JP2008275288A - Evaporation type air conditioner - Google Patents

Evaporation type air conditioner Download PDF

Info

Publication number
JP2008275288A
JP2008275288A JP2007122505A JP2007122505A JP2008275288A JP 2008275288 A JP2008275288 A JP 2008275288A JP 2007122505 A JP2007122505 A JP 2007122505A JP 2007122505 A JP2007122505 A JP 2007122505A JP 2008275288 A JP2008275288 A JP 2008275288A
Authority
JP
Japan
Prior art keywords
container
cooling
heating
air conditioner
heat exchangers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2007122505A
Other languages
Japanese (ja)
Other versions
JP4857179B2 (en
Inventor
Masaaki Imai
正昭 今井
Yoshinori Inoue
良則 井上
Hiroaki Hayase
宏明 早瀬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sasakura Engineering Co Ltd
Original Assignee
Sasakura Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sasakura Engineering Co Ltd filed Critical Sasakura Engineering Co Ltd
Priority to JP2007122505A priority Critical patent/JP4857179B2/en
Publication of JP2008275288A publication Critical patent/JP2008275288A/en
Application granted granted Critical
Publication of JP4857179B2 publication Critical patent/JP4857179B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/16Receivers

Abstract

<P>PROBLEM TO BE SOLVED: To cool or heat a plurality of cooling and heating portions separately in an evaporation type air conditioner which cools the plurality of cooling and heating portions by an evaporative liquid cooled by boiling and evaporation in one of a first container and a second container, and heats the portions by the evaporative liquid heated by evaporation and condensation in the other container. <P>SOLUTION: In this evaporation type air conditioner, each of cooling and heating heat exchangers 4, 5 and 6 disposed at each of the plurality of cooling and heating portions 1, 2 and 3 is provided with a switching means for switching a first state for supplying the evaporative liquid cooled by boiling and evaporation and a second state for supplying the evaporative liquid heated by vapor condensation. The switching means is switched to the first state and the second state, and in addition, switched to a third state for stopping the supply of the evaporative liquids from both containers to the respective cooling and heating heat exchangers. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は,例えば,水等のような蒸発性を有する液体,つまり,蒸発性液体を使用して,大気空気にて複数の冷暖房箇所における冷暖房を行うようにした蒸発式の空調装置に関するものである。   The present invention relates to an evaporative air conditioner that uses a liquid having evaporability such as water, that is, an evaporative liquid, to perform air-conditioning at a plurality of air-conditioning locations using atmospheric air. is there.

先行技術としての特許文献1には,
「少なくとも,減圧に保持した第1容器及び第2容器と,冷暖房箇所に設置した冷暖房用熱交換器と,大気空気との間で熱交換を行う放吸熱用熱交換器とを備え,更に,前記第1容器内における水等の蒸発性液体を前記冷暖房用熱交換器との間を循環する第1循環管路と,前記第2容器内における水等の蒸発性液体を前記放吸熱用熱交換器との間を循環する第2循環管路と,前記第1容器と第2容器の相互間を接続する蒸気ダクト中に正逆回転可能の蒸気圧縮機を設けて成る。」
構成が記載されている。
Patent Document 1 as a prior art includes:
“At least a first container and a second container held at a reduced pressure, an air conditioner heat exchanger installed at an air conditioner, and an endothermic heat exchanger for exchanging heat with atmospheric air, A first circulation pipe for circulating an evaporative liquid such as water in the first container between the heat exchanger for cooling and heating; and an evaporating liquid such as water in the second container for the heat for releasing heat. A steam compressor capable of forward and reverse rotation is provided in a second circulation line that circulates between the exchanger and a steam duct that connects the first container and the second container. "
The configuration is described.

この先行技術の構成においては,前記蒸気圧縮機を,前記第1容器から前記第2容器の方向に蒸気圧縮を行うように正方向に回転するとき,前記第1容器における蒸発性液体は沸騰蒸発にて所定温度に冷却されたのち冷暖房用熱交換器に送られたのち再び前記第1容器に戻って沸騰蒸発することを繰り返す一方,前記第1容器内での沸騰蒸発にて発生した蒸気は前記蒸気圧縮機にて圧縮されたのち前記第2容器に至り,この第2容器における蒸発性液体にて凝縮され,この蒸気凝縮にて温度が高くなった蒸発性液体は放吸熱用熱交換器に送られて大気空気との熱交換にて冷却されたのち再び前記第2容器に戻って蒸気を凝縮することを繰り返すから,冷暖房箇所の冷房を行うという冷房運転にすることができる。   In this prior art configuration, when the vapor compressor is rotated in the forward direction to perform vapor compression from the first container to the second container, the evaporating liquid in the first container is boiled and evaporated. After being cooled to a predetermined temperature in step 1, after being sent to a heat exchanger for air conditioning, the vapor is generated by boiling evaporation in the first container while returning to the first container and evaporating again. After being compressed by the vapor compressor, the vapor reaches the second container and is condensed by the evaporative liquid in the second container. Since the steam is repeatedly returned to the second container and condensed after being cooled by heat exchange with the atmospheric air, it is possible to perform a cooling operation in which the cooling / heating portion is cooled.

また,前記蒸気圧縮機を,今度は,前記第2容器から前記第1容器の方向に蒸気圧縮を行うように逆方向に回転すると,前記第2容器における蒸発性液体は沸騰蒸発にて所定温度に冷却されたのち放吸熱用熱交換器に送られ,ここで,大気空気との熱交換にて吸熱して暖められたのち再び前記第2容器に戻って沸騰蒸発することを繰り返す一方,前記第2容器内での沸騰蒸発にて発生した蒸気は前記蒸気圧縮機にて圧縮されたのち前記第1容器に至り,この第1容器における蒸発性液体にて凝縮され,この蒸気の凝縮にて温度が高くなった蒸発性液体は冷暖房用熱交換器に送られたのち再び前記第1容器に戻って蒸気を凝縮することを繰り返すから,冷暖房箇所の暖房を行うという暖房運転にすることができる。
特開2006−97989号公報
Further, when the vapor compressor is rotated in the opposite direction so as to perform vapor compression in the direction from the second container to the first container, the evaporable liquid in the second container is heated to a predetermined temperature by boiling evaporation. After being cooled to the heat exchanger for releasing heat absorption, where the heat is absorbed and heated by heat exchange with the atmospheric air, and then returned to the second container again and repeatedly boiled and evaporated. Vapor generated by boiling evaporation in the second container is compressed by the vapor compressor and then reaches the first container, where it is condensed by the evaporating liquid in the first container. Since the evaporating liquid whose temperature has been increased is sent to the heat exchanger for air conditioning, it returns to the first container and condenses the vapor repeatedly, so that it is possible to perform a heating operation of heating the air conditioning location. .
Japanese Patent Application Laid-Open No. 2006-97989

前記先行技術の装置は,前記したように,冷暖房箇所に冷暖房用熱交換器を配設し,冷房運転の時には,前記冷暖房用熱交換器に,前記蒸気圧縮機を正回転することで第1容器において冷却された蒸発性液体を供給することにより,前記冷暖房箇所の冷房を行う一方,暖房運転の時には,前記冷暖房用熱交換器に,前記蒸気圧縮機を逆回転することで第1容器において温度が高くなった蒸発性液体を供給することにより,前記冷暖房箇所の暖房を行うという構成である。   As described above, the prior art apparatus is provided with a heat exchanger for air conditioning at the air conditioning location, and during the cooling operation, the steam compressor is rotated forward in the heat exchanger for air conditioning. By supplying the evaporative liquid cooled in the container, the air-conditioning part is cooled, while in the heating operation, the steam compressor is reversely rotated to the air-conditioning heat exchanger in the first container. It is the structure which heats the said air-conditioning location by supplying the evaporating liquid whose temperature became high.

しかし,前記先行技術のように,蒸気圧縮機を正逆回転することは,当該蒸気圧縮機における耐久性が大幅に低下するばかりか,各冷暖房箇所における冷暖房用熱交換器に供給する蒸発性液体の温度を,大気温度の変化及び熱負荷等に対して,略一定に保つように,前記蒸気圧縮機を回転制御する場合,この回転制御が困難であるという問題がある。   However, rotating the steam compressor forward and backward as in the prior art not only greatly reduces the durability of the steam compressor, but also evaporative liquid supplied to the air conditioner heat exchanger at each air conditioning location. When the steam compressor is rotationally controlled so that the temperature of the steam compressor is kept substantially constant with respect to changes in atmospheric temperature and heat load, there is a problem that this rotational control is difficult.

