WO2015059957A1 - Echangeur de chaleur et système d'échange de chaleur - Google Patents

Echangeur de chaleur et système d'échange de chaleur Download PDF

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Publication number
WO2015059957A1
WO2015059957A1 PCT/JP2014/066036 JP2014066036W WO2015059957A1 WO 2015059957 A1 WO2015059957 A1 WO 2015059957A1 JP 2014066036 W JP2014066036 W JP 2014066036W WO 2015059957 A1 WO2015059957 A1 WO 2015059957A1
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WIPO (PCT)
Prior art keywords
flow path
heat exchange
path forming
heat exchanger
exchange liquid
Prior art date
Application number
PCT/JP2014/066036
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English (en)
Japanese (ja)
Inventor
俊範 岡田
高橋　大輔
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シャープ株式会社
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Publication of WO2015059957A1 publication Critical patent/WO2015059957A1/fr

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    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
    • A23C3/00—Preservation of milk or milk preparations
    • A23C3/02—Preservation of milk or milk preparations by heating
    • A23C3/03—Preservation of milk or milk preparations by heating the materials being loose unpacked
    • A23C3/033—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus
    • A23C3/0337—Preservation of milk or milk preparations by heating the materials being loose unpacked and progressively transported through the apparatus the milk flowing through with indirect heat exchange, containing rotating elements, e.g. for improving the heat exchange
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/028—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of at least one medium being helically coiled, the coils having a conical configuration

