WO2011024371A1 - Evaporative cooling device - Google Patents

Evaporative cooling device Download PDF

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Publication number
WO2011024371A1
WO2011024371A1 PCT/JP2010/004387 JP2010004387W WO2011024371A1 WO 2011024371 A1 WO2011024371 A1 WO 2011024371A1 JP 2010004387 W JP2010004387 W JP 2010004387W WO 2011024371 A1 WO2011024371 A1 WO 2011024371A1
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Prior art keywords
chamber
space
evaporation chamber
pressure
cooling device
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PCT/JP2010/004387
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French (fr)
Japanese (ja)
Inventor
佐藤祐
元永昇
西村靖史
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株式会社ササクラ
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Priority to CN2010800037913A priority Critical patent/CN102265101A/en
Publication of WO2011024371A1 publication Critical patent/WO2011024371A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B39/00Evaporators; Condensers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D31/00Other cooling or freezing apparatus

Definitions

  • the present invention relates to an evaporative cooling device that performs cooling using evaporation and condensation of a liquid having evaporability such as water.
  • a steam compression refrigerator for example, see Patent Document 1.
  • an evaporator 60 a condenser 62 interconnected to the evaporator 60 by a connecting pipe 61, and the evaporator 60 and the condenser 62.
  • a compressor 64 disposed in a connecting pipe (duct) 63 that connects the two to each other.
  • the inside of the evaporator 60 is evaporated by evacuating the interior with the vacuum pump 65 and the compressor 64 is operated, and the temperature in the evaporator 60 is lowered to produce cold water
  • a cold water pump 66 supplies the load 67 such as a radiant panel.
  • the water vapor evaporated by the evaporator 60 is compressed by the compressor 64 and then guided to the condenser 62.
  • the condenser 62 it is condensed by the cooling water from the cooling tower 68 and returned to the water again.
  • the cooling water heated up by the condensation of the high temperature steam is sent to the cooling tower 68 by the cooling water pump 69, and the heat is radiated to the outside by the cooling tower 68.
  • the evaporator 60 and the condenser 62 are each constituted by individual containers, and in order to arrange the individual containers in this way, a large installation space is required and the apparatus itself is large. Along with this, there is a problem that costs increase in terms of materials and manufacturing.
  • the present invention has been made in view of the above-described points, and it is an object of the present invention to reduce the installation space and to reduce the size of the entire apparatus, and further reduce the cost in terms of materials and manufacturing.
  • An evaporative cooling apparatus includes an evaporation chamber for boiling and evaporating an evaporable liquid at a pressure lower than atmospheric pressure, a vapor compressor for compressing vapor generated in the evaporation chamber, and the vapor compressor compressing the vapor.
  • the shape of the single container is not particularly limited as long as it can be sealed, and may be, for example, a cylindrical shape that can be sealed, a rectangular tube shape, or the like.
  • the partition may be double or more.
  • the partition is not particularly limited as long as the inside of a single container can be partitioned into at least two chambers, an evaporation chamber and a condensation chamber.
  • the volumes of the evaporation chamber and the condensation chamber may be equally divided by the partition, or may be partitioned unevenly.
  • the partition may be composed of, for example, a plate material that is separate from the container, and may be integrated with the container by welding or the like.
  • the partition may be referred to as a partition plate, or may constitute a part of the container wall and may be referred to as a partition wall.
  • the evaporation chamber and the condensing chamber are formed in a single container instead of separate containers. Therefore, the evaporation chamber and the condensing chamber are configured as separate containers, and two containers are formed. Unlike the conventional apparatus that has been installed, the overall size of the apparatus can be reduced, the installation space can be reduced, and further, the material cost and thus the manufacturing cost can be reduced. In addition, since the space is interposed between the double partitions interposed between the evaporation chamber and the condensation chamber, this space is used as a space for heat insulation to effectively transfer heat from the condensation chamber to the evaporation chamber. It can block
  • the material constituting the partition may be a material having a low thermal conductivity different from that of the container, and a heat insulating material is filled in the space between the double partitions. May be.
  • the space interposed between the double partitions is in a reduced pressure state.
  • the space may be sealed in a reduced pressure state at the manufacturing stage, or the space may be connected to a vacuum pump or the like to be in a reduced pressure state.
  • any one of the evaporating chamber and the condensing chamber and a space between the two partitions communicate with each other through a pressure guiding tube, and the pressure in the one of the chambers is The pressure in the space is the same pressure.
  • the pressure in the space between the double partitions is the same as the internal pressure of either the evaporation chamber or the condensation chamber.
  • the stress due to the pressure is not received, so that the material cost can be reduced by making the structure thinner than the other partition.
  • the space becomes a vacuum lower than the atmospheric pressure, heat transfer from the condensation chamber to the evaporation chamber can be effectively blocked.
  • the double partition is constituted by two partition plates facing each other across the space.
  • the partition plates sandwich the space between them, heat transfer between the evaporation chamber and the condensation chamber can be prevented via the partition plates.
  • the single container includes a cylindrical container body, and the evaporation chamber and the two partition plates bisect a circular cross section of the container body.
  • Each of the condensing chambers is partitioned and formed in a semicylindrical shape.
  • the apparatus can be downsized with a simple structure. it can.
  • the entire apparatus is reduced in size and installed as compared with the conventional apparatus in which the evaporation chamber and the condensation chamber are formed as separate containers. Space and material and manufacturing costs can be reduced. Moreover, since the space between the evaporation chamber and the condensing chamber is at least double partitioned, the heat transfer from the condensing chamber to the evaporation chamber is effectively blocked by the space, effectively preventing a decrease in thermal efficiency. can do.
  • FIG. 1 is a diagram showing a system configuration example of an evaporative cooling apparatus according to an embodiment of the present invention.
  • FIG. 2 is a perspective view of the container of FIG.
  • FIG. 3 is a side view of the container of FIG. 4 is a cross-sectional view taken along the line AA in FIG.
  • FIG. 5 is a diagram showing a system configuration example of an evaporative cooling device according to another embodiment of the present invention.
  • FIG. 6 is a cross-sectional view of a container according to another embodiment of the present invention.
  • FIG. 7 is a diagram showing a system configuration example of a conventional apparatus.
  • FIG. 1 shows a system configuration of an evaporative cooling apparatus according to an embodiment of the present invention.
  • the inside of a single sealed container 1 is divided into two chambers by two partition plates 2a and 2b as described later.
  • One chamber is the evaporation chamber 3, the other chamber is the condensation chamber 4, and the space 5 is interposed between the two partition plates 2a and 2b. This space 5 can insulate the evaporation chamber 3 and the condensation chamber 4.
  • the evaporation chamber 3 and the condensation chamber 4 can be disposed compactly adjacent to each other inside the single container 1. Therefore, it is possible to reduce the size of the entire apparatus and to reduce manufacturing costs and material costs. In addition, it is possible to effectively suppress the heat transfer between the two chambers 3 and 4 to prevent a decrease in thermal efficiency.
  • the evaporating chamber 3 evaporates an evaporating liquid, for example, water, which is contained in the evaporating chamber 3 at a reduced pressure lower than the atmospheric pressure.
