JP2006017427A - Cooling system - Google Patents

Cooling system Download PDF

Info

Publication number
JP2006017427A
JP2006017427A JP2004198018A JP2004198018A JP2006017427A JP 2006017427 A JP2006017427 A JP 2006017427A JP 2004198018 A JP2004198018 A JP 2004198018A JP 2004198018 A JP2004198018 A JP 2004198018A JP 2006017427 A JP2006017427 A JP 2006017427A
Authority
JP
Japan
Prior art keywords
steam
hot water
condenser
cooling
pipe
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
JP2004198018A
Other languages
Japanese (ja)
Other versions
JP4317793B2 (en
Inventor
Kenji Ikoma
賢二 生駒
Isao Hirano
功 平野
Shinichiro Watabe
信一郎 渡部
Tatsu Ninomiya
達 二宮
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.)
Kansai Electric Power Co Inc
Toyo Seisakusho KK
Original Assignee
Kansai Electric Power Co Inc
Toyo Seisakusho KK
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 Kansai Electric Power Co Inc, Toyo Seisakusho KK filed Critical Kansai Electric Power Co Inc
Priority to JP2004198018A priority Critical patent/JP4317793B2/en
Publication of JP2006017427A publication Critical patent/JP2006017427A/en
Application granted granted Critical
Publication of JP4317793B2 publication Critical patent/JP4317793B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P80/00Climate change mitigation technologies for sector-wide applications
    • Y02P80/10Efficient use of energy, e.g. using compressed air or pressurized fluid as energy carrier
    • Y02P80/15On-site combined power, heat or cool generation or distribution, e.g. combined heat and power [CHP] supply

Landscapes

  • Heat-Pump Type And Storage Water Heaters (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To carry out effective utilization of energy by concurrently or selectively supplying steam and hot water by using condensation exhaust heat recovered from a condensing unit as a heat source, to use a compressor and a cooling tower of smaller scales in the condensing unit, and to reduce device costs and running costs. <P>SOLUTION: The cooling system is provided with the condensing unit 1 connected to a cooling tower 12, and a heat pump type steam/hot water generator 17 heating water supplied to a condensing means by heat of condensation of a refrigerant to supply steam and hot water. A change-over mechanism 20 is provided for changing over water from a condenser 3 in the condensing unit 1 to one or both of the cooling tower 12, and an evaporator in the steam/hot water generator 17, and it is composed such that the condensation exhaust heat can be changed over to one or both of discharge to the atmosphere from the cooling tower, and recovery by the steam/hot water generator. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は冷熱を発生するコンデンシングユニットの凝縮排熱を蒸気・温水発生装置の熱源とする冷却システムに関する。   The present invention relates to a cooling system that uses the condensed exhaust heat of a condensing unit that generates cold as a heat source of a steam / hot water generator.

各種工場においては冷熱と蒸気・温水を同時に利用するケースが多く、例えば食品製造工場においては、空調装置、冷却・凍結装置や冷凍・冷蔵倉庫のように多量の冷熱を使用する反面、蒸気殺菌、加熱工程で多量の低圧蒸気や90℃以上の殺菌洗浄用高温水を使用する。   Many factories often use cold heat and steam / hot water at the same time.For example, food manufacturing factories use large amounts of cold heat, such as air conditioners, cooling / freezing devices, and refrigerated / refrigerated warehouses. A large amount of low-pressure steam or high-temperature water for sterilization and washing at 90 ° C. or higher is used in the heating process.

上記冷熱の生成においては、圧縮式冷媒回路を備える冷却装置によるのが一般的であり、同冷却装置のコンデンシングユニットは冷媒の凝縮熱を冷却塔から大気に排熱として放出している。この排熱はヒートアイランド現象の主な原因であることが指摘されており、排熱を回収できるようにすることは省エネルギの観点からだけではなく環境面からも要求される。   The generation of the cold is generally performed by a cooling device including a compression refrigerant circuit, and the condensing unit of the cooling device releases the heat of condensation of the refrigerant from the cooling tower to the atmosphere as exhaust heat. It has been pointed out that this exhaust heat is the main cause of the heat island phenomenon, and it is required not only from the viewpoint of energy saving but also from the environmental aspect to be able to recover the exhaust heat.

また、上記コンデンシングユニットの圧縮機および冷却塔は、冷却装置に要求される冷凍能力に応じた性能のものを採用する必要があり、通常は冷却負荷が最も大となり、しかも冷却水温度が高くなって凝縮温度が上昇する夏季の日中における外気温湿度の条件下で充分な冷凍能力を得られるようにしなければならず、夏季日中以外の時季、時間帯においては圧縮機、冷却塔の能力が過大となり、装置コスト、ランニングコストともに嵩むという問題がある。   In addition, the compressor and cooling tower of the condensing unit must be of a performance according to the refrigeration capacity required for the cooling device. Usually, the cooling load is the largest and the cooling water temperature is high. Therefore, sufficient refrigeration capacity must be obtained under the conditions of outside air temperature and humidity during the daytime in summer when the condensation temperature rises. There is a problem that the capacity becomes excessive and both the apparatus cost and the running cost increase.

特に、凍結庫用の冷却装置では凍結庫の冷やし込みを行う場合に負荷が極めて大となるので、冷却塔には通常運転時に要求される熱交換能力の1.6倍が要求され、その分規模の大なる冷却塔を設けなければならない。   In particular, in a freezer cooling device, the load becomes extremely large when the freezer is cooled, so the cooling tower is required to have 1.6 times the heat exchange capacity required during normal operation. A large cooling tower must be provided.

ヒートポンプ式冷媒回路を用いて排熱回収を行なって蒸気や温水の生成熱源として有効利用するための技術については、従来から各種のものが提案されているが(例えば、特許文献1乃至3参照)、既存のコンデンシングユニットから凝縮排熱を回収することによって冷却装置の凝縮温度を低下せしめ、コンデンシングユニットにおける圧縮機、冷却塔の能力を小規模のものとすることができるようにしたものはない。   Various techniques have been conventionally proposed for recovering exhaust heat using a heat pump refrigerant circuit and effectively using it as a heat source for generating steam or hot water (see, for example, Patent Documents 1 to 3). , By reducing the condensation temperature of the cooling device by recovering the condensed exhaust heat from the existing condensing unit, so that the capacity of the compressor and cooling tower in the condensing unit can be reduced Absent.

また、回収排熱を熱源として蒸気と温水の両方を同時に生成できるようにした構成の装置についても実用化されていないのが現状である。
特開昭59−180016号公報(第1〜5頁、第1図および第2図) 特開昭61−125547号公報(第1〜2頁、第1図および第2図) 特開平7−139847号(第1〜4頁、図1)
In addition, an apparatus having a configuration in which both steam and hot water can be generated at the same time using the recovered exhaust heat as a heat source has not been put into practical use.
JP 59-180016 (pages 1 to 5, FIGS. 1 and 2) JP 61-125547 A (pages 1 and 2, FIGS. 1 and 2) JP-A-7-139847 (pages 1 to 4, FIG. 1)

本発明は、既存のコンデンシングユニットから凝縮排熱を回収してこの排熱を熱源として蒸気と温水を同時に供給することができ、しかも蒸気のみあるいは温水のみを弁の切り換えによって選択的に供給することもでき、もってエネルギの有効利用を図ることができるとともに、コンデンシングユニットにおける圧縮機、冷却塔により小規模のものを利用できて装置コストおよびランニングコストの低減も期すことのできる冷却システムを提供できるようにすることを課題としている。   The present invention can recover the condensed exhaust heat from the existing condensing unit and supply steam and hot water at the same time using this exhaust heat as a heat source, and selectively supply only steam or only hot water by switching the valve. Therefore, it is possible to effectively use energy and provide a cooling system that can reduce the cost of equipment and running by using a small-sized compressor and cooling tower in the condensing unit. The challenge is to make it possible.

上記目的を達成するために、本発明に係る装置は、圧縮式冷媒回路を備え、同冷媒回路における凝縮排熱を冷却塔にて大気に放出するコンデンシングユニットと、圧縮手段、凝縮手段、膨張弁、蒸発器をこの順に備え、外部から前記凝縮手段に供給される水を同凝縮手段における冷媒の凝縮熱により加熱して蒸気・温水を供給するヒートポンプ式蒸気・温水発生装置を備え、前記コンデンシングユニットにおける凝縮器からの水を、前記冷却塔と、前記蒸気・温水発生装置における蒸発器とのいずれか一方あるいは両方に切替えて流通させる切替機構を備え、コンデンシングユニットからの凝縮排熱を冷却塔から大気への放出と、蒸気・温水発生装置による回収の一方または両方に切替えることができるようにした構成のものとしてある。   In order to achieve the above object, an apparatus according to the present invention includes a compression refrigerant circuit, a condensing unit that releases condensed exhaust heat in the refrigerant circuit to the atmosphere in a cooling tower, a compression unit, a condensation unit, and an expansion unit. A heat pump steam / hot water generator for supplying steam / hot water by heating water supplied from the outside to the condensing means by the heat of condensation of the refrigerant in the condensing means; A switching mechanism for switching and circulating the water from the condenser in the cooling unit to one or both of the cooling tower and the evaporator in the steam / hot water generator. The structure is such that it can be switched to one or both of the release from the cooling tower to the atmosphere and the recovery by the steam / hot water generator.