Definitions

  • the present invention relates to a heat exchanger and a heat exchange system for exchanging heat between fluids, and more particularly to a heat exchanger and a heat exchange system suitable for cooling a high-temperature liquid for beverage with a low-temperature fluid.
  • Patent Document 1 includes holding means for swingably holding the baby bottle in the cooling container, and the baby bottle is swung by swinging the cooling container, whereby the milk in the baby bottle In addition, the refrigerant in the cooling container is agitated by swinging the baby bottle.
  • Patent Document 2 discloses an apparatus that cools hot water by introducing water that has been heated to near the boiling temperature into a pipe that passes through a cooling water tank and cooling it.
  • Patent Document 3 a fluid is allowed to flow on a working surface that exhibits a curvature that substantially matches at least one logarithmic curve according to the “golden section”, and heat is exchanged between the working surface and the fluid. An exchanger is described.
  • the liquid cooling time is shorter than that in the configuration shown in Patent Document 1.
  • it is difficult to remove the pipe through which the liquid flows and clean the inside of the pipe and it is also difficult to visually check the state in the pipe. Therefore, it is difficult to keep beverages such as coffee and tea, not just milk after conditioning.
  • the present invention has been made in view of the above-described problems, and provides a heat exchanger and a heat exchange system that have good heat exchange efficiency and that are easy to clean, disinfect, and check the state of a fluid flow path. It is aimed.
  • a heat exchanger includes a first flow path forming member having a container shape, and the first flow path inside the first flow path forming member.
  • a second flow path-shaped member that is detachably disposed with respect to the path forming member, wherein the first flow path forming member has a diameter of the inner peripheral surface of the container-shaped peripheral wall portion from the upper part to the lower part.
  • a first flow path that gradually decreases and flows the heat exchange liquid is formed in the peripheral wall, and the inner peripheral surface of the first flow path forming member and the outer peripheral surface of the second flow path forming member
  • a spiral second flow path is formed between the inner peripheral surface and the outer peripheral surface to allow the heat exchange liquid to exchange heat with the heat exchange liquid.
  • the heat exchange efficiency is good, and the fluid flow path can be easily cleaned, disinfected, and checked.
  • FIG. 5A is an enlarged view of a portion A shown in FIG. 4
  • FIG. 5B is an enlarged view of a portion B shown in FIG.
  • FIG. 5A is an enlarged view of a portion A shown in FIG. 4
  • FIG. 5B is an enlarged view of a portion B shown in FIG.
  • FIG. 5A is an enlarged view of a portion A shown in FIG. 4
  • FIG. 5B is an enlarged view of a portion B shown in FIG.
  • FIG. 5B is an enlarged view of a portion B shown in FIG.
  • It is a longitudinal cross-sectional view which shows the use condition of the heat exchanger shown in FIG.
  • FIG. 5B is an enlarged view of a portion B shown in FIG.
  • FIG. 1 It is a perspective view containing the longitudinal cross-section of the heat exchanger of further another embodiment of this invention. It is a schematic diagram which shows the structure of the heat exchange system of the other example of the heat exchange system shown in FIG. It is a schematic diagram which shows the structure of the heat exchange system of the further another example of the heat exchange system shown in FIG.
  • FIG. 1 is a schematic diagram showing a configuration of a heat exchange system according to an embodiment of the present invention.
  • the heat exchange system 100 includes a heat exchanger 1, a tank (storage unit) 2, and a pump (supply unit) 3.
  • the heat exchanger 1 performs heat exchange between the heat exchange liquid 130 and the heat exchange liquid 110.
  • the heat exchanger 1 is connected to the tank 2 and the pump 3 respectively.
  • the tank 2 stores the heat exchange liquid 130.
  • the pump 3 sends out the heat exchange liquid 130 stored in the tank 2 to the heat exchanger 1.
  • the heat exchange liquid 130 circulates through the tank 2, the pump 3 and the heat exchanger 1. Specifically, the heat exchange liquid 130 is sent from the tank 2 to the heat exchanger 1 by the pump 3, passes through the flow path disposed in the heat exchanger 1, and the heat exchange liquid 110. After heat exchange, it is returned to the tank 2.
  • a heat exchange liquid outlet 4 is disposed at the top of the heat exchanger 1, and a heat exchange liquid 110 that receives heat exchange from the heat exchange liquid outlet 4 is poured into the heat exchanger 1.
  • the heat exchanger 1 has a flow path for flowing the heat exchange liquid 110 poured from above.
  • the heat exchange liquid 110 flows down from the top to the bottom in the flow path of the heat exchanger 1, and during this time, heat exchange between the heat exchange liquid 130 and the heat exchange liquid 110 is performed. Thereafter, the heat exchange liquid 110 flows out of the heat exchanger 1 and is poured into the cup 5. If the heat exchange liquid 110 is milk for infants, a baby bottle may be placed directly instead of the cup 5.
  • the heat exchange amount with respect to the heat exchange liquid 110 in the heat exchanger 1 can be changed.
  • the temperature of the to-be-heated liquid 110 flowing out from the heat exchanger 1 can be adjusted.
  • the temperature of the heat exchange liquid 110 changes in a direction approaching the temperature of the heat exchange liquid 130
  • the flow rate is reduced, the temperature changes in a direction away from the heat exchange liquid 110.
  • the high-temperature heat exchange liquid 110 with the low-temperature heat exchange liquid 130 when the feed flow rate of the heat exchange liquid 130 is increased, the heat exchange flowing out from the heat exchanger 1 is performed.
  • the temperature of the liquid 110 decreases.