  • the evaporating chamber 3 pumps water accumulated in the evaporating chamber 3 from the evaporating liquid outlet 6 via the pipe 8 by the circulation pump 7 and supplies a cooling source to the indirect heat exchanger 9 on the load side such as a cooling place. Is supplied to the evaporative liquid inlet 11 via the conduit 10 and is then circulated back into the evaporating chamber 3 so as to be ejected from the upper nozzle 12.
  • the condensing chamber 4 draws a cooling fluid, for example, water, stored in the condensing chamber 4 from the cooling fluid outlet 13 through the pipe 16 by the circulation pump 14 and supplies it to the indirect heat exchanger 15 on the heat radiation side to the atmosphere. It is cooled by heat dissipation.
  • the condensation chamber 4 circulates by supplying the water cooled by the indirect heat exchanger 15 to the cooling liquid inlet 18 via the pipe line 17 and returning it to the condensation chamber 4 so as to be ejected from the nozzle 19 at the upper part thereof. Is configured to do.
  • a root type compressor is provided as the steam compressor 23 to be fed into the tank.
  • steam can be compressed by about 10 ° C. due to a temperature difference.
  • the steam compressor 23 is not limited to a Roots type compressor, and a blower compressor, a screw type compressor, and other compressors can be used.
  • the inside of the evaporating chamber 3 and the inside of the condensing chamber 4 are kept at a reduced pressure lower than the atmospheric pressure by a vacuum pump 25 connected to the vacuum exhaust port 24 of the condensing chamber 4. It is comprised so that boiling evaporation may be performed.
  • connection port 30 at the bottom of the evaporation chamber 3 and the connection port 31 at the bottom of the condenser 4 are connected by a communication pipe 26, and a part of the water in the condensation chamber 4 is passed through the communication pipe 26. 3 is supplied.
  • the evaporation chamber 3 and the condensation chamber 4 are doubled by the two partition plates 2a and 2b provided in the center of the container 1.
  • the space 5 for heat insulation between the partition plates 2a and 2b is made to have the same pressure as the evaporation chamber 3 by the pressure guiding pipe 27 that connects the connection port 29 corresponding to the space 5 and the connection port 28 of the evaporation chamber 3. .
  • the partition plate 2b on the evaporation chamber 3 side of the partition plates 2a and 2b is not subjected to stress due to the differential pressure, and a thinner partition plate can be used than the partition plate 2a on the condensation chamber 4 side. it can.
  • FIG. 2 is a perspective view of the container 1 of FIG. 1
  • FIG. 3 is a side view thereof
  • FIG. 4 is a cross-sectional view taken along the line AA of FIG. 3.
  • FIG. Corresponding parts bear the same reference symbols.
  • the container 1 is made of stainless steel, for example, and includes a cylindrical container body 1a, a front plate 1b that closes the opening at the front end, and a rear plate 1c that closes the opening at the rear end.
  • the front plate 1b and the rear plate 1c close the space 5 between the evaporation chamber 3, the condensation chamber 4, and the partition plates 2a and 2b, respectively.
  • the material constituting the container 1 is not limited to a metal such as stainless steel but may be a hard synthetic resin.
  • the container main body 1a is disposed sideways by four mounting legs 51 so that its axis 50 is horizontal.
  • two flat plate-like partition plates 2a and 2b extending in the direction of the axis 50 of the container body 1a are arranged in the diameter direction so as to bisect the circular cross section of the container body 1a.
  • the evaporating chamber 3 and the condensing chamber 4 are partitioned and formed in a semicylindrical shape.
  • the vapor outlet 20 is provided at the upper part of the main body on the evaporation chamber 3 side, while the vapor inlet 21 is provided at the upper part of the main body on the condensation chamber 4 side.
  • the front plate 1b on the evaporation chamber 3 side is provided with a connection port 28 to which one end of the pressure guiding tube 27 is connected, while the upper portion of the main body corresponding to the heat insulating space 5 sandwiched between the two partition plates 2a and 2b. Is provided with a connection port 29 to which the other end of the pressure guiding tube 27 is connected.
  • the evaporative liquid inlet 11 is provided at three locations on the main body side on the evaporation chamber 3 side, while the cooling fluid inlet 18 is provided at three locations on the main body side on the condensation chamber 4 side.
  • an evaporative liquid outlet 6 is provided near the front surface of the lower part of the main body on the evaporation chamber 3 side, while a cooling liquid outlet 13 is provided near the rear surface of the lower part of the main body on the condensing chamber 4 side.
  • a connection port 30 to which one end of the communication pipe 26 is connected is provided on the front side of the lower part of the main body on the evaporation chamber 3 side, while the connection pipe 26 is provided on the front side of the lower part of the main body on the condensing chamber 4 side.
  • a connection port 31 to which the end is connected is provided.
  • a drain pipe (not shown) is provided at the bottom of the heat insulating space 5 sandwiched between the two partition plates 2a and 2b, and in the unlikely event that refrigerant is mixed into the space 5. Can discharge the refrigerant.
  • Exhaust ports 32 and 24 for vacuum exhaust are respectively provided on the evaporation chamber 3 side and the condensation chamber 4 side of the front plate 1b.
  • a mounting seat (not shown) for mounting the vapor compressor 23 and a motor for driving the vapor compressor 23 is provided on the upper portion of the container main body 1a.
  • the installation space is reduced.
  • the above-described system shown in FIG. 1 is configured using the container 1 having such a configuration.
  • the water that has been cooled by boiling and evaporating in the evaporation chamber 3 under reduced pressure is sent to the load side by the circulation pump 7 via the pipe 8 and indirectly.
  • the water which has been subjected to heat exchange in the heat exchanger 9 and used for cooling or the like and whose temperature has risen on the load side returns to the evaporation chamber 3 again via the pipe line 10, and is cooled by boiling and evaporating again here. The temperature is lowered.
  • the vapor generated by boiling evaporation in the evaporation chamber 3 is sucked and compressed by the vapor compressor 23 to reach the condensation chamber 4 and condensed by cooling in the condensation chamber 4.
  • a part of the pressure is supplied to the evaporation chamber 3 through the communication pipe 26 due to a pressure difference.
  • the water condensed and liquefied by releasing heat in the condensing chamber 4 is sent to the heat radiation side by the circulation pump 14 via the pipe line 16 and cooled by heat radiation to the atmosphere in the indirect heat exchanger 15, The circulation of returning to the condensation chamber 4 through the pipe line 17 is repeated.
  • the evaporation chamber 3 and the condensation chamber 4 are partitioned by dividing the inside of a single container 1 by two partition plates 2a and 2b.
  • the overall size can be reduced to reduce the installation space and cost.
  • the space between the evaporation chamber 3 and the condensing chamber 4 is double partitioned with the space 5 for heat insulation interposed, heat transfer from the condensing chamber 4 to the evaporation chamber 3 is interrupted to prevent a decrease in thermal efficiency. be able to.
  • the space 5 for heat insulation is not connected to the evaporation chamber 3 or the condensing chamber 4 by the pressure guiding tube to be the same pressure as the evaporation chamber 3 or the condensing chamber 4. 5 may simply be in a reduced pressure state.