より詳しくは、前記コンデンシングユニットにおける凝縮器からの水を前記冷却塔に送る冷却水送出管の途中に冷却水送出枝管の一端を接続するとともに、冷却塔から凝縮器へ冷却水を供給する冷却水供給管の途中に冷却水供給枝管の一端を接続し、前記冷却水送出枝管の他端と冷却水供給枝管の他端を、それぞれ前記蒸気・温水発生装置における蒸発器の水入口と同出口に接続し、かつ前記冷却水送出管と同枝管との分岐部および前記冷却水供給管と同枝管の分岐部に、コンデンシングユニットと冷却塔との間またはコンデンシングユニットと蒸気・温水発生装置との間あるいはコンデンシングユニットと冷却塔および蒸気・温水発生装置の両方との間に冷却水を切替えて流通させる切替機構を備え、コンデンシングユニットからの凝縮排熱を冷却塔から大気への放出と、蒸気・温水発生装置による回収の一方または両方に切替えてコンデンシングユニットにおける凝縮温度を低く維持することができるように構成したものとしてある。   More specifically, one end of the cooling water delivery branch pipe is connected to the middle of the cooling water delivery pipe for sending water from the condenser in the condensing unit to the cooling tower, and the cooling water is supplied from the cooling tower to the condenser. One end of the cooling water supply branch pipe is connected in the middle of the cooling water supply pipe, and the other end of the cooling water delivery branch pipe and the other end of the cooling water supply branch pipe are respectively connected to the water of the evaporator in the steam / hot water generator. A condensing unit or a condensing unit is connected between the condensing unit and the cooling tower at the branch portion between the cooling water delivery pipe and the branch pipe and the branch portion between the cooling water supply pipe and the branch pipe. A condensing unit is provided with a switching mechanism for switching the cooling water between the cooling unit and the steam / hot water generator or between the condensing unit and the cooling tower and the steam / hot water generator. Some as a discharge to the atmosphere from the cooling tower, and configured to be able to maintain the condensing temperature in condensing unit lower switch to either or both of the recovery by steam-heated generator.

また、前記ヒートポンプ式蒸気・温水発生装置は、前記凝縮手段を冷媒往管に直列に接続した第1凝縮器と第2凝縮器で構成し、前記第1凝縮器と第2凝縮器からそれぞれ蒸気と温水が同時に供給されるように構成し、さらに前記ヒートポンプ式蒸気・温水発生装置は、前記凝縮手段を冷媒往管に直列に接続した第1凝縮器と第2凝縮器で構成し、前記第1凝縮器と第2凝縮器からそれぞれ蒸気と温水が同時に供給されるように構成し、かつ前記圧縮手段を低段側と高段側の2段の圧縮機で構成し、また前記第2凝縮器と前記膨張弁との間における冷媒往管に中間冷却器を設けるとともに、この中間冷却器の気相に一端が接続されたガス冷媒戻し管の他端を、前記低段側圧縮機の吐出側と高段側圧縮機の吸入側との間に接続された中圧冷媒管の途中に接続し、前記第2凝縮器と中間冷却器間の冷媒往管の途中に中間冷却器用の膨張弁とバイパス管とをこれら膨張弁とバイパス管が並列となるように設け、このバイパス管に、外部へ蒸気のみを供給する蒸気供給運転の際には閉ざされているが、蒸気と温水の両方を同時に供給する蒸気・温水供給運転および温水のみを供給する温水供給運転の際には開かれる第1開閉弁を備え、また、前記ガス冷媒戻し管の途中に、前記蒸気供給運転の際には開かれているが、前記蒸気・温水供給運転と温水供給運転の際には閉ざされる第2開閉弁を備え、さらに、前記第2凝縮器への給水管に、前記蒸気供給運転の際には閉ざされているが、前記蒸気・温水供給運転と温水供給運転の際には開かれる第3開閉弁を設けた構成のものとしてある。   The heat pump steam / warm water generator includes a first condenser and a second condenser in which the condensing means is connected in series to a refrigerant forward pipe, and steam is respectively generated from the first condenser and the second condenser. And the heat pump steam / warm water generator comprises a first condenser and a second condenser in which the condensing means is connected in series with a refrigerant forward pipe, Steam and hot water are supplied simultaneously from the first condenser and the second condenser, respectively, and the compression means is composed of a two-stage compressor on the low-stage side and the high-stage side, and the second condensation An intermediate cooler is provided in the refrigerant forward pipe between the compressor and the expansion valve, and the other end of the gas refrigerant return pipe connected at one end to the gas phase of the intermediate cooler is connected to the discharge of the low-stage compressor. Pressure refrigerant pipe connected between the suction side and the suction side of the high stage compressor An intermediate valve is connected to the intermediate condenser, and an expansion valve for the intermediate cooler and a bypass pipe are provided in the middle of the refrigerant outgoing pipe between the second condenser and the intermediate cooler so that the expansion valve and the bypass pipe are in parallel. In addition, it is closed during the steam supply operation for supplying only steam to the outside, but it is open during the steam / hot water supply operation for supplying both steam and hot water at the same time and for the hot water supply operation for supplying only hot water. A first open / close valve that is open during the steam supply operation and is closed during the steam / hot water supply operation and the hot water supply operation in the middle of the gas refrigerant return pipe. And a second water supply pipe to the second condenser is closed during the steam supply operation, but is opened during the steam / hot water supply operation and the hot water supply operation. The configuration is such that three open / close valves are provided.

また、前記コンデンシングユニットはその起動時において、前記ヒートポンプ式蒸気・温水発生装置を駆動せしめるとともに、前記切替機構がコンデンシングユニットからの冷却水を前記冷却塔と蒸気・温水発生装置の両方に送るよう切替えられるように構成したものとしてある。   The condensing unit drives the heat pump steam / hot water generator at the time of activation, and the switching mechanism sends the cooling water from the condensing unit to both the cooling tower and the steam / hot water generator. It is configured to be switched as described above.

さらに前記ヒートポンプ式蒸気・温水発生装置における第1凝縮器への給水管の途中に、第1凝縮器への給水量を制御するための給水制御手段を設けて、第1凝縮器から温水または蒸気のいずれかを選択的に供給できるように構成し、前記ヒートポンプ式蒸気・温水発生装置における第2凝縮器への給水管の途中に、第2凝縮器への給水量を制御するための給水制御手段を設けて、第2凝縮器への給水量の調節により同第2凝縮器から供給される温水が所要の温度となるよう調節できるように構成し、前記ヒートポンプ式蒸気・温水発生装置における第2凝縮器への給水管の途中に、第2凝縮器への給水量を制御するための給水制御手段を設けて、第2凝縮器への給水量の調節により冷媒往管内における冷媒圧力を常に所定の圧力以下に維持することができるようにした構成のものとしてある。   Furthermore, water supply control means for controlling the amount of water supplied to the first condenser is provided in the middle of the water supply pipe to the first condenser in the heat pump steam / hot water generator, and the hot water or steam is supplied from the first condenser. Water supply control for controlling the amount of water supplied to the second condenser in the middle of the water supply pipe to the second condenser in the heat pump steam / hot water generator Means for adjusting the amount of water supplied to the second condenser so that the hot water supplied from the second condenser can be adjusted to a required temperature, and the heat pump steam / hot water generator in the heat pump type 2 A water supply control means for controlling the amount of water supplied to the second condenser is provided in the middle of the water supply pipe to the condenser, and the refrigerant pressure in the refrigerant forward pipe is always adjusted by adjusting the amount of water supplied to the second condenser. Maintain below specified pressure There as having the configuration to allow Rukoto.

また前記切替機構を三方制御弁で構成し、この三方制御弁をコントロールする制御回路にコンデンシングユニットの高圧側冷媒圧力と低圧側冷媒圧力を検出する高圧側圧力スイッチと低圧側圧力スイッチを接続し、高圧側または低圧側の冷媒圧力が所定の値を超えるとコンデンシングユニットからの冷却水を前記冷却塔と蒸気・温水発生装置の両方に送り、上記冷媒圧力が予め設定された値以下に低下すると徐々に冷却塔への冷却水の供給を減少せしめるように構成したものとしてある。   The switching mechanism is composed of a three-way control valve, and a high pressure side pressure switch and a low pressure side pressure switch for detecting the high pressure side refrigerant pressure and the low pressure side refrigerant pressure of the condensing unit are connected to a control circuit for controlling the three way control valve. When the refrigerant pressure on the high-pressure side or low-pressure side exceeds a predetermined value, the cooling water from the condensing unit is sent to both the cooling tower and the steam / hot water generator, and the refrigerant pressure drops below a preset value. As a result, the cooling water supply to the cooling tower is gradually reduced.

さらに前記制御回路に前記蒸気・温水発生装置からの蒸気供給量と温水供給量をそれぞれ検出する流量計を接続し、蒸気供給量と温水供給量が減少するとコンデンシングユニットから前記冷却塔への冷却水の供給量を徐々に大ならしめ、蒸気・温水発生装置が停止されると冷却水の全量を冷却塔へ送るように切り替えられるように構成したものとしてある。   Further, a flow meter for detecting the steam supply amount and the hot water supply amount from the steam / hot water generator is connected to the control circuit. When the steam supply amount and the hot water supply amount decrease, cooling from the condensing unit to the cooling tower is performed. The water supply amount is gradually increased, and when the steam / hot water generator is stopped, the entire amount of cooling water can be switched to be sent to the cooling tower.

本発明によれば、コンデンシングユニットの凝縮排熱を利用して蒸気と温水とを同時に、または蒸気と温水のいずれかを選択的に供給することができ、しかも構造が簡単で構成機器には特殊な構成、構造のものは不要であり、従来から冷凍機に使用されている既存の機器を採用することができて、製造コストの低減も期すことができる。   According to the present invention, it is possible to supply steam and hot water at the same time or selectively supply steam and hot water using the condensation exhaust heat of the condensing unit. No special configuration or structure is required, and existing equipment that has been used in refrigerators can be used, and the manufacturing cost can be reduced.