  • the feed flow rate of the heat exchange liquid 130 is decreased, the temperature of the heat exchange liquid 110 flowing out of the heat exchanger 1 increases.
  • FIG. 2 is a perspective view showing the appearance of the heat exchanger 1.
  • FIG. 3 is an exploded perspective view of the heat exchanger 1 shown in FIG.
  • FIG. 4 is a perspective view including a longitudinal section of the heat exchanger 1 shown in FIG.
  • FIG. 5A is an enlarged view of a portion A shown in FIG. 4
  • FIG. 5B is an enlarged view of a portion B shown in FIG.
  • the heat exchanger 1 includes, as main components, a flow path forming first member (flow path forming inner member) 11, a flow path forming second member 12, and a flow path forming third member (flow path forming).
  • the flow path forming first to third members 11 to 13 have a substantially conical shape, are arranged with the bottom surface of the conical shape facing up, and have a container shape with the bottom surface opened. This shape is substantially the same as the conical portion of the funnel, for example.
  • the flow path forming second member 12 is disposed on the inner surface (inside) of the flow path forming first member 11, and the flow path forming third member 13 is disposed on the outer surface of the flow path forming first member 11. That is, the heat exchanger 1 arranges the flow path forming first member 11 in the flow path forming third member 13, arranges the flow path forming second member 12 in the flow path forming first member 11, These flow path forming first to third members 11 to 13 are formed by overlapping them.
  • the central axis of the conical portion is shown as the Z axis, and the axes orthogonal to the central axis (Z axis) of the conical portion are shown as the X axis and Y axis, respectively.
  • the flow path forming first member 11 has a conical portion 111 and a flange portion 112 which are main body portions.
  • the flange portion 112 is formed horizontally (perpendicular to the Z axis) around the conical portion 111 at the upper end portion of the conical portion 111.
  • a lower end opening 113 is formed at the lower end of the flow path forming first member 11.
  • the flow path forming first member 11 is formed, for example, by press molding a thin metal plate.
  • a cheap and corrosion-resistant metal for example, SUS
  • SUS stainless steel
  • it is a metal member, its heat conductivity is higher than that of the resin molding material, and the heat exchange efficiency between the heat exchange liquid 110 and the heat exchange liquid 130 can be improved.
  • the flow path forming second member 12 has a conical part 121 which is a main body part, and a processing liquid receiving part 123.
  • a spiral groove 122 having a V-shaped recess with respect to the outer peripheral surface is formed from the upper part to the lower part.
  • the V-shaped spiral groove 122 has a first inner surface extending substantially horizontally from the groove bottom (V-shaped valley bottom) and a second inner surface extending from the groove bottom (V-shaped valley bottom). This is a shape extending downward at an angle of 90 degrees or more with respect to the inner surface of one. This also applies to the other embodiments described below.
  • the spiral groove 122 is formed on the outer peripheral surface of the conical portion 121, the inner surface of the flow path forming first member 11 can be obtained when the flow path forming second member 12 is disposed on the inner surface of the flow path forming first member 11.
  • a second channel 114 having a spiral shape is formed between the outer surface of the channel-forming second member 12.
  • the second flow path 114 is a flow path through which the heat exchange liquid 110 flows.
  • the lower end of the flow path forming second member 12 has a closed structure, and the lower end of the flow path forming second member 12 in a state where the flow path forming second member 12 is disposed on the inner surface of the flow path forming first member 11.
  • a gap having a predetermined height is formed between the lower surface of the first member 11 and the upper surface of the lower end of the flow path forming first member 11.
  • the treatment liquid receiving portion 123 is formed in an annular groove shape on the outer peripheral portion of the upper end portion of the conical portion 121.
  • a liquid inlet 124 is formed on the bottom surface of the processing liquid receiving portion 123.
  • the flow path forming second member 12 is formed, for example, by resin molding using a mold.
  • the flow path forming second member 12 includes the spiral groove 122 and has a shape in which an undercut is not generated in the vertical direction (Z-axis direction) with respect to the XY plane and a draft is easily provided.
  • the flow path forming second member 12 can be easily manufactured at low cost when manufactured by resin molding.
  • the flow path forming third member 13 has a conical portion 136 and a flange portion 135 which are main body portions.
  • the collar portion 135 is formed horizontally (perpendicular to the Z axis) around the conical portion 136 at the upper end portion of the conical portion 136.
  • a lower end opening 133 is formed at the lower end of the flow path forming first member 11.
  • the lower surface of the lower end portion of the flow path forming first member 11 is on the upper surface of the lower end portion of the flow path forming third member 13. Be placed. Specifically, as shown in FIG. 5B, an O-ring 18 is provided around the lower end opening 113 of the flow path forming third member 13, and the lower end of the flow path forming first member 11. The lower surface of the part is disposed on the O-ring 18.
  • a first flow path 134 is formed between the inner peripheral surface of the conical portion 136 of the flow path forming third member 13 and the outer peripheral surface of the conical portion 111 of the flow path forming first member 11.
  • the first flow path 134 is a flow path through which the heat exchange liquid 130 flows.
  • a liquid inlet 131 and a liquid outlet 132 connected to the first flow path 134 are formed on the outer surface of the conical portion 136 of the flow path forming third member 13.
  • the liquid inlet 131 is an inlet of the first flow path 134 of the heat exchange liquid 130 supplied by the pump 3, that is, the heat exchanger 1.