  • the space 5 for heat insulation is sealed at atmospheric pressure, after the operation of the evaporative cooling device is started, the space 5 and the decompressed evaporation chamber 3 and the decompressed condensing chamber 4 on both sides thereof are separated. Since the differential pressure between them becomes large, the partition plates 2a and 2b need to be thick so that they can withstand the differential pressure. A pressure can be made small and the partition plates 2a and 2b can be made thin.
  • the space 5 may be sealed in a reduced pressure state at the manufacturing stage, or the space 5 may be directly connected via a pipe 55 as shown in FIG.
  • the pressure may be reduced by connecting to the vacuum pump 25. Further, the pressure may be reduced by connecting to a vacuum pump different from the vacuum pump 25.
  • the cylindrical container 1 is arranged in the horizontal direction.
  • the cylindrical container 1 may be arranged in the vertical direction.
  • the circular cross section of the cylindrical container body 1a is divided into two, and the evaporation chamber 3 and the condensation chamber 4 are partitioned and formed in a semi-cylindrical shape.
  • FIG. The evaporation chamber and the condensation chamber may be partitioned and formed in a cylindrical shape by partitioning so as to be orthogonal to the axis 50 of the cylindrical container body 1a shown in FIG.
  • cylindrical double partition members 37a and 37b are concentrically housed inside a cylindrical container 36
  • the inside of the inner partition member 37b is the inner container 36a
  • the outer partition member 37a A section between the outer periphery and the inner periphery of the container 36 may be formed as an annular outer container 36b.
  • one of the inner container 36 a and the outer container 36 b may be the evaporation chamber 3 and the other may be the condensation chamber 4.
  • a heat insulating space 38 is interposed between the double partition members 37a and 37b.
  • This space 38 is preferably set to the same pressure as either the evaporation chamber 3 or the condensation chamber 4.
  • both ends of the container 36 and the partition members 37a and 37b are closed with a lid, and the lid is provided with a necessary vapor or liquid inlet / outlet corresponding to the evaporation chamber 3 and the condensation chamber 4.
  • the inner vessel 36 a is used as the evaporation chamber 3 and the outer vessel 36 b is used as the condensation chamber 4 in order to reduce the thermal influence that the evaporation chamber 3 receives from the atmosphere. Is preferable.
  • the inner container 36 a and the outer container 36 b are arranged concentrically, but may be eccentric as another embodiment.
  • water is used as the evaporating liquid, but the present invention is not limited to water, and alcohol or other evaporating liquids may be used.
  • the present invention is particularly useful as a steam compression refrigerator.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

Disclosed is an evaporative cooling device provided with an evaporation chamber in which an evaporative liquid is boiled and evaporated by reducing the pressure to a pressure lower than atmospheric pressure, a vapor compressor which compresses vapor generated in the evaporation chamber, and a condensation chamber in which the vapor compressed by the vapor compressor is condensed, wherein a single container is divided by double partition plates into two chambers, i.e., the evaporation chamber and the condensation chamber, and a space is provided between the partition plates.

Description

蒸発式冷却装置Evaporative cooling device
 本発明は、水等のように蒸発性を有する液体の蒸発、凝縮を利用して冷却を行う蒸発式冷却装置に関するものである。 The present invention relates to an evaporative cooling device that performs cooling using evaporation and condensation of a liquid having evaporability such as water.
 かかる蒸発式冷却装置として、水蒸気圧縮冷凍機がある(例えば、特許文献1参照)。図7を参照して、同特許文献1の水蒸気圧縮冷凍機においては、蒸発器60と、該蒸発器60に連結配管61で相互連結された凝縮器62と、該蒸発器60と凝縮器62との相互間を接続する連結配管(ダクト)63に配設した圧縮機64とを備えている。 As such an evaporative cooling device, there is a steam compression refrigerator (for example, see Patent Document 1). Referring to FIG. 7, in the steam compression refrigerator of Patent Document 1, an evaporator 60, a condenser 62 interconnected to the evaporator 60 by a connecting pipe 61, and the evaporator 60 and the condenser 62. And a compressor 64 disposed in a connecting pipe (duct) 63 that connects the two to each other.
 この水蒸気圧縮冷凍機では、真空ポンプ65で内部を真空状態にし、圧縮機64を運転することで蒸発器60内の水蒸気が蒸発し、蒸発器60内の温度を低下させて冷水を製造し、冷水ポンプ66により放射パネル等の負荷67へ供給する。蒸発器60で蒸発した水蒸気は、圧縮機64によって圧縮された後、凝縮器62に導かれる。凝縮器62では冷却塔68からの冷却水によって凝縮され再び水に戻る。高温水蒸気の凝縮によって昇温された冷却水は、冷却水ポンプ69によって冷却塔68に送られ、その熱を該冷却塔68により外部へ放熱する。 In this steam compression refrigerator, the inside of the evaporator 60 is evaporated by evacuating the interior with the vacuum pump 65 and the compressor 64 is operated, and the temperature in the evaporator 60 is lowered to produce cold water A cold water pump 66 supplies the load 67 such as a radiant panel. The water vapor evaporated by the evaporator 60 is compressed by the compressor 64 and then guided to the condenser 62. In the condenser 62, it is condensed by the cooling water from the cooling tower 68 and returned to the water again. The cooling water heated up by the condensation of the high temperature steam is sent to the cooling tower 68 by the cooling water pump 69, and the heat is radiated to the outside by the cooling tower 68.
特開2006-97989号公報JP 2006-9789 A
 かかる従来例では、蒸発器60および凝縮器62は、それぞれ個別の容器で構成されており、このように個別の容器を並設するために、大きな設置スペースを必要とするとともに、装置自体が大型化し、これと共に、材料面や製造面でコスト高になるという課題がある。 In such a conventional example, the evaporator 60 and the condenser 62 are each constituted by individual containers, and in order to arrange the individual containers in this way, a large installation space is required and the apparatus itself is large. Along with this, there is a problem that costs increase in terms of materials and manufacturing.
 本発明は、上述の点に鑑みてなされたものであって、設置スペースも小さくて済むと共に、装置全体の小型化、ひいては材料面や製造面でのコスト低減を図ることを目的とする。 The present invention has been made in view of the above-described points, and it is an object of the present invention to reduce the installation space and to reduce the size of the entire apparatus, and further reduce the cost in terms of materials and manufacturing.
 本発明では、上記目的を達成するために、次のように構成している。 In the present invention, in order to achieve the above object, the following configuration is provided.
 本発明にかかる蒸発式冷却装置は、蒸発性液体を大気圧よりも低い減圧で沸騰蒸発させる蒸発室と、この蒸発室において発生した蒸気を圧縮する蒸気圧縮機と、この蒸気圧縮機で圧縮した蒸気を凝縮する凝縮室とを備え、単一容器の内部に少なくとも二重の仕切りによって相互に仕切られた前記蒸発室と前記凝縮室とを有すると共に、前記二重の仕切りの間に空間が介在している。 An evaporative cooling apparatus according to the present invention includes an evaporation chamber for boiling and evaporating an evaporable liquid at a pressure lower than atmospheric pressure, a vapor compressor for compressing vapor generated in the evaporation chamber, and the vapor compressor compressing the vapor. A condensing chamber for condensing steam, and having the evaporation chamber and the condensing chamber separated from each other by at least a double partition inside a single container, and a space is interposed between the double partitions is doing.
