.

  The total amount of pentadecane injected was 5 ml. On the other hand, when the bulk volume of 75 g of the copper powder was measured using a 50 ml graduated cylinder, it was 13.75 ml. Therefore, in this case, the amount of the heat transfer liquid (pentadecane) added to the heat transfer powder (copper powder) is about 36 (= (5 / 13.75) × 100) volume% in volume ratio.

Example 5
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a particle size of 0.3 mm indicated by the manufacturer was weighed using the electronic scale and transferred into a B-4 plastic bag. Thereafter, a heat transfer pad (left side in FIG. 9) was produced in the same manner as in Example 1 described above.

  The total amount of pentadecane injected was 5 ml. On the other hand, when the bulk volume of 75 g of the copper powder was measured using a 50 ml graduated cylinder, it was 14.25 ml. Therefore, in this case, the addition amount of the heat transfer liquid (pentadecane) to the heat transfer powder (copper powder) is about 35 (= (5 / 14.25) × 100) volume% in volume ratio.

Example 6
75 g of copper powder (manufactured by Hikari Kogyo Kogyo Co., Ltd., purity 99.9 w%) having a particle size of 53 to 150 μm (0.053 to 0.15 mm) was weighed out using the electronic scale, and B-4 poly Moved into the bag. Thereafter, a heat transfer pad was produced in the same manner as in Example 1 described above.

  The total amount of pentadecane injected was 5 ml. On the other hand, when the bulk volume of 75 g of the copper powder was measured using a 50 ml graduated cylinder, it was 14 ml. Therefore, in this case, the amount of the heat transfer liquid (pentadecane) added to the heat transfer powder (copper powder) is about 36 (= (5/14) × 100) volume% in volume ratio.

  Moreover, the heat-transfer pad which accommodated only any one of heat-transfer powder (copper powder) and a heat-transfer liquid (pentadecane) was produced as follows.

<< Comparative Example 1 >>
A state in which copper powder (manufactured by ECKA Granules Germany GmbH) having a particle size of 0.07 mm is weighed by 75 g using the electronic balance, transferred into a B-4 plastic bag, and air in the bag is removed as much as possible. The final heat transfer pad was sealed.

<< Comparative Example 2 >>
Pentadecane (C ₁₅ H ₃₂ ) (Wako Pure Chemical Industries, Ltd., Wako Special Grade) is weighed in 20 ml using the pipette, transferred to a B-4 plastic bag, and with the air in the bag removed as much as possible. Sealing was performed to obtain a final heat transfer pad.

  Moreover, the heat-transfer pad which accommodated the heat-transfer liquid which solidifies at a temperature higher than pentadecane was produced as follows.

Example 7
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-specified particle size of 0.07 mm was weighed out using the electronic balance and transferred into a B-4 plastic bag. Next, hexadecane (C ₁₆ H ₃₄ ) (manufactured by Wako Pure Chemical Industries, Ltd., Wako Special Grade) was added dropwise with 0.5 ml of the pipette while slowly acclimatizing, and the liquid level was visually observed on the copper powder surface. Then, 0.5 ml was added. Air bubbles in the prepared heat transfer pad were sufficiently removed by vibration or the like, and sealed with the air in the bag removed as much as possible to obtain a final heat transfer pad.

  The total amount of hexadecane injected was 5 ml. On the other hand, as described above, since the bulk volume of the copper powder 75 g is 14 ml, in this case, the addition amount of the heat transfer liquid (hexadecane) to the heat transfer powder (Cu) is about 36 (= (5/14) × 100) capacity%.

  In addition, a heat transfer pad containing a heat transfer liquid that was not yet solidified at the target temperature (the solidification temperature was lower than the target temperature) was prepared as follows.

<< Comparative Example 3 >>
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-specified particle size of 0.07 mm was weighed out using the electronic balance and transferred into a B-4 plastic bag. Next, silicone oil (AZ silicone oil manufactured by AZET Co., Ltd.) was added dropwise using the pipette while gradually acclimatizing 0.5 ml, and the liquid level was confirmed visually on the surface of the copper powder. After that, another 0.5 ml was added. Air bubbles in the prepared heat transfer pad were sufficiently removed by vibration or the like, and sealed with the air in the bag removed as much as possible to obtain a final heat transfer pad.