  • the liquid outlet 132 is an outlet for the heat exchange liquid 130 discharged from the first flow path 134, that is, the heat exchanger 1.
  • the liquid inlet 131 is provided near the lower end portion of the conical portion 136, and the liquid outlet 132 is provided near the upper end portion of the conical portion 136.
  • the seal member 14 has a thin flat ring shape, and is disposed between the flange 135 of the flow path forming third member 13 and the flange 112 of the flow path forming first member 11.
  • the collar part 135 and the collar part 112 are fixed to each other by a fixing member (not shown). With such a configuration, the position of the upper end portion of the first flow path 134, that is, the positions of both flange portions 135 and 112 are sealed.
  • the fastening first member 15 has a male screw shape having a head, and a through hole reaching the lower end from the upper end to the center is formed. This through hole serves as a discharge port 17 for the heat exchange liquid 110 from the second flow path 114.
  • the fastening first member 15 has a head disposed on the upper surface of the lower end portion of the flow path forming first member 11, and a male screw portion of the lower end opening 113 of the flow path forming first member 11 and the flow path forming third member 13. It arrange
  • the fastening second member 16 is a female screw, and is fastened to the male screw portion of the fastening first member 15 protruding from the lower end opening 133 of the flow path forming third member 13. Therefore, the lower ends of the flow path forming first member 11 and the flow path forming third member 13 are fastened together via the O-ring 18 by the fastening first member 15 and the fastening second member 16. Thereby, the position of the lower end part in the 1st flow path 134, ie, the position of the lower end part of the flow path formation 1st member 11, and the lower end part of the flow path formation 3rd member 13, is sealed.
  • the first flow path 134 formed by combining the flow path forming first member 11 and the flow path forming third member 13 is appropriately sealed at the upper end portion and the lower end portion. A situation in which the heat exchange liquid 130 in the flow path 134 leaks or a situation in which the heat exchange liquid 130 is mixed with the heat exchange liquid 110 in the second flow path 114 is reliably prevented.
  • the heat exchanger 1 is for treating milk for infants or liquid for beverages as the heat exchange liquid 110, it is handled so that there is no problem in terms of hygiene. Therefore, before use or after use, it is usually washed with a detergent or the like and then boiled or disinfected with a chemical solution. Disinfectant containing sodium hypochlorite is often used as a chemical solution, and is usually used diluted to about 0.0125%.
  • the material of the heat exchanger 1 is preferably a material having high thermal conductivity, and metal, particularly aluminum or copper-based material is optimal.
  • the heat exchanger 1 is made of a metal material, it is molded by casting, die casting, or the like, and then the surface is coated with a fluorine paint or the like to impart corrosion resistance.
  • the above-mentioned sodium hypochlorite contained in the disinfectant is corrosive to metals, and therefore it is necessary to perform a special coating on the heat exchanger 1. This is because pores are formed in the normal coating, and the heat exchanger 1 is eroded from the pores. Thus, when performing special coating with respect to the heat exchanger 1, the manufacturing cost of the heat exchanger 1 becomes very expensive.
  • the flow path forming first member 11 is in direct contact with the heat exchange liquid 110 and the heat exchange liquid 130. Therefore, producing the flow path forming first member 11 with metal is most efficient in improving the heat exchange efficiency.
  • the surface area where the heat exchange liquid 110 and the heat exchange liquid 130 are in contact with each other is increased. Is preferred.
  • the press molding if the flow path forming first to third members 11 to 13 are complicated, the mold becomes expensive, leading to an increase in cost.
  • the flow path of the second flow path 114 through which the heat exchange liquid 110 flows in order to improve the heat exchange efficiency between the heat exchange liquid 110 and the heat exchange liquid 130, the flow path of the second flow path 114 through which the heat exchange liquid 110 flows.
  • the length is long. Specifically, the flow path length of the heat exchange liquid 110 is increased by making the second flow path 114 spiral.
  • the flow path forming second member 12 is formed of metal, like the flow path forming first member 11, from the viewpoint of improving the heat exchange efficiency.
  • the main role of the flow path forming second member 12 is to lengthen the second flow path 114 through which the heat exchange liquid 110 flows, the flow path forming second member 12 is made of a resin having low thermal conductivity. Even if it forms, the performance fall of the heat exchanger 1 can be decreased.
  • FIG. 6 is a vertical cross-sectional view showing the usage state of the heat exchanger 1.
  • the heat exchange liquid 110 When the heat exchange liquid 110 is poured from the heat exchange liquid outlet 4 (see FIG. 1) into the processing liquid receiving portion 123 of the heat exchanger 1, the heat exchange liquid 110 becomes a liquid inlet of the processing liquid receiving portion 123. It flows into the second flow path 114 via 124. The heat exchange liquid 110 flowing into the second flow path 114 flows from the upper part to the lower part of the heat exchanger 1 along the spiral second flow path 114. Thereafter, the heat exchange liquid 110 is discharged from the discharge port 17 at the lower end of the heat exchanger 1 and poured into the cup 5 (see FIG. 1).
  • the heat exchange liquid 130 is sent from the tank 2 to the heat exchanger 1 by the pump 3.
  • the heat exchange liquid 130 flows into the first flow path 134 from the liquid inlet 131 at the bottom of the heat exchanger 1, and is discharged out of the first flow path 134 from the liquid outlet 132 at the top of the heat exchanger 1. , Returned to the tank 2.