 前記単一の容器の形状は、密閉可能であれば特に限定されるものではなく、例えば、密閉可能な円筒状や角筒状やその他であってもよい。前記仕切りは、二重以上であればよい。前記仕切りは、単一容器の内部を少なくとも蒸発室と凝縮室との二室に区画できればよく、その仕切り方には特に限定されない。 The shape of the single container is not particularly limited as long as it can be sealed, and may be, for example, a cylindrical shape that can be sealed, a rectangular tube shape, or the like. The partition may be double or more. The partition is not particularly limited as long as the inside of a single container can be partitioned into at least two chambers, an evaporation chamber and a condensation chamber.
 前記単一の容器内において、前記蒸発室と前記凝縮室は、その容積を前記仕切りにより均等に仕切られてもよいし、不均等に仕切られてもよい。 In the single container, the volumes of the evaporation chamber and the condensation chamber may be equally divided by the partition, or may be partitioned unevenly.
 前記仕切りは、容器とは別体の例えば板材で構成し、容器に対して溶接等で一体化してもよい。この場合、仕切りは仕切り板と称することができるし、あるいは、容器壁の一部を構成するものとし、仕切り壁と称することもできる。 The partition may be composed of, for example, a plate material that is separate from the container, and may be integrated with the container by welding or the like. In this case, the partition may be referred to as a partition plate, or may constitute a part of the container wall and may be referred to as a partition wall.
 本発明の蒸発式冷却装置によると、蒸発室と凝縮室とを別々の容器ではなく、単一の容器内に形成するので、蒸発室と凝縮室とを別々の容器で構成し2つの容器を設置していた従来装置とは異なり、装置の全体サイズを小型にできると共に、設置スペースを削減でき、更に、材料コストひいては製造コストを削減することが可能となる。しかも、蒸発室と凝縮室との間に介在した二重仕切りの間に空間を介在させた構成を有するので、この空間を断熱用の空間として、凝縮室から蒸発室への伝熱を有効に遮断して熱効率の低下を効果的に抑制することができる。 According to the evaporative cooling device of the present invention, the evaporation chamber and the condensing chamber are formed in a single container instead of separate containers. Therefore, the evaporation chamber and the condensing chamber are configured as separate containers, and two containers are formed. Unlike the conventional apparatus that has been installed, the overall size of the apparatus can be reduced, the installation space can be reduced, and further, the material cost and thus the manufacturing cost can be reduced. In addition, since the space is interposed between the double partitions interposed between the evaporation chamber and the condensation chamber, this space is used as a space for heat insulation to effectively transfer heat from the condensation chamber to the evaporation chamber. It can block | block and can suppress the fall of thermal efficiency effectively.
 なお、伝熱を遮断する観点から、上記仕切りを構成する材料を、容器とは異なる低い熱伝導率の材料としてもよく、また、二重の仕切りの間の空間内に、断熱材料を充填してもよい。 From the viewpoint of blocking heat transfer, the material constituting the partition may be a material having a low thermal conductivity different from that of the container, and a heat insulating material is filled in the space between the double partitions. May be.
 本発明の他の実施態様では、前記二重の仕切りの間に介在している前記空間が、減圧状態にされている。 In another embodiment of the present invention, the space interposed between the double partitions is in a reduced pressure state.
 前記空間は、製造段階で減圧状態にして密閉してもよいし、前記空間を真空ポンプ等に連結して減圧状態にしてもよい。 The space may be sealed in a reduced pressure state at the manufacturing stage, or the space may be connected to a vacuum pump or the like to be in a reduced pressure state.
 前記二重の仕切り間の前記空間が大気圧のままで密閉されると、当該蒸発式冷却装置の運転を開始した後に、二重の仕切りの両側、すなわち、前記空間の両側の減圧された蒸発室および減圧された凝縮室と、前記空間との間の差圧がそれぞれ大きなものとなる。したがって、この場合には、二重の仕切りは、その差圧に耐える必要があるために、仕切りを構成する部材、例えば、仕切り板を厚くする必要がある。しかしながら、この実施態様では、前記空間が減圧状態にされるので、前記差圧が小さくなり、仕切り板の厚みを薄くすることができる。 When the space between the double partitions is sealed at atmospheric pressure, after the operation of the evaporative cooling device is started, reduced evaporation on both sides of the double partition, that is, both sides of the space, is performed. The differential pressure between the chamber and the decompressed condensing chamber and the space is increased. Therefore, in this case, since the double partition needs to withstand the differential pressure, it is necessary to increase the thickness of a member constituting the partition, for example, the partition plate. However, in this embodiment, since the space is in a reduced pressure state, the differential pressure is reduced, and the thickness of the partition plate can be reduced.
 本発明の好ましい実施態様では、前記蒸発室および前記凝縮室のうちのいずれか一方の室と前記両仕切りの間の空間とが、導圧管で連通して、前記いずれか一方の室内の圧力と前記空間の圧力とが同圧になっている。 In a preferred embodiment of the present invention, any one of the evaporating chamber and the condensing chamber and a space between the two partitions communicate with each other through a pressure guiding tube, and the pressure in the one of the chambers is The pressure in the space is the same pressure.
 この実施態様によると、二重の仕切りの間の空間の圧力は、蒸発室または凝縮室のいずれか一方の室内圧と同圧となるので、二重の仕切りの内、一方の仕切りは、差圧による応力を受けることがなくなり、これにより他方の仕切りに比べて薄く構成して材料コストを削減することができる。さらに、前記空間が、大気圧よりも低い真空となるので、凝縮室から蒸発室への伝熱を効果的に遮断することができる。 According to this embodiment, the pressure in the space between the double partitions is the same as the internal pressure of either the evaporation chamber or the condensation chamber. The stress due to the pressure is not received, so that the material cost can be reduced by making the structure thinner than the other partition. Furthermore, since the space becomes a vacuum lower than the atmospheric pressure, heat transfer from the condensation chamber to the evaporation chamber can be effectively blocked.
 本発明の別の好ましい実施態様では、前記二重の仕切りを、前記空間を挟んで対向する二枚の仕切り板によって構成している。 In another preferred embodiment of the present invention, the double partition is constituted by two partition plates facing each other across the space.
 この実施態様によると、これら仕切り板は互いの間に前記空間を挟むので、仕切り板を介して前記蒸発室と前記凝縮室との間で熱移動することを阻止することができる。 According to this embodiment, since the partition plates sandwich the space between them, heat transfer between the evaporation chamber and the condensation chamber can be prevented via the partition plates.
 本発明のさらに別の好ましい実施態様では、前記単一の容器は、円筒状の容器本体を含み、前記二枚の仕切り板によって、前記容器本体の円形断面を二分するように、前記蒸発室および前記凝縮室を、半円筒状にそれぞれ区画形成するものである。 In still another preferred embodiment of the present invention, the single container includes a cylindrical container body, and the evaporation chamber and the two partition plates bisect a circular cross section of the container body. Each of the condensing chambers is partitioned and formed in a semicylindrical shape.