また、コンデンシングユニットの凝縮排熱を蒸気・温水の生成用熱源として回収するので、凝縮排熱を無駄に大気に放出することがなくて省エネルギ化を図ることができるとともに環境への影響も低減でき、しかもコンデンシングユニットにおいては、凝縮温度を低くすることができ、したがってコンデンシングユニットにおける圧縮機や冷却塔の小型化、低動力化を図ることもでき、装置コストおよびランニングコストの低減を期せる。
なお、冷却塔に冷却水を送る冷却水ポンプの小型化、低動力化も図ることができる。
In addition, since the condensed exhaust heat of the condensing unit is recovered as a heat source for generating steam and hot water, it is possible to save energy without wastefully releasing the condensed exhaust heat to the atmosphere. In addition, the condensation temperature can be lowered in the condensing unit. Therefore, the compressor and cooling tower in the condensing unit can be reduced in size and power can be reduced, and the apparatus cost and running cost can be reduced. I can expect.
Note that it is possible to reduce the size and power of the cooling water pump that sends cooling water to the cooling tower.

さらに、コンデンシングユニットにおける冷却塔への冷却水循環路を蒸気・温水装置に導くようにする簡単な構成であるので、既存のコンデンシングユニットへの適用も容易であるという実用上のメリットもある。   Further, since the cooling water circulation path to the cooling tower in the condensing unit is a simple configuration that leads to the steam / hot water apparatus, there is a practical advantage that it can be easily applied to the existing condensing unit.

以下、本発明に係る装置の実施例を添付図面に示す具体例に基づいて詳細に説明する。
コンデンシングユニット1は圧縮機2、凝縮器3を備え、凝縮器からの冷媒往管4は膨張弁5を介して被冷却室たる凍結庫6の空調器7における蒸発器8の冷媒入口に接続されていて、同蒸発器の冷媒出口に一端が接続された冷媒復管9の他端が前記コンデンシングユニット1の圧縮機2の吸入側に接続されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the apparatus according to the present invention will be described below in detail based on specific examples shown in the accompanying drawings.
The condensing unit 1 includes a compressor 2 and a condenser 3, and a refrigerant outgoing pipe 4 from the condenser is connected via an expansion valve 5 to a refrigerant inlet of an evaporator 8 in an air conditioner 7 of a freezer 6 serving as a room to be cooled. The other end of the refrigerant return pipe 9 having one end connected to the refrigerant outlet of the evaporator is connected to the suction side of the compressor 2 of the condensing unit 1.

また、コンデンシングユニット1の凝縮器3の冷却水出口に一端が接続された冷却水送出管10の他端が冷却水ポンプ11を介して屋外の冷却塔12の水入口に接続され、同出口に一端が接続された冷却水供給管13の他端が凝縮器の冷却水入口に接続されている。   The other end of the cooling water delivery pipe 10 whose one end is connected to the cooling water outlet of the condenser 3 of the condensing unit 1 is connected to the water inlet of the outdoor cooling tower 12 via the cooling water pump 11, The other end of the cooling water supply pipe 13 connected at one end to the cooling water inlet is connected to the cooling water inlet of the condenser.

上述したコンデンシングユニット1、空調器7および冷却塔12で凍結庫6用の冷却装置が構成されていて、コンデンシングユニット1において圧縮、凝縮された冷媒が膨張弁5を経て蒸発器8に送られ、凍結庫内の空気を冷却して圧縮機に戻され、蒸発器で冷却された空気は送風機14によって凍結庫内に送出される。   The condensing unit 1, the air conditioner 7 and the cooling tower 12 described above constitute a cooling device for the freezer 6, and the refrigerant compressed and condensed in the condensing unit 1 is sent to the evaporator 8 through the expansion valve 5. The air in the freezer is cooled and returned to the compressor, and the air cooled by the evaporator is sent out into the freezer by the blower 14.

また、凝縮器において高温冷媒を冷却、液化させた冷却水は前記冷却水送出管10により冷却塔12に送られ、この冷却塔で外気との熱交換により冷却されて凝縮器に供給される。   Further, the cooling water obtained by cooling and liquefying the high-temperature refrigerant in the condenser is sent to the cooling tower 12 through the cooling water delivery pipe 10, and is cooled by heat exchange with the outside air in the cooling tower and supplied to the condenser.

しかして本発明のシステムにおいては、前記冷却水送出管10と冷却水供給管13の途中にそれぞれ冷却水送出枝管15と冷却水供給枝管16の一端がそれぞれ接続されていて、各枝管の他端は後述する蒸気・温水発生装置17の蒸発器30の水入口18と同出口19にそれぞれ接続されている。   In the system of the present invention, one end of each of the cooling water delivery branch pipe 15 and the cooling water supply branch pipe 16 is connected to the cooling water delivery pipe 10 and the cooling water supply pipe 13, respectively. The other end of each is connected to a water inlet 18 and an outlet 19 of an evaporator 30 of a steam / hot water generator 17 which will be described later.

また、冷却水送出枝管15と冷却水供給枝管16の冷却水送出管10、冷却水供給管13との分岐部には、コンデンシングユニットと冷却塔との間またはコンデンシングユニットと蒸気・温水発生装置との間あるいはコンデンシングユニットと冷却塔および蒸気・温水発生装置の両方との間に冷却水を切替えて流通させる切替機構20を設けてある。   Further, a branching portion between the cooling water delivery branch pipe 15 and the cooling water delivery pipe 10 and the cooling water supply pipe 13 of the cooling water supply branch pipe 16 is provided between the condensing unit and the cooling tower or between the condensing unit and the steam / A switching mechanism 20 is provided for switching the cooling water to flow between the hot water generator or between the condensing unit and both the cooling tower and the steam / hot water generator.

上記切替機構20は、例えば冷却水送出管10と同枝管15との分岐部よりも冷却塔寄りの送出管12の途中および冷却水送出枝管の途中にそれぞれ設けた開閉弁V8、V9と、冷却水供給管13と同枝管16との分岐部よりも冷却塔寄りの供給管の途中および冷却水供給枝管の途中にそれぞれ設けた開閉弁V10、V11で構成してある。 The switching mechanism 20 is, for example, an on-off valve V 8 , V 8 provided in the middle of the delivery pipe 12 closer to the cooling tower than the branch between the cooling water delivery pipe 10 and the branch pipe 15 and in the middle of the cooling water delivery branch pipe, respectively. 9 and on-off valves V 10 and V 11 provided in the middle of the supply pipe closer to the cooling tower than the branch of the cooling water supply pipe 13 and the branch pipe 16 and in the middle of the cooling water supply branch pipe, respectively. is there.

そして、夏季の日中のように外気の温湿度が高くて冷却負荷が大となる場合には、上記開閉弁V8、V9、V10、V11を全て開成し、コンデンシングユニットの凝縮排熱によって昇温した冷却水が冷却塔12と蒸気・温水発生装置17の蒸発器30の両方に供給され、これら冷却塔と蒸発器で冷却された冷却水がコンデンシングユニットに戻される。 When the temperature and humidity of the outside air is high and the cooling load becomes large, such as during the daytime in summer, all of the on-off valves V 8 , V 9 , V 10 and V 11 are opened to condense the condensing unit. The cooling water heated by the exhaust heat is supplied to both the cooling tower 12 and the evaporator 30 of the steam / hot water generator 17, and the cooling water cooled by the cooling tower and the evaporator is returned to the condensing unit.

また、冷却負荷がさほど大ではなく、蒸気や温水を利用しない場合には、前記開閉弁V8、V10が開、開閉弁V9、V11が閉となってコンデンシングユニットからの昇温冷却水は冷却塔12だけに供給される。 Further, when the cooling load is not so large and steam or hot water is not used, the on-off valves V 8 and V 10 are opened and the on-off valves V 9 and V 11 are closed to raise the temperature from the condensing unit. The cooling water is supplied only to the cooling tower 12.

さらに、冷却負荷がさほど大ではなく、蒸気や温水を利用する場合には、前記開閉弁V9、V11が開、開閉弁V8、V10が閉となってコンデンシングユニットからの昇温冷却水は蒸気・温水発生装置17だけに供給される。 Further, when the cooling load is not so large and steam or hot water is used, the on-off valves V 9 and V 11 are opened, the on-off valves V 8 and V 10 are closed, and the temperature rises from the condensing unit. The cooling water is supplied only to the steam / hot water generator 17.

また、凍結庫内を常温から所要の低温まで冷やし込む必要のあるコンデンシングユニットの起動時においては、先に蒸気・温水発生装置を駆動せしめ、上述した冷却負荷が大である場合と同様にコンデンシングユニットからの冷却水が冷却塔12と蒸気・温水発生装置17の両方に供給されるように切替機構が操作されるようにしておく。   In addition, when starting a condensing unit that needs to cool the freezer from room temperature to the required low temperature, the steam / hot water generator is driven first, and the condensing unit is the same as when the cooling load is large. The switching mechanism is operated so that the cooling water from the cooling unit is supplied to both the cooling tower 12 and the steam / hot water generator 17.

かくすると、起動時における一時的な負荷の増大に十分対応することができ、小能力の圧縮機、冷却塔であってもスムーズな起動を行うことができる。   In this way, it is possible to sufficiently cope with a temporary load increase at the time of start-up, and smooth start-up can be performed even with a small capacity compressor and cooling tower.

なお、上述した切替機構20の構成はコンデンシングユニットからの昇温冷却水を冷却塔と蒸気・温水発生装置の一方に切替えてあるいは両方に供給できる構成であれば事が足り、上述した4つの開閉弁に代えて例えば各分岐部に適宜の三方切替弁を設けるようにする場合もあるし、図7に示されるように三方制御弁43を設け、この三方制御弁を制御回路44によりコントロールして、コンデンシングユニット1における冷媒圧力の制御をもできるようにする場合もあり、詳細については後述する。   The above-described switching mechanism 20 may have any configuration as long as it can switch the heating / cooling water from the condensing unit to one of the cooling tower and the steam / hot water generator, or to both of them. For example, an appropriate three-way switching valve may be provided at each branch portion instead of the on-off valve, or a three-way control valve 43 is provided as shown in FIG. 7, and the three-way control valve is controlled by the control circuit 44. In some cases, the refrigerant pressure in the condensing unit 1 can be controlled. Details will be described later.