  • the heat exchange liquid 110 is heat exchanged with the heat exchange liquid 130 flowing through the first flow path 134 while flowing through the second flow path 114.
  • the second flow path 114 is formed in a spiral shape, and the flow path length is long.
  • the area where the heat exchange liquid 110 contacts the flow path forming first member 11 increases per flow rate of the second flow path 114. That is, the area where the heat exchange liquid 110 comes into contact with the heat exchange liquid 130 in the second flow path 134 via the flow path forming first member 11 increases per flow rate of the second flow path 114.
  • the efficiency of heat exchange between the heat exchange liquid 110 and the heat exchange liquid 130 is improved.
  • a fixing base having an insertion port at the liquid inlet 131 and the liquid outlet 132
  • the heat exchanger 1 and the pipe passing through the heat exchange liquid can be easily inserted and removed.
  • piping such as a silicone tube may be fixed with a hose band or the like.
  • the flow path forming first member 11, the flow path forming second member 12, and the flow path forming third member 13 can be easily disassembled. Therefore, the flow path forming second member 12 is removed from the flow path forming first member 11, and the conical portion 111 can be easily cleaned, disinfected, and checked for conditions (particularly, checking for sanitary problems). it can. Thereby, hygiene management of the flow path through which the heat exchange liquid 110 flows is easy. Further, by removing the flow path forming third member 13, it is possible to easily clean the first flow path 134 through which the heat exchange liquid 130 flows and to check the state of the first flow path 134.
  • the manufacturing cost can be reduced.
  • the liquid inlet 131 is provided at the lower part, and the liquid outlet 132 is provided at the upper part.
  • the liquid inlet 131 is provided at the lower part, and the liquid outlet 132 is provided at the upper part.
  • the positional relationship between the liquid inlet 131 and the liquid outlet 132 is not limited to this, and the liquid inlet 131 may be provided at the upper part and the liquid outlet 132 may be provided at the lower part.
  • the shape of the flow path forming first to third members 11 to 13 that form the first flow path 134 and the second flow path 114 is not limited to a conical shape.
  • the second flow path 114 only needs to be formed in a spiral shape whose diameter gradually decreases from the upper part toward the lower part, and the flow path forming first member 11 and the flow path forming second member 12 have such a shape.
  • the channel forming third member 13 that can form the second channel 114 may have a shape corresponding to the channel forming first member 11. The same applies to the heat exchangers of other embodiments described later.
  • the heat exchange liquid 110 is not limited to milk, and may be any liquid such as a beverage liquid.
  • the heat exchange liquid 130 is not limited to water, and may be any liquid.
  • any gas may be used as the heat exchange fluid.
  • the heat exchange liquid 130 does not come into contact with anything that directly touches the human mouth, such as the heat exchange liquid 130.
  • miscellaneous bacteria and the like may move from the first flow path 134 of the heat exchange liquid 130 to the second flow path 114 of the heat exchange liquid 110. Therefore, it is preferable to use a heat exchange liquid 130 that does not have a sanitary problem.
  • the heat exchanger 1 is described as cooling the heat exchange liquid 110 with the heat exchange liquid 130, but the heat exchange liquid 110 is heated by the heat exchange liquid 130. There may be.
  • FIG. 7 is a perspective view including a longitudinal section of the heat exchanger 201 according to the embodiment of the present invention.
  • the heat exchanger 201 includes a flow path forming second member 211 instead of the flow path forming second member 12 of the heat exchanger 1 shown in FIG. Similar to the flow path forming second member 12, the flow path forming second member 211 has a spiral groove 212 having a V-shaped cross section formed on the outer peripheral surface (side surface) of the conical portion 121 from the upper part to the lower part. However, in the spiral groove 212, the width of the groove gradually increases and the depth of the groove increases from the top to the bottom.
  • the inner surface of the flow path forming first member 11 can be obtained when the flow path forming second member 211 is disposed on the inner surface of the flow path forming first member 11.
  • a spiral second channel 213 through which the heat exchange liquid 110 flows is formed between the second channel 211 and the outer surface of the channel forming second member 211.
  • the second channel 213 has the spiral groove 212 formed as described above, so that the channel length for one round is gradually shorter from the upstream side (upper part) where the channel length for one cycle is long.
  • the size of the flow path (allowable flow rate of the heat exchange liquid 110 in the flow path) gradually increases toward the downstream side (lower part).
  • the liquid level of the heat exchange liquid 110 rises to the upper side of the second flow path 213. Is likely to occur. In this case, the substantial flow path length of the 2nd flow path 213 becomes short, and the heat exchange efficiency in the heat exchanger 201 falls.
  • the size of the second flow path 213 (allowable flow rate of the heat exchange liquid 110 in the flow path) gradually increases from the upstream side toward the downstream side. Therefore, the amount of the second flow path 213 that can hold the heat exchange liquid 110 on the downstream side increases, and therefore the liquid level of the heat exchange liquid 110 is unlikely to rise. As a result, the channel length of the heat exchange liquid 110 in the second channel 213 can be ensured, and a decrease in heat exchange efficiency can be suppressed.
  • FIG. 8 is a perspective view including a longitudinal section of the heat exchanger 202 according to the embodiment of the present invention.