しかも,前記先行技術の空調装置においては,当該空調装置を構成する第1容器,第2容器,放吸熱用熱交換器及び蒸気圧縮機を,前記複数の冷暖房箇所ごとに配設するという構成にしなければならないから,全体としての装置が非常に大型化するばかりか,価格の大幅なアップを招来し,しかも,冷暖房に要するランニングコストも大幅にアップするという問題があった。   In addition, in the prior art air conditioner, the first container, the second container, the heat exchanger for releasing heat and the steam compressor constituting the air conditioner are arranged for each of the plurality of cooling / heating locations. Therefore, there is a problem that not only the apparatus as a whole becomes very large, but also the price is greatly increased, and the running cost required for air conditioning is also greatly increased.

本発明は,複数の冷暖房箇所を冷房及び暖房することが,前記のような問題を招来することなく,確実に達成できるようにした蒸発式の空調装置を提供することを技術的課題とするものである。   It is a technical object of the present invention to provide an evaporative air conditioner that can reliably achieve cooling and heating of a plurality of cooling and heating points without causing the above-described problems. It is.

この技術的課題を達成するため請求項1は,
「少なくとも,減圧に保持した第1容器及び第2容器と,複数の各冷暖房箇所の各々に設置した複数個の冷暖房用熱交換器と,大気との間で熱交換を行う放吸熱用熱交換器とを備え,更に,前記第1容器における蒸発性液体を前記各冷暖房用熱交換器に並列に供給しこの各冷暖房用熱交換器から前記第1容器に戻るように循環する第1循環管路と,前記第2容器における蒸発性液体を前記放吸熱用熱交換器に供給しこの放吸熱用熱交換器から前記第2容器に戻すように循環する第2循環管路と,前記第1容器と第2容器の相互間を接続する蒸気ダクトと,この蒸気ダクトに前記第1容器から第2容器の方向に蒸気圧縮を行うようにした蒸気圧縮機とを備えて成り,
前記第1容器における蒸発性液体を前記各冷暖房箇所における冷暖房用熱交換器との間で循環する一方,前記第2容器における蒸発性液体を前記放吸熱用熱交換器との間で循環するという冷房運転と,
前記第1容器における蒸発性液体を前記放吸熱用熱交換器との間で循環する一方,前記第2容器における蒸発性液体を前記各冷暖房箇所における冷暖房用熱交換器との間で循環するという暖房運転とに,
切り換え可能に構成した。」
ことを特徴としている。
In order to achieve this technical problem, claim 1
“At least the first and second containers kept under reduced pressure, a plurality of cooling / heating heat exchangers installed in each of the plurality of cooling / heating locations, and heat exchange for heat release and absorption that exchanges heat with the atmosphere. A first circulation pipe for supplying the evaporative liquid in the first container to each of the air conditioner heat exchangers in parallel and circulating the air from the air conditioner heat exchangers back to the first container. A second circulation line that circulates the evaporative liquid in the second container to supply to the heat-dissipating heat-absorbing heat exchanger and returns from the heat-dissipating heat-absorbing heat exchanger to the second container; A steam duct connecting between the container and the second container, and a steam compressor configured to perform steam compression in the direction of the second container from the first container to the steam duct,
The evaporative liquid in the first container circulates between the cooling / heating heat exchangers in each of the air-conditioning locations, while the evaporative liquid in the second container circulates between the heat-dissipating heat exchangers. Cooling operation,
The evaporative liquid in the first container circulates between the heat exchanger for heat release and absorption, while the evaporative liquid in the second container circulates between the air conditioner and the heat exchanger for cooling / heating. For heating operation,
It was configured to be switchable. "
It is characterized by that.

また,請求項2は,
「前記請求項1の記載において,前記複数の各冷暖房箇所における冷暖房用熱交換器の各々に,
前記冷房運転の中に,前記各冷暖房用熱交換器のうち一部の冷暖房用熱交換器に対する前記第1容器からの蒸発性液体の供給を止めて当該一部の冷暖房用熱交換器に対して前記第2容器における蒸発性液体を供給しこの一部の冷暖房用熱交換器から前記第2容器に戻す第1状態と,
前記暖房運転の中に,前記各冷暖房用熱交換器のうち一部の冷暖房用熱交換器に対する前記第2容器からの蒸発性液体の供給を止めて当該一部の冷暖房用熱交換器に対して前記第1容器の蒸発性液体を供給しこの一部の冷暖房用熱交換器から前記第1容器に戻す第2状態とに,
切り換えるようにした切換手段を備えている。」
ことを特徴としている。
Claim 2
"In the description of claim 1, each of the heat exchangers for cooling and heating at each of the plurality of cooling and heating locations,
During the cooling operation, supply of the evaporative liquid from the first container to a part of the air conditioner heat exchangers among the air conditioner heat exchangers is stopped and the part of the air conditioner heat exchangers is stopped. A first state in which the evaporative liquid in the second container is supplied and returned to the second container from a part of the heat exchanger for cooling and heating,
During the heating operation, supply of the evaporative liquid from the second container to some of the cooling / heating heat exchangers among the heating / cooling heat exchangers is stopped, and the partial cooling / heating heat exchangers are stopped. To the second state in which the evaporative liquid in the first container is supplied and returned to the first container from a part of the heat exchanger for cooling and heating,
Switching means adapted to switch is provided. "
It is characterized by that.

更にまた,請求項3は,
「前記請求項2の記載において,前記各切換手段が,
前記第1状態と前記第2状態とに切り換える構成であることに加えて,
前記各冷暖房用熱交換器に対する両容器からの蒸発性液体の供給を止めるようにした第3状態にも切り換えできる,
構成である。」
ことを特徴としている。
Furthermore, claim 3
“In the description of claim 2, each of the switching means includes:
In addition to being configured to switch between the first state and the second state,
It is possible to switch to the third state in which the supply of the evaporable liquid from both containers to each of the air conditioner heat exchangers is stopped.
It is a configuration. "
It is characterized by that.

加えて,請求項4は,
「前記請求項2又は3の記載において,前記切換手段が,
前記第2容器における蒸発性液体の一部を前記各冷暖房用熱交換器の入口に供給するバイパス供給管路と,
前記各冷暖房用熱交換器の出口を前記第2容器又は前記第2循環管路に接続するバイパス戻り管路と,
前記第1循環管路及び前記バイパス供給管路のうち前記各冷暖房用熱交換器の入口に接続する部分に設けた入口側開閉弁と,
前記第1循環管路及び前記バイパス戻り管路のうち前記各冷暖房用熱交換器の出口に接続する部分に設けた出口側開閉弁とで,
構成されている。」
ことを特徴としている。
In addition, claim 4
“In the claim 2 or 3, the switching means is:
A bypass supply line for supplying a part of the evaporable liquid in the second container to the inlet of each of the air conditioner heat exchangers;
A bypass return pipe connecting an outlet of each of the air conditioner heat exchangers to the second container or the second circulation pipe;
An inlet-side on-off valve provided at a portion of the first circulation pipe and the bypass supply pipe connected to the inlet of each of the air conditioner heat exchangers;
An outlet-side on-off valve provided at a portion of the first circulation line and the bypass return line that is connected to the outlet of each heat exchanger for cooling and heating,
It is configured. "
It is characterized by that.

前記請求項1の記載において,前記第1容器における蒸発性液体は沸騰蒸発することにより冷却される一方,この第1容器における沸騰蒸発にて発生した蒸気は蒸気圧縮機にて圧縮されたのち前記第2容器に至り,この第2容器における蒸発性液体にて凝縮されるこにより,前記第2容器における蒸発性液体はその温度が高くなる。   The vaporized liquid in the first container is cooled by boiling and evaporating, and the vapor generated by boiling and evaporating in the first container is compressed by a vapor compressor and then By reaching the second container and being condensed by the evaporating liquid in the second container, the temperature of the evaporating liquid in the second container is increased.

そこで,前記第1容器における蒸発性液体を前記各冷暖房用熱交換器との間で循環する一方,前記第2容器における蒸発性液体を前記放吸熱用熱交換器との間で循環するという冷房運転にすることにより,第1容器において沸騰蒸発にて冷却された蒸発性液体は,複数の各冷暖房箇所における冷暖房用熱交換器に一斉に送られたのち再び前記第1容器に戻って沸騰蒸発することを繰り返す一方,前記第2容器において蒸気凝縮にて温度が高くなった蒸発性液体は,放吸熱用熱交換器に送られて大気空気との熱交換にて冷却(放熱)されたのち再び前記第2容器に戻って蒸気を凝縮することを繰り返すから,前記複数の各冷暖房箇所を一斉に冷房することができる。   Therefore, the evaporating liquid in the first container is circulated between the heat exchangers for cooling and heating, while the evaporating liquid in the second container is circulated between the heat exchangers for releasing and absorbing heat. By making the operation, the evaporative liquid cooled by boiling evaporation in the first container is sent all at once to the heat exchanger for cooling and heating at each of the plurality of cooling and heating locations, and then returns to the first container again to evaporate to boiling. On the other hand, the evaporative liquid whose temperature has been increased by vapor condensation in the second container is sent to a heat exchanger for heat release and is cooled (heat radiation) by heat exchange with atmospheric air. Since the process of returning to the second container and condensing the steam is repeated, the plurality of cooling / heating locations can be simultaneously cooled.