しかして前記蒸気・温水発生装置17においては、低段側圧縮機21の吐出側に一端が接続された中圧冷媒管22の他端が高段側圧縮機23の吸入側に接続され、上記低段側と高段側の圧縮機で圧縮手段を構成してある。   Thus, in the steam / hot water generator 17, the other end of the medium pressure refrigerant pipe 22 whose one end is connected to the discharge side of the low-stage compressor 21 is connected to the suction side of the high-stage compressor 23, and The compression means is composed of the low-stage and high-stage compressors.

前記高段側圧縮機23の吐出側に一端が接続された冷媒往管24の他端は凝縮手段たる第1凝縮器25と第2凝縮器26、中間冷却器用膨張弁27、中間冷却器28および蒸発器用膨張弁29を介して蒸発器30に接続されていて、同蒸発器の出口に一端が接続された冷媒復管31の他端が前記低段圧縮機21の吸入側に接続されている。   The other end of the refrigerant forward pipe 24 having one end connected to the discharge side of the high-stage compressor 23 is a first condenser 25 and a second condenser 26 which are condensing means, an intermediate cooler expansion valve 27, and an intermediate cooler 28. And the other end of the refrigerant return pipe 31 connected to the evaporator 30 via the evaporator expansion valve 29 and having one end connected to the outlet of the evaporator is connected to the suction side of the low-stage compressor 21. Yes.

そして、前記冷媒往管24における中間冷却器用膨張弁27の部分には、同膨張弁を跨ぐバイパス管32を設けてあってこのバイパス管32に後述する第1開閉弁V1を設けてある。 The intermediate cooler expansion valve 27 in the refrigerant forward pipe 24 is provided with a bypass pipe 32 straddling the expansion valve, and the bypass pipe 32 is provided with a first on-off valve V 1 described later.

また、前記中間冷却器28の気相に一端が接続されたガス冷媒戻し管33の他端を前記中圧冷媒管22の途中に接続してあって、ガス冷媒戻し管の途中に、後述する第2開閉弁V2を設けてある。 Further, the other end of the gas refrigerant return pipe 33 whose one end is connected to the gas phase of the intermediate cooler 28 is connected to the middle pressure refrigerant pipe 22 and will be described later in the middle of the gas refrigerant return pipe. A second on-off valve V 2 is provided.

前記第1凝縮器25の2次側入口には第1給水管34を、同出口には蒸気・温水供給管35をそれぞれ接続してあって、上記第1給水管34の途中には給水制御手段たる流量制御弁V4を設けてある。 A first water supply pipe 34 is connected to the secondary side inlet of the first condenser 25, and a steam / hot water supply pipe 35 is connected to the outlet, and water supply control is provided in the middle of the first water supply pipe 34. A flow control valve V 4 as means is provided.

また、前記第2凝縮器26の2次側入口には第2給水管36を、同出口には温水供給管37をそれぞれ接続してあって、上記第2給水管36の途中には給水制御手段たる流量制御弁V5と、後述する第3開閉弁V3を設けてある。 Further, a second water supply pipe 36 is connected to the secondary side inlet of the second condenser 26 and a hot water supply pipe 37 is connected to the outlet, and water supply control is provided in the middle of the second water supply pipe 36. A flow control valve V 5 serving as a means and a third on-off valve V 3 described later are provided.

そして前述したように前記蒸発器30の水入口18には前記冷却水送出枝管15を、同出口19には前記冷却水供給枝管16をそれぞれ接続してある。   As described above, the cooling water delivery branch pipe 15 is connected to the water inlet 18 of the evaporator 30 and the cooling water supply branch pipe 16 is connected to the outlet 19 thereof.

上述のように構成した本発明の装置は、例えば冷媒としてオゾン破壊係数ODPがゼロであり、温暖化係数GWPが950と実用化フロン冷媒の中で最も低いR245faを使用し、図3に示す各開閉弁V1、V2、V3の開閉制御によって蒸気供給運転、温水供給運転、蒸気・温水供給運転に切替えられるように構成されており、以下に本発明の装置における作用について説明する。 The apparatus of the present invention configured as described above uses, for example, R245fa having a ozone depletion coefficient ODP of zero as a refrigerant and a global warming coefficient GWP of 950, which is the lowest among practical chlorofluorocarbon refrigerants. It is configured to be switched to a steam supply operation, a hot water supply operation, and a steam / hot water supply operation by open / close control of the on-off valves V 1 , V 2 , V 3 , and the operation in the apparatus of the present invention will be described below.

蒸気供給運転モードにおいては、第1開閉弁V1と第3開閉弁V3が閉、第2開閉弁V2が開とされ、図4に示されるように低段圧縮機21から吐出された冷媒が高段圧縮機23にてさらに圧縮され、高温高圧のガス冷媒となって第1凝縮器5に流入し、第1給水管34からの水を加熱して蒸気を発生させ、発生した蒸気は蒸気・温水供給管35により外部に供給される。 In the steam supply operation mode, the first on-off valve V 1 and the third on-off valve V 3 are closed, and the second on-off valve V 2 is opened, and discharged from the low-stage compressor 21 as shown in FIG. The refrigerant is further compressed by the high-stage compressor 23, becomes a high-temperature and high-pressure gas refrigerant, flows into the first condenser 5, heats the water from the first water supply pipe 34, generates steam, and the generated steam Is supplied to the outside through a steam / hot water supply pipe 35.

そして第1凝縮器25で水との熱交換により凝縮した冷媒は第2凝縮器26を流過するが、第2給水管36の第3開閉弁V3が閉止されているので、水との熱交換はせずにそのまま第2凝縮器から流出する。 The refrigerant condensed in the first condenser 25 by heat exchange with the water is flowing through the second condenser 26, the third on-off valve V 3 of the second water supply pipe 36 is closed, with water It flows out from the second condenser without heat exchange.

第2凝縮器26からの冷媒はバイパス管32の第1開閉弁V1が閉止されているので、膨張弁27により減圧されて気化し、中間冷却器28に流入し、同中間冷却器28で気液分離された液相の冷媒は膨張弁29を経て蒸発器30に流入する。 Since the first on-off valve V 1 of the bypass pipe 32 is closed, the refrigerant from the second condenser 26 is reduced in pressure by the expansion valve 27, vaporizes, flows into the intermediate cooler 28, and then passes through the intermediate cooler 28. The gas-liquid separated liquid phase refrigerant flows into the evaporator 30 through the expansion valve 29.

蒸発器30に送られた冷媒は前記膨張弁29による減圧されているとともに、冷却水送出枝管15からの冷却水すなわちコンデンシングユニットの凝縮排熱により昇温された水の熱を奪って気化し、冷媒復管31により低段圧縮機21に戻される。
前記冷却水は蒸発器30にて冷却され、冷却水供給枝管15、冷却水供給管13によりコンデンシングユニットに戻される。
The refrigerant sent to the evaporator 30 is depressurized by the expansion valve 29 and takes the heat of the cooling water from the cooling water delivery branch pipe 15, that is, the water heated by the condensation exhaust heat of the condensing unit. And returned to the low-stage compressor 21 by the refrigerant return pipe 31.
The cooling water is cooled by the evaporator 30 and returned to the condensing unit by the cooling water supply branch pipe 15 and the cooling water supply pipe 13.

しかして、前記中間冷却器28内のガス冷媒は、第2開閉弁V2が開かれているガス冷媒戻し管33によって前記中圧冷媒管22に戻され、低段圧縮機21を経ずに高段圧縮機23から再び冷媒往管24に送り出される。 Thus, the gas refrigerant in the intermediate cooler 28 is returned to the intermediate pressure refrigerant pipe 22 by the gas refrigerant return pipe 33 in which the second on-off valve V 2 is opened, and without passing through the low stage compressor 21. The refrigerant is sent again from the high stage compressor 23 to the refrigerant forward pipe 24.

上述のように中間冷却器を介在せしめることによってガス冷媒が前記低段側圧縮機21を経ずに高段側圧縮機23から再び第1、第2の凝縮器に送られるので、成績係数COPhを向上せしめることができる。 By interposing the intercooler as described above, the gas refrigerant is sent again from the high stage compressor 23 to the first and second condensers without passing through the low stage compressor 21, so that the coefficient of performance COP h can be improved.

ところで、前記第1給水管34の流量調節弁V4は、必要な温度の蒸気が供給されるように給水量、給水圧力を適宜制御するためのものとしてあり、流量を小なるものとすれば高温に、大なるものとすれば低温に調節することができる。 By the way, the flow rate adjusting valve V 4 of the first water supply pipe 34 is for appropriately controlling the water supply amount and the water supply pressure so that steam having a necessary temperature is supplied, and if the flow rate is reduced. The temperature can be adjusted to a low temperature if the temperature is high.

次に、蒸気と温水を同時に供給する蒸気・温水供給運転モードでは、第1開閉弁V1と第3開閉弁V3が開、第2開閉弁V2が閉とされ、図5に示されるように低段圧縮機21から吐出された冷媒が高段圧縮機23にてさらに圧縮され、高温高圧のガス冷媒となって第1凝縮器25に流入し、第1給水管34からの水を加熱して蒸気を発生させ、発生した蒸気は蒸気・温水供給管35により外部に供給される。 Next, in the steam / hot water supply operation mode in which steam and hot water are supplied simultaneously, the first on-off valve V 1 and the third on-off valve V 3 are opened, and the second on-off valve V 2 is closed, as shown in FIG. As described above, the refrigerant discharged from the low-stage compressor 21 is further compressed by the high-stage compressor 23, becomes high-temperature and high-pressure gas refrigerant, flows into the first condenser 25, and draws water from the first water supply pipe 34. Steam is generated by heating, and the generated steam is supplied to the outside through a steam / hot water supply pipe 35.