  • the heat exchanger 202 includes a flow path forming second member 221 instead of the flow path forming second member 12 of the heat exchanger 1 shown in FIG.
  • the flow path forming second member 221 has a lower end opening 222 formed at the lower end.
  • a lower end opening 222 is formed at the lower end of the flow path forming second member 221. Therefore, the amount of the heat exchange liquid 110 that exceeds the amount that can be discharged from the discharge port 17 can flow into the region inside the flow path forming second member 221 from the lower end opening 222, and the second flow path 114. Then, the liquid level of the heat exchange liquid 110 becomes difficult to rise. As a result, the channel length of the heat exchange liquid 110 in the second channel 114 can be ensured, and a decrease in heat exchange efficiency can be suppressed.
  • the configuration of the present embodiment is naturally applicable not only to the heat exchanger 1 (see FIG. 4) but also to the heat exchanger 201 (see FIG. 7).
  • the flow path forming second member 12 has a container shape. Such a configuration is preferable for reducing the weight of the heat exchanger 1, facilitating manufacturing, and reducing material costs.
  • the flow path forming second member 12 is not limited to the container shape.
  • the flow path forming second member 12 may have a structure in which the upper surface of the conical portion 121 is closed.
  • the flow path forming second member 12 may have a structure in which members are packed inside the conical portion 121 (a structure in which the inside is not a cavity). That is, the flow path forming second member 12 forms the flow path forming first member 11 together with the flow path forming first member 11, and the second flow path 114 can be easily cleaned, disinfected, and checked. Any material that can be easily removed from the flow path forming first member 11 may be used.
  • the heat exchanger 1 shown in FIG. 4 is not limited to the configuration including the flow path forming first to third members 11 to 13.
  • the first flow path forming first member 11 and the flow path forming third member 13 are integrated.
  • the flow path forming member may be provided.
  • a container-shaped first flow path forming member is provided, and the first flow path is formed in the peripheral wall of the first flow path forming member. 134 is formed, the flow path forming second member 12 is detachably disposed on the inner surface of the flow path forming member, and the first flow path forming member and the flow path forming second member (second flow path forming member) 12 are disposed.
  • the 2nd flow path 114 may be formed between these.
  • the above configuration can be similarly applied to the other heat exchangers 201 and 202.
  • the second flow path 114 is used as the flow path for the heat exchange liquid 110 and the first flow path 134 is used as the flow path for the heat exchange liquid 130.
  • the present invention is not limited to this. That is, the second flow path 114 may be the flow path of the heat exchange liquid 130 and the first flow path may be the flow path of the heat exchange liquid 110.
  • FIG. 9 is a schematic diagram illustrating a configuration of a heat exchange system 101 according to a modification of the heat exchange system 100.
  • a heat exchange system 101 shown in FIG. 9 is different from the heat exchange system 100 shown in FIG. 1 in that an auxiliary cooling mechanism 6 is installed in the tank 2.
  • the auxiliary cooling mechanism 6 is an air cooling mechanism using a fan, a cooling mechanism using a Peltier element, a heat dissipation mechanism including fins, or the like.
  • the temperature of the heat exchange liquid 130 increases due to heat exchange with the heat exchange liquid 110.
  • the amount of the heat exchange liquid 110 is large (relative to the heat exchange liquid 130) or the temperature of the heat exchange liquid 110 is very high, the temperature of the heat exchange liquid 130 increases. Will grow.
  • the temperature of the heat exchange liquid 130 rises, the temperature difference from the heat exchange liquid 110 becomes smaller, and the amount of heat exchange decreases.
  • the heat exchange liquid 130 stored in the tank 2 is cooled by the auxiliary cooling mechanism 6, the temperature of the heat exchange liquid 130 that has risen due to the heat exchange can be efficiently reduced. Thereby, the temperature of the heat exchange liquid 130 can be maintained at a low temperature, and a decrease in the heat exchange amount can be suppressed. Furthermore, the amount of the heat exchange liquid 130 as cooling water stored in the tank 2 can be reduced.
  • FIG. 10 is a schematic diagram illustrating a configuration of a heat exchange system 102 according to another modification of the heat exchange system 100.
  • a heat exchanging system 102 shown in FIG. 10 is different from the heat exchanging system 100 shown in FIG.
  • the heat exchange system 102 in this case warms the low-temperature heat exchange liquid 110 using the high-temperature heat exchange liquid 130.
  • Refrigerating liquid stored in a refrigerator or the like is generally heated by a microwave oven.
  • heating by a microwave oven is non-uniform and a hot hot spot is locally generated.
  • heating by the heat exchange system 102 is suitable.
  • the heat exchanger shown in each example can adjust the temperature of the heat exchange liquid (particularly cooling the milk after milk preparation) to an appropriate temperature in a sanitary manner in a short time. it can. Furthermore, since the heat exchanger has a simple structure, it can be manufactured at low cost. In addition, it is possible to cool and warm hygienic beverages, in particular, to cool hot milk after preparation to an appropriate temperature. For this reason, the troublesome operation
  • the heat exchanger according to the first aspect of the present invention includes a first flow path forming member (a flow path forming first member 11 and a flow path forming third member 13) having a container shape, and the first flow path forming member. And a second flow path-shaped member (flow path forming second members 12, 211, 221) disposed detachably with respect to the first flow path forming member.