 この実施態様によると、円筒状の容器本体内を、二枚の仕切り板で半円筒状に仕切って蒸発室と凝縮室とを区画形成するので、簡単な構造で装置の小型化を図ることができる。 According to this embodiment, since the inside of the cylindrical container body is divided into a semi-cylindrical shape by the two partition plates and the evaporation chamber and the condensation chamber are partitioned, the apparatus can be downsized with a simple structure. it can.
 本発明装置によれば、蒸発室と凝縮室とを同一容器内に形成するので、蒸発室と凝縮室とを別々の容器で形成した従来装置に比べて、装置全体を小型化して装置の設置スペース、および材料や製造のコストを削減することが可能となる。しかも、蒸発室と凝縮室との間を、空間を介在させて少なくとも二重に仕切るので、凝縮室から蒸発室への伝熱を前記空間により有効に遮断して熱効率の低下を効果的に防止することができる。 According to the apparatus of the present invention, since the evaporation chamber and the condensation chamber are formed in the same container, the entire apparatus is reduced in size and installed as compared with the conventional apparatus in which the evaporation chamber and the condensation chamber are formed as separate containers. Space and material and manufacturing costs can be reduced. Moreover, since the space between the evaporation chamber and the condensing chamber is at least double partitioned, the heat transfer from the condensing chamber to the evaporation chamber is effectively blocked by the space, effectively preventing a decrease in thermal efficiency. can do.
図1は本発明の一実施形態に係る蒸発式冷却装置のシステム構成例を示す図である。FIG. 1 is a diagram showing a system configuration example of an evaporative cooling apparatus according to an embodiment of the present invention. 図2は図1の容器の斜視図である。FIG. 2 is a perspective view of the container of FIG. 図3は図2の容器の側面図である。FIG. 3 is a side view of the container of FIG. 図4は図3の矢視A-A断面図である。4 is a cross-sectional view taken along the line AA in FIG. 図5は本発明の他の実施形態の蒸発式冷却装置のシステム構成例を示す図である。FIG. 5 is a diagram showing a system configuration example of an evaporative cooling device according to another embodiment of the present invention. 図6は本発明の他の実施形態の容器の断面図である。FIG. 6 is a cross-sectional view of a container according to another embodiment of the present invention. 図7は従来装置のシステム構成例を示す図である。FIG. 7 is a diagram showing a system configuration example of a conventional apparatus.
 以下、図面によって本発明の実施形態について詳細に説明する。図1に、本発明の実施形態に係る蒸発式冷却装置のシステム構成を示す。図1を参照して、この実施形態に係る蒸発式冷却装置では、密閉型の単一の容器1の内部を、後述のように、二枚の仕切り板2a,2bによって2つの室に仕切ると共に、一方の室を蒸発室3とし、他方の室を凝縮室4とし、かつ、二枚の仕切り板2a,2bの間に空間5を介在させた構成としている。この空間5は、蒸発室3と凝縮室4とを断熱することができる。 Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. FIG. 1 shows a system configuration of an evaporative cooling apparatus according to an embodiment of the present invention. Referring to FIG. 1, in the evaporative cooling apparatus according to this embodiment, the inside of a single sealed container 1 is divided into two chambers by two partition plates 2a and 2b as described later. One chamber is the evaporation chamber 3, the other chamber is the condensation chamber 4, and the space 5 is interposed between the two partition plates 2a and 2b. This space 5 can insulate the evaporation chamber 3 and the condensation chamber 4.
 こうして密閉型の単一容器1の内部を二枚の仕切り板2a,2bによって仕切ることにより、蒸発室3と凝縮室4とを単一容器1内部にコンパクトに隣接配置させることが可能となって、装置全体の小型化ならびに製造コストや材料コストを低減することが可能となる。しかも、これら両室3,4の相互間での熱移動を効果的に抑制して熱効率の低下を防止することが可能となる。 Thus, by separating the inside of the sealed single container 1 by the two partition plates 2a and 2b, the evaporation chamber 3 and the condensation chamber 4 can be disposed compactly adjacent to each other inside the single container 1. Therefore, it is possible to reduce the size of the entire apparatus and to reduce manufacturing costs and material costs. In addition, it is possible to effectively suppress the heat transfer between the two chambers 3 and 4 to prevent a decrease in thermal efficiency.
 蒸発室3は、その内部に入れた蒸発性液体、例えば水を大気圧より低い減圧の状態で沸騰蒸発させるものである。蒸発室3は、蒸発室3内に溜まる水を、蒸発性液体出口6より管路8を介して循環ポンプ7にて汲み出し、冷房箇所等の負荷側における間接熱交換器9に対して冷却源として供給した後、管路10を介して蒸発性液体入口11に供給し、再び蒸発室3内に、その上部のノズル12から噴出するように戻るという循環を行うように構成されている。 The evaporating chamber 3 evaporates an evaporating liquid, for example, water, which is contained in the evaporating chamber 3 at a reduced pressure lower than the atmospheric pressure. The evaporating chamber 3 pumps water accumulated in the evaporating chamber 3 from the evaporating liquid outlet 6 via the pipe 8 by the circulation pump 7 and supplies a cooling source to the indirect heat exchanger 9 on the load side such as a cooling place. Is supplied to the evaporative liquid inlet 11 via the conduit 10 and is then circulated back into the evaporating chamber 3 so as to be ejected from the upper nozzle 12.
 凝縮室4は、その内部に溜まる冷却用流体、例えば水を冷却用流体出口13より管路16を介して循環ポンプ14にて汲み出し、放熱側における間接熱交換器15に供給して、大気への放熱等よって冷却するものである。凝縮室4は、間接熱交換器15によって冷却した水を、管路17を介して冷却用液体入口18に供給し、凝縮室4内に、その上部のノズル19から噴出するように戻すという循環を行うように構成されている。 The condensing chamber 4 draws a cooling fluid, for example, water, stored in the condensing chamber 4 from the cooling fluid outlet 13 through the pipe 16 by the circulation pump 14 and supplies it to the indirect heat exchanger 15 on the heat radiation side to the atmosphere. It is cooled by heat dissipation. The condensation chamber 4 circulates by supplying the water cooled by the indirect heat exchanger 15 to the cooling liquid inlet 18 via the pipe line 17 and returning it to the condensation chamber 4 so as to be ejected from the nozzle 19 at the upper part thereof. Is configured to do.
 更に、蒸発室3の蒸気出口20と凝縮室4の蒸気入口21とを、蒸気ダクト22で接続するとともに、この蒸気ダクト22の途中には、蒸発室3からの蒸気を圧縮して凝縮室4に送り込む蒸気圧縮機23としてルーツ型圧縮機を設けている。このルーツ型圧縮機では、例えば,蒸気を温度差で約10℃程度圧縮することができる。なお、蒸気圧縮機23としては、ルーツ型圧縮機に限らず、ブロワー圧縮機、ねじ型圧縮機やその他の圧縮機を使用することができる。 Further, the vapor outlet 20 of the evaporation chamber 3 and the vapor inlet 21 of the condensation chamber 4 are connected by a vapor duct 22, and the vapor from the evaporation chamber 3 is compressed in the middle of the vapor duct 22 to condense the chamber 4. A root type compressor is provided as the steam compressor 23 to be fed into the tank. In this roots type compressor, for example, steam can be compressed by about 10 ° C. due to a temperature difference. The steam compressor 23 is not limited to a Roots type compressor, and a blower compressor, a screw type compressor, and other compressors can be used.