そして第1凝縮器25で水との熱交換により凝縮した冷媒は第2凝縮器26に流入し、第3開閉弁V3が開かれている第2給水管36からの水を加熱して温水を発生させてさらに低温の液冷媒となる。
同第2凝縮器26で発生した温水は温水供給管37から外部に供給される。
The refrigerant condensed in the first condenser 25 by heat exchange with the water to heat the water from the second water supply pipe 36 flows into the second condenser 26, the third on-off valve V 3 is opened hot water To generate a liquid refrigerant at a lower temperature.
Hot water generated in the second condenser 26 is supplied to the outside through a hot water supply pipe 37.

第2凝縮器26からの冷媒は第1開閉弁V1が開かれているバイパス管32を流過して中間冷却器28に流入し、同中間冷却器28における液冷媒は前述した蒸気供給運転モードの場合と同様に膨張弁29を経て蒸発器30に流入し、蒸発器30にて音電信具ユニットからの昇温冷却水の熱を回収して気化し、低段圧縮機21に戻される。
すなわち、この蒸気・温水供給運転モードでは前記中間冷却器28は受液器として作用する。
The refrigerant from the second condenser 26 flows into the intermediate cooler 28 through the bypass pipe 32 in which the first on-off valve V 1 is opened, and the liquid refrigerant in the intermediate cooler 28 is the steam supply operation described above. In the same manner as in the mode, the refrigerant flows into the evaporator 30 through the expansion valve 29, and the evaporator 30 collects and vaporizes the heat of the heating / cooling water from the sonoelectric equipment unit and returns it to the low-stage compressor 21. .
That is, in the steam / hot water supply operation mode, the intermediate cooler 28 functions as a liquid receiver.

上述した蒸気・温水供給運転モードにおいては、第1凝縮器25から蒸気を供給する構成としてあるが、前記流量調節弁V4による給水量、給水圧力の制御によって、第1凝縮器5からも第2凝縮器26と同様に温水を供給する場合もあり、この場合には第1凝縮器25からは高温水を、第2凝縮器26からは中温水をそれぞれ供給することができる。 In the above-described steam-hot water supply operation mode, there is a structure for supplying the steam from the first condenser 25, the water supply amount by the flow rate control valve V 4, the control of water pressure, from the first condenser 5 second In some cases, hot water may be supplied in the same manner as the two condenser 26, and in this case, high temperature water can be supplied from the first condenser 25, and medium temperature water can be supplied from the second condenser 26.

すなわち、開閉弁V1、V2、V3の開閉状態を前述した蒸気・温水供給運転モードと同様にしたまま、前記流量調節弁のV4の開度を制御することにより、蒸気・温水供給運転モードから温水のみを供給する温水供給運転モードに切替えることができるようになっている。 That is, steam / hot water supply is performed by controlling the opening degree of V 4 of the flow rate control valve while keeping the open / close state of the open / close valves V 1 , V 2 , V 3 in the same manner as the steam / hot water supply operation mode described above. The operation mode can be switched to the hot water supply operation mode for supplying only hot water.

すなわち、上記流量調節弁V4の開度を蒸気・温水供給運転モードの状態からさらに大なるものとすれば、蒸気・温水供給管35からの蒸気を温水にすることができ、蒸気・温水供給運転モードと温水供給運転モードはこの流量調節弁V4の開度制御で選択することができるようになっている。 That is, if the opening degree of the flow rate control valve V 4 is further increased from the state of the steam / hot water supply operation mode, the steam from the steam / hot water supply pipe 35 can be changed to warm water, and steam / hot water supply is performed. operation mode and hot water supply operation mode is adapted to be able to select in the control of the opening degree of the flow control valve V 4.

なお、蒸気・温水供給管35からの蒸気温度や蒸気と温水の切替は、上述のように第1凝縮器25に供給する水の量を調節すればよいのであるから、本実施例の流量調節弁V4に代えて第1給水管34に水を送る図示を省略した給水ポンプの駆動を制御する場合もある。 The switching of the steam temperature and the steam / hot water from the steam / hot water supply pipe 35 may be performed by adjusting the amount of water supplied to the first condenser 25 as described above. The drive of a water supply pump (not shown) that sends water to the first water supply pipe 34 instead of the valve V 4 may be controlled.

また、前記第2給水管36の流量調節弁V5を制御することにより、温水供給管37から供給される温水の温度も所定の範囲内で任意に調節することができ、流量を小なるものとすれば高温に、大なるものとすれば低温に調節することができる。 Further, by controlling the flow rate adjustment valve V 5 of the second water supply pipe 36, the temperature of the hot water supplied from the hot water supply pipe 37 can be arbitrarily adjusted within a predetermined range, and the flow rate can be reduced. If it is, it can be adjusted to high temperature, and if it is large, it can be adjusted to low temperature.

さらに、上記流量調節弁V5を制御することによって冷媒往管24内における冷媒圧力を調節することもでき、この場合、冷媒往管内における高圧冷媒の圧力を図示省略のセンサで検出し、同圧力が所定の上限圧力となった場合には第2給水管36への給水量を大ならしめて冷媒の温度を低下せしめ、圧力上昇を抑えて高圧冷媒の圧力を所定の範囲内に調節する。 Further, the refrigerant pressure in the refrigerant forward pipe 24 can be adjusted by controlling the flow rate adjusting valve V 5. In this case, the pressure of the high-pressure refrigerant in the refrigerant forward pipe is detected by a sensor (not shown), When the pressure reaches a predetermined upper limit pressure, the amount of water supplied to the second water supply pipe 36 is increased to lower the temperature of the refrigerant, and the pressure rise is suppressed to adjust the pressure of the high-pressure refrigerant within a predetermined range.

なお、温水供給管36からの温水温度の切替や高圧冷媒の圧力制御は、前述した蒸気・温水供給管35からの蒸気温度や蒸気と温水の切替の場合と同様に、第2凝縮器26に供給する水の量を調節すればよいのであるから、本実施例の流量調節弁V5に代えて第2給水管36に水を送る図示を省略した給水ポンプの駆動を制御する場合もある。 The switching of the hot water temperature from the hot water supply pipe 36 and the pressure control of the high-pressure refrigerant are performed in the second condenser 26 in the same manner as in the case of the switching of the steam temperature and the steam and hot water from the steam / hot water supply pipe 35 described above. Since the amount of water to be supplied may be adjusted, the drive of a water supply pump (not shown) that sends water to the second water supply pipe 36 instead of the flow rate adjustment valve V 5 of this embodiment may be controlled.

上述した実施例の装置においては、中間冷却器28からの液冷媒がそのまま膨張弁29を経て蒸発器30に送られる構成となっているが、図6に示される第2実施例の装置のように、中間冷却器28と膨張弁29との間に熱交換器40を設け、第3給水管41からの水を加熱して第2温水供給管32から中温水を送出できるようにする場合もある。   In the apparatus of the above-described embodiment, the liquid refrigerant from the intermediate cooler 28 is directly sent to the evaporator 30 via the expansion valve 29, but like the apparatus of the second embodiment shown in FIG. In addition, a heat exchanger 40 may be provided between the intermediate cooler 28 and the expansion valve 29 to heat the water from the third water supply pipe 41 so that the medium hot water can be sent out from the second hot water supply pipe 32. is there.

なお、同図6中の符号V6は開閉弁、V7は流量調節弁を示し、開閉弁V6は中温水の取り出しの要否に応じて開閉操作され、流量調節弁V7は熱交換器40への給水量を制御して中温水の温度を調節するためのものである。 In FIG. 6, symbol V 6 indicates an opening / closing valve, V 7 indicates a flow rate adjusting valve, and the opening / closing valve V 6 is opened / closed according to the necessity of taking out the medium temperature water, and the flow rate adjusting valve V 7 is heat exchanged. This is for controlling the amount of water supplied to the vessel 40 and adjusting the temperature of the medium temperature water.

この第2実施例のものは、第1実施例の装置と同様に図3の表のように運転モードに対応する弁の開閉操作が行われるが、前記開閉弁V6は図3における蒸気供給運転モードに対応する運転モードにおいて開成され、蒸気・温水供給運転モードおよび温水供給運転モードの場合には原則として閉止される。 This is what the second embodiment, although the opening and closing operation of the valve corresponding to the operation mode as device as well as the table of FIG. 3 in the first embodiment is performed, the on-off valve V 6 is steam supply in FIG. 3 It is opened in an operation mode corresponding to the operation mode, and is closed in principle in the steam / hot water supply operation mode and the hot water supply operation mode.

すなわち、第1実施例における蒸気供給運転モードの場合には第2凝縮器26における熱交換を行わないので、中間冷却器28の液相における冷媒に取り出し可能な熱が残留しており、第2実施例のものの場合にはこの中間冷却器28の液相における冷媒の熱により熱交換器40において中温水を生成することができるのである。   That is, in the steam supply operation mode in the first embodiment, heat exchange in the second condenser 26 is not performed, so that heat that can be taken out remains in the refrigerant in the liquid phase of the intermediate cooler 28, and the second In the case of the embodiment, intermediate heat water can be generated in the heat exchanger 40 by the heat of the refrigerant in the liquid phase of the intermediate cooler 28.