また,前記第1容器における蒸発性液体を前記放吸熱用熱交換器との間で循環する一方,前記第2容器における蒸発性液体を前記各冷暖房用熱交換器との間で循環するという暖房運転にすることにより,第1容器において沸騰蒸発にて冷却された蒸発性液体は,放吸熱用熱交換器に送られて大気空気との熱交換にて暖められた(吸熱)のち再び第1容器にに戻って沸騰蒸発することを繰り返す一方,前記第2容器において蒸気凝縮にて温度が高くなった蒸発性液体は,複数の各冷暖房箇所における冷暖房用熱交換器に一斉に送られたのち再び前記第1容器に戻って蒸気を凝縮することを繰り返すから,前記複数の各冷暖房箇所を一斉に暖房することができる。   Further, the evaporating liquid in the first container is circulated between the heat-dissipating heat exchanger and the evaporating liquid in the second container is circulated between the air-conditioning heat exchangers. By making the operation, the evaporative liquid cooled by boiling evaporation in the first container is sent to the heat exchanger for heat release and heat absorption and warmed by heat exchange with the atmospheric air (heat absorption), and then the first liquid again. While returning to the container and repeatedly evaporating to the boil, the evaporating liquid whose temperature has increased due to vapor condensation in the second container is sent to the air conditioner heat exchangers in each of the plurality of air conditioners at the same time. Since the process of returning to the first container and condensing the steam is repeated, the plurality of cooling / heating locations can be heated at the same time.

このように,本発明によると,複数の冷暖房箇所を,これらについて共通する第1容器,第2容器,放吸熱用熱交換器及び蒸気圧縮機等にて,一斉に,冷房及び暖房することができるから,全体としての装置が非常に小型化できるばかりか,価格の大幅な低減を達成することができ,しかも,冷暖房に要するランニングコストの大幅な低減も達成することができる。   As described above, according to the present invention, it is possible to simultaneously cool and heat a plurality of air-conditioning locations in the first container, the second container, the heat-dissipating heat exchanger, the steam compressor, and the like, which are common to them. As a result, not only the overall device can be made very small, but also a significant reduction in price can be achieved, and in addition, a significant reduction in running cost required for air conditioning can be achieved.

その上,前記蒸気圧縮機を,先行技術のように正逆回転することなく,複数の冷暖房箇所を冷房又は暖房することができ,換言すると,蒸気圧縮機は,一方向への回転で良いから,その耐久性を大幅に向上できるとともに,各冷暖房箇所における冷暖房用熱交換器に供給する蒸発性液体の温度を,大気温度の変化及び熱負荷等に対して,略一定に保つように,前記蒸気圧縮機を回転制御することが,確実且つ正確にできる。   In addition, the steam compressor can be cooled or heated without forward and reverse rotation as in the prior art, in other words, the steam compressor can be rotated in one direction. The temperature of the evaporating liquid supplied to the cooling / heating heat exchanger at each heating / cooling location can be kept substantially constant with respect to changes in atmospheric temperature and heat load, etc. It is possible to reliably and accurately control the rotation of the steam compressor.

この場合において,請求項2に記載した構成によると,前記した一斉冷房中に,前記複数の各冷暖房箇所のうち任意の冷暖房箇所における冷暖房用熱交換器のみを,前記第1状態に切り換えることにより,前記第2容器において蒸気凝縮で温度が高くなった蒸発性液体の一部が,前記任意の冷暖房箇所における冷暖房用熱交換器のみに供給されたのちこの冷暖房用熱交換器より前記第2容器に戻るように流れることになるから,前記任意の冷暖房箇所のみを暖房にすることができる。   In this case, according to the configuration described in claim 2, during the simultaneous cooling described above, by switching only the heat exchanger for air conditioning at any air conditioning location among the plurality of air conditioning locations, to the first state. A part of the evaporating liquid whose temperature has increased in the second container due to vapor condensation is supplied only to the air conditioner heat exchanger in the arbitrary air conditioner, and then the second container is supplied from the air conditioner heat exchanger. Therefore, only the arbitrary cooling / heating point can be heated.

また,請求項2に記載した構成によると,前記した一斉暖房中において,前記複数の各冷暖房箇所のうち任意の冷暖房箇所における冷暖房用熱交換器のみを,前記第2状態に切り換えることにより,前記第2容器において沸騰蒸発にて温度が低くなった蒸発性液体の一部が,前記任意の冷暖房箇所における冷暖房用熱交換器に供給されたのちこの冷暖房用熱交換器より前記バイパス戻り管路を介して前記第2容器に戻るように流れることになるから,前記任意の冷暖房箇所のみを冷房にすることができる。   Further, according to the configuration described in claim 2, during the simultaneous heating described above, by switching only the heat exchanger for cooling / heating in any cooling / heating location among the plurality of cooling / heating locations to the second state, After a part of the evaporating liquid whose temperature has been lowered by boiling evaporation in the second container is supplied to the air conditioner heat exchanger at the arbitrary air conditioner location, the bypass return pipe is routed from the air conditioner heat exchanger. Therefore, only the arbitrary cooling / heating point can be cooled.

つまり,請求項2によると,前記複数の冷暖房箇所を各々別々に冷房及び暖房することができる。   That is, according to claim 2, the plurality of cooling / heating locations can be individually cooled and heated.

特に,請求項3に記載した構成によると,前記複数の冷暖房箇所の各々を冷房又は暖房している状態において,前記複数の冷暖房箇所のうち任意の冷暖房箇所における冷暖房用熱交換器のみを,当該冷暖房用熱交換器に蒸発性液体を流さないという第3状態に切り換えることにより,前記任意の冷暖房箇所のみを,冷房停止又は暖房停止にすることができるから,前記複数の冷暖房箇所を別々に冷房又は暖房にしたり,或いは冷暖房停止にしたりすることが自在にできる。   In particular, according to the configuration described in claim 3, in the state where each of the plurality of cooling / heating locations is cooled or heated, only the heat exchanger for cooling / heating at any of the plurality of cooling / heating locations is By switching to the third state in which no evaporating liquid is allowed to flow through the heat exchanger for cooling and heating, it is possible to stop cooling or heating only the arbitrary cooling and heating location, so that the plurality of cooling and heating locations can be separately cooled. Alternatively, it is possible to freely set the heating or to stop the cooling and heating.

そして,請求項4に記載した構成によると,前記複数の冷暖房箇所を別々に冷房又は暖房にしたり,或いは冷暖房停止にしたりすることの切り換えが,簡単な構成で確実に達成できる利点がある。   And according to the structure described in Claim 4, there exists an advantage which can be reliably achieved with a simple structure that the several air-conditioning location can be made into cooling or heating separately, or switching to air-conditioning stop.

以下,本発明の実施の形態を図面について説明する。   Embodiments of the present invention will be described below with reference to the drawings.

図1は,第1の実施の形態を示す。   FIG. 1 shows a first embodiment.

この図1において,符号1は,第1の冷暖房箇所を,符号2は,第2の冷暖房箇所を,そして,符号3は,第3の冷暖房箇所を各々示し,これら各冷暖房箇所1,2,3の各々には,間接熱交換式の冷暖房用熱交換器4,5,6が配設され,この各冷暖房用熱交換器4,5,6における入口4a,5a,6aには,ゾーンポンプ7,8,9が接続されている。   In FIG. 1, reference numeral 1 denotes a first cooling / heating location, reference numeral 2 denotes a second cooling / heating location, and reference 3 denotes a third cooling / heating location. 3 is provided with indirect heat exchange type air conditioners 4, 5, 6, and zone pumps are provided at the inlets 4 a, 5 a, 6 a of the air conditioners 4, 5, 6. 7, 8, and 9 are connected.

また,前記図1において,符号10は,密閉構造にした第1容器を,符号11は,同じく密閉構造にした第2容器を各々示し,これら両容器10,11のうちいずれか一方又は両方には,前記第1容器10及び前記第2容器11内の両方を大気圧より低い減圧にするための真空ポンプ12等の真空発生装置が接続されている。   In FIG. 1, reference numeral 10 denotes a first container having a sealed structure, and reference numeral 11 denotes a second container having the same sealed structure, and either or both of these containers 10 and 11 are shown. Is connected to a vacuum generator such as a vacuum pump 12 for reducing the pressure in both the first container 10 and the second container 11 below atmospheric pressure.