 蒸発室3の内部および凝縮室4の内部は、凝縮室4の真空用排気口24に接続した真空ポンプ25によって大気圧よりも低い減圧に保持することによって、蒸発室3内で蒸発性液体の沸騰蒸発を行わせるように構成されている。 The inside of the evaporating chamber 3 and the inside of the condensing chamber 4 are kept at a reduced pressure lower than the atmospheric pressure by a vacuum pump 25 connected to the vacuum exhaust port 24 of the condensing chamber 4. It is comprised so that boiling evaporation may be performed.
 また、蒸発室3の底部の接続口30と凝縮器4の底部の接続口31とは、連通管26で接続され、凝縮室4内の水の一部を、連通管26を介して蒸発室3内に供給するようにしている。 The connection port 30 at the bottom of the evaporation chamber 3 and the connection port 31 at the bottom of the condenser 4 are connected by a communication pipe 26, and a part of the water in the condensation chamber 4 is passed through the communication pipe 26. 3 is supplied.
 蒸発室3と凝縮室4とは、上述のように、容器1の中央部に設けた二枚の仕切り板2a,2bによって二重に仕切られている。両仕切り板2a,2bの間の断熱用の空間5は、該空間5に対応する接続口29と蒸発室3の接続口28とを接続する導圧管27によって蒸発室3と同圧とされる。これによって、両仕切り板2a,2bの内の蒸発室3側の仕切り板2bは、差圧による応力を受けず、凝縮室4側の仕切り板2aに比べて、薄い仕切り板を使用することができる。 As described above, the evaporation chamber 3 and the condensation chamber 4 are doubled by the two partition plates 2a and 2b provided in the center of the container 1. The space 5 for heat insulation between the partition plates 2a and 2b is made to have the same pressure as the evaporation chamber 3 by the pressure guiding pipe 27 that connects the connection port 29 corresponding to the space 5 and the connection port 28 of the evaporation chamber 3. . As a result, the partition plate 2b on the evaporation chamber 3 side of the partition plates 2a and 2b is not subjected to stress due to the differential pressure, and a thinner partition plate can be used than the partition plate 2a on the condensation chamber 4 side. it can.
 図2は、図1の容器1の斜視図であり、図3は、その側面図であり、図4は、図3の矢視A-A断面図であり、これらの図において、図1に対応する部分には、同一の参照符号を付す。 2 is a perspective view of the container 1 of FIG. 1, FIG. 3 is a side view thereof, and FIG. 4 is a cross-sectional view taken along the line AA of FIG. 3. In these drawings, FIG. Corresponding parts bear the same reference symbols.
 この容器1は、例えば、ステンレス製であり、円筒状の容器本体1aと、前端の開口を閉塞する前面板1bと、後端の開口を閉塞する後面板1cとを備えている。前面板1bおよび後面板1cは、蒸発室3、凝縮室4および仕切り板2a,2b間の空間5をそれぞれ閉塞する。容器1を構成する材料は、ステンレスなどの金属に限らず、硬質の合成樹脂などであってもよい。 The container 1 is made of stainless steel, for example, and includes a cylindrical container body 1a, a front plate 1b that closes the opening at the front end, and a rear plate 1c that closes the opening at the rear end. The front plate 1b and the rear plate 1c close the space 5 between the evaporation chamber 3, the condensation chamber 4, and the partition plates 2a and 2b, respectively. The material constituting the container 1 is not limited to a metal such as stainless steel but may be a hard synthetic resin.
 容器本体1aは、図3に示すように、その軸線50が水平になるように4本の取付脚51によって横向きに配置されている。円筒状の容器本体1aには、容器本体1aの軸線50方向に延びる平板状の二枚の仕切り板2a,2bが、容器本体1aの円形断面を二分するように直径方向に配置されることによって、蒸発室3および凝縮室4を、それぞれ半円筒状に区画形成している。 As shown in FIG. 3, the container main body 1a is disposed sideways by four mounting legs 51 so that its axis 50 is horizontal. In the cylindrical container body 1a, two flat plate- like partition plates 2a and 2b extending in the direction of the axis 50 of the container body 1a are arranged in the diameter direction so as to bisect the circular cross section of the container body 1a. The evaporating chamber 3 and the condensing chamber 4 are partitioned and formed in a semicylindrical shape.
 蒸発室3側の本体上部には、蒸気出口20が設けられる一方、凝縮室4側の本体上部には、蒸気入口21が設けられる。蒸発室3側の前面板1bには、導圧管27の一端が接続される接続口28が設けられる一方、二枚の仕切り板2a,2bで挟まれた断熱用の空間5に対応する本体上部には、導圧管27の他端が接続される接続口29が設けられる。 The vapor outlet 20 is provided at the upper part of the main body on the evaporation chamber 3 side, while the vapor inlet 21 is provided at the upper part of the main body on the condensation chamber 4 side. The front plate 1b on the evaporation chamber 3 side is provided with a connection port 28 to which one end of the pressure guiding tube 27 is connected, while the upper portion of the main body corresponding to the heat insulating space 5 sandwiched between the two partition plates 2a and 2b. Is provided with a connection port 29 to which the other end of the pressure guiding tube 27 is connected.
 蒸発室3側の本体側部には、蒸発性液体入口11が三箇所に設けられる一方、凝縮室4側の本体側部には、冷却用流体入口18が三箇所に設けられる。また、蒸発室3側の本体下部の前面寄りには、蒸発性液体出口6が設けられる一方、凝縮室4側の本体下部の後面寄りには、冷却用液体出口13が設けられる。更に、蒸発室3側の本体下部の前面側には、連通管26の一端が接続される接続口30が設けられる一方、凝縮室4側の本体下部の前面側には、連通管26の他端が接続される接続口31が設けられる。二枚の仕切り板2a,2bで挟まれた断熱用の空間5の底部には、ドレン配管(図示せず)が設けられており、万一、空間5内に冷媒が混入したような場合には、冷媒を排出できるようになっている。前面板1bの蒸発室3側および凝縮室4側には、真空排気用の排気口32,24がそれぞれ設けられる。 The evaporative liquid inlet 11 is provided at three locations on the main body side on the evaporation chamber 3 side, while the cooling fluid inlet 18 is provided at three locations on the main body side on the condensation chamber 4 side. Further, an evaporative liquid outlet 6 is provided near the front surface of the lower part of the main body on the evaporation chamber 3 side, while a cooling liquid outlet 13 is provided near the rear surface of the lower part of the main body on the condensing chamber 4 side. Furthermore, a connection port 30 to which one end of the communication pipe 26 is connected is provided on the front side of the lower part of the main body on the evaporation chamber 3 side, while the connection pipe 26 is provided on the front side of the lower part of the main body on the condensing chamber 4 side. A connection port 31 to which the end is connected is provided. A drain pipe (not shown) is provided at the bottom of the heat insulating space 5 sandwiched between the two partition plates 2a and 2b, and in the unlikely event that refrigerant is mixed into the space 5. Can discharge the refrigerant. Exhaust ports 32 and 24 for vacuum exhaust are respectively provided on the evaporation chamber 3 side and the condensation chamber 4 side of the front plate 1b.