なお、第1実施例の蒸気・温水供給運転モードおよび温水供給運転モードに対応する運転を第2実施例のもので行う場合においても、必要に応じて前記開閉弁V6を開成して比較的温度の低い中温水を取り出すことも可能である。 Even when the operation corresponding to the steam / warm water supply operation mode and the warm water supply operation mode of the first embodiment is performed in the second embodiment, the on-off valve V 6 is opened as necessary to perform the operation relatively. It is also possible to take out the medium temperature water having a low temperature.

図7はコンデンシングユニット1からの冷却水を切替機構たる前記三方制御弁43によって冷却塔12と蒸気・温水発生装置17とに送る量の割合を制御できるようにした構成の冷却システムの具体例を示している。   FIG. 7 shows a specific example of a cooling system configured so that the ratio of the amount of cooling water sent from the condensing unit 1 to the cooling tower 12 and the steam / hot water generator 17 can be controlled by the three-way control valve 43 serving as a switching mechanism. Is shown.

しかして上記三方制御弁43は制御回路44からの指令に従って冷却水の供給割合を制御するものとしてあり、制御回路44はコンデンシングユニット1における高圧側冷媒管に設けた高圧側圧力スイッチ45および低圧側冷媒管に設けた低圧側圧力スイッチ46と接続され、また、蒸気・温水発生装置17における蒸気・温水供給管35および温水供給管37にそれぞれ設けた流量計47、48と接続されている。   Thus, the three-way control valve 43 controls the supply rate of the cooling water in accordance with a command from the control circuit 44. The control circuit 44 includes a high-pressure side pressure switch 45 provided on the high-pressure side refrigerant pipe in the condensing unit 1 and a low-pressure. The low pressure side pressure switch 46 provided on the side refrigerant pipe is connected to the flow meters 47 and 48 provided on the steam / hot water supply pipe 35 and the hot water supply pipe 37 in the steam / hot water generator 17 respectively.

上述のように構成したシステムにおいては、コンデンシングユニットの高圧側または低圧側の冷媒圧力が所定の値を超えると高圧側圧力スイッチ45または低圧側圧力スイッチから圧力警告信号が制御回路44に送られ、制御回路はコンデンシングユニットからの冷却水を冷却塔12と蒸気・温水発生装置17の両方に流すよう三方制御弁43をコントロールする。   In the system configured as described above, when the refrigerant pressure on the high pressure side or low pressure side of the condensing unit exceeds a predetermined value, a pressure warning signal is sent to the control circuit 44 from the high pressure side pressure switch 45 or the low pressure side pressure switch. The control circuit controls the three-way control valve 43 so that the cooling water from the condensing unit flows to both the cooling tower 12 and the steam / hot water generator 17.

かくすると、冷却水が冷却塔と蒸気・温水発生装置との両方で冷却されてコンデンシングユニットにおける凝縮温度を低下せしめて冷媒圧力が下げられ、高圧側冷媒圧力が危険な高圧となるのを防止することができ(高圧安全コントロール)、また低圧側冷媒圧力の上昇に伴う圧縮機の過負荷(オーバーロード)の上昇によって圧縮機駆動用モータの焼け付きを防止することができる。   In this way, the cooling water is cooled by both the cooling tower and the steam / hot water generator, reducing the condensation temperature in the condensing unit and lowering the refrigerant pressure, preventing the high-pressure side refrigerant pressure from becoming a dangerously high pressure. This can be done (high pressure safety control), and burn-in of the compressor drive motor can be prevented by an increase in the overload of the compressor accompanying an increase in the low-pressure side refrigerant pressure.

なお、冷却塔12と蒸気・温水発生装置17への冷却水の送水により高圧側冷媒圧力と低圧側冷媒圧力が低下したら冷却塔12への供給を徐々に減少せしめ、その後蒸気・温水発生装置だけに冷却水を供給する。   If the high-pressure side refrigerant pressure and the low-pressure side refrigerant pressure drop due to the supply of cooling water to the cooling tower 12 and the steam / hot water generator 17, the supply to the cooling tower 12 is gradually reduced, and then only the steam / hot water generator is used. Supply cooling water to

また、蒸気・温水発生装置17に対する蒸気と温水の必要量が減少すると、制御回路44は流量計からの信号により蒸気や温水の流量が低下したことを検知し、コンデンシングユニットからの冷却水を冷却塔に流し、蒸気・温水発生装置17を停止すると冷却水の全量を冷却塔に流す。   When the required amount of steam and hot water for the steam / hot water generator 17 is reduced, the control circuit 44 detects that the flow rate of steam and hot water is reduced by a signal from the flow meter, and supplies the cooling water from the condensing unit. When the steam / warm water generator 17 is stopped after flowing into the cooling tower, the entire amount of cooling water is passed through the cooling tower.

上述のように三方制御弁43による流量制御を行う構成とすることにより、コンデンシングユニット1および蒸気・温水発生装置17のそれぞれの運転状況に応じて冷却水の制御を最も適切な状態にコントロールすることができ、常に安定した運転を行うことができる。   By adopting a configuration in which the flow control is performed by the three-way control valve 43 as described above, the control of the cooling water is controlled to the most appropriate state according to the respective operating conditions of the condensing unit 1 and the steam / hot water generator 17. Can always be operated stably.

本発明に係る冷却システムの実施例を示す構成図。The block diagram which shows the Example of the cooling system which concerns on this invention. 蒸気・温水発生装置の具体例を示す構成図。The block diagram which shows the specific example of a steam and warm water generator. 蒸気・温水発生装置における運転モードと開閉弁の状態を示す表。The table | surface which shows the operation mode and the state of an on-off valve in a steam / hot water generator. 蒸気・温水発生装置の蒸気供給運転における冷媒の流れを示す構成図。The block diagram which shows the flow of the refrigerant | coolant in the vapor | steam supply operation | movement of a vapor | steam / hot water generator. 蒸気・温水発生装置の蒸気・温水供給運転モードおよび温水供給運転モードにおける冷媒の流れを示す構成図。The block diagram which shows the flow of the refrigerant | coolant in the steam / hot water supply operation mode of the steam / hot water generator, and the hot water supply operation mode. 蒸気・温水発生装置の他の例を示す構成図。The block diagram which shows the other example of a steam and warm water generator. 冷却システムの他の例を示す構成図。The block diagram which shows the other example of a cooling system.

符号の説明Explanation of symbols

1 コンデンシングユニット
2 圧縮機
3 凝縮器
4 冷媒往管
5 膨張弁
6 凍結庫
7 空調器
8 蒸発器
9 冷媒復管
10 冷却水送出管
11 冷却水ポンプ
12 冷却塔
13 冷却水供給管
14 送風機
15 冷却水送出枝管
16 冷却水供給枝管
17 蒸気・温水発生装置
18 水入口
19 水出口
20 切替機構
21 低段側圧縮機
22 中圧冷媒管
23 高段側圧縮機
24 冷媒往管
25 第1凝縮器
26 第2凝縮器
27 中間冷却器用膨張弁
28 中間冷却器
29 蒸発器用膨張弁
30 蒸発器
31 冷媒復管
32 バイパス管
33 ガス冷媒戻し管
34 第1給水管
35 蒸気・温水供給管
36 第2給水管
37 温水供給管
40 熱交換器
41 第3給水管
42 第2温水供給管
43 三方制御弁
44 制御回路
45 高圧側圧力スイッチ
46 低圧側圧力スイッチ
47、48 流量計
1、V2、V3、V6、V8、V9、V10、V11 開閉弁
4、V5、V7 流量制御弁
1 Condensing unit
2 Compressor
3 Condenser
4 Refrigerant outbound pipe
5 Expansion valve
6 Freezer
7 Air conditioner
8 Evaporator
DESCRIPTION OF SYMBOLS 9 Refrigerant return pipe 10 Cooling water delivery pipe 11 Cooling water pump 12 Cooling tower 13 Cooling water supply pipe 14 Blower 15 Cooling water delivery branch pipe 16 Cooling water supply branch pipe 17 Steam / hot water generator 18 Water inlet 19 Water outlet 20 Switching mechanism DESCRIPTION OF SYMBOLS 21 Low stage side compressor 22 Medium pressure refrigerant pipe 23 High stage side compressor 24 Refrigerant going pipe 25 1st condenser 26 2nd condenser 27 Expansion valve for intermediate coolers 28 Intermediate cooler 29 Expansion valve for evaporators 30 Evaporator 31 Refrigerant return pipe 32 Bypass pipe 33 Gas refrigerant return pipe 34 First water supply pipe 35 Steam / hot water supply pipe 36 Second water supply pipe 37 Hot water supply pipe 40 Heat exchanger 41 Third water supply pipe 42 Second hot water supply pipe 43 Three-way control valve 44 Control circuit 45 High pressure side pressure switch 46 Low pressure side pressure switch 47, 48 Flowmeter V 1 , V 2 , V 3 , V 6 , V 8 , V 9 , V 10 , V 11 On- off valve V 4 , V 5 , V 7 flow control valve

Claims (10)