  • the path forming member has a diameter of the inner peripheral surface of the container-shaped peripheral wall portion that gradually decreases from the top to the bottom, and a first flow path 134 through which the heat exchange liquid 130 flows is formed in the peripheral wall portion.
  • the heat exchange liquid 130 is exchanged by the inner peripheral surface and the outer peripheral surface.
  • a spiral second flow path 114 through which the heat exchange liquid 110 flows is formed.
  • the first flow path forming member is disposed inside the first flow path forming member.
  • the spiral second flow path 114 can be easily formed between the inner peripheral surface of the first flow path forming member and the outer peripheral surface of the second flow path forming member. Can be formed.
  • the second flow path 114 formed in this way has a diameter that gradually decreases from the upper part (upstream side) to the lower part (downstream side).
  • the second flow path 114 is formed in a spiral shape and has a long flow path length, the heat exchange liquid 110 that flows through the second flow path 114 and the heat exchange liquid 130 that flows through the first flow path 134 The heat exchange efficiency is improved.
  • the second flow path member is detachably disposed with respect to the first flow path forming member, the second flow path member can be removed by washing the second flow path 114, Disinfection and status check can be easily performed.
  • the first flow path forming member (the flow path forming first member 11 and the flow path forming third member 13) is the second flow path 114.
  • a discharge port 17 for discharging the heat exchange liquid 110 from the bottom is formed at the lower end, and the second flow path forming member (flow path forming second member 12) has a container shape and has an opening at the lower end. (Lower end opening 222) is formed.
  • the excess heat exchange liquid 110 is transferred to the heat exchanger. It will accumulate in the lower part of 202.
  • the liquid level of the heat exchange liquid 110 may rise to the upper side (upstream side) of the second flow path 114. It is likely to occur. In this case, the substantial flow path length of the 2nd flow path 114 becomes short, and the heat exchange efficiency in the heat exchanger 202 falls.
  • the heat exchange liquid 110 that exceeds the amount that can be discharged from the discharge port 17 can flow into the region inside the second flow path forming member from the opening of the second flow path forming member.
  • the liquid level of the heat exchange liquid 110 is difficult to rise. As a result, the channel length of the heat exchange liquid 110 in the second channel 114 can be ensured, and a decrease in heat exchange efficiency can be suppressed.
  • the first flow path forming member includes a flow path forming inner member (flow path forming first member 11) and a flow path forming outer member ( A flow path forming third member 13) between the outer peripheral surface of the flow path forming inner member and the inner peripheral surface of the flow path forming outer member by the inner peripheral surface and the outer peripheral surface.
  • a flow path 134 is formed, and between the inner peripheral surface of the flow path forming inner member and the outer peripheral surface of the second flow path forming member (flow path forming second member 12), these inner peripheral surface and outer periphery
  • the second flow path 114 is formed by the surface.
  • the first flow path forming member includes the flow path forming inner member and the flow path forming outer member that form the second flow path 114. It can be formed by press molding a thin metal plate having high thermal conductivity. In this case, a metal material that is inexpensive and has corrosion resistance to the disinfectant in the second flow path 114 can be used as the material for the flow path forming inner member. In this case, the heat exchange efficiency between the heat exchange liquid 110 in the second flow path 114 and the heat exchange liquid 130 in the first flow path 134 can be improved.
  • the heat exchanger according to aspect 4 of the present invention is the heat exchanger according to any one of the aspects 1 to 3, wherein the first flow path forming member (the flow path forming first member 11 and the flow path forming third member 13) is A discharge port 17 for discharging the heat exchange liquid 110 from the second channel 213 is formed at the lower end, and the size of the channel of the second channel 213 gradually increases from the top to the bottom. ing.
  • the heat exchanger 201 when the amount of the heat exchange liquid 110 supplied to the second flow path 213 exceeds the amount that can be discharged from the discharge port 17, the excess heat exchange is performed.
  • the liquid 110 accumulates in the lower part of the heat exchanger.
  • the liquid surface of the heat exchange liquid 110 is on the upper side of the second flow path 213 ( It is easy to get up to the upstream). In this case, the substantial flow path length of the 2nd flow path 213 becomes short, and the heat exchange efficiency in a heat exchanger falls.
  • the size of the second flow path 213 gradually increases from the upper part (upstream side) to the lower part (downstream side). Therefore, the amount of the second flow path 213 that can hold the heat exchange liquid 110 on the downstream side increases, and therefore the liquid level of the heat exchange liquid 110 is unlikely to rise. As a result, the channel length of the heat exchange liquid 110 in the second channel 213 can be ensured, and a decrease in heat exchange efficiency can be suppressed.
  • a heat exchanger according to Aspect 5 of the present invention is a heat exchanger 1, 201, 202 according to any one of Aspects 1 to 4, a storage unit (tank 2) for storing the heat exchange liquid 130, and A supply unit (pump 3) for supplying the heat exchange liquid 130 from the storage unit to the heat exchangers 1, 201, 202;
  • the present invention can be used for cooling and heating hygienic beverages, in particular, cooling high-temperature milk after milk preparation to an appropriate temperature.