  The total amount of silicone oil injected was 5 ml. On the other hand, as described above, the bulk volume of the copper powder 75 g is 14 ml. In this case, the amount of heat transfer liquid (silicone oil) added to the heat transfer powder (Cu) is about 36 (volume ratio). = (5/14) x 100) Capacity%.

<< Comparative Example 4 >>
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a particle size of 0.3 mm indicated by the manufacturer was weighed using the electronic scale and transferred into a B-4 plastic bag. Thereafter, a heat transfer pad was produced in the same manner as in Comparative Example 3 described above.

  The total amount of silicone oil injected was 5 ml. On the other hand, as described above, since the bulk volume of the copper powder 75 g is 14.25 ml, in this case, the addition amount of the heat transfer liquid (silicone oil) to the heat transfer powder (copper powder) is a volume ratio, About 35 (= (5 / 14.25) × 100) volume%.

  Moreover, the heat-transfer pad which accommodated the heat-transfer powder (metal powder) from which heat conductivity differs from copper (Cu) was produced as follows.

Example 8
35 g of aluminum (Al) powder (manufactured by Hikari Material Industries Co., Ltd., purity 99.7 w%) having a particle size of ˜150 μm (˜0.15 mm) is weighed using the electronic scale, and a B-4 plastic bag Moved in. Thereafter, a heat transfer pad was produced in the same manner as in Example 1 described above.

  The total amount of pentadecane injected was 8 ml. On the other hand, when the bulk volume of 35 g of the aluminum powder was measured using a 50 ml graduated cylinder, it was 22 ml. Therefore, in this case, the amount of heat transfer liquid (pentadecane) added to the heat transfer powder (aluminum powder) is about 36 (= (8/22) × 100) volume% in volume ratio.

Example 9
75 g of tin (Sn) powder (manufactured by Hikari Material Industries Co., Ltd.) having a particle size indicated by the manufacturer of ˜150 μm (˜0.15 mm) was weighed using the electronic scale and transferred into a B-4 plastic bag. Thereafter, a heat transfer pad was produced in the same manner as in Example 1 described above.

  The total amount of pentadecane injected was 5.5 ml. On the other hand, when the bulk volume of 75 g of the tin powder was measured using a 50 ml graduated cylinder, it was 16.5 ml. Accordingly, in this case, the amount of heat transfer liquid (pentadecane) added to the heat transfer powder (tin powder) is about 33 (= (5.5 / 16.5) × 100) volume% in volume ratio.

Example 10
Zinc (Zn) powder (manufactured by Hikari Material Industries Co., Ltd.) having a particle size indicated by the manufacturer of ˜53 μm (˜0.053 mm) was weighed by 75 g using the electronic balance and transferred into a B-4 plastic bag. Thereafter, a heat transfer pad was produced in the same manner as in Example 1 described above.

  The total amount of pentadecane injected was 7.5 ml. On the other hand, when the bulk volume of 75 g of the zinc powder was measured using a 50 ml graduated cylinder, it was 19.25 ml. Therefore, in this case, the amount of heat transfer liquid (pentadecane) added to the heat transfer powder (zinc powder) is approximately 39 (= (7.5 / 19.25) × 100) volume% in volume ratio.

  In addition, a plurality of types of heat transfer pads having different amounts of heat transfer liquid (pentadecane) were prepared as follows.

Example 11
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-designated particle size of 0.07 mm was weighed using the electronic scale and transferred into a B-4 plastic bag. Next, 1.66 ml of pentadecane (C ₁₅ H ₃₂ ) (manufactured by Wako Pure Chemical Industries, Ltd., Wako Special Grade) was added dropwise using the pipette while slowly acclimatizing, and stirred well to make it uniform. Then, air bubbles in the heat transfer pad were sufficiently removed by vibration or the like, and sealed in a state where air in the bag was removed as much as possible to obtain a final heat transfer pad.

  As described above, since the bulk volume of the copper powder 75 g is 14 ml, in this case, the amount of the heat transfer liquid (pentadecane) added to the heat transfer powder (Cu) is about 12 (= (1.66 / 14) x 100) Capacity%.

Example 12
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-designated particle size of 0.07 mm was weighed using the electronic scale and transferred into a B-4 plastic bag. Next, 3.33 ml of pentadecane (C ₁₅ H ₃₂ ) (manufactured by Wako Pure Chemical Industries, Ltd., Wako Special Grade) was dropped with the above pipette while slowly acclimatizing, and stirred well with a stick to make it uniform. After that, air bubbles in the heat transfer pad were sufficiently removed by vibration or the like, and sealed with the air in the bag removed as much as possible to obtain a final heat transfer pad.