前記第1容器10と,前記各冷暖房用熱交換器4,5,6の入口4a,5a,6aにおけるゾーンポンプ7,8,9の吸い込み側との間を,循環ポンプ13を備えた第1循環供給管路14を介して並列に接続する一方,前記各冷暖房用熱交換器4,5,6の出口4b,5b,6bと,前記第1容器10との間を,第1循環戻り管路15を介して並列に接続することにより,前記第1容器10内に入れた水等の蒸発性液体を,第1循環供給管路14を介して前記各冷暖房用熱交換器4,5,6の入口4a,5a,6aに対して並列に供給したのち,この各冷暖房用熱交換器4,5,6の出口4b,5b,6bから第1循環戻り管路15を介して再び前記第1容器10内の上部にノズル16から噴出するように戻すという循環を行うように構成している。   A first circulation pump 13 is provided between the first container 10 and the suction side of the zone pumps 7, 8, 9 at the inlets 4 a, 5 a, 6 a of the heat exchangers 4, 5, 6. A first circulation return pipe is connected between the outlets 4b, 5b, 6b of the heat exchangers 4, 5, 6 and the first container 10 while being connected in parallel via the circulation supply pipe 14. By connecting in parallel via the passage 15, evaporating liquid such as water placed in the first container 10 is supplied to the heat exchangers 4, 5, 5 through the first circulation supply pipe 14. 6 in parallel to the inlets 4a, 5a and 6a, the outlets 4b, 5b and 6b of the heat exchangers 4 and 5 and 6 for the cooling and heating are again connected to the first through the first circulation return line 15. It is configured to circulate such that it returns to the upper part in one container 10 so as to be ejected from the nozzle 16. There.

前記第1循環供給管路14のうち前記各ゾーンポンプ7,8,9の吸い込み側への接続部には,入口側第1開閉弁17,18,19を設けており,また,前記第1循環戻り管路15のうち前記各冷暖房用熱交換器4,5,6における出口4b,5b,6bへの接続部には,出口側第1開閉弁20,21,22を設けている。   In the first circulation supply pipe 14, inlet-side first on-off valves 17, 18, 19 are provided at the connection portions of the zone pumps 7, 8, 9 to the suction side. Outlet-side first on-off valves 20, 21, and 22 are provided at the connection portions of the circulation return pipe 15 to the outlets 4 b, 5 b, 6 b in the heat exchangers 4, 5, 6.

一方,前記第2容器11内に入れた水等の蒸発性液体は,循環ポンプ23を備えた第2循環供給管路24にて汲み出して密閉型に構成した放吸熱用熱交換器25に送ったのち,第2循環戻り管路26を介して再び前記第2容器11内の上部にノズル27から噴出するように戻すという循環を行うように構成している。   On the other hand, evaporative liquid such as water put in the second container 11 is pumped out by a second circulation supply line 24 provided with a circulation pump 23 and sent to a heat-release heat exchanger 25 configured in a sealed type. After that, the circulation is performed such that the nozzle 27 returns to the upper part in the second container 11 again through the second circulation return pipe 26.

この場合,前記放吸熱用熱交換器25は,屋外に設置した通風塔25aと,その内部に設けた密閉構造の伝熱管25bとを備えて,前記第2容器11内における蒸発性液体が前記伝熱管25bの内部との間を循環するように構成する一方,前記通風塔25a内において,前記伝熱管25bの外側を,ポンプ25cにて循環する水を散布することに加えて,フアン25dにて大気の空気を強制通風するように構成している。   In this case, the heat exchanger 25 for releasing and absorbing heat includes a ventilation tower 25a installed outdoors, and a heat transfer tube 25b having a sealed structure provided therein, and the evaporating liquid in the second container 11 is the While being configured to circulate between the inside of the heat transfer tube 25b, in addition to spraying water circulating in the pump 25c outside the heat transfer tube 25b in the ventilation tower 25a, It is configured to forcibly vent the atmospheric air.

前記第2循環供給管路24における途中部分又は前記第2容器11と,前記各冷暖房用熱交換器4,5,6の入口4a,5a,6aにおけるゾーンポンプ7,8,9の吸い込み側との間を,バイパス供給管路28を介して並列に接続する一方,前記第2循環戻り管路26の途中部分又は前記第2容器11と,前記前記各冷暖房用熱交換器4,5,6の出口4b,5b,6bとの間を,バイパス戻り管路29を介して並列に接続することにより,前記第2容器11における蒸発性液体を,前記バイパス供給管路28を介して前記各冷暖房用熱交換器4,5,6の入口4a,5a,6aに対して並列に供給したのち,この各冷暖房用熱交換器4,5,6の出口4b,5b,6bから前記バイパス戻り管路29を介して前記第2容器11に戻すように構成している。   The middle part of the second circulation supply pipe 24 or the second container 11 and the suction side of the zone pumps 7, 8, 9 at the inlets 4 a, 5 a, 6 a of the heat exchangers 4, 5, 6. Are connected in parallel via a bypass supply line 28, while the middle part of the second circulation return line 26 or the second container 11 and the heat exchangers 4, 5 and 6 for cooling and heating. By connecting the outlets 4b, 5b, and 6b of the second container 11 in parallel via the bypass return pipe 29, the evaporating liquid in the second container 11 is supplied to the cooling / heating units via the bypass supply pipe 28. After supplying in parallel to the inlets 4a, 5a and 6a of the heat exchangers 4, 5 and 6, the bypass return pipes from the outlets 4b, 5b and 6b of the respective heat exchangers 4 and 5 and 6 for cooling and heating 29 to return to the second container 11 It is configured.

前記バイパス供給管路28のうち前記各ゾーンポンプ7,8,9の吸い込み側への接続部には,入口側第2開閉弁30,31,32を設けており,また,前記バイパス戻り管路29のうち前記各冷暖房用熱交換器4,5,6における出口4b,5b,6bへの接続部には,出口側第2開閉弁33,34,35を設けている。   In the bypass supply pipe 28, inlet-side second on-off valves 30, 31, 32 are provided at the connection portions of the zone pumps 7, 8, 9 to the suction side, and the bypass return pipe 29, outlet side second on-off valves 33, 34, and 35 are provided at connection portions to the outlets 4b, 5b, and 6b in the heat exchangers 4, 5, and 6 for cooling and heating.

更に,前記第1容器10の上部と前記第2容器11の上部の間は,蒸気ダクト36を介して接続され,この蒸気ダクト36の途中には,前記第1容器10における蒸気を圧縮して前記第2容器11に送り込むようにした回転式蒸気圧縮機における一つの例であるところのルーツ式圧縮機37が設けられている。   Furthermore, the upper part of the first container 10 and the upper part of the second container 11 are connected via a steam duct 36. The steam in the first container 10 is compressed in the middle of the steam duct 36. A Roots compressor 37 is provided as an example of the rotary steam compressor that is fed into the second container 11.

そして,前記第2容器11から放吸熱用熱交換器25への前記第2循環供給管路24の途中には,冷暖房用の第1切換弁38を設けるとともに,当該第2循環供給管路24のうち前記第1切換弁38より下流側の部分に,一端を前記第1容器10に対する前記第1循環供給管路14に接続するか又は前記第1容器10に接続して成る暖房用バイパス供給管路39の他端を接続して,この暖房用バイパス供給管路39に冷暖房用の第2切換弁40を設ける一方,前記第2容器11への前記第2循環戻り管路24には,冷暖房用の第3切換弁41を設けるとともに,当該第2循環戻り管路24のうち前記第3切換弁41の上流側の部分に,一端を前記第1容器10への第1循環戻り管路15に対して分岐接続するか又は前記第1容器10に接続して成る暖房用バイパス戻り管路42の他端を接続して,この暖房用バイパス戻り管路42に,冷暖房用の第4切換弁43を設ける。   A first switching valve 38 for cooling and heating is provided in the middle of the second circulation supply line 24 from the second container 11 to the heat exchanger 25 for releasing and absorbing heat, and the second circulation supply line 24 is provided. Of the first switching valve 38, one end of which is connected to the first circulation supply pipe 14 for the first container 10 or connected to the first container 10 for heating bypass supply. The other end of the pipe line 39 is connected, and a second switching valve 40 for cooling and heating is provided in the heating bypass supply pipe line 39, while the second circulation return pipe line 24 to the second container 11 is A third switching valve 41 for air conditioning is provided, and one end of the second circulation return pipe 24 on the upstream side of the third switching valve 41 is connected to the first container 10. 15 for branch connection or to the first container 10 Connect the other end of the heating bypass return line 42 comprising, in the heating bypass return line 42, provided with a fourth switch valve 43 for heating and cooling.