 なお、容器本体1aの上部には、蒸気圧縮器23およびそれを駆動するモータなどを取り付けるための図示しない取付座が設けられており、容器本体1aの上部のスペースを有効に利用し、装置全体の設置スペースを削減している。かかる構成を有する容器1を用いて、上述の図1のシステムが構成される。 Note that a mounting seat (not shown) for mounting the vapor compressor 23 and a motor for driving the vapor compressor 23 is provided on the upper portion of the container main body 1a. The installation space is reduced. The above-described system shown in FIG. 1 is configured using the container 1 having such a configuration.
 再び図1を参照して、蒸発室3内における減圧状態での沸騰蒸発にて冷却されて温度が低くなった水は、管路8を介して循環ポンプ7にて負荷側に送られて間接熱交換器9で熱交換されて冷房等に供され、この負荷側において温度が上昇した水は、管路10を介して再び蒸発室3内に戻って、ここで再び沸騰蒸発することで冷却されて温度が低くなる。 Referring to FIG. 1 again, the water that has been cooled by boiling and evaporating in the evaporation chamber 3 under reduced pressure is sent to the load side by the circulation pump 7 via the pipe 8 and indirectly. The water which has been subjected to heat exchange in the heat exchanger 9 and used for cooling or the like and whose temperature has risen on the load side returns to the evaporation chamber 3 again via the pipe line 10, and is cooled by boiling and evaporating again here. The temperature is lowered.
 一方、蒸発室3内における沸騰蒸発にて発生した蒸気は、蒸気圧縮機23にて吸引されて圧縮されて凝縮室4内に至り、凝縮室4での冷却にて凝縮され、この凝縮水の一部は、圧力差によって連通管26を介して蒸発室3に供給される。 On the other hand, the vapor generated by boiling evaporation in the evaporation chamber 3 is sucked and compressed by the vapor compressor 23 to reach the condensation chamber 4 and condensed by cooling in the condensation chamber 4. A part of the pressure is supplied to the evaporation chamber 3 through the communication pipe 26 due to a pressure difference.
 また、凝縮室4内で熱を放出して凝縮液化した水は、管路16を介して循環ポンプ14にて放熱側に送られて間接熱交換器15で大気への放熱等よって冷却され、管路17を介して凝縮室4内に戻るという循環を繰り返す。 Further, the water condensed and liquefied by releasing heat in the condensing chamber 4 is sent to the heat radiation side by the circulation pump 14 via the pipe line 16 and cooled by heat radiation to the atmosphere in the indirect heat exchanger 15, The circulation of returning to the condensation chamber 4 through the pipe line 17 is repeated.
 以上の構成の蒸発式冷却装置では、単一の容器1の内部を、二枚の仕切り板2a,2bで二重に仕切ることによって蒸発室3および凝縮室4を区画形成しているので、装置全体を小型化して設置スペースおよびコストを削減することができる。しかも、蒸発室3と凝縮室4との間を、断熱用の空間5を介在させて二重に仕切るので、凝縮室4から蒸発室3への伝熱を遮断して熱効率の低下を防止することができる。 In the evaporative cooling apparatus having the above configuration, the evaporation chamber 3 and the condensation chamber 4 are partitioned by dividing the inside of a single container 1 by two partition plates 2a and 2b. The overall size can be reduced to reduce the installation space and cost. In addition, since the space between the evaporation chamber 3 and the condensing chamber 4 is double partitioned with the space 5 for heat insulation interposed, heat transfer from the condensing chamber 4 to the evaporation chamber 3 is interrupted to prevent a decrease in thermal efficiency. be able to.
 本発明の他の実施形態として、断熱用の空間5を、導圧管によって蒸発室3または凝縮室4と接続して蒸発室3または凝縮室4と同圧にするのではなく、断熱用の空間5を、単に減圧状態としてもよい。 As another embodiment of the present invention, the space 5 for heat insulation is not connected to the evaporation chamber 3 or the condensing chamber 4 by the pressure guiding tube to be the same pressure as the evaporation chamber 3 or the condensing chamber 4. 5 may simply be in a reduced pressure state.
 断熱用の空間5が大気圧のまま密閉されていると、当該蒸発式冷却装置の運転を開始した後に、空間5と、その両側の減圧された蒸発室3および減圧された凝縮室4との間の差圧がそれぞれ大きなものとなるので、仕切り板2a,2bは、その差圧に耐えることができるように厚くする必要があるが、断熱用の空間5を減圧状態にすることによって、差圧を小さくすることができ、仕切り板2a,2bを薄くすることができる。 If the space 5 for heat insulation is sealed at atmospheric pressure, after the operation of the evaporative cooling device is started, the space 5 and the decompressed evaporation chamber 3 and the decompressed condensing chamber 4 on both sides thereof are separated. Since the differential pressure between them becomes large, the partition plates 2a and 2b need to be thick so that they can withstand the differential pressure. A pressure can be made small and the partition plates 2a and 2b can be made thin.
 断熱用の空間5を減圧状態にするには、製造段階で空間5を減圧状態にして密閉してもよいし、あるいは、空間5を、例えば図5に示すように、配管55を介して直接真空ポンプ25に接続して減圧してもよい。また、真空ポンプ25とは別の真空ポンプに接続して減圧状態としてもよい。 In order to bring the space 5 for heat insulation into a reduced pressure state, the space 5 may be sealed in a reduced pressure state at the manufacturing stage, or the space 5 may be directly connected via a pipe 55 as shown in FIG. The pressure may be reduced by connecting to the vacuum pump 25. Further, the pressure may be reduced by connecting to a vacuum pump different from the vacuum pump 25.
 上述の実施形態では、円筒状の容器1を横向きに配置したけれども、他の実施形態として、縦向きに配置する構成としてもよい。また、上述の実施形態では、円筒状の容器本体1aの円形断面を二分するように仕切って、蒸発室3および凝縮室4をそれぞれ半円筒状に区画形成したけれども、他の実施形態として、図3に示す円筒状の容器本体1aの軸線50に直交するように仕切って、蒸発室および凝縮室をそれぞれ円筒状に区画形成してもよい。 In the above-described embodiment, the cylindrical container 1 is arranged in the horizontal direction. However, as another embodiment, the cylindrical container 1 may be arranged in the vertical direction. Further, in the above-described embodiment, the circular cross section of the cylindrical container body 1a is divided into two, and the evaporation chamber 3 and the condensation chamber 4 are partitioned and formed in a semi-cylindrical shape. However, as another embodiment, FIG. The evaporation chamber and the condensation chamber may be partitioned and formed in a cylindrical shape by partitioning so as to be orthogonal to the axis 50 of the cylindrical container body 1a shown in FIG.