  As described above, since the bulk volume of the copper powder 75 g is 14 ml, in this case, the amount of the heat transfer liquid (pentadecane) added to the heat transfer powder (Cu) is about 24 (= (3.33 / 14) x 100) Capacity%.

Example 13
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-designated particle size of 0.07 mm was weighed using the electronic scale and transferred into a B-4 plastic bag. Next, 3.88 ml of pentadecane (C ₁₅ H ₃₂ ) (manufactured by Wako Pure Chemical Industries, Ltd., Wako Special Grade) was dropped using the pipette while slowly acclimatizing, and stirred well with a stick to make it uniform. After that, air bubbles in the heat transfer pad were sufficiently removed by vibration or the like, and sealed with the air in the bag removed as much as possible to obtain a final heat transfer pad.

  As described above, the bulk volume of the copper powder 75 g is 14 ml. In this case, the amount of the heat transfer liquid (pentadecane) added to the heat transfer powder (Cu) is about 28 (= (3.88 / 14) x 100) Capacity%.

Example 14
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-designated particle size of 0.07 mm was weighed using the electronic scale and transferred into a B-4 plastic bag. Next, 4.44 ml of pentadecane (C ₁₅ H ₃₂ ) (manufactured by Wako Pure Chemical Industries, Ltd., Wako Special Grade) was added dropwise using the pipette while slowly acclimatizing, and stirred well with a stick to make it uniform. After that, air bubbles in the heat transfer pad were sufficiently removed by vibration or the like, and sealed with the air in the bag removed as much as possible to obtain a final heat transfer pad.

  As described above, since the bulk volume of the copper powder 75 g is 14 ml, in this case, the addition amount of the heat transfer liquid (pentadecane) to the heat transfer powder (Cu) is about 32 (= (4.44 / 14) x 100) Capacity%.

Example 15
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-designated particle size of 0.07 mm was weighed using the electronic scale and transferred into a B-4 plastic bag. Next, 6.66 ml of pentadecane (C ₁₅ H ₃₂ ) (manufactured by Wako Pure Chemical Industries, Ltd., Wako Special Grade) is dropped using the pipette while slowly acclimatizing, and the bubbles in the heat transfer pad are vibrated. It was removed sufficiently, etc., and sealed with the air in the bag removed as much as possible to obtain the final heat transfer pad.

  As described above, since the bulk volume of the copper powder 75 g is 14 ml, in this case, the amount of the heat transfer liquid (pentadecane) added to the heat transfer powder (Cu) is about 48 (= (6.66 / 14) x 100) Capacity%.

Example 16
75 g of copper powder (manufactured by ECKA Granules Germany GmbH) having a manufacturer-designated particle size of 0.07 mm was weighed using the electronic scale and transferred into a B-4 plastic bag. Next, 8.33 ml of pentadecane (C ₁₅ H ₃₂ ) (manufactured by Wako Pure Chemical Industries, Ltd., Wako Special Grade) was dropped using the pipette while slowly acclimatizing, and the bubbles in the heat transfer pad were vibrated. It was removed sufficiently, etc., and sealed with the air in the bag removed as much as possible to obtain the final heat transfer pad.

  In addition, since the bulk volume of the said copper powder 75g is 14 ml as mentioned above, in this case, the addition amount of the heat transfer liquid (pentadecane) to the heat transfer powder (Cu) is about 60 (= (8.33 / 14) x 100) Capacity%.

  Next, the cooling performance (heat transfer performance) of each heat transfer pad was measured as follows.

  First, as shown in FIG. 10, the center of the filling portion of the heat transfer pad to be measured is an unopened bottle wine (750 ml) (diameter 72 mm, height 301 mm) shoulder (around 208 mm height from the bottom). After arranging the heat transfer pad so as to be sandwiched between the low temperature part (the heat transfer block of the Peltier unit) of the Peltier cooling tester (having the same structure as the main body part 111 shown in FIG. 1), The bottle wine was pressed against the heat transfer pad and brought into close contact.

  Next, a temperature sensor (thermocouple) was attached to the side surface of the lower part of the bottle wine (height near the bottom 20 mm), and cooling from room temperature was performed while measuring the temperature. And temperature difference (DELTA) T (= T1-T2) of temperature T1 at the time of 10-minute progress after cooling start and temperature T2 at the time of 60-minute progress after cooling start was calculated as a parameter | index of cooling performance (heat transfer performance).