この構成において,図2に示すように,冷暖房用の第1切換弁38及び第3切換弁41を開いて冷暖房用の第2切換弁40及び第4切換弁43を閉じるという冷房運転の状態にすることに加えて,前記複数の各冷暖房箇所1,2,3における冷暖房用熱交換器4,5,6に対する入口側第1開閉弁17,18,19及び出口側第1開閉弁20,21,22を開いて入口側第2開閉弁30,31,32及び出口側第2開閉弁33,34,35を閉じるという状態に切り換え操作する。   In this configuration, as shown in FIG. 2, the first and second switching valves 38 and 41 for air conditioning are opened and the second switching valve 40 and the fourth switching valve 43 for cooling and heating are closed. In addition, the inlet side first on-off valves 17, 18, 19 and the outlet side first on-off valves 20, 21 for the heat exchangers 4, 5, 6 for the plurality of air conditioning locations 1, 2, 3 are used. , 22 are opened and the inlet side second on-off valves 30, 31, 32 and the outlet side second on-off valves 33, 34, 35 are closed.

これにより,前記第1容器10における蒸発性液体は沸騰蒸発し,この沸騰蒸発にて所定温度に冷却されたのち第1循環供給管路14を介して各冷暖房箇所1,2,3における冷暖房用熱交換器4,5,6に送られたのち第1循環戻り管路15を介して再び前記第1容器10に戻って沸騰蒸発することを繰り返す一方,前記第1容器10内での沸騰蒸発にて発生した蒸気は前記ルーツ式圧縮機37にて圧縮されたのち前記第2容器11に至り,ここにおける蒸発性液体にて凝縮され,この蒸気凝縮にて温度が高くなった蒸発性液体は,第2循環供給管路24を介して放吸熱用熱交換器25に送られてここでの大気空気との熱交換にて冷却された(放熱)のち第2循環戻り管路26を介して再び前記第2容器11に戻って蒸気を凝縮することを繰り返すから,前記複数の各冷暖房箇所1,2,3を一斉に冷房することができる。   As a result, the evaporating liquid in the first container 10 evaporates and is cooled to a predetermined temperature by the boiling evaporation, and then is used for cooling and heating at the heating and cooling locations 1, 2 and 3 via the first circulation supply pipe 14. After being sent to the heat exchangers 4, 5, and 6, it is repeatedly boiled and evaporated back to the first container 10 through the first circulation return line 15, while boiling evaporation in the first container 10 is repeated. The vapor generated in is compressed by the roots compressor 37 and then reaches the second container 11 where it is condensed by the evaporating liquid. The evaporating liquid whose temperature has been increased by the vapor condensation is Then, after being sent to the heat exchanger 25 for heat release and absorption through the second circulation supply line 24 and cooled by heat exchange with the atmospheric air here (heat radiation), via the second circulation return line 26 Back to the second container 11 again to condense the vapor. Since return Ri, it is possible to cool the plurality of the respective heating and cooling portions 1, 2 and 3 simultaneously.

この一斉冷房中において,図3に示すように,前記複数の各冷暖房箇所1,2,3のうち任意の冷暖房箇所,例えば,第2冷暖房箇所2における冷暖房用熱交換器5に対する入口側第1開閉弁18及び出口側第1開閉弁21を閉じて入口側第2開閉弁31及び出口側第2開閉弁34を開くことにより,前記第2冷暖房箇所2における冷暖房用熱交換器5に対して前記第1容器10からの蒸発性液体を供給止めて当該第2冷暖房箇所2における冷暖房用熱交換器5に対して前記第2容器11における蒸発性液体を供給しこの冷暖房用熱交換器5から前記第2容器11に戻すという第1状態に切り換える。   During this simultaneous cooling, as shown in FIG. 3, the first air inlet side with respect to the heating / cooling heat exchanger 5 at an arbitrary cooling / heating location, for example, the second cooling / heating location 2, among the plurality of cooling / heating locations 1, 2, 3. By closing the on-off valve 18 and the outlet-side first on-off valve 21 and opening the inlet-side second on-off valve 31 and the outlet-side second on-off valve 34, the air conditioner heat exchanger 5 in the second air conditioning location 2 The supply of the evaporating liquid from the first container 10 is stopped, and the evaporating liquid in the second container 11 is supplied to the cooling / heating heat exchanger 5 in the second cooling / heating section 2 from the cooling / heating heat exchanger 5. The first container is switched back to the second container 11.

これにより,前記第2冷暖房箇所2における冷暖房用熱交換器5には,前記第2容器11において蒸気凝縮で温度が高くなった蒸発性液体の一部が,バイパス供給管路28を介して供給されたのちバイパス戻り管路29を介して第2容器11に戻るように流れるから,前記第2冷暖房箇所2のみを,他の第1冷暖房箇所1及び第3冷暖房箇所3を冷房にしたままで,暖房にすることができる。   As a result, a part of the evaporating liquid whose temperature has increased due to vapor condensation in the second container 11 is supplied to the cooling / heating heat exchanger 5 in the second cooling / heating section 2 via the bypass supply line 28. After that, since it flows so as to return to the second container 11 via the bypass return conduit 29, only the second air-conditioning location 2 is left in the other first air-conditioning location 1 and the third air-conditioning location 3 while cooling. , Can be heating.

また,前記第2冷暖房箇所2における冷暖房用熱交換器5に対する入口側第1開閉弁18及び出口側第1開閉弁21を閉じるとともに,入口側第2開閉弁31及び出口側第2開閉弁34を閉じるという第3状態に切り換えることにより,前記第2冷暖房箇所2のみを,他の第1冷暖房箇所1及び第3冷暖房箇所3を冷房にしたままで,冷房停止にすることができる。   In addition, the inlet-side first on-off valve 18 and the outlet-side first on-off valve 21 for the air-conditioning heat exchanger 5 in the second air-conditioning location 2 are closed, and the inlet-side second on-off valve 31 and the outlet-side second on-off valve 34 are closed. By switching to the third state that is closed, it is possible to stop the cooling while only the second cooling / heating point 2 is kept in the cooling state of the other first cooling / heating points 1 and the third cooling / heating point 3.

これら第1状態への切り換え操作又は第3状態への切り換え操作は,他の第1冷暖房箇所1及び第3冷暖房箇所3についても同様に行うことができることはいうまでもない。   It goes without saying that the switching operation to the first state or the switching operation to the third state can be similarly performed for the other first air-conditioning places 1 and the third air-conditioning places 3.

次に,図4に示すように,冷暖房用の第1切換弁38及び第3切換弁41を閉じて冷暖房用の第2切換弁40及び第4切換弁43を開くという暖房運転の状態にすることに加えて,前記複数の各冷暖房箇所1,2,3における冷暖房用熱交換器4,5,6に対する入口側第1開閉弁17,18,19及び出口側第1開閉弁20,21,22を閉じて入口側第2開閉弁30,31,32及び出口側第2開閉弁34,35,36を開くという状態に切り換え操作する。   Next, as shown in FIG. 4, the first and second switching valves 38 and 41 for cooling and heating are closed and the second switching valve 40 and the fourth switching valve 43 for cooling and heating are opened. In addition, the inlet-side first on-off valves 17, 18, 19 and the outlet-side first on-off valves 20, 21, with respect to the air-conditioning heat exchangers 4, 5, 6 at the plurality of air-conditioning locations 1, 2, 3, 22 is closed and the inlet-side second on-off valves 30, 31, 32 and the outlet-side second on-off valves 34, 35, 36 are opened.

これにより,前記第1容器10において沸騰蒸発にて冷却された蒸発性液体は,各冷暖房用熱交換器4,5,6に送られることなく,暖房用バイパス供給管路39を介して放吸熱用熱交換器25に送られ,ここで大気空気との熱交換にて暖められた(吸熱)のち暖房用バイパス戻り管路42を介して再び前記第1容器10に戻って沸騰蒸発することを繰り返す一方,前記第1容器10内での沸騰蒸発にて発生した蒸気は前記ルーツ式圧縮機37で圧縮されたのち前記第2容器11に至り,ここにおける蒸発性液体にて凝縮され,この蒸気凝縮にて温度が高くなった蒸発性液体は,放吸熱用熱交換器25に送られることなく,バイパス供給管路28を介して各冷暖房箇所1,2,3における冷暖房用熱交換器4,5,6に一斉に送られたのちバイパス戻り管路29を介して再び前記第2容器11に戻って蒸気を凝縮することを繰り返すから,前記複数の各冷暖房箇所1,2,3を一斉暖房にすることができる。   As a result, the evaporative liquid cooled by boiling evaporation in the first container 10 is not sent to the heat exchangers 4, 5, 6 for cooling and heating, but is released and absorbed through the heating bypass supply pipe 39. Is sent to the heat exchanger 25 for heating, where it is heated by heat exchange with the atmospheric air (heat absorption), and then returns to the first container 10 again via the heating bypass return line 42 to evaporate to the boil. On the other hand, the steam generated by boiling evaporation in the first container 10 is compressed by the roots compressor 37 and then reaches the second container 11 where it is condensed by the evaporating liquid. The evaporating liquid whose temperature has increased due to the condensation is not sent to the heat-dissipating heat exchanger 25, but is supplied to the air-conditioning heat exchangers 4, 1, 2, 3 via the bypass supply pipe 28. After being sent to 5 and 6 all at once Since repeated to condense the steam back to the second container 11 again via the return path pipe 29, the plurality of the respective heating and cooling locations 1,2,3 can be simultaneously heating.