圧縮式冷媒回路を備え、同冷媒回路における凝縮排熱を冷却塔にて大気に放出するコンデンシングユニットと、圧縮手段、凝縮手段、膨張弁、蒸発器をこの順に備え、外部から前記凝縮手段に供給される水を同凝縮手段における冷媒の凝縮熱により加熱して蒸気・温水を供給するヒートポンプ式蒸気・温水発生装置を備え、前記コンデンシングユニットにおける凝縮器からの水を、前記冷却塔と、前記蒸気・温水発生装置における蒸発器とのいずれか一方あるいは両方に切替えて流通させる切替機構を備え、コンデンシングユニットからの凝縮排熱を冷却塔から大気への放出と、蒸気・温水発生装置による回収の一方または両方に切替えることができるように構成してなる冷却システム。   A condensing unit that includes a compression refrigerant circuit, and that discharges the condensed exhaust heat in the refrigerant circuit to the atmosphere in the cooling tower, a compression unit, a condensing unit, an expansion valve, and an evaporator are provided in this order. A heat pump type steam / hot water generator for supplying steam / hot water by heating the supplied water with the heat of condensation of the refrigerant in the condensing means, water from the condenser in the condensing unit, the cooling tower, Provided with a switching mechanism for switching to one or both of the evaporators in the steam / hot water generator and circulating the condensed exhaust heat from the condensing unit to the atmosphere from the cooling tower, and by the steam / hot water generator A cooling system configured to be switched to one or both of recovery. 圧縮式冷媒回路を備え、同冷媒回路における凝縮排熱を冷却塔にて大気に放出するコンデンシングユニットと、圧縮手段、凝縮手段、膨張弁、蒸発器をこの順に備え、外部から前記凝縮手段に供給される水を同凝縮手段における冷媒の凝縮熱により加熱して蒸気・温水を供給するヒートポンプ式蒸気・温水発生装置を備え、前記コンデンシングユニットにおける凝縮器からの水を前記冷却塔に送る冷却水送出管の途中に冷却水送出枝管の一端を接続するとともに、冷却塔から凝縮器へ冷却水を供給する冷却水供給管の途中に冷却水供給枝管の一端を接続し、前記冷却水送出枝管の他端と冷却水供給枝管の他端を、それぞれ前記蒸気・温水発生装置における蒸発器の水入口と同出口に接続し、かつ前記冷却水送出管と同枝管との分岐部および前記冷却水供給管と同枝管の分岐部に、コンデンシングユニットと冷却塔との間またはコンデンシングユニットと蒸気・温水発生装置との間あるいはコンデンシングユニットと冷却塔および蒸気・温水発生装置の両方との間に冷却水を切替えて流通させる切替機構を備え、コンデンシングユニットからの凝縮排熱を冷却塔から大気への放出と、蒸気・温水発生装置による回収の一方または両方に切替えてコンデンシングユニットにおける凝縮温度を低く維持することができるように構成してなる冷却システム。   A condensing unit that includes a compression refrigerant circuit, and that discharges the condensed exhaust heat in the refrigerant circuit to the atmosphere in the cooling tower, a compression unit, a condensing unit, an expansion valve, and an evaporator are provided in this order. A heat pump type steam / hot water generator for supplying steam / hot water by heating the supplied water with the condensation heat of the refrigerant in the condensing means, and cooling the water from the condenser in the condensing unit to the cooling tower One end of the cooling water delivery branch pipe is connected to the middle of the water delivery pipe, and one end of the cooling water supply branch pipe is connected to the middle of the cooling water supply pipe for supplying the cooling water from the cooling tower to the condenser. The other end of the delivery branch pipe and the other end of the cooling water supply branch pipe are respectively connected to the water inlet and the outlet of the evaporator in the steam / hot water generator, and the cooling water delivery pipe and the branch pipe are branched. Department and front At the branch of the cooling water supply pipe and the branch pipe, between the condensing unit and the cooling tower, between the condensing unit and the steam / hot water generator, or both the condensing unit and the cooling tower and the steam / hot water generator With a switching mechanism for switching and circulating the cooling water between them, and condensing by exhausting the condensed exhaust heat from the condensing unit to one or both of releasing it from the cooling tower to the atmosphere and collecting it with the steam / hot water generator A cooling system configured so that the condensation temperature in the unit can be kept low. 前記ヒートポンプ式蒸気・温水発生装置は、前記凝縮手段を冷媒往管に直列に接続した第1凝縮器と第2凝縮器で構成し、前記第1凝縮器と第2凝縮器からそれぞれ蒸気と温水が同時に供給されるように構成してなる請求項1または2に記載の冷却システム。   The heat pump steam / warm water generator comprises a first condenser and a second condenser in which the condensing means is connected in series with a refrigerant forward pipe, and steam and hot water are respectively supplied from the first condenser and the second condenser. The cooling system according to claim 1 or 2, wherein the cooling system is configured to be supplied simultaneously. 前記ヒートポンプ式蒸気・温水発生装置は、前記凝縮手段を冷媒往管に直列に接続した第1凝縮器と第2凝縮器で構成し、前記第1凝縮器と第2凝縮器からそれぞれ蒸気と温水が同時に供給されるように構成し、かつ前記圧縮手段を低段側と高段側の2段の圧縮機で構成し、また前記第2凝縮器と前記膨張弁との間における冷媒往管に中間冷却器を設けるとともに、この中間冷却器の気相に一端が接続されたガス冷媒戻し管の他端を、前記低段側圧縮機の吐出側と高段側圧縮機の吸入側との間に接続された中圧冷媒管の途中に接続し、前記第2凝縮器と中間冷却器間の冷媒往管の途中に中間冷却器用の膨張弁とバイパス管とをこれら膨張弁とバイパス管が並列となるように設け、このバイパス管に、外部へ蒸気のみを供給する蒸気供給運転の際には閉ざされているが、蒸気と温水の両方を同時に供給する蒸気・温水供給運転および温水のみを供給する温水供給運転の際には開かれる第1開閉弁を備え、また、前記ガス冷媒戻し管の途中に、前記蒸気供給運転の際には開かれているが、前記蒸気・温水供給運転と温水供給運転の際には閉ざされる第2開閉弁を備え、さらに、前記第2凝縮器への給水管に、前記蒸気供給運転の際には閉ざされているが、前記蒸気・温水供給運転と温水供給運転の際には開かれる第3開閉弁を設けてなる請求項1または2に記載の冷却システム。   The heat pump steam / warm water generator comprises a first condenser and a second condenser in which the condensing means is connected in series with a refrigerant forward pipe, and steam and hot water are respectively supplied from the first condenser and the second condenser. At the same time, and the compression means is composed of a two-stage compressor of a low-stage side and a high-stage side, and a refrigerant forward pipe between the second condenser and the expansion valve is provided. An intermediate cooler is provided, and the other end of the gas refrigerant return pipe having one end connected to the gas phase of the intermediate cooler is connected between the discharge side of the low-stage compressor and the suction side of the high-stage compressor. An intermediate-pressure refrigerant pipe is connected in the middle of the refrigerant outlet pipe between the second condenser and the intermediate cooler, and an expansion valve and a bypass pipe for the intermediate cooler are connected in parallel. The steam supply operation of supplying only steam to the outside to this bypass pipe Is provided with a first on-off valve that is opened during steam / hot water supply operation for supplying both steam and hot water at the same time and hot water supply operation for supplying only hot water. A second open / close valve is provided in the middle of the pipe, which is opened during the steam supply operation but is closed during the steam / hot water supply operation and the hot water supply operation, and further to the second condenser. 3. A third open / close valve that is closed during the steam supply operation but is opened during the steam / hot water supply operation and the hot water supply operation is provided in the water supply pipe of claim 1. Cooling system. 前記コンデンシングユニットの起動時において、前記ヒートポンプ式蒸気・温水発生装置を駆動せしめるとともに、前記切替機構がコンデンシングユニットからの冷却水を前記冷却塔と蒸気・温水発生装置の両方に送るよう切替えられるように構成してなる請求項1または2に記載の冷却システム。   When starting the condensing unit, the heat pump steam / hot water generator is driven, and the switching mechanism is switched to send the cooling water from the condensing unit to both the cooling tower and the steam / hot water generator. The cooling system according to claim 1 or 2, wherein the cooling system is configured as described above. 前記ヒートポンプ式蒸気・温水発生装置における第1凝縮器への給水管の途中に、第1凝縮器への給水量を制御するための給水制御手段を設けて、第1凝縮器から温水または蒸気のいずれかを選択的に供給できるようにした請求項3または4に記載の冷却システム。   A water supply control means for controlling the amount of water supplied to the first condenser is provided in the middle of the water supply pipe to the first condenser in the heat pump steam / hot water generator, and the hot water or steam is supplied from the first condenser. The cooling system according to claim 3 or 4, wherein either of them can be selectively supplied. 前記ヒートポンプ式蒸気・温水発生装置における第2凝縮器への給水管の途中に、第2凝縮器への給水量を制御するための給水制御手段を設けて、第2凝縮器への給水量の調節により同第2凝縮器から供給される温水が所要の温度となるよう調節できるようにした請求項3または4に記載の冷却システム。   A water supply control means for controlling the amount of water supplied to the second condenser is provided in the middle of the water supply pipe to the second condenser in the heat pump steam / hot water generator, and the amount of water supplied to the second condenser is controlled. The cooling system according to claim 3 or 4, wherein the hot water supplied from the second condenser can be adjusted to a required temperature by adjustment. 前記ヒートポンプ式蒸気・温水発生装置における第2凝縮器への給水管の途中に、第2凝縮器への給水量を制御するための給水制御手段を設けて、第2凝縮器への給水量の調節により冷媒往管内における冷媒圧力を常に所定の圧力以下に維持することができるようにした請求項3または4に記載の冷却システム。   A water supply control means for controlling the amount of water supplied to the second condenser is provided in the middle of the water supply pipe to the second condenser in the heat pump steam / hot water generator, and the amount of water supplied to the second condenser is controlled. The cooling system according to claim 3 or 4, wherein the refrigerant pressure in the refrigerant forward pipe can always be maintained below a predetermined pressure by adjustment. 前記切替機構を三方制御弁で構成し、この三方制御弁をコントロールする制御回路にコンデンシングユニットの高圧側冷媒圧力と低圧側冷媒圧力を検出する高圧側圧力スイッチと低圧側圧力スイッチを接続し、高圧側または低圧側の冷媒圧力が所定の値を超えるとコンデンシングユニットからの冷却水を前記冷却塔と蒸気・温水発生装置の両方に送り、上記冷媒圧力が予め設定された値以下に低下すると徐々に冷却塔への冷却水の供給を減少せしめるように構成してなる請求項1または2に記載の冷却システム。   The switching mechanism is constituted by a three-way control valve, and a high-pressure side pressure switch and a low-pressure side pressure switch for detecting the high-pressure side refrigerant pressure and the low-pressure side refrigerant pressure of the condensing unit are connected to a control circuit that controls the three-way control valve, When the refrigerant pressure on the high-pressure side or low-pressure side exceeds a predetermined value, the cooling water from the condensing unit is sent to both the cooling tower and the steam / hot water generator, and the refrigerant pressure falls below a preset value. The cooling system according to claim 1 or 2, wherein the cooling system is configured to gradually reduce the supply of cooling water to the cooling tower. 前記切替機構を三方制御弁で構成し、この三方制御弁をコントロールする制御回路に前記蒸気・温水発生装置からの蒸気供給量と温水供給量をそれぞれ検出する流量計を接続し、蒸気供給量と温水供給量が減少するとコンデンシングユニットから前記冷却塔への冷却水の供給量を徐々に大ならしめ、蒸気・温水発生装置が停止されると冷却水の全量を冷却塔へ送るように切り替えられるように構成してなる請求項1または2に記載の冷却システム。   The switching mechanism is constituted by a three-way control valve, and a flow meter for detecting the steam supply amount and the hot water supply amount from the steam / hot water generator is connected to a control circuit for controlling the three-way control valve, When the hot water supply amount decreases, the cooling water supply amount from the condensing unit to the cooling tower is gradually increased, and when the steam / hot water generator is stopped, the entire amount of cooling water can be sent to the cooling tower. The cooling system according to claim 1 or 2, wherein the cooling system is configured as described above.
JP2004198018A 2004-07-05 2004-07-05 Cooling system Expired - Lifetime JP4317793B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004198018A JP4317793B2 (en) 2004-07-05 2004-07-05 Cooling system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004198018A JP4317793B2 (en) 2004-07-05 2004-07-05 Cooling system