  FIG. 11 is a table showing the measurement results of each heat transfer pad.

  As shown in the figure, in comparison with Comparative Example 1 (copper powder alone) and Comparative Example 2 (pentadecane alone), all of Examples 1 to 16 have relatively high cooling performance (heat transfer performance). Show.

  In comparison with Comparative Examples 3 and 4 (copper powder + silicone oil), Examples 2, 3, 6 to 10, and 12 to 16 show relatively high cooling performance (heat transfer performance), Especially about Example 2, 3, 6-10, 13-16, (DELTA) T is 4.0 or more, and has shown the remarkably high cooling performance (heat-transfer performance).

  From the above results, first, focusing on the particle size of the heat transfer powder, it is considered that if the particle size is about 0.04 mm to 0.16 mm, a significantly high cooling performance (heat transfer performance) can be obtained. It is done.

  Further, when focusing on the amount of heat transfer liquid added to the heat transfer powder, a high cooling performance (heat transfer performance) can be obtained if the volume ratio is 24% by volume or more, and if it is 28% by volume or more. It is considered that remarkably high cooling performance (heat transfer performance) can be obtained. In Examples 15 and 16, precipitation of heat transfer powder (copper powder) occurred in the heat transfer pad, and during the measurement, the portion of the heat transfer powder precipitated was the shoulder of the bottle wine. And the low temperature part of the Peltier cooling tester. Therefore, between Example 15 and Example 16, it is thought that the increase in the heat transfer liquid hardly affects the cooling performance (heat transfer performance). In fact, both have the same cooling performance (heat transfer performance). Performance). From the above, high cooling performance (heat transfer performance) can be obtained if the amount of heat transfer liquid added is about 24 to 48% by volume, and remarkably high cooling performance if it is about 28 to 48% by volume. It is considered that (heat transfer performance) can be obtained.

  Further, when paying attention to the material of the heat transfer powder, a remarkably high cooling performance (heat transfer performance) is obtained for any metal species of copper, aluminum, tin, and zinc. Among these metal species, tin, which has the lowest thermal conductivity, has a thermal conductivity of 66.8 W / m · K. Therefore, as a material for the heat transfer powder, the thermal conductivity is generally 60 W / m · K. It is considered that high cooling performance (heat transfer performance) can be obtained if a material having a temperature of about K or higher is used.

  Further, the cooling performance (heat transfer performance) of the heat transfer pad (Example 3) in a state where the bottle wine was inclined at a predetermined angle was measured as follows.

  First, as shown in FIG. 12, the Peltier-type cooling tester 400 to which a heat transfer plate (80 mm × 250 mm × 5 mm copper plate) 440 is added is inclined by 30 ° from the vertical direction, and then the heat transfer pad of Example 3 is used. Heat transfer pad so that the center of the filling portion of 430 is sandwiched between the shoulder portion of the unopened bottle wine (750 ml) (diameter 72 mm, height 301 mm) (around 208 mm height from the bottom) and the heat transfer plate 440 430 was placed, and the bottle wine was pressed against the heat transfer pad 430 and brought into close contact therewith.

  Next, a temperature sensor (thermocouple) is attached to each of the side surface portion A (a height of about 20 mm from the bottom surface) and B (a height of about 100 mm from the bottom surface) of the lower part of the bottle wine, and the temperature is measured while measuring the temperature. Cooling from the state was performed. And temperature difference (DELTA) T (= T1-T2) of temperature T1 at the time of 10-minute progress after cooling start and temperature T2 at the time of 60-minute progress after cooling start was calculated as a parameter | index of cooling performance (heat transfer performance).

  Similarly, after tilting the Peltier cooling tester 400 by 45 ° and 60 °, the same measurement was performed for each case, and ΔT was calculated.

  FIG. 13 is a table showing the measurement results.

  As shown in the figure, cooling is more effective when the bottle wine is not inclined much (when the inclination angles are 30 ° and 45 °) than when the bottle wine is greatly inclined (when the inclination angle is 60 °). The performance is high.

  In the case of the configuration shown in FIG. 12, it is considered that when the bottle wine is tilted greatly, convection inside the bottle hardly occurs and the cooling efficiency decreases.