この一斉暖房中において,図5に示すように,前記複数の各冷暖房箇所1,2,3のうち任意の冷暖房箇所,例えば,第2冷暖房箇所2における冷暖房用熱交換器5に対する入口側第1開閉弁18及び出口側第1開閉弁21を開いて入口側第2開閉弁31及び出口側第2開閉弁34を閉じることにより,前記第2冷暖房箇所2における冷暖房用熱交換器5に対して前記第2容器11からの蒸発性液体を供給することを止めて当該第2冷暖房箇所2における冷暖房用熱交換器5に対して前記第1容器10からの蒸発性液体を供給しこの冷暖房用熱交換器5から前記第1容器10に戻すとする第2状態に切り換える。   During this simultaneous heating, as shown in FIG. 5, the first air inlet side with respect to the heating / cooling heat exchanger 5 in any one of the plurality of cooling / heating locations 1, 2, 3, for example, the second cooling / heating location 2. By opening the on-off valve 18 and the outlet-side first on-off valve 21 and closing the inlet-side second on-off valve 31 and the outlet-side second on-off valve 34, the air-conditioning heat exchanger 5 in the second air-conditioning location 2 The supply of the evaporative liquid from the second container 11 is stopped, and the evaporative liquid from the first container 10 is supplied to the cooling / heating heat exchanger 5 at the second cooling / heating location 2 to thereby supply the heating / cooling heat. It switches to the 2nd state which returns to the said 1st container 10 from the exchanger 5. FIG.

これにより,前記第2冷暖房箇所2における冷暖房用熱交換器5には,前記第1容器10において沸騰蒸発にて温度が低くなった蒸発性液体の一部が,第1循環供給管路14を介して供給されたのち第1循環戻り管路15を介して第1容器10に戻るように流れるから,前記第2冷暖房箇所2のみを,他の第1冷暖房箇所1及び第3冷暖房箇所3を暖房にしたままで,冷房にすることができる。   As a result, a part of the evaporating liquid whose temperature has been lowered by boiling evaporation in the first container 10 passes through the first circulation supply line 14 in the heat exchanger 5 for cooling and heating in the second cooling / heating section 2. Since it flows so that it may return to the 1st container 10 via the 1st circulation return pipe line 15, only the said 2nd cooling / heating location 2 is connected to the other 1st cooling / heating location 1 and the 3rd cooling / heating location 3. It can be cooled with heating.

また,前記第2冷暖房箇所2における冷暖房用熱交換器5に対する入口側第1開閉弁18及び出口側第1開閉弁21を閉じるとともに,入口側第2開閉弁31及び出口側第2開閉弁34を閉じるという第3状態に切り換えることにより,前記第2冷暖房箇所2のみを,他の第1冷暖房箇所1及び第3冷暖房箇所3を暖房にしたままで,暖房停止にすることができる。   In addition, the inlet-side first on-off valve 18 and the outlet-side first on-off valve 21 for the air-conditioning heat exchanger 5 in the second air-conditioning location 2 are closed, and the inlet-side second on-off valve 31 and the outlet-side second on-off valve 34 are closed. By switching to the third state of closing, the heating can be stopped while only the second cooling / heating point 2 is heated while the other first cooling / heating point 1 and the third cooling / heating point 3 are heated.

これら第2状態への切り換え操作又は第3状態への切り換え操作は,他の第1冷暖房箇所1及び第3冷暖房箇所3についても同様に行うことができることはいうまでもない。   It goes without saying that the switching operation to the second state or the switching operation to the third state can be performed in the same manner for the other first cooling / heating points 1 and the third cooling / heating point 3.

以上のとおり,本実施の形態によると,複数の各冷暖房箇所1,2,3を一斉に冷房又は暖房することができることに加えて,前記複数の冷暖房箇所1,2,3を各々別々に冷房及び暖房することができるとともに,前記複数の冷暖房箇所1,2,3を各々別々に冷房停止及び暖房停止にすることができる。   As described above, according to the present embodiment, in addition to being able to simultaneously cool or heat each of the plurality of cooling and heating locations 1, 2, and 3, the plurality of cooling and heating locations 1, 2, and 3 can be individually cooled. In addition, the plurality of cooling / heating locations 1, 2, and 3 can be individually stopped for cooling and heating.

図6は,第2の実施の形態を示す。   FIG. 6 shows a second embodiment.

前記した第1の実施の形態は,前記第2容器11における蒸発性液体(冷房運転のとき)又は第1容器10における蒸発性液体(暖房運転のとき)を,密閉型の放吸熱用熱交換器25に送って大気と間接的に熱交換する場合であったが,この第2の実施の形態は,前記第2容器11における蒸発性液体又は第1容器10における蒸発性液体と大気との間接的な熱交換に,開放型の放吸熱用熱交換器44を使用した場合であり,その他の構成は,前記第1の実施の形態の場合と同様である。   In the first embodiment described above, the evaporative liquid in the second container 11 (during cooling operation) or the evaporative liquid in the first container 10 (during heating operation) is used as a heat exchanger for hermetic heat release. In the second embodiment, the second container 11 or the volatile liquid in the first container 10 and the atmosphere are exchanged heat with the atmosphere. This is a case where an open-type heat release / absorption heat exchanger 44 is used for indirect heat exchange, and the other configurations are the same as those in the first embodiment.

すなわち,この第2の実施の形態における開放型の冷却用熱交換器44は,不凍液を入れた流体室44a内に密閉型の伝熱管44bを設けて,この伝熱管44bの内部と前記第2容器11又は前記第1容器10との間を,その蒸発性液体が循環するようにして,前記流体室44a内において,前記第2容器11における蒸発性液体又は第1容器10における蒸発性液体と,当該流体室44a内に入れた不凍液との間で間接的な熱交換を行うように構成する一方,フアン44cによる強制通風の通風塔44d内に,ラシヒリング等の充填層44eを設け,この通風塔44dの底に溜まる前記不凍液を循環ポンプ44fにて汲み出して,前記流体室44a内に供給し,次いで,この流体室44a内における不凍液を前記通風塔44d内における充填層44eに対してノズル44gにて散布して,この充填層44eを流下するという循環を行うことにより,前記不凍液を,前記通風塔44d内における大気空気との直接接触にて熱交換し,この熱交換したあとの不凍液と,前記第2容器11又は第1容器10と前記伝熱管44b内との間を循環する蒸発性液体とを間接的に熱交換するように構成したものである。   That is, the open type cooling heat exchanger 44 in the second embodiment is provided with a sealed heat transfer tube 44b in a fluid chamber 44a containing an antifreeze liquid, and the inside of the heat transfer tube 44b and the second heat transfer tube 44b. In the fluid chamber 44a, the evaporating liquid in the second container 11 or the evaporating liquid in the first container 10 is circulated between the container 11 or the first container 10 and the evaporating liquid in the fluid chamber 44a. In addition, an indirect heat exchange with the antifreeze contained in the fluid chamber 44a is performed, while a packed bed 44e such as Raschig ring is provided in a forced ventilation ventilating tower 44d by the fan 44c. The antifreeze liquid accumulated at the bottom of the tower 44d is pumped out by the circulation pump 44f and supplied into the fluid chamber 44a, and then the antifreeze liquid in the fluid chamber 44a is filled in the ventilation tower 44d. By spraying the nozzle 44g on the layer 44e and circulating the packed bed 44e, the antifreeze liquid is subjected to heat exchange in direct contact with atmospheric air in the ventilation tower 44d. The antifreeze after the heat exchange and the evaporating liquid circulating between the second container 11 or the first container 10 and the heat transfer pipe 44b are indirectly heat exchanged.