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Medical Preparation Storing Or Oral Administration Devices (AREA)

Abstract

La présente invention concerne un échangeur de chaleur et un système d'échange de chaleur qui présentent une efficacité d'échange de chaleur satisfaisante, permettent de nettoyer un passage de fluide, se stérilisent facilement et permettent aux conditions de celui-ci d'être facilement confirmées. Un échangeur de chaleur est doté d'un premier élément (11, 13) de formation de passage d'écoulement ayant la forme d'un récipient ; et d'un second élément (12) de formation de passage d'écoulement disposé sur l'intérieur du premier élément (11, 13) de formation de passage d'écoulement afin que le second élément (12) de formation de passage d'écoulement puisse être monté et démonté à partir du premier élément (11, 13) de formation de passage d'écoulement. Le premier élément (11, 13) de formation de passage d'écoulement de l'échangeur (1) de chaleur est conçu de telle manière que : le diamètre de la surface périphérique intérieure de la section de paroi périphérique de la forme de récipient décroisse graduellement à partir de la partie supérieure en direction de la partie inférieure ; un premier passage (134) d'écoulement, à travers lequel le liquide d'échange de chaleur s'écoule, soit formé à l'intérieur de la section de paroi périphérique ; et un second passage (114) hélicoïdal d'écoulement, à travers lequel le liquide devant être soumis à l'échange de chaleur s'écoule, soit formé entre la surface périphérique intérieure du premier élément (11, 13) de formation de passage d'écoulement et la surface périphérique extérieure du second élément (12) de formation de passage d'écoulement.
PCT/JP2014/066036 2013-10-22 2014-06-17 Echangeur de chaleur et système d'échange de chaleur WO2015059957A1 (fr)

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JP2013-219469 2013-10-22
JP2013219469A JP2015081716A (ja) 2013-10-22 2013-10-22 熱交換器および熱交換システム

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Cited By (1)

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TWI619919B (zh) * 2017-11-30 2018-04-01 英業達股份有限公司 散熱排

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20230020370A1 (en) 2019-12-20 2023-01-19 M. Technique Co., Ltd. Heat exchanger
WO2021131006A1 (fr) 2019-12-26 2021-07-01 エム・テクニック株式会社 Réacteur en écoulement
JP6813233B1 (ja) 2019-12-26 2021-01-13 エム・テクニック株式会社 熱交換器

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JPS57500706A (fr) * 1980-05-27 1982-04-22
JPS5814817U (ja) * 1981-07-20 1983-01-29 三菱アルミニウム株式会社 液体飲料用簡易熱交換器
JPH0677839U (ja) * 1993-04-07 1994-11-01 森永乳業株式会社 分離機能を有する粉体熱交換器
JPH1118944A (ja) * 1997-07-02 1999-01-26 Orion Mach Co Ltd 調理装置
JP2013130391A (ja) * 2013-03-19 2013-07-04 Sanoh Industrial Co Ltd 熱交換器

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JPS58434Y2 (ja) * 1980-08-21 1983-01-06 禎美 伊藤 ドリツプ式アイスコ−ヒ−入れ器
JPS607628Y2 (ja) * 1982-08-10 1985-03-14 圭一 薮野 アイスコ−ヒ−・アイス紅茶用冷却具
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JPS57500706A (fr) * 1980-05-27 1982-04-22
JPS5814817U (ja) * 1981-07-20 1983-01-29 三菱アルミニウム株式会社 液体飲料用簡易熱交換器
JPH0677839U (ja) * 1993-04-07 1994-11-01 森永乳業株式会社 分離機能を有する粉体熱交換器
JPH1118944A (ja) * 1997-07-02 1999-01-26 Orion Mach Co Ltd 調理装置
JP2013130391A (ja) * 2013-03-19 2013-07-04 Sanoh Industrial Co Ltd 熱交換器

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI619919B (zh) * 2017-11-30 2018-04-01 英業達股份有限公司 散熱排

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