DESCRIPTION OF SYMBOLS 1 Bottle wine 100 Wine temperature control apparatus 110 Bottle accommodating part 111 Main body part 112 Cover part 113 Heat insulating material 114 Hinge mechanism 115 Leaf spring 120 Peltier unit 121 Heat transfer block 1211 Upper surface 122 Radiation fin 1221 Rectangular flat plate 1222 Fin 123 Case 1231 Side wall part 1232 Overhang portion 124 Thermoelectric conversion module 125 Tab terminal 126 Lead wire 130 Heat transfer pad 200 Wine temperature control device 230 Heat transfer pad 240 Heat transfer plate 300 Wine temperature control device 331 to 336 Heat transfer pad 400 Peltier cooling test machine 430 Thermal pad 440 Heat transfer plate 610 π-type thermoelectric element 611 n-type semiconductor element 612 p-type semiconductor element 613, 620 Metal electrode 630 Insulating substrate

Claims (19)

A heat transfer member that comes into contact with a part of the side surface of the container-containing beverage to be temperature controlled;
A temperature adjusting unit for adjusting the temperature of the beverage in the container via the heat transfer member;
The heat transfer member is composed of a deformable bag, and heat transfer powder and heat transfer liquid accommodated in the bag,
The container-containing beverage temperature adjusting device, wherein the heat transfer liquid is a liquid that solidifies at a temperature higher than a target temperature. The container-containing beverage temperature adjusting device according to claim 1, further comprising an urging portion for bringing the container-containing beverage and the heat transfer member into contact with each other. The said heat-transfer member contacts the upper part of the said drink in a container, The drink temperature adjustment apparatus in a container of Claim 1 or 2 characterized by the above-mentioned. The said heat-transfer member contact | abuts over the whole region from the upper part to the lower part of the said drink in a container, The drink temperature control apparatus in a container of Claim 1 or 2 characterized by the above-mentioned. A plurality of the heat transfer members;
The said heat-transfer member is arrange | positioned at intervals so that the longitudinal direction of the said drink in a container may be followed, The drink temperature adjustment apparatus in a container of Claim 1 or 2 characterized by the above-mentioned. The container-containing beverage temperature adjustment device according to claim 4 or 5, further comprising a second heat transfer member disposed between the heat transfer member and the temperature adjustment unit. The said 2nd heat-transfer member is comprised with the metal plate, The drink temperature control apparatus with a container of Claim 6 characterized by the above-mentioned. Before starting the temperature control of the beverage in the container, the heat control member is heated by the temperature control unit to melt the solidified heat transfer liquid. The container drink temperature control apparatus as described in any one of Claims. The said heat-transfer powder is comprised with the metal powder, The drink temperature control apparatus with a container as described in any one of Claims 1-8 characterized by the above-mentioned. The said heat-transfer liquid is comprised by either a linear hydrocarbon, a primary alcohol, a linear aldehyde, and a linear carboxylic acid, The Claim 1-9 characterized by the above-mentioned. Container drink temperature control device. 11. The beverage temperature adjusting device in a container according to claim 1, wherein an amount of the heat transfer liquid added to the heat transfer powder is 24% by volume or more in a volume ratio. The amount of the heat-transfer liquid added to the heat-transfer powder is about 28 to 48% by volume in volume ratio. The particle size of the heat transfer powder is in a range of 0.04 mm to 0.16 mm, and the containerized beverage temperature adjusting device according to any one of claims 1 to 12. A heat transfer member used to adjust the temperature of a temperature adjustment object to a target temperature,
A deformable bag, and heat transfer powder and heat transfer liquid contained in the bag,
The heat transfer member is a liquid that solidifies at a temperature higher than the target temperature. The heat transfer member according to claim 14, wherein the heat transfer powder is made of metal powder. The heat transfer member according to claim 14 or 15, wherein the heat transfer liquid is composed of any one of a linear hydrocarbon, a primary alcohol, a linear aldehyde, and a linear carboxylic acid. The heat transfer member according to any one of claims 14 to 16, wherein an addition amount of the heat transfer liquid to the heat transfer powder is 24% by volume or more in volume ratio. The heat transfer member according to any one of claims 14 to 16, wherein an amount of the heat transfer liquid added to the heat transfer powder is about 28 to 48% by volume in volume ratio. The heat transfer member according to any one of claims 14 to 18, wherein a particle size of the heat transfer powder is in a range of 0.04 mm to 0.16 mm.