Publications (2)

Publication Number Publication Date
JP2006017427A true JP2006017427A (en) 2006-01-19
JP4317793B2 JP4317793B2 (en) 2009-08-19

Family

ID=35791878

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004198018A Expired - Lifetime JP4317793B2 (en) 2004-07-05 2004-07-05 Cooling system

Country Status (1)

Country Link
JP (1) JP4317793B2 (en)

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007202446A (en) * 2006-01-31 2007-08-16 Kansai Electric Power Co Inc:The Heating/cooling device for sterilization
JP2007232357A (en) * 2006-02-01 2007-09-13 Kansai Electric Power Co Inc:The Heat pump type steam and warm water generator
JP2007301018A (en) * 2006-05-09 2007-11-22 Toshiba Corp Clothes dryer
JP2008298406A (en) * 2007-06-04 2008-12-11 Toyo Eng Works Ltd Multiple heat pump-type steam-hot water generation device
JP2009085540A (en) * 2007-10-01 2009-04-23 Mitsubishi Heavy Ind Ltd Steam generation device and steam generation method
JP2009216383A (en) * 2009-06-30 2009-09-24 Toyo Eng Works Ltd Multiple heat pump type steam/hot water generating device
WO2010056556A1 (en) * 2008-11-12 2010-05-20 Johnson Controls Technology Company Multi-stage heat exchanger
JP2011021806A (en) * 2009-07-15 2011-02-03 Fujitsu General Ltd Water-cooled heat pump heat source device
CN102213505A (en) * 2010-04-09 2011-10-12 吕瑞强 Distributary partial cold source and heat source complementary system for heating water by byproduct heat of refrigerator
JP2012037197A (en) * 2010-08-11 2012-02-23 Miura Co Ltd Heat pump type steam generator
JP2014055692A (en) * 2012-09-11 2014-03-27 Takenaka Komuten Co Ltd Double bundle type freezing machine
KR101856414B1 (en) * 2017-04-06 2018-05-09 (주)유천써모텍 Large temperature differential water heat storage system
CN108826678A (en) * 2018-08-13 2018-11-16 珠海格力电器股份有限公司 Heat exchanger structure and air can water heater
CN111550943A (en) * 2020-04-26 2020-08-18 珠海格力电器股份有限公司 Secondary throttling double-condensation refrigerating system, air conditioner and control method
CN111550942A (en) * 2020-04-26 2020-08-18 珠海格力电器股份有限公司 Double-enthalpy-increasing double-condensing three-stage compression refrigeration system, air conditioner and control method
CN111623546A (en) * 2020-04-26 2020-09-04 珠海格力电器股份有限公司 Triple throttling enthalpy-increasing double-condensation refrigerating system, air conditioner and control method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101403452B1 (en) * 2012-11-01 2014-06-03 주식회사 티이애플리케이션 Chiller System

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007202446A (en) * 2006-01-31 2007-08-16 Kansai Electric Power Co Inc:The Heating/cooling device for sterilization
JP4587964B2 (en) * 2006-01-31 2010-11-24 関西電力株式会社 Heating / cooling device for sterilization
JP2007232357A (en) * 2006-02-01 2007-09-13 Kansai Electric Power Co Inc:The Heat pump type steam and warm water generator
JP2007301018A (en) * 2006-05-09 2007-11-22 Toshiba Corp Clothes dryer
JP2008298406A (en) * 2007-06-04 2008-12-11 Toyo Eng Works Ltd Multiple heat pump-type steam-hot water generation device
JP2009085540A (en) * 2007-10-01 2009-04-23 Mitsubishi Heavy Ind Ltd Steam generation device and steam generation method
WO2010056556A1 (en) * 2008-11-12 2010-05-20 Johnson Controls Technology Company Multi-stage heat exchanger
JP2009216383A (en) * 2009-06-30 2009-09-24 Toyo Eng Works Ltd Multiple heat pump type steam/hot water generating device
JP2011021806A (en) * 2009-07-15 2011-02-03 Fujitsu General Ltd Water-cooled heat pump heat source device
CN102213505A (en) * 2010-04-09 2011-10-12 吕瑞强 Distributary partial cold source and heat source complementary system for heating water by byproduct heat of refrigerator
JP2012037197A (en) * 2010-08-11 2012-02-23 Miura Co Ltd Heat pump type steam generator
JP2014055692A (en) * 2012-09-11 2014-03-27 Takenaka Komuten Co Ltd Double bundle type freezing machine
KR101856414B1 (en) * 2017-04-06 2018-05-09 (주)유천써모텍 Large temperature differential water heat storage system
CN108826678A (en) * 2018-08-13 2018-11-16 珠海格力电器股份有限公司 Heat exchanger structure and air can water heater
CN111550943A (en) * 2020-04-26 2020-08-18 珠海格力电器股份有限公司 Secondary throttling double-condensation refrigerating system, air conditioner and control method
CN111550942A (en) * 2020-04-26 2020-08-18 珠海格力电器股份有限公司 Double-enthalpy-increasing double-condensing three-stage compression refrigeration system, air conditioner and control method
CN111623546A (en) * 2020-04-26 2020-09-04 珠海格力电器股份有限公司 Triple throttling enthalpy-increasing double-condensation refrigerating system, air conditioner and control method

Also Published As

Publication number Publication date
JP4317793B2 (en) 2009-08-19

Similar Documents

Publication Publication Date Title
KR101155496B1 (en) Heat pump type speed heating apparatus
KR101192346B1 (en) Heat pump type speed heating apparatus
JP4317793B2 (en) Cooling system
KR101155497B1 (en) Heat pump type speed heating apparatus
JP5166385B2 (en) Air conditioning and hot water supply system
JP4471992B2 (en) Multi-source heat pump steam / hot water generator
JP4827191B2 (en) Operation method of heat pump using CO2 as refrigerant
JP2010065986A (en) Refrigeration cycle device and air conditioner
JP2004218944A (en) Heat pump air conditioning and water heater
JP4044917B2 (en) Heat pump steam / hot water generator
JP2007051841A (en) Refrigeration cycle device
JP2009156496A (en) Air conditioner
WO2006112157A1 (en) Refrigeration cycle device and method of operating the same
JP5313774B2 (en) Air conditioner
JP4084915B2 (en) Refrigeration system
JP2017161159A (en) Outdoor uni of air conditioner
JP6613404B2 (en) Refrigeration system
JP3871207B2 (en) Refrigeration system combining absorption and compression
KR100613502B1 (en) Heat pump type air conditioner
JP3918980B2 (en) Refrigeration equipment
JP3871206B2 (en) Refrigeration system combining absorption and compression
JP2005147582A (en) Air conditioner
KR101212686B1 (en) Heat pump type speed heating apparatus
DK2496894T3 (en) COOLING SYSTEM AND PROCEDURE FOR COOLING SYSTEM OPERATION
JP3253276B2 (en) Thermal storage type air conditioner and operation method thereof

Legal Events

Date Code Title Description
A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20051004

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060425

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20081201

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20081209

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090130

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: 20090428

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: 20090525

R150 Certificate of patent or registration of utility model

Ref document number: 4317793

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

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

Free format text: PAYMENT UNTIL: 20120529

Year of fee payment: 3

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

Free format text: PAYMENT UNTIL: 20120529

Year of fee payment: 3

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

Free format text: PAYMENT UNTIL: 20130529

Year of fee payment: 4

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

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

Free format text: PAYMENT UNTIL: 20130529

Year of fee payment: 4

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

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

Free format text: PAYMENT UNTIL: 20130529

Year of fee payment: 4

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

Free format text: PAYMENT UNTIL: 20140529

Year of fee payment: 5

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

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

R360 Written notification for declining of transfer of rights

Free format text: JAPANESE INTERMEDIATE CODE: R360

R370 Written measure of declining of transfer procedure

Free format text: JAPANESE INTERMEDIATE CODE: R370

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313115

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

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

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