この第2の実施の形態においては,前記第1容器10内及び第2容器11内を大気圧よりも低い減圧に保った状態のもとで,「開放型の冷却用熱交換器44」を使用することができる。また,大気との熱交換に不凍液を使用することにより,大気温度が氷点以下に下がった場合において,前記第2容器11における蒸発性液体又は第1容器10における蒸発性液体に凍結が発生することを確実に回避できる。   In the second embodiment, the “open-type cooling heat exchanger 44” is installed in a state where the inside of the first container 10 and the second container 11 is maintained at a pressure lower than the atmospheric pressure. Can be used. Further, by using an antifreeze liquid for heat exchange with the atmosphere, freezing occurs in the evaporating liquid in the second container 11 or the evaporating liquid in the first container 10 when the atmospheric temperature falls below the freezing point. Can be avoided reliably.

従って,前記した請求項1のうち「大気との間で熱交換を行う放吸熱用熱交換器」には,前記第1の実施の形態において説明した「密閉型の放吸熱用熱交換器25」は勿論のこと,前記第2の実施の形態において説明した「開放型の放吸熱用熱交換器44」を当然に含むものである。   Therefore, in the above-mentioned claim 1, the “heat release heat exchanger for exchanging heat with the atmosphere” includes the “sealed heat release heat exchanger 25” described in the first embodiment. Needless to say, the “open heat release heat exchanger 44” described in the second embodiment is naturally included.

なお,前記各実施の形態において,第1容器10における蒸発性液体及び第2容器11における蒸発性液体としては,前記各実施の形態として説明した水か,又は各種の水溶液に限らず,アルコール等のようなその他の蒸発性液体を使用することができるほか,これら水等の蒸発性液体に不凍結剤,防蝕剤,防錆剤又は防スケール剤を適宜添加しても良いことはいうまでもない。   In each of the above embodiments, the evaporating liquid in the first container 10 and the evaporating liquid in the second container 11 are not limited to the water described in each of the above embodiments or various aqueous solutions, but may be alcohol or the like. It is needless to say that other evaporating liquids such as can be used, and antifreezing agents, anticorrosives, rust inhibitors or scale inhibitors may be appropriately added to these evaporating liquids such as water. Absent.

また,前記蒸気圧縮機としては,前記各実施の形態で説明したルーツ式圧縮機に限らず,可変翼式圧縮機又はねじ式圧縮機等のような回転式圧縮機を使用することができる。   Further, the steam compressor is not limited to the Roots compressor described in each of the above embodiments, and a rotary compressor such as a variable wing compressor or a screw compressor can be used.

本発明の第1の実施の形態を示す図である。It is a figure which shows the 1st Embodiment of this invention. 前記第1の実施の形態において複数の冷暖房箇所を一斉冷房にしている場合を示す図である。It is a figure which shows the case where the several air-conditioning location is made into simultaneous cooling in the said 1st Embodiment. 前記第1の実施の形態において一斉冷房中に一部の冷暖房箇所のみを暖房にしている場合を示す図である。It is a figure which shows the case where only some air-conditioning locations are heating during simultaneous cooling in the said 1st Embodiment. 前記第1の実施の形態において複数の冷暖房箇所を一斉暖房にしている場合を示す図である。It is a figure which shows the case where the several air-conditioning location is made into simultaneous heating in the said 1st Embodiment. 前記第1の実施の形態において一斉冷房中に一部の冷暖房箇所のみを冷房にしている場合を示す図である。It is a figure which shows the case where only the one part air-conditioning location is air-conditioning during simultaneous air_conditioning | cooling in the said 1st Embodiment. 本発明の第2の実施の形態における放吸熱用熱交換器を示す図である。It is a figure which shows the heat exchanger for endothermic heat absorption in the 2nd Embodiment of this invention.

符号の説明Explanation of symbols

1,2,3 冷暖房箇所
4,5,6 冷暖房用熱交換器
4a,5a,6a 冷暖房用熱交換器の入口
4b,5b,6b 冷暖房用熱交換器の出口
10 第1容器
11 第2容器
12 真空ポンプ
14 第1循環供給管路
15 第1循環戻り管路
25,44 放吸熱用熱交換器
24 第2循環供給管路
26 第2循環戻り管路
17,18,19 入口側第1開閉弁
20,21,22 出口側第1開閉弁
28 バイパス供給管路
29 バイパス戻り管路
30,31,32 入口側第2開閉弁
33,34,35 出口側第2開閉弁
36 蒸気ダクト
37 ルーツ式圧縮機(蒸気圧縮機)
39 暖房用バイパス供給管路
42 暖房用バイパス戻り管路
38 暖房用第1切換弁
40 暖房用第2切換弁
41 暖房用第3切換弁
43 暖房用第4切換弁
1, 2, 3 Heating / cooling points 4, 5, 6 Heat exchanger for air conditioning 4a, 5a, 6a Entrance of heat exchanger for air conditioning 4b, 5b, 6b Exit of heat exchanger for air conditioning 10 First container 11 Second container 12 Vacuum pump 14 First circulation supply line 15 First circulation return line 25, 44 Heat exchanger for heat release and absorption 24 Second circulation supply line 26 Second circulation return line 17, 18, 19 Inlet side first on-off valve 20, 21, 22 Outlet side first on-off valve 28 Bypass supply line 29 Bypass return line 30, 31, 32 Inlet side second on-off valve 33, 34, 35 Outlet side second on-off valve 36 Steam duct 37 Roots type compression Machine (steam compressor)
39 Heating bypass supply line 42 Heating bypass return line 38 Heating first switching valve 40 Heating second switching valve 41 Heating third switching valve 43 Heating fourth switching valve

Claims (4)

少なくとも,減圧に保持した第1容器及び第2容器と,複数の各冷暖房箇所の各々に設置した複数個の冷暖房用熱交換器と,大気との間で熱交換を行う放吸熱用熱交換器とを備え,更に,前記第1容器における蒸発性液体を前記各冷暖房用熱交換器に並列に供給しこの各冷暖房用熱交換器から前記第1容器に戻るように循環する第1循環管路と,前記第2容器における蒸発性液体を前記放吸熱用熱交換器に供給しこの放吸熱用熱交換器から前記第2容器に戻すように循環する第2循環管路と,前記第1容器と第2容器の相互間を接続する蒸気ダクトと,この蒸気ダクトに前記第1容器から第2容器の方向に蒸気圧縮を行うようにした蒸気圧縮機とを備えて成り,
前記第1容器における蒸発性液体を前記各冷暖房箇所における冷暖房用熱交換器との間で循環する一方,前記第2容器における蒸発性液体を前記放吸熱用熱交換器との間で循環するという冷房運転と,
前記第1容器における蒸発性液体を前記放吸熱用熱交換器との間で循環する一方,前記第2容器における蒸発性液体を前記各冷暖房箇所における冷暖房用熱交換器との間で循環するという暖房運転とに,
切り換え可能に構成した,
ことを特徴とする蒸発式空調装置。
At least a first container and a second container held under reduced pressure, a plurality of cooling / heating heat exchangers installed at each of a plurality of cooling / heating locations, and a heat exchanger for heat release and absorption that exchanges heat with the atmosphere And supplying the evaporative liquid in the first container to each of the air conditioner heat exchangers in parallel and circulating the air from the air conditioner heat exchangers back to the first container. A second circulation line that circulates the evaporative liquid in the second container to the heat release heat exchanger and circulates back to the second container from the heat release heat exchanger, and the first container A steam duct connecting between the first container and the second container, and a steam compressor configured to perform steam compression in the direction from the first container to the second container in the steam duct,
The evaporative liquid in the first container circulates between the cooling / heating heat exchangers in each of the air-conditioning locations, while the evaporative liquid in the second container circulates between the heat-dissipating heat exchangers. Cooling operation,
The evaporative liquid in the first container is circulated between the heat-release heat exchanger and the evaporative liquid in the second container is circulated between the air-conditioner heat exchangers in the respective air-conditioning locations. For heating operation,
Configured to be switchable,
An evaporative air conditioner characterized by that.
前記請求項1の記載において,前記複数の各冷暖房箇所における冷暖房用熱交換器の各々に,
前記冷房運転の中に,前記各冷暖房用熱交換器のうち一部の冷暖房用熱交換器に対する前記第1容器からの蒸発性液体の供給を止めて当該一部の冷暖房用熱交換器に対して前記第2容器における蒸発性液体を供給しこの一部の冷暖房用熱交換器から前記第2容器に戻す第1状態と,
前記暖房運転の中に,前記各冷暖房用熱交換器のうち一部の冷暖房用熱交換器に対する前記第2容器からの蒸発性液体の供給を止めて当該一部の冷暖房用熱交換器に対して前記第1容器の蒸発性液体を供給しこの一部の冷暖房用熱交換器から前記第1容器に戻す第2状態とに,
切り換えるようにした切換手段を備えている,
ことを特徴とする蒸発式空調装置。
In the description of claim 1, in each of the heat exchangers for cooling and heating at each of the plurality of cooling and heating locations,
During the cooling operation, supply of the evaporative liquid from the first container to a part of the air conditioner heat exchangers among the air conditioner heat exchangers is stopped and the part of the air conditioner heat exchangers is stopped. A first state in which the evaporative liquid in the second container is supplied and returned to the second container from a part of the heat exchanger for cooling and heating,
During the heating operation, the supply of the evaporative liquid from the second container to a part of the air conditioner heat exchangers among the air conditioner heat exchangers is stopped to the part of the air conditioner heat exchangers. To the second state in which the evaporative liquid in the first container is supplied and returned to the first container from a part of the heat exchanger for cooling and heating,
Switching means adapted to switch,
An evaporative air conditioner characterized by that.
前記請求項2の記載において,前記各切換手段が,
前記第1状態と前記第2状態とに切り換える構成であることに加えて,
前記各冷暖房用熱交換器に対する両容器からの蒸発性液体の供給を止めるようにした第3状態にも切り換えできる,
構成であることを特徴とする蒸発式空調装置。
In the description of claim 2, each of the switching means includes:
In addition to being configured to switch between the first state and the second state,
It is possible to switch to the third state in which the supply of the evaporable liquid from both containers to each of the air conditioner heat exchangers is stopped.
An evaporative air conditioner characterized by having a configuration.
前記請求項2又は3の記載において,前記各切換手段が,
前記第2容器における蒸発性液体の一部を前記各冷暖房用熱交換器の入口に供給するバイパス供給管路と,
前記各冷暖房用熱交換器の出口を前記第2容器又は前記第2循環管路に接続するバイパス戻り管路と,
前記第1循環管路及び前記バイパス供給管路のうち前記各冷暖房用熱交換器の入口に接続する部分に設けた入口側開閉弁と,
前記第1循環管路及び前記バイパス戻り管路のうち前記各冷暖房用熱交換器の出口に接続する部分に設けた出口側開閉弁とで,
構成されていることを特徴とする蒸発式空調装置。
In the claim 2 or 3, the switching means is
A bypass supply line for supplying a part of the evaporable liquid in the second container to the inlet of each of the air conditioner heat exchangers;
A bypass return pipe connecting an outlet of each of the air conditioner heat exchangers to the second container or the second circulation pipe;
An inlet-side on-off valve provided at a portion of the first circulation pipe and the bypass supply pipe connected to the inlet of each of the air conditioner heat exchangers;
An outlet-side on-off valve provided at a portion of the first circulation line and the bypass return line that is connected to the outlet of each heat exchanger for cooling and heating,
An evaporative air conditioner characterized by comprising.
JP2007122505A 2007-05-07 2007-05-07 Evaporative air conditioner Expired - Fee Related JP4857179B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007122505A JP4857179B2 (en) 2007-05-07 2007-05-07 Evaporative air conditioner