 更に、上述の実施形態では、円筒状の容器1の内部を、平板状の仕切り板2a,2bで二重に仕切ったけれども、本発明の他の実施形態として、例えば、図6の断面図に示すように、円筒状の容器36の内部に、円筒状の二重の仕切り部材37a,37bを同心状に内装し、内側の仕切り部材37bの内部を内側容器36aとし、外側の仕切り部材37aの外周と容器36の内周との間を環状の外側容器36bとして区画形成してもよい。この場合、内側容器36aまたは外側容器36bのいずれか一方を、蒸発室3とし、他方を凝縮室4としてもよい。そして、二重の仕切り部材37a,37bの間には、断熱用の空間38を介在させる。この空間38を、蒸発室3または凝縮室4のいずれか一方と同圧にするのが好ましい。なお、容器36および仕切り部材37a,37bの両端は、蓋体で閉塞されるとともに、この蓋体には、蒸発室3および凝縮室4に対応して必要な蒸気や液体の出入口が設けられる。 Furthermore, in the above-mentioned embodiment, although the inside of the cylindrical container 1 is partitioned twice by the flat partition plates 2a and 2b, as another embodiment of the present invention, for example, in the cross-sectional view of FIG. As shown, cylindrical double partition members 37a and 37b are concentrically housed inside a cylindrical container 36, the inside of the inner partition member 37b is the inner container 36a, and the outer partition member 37a A section between the outer periphery and the inner periphery of the container 36 may be formed as an annular outer container 36b. In this case, one of the inner container 36 a and the outer container 36 b may be the evaporation chamber 3 and the other may be the condensation chamber 4. A heat insulating space 38 is interposed between the double partition members 37a and 37b. This space 38 is preferably set to the same pressure as either the evaporation chamber 3 or the condensation chamber 4. In addition, both ends of the container 36 and the partition members 37a and 37b are closed with a lid, and the lid is provided with a necessary vapor or liquid inlet / outlet corresponding to the evaporation chamber 3 and the condensation chamber 4.
 また、蒸発室3は、凝縮室4に比べて温度が低いので、蒸発室3が大気から受ける熱的影響を低減するために、内側容器36aを蒸発室3とし、外側容器36bを凝縮室4とするのが好ましい。 Further, since the temperature of the evaporation chamber 3 is lower than that of the condensation chamber 4, the inner vessel 36 a is used as the evaporation chamber 3 and the outer vessel 36 b is used as the condensation chamber 4 in order to reduce the thermal influence that the evaporation chamber 3 receives from the atmosphere. Is preferable.
 図6では、内側容器36aと外側容器36bとは、同心状に配置したけれども、他の実施形態として、偏心していてもよい。 In FIG. 6, the inner container 36 a and the outer container 36 b are arranged concentrically, but may be eccentric as another embodiment.
 上述の実施形態では、蒸発性液体として水を使用したけれども、本発明は水に限らず、アルコールその他の蒸発性液体を使用してもよい。 In the above embodiment, water is used as the evaporating liquid, but the present invention is not limited to water, and alcohol or other evaporating liquids may be used.
 本発明にかかるは、水蒸気圧縮冷凍機として特に有用である。 The present invention is particularly useful as a steam compression refrigerator.
 1,36       容器
 1a         容器本体
 2a,2b      仕切り板
 3          蒸発室
 4          凝縮室
 5,38       空間
 37a,37b    仕切り部材
DESCRIPTION OF SYMBOLS 1,36 Container 1a Container main body 2a, 2b Partition plate 3 Evaporation chamber 4 Condensing chamber 5,38 Space 37a, 37b Partition member

Claims (5)

  1.  蒸発性液体を大気圧よりも低い減圧で沸騰蒸発させる蒸発室と、
     この蒸発室において発生した蒸気を圧縮する蒸気圧縮機と、
     前記蒸気圧縮機で圧縮した蒸気を凝縮する凝縮室と、
     を備え、
     単一容器の内部に少なくとも二重の仕切りによって相互に仕切られた前記蒸発室と前記凝縮室とを有すると共に、前記二重の仕切りの間に空間が介在している、
     蒸発式冷却装置。
    An evaporation chamber for boiling and evaporating the evaporable liquid at a pressure lower than atmospheric pressure;
    A vapor compressor for compressing the vapor generated in the evaporation chamber;
    A condensing chamber for condensing the steam compressed by the steam compressor;
    With
    The evaporation chamber and the condensation chamber are mutually partitioned by at least a double partition inside a single container, and a space is interposed between the double partitions,
    Evaporative cooling device.
  2.  前記二重の仕切りの間に介在している前記空間が、減圧状態にされる、
     請求項1に記載の蒸発式冷却装置。
    The space interposed between the double partitions is in a reduced pressure state;
    The evaporative cooling device according to claim 1.
  3.  前記蒸発室および前記凝縮室のうちのいずれか一方の室と前記二重の仕切りの間に介在している前記空間とが、導圧管で連通して、前記いずれか一方の室の室内圧力と前記空間の圧力とが同圧になっている、
     請求項1に記載の蒸発式冷却装置。
    Any one of the evaporation chamber and the condensing chamber and the space interposed between the double partitions communicate with each other through a pressure guiding pipe, The pressure in the space is the same pressure,
    The evaporative cooling device according to claim 1.
  4.  前記二重の仕切りを、前記空間を挟んで対向する二枚の仕切り板によって構成している、
     請求項1ないし3のいずれかに記載の蒸発式冷却装置。
    The double partition is constituted by two partition plates facing each other across the space.
    The evaporative cooling device according to any one of claims 1 to 3.
  5.  前記単一の容器は、円筒状の容器本体を含み、前記二枚の仕切り板によって、前記容器本体の円形断面を二分するように、前記蒸発室および前記凝縮室を、半円筒状にそれぞれ区画形成した、
     請求項4に記載の蒸発式冷却装置。
    The single container includes a cylindrical container main body, and the evaporation chamber and the condensing chamber are divided into semi-cylindrical shapes so as to bisect the circular cross section of the container main body by the two partition plates. Formed,
    The evaporative cooling device according to claim 4.
PCT/JP2010/004387 2009-08-28 2010-07-05 Evaporative cooling device WO2011024371A1 (en)

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JP5765862B2 (en) * 2013-08-30 2015-08-19 株式会社アンレット Low pressure steam recycling equipment
FR3069624B1 (en) * 2017-07-28 2019-10-18 Alpinov X REFRIGERATING INSTALLATION
TWI757508B (en) * 2017-08-02 2022-03-11 日商笹倉機械工程股份有限公司 Fresh water generation device

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JP2003042597A (en) * 2001-07-27 2003-02-13 Denso Corp Integrated heat exchanger
JP2003112797A (en) * 2001-10-05 2003-04-18 Sapporo Breweries Ltd Beverage cooling and feeding device
JP2003156267A (en) * 2001-11-16 2003-05-30 Daikin Ind Ltd Separate type air-conditioner and heat insulating double pipe to be used for the same
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