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2007122505A JP4857179B2 (en) 2007-05-07 2007-05-07 Evaporative air conditioner

Publications (2)

Publication Number Publication Date
JP2008275288A true JP2008275288A (en) 2008-11-13
JP4857179B2 JP4857179B2 (en) 2012-01-18

Family

ID=40053438

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2007122505A Expired - Fee Related JP4857179B2 (en) 2007-05-07 2007-05-07 Evaporative air conditioner

Country Status (1)

Country Link
JP (1) JP4857179B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012147366A1 (en) * 2011-04-28 2012-11-01 パナソニック株式会社 Freezer
JP2014214936A (en) * 2013-04-24 2014-11-17 株式会社ササクラ Air conditioning system
JP2015520351A (en) * 2012-05-16 2015-07-16 エフィシエント・エネルギ・ゲーエムベーハー Heat pump and heat pump method in free cooling mode
US20160054033A1 (en) * 2014-08-21 2016-02-25 Panasonic Intellectual Property Management Co., Ltd. Refrigerating cycle apparatus
US9719699B2 (en) 2011-04-28 2017-08-01 Panasonic Intellectual Property Management Co., Ltd. Refrigeration device

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0252964A (en) * 1988-08-15 1990-02-22 Mitsubishi Electric Corp Multiroom type refrigerating circuit
JPH02146474A (en) * 1988-11-26 1990-06-05 Toupure Kk Air-conditioning equipment
JP2003314915A (en) * 2002-04-22 2003-11-06 Sanken Setsubi Kogyo Co Ltd Water cooling medium natural-circulation cooling system by water vapor compression refrigerating machine
JP2004340492A (en) * 2003-05-16 2004-12-02 Sanken Setsubi Kogyo Co Ltd Cooling system
JP2006038333A (en) * 2004-07-27 2006-02-09 Sanken Setsubi Kogyo Co Ltd Air conditioning system using vapor compression refrigerating machine

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0252964A (en) * 1988-08-15 1990-02-22 Mitsubishi Electric Corp Multiroom type refrigerating circuit
JPH02146474A (en) * 1988-11-26 1990-06-05 Toupure Kk Air-conditioning equipment
JP2003314915A (en) * 2002-04-22 2003-11-06 Sanken Setsubi Kogyo Co Ltd Water cooling medium natural-circulation cooling system by water vapor compression refrigerating machine
JP2004340492A (en) * 2003-05-16 2004-12-02 Sanken Setsubi Kogyo Co Ltd Cooling system
JP2006038333A (en) * 2004-07-27 2006-02-09 Sanken Setsubi Kogyo Co Ltd Air conditioning system using vapor compression refrigerating machine

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012147366A1 (en) * 2011-04-28 2012-11-01 パナソニック株式会社 Freezer
CN103502748A (en) * 2011-04-28 2014-01-08 松下电器产业株式会社 Freezer
US9157684B2 (en) 2011-04-28 2015-10-13 Panasonic Intellectual Property Management Co., Ltd. Refrigeration apparatus
CN103502748B (en) * 2011-04-28 2016-01-13 松下电器产业株式会社 Refrigerating plant
JP5923739B2 (en) * 2011-04-28 2016-05-25 パナソニックIpマネジメント株式会社 Refrigeration equipment
US9719699B2 (en) 2011-04-28 2017-08-01 Panasonic Intellectual Property Management Co., Ltd. Refrigeration device
JP2015520351A (en) * 2012-05-16 2015-07-16 エフィシエント・エネルギ・ゲーエムベーハー Heat pump and heat pump method in free cooling mode
US10041708B2 (en) 2012-05-16 2018-08-07 Efficient Energy Gmbh Heat pump and method for pumping heat in a free cooling mode
US10222103B2 (en) 2012-05-16 2019-03-05 Efficient Energy Gmbh Heat pump and method for pumping heat in a free cooling mode
JP2014214936A (en) * 2013-04-24 2014-11-17 株式会社ササクラ Air conditioning system
US20160054033A1 (en) * 2014-08-21 2016-02-25 Panasonic Intellectual Property Management Co., Ltd. Refrigerating cycle apparatus
US9689588B2 (en) * 2014-08-21 2017-06-27 Panasonic Intellectual Property Management Co., Ltd. Refrigerating cycle apparatus

Also Published As

Publication number Publication date
JP4857179B2 (en) 2012-01-18

Similar Documents

Publication Publication Date Title
US6321460B1 (en) Drying apparatus
JP4753312B2 (en) Air conditioner using groundwater
JPH0221139A (en) Indirect type air conditioner
JP4857179B2 (en) Evaporative air conditioner
JPH07233968A (en) Air conditioner system
KR101347582B1 (en) Low temperature water two-stage absorbtion type refrigerator and heater which can heating water
KR101552346B1 (en) recovery apparatus of oil vapor
JP6818198B2 (en) Energy efficient central air conditioning and heat pump system
JPH03233265A (en) Absorbing type heat pump
KR100243521B1 (en) Air-cooled absorption-type air conditioning apparatus
JP4958628B2 (en) Evaporative air conditioner
JP2008261604A (en) Evaporative air conditioner
JP2010255939A (en) Air conditioning system
KR100946381B1 (en) Hybrid heat pump type cooling and heating apparatus
CN105723167B (en) Pipeline configuration, cooling device and refrigerant vapour carrying method using pipeline configuration
JP2007253067A (en) Wet dehumidifier
US20180035568A1 (en) Data center cooling system
JP2007285531A (en) Heat exchange tube, evaporator and heat pump
JP5921788B1 (en) Cooling system
CN219995453U (en) Runner dehumidification device of self-supply cold source
KR100818544B1 (en) Regenerative Heat Pump Air Conditioning System
KR101343424B1 (en) Regenerative evaporative cooler
JP2008000660A (en) Organic solvent concentrator
KR20040019825A (en) Equipment for dehumidification and dryness
CN207317573U (en) Cooling tower

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20100218

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20110914

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20111018

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20111031

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20141104

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

Ref document number: 4857179

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees