JP2002071245A - Heat pump equipment - Google Patents
Heat pump equipmentInfo
- Publication number
- JP2002071245A JP2002071245A JP2000257392A JP2000257392A JP2002071245A JP 2002071245 A JP2002071245 A JP 2002071245A JP 2000257392 A JP2000257392 A JP 2000257392A JP 2000257392 A JP2000257392 A JP 2000257392A JP 2002071245 A JP2002071245 A JP 2002071245A
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- JP
- Japan
- Prior art keywords
- heat
- heat exchanger
- refrigerant
- load
- liquid
- 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.)
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Links
Landscapes
- Air Conditioning Control Device (AREA)
Abstract
(57)【要約】
【課題】 除霜運転において凍結トラブルを防止する。
【解決手段】 対空気熱交換器2を冷媒蒸発器Eとして
機能させ、かつ、対負荷熱交換器3を冷媒凝縮器Cとし
て機能させる負荷対応運転と、対液熱交換器1を冷媒蒸
発器Eとして機能させ、かつ、対空気熱交換器2を冷媒
凝縮器Cとして機能させる主除霜運転と、対負荷熱交換
器3を冷媒蒸発器Eとして機能させ、かつ、対空気熱交
換器2を冷媒凝縮器Cとして機能させる補助除霜運転と
の切り換えを可能にし、対空気熱交換器2に対する除霜
運転の必要時に、対液熱交換器1で冷媒Rと熱交換させ
る熱源側熱媒液Lbの温度tb、及び、対負荷熱交換器
3で冷媒Rと熱交換させる負荷側熱媒液Lfの温度tf
に応じて主除霜運転と補助除霜運転とを自動的に選択実
施する除霜制御手段14を設ける。
(57) [Summary] [Problem] To prevent freezing trouble in defrosting operation. A load-adaptive operation in which an air heat exchanger (2) functions as a refrigerant evaporator (E) and a load heat exchanger (3) functions as a refrigerant condenser (C), and the liquid heat exchanger (1) operates as a refrigerant evaporator. E, and the main defrosting operation in which the air heat exchanger 2 functions as the refrigerant condenser C, and the anti-load heat exchanger 3 functions as the refrigerant evaporator E, and the air heat exchanger 2 Can be switched to an auxiliary defrosting operation in which the heat exchanger functions as a refrigerant condenser C, and when the defrosting operation for the air heat exchanger 2 is necessary, the heat source side heat medium that exchanges heat with the refrigerant R in the liquid heat exchanger 1 The temperature tb of the liquid Lb, and the temperature tf of the load-side heat transfer fluid Lf for exchanging heat with the refrigerant R in the anti-load heat exchanger 3
And a defrosting control means 14 for automatically selecting and executing the main defrosting operation and the auxiliary defrosting operation according to the conditions.
Description
【0001】[0001]
【発明の属する技術分野】本発明はヒートポンプ装置に
関し、詳しくは、冷媒を大気空気と熱交換させる対空気
熱交換器を冷媒蒸発器として機能させ、かつ、冷媒を負
荷側熱媒液と熱交換させる対負荷熱交換器を冷媒凝縮器
として機能させる負荷対応運転の実施により種々の用途
の温熱を発生するヒートポンプ装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat pump device, and more particularly, to a heat pump device for exchanging heat between a refrigerant and atmospheric air, which functions as a refrigerant evaporator, and heat exchange between the refrigerant and a load side heat transfer fluid. The present invention relates to a heat pump device that generates heat for various uses by performing a load-corresponding operation in which a load heat exchanger to be operated functions as a refrigerant condenser.
【0002】[0002]
【従来の技術】この種のヒートポンプ装置では、上記負
荷対応運転の実施において対空気熱交換器に一定量以上
の着霜が生じると、その霜を除去する除霜運転が必要に
なるが、従来、この除霜については、対負荷熱交換器を
冷媒蒸発器として機能させ、かつ、対空気熱交換器を冷
媒凝縮器として機能させる運転を実施して、対空気熱交
換器での発生凝縮熱により霜を融解させる方式が一般的
に採られている。2. Description of the Related Art In this type of heat pump device, when a certain amount or more of frost is formed in an air heat exchanger in the above-described load-response operation, a defrosting operation for removing the frost is required. Regarding this defrosting, the operation in which the anti-load heat exchanger functions as the refrigerant evaporator and the anti-air heat exchanger functions as the refrigerant condenser is performed, and the generated heat of condensation in the anti-air heat exchanger is performed. In general, a method of melting frost by frost is adopted.
【0003】[0003]
【発明が解決しようとする課題】しかし、対負荷熱交換
器を冷媒蒸発器として機能させる上記の除霜運転では、
負荷側から採熱するため、例えば、負荷装置が融雪装置
や路面凍結防止装置などである場合、その負荷装置側で
凍結トラブルを招く虞があり、また、そのような凍結の
虞は無い場合にしても、温熱を必要とする負荷側から採
熱することは負荷側にとって好ましくないものであっ
た。However, in the above-described defrosting operation in which the load heat exchanger functions as a refrigerant evaporator,
Since heat is collected from the load side, for example, when the load device is a snow melting device or a road surface freezing prevention device, there is a possibility that a freezing trouble may be caused on the load device side, and that there is no possibility of such freezing. However, it is not preferable for the load side to collect heat from the load side that requires heat.
【0004】そして、この問題を解決するのに、冷媒を
熱源側熱媒液と熱交換させる対液熱交換器を付加装備し
て、除霜の際には、対液熱交換器を冷媒蒸発器として機
能させ、かつ、対空気熱交換器を冷媒凝縮器として機能
させる運転を実施することで、熱源側熱媒液の側から採
熱する形態にして負荷側からの採熱を必要とせずに除霜
を行なえるようにした装置も考えたが、この改善装置に
しても、着霜を生じる低温季に熱源側熱媒液の側から採
熱することにおいて、その熱源側熱媒液の側で凍結トラ
ブルを招く虞がある問題があった。In order to solve this problem, a liquid-to-liquid heat exchanger for exchanging heat between the refrigerant and the heat-source-side heat transfer medium is additionally provided. By performing the operation of functioning as a heat exchanger and functioning the air heat exchanger as a refrigerant condenser, heat is collected from the heat source side heat transfer fluid side, eliminating the need for heat collection from the load side. We thought about a device that can perform defrosting, but even with this improved device, in the low-temperature season when frost is formed, heat is collected from the heat-source-side heat transfer fluid in order to remove the heat-source-side heat transfer fluid. There is a problem that a freezing trouble may be caused on the side.
【0005】この実情に鑑み、本発明の主たる課題は、
凍結トラブルを効果的に防止し、また、負荷側からの採
熱を効果的に軽減しながら、対空気熱交換器の除霜を行
なえるようにする点にある。[0005] In view of this situation, the main problems of the present invention are:
It is to prevent defrosting of the air heat exchanger while effectively preventing freezing trouble and effectively reducing heat collection from the load side.
【0006】[0006]
【課題を解決するための手段】〔1〕請求項1に係る発
明では、冷媒を大気空気と熱交換させる対空気熱交換器
と、冷媒を熱源側熱媒液と熱交換させる対液熱交換器
と、冷媒を負荷側熱媒液と熱交換させる対負荷熱交換器
とを設け、前記対空気熱交換器を冷媒蒸発器として機能
させ、かつ、前記対負荷熱交換器を冷媒凝縮器として機
能させる負荷対応運転と、前記対液熱交換器を冷媒蒸発
器として機能させ、かつ、前記対空気熱交換器を冷媒凝
縮器として機能させる主除霜運転と、前記対負荷熱交換
器を冷媒蒸発器として機能させ、かつ、前記対空気熱交
換器を冷媒凝縮器として機能させる補助除霜運転との切
り換えを可能にし、前記負荷対応運転の実施で前記対空
気熱交換器に着霜した霜を除去する除霜運転の必要時
に、前記熱源側熱媒液の温度及び前記負荷側熱媒液の温
度に応じて前記主除霜運転と前記補助除霜運転とを自動
的に選択実施する除霜制御手段を設ける。Means for Solving the Problems [1] In the invention according to claim 1, an air heat exchanger for exchanging heat between a refrigerant and atmospheric air, and a liquid heat exchange for exchanging heat between a refrigerant and a heat source side heat transfer fluid. A heat exchanger for heat exchange between the refrigerant and the load-side heat medium liquid, a heat exchanger for the load is provided, the heat exchanger for the air functions as a refrigerant evaporator, and the heat exchanger for the load as a refrigerant condenser. A load corresponding operation to function; a main defrosting operation in which the liquid heat exchanger functions as a refrigerant evaporator, and the air heat exchanger functions as a refrigerant condenser; and The frost formed on the air heat exchanger by performing the load corresponding operation is enabled to function as an evaporator and to be switched to an auxiliary defrosting operation in which the air heat exchanger functions as a refrigerant condenser. When the defrosting operation for removing heat is necessary, the heat source side heat transfer fluid Providing a defrosting control unit for automatically selecting out the said auxiliary defrosting operation and the main defrosting operation in accordance with the temperature of the temperature and the load-side heat transfer fluid.
【0007】つまり、この構成によれば、対空気熱交換
器に対する除霜の必要時に、熱源側熱媒液の側から採熱
して除霜を行なう上記の主除霜運転と、負荷側から採熱
して除霜を行なう上記の補助除霜運転とを、熱源側熱媒
液の温度及び負荷側熱媒液の温度に応じて除霜制御手段
に自動的に選択実施させるから、その選択基準を予め適
当に設定しておけば、負荷装置側での凍結や負荷側熱媒
液自身の凍結といった負荷側での凍結トラブル、及び、
熱源側熱媒液を採熱作用させる採熱源の凍結や熱源側熱
媒液自身の凍結といった熱源側熱媒液の側での凍結トラ
ブルを効果的に防止しながら、また、主除霜運転の方を
優先実施する形態にして温熱を必要とする負荷側からの
採熱を効果的に軽減しながら、対空気熱交換器の除霜を
行なうことができる。In other words, according to this configuration, when defrosting is required for the air heat exchanger, the above main defrosting operation is performed in which the heat is removed from the heat source side heat transfer medium to perform defrosting, and the load is removed from the load side. The above-mentioned auxiliary defrosting operation for heating and defrosting is automatically selected and executed by the defrosting control means according to the temperature of the heat source side heat transfer fluid and the temperature of the load side heat transfer fluid. If properly set in advance, freezing trouble on the load side such as freezing on the load device side and freezing on the load side heat transfer fluid itself, and,
While effectively preventing freezing trouble on the heat source side heat transfer fluid side such as freezing of the heat collection source causing the heat source side heat transfer fluid to act as a heat source and freezing of the heat source side heat transfer fluid itself, the main defrosting operation is also performed. In a preferred embodiment, the defrosting of the air-to-air heat exchanger can be performed while effectively reducing the heat collection from the load side requiring the heat.
【0008】〔2〕請求項2に係る発明では、請求項1
に係る発明の実施において、前記熱源側熱媒液を水と熱
交換させる複数の採熱用熱交換器を設け、前記対液熱交
換器を冷媒蒸発器として機能させ、かつ、前記対負荷熱
交換器又は前記対空気熱交換器を冷媒凝縮器として機能
させる液熱源運転において、複数の前記採熱用熱交換器
のうち前記熱源側熱媒液を器内通過させるものを、前記
熱源側熱媒液と水との熱交換状態に応じて、又は、設定
時間毎に自動的に切り換える凍結防止制御手段を設け
る。[2] In the invention according to claim 2, claim 1
In the implementation of the invention according to the present invention, a plurality of heat collecting heat exchangers for exchanging the heat source side heat transfer fluid with water are provided, the liquid heat exchanger functions as a refrigerant evaporator, and the heat load In the liquid heat source operation in which the exchanger or the air-to-air heat exchanger functions as a refrigerant condenser, the heat source-side heat medium of the plurality of heat-collecting heat exchangers is passed through the heat source-side heat exchanger. An anti-freezing control means is provided which automatically switches according to the heat exchange state between the medium and the water or at set time intervals.
【0009】つまり、この構成では、上記液熱源運転
で、熱源側熱媒液を水と熱交換させて水から採熱する形
態を採る場合、特に低温季にその水の凍結を招く虞があ
ることに対し、上記の如く、熱源側熱媒液を水と熱交換
させる採熱用熱交換器を複数設けて、それら複数の採熱
用熱交換器のうち熱源側熱媒液を器内通過させるもの
(すなわち、熱交換器として実機能させるもの)を、熱
源側熱媒液と水との熱交換状態に応じて、又は、設定時
間毎に自動的に切り換えることにより、その切り換え使
用において、各々の採熱用熱交換器での熱源側熱媒液と
水との熱交換を水の凍結に至るまでの段階に止めるよう
にし、また、熱源側熱媒液の器内通過を断った休止期間
中に各々の採熱用熱交換器を温度回復させるようにし、
これにより、水から採熱することにおいて、その水の凍
結を防止する。In other words, in this configuration, in the above-mentioned liquid heat source operation, when the heat source side heat transfer medium exchanges heat with water to take heat from water, there is a possibility that the water is frozen particularly in a low temperature season. In contrast, as described above, a plurality of heat collecting heat exchangers for exchanging the heat source side heat medium liquid with water are provided, and the heat source side heat medium liquid among the plurality of heat collecting heat exchangers passes through the chamber. In the switching use, by automatically switching what is to be performed (that is, what is actually functioning as a heat exchanger) according to the heat exchange state between the heat source side heat transfer fluid and water or at set time intervals, Stop the heat exchange between the heat source side heat transfer fluid and water in each heat collection heat exchanger at the stage before freezing the water, and also stop the heat source side heat transfer fluid from passing through the vessel During the period, to recover the temperature of each heat exchanger for heat collection,
This prevents freezing of the water when collecting heat from the water.
【0010】すなわち、このように採熱用熱交換器の自
動切り換え使用により水の凍結を防止する上記構成であ
れば、水の凍結防止のために水からの採熱を完全に断っ
てしまうような事態を回避できて、ないしは、そのよう
な事態に至り難くすることができて、低温季にも長期間
にわたり安定的に水から採熱することができ、この点
で、採熱性に一層優れた装置にすることができる。That is, with the above-described configuration in which the freezing of water is prevented by the automatic switching use of the heat-exchanging heat exchanger, the collection of heat from water is completely cut off to prevent the freezing of water. Can be avoided, or such a situation can hardly be reached, and it is possible to stably collect heat from water over a long period of time even in the low temperature season, and in this regard, the heat collecting property is more excellent. Device.
【0011】〔3〕請求項3に係る発明では、請求項1
に係る発明の実施において、前記熱源側熱媒液に水を用
いるとともに、前記対液熱交換器を複数設け、前記対液
熱交換器を冷媒蒸発器として機能させ、かつ、前記対負
荷熱交換器又は前記対空気熱交換器を冷媒凝縮器として
機能させる液熱源運転において、複数の前記対液熱交換
器のうち冷媒を器内通過させるものを、冷媒と水との熱
交換状態に応じて、又は、設定時間毎に自動的に切り換
える凍結防止制御手段を設ける。[3] In the invention according to claim 3, claim 1
In the embodiment of the present invention, water is used as the heat source side heat transfer fluid, a plurality of the liquid heat exchangers are provided, the liquid heat exchanger functions as a refrigerant evaporator, and the load heat exchange is performed. In the liquid heat source operation in which the heat exchanger for air or the air heat exchanger functions as a refrigerant condenser, one of the plurality of heat exchangers for liquid passing the refrigerant in the chamber, depending on the heat exchange state between the refrigerant and water. Alternatively, there is provided an anti-freezing control means for automatically switching every set time.
【0012】つまり、この構成では、上記液熱源運転
で、熱源側熱媒液に水を用いてその水から採熱する形態
を採る場合、特に低温季にその水の凍結を招く虞がある
ことに対し、上記の如く、対液熱交換器(この場合、冷
媒を水と熱交換させる熱交換器)を複数設けて、それら
複数の対液熱交換器のうち冷媒を器内通過させるもの
(すなわち、熱交換器として実機能させるもの)を、冷
媒と水との熱交換状態に応じて、又は、設定時間毎に自
動的に切り換えることにより、その切り換え使用におい
て、各々の対液熱交換器での冷媒と水との熱交換を水の
凍結に至るまでの段階に止めるようにし、また、冷媒の
器内通過を断った休止期間中に各々の対液熱交換器を温
度回復させるようにし、これにより、水から採熱するこ
とにおいて、その水の凍結を防止する。In other words, in this configuration, when the liquid heat source is operated, and water is used as the heat source side heat transfer medium and heat is taken from the water, the water may be frozen particularly in a low temperature season. In contrast, as described above, a plurality of liquid heat exchangers (in this case, heat exchangers for exchanging heat between a refrigerant and water) are provided, and among the plurality of liquid heat exchangers, the refrigerant passes through the inside of the apparatus ( That is, by automatically switching the heat exchanger between the refrigerant and the water according to the heat exchange state between the refrigerant and the water or at set time intervals, each of the liquid heat exchangers is used in the switching use. The heat exchange between the refrigerant and the water in the process is stopped at the stage before the water freezes, and the temperature of each of the liquid heat exchangers is restored during the suspension period in which the passage of the refrigerant through the vessel is stopped. , Thereby obtaining heat from the water, To prevent binding.
【0013】すなわち、このように対液熱交換器の自動
切り換え使用により水の凍結を防止する上記構成であれ
ば、請求項2に係る発明と同様、水の凍結防止のために
水からの採熱を完全に断ってしまうような事態を回避で
きて、ないしは、そのような事態に至り難くすることが
できて、低温季にも長期間にわたり安定的に水から採熱
することができ、この点で、採熱性に一層優れた装置に
することができる。That is, according to the above-described structure in which the freezing of water is prevented by the automatic switching use of the liquid heat exchanger, the water is collected from the water in order to prevent the freezing of water. It is possible to avoid a situation in which heat is completely turned off, or to make such a situation hard to occur, and to stably collect heat from water over a long period of time even in a low temperature season. In this respect, it is possible to make the apparatus more excellent in heat collecting property.
【0014】なお、請求項2に係る発明や請求項3に係
る発明による上記効果は、対空気熱交換器を設けないヒ
ートポンプ装置においても得ることができるが、対液熱
交換器を冷媒蒸発器として機能させ、かつ、対空気熱交
換器を冷媒凝縮器として機能させる液熱源運転(すなわ
ち、前記の主除霜運転)において、上記の如く水の凍結
を防止すれば、請求項1に係る発明と相俟って、対空気
熱交換器の除霜の際の熱源側熱媒液の側での凍結トラブ
ルを一層確実に防止でき、また、低温季にも長期間にわ
たり安定的に水から採熱できる点で、対空気熱交換器の
除霜において負荷側からの採熱を一層効果的に軽減でき
る。The above-mentioned effects of the invention according to claim 2 and the invention according to claim 3 can be obtained also in a heat pump apparatus having no air heat exchanger. In the liquid heat source operation (that is, the main defrosting operation) in which the freezing of water is prevented as described above in the liquid heat source operation that causes the air heat exchanger to function as the refrigerant condenser, the invention according to claim 1. In conjunction with this, freezing trouble on the heat source side heat transfer fluid side during defrosting of the air heat exchanger can be more reliably prevented, and the water can be stably collected for a long period of time even in the low temperature season. In terms of being able to heat, the heat collection from the load side can be more effectively reduced in the defrosting of the air heat exchanger.
【0015】また、請求項2に係る発明において熱源側
熱媒液と熱交換させる水、及び、請求項3に係る発明に
おいて熱源側熱媒液として用いる水には夫々、河川水、
湖沼水、地下水、湧水などの自然水、あるいは、対地熱
交換器、対下水熱交換器、排熱回収熱交換器などの他装
置に対して循環させる循環水など、採熱源としての使用
が可能な水であれば、種々のものを使用できる。In the second aspect of the present invention, the water for heat exchange with the heat source side heat transfer fluid and the water used as the heat source side heat transfer fluid in the third aspect of the invention are river water,
Use as a heat source, such as natural water such as lake water, groundwater, or spring water, or circulating water that circulates to other devices such as a ground heat exchanger, a sewage heat exchanger, or a waste heat recovery heat exchanger. Various water can be used as long as the water is possible.
【0016】[0016]
【発明の実施の形態】〔第1実施形態〕図1はヒートポ
ンプを用いた融雪設備を示し、1は冷媒Rを熱源側熱媒
液Lbと熱交換させる対液熱交換器、2は冷媒Rを大気
空気Aと熱交換させる対空気熱交換器、2aは対空気熱
交換器2に対し熱交換対象の空気Aを通風するファン、
3は冷媒Rを負荷側熱媒液Lfと熱交換させる対負荷熱
交換器である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS [First Embodiment] FIG. 1 shows a snow melting facility using a heat pump, 1 is a liquid heat exchanger for exchanging heat of a refrigerant R with a heat source side heat medium liquid Lb, and 2 is a refrigerant R A heat exchanger for exchanging heat with the atmospheric air A, 2a is a fan for passing air A to be heat-exchanged to the air heat exchanger 2,
Reference numeral 3 denotes a load heat exchanger for exchanging the refrigerant R with the load side heat transfer fluid Lf.
【0017】なお、本第1実施形態では、熱源側熱媒液
Lb及び負荷側熱媒液Lfの夫々にブライン(不凍液)
を用いている。In the first embodiment, each of the heat source side heat transfer fluid Lb and the load side heat transfer liquid Lf is provided with brine (antifreeze).
Is used.
【0018】4は圧縮機、5は膨張弁、6は4つの逆止
弁6a〜6dをブリッジ回路状に組み合わせた冷媒案内
回路、7はレシーバ、V1〜V3は冷媒経路切換用の第
1〜第3の四方弁、V4,V5は同じく冷媒経路切換用
の第1及び第2の開閉弁であり、これらと上記3つの熱
交換器1,2,3を主要構成装置としてヒートポンプ回
路(冷凍回路)Hを形成してある。Reference numeral 4 denotes a compressor, 5 denotes an expansion valve, 6 denotes a refrigerant guide circuit in which four check valves 6a to 6d are combined in a bridge circuit, 7 denotes a receiver, and V1 to V3 denote first to third refrigerant paths. The third four-way valves V4 and V5 are first and second on-off valves for switching the refrigerant path, and the heat pump circuit (refrigeration circuit) includes these and the three heat exchangers 1, 2, and 3 as main constituent devices. ) H is formed.
【0019】8A,8Bは熱源側熱媒液Lbを採熱源と
しての水Wと熱交換させる第1及び第2の採熱用熱交換
器、9はこれら第1及び第2採熱用熱交換器8A,8B
の夫々と対液熱交換器1との間で熱源側熱媒液Lbを循
環ポンプ10により循環させる熱源側循環路であり、V
6は熱源側熱媒液Lbを第1の採熱用熱交換器8Aに循
環させる状態と第2の採熱用熱交換器8Bに循環させる
状態との切り換えを行う液側三方弁、V7,V8は採熱
源としての水Wを第1の採熱用熱交換器8Aに通水する
状態と第2の採熱用熱交換器8Bに通水する状態との切
り換えを行なう水側開閉弁である。Reference numerals 8A and 8B denote first and second heat-exchanging heat exchangers for exchanging the heat source side heat transfer fluid Lb with water W as a heat-extracting source, and 9 denotes these first and second heat-exchanging heat exchangers. Vessels 8A, 8B
Is a heat source side circulation path in which the heat source side heat transfer fluid Lb is circulated by the circulation pump 10 between each of the liquid heat exchangers 1 and 2.
Reference numeral 6 denotes a liquid-side three-way valve for switching between a state in which the heat source side heat transfer medium Lb is circulated through the first heat-exchange heat exchanger 8A and a state in which the heat-source-side heat medium liquid Lb is circulated through the second heat-exchange heat exchanger 8B. V8 is a water-side on-off valve for switching between a state in which water W as a heat collection source flows through the first heat collection heat exchanger 8A and a state in which water W flows through the second heat collection heat exchanger 8B. is there.
【0020】また、11は負荷側熱媒液Lfを熱源にし
て融雪対象箇所の降着雪を融かす負荷装置としての融雪
熱交換器、12はこの融雪熱交換器11と対負荷熱交換
器3との間で負荷側熱媒液Lfを循環ポンプ13により
循環させる負荷側循環路である。Reference numeral 11 denotes a snow melting heat exchanger as a load device for melting snow accretion at a snow melting target location using the load side heat transfer fluid Lf as a heat source, and 12 denotes the snow melting heat exchanger 11 and the load heat exchanger 3. And a load-side circulation path for circulating the load-side heat transfer fluid Lf by the circulation pump 13.
【0021】そして、この融雪設備では、上記四方弁V
1〜V3及び開閉弁V4,V5による冷媒経路の切り換
えで次の(イ)〜(ホ)の運転を選択的に実施する。In the snow melting facility, the four-way valve V
The following operations (a) to (e) are selectively performed by switching the refrigerant paths by 1 to V3 and the on-off valves V4 and V5.
【0022】(イ)空気熱源の負荷対応運転 この運転では、図2に示す如くヒートポンプ回路Hにお
いて、冷媒Rを圧縮機4−第1四方弁V1−対負荷熱交
換器3−冷媒案内回路6−レシーバ7−膨張弁5−冷媒
案内回路6−第2四方弁V2−対空気熱交換器2−第1
四方弁V1−第3四方弁V3−圧縮機4の順に循環させ
る。(A) Operation corresponding to load of air heat source In this operation, as shown in FIG. 2, in the heat pump circuit H, the refrigerant R is supplied to the compressor 4-first four-way valve V1-pair load heat exchanger 3-refrigerant guide circuit 6 -Receiver 7-Expansion valve 5-Refrigerant guide circuit 6-Second four-way valve V2-Air heat exchanger 2- First
The four-way valve V1-the third four-way valve V3-the compressor 4 are circulated in this order.
【0023】すなわち、この冷媒循環より、負荷側熱媒
液Lfの循環運転の下で、対空気熱交換器2を冷媒蒸発
器Eとして機能させ、かつ、対負荷熱交換器3を冷媒凝
縮器Cとして機能させ、これにより、空気Aから採熱す
る形態で、融雪熱交換器11に送る負荷側熱媒液Lfを
加熱して融雪を行なう。That is, the refrigerant circulation allows the heat exchanger for air 2 to function as the refrigerant evaporator E and the heat exchanger for load 3 to operate as the refrigerant condenser under the circulation operation of the load side heat transfer fluid Lf. In this manner, the load-side heat transfer fluid Lf sent to the snow melting heat exchanger 11 is heated in the form of collecting heat from the air A to melt snow.
【0024】(ロ)2熱源(空気→水)の負荷対応運転 この運転では、図3に示す如くヒートポンプ回路Hにお
いて、冷媒Rを圧縮機4−第1四方弁V1−対負荷熱交
換器3−冷媒案内回路6−レシーバ7−膨張弁5−冷媒
案内回路6−第2四方弁V2−対空気熱交換器2−第1
開閉弁V4−対液熱交換器1−第3四方弁V3−圧縮機
4の順に循環させる。(B) Operation corresponding to load of two heat sources (air → water) In this operation, in the heat pump circuit H, the refrigerant R is supplied to the compressor 4-first four-way valve V1-to-load heat exchanger 3 as shown in FIG. -Refrigerant guide circuit 6-receiver 7-expansion valve 5-refrigerant guide circuit 6-second four-way valve V2-air heat exchanger 2-first
The on-off valve V4-the liquid heat exchanger 1-the third four-way valve V3-the compressor 4 are circulated in this order.
【0025】すなわち、この冷媒循環により、熱源側熱
媒液Lb及び負荷側熱媒液Lfの循環運転の下で、対空
気熱交換器2及び対液熱交換器1をその順の直列配置で
共に冷媒蒸発器Eとして機能させ、かつ、対負荷熱交換
器3を冷媒凝縮器Cとして機能させ、これにより、空気
A及び水Wから採熱する形態で、融雪熱交換器11に送
る負荷側熱媒液Lfを加熱して融雪を行なう。That is, due to the circulation of the refrigerant, the air-to-air heat exchanger 2 and the liquid-to-liquid heat exchanger 1 are arranged in series in this order under the circulation operation of the heat source side heat transfer fluid Lb and the load side heat transfer liquid Lf. Both are made to function as the refrigerant evaporator E and the load heat exchanger 3 is made to function as the refrigerant condenser C, whereby the heat is taken from the air A and the water W, and the load side to be sent to the snow melting heat exchanger 11 The heating medium Lf is heated to melt snow.
【0026】(ハ)水熱源の負荷対応運転 この運転では、図4に示す如くヒートポンプ回路Hにお
いて、冷媒Rを圧縮機4−第1四方弁V1−対負荷熱交
換器3−冷媒案内回路6−レシーバ7−膨張弁5−冷媒
案内回路6−第2四方弁V2−対液熱交換器1−第3四
方弁V3−圧縮機4の順に循環させる。(C) Operation corresponding to load of water heat source In this operation, as shown in FIG. 4, in the heat pump circuit H, the refrigerant R is supplied to the compressor 4-first four-way valve V1-to-load heat exchanger 3-refrigerant guide circuit 6 -Receiver 7-Expansion valve 5-Refrigerant guide circuit 6-Second four-way valve V2-Liquid heat exchanger 1-Third four-way valve V3-Compressor 4
【0027】すなわち、この冷媒循環により、熱源側熱
媒液Lb及び負荷側熱媒液Lfの循環運転の下で、対液
熱交換器1を冷媒蒸発器Eとして機能させ、かつ、対負
荷熱交換器3を冷媒凝縮器Cとして機能させ、これによ
り、水Wから採熱する形態で、融雪熱交換器11に送る
負荷側熱媒液Lfを加熱して融雪を行なう。That is, due to the circulation of the refrigerant, the liquid heat exchanger 1 functions as the refrigerant evaporator E under the circulation operation of the heat source side heat transfer fluid Lb and the load side heat transfer liquid Lf. The exchanger 3 functions as a refrigerant condenser C, and thereby heats the load-side heat medium liquid Lf sent to the snow melting heat exchanger 11 in a form of collecting heat from the water W to melt snow.
【0028】(ニ)主除霜運転 この運転では、図5に示す如くヒートポンプ回路Hにお
いて、冷媒Rを圧縮機4−第1四方弁V1−対空気熱交
換器2−第2開閉弁V5−レシーバ7−膨張弁5−冷媒
案内回路6−第2四方弁V2−対液熱交換器1−第3四
方弁V3−圧縮機4の順に循環させる。(D) Main defrosting operation In this operation, as shown in FIG. 5, in the heat pump circuit H, the refrigerant R is supplied to the compressor 4-first four-way valve V1-air heat exchanger 2-second on-off valve V5- The receiver 7-expansion valve 5-refrigerant guide circuit 6-second four-way valve V2-liquid heat exchanger 1-third four-way valve V3-compressor 4 is circulated in this order.
【0029】すなわち、この冷媒循環により、熱源側熱
媒液Lbの循環運転の下で、対液熱交換器1を冷媒蒸発
器Eとして機能させ、かつ、対空気熱交換器2を冷媒凝
縮器Cとして機能させ、これにより、水Wから採熱する
形態で対空気熱交換器2の除霜を行なう。That is, by the circulation of the refrigerant, the liquid heat exchanger 1 functions as the refrigerant evaporator E and the air heat exchanger 2 functions as the refrigerant condenser under the circulation operation of the heat source side heat transfer fluid Lb. C, thereby performing defrosting of the air heat exchanger 2 in a form of collecting heat from the water W.
【0030】(ホ)補助除霜運転 この運転では、図6に示す如くヒートポンプ回路Hにお
いて、冷媒Rを圧縮機4−第1四方弁V1−対空気熱交
換器2−第2四方弁V2−冷媒案内回路6−レシーバ7
−膨張弁5−冷媒案内回路6−対負荷熱交換器3−第1
四方弁V1−第3四方弁V3−圧縮機4の順に循環させ
る。(E) Auxiliary defrosting operation In this operation, as shown in FIG. 6, in the heat pump circuit H, the refrigerant R is supplied to the compressor 4-first four-way valve V1-air heat exchanger 2-second four-way valve V2- Refrigerant guide circuit 6-receiver 7
-Expansion valve 5-refrigerant guide circuit 6-load heat exchanger 3-first
The four-way valve V1-the third four-way valve V3-the compressor 4 are circulated in this order.
【0031】すなわち、この冷媒循環により、負荷側熱
媒液Lfの循環運転の下で、対負荷側熱交換器3を冷媒
蒸発器Eとして機能させ、かつ、対空気熱交換器2を冷
媒凝縮器Cとして機能させ、これにより、負荷側から採
熱する形態で対空気熱交換器2の除霜を行なう。That is, due to the circulation of the refrigerant, the load-side heat exchanger 3 functions as the refrigerant evaporator E and the air-side heat exchanger 2 condenses the refrigerant under the circulation operation of the load-side heat medium liquid Lf. The air heat exchanger 2 is defrosted in such a manner that the air heat exchanger 2 is functioned as a device C and heat is taken from the load side.
【0032】S1は採熱用熱交換器8A,8Bに供給す
る水Wの温度twを検出するセンサ、S2は対空気熱交
換器2に通風する空気Aの温度taを検出するセンサ、
S3は採熱用熱交換器8A,8Bに通過させる熱源側熱
媒液Lbの温度tbを検出するセンサ、S4は融雪熱交
換器11に通過させる負荷側熱媒液Lfの温度tfを検
出するセンサ、S5,S6は第1及び第2採熱用熱交換
器8A,8Bの各々から送出される水Wの温度t1,t
2を検出するセンサである。S1 is a sensor for detecting the temperature tw of the water W supplied to the heat collecting heat exchangers 8A and 8B, S2 is a sensor for detecting the temperature ta of the air A passing through the air heat exchanger 2,
S3 is a sensor for detecting the temperature tb of the heat-source-side heat transfer fluid Lb passed through the heat-exchanging heat exchangers 8A and 8B, and S4 is detecting the temperature tf of the load-side heat transfer fluid Lf passed through the snow-melting heat exchanger 11. The sensors S5 and S6 are the temperatures t1 and t of the water W sent from each of the first and second heat sampling heat exchangers 8A and 8B.
2 is a sensor for detecting
【0033】14は各センサS1〜S6の検出温度に基
づき上記の各運転を自動的に選択実施する制御器であ
り、この制御器14は、(イ)〜(ハ)の負荷対応運転
の自動選択として、センサS1,S2により検出される
水温度tw及び空気温度taをパラメータとする状態点
P(tw,ta)が、予め設定された図7に示す如き選
択基準D1上で領域K1にある状況では、空気Aのみか
ら採熱する(イ)の負荷対応運転を選択実施し、同状態
点P(tw,ta)が領域K2にある状況では、空気A
及び水Wの両方から採熱する(ロ)の負荷対応運転を選
択実施し、同状態点P(tw,ta)が領域K3にある
状況では、水Wのみから採熱する(ハ)の負荷対応運転
を選択実施する。A controller 14 automatically selects and executes each of the above-mentioned operations based on the detected temperatures of the sensors S1 to S6. This controller 14 automatically controls the operations corresponding to the loads (a) to (c). As a selection, a state point P (tw, ta) using the water temperature tw and the air temperature ta detected by the sensors S1 and S2 as parameters is in a region K1 on a preset selection criterion D1 as shown in FIG. In the situation, the load corresponding operation of (a) in which heat is taken only from the air A is selected and executed, and in the situation where the state point P (tw, ta) is in the region K2, the air A
And the load corresponding operation of (b) in which heat is collected from both the water W and the state point P (tw, ta) is in the region K3, the load of (c) in which heat is collected only from the water W Select and execute the corresponding operation.
【0034】また、この制御器14は、空気Aからの採
熱を伴う(イ)又は(ロ)の負荷対応運転中に対空気熱
交換器2において一定量以上の着霜が生じたことが着霜
検出手段により検出されたとき、(ニ)又は(ホ)の除
霜運転に運転を自動的に切り換えるとともに、これら
(ニ)又は(ホ)の除霜運転の自動選択として、(ニ)
の主除霜運転の実施でセンサS3により検出される熱源
側熱媒液Lbの温度tb及び、(ホ)の補助除霜運転の
実施でセンサS4により検出される負荷側熱媒液Lfの
温度tfをパラメータとする状態点Q(tb,tf)
が、予め設定された図8に示す如き選択基準D2上で領
域M1にある状況では、水Wから採熱する(ニ)の主除
霜運転を選択実施し、同状態点Q(tb,tf)が領域
M2にある状況では、負荷側から採熱する(ホ)の補助
除霜運転を選択実施する。The controller 14 determines that a certain amount or more of frost has occurred in the air heat exchanger 2 during the load corresponding operation (a) or (b) involving heat collection from the air A. When it is detected by the frost detection means, the operation is automatically switched to the defrosting operation of (d) or (e), and the automatic selection of the defrosting operation of (d) or (e) is performed as (d)
The temperature tb of the heat source side heat transfer fluid Lb detected by the sensor S3 when the main defrosting operation is performed, and the temperature of the load side heat transfer fluid Lf detected by the sensor S4 during the execution of the auxiliary defrosting operation (e). State point Q (tb, tf) using tf as a parameter
However, in a situation where the temperature is in the region M1 on the preset selection criterion D2 as shown in FIG. 8, the main defrosting operation of (d) collecting heat from the water W is selected and executed, and the same state points Q (tb, tf) are obtained. ) Is in the region M2, the auxiliary defrosting operation of (e) for collecting heat from the load side is selectively executed.
【0035】なお、(ニ)の主除霜運転の実施中に上記
状態点Q(tb,tf)が領域M2に移行すると、それ
に伴い(ホ)の補助除霜運転に運転を切り換え、また同
様に、(ホ)の補助除霜運転中に上記状態点Q(tb,
tf)が領域M1に移行すると、それに伴い(ニ)の主
除霜運転に運転を切り換える。そして、除霜が完了する
と(ニ)又は(ホ)の除霜運転を自動的に終了し、その
後、(イ)〜(ハ)の負荷対応運転の選択実施に復帰す
る。When the state point Q (tb, tf) shifts to the area M2 during the execution of the main defrosting operation (d), the operation is switched to the auxiliary defrosting operation (e) accordingly. During the auxiliary defrosting operation (e), the state point Q (tb,
When the time tf) shifts to the area M1, the operation is switched to the main defrosting operation (d). Then, when the defrosting is completed, the defrosting operation of (d) or (e) is automatically terminated, and thereafter, the operation returns to the selection execution of the load corresponding operation of (a) to (c).
【0036】さらにまた、上記制御器14は、水Wから
の採熱を伴う(ロ)又は(ハ)の負荷対応運転、あるい
は、(ニ)の主除霜運転では、センサS5,S6の検出
温度t1,t2に基づく液側二方弁V6及び水側開閉弁
V7,V8の切り換え操作により、第1及び第2採熱用
熱交換器8A,8Bのうち熱源側熱媒液Lb及び水Wを
器内通過させるもの(すなわち、熱交換器として実機能
させるもの)を、熱源側熱媒液Lb及び水Wの通過状態
にある採熱用熱交換器8A,8Bからの送出水温度t
1,t2が設定下限温度tx(水の凍結近傍温度)まで
低下するごとに自動的に交互切り換えする。Further, the controller 14 detects the sensors S5 and S6 in the load corresponding operation (b) or (c) accompanied by heat extraction from the water W or in the main defrosting operation (d). The switching operation of the liquid-side two-way valve V6 and the water-side on-off valves V7 and V8 based on the temperatures t1 and t2 causes the heat source side heat transfer fluid Lb and the water W in the first and second heat-collecting heat exchangers 8A and 8B. Is passed through the inside of the vessel (that is, the one that actually functions as a heat exchanger) is changed to the water temperature t sent from the heat-collecting heat exchangers 8A and 8B in a state where the heat source side heat transfer fluid Lb and the water W pass.
Each time the temperature t1 or t2 decreases to the set lower limit temperature tx (temperature near freezing of water), the switching is automatically performed.
【0037】図7において、tasは負荷対応運転にお
いて水Wからの採熱を行なうか否かの設定閾空気温度で
ある。In FIG. 7, tas is a set threshold air temperature for determining whether or not to take heat from water W in a load corresponding operation.
【0038】図8において、tb1,tb2は熱源側熱
媒液Lbの側について設定した凍結危険温度と凍結注意
温度、tf1,tf2は負荷側について設定した凍結危
険温度と凍結注意温度であり、上記除霜運転の自動選択
では、センサS3,S4による熱源側及び負荷側の検出
熱媒液温度tb,tfが、ともに凍結危険温度と凍結注
意温度との間にある状況や、ともに凍結注意温度以上に
ある状況のときには(ニ)の主除霜運転を選択実施する
ことで、(ニ)の主除霜運転と(ホ)の補助除霜運転と
のうち全体としては(ニ)の主除霜運転の方を優先的に
実施するようにしてある。In FIG. 8, tb1 and tb2 are the freezing dangerous temperature and freezing caution temperature set for the heat source side heat transfer fluid Lb, and tf1 and tf2 are the freezing dangerous temperature and freezing caution temperature set for the load side. In the automatic selection of the defrosting operation, the detected heat medium liquid temperatures tb and tf on the heat source side and the load side by the sensors S3 and S4 are both between the freezing dangerous temperature and the freezing caution temperature, and are both higher than the freezing caution temperature. In the situation described in (2), the main defrosting operation of (d) is selected and performed, and as a whole, the main defrosting operation of (d) and the auxiliary defrosting operation of (e) are performed. Driving is prioritized.
【0039】また、本第1実施形態では、第1及び第2
採熱用熱交換器8A,8Bの上記交互使用において、休
止側の採熱用熱交換器8A,8Bに対する水Wの通過は
完全には遮断せず、休止側の採熱用熱交換器8A,8B
にも少量の水Wを通過させることで、その休止側の採熱
用熱交換器8A,8Bの温度回復を促進するようにして
ある。In the first embodiment, the first and second
In the alternate use of the heat collecting heat exchangers 8A and 8B, the passage of the water W to the inactive side heat collecting heat exchangers 8A and 8B is not completely blocked, and the inactive side heat collecting heat exchanger 8A is not used. , 8B
Also, by passing a small amount of water W, the recovery of the temperature of the heat-exchange heat exchangers 8A and 8B on the rest side is promoted.
【0040】以上、本第1実施形態において、制御器1
4は、(イ)又は(ロ)の負荷対応運転の実施で対空気
熱交換器2に着霜した霜を除去する除霜運転の必要時
に、熱源側熱媒液Lbの温度tb及び負荷側熱媒液Lf
の温度tfに応じて(ニ)の主除霜運転と(ホ)の補助
除霜運転とを自動的に選択実施する除霜制御手段を構成
する。As described above, in the first embodiment, the controller 1
4 indicates the temperature tb of the heat source side heat transfer fluid Lb and the load side when the defrosting operation for removing the frost formed on the air heat exchanger 2 in the execution of the load corresponding operation (a) or (b) is required. Heat medium liquid Lf
A defrost control unit that automatically selects and executes the main defrosting operation (d) and the auxiliary defrosting operation (e) according to the temperature tf of (i).
【0041】また、この制御器14は、対液熱交換器1
を冷媒蒸発器Eとして機能させ、かつ、対負荷熱交換器
3又は対空気熱交換器2を冷媒凝縮器Cとして機能させ
る(ロ),(ハ),(ニ)の運転(液熱源運転)におい
て、熱源側熱媒液Lbを水Wと熱交換させる複数の採熱
用熱交換器8A,8Bのうち熱源側熱媒液Lbを器内通
過させるものを、熱源側熱媒液Lbと水Wとの熱交換状
態に応じて自動的に切り換える凍結防止制御手段を構成
する。The controller 14 controls the liquid heat exchanger 1
(B), (c), and (d) (liquid heat source operation) in which the heat exchanger 3 functions as the refrigerant evaporator E and the heat exchanger 3 or the heat exchanger 2 for air functions as the refrigerant condenser C. In the plurality of heat collecting heat exchangers 8A and 8B for exchanging the heat source side heat medium liquid Lb with water W, the heat source side heat medium liquid Lb that passes through the heat source side heat medium liquid Lb and the water The antifreezing control means automatically switches according to the state of heat exchange with W.
【0042】なお、本第1実施形態の融雪設備では、上
記した(イ)〜(ホ)の運転の他、必要に応じて次の
(へ)〜(チ)の運転を選択実施できる。In the snow melting facility of the first embodiment, in addition to the above-described operations (a) to (e), the following operations (f) to (h) can be selectively executed as necessary.
【0043】(へ)逆2熱源(水→空気)の負荷対応運
転 この運転では、ヒートポンプ回路Hにおいて、冷媒Rを
圧縮機4−第1四方弁V1−対負荷熱交換器3−冷媒案
内回路6−レシーバ7−膨張弁5−冷媒案内回路6−第
2四方弁V2−対液熱交換器1−第3四方弁V3−第2
四方弁V2−対空気熱交換器2−第1四方弁V1−第3
四方弁V3−圧縮機4の順に循環させる。(F) Operation corresponding to load of two reverse heat sources (water → air) In this operation, in the heat pump circuit H, the refrigerant R is supplied to the compressor 4-first four-way valve V1-to-load heat exchanger 3-refrigerant guide circuit. 6-Receiver 7-Expansion valve 5-Refrigerant guide circuit 6-Second four-way valve V2-Liquid heat exchanger 1-Third four-way valve V3-Second
Four-way valve V2-to air heat exchanger 2-first four-way valve V1-third
Circulate in the order of the four-way valve V3-compressor 4.
【0044】すなわち、この冷媒循環により、熱源側熱
媒液Lb及び負荷側熱媒液Lfの循環運転の下で、対液
熱交換器1及び対空気熱交換器2をその順の直列配置で
共に冷媒蒸発器Eとして機能させ、かつ、対負荷熱交換
器3を冷媒凝縮器Cとして機能させ、これにより、水W
及び空気Aから採熱する形態で、融雪熱交換器11に送
る負荷側熱媒液Lfを加熱して融雪を行なう。That is, by this refrigerant circulation, the liquid heat exchanger 1 and the air heat exchanger 2 are arranged in series in this order under the circulation operation of the heat source side heat transfer fluid Lb and the load side heat transfer liquid Lf. Both function as a refrigerant evaporator E and the load heat exchanger 3 functions as a refrigerant condenser C.
In addition, the load-side heat transfer fluid Lf sent to the snow-melting heat exchanger 11 is heated in the form of collecting heat from the air A to melt snow.
【0045】(ト)除霜・負荷対応併用運転 この運転では、ヒートポンプ回路Hにおいて、冷媒Rを
圧縮機4−第1四方弁V1−対空気熱交換器2−第2四
方弁V2−第3四方弁V3−第1四方弁V1−対負荷熱
交換器3−冷媒案内回路6−レシーバ7−膨張弁5−冷
媒案内回路6−第2四方弁V2−対液熱交換器1−第3
四方弁V3−圧縮機4の順に循環させる。(G) Combined operation for defrosting / loading In this operation, in the heat pump circuit H, the refrigerant R is supplied to the compressor 4-first four-way valve V1-air heat exchanger 2-second four-way valve V2-third. Four-way valve V3-first four-way valve V1-load heat exchanger 3-refrigerant guide circuit 6-receiver 7-expansion valve 5-refrigerant guide circuit 6-second four-way valve V2-liquid heat exchanger 1-third
Circulate in the order of the four-way valve V3-compressor 4.
【0046】すなわち、この冷媒循環により、熱源側熱
媒液Lb及び負荷側熱媒液Lfの循環運転の下で、対液
熱交換器1を冷媒蒸発器Eとして機能させ、かつ、対空
気熱交換器2及び対負荷熱交換器3をその順の直列配置
で共に冷媒凝縮器Cとして機能させ、これにより、水W
から採熱する形態で、融雪熱交換器11に送る負荷側熱
媒液Lfを加熱して融雪を行なうとともに、それに並行
して対空気熱交換器2の除霜を行なう。That is, due to the circulation of the refrigerant, the liquid heat exchanger 1 functions as the refrigerant evaporator E under the circulation operation of the heat source side heat medium liquid Lb and the load side heat medium liquid Lf. The heat exchanger 3 and the heat exchanger 3 are arranged together in this order to function as a refrigerant condenser C.
In this mode, the load-side heat transfer fluid Lf sent to the snow melting heat exchanger 11 is heated to melt snow, and in parallel with this, defrosting of the air heat exchanger 2 is performed.
【0047】(チ)2熱源除霜運転 この運転では、ヒートポンプ回路Hにおいて、冷媒Rを
圧縮機4−第1四方弁V1−対空気熱交換器2−第2四
方弁V2−冷媒案内回路6−レシーバ7−膨張弁5−冷
媒案内回路6−対負荷熱交換器3−第1四方弁V1−第
3四方弁V3−第2四方弁V2−対液熱交換器1−第3
四方弁V3−圧縮機4の順に循環させる。(H) Two heat source defrosting operation In this operation, in the heat pump circuit H, the refrigerant R is supplied to the compressor 4-first four-way valve V1-air heat exchanger 2-second four-way valve V2-refrigerant guide circuit 6 -Receiver 7-Expansion valve 5-Refrigerant guide circuit 6-Load heat exchanger 3-First four-way valve V1-Third four-way valve V3-Second four-way valve V2-Liquid heat exchanger 1-Third
Circulate in the order of the four-way valve V3-compressor 4.
【0048】すなわち、この冷媒循環により、熱源側熱
媒液Lb及び負荷側熱媒液Lfの循環運転の下で、対負
荷熱交換器3及び対液熱交換器1をその順の直列配置で
共に冷媒蒸発器Eとして機能させ、かつ、対空気熱交換
器2を冷媒凝縮器Cとして機能させ、これにより、負荷
側及び水Wから採熱する形態で対空気熱交換器2の除霜
を行なう。That is, by the circulation of the refrigerant, the load heat exchanger 3 and the liquid heat exchanger 1 are arranged in series in this order under the circulation operation of the heat source side heat medium liquid Lb and the load side heat medium liquid Lf. Both function as a refrigerant evaporator E, and the air heat exchanger 2 functions as a refrigerant condenser C. Thereby, the defrosting of the air heat exchanger 2 is performed in a mode of collecting heat from the load side and the water W. Do.
【0049】そして、これら(へ)〜(チ)の運転につ
いても、水Wからの採熱を伴うことに対し、制御器14
は、(ロ),(ハ),(ニ)の運転と同様、センサS
5,S6の検出温度t1,t2に基づく前述の如き第1
及び第2採熱用熱交換器8A,8Bの自動交互使用を行
なう。Also, in the operations of (h) to (h), the control unit 14
Is the sensor S in the same manner as in (b), (c) and (d).
5 based on the detected temperatures t1 and t2 of S6.
Then, the automatic alternate use of the second heat collection heat exchangers 8A and 8B is performed.
【0050】〔第2実施形態〕図9はヒートポンプを用
いた別の融雪設備を示し、第1実施形態のものとの相違
点としては、対液熱交換器1として第1及び第2の二個
の対液熱交換器1A,1Bを設け、そして、対液熱交換
器1(1A,1B)で冷媒Rと熱交換させる熱源側熱媒
液に採熱源としての水Wを直接使用するようにしてあ
る。[Second Embodiment] FIG. 9 shows another snow melting facility using a heat pump. The difference between the second embodiment and the first embodiment is that the liquid heat exchanger 1 has the first and second heat exchangers. A plurality of liquid heat exchangers 1A and 1B are provided, and water W as a heat source is directly used as a heat source side heat transfer fluid to be exchanged with the refrigerant R in the liquid heat exchanger 1 (1A, 1B). It is.
【0051】なお、第1実施形態のものと同機能の部分
については、第1実施形態で用いたのと同じ符号を用い
てある。The parts having the same functions as those of the first embodiment are denoted by the same reference numerals as those used in the first embodiment.
【0052】V6′は冷媒Rを第1の対液熱交換器1A
に通過させる状態と第2の対液熱交換器8Bに通過させ
る状態との切り換えを行う冷媒側三方弁、V7′,V
8′は採熱源としての水Wを第1の対液熱交換器1Aに
通水する状態と第2の対液熱交換器1Bに通水する状態
との切り換えを行なう水側開閉弁である。V6 'transfers the refrigerant R to the first liquid heat exchanger 1A.
, V7 ′, V that switches between a state of passing through the second liquid heat exchanger 8B and a state of passing through the second liquid heat exchanger 8B
Reference numeral 8 'denotes a water-side opening / closing valve for switching between a state in which water W as a heat source is passed through the first liquid heat exchanger 1A and a state in which water W is passed through the second liquid heat exchanger 1B. .
【0053】また、S1′は対液熱交換器1A,1Bに
供給する水Wの温度twを検出するセンサ、S5′,S
6′は第1及び第2対液熱交換器1A,1Bの各々から
送出される水Wの温度t1′,t2′を検出するセンサ
である。S1 'is a sensor for detecting the temperature tw of the water W supplied to the liquid heat exchangers 1A and 1B, S5' and S5 '
Reference numeral 6 'denotes a sensor for detecting the temperatures t1' and t2 'of the water W sent from the first and second liquid heat exchangers 1A and 1B.
【0054】14′は各センサの検出温度に基づき前述
と同様の(イ)〜(ホ)の各運転を自動的に選択実施す
る制御器であり、この制御器14′は、(イ)〜(ハ)
の負荷対応運転の自動選択として、第1実施形態と同
様、センサS1′,S2により検出される水温度tw及
び空気温度taをパラメータとする状態点P(tw,t
a)が、図7に示す如き選択基準D1上で領域K1〜K
3のいずれに存在するかによって、(イ)〜(ハ)の負
荷対応運転を択一的に選択実施する。Reference numeral 14 'denotes a controller for automatically selecting and executing each of the above-mentioned operations (a) to (e) based on the temperature detected by each sensor. (C)
As in the first embodiment, the state point P (tw, t) using the water temperature tw and the air temperature ta detected by the sensors S1 'and S2 as parameters, as in the first embodiment.
a) is a region K1 to K1 on a selection criterion D1 as shown in FIG.
3, the operation corresponding to the load of (a) to (c) is selectively performed selectively.
【0055】また、この制御器14′は、空気Aからの
採熱を伴う(イ)又は(ロ)の負荷対応運転中に対空気
熱交換器2において一定量以上の着霜が生じたことが着
霜検出手段により検出されたとき、(ニ)又は(ホ)の
除霜運転に運転を自動的に切り換えるとともに、これら
(ニ)又は(ホ)の除霜運転の自動選択として、センサ
S1′により検出される水温度tw、及び、(ホ)の補
助除霜運転の実施でセンサS4により検出される負荷側
熱媒液Lbの温度tfをパラメータとする状態点Q′
(tw,tf)が、予め設定された図10に示す如き選
択基準D2′上で領域M1′にある状況では、水Wから
採熱する(ニ)の主除霜運転を選択実施し、同状態点
Q′(tw,tf)が領域M2′にある状況では、負荷
側から採熱する(ホ)の補助除霜運転を選択実施する。The controller 14 'detects that a certain amount or more of frost has formed in the air heat exchanger 2 during the operation corresponding to the load (a) or (b) accompanied by heat collection from the air A. Is detected by the frost detection means, the operation is automatically switched to the defrosting operation of (d) or (e), and the sensor S1 is automatically selected as the defrosting operation of (d) or (e). And the state point Q ′ using the temperature tf of the load-side heat transfer fluid Lb detected by the sensor S4 in the execution of the auxiliary defrosting operation (e) as a parameter.
In a situation where (tw, tf) is in the region M1 'on the preset selection criterion D2' as shown in FIG. 10, the main defrosting operation of (d) for collecting heat from the water W is selected and executed. In a situation where the state point Q '(tw, tf) is in the region M2', the auxiliary defrosting operation of (e) for collecting heat from the load side is selectively executed.
【0056】なお、第1実施形態と同様、(ニ)の主除
霜運転の実施中に上記状態点Q′(tw,tf)が領域
M2に移行すると、それに伴い(ホ)の補助除霜運転に
運転を切り換え、また同様に、(ホ)の補助除霜運転中
に上記状態点Q′(tw,tf)が領域M1に移行する
と、それに伴い(ニ)の主除霜運転に運転を切り換え
る。そして、除霜が完了すると(ニ)又は(ホ)の除霜
運転を自動的に終了し、その後、(イ)〜(ハ)の負荷
対応運転の選択実施に復帰する。As in the first embodiment, if the state point Q '(tw, tf) shifts to the area M2 during the execution of the main defrosting operation of (d), the auxiliary defrosting of (e) is accordingly performed. When the state point Q '(tw, tf) shifts to the area M1 during the auxiliary defrosting operation (e), the operation is switched to the main defrosting operation (d). Switch. Then, when the defrosting is completed, the defrosting operation of (d) or (e) is automatically terminated, and thereafter, the operation returns to the selection execution of the load corresponding operation of (a) to (c).
【0057】さらにまた、この制御器14′は、水Wか
らの採熱を伴う(ロ)又は(ハ)の負荷対応運転、ある
いは、(ニ)の主除霜運転では、センサS5′,S6′
の検出温度t1′,t2′に基づく冷媒側二方弁V6′
及び水側開閉弁V7′,V8′の切り換え操作により、
第1及び第2の対液熱交換器1A,1Bのうち冷媒R及
び水Wを器内通過させるもの(すなわち、熱交換器とし
て実機能させるもの)を、冷媒R及び水Wの通過状態に
ある対液熱交換器1A,1Bからの送出水温度t1′,
t2′が設定下限温度tx(水の凍結近傍温度)まで低
下するごとに自動的に交互切り換えする。Further, in the controller 14 'for the load corresponding operation (b) or (c) involving the heat collection from the water W or the main defrosting operation (d), the sensors S5' and S6 are used. ′
Refrigerant two-way valve V6 'based on the detected temperatures t1' and t2 '
And the switching operation of the water-side on-off valves V7 'and V8'
Of the first and second liquid heat exchangers 1A and 1B, the one that allows the refrigerant R and the water W to pass through the inside of the chamber (that is, the one that actually functions as a heat exchanger) is set to the state where the refrigerant R and the water W pass. Outgoing water temperature t1 'from a certain liquid heat exchanger 1A, 1B,
Each time t2 'falls to the set lower limit temperature tx (temperature near freezing of water), the switching is automatically performed.
【0058】図10において、tw1,tw2は水Wの
側について設定した凍結危険温度と凍結注意温度、tf
1,tf2は負荷側について設定した凍結危険温度と凍
結注意温度であり、上記除霜運転の自動選択では、第1
実施形態と同様、センサS1′,S4による水Wの検出
温度tw及び負荷側熱媒液Lfの検出温度tfが、とも
に凍結危険温度と凍結注意温度との間にある状況や、と
もに凍結注意温度以上にある状況のときには(ニ)の主
除霜運転を選択実施することで、(ニ)の主除霜運転と
(ホ)の補助除霜運転とのうち全体としては(ニ)の主
除霜運転の方を優先的に実施するようにしてある。In FIG. 10, tw1 and tw2 are the freezing dangerous temperature and the freezing caution temperature set for the water W side, and tf.
1 and tf2 are the freezing dangerous temperature and the freezing caution temperature set for the load side.
Similarly to the embodiment, the detection temperature tw of the water W and the detection temperature tf of the load side heat transfer fluid Lf detected by the sensors S1 'and S4 are both between the freezing dangerous temperature and the freezing caution temperature, and both are the freezing caution temperature. In the situation described above, the main defrosting operation of (d) is selected and executed, so that the main defrosting operation of (d) and the auxiliary defrosting operation of (e) are performed as a whole. The frost operation is preferentially performed.
【0059】また、本第2実施形態においても、第1実
施形態と同様、第1及び第2対液熱交換器1A,1Bの
上記交互使用において、休止側の対液熱交換器1A,1
Bに対する水Wの通過は完全には遮断せず、休止側の対
液熱交換器1A,1Bにも少量の水Wを通過させること
で、その休止側の対液熱交換器1A,1Bの温度回復を
促進するようにしてある。Also in the second embodiment, as in the first embodiment, in the alternate use of the first and second liquid heat exchangers 1A and 1B, the inactive liquid heat exchangers 1A and 1B are used.
The passage of the water W to B is not completely shut off, but a small amount of water W is also passed to the non-liquid heat exchangers 1A and 1B on the non-operating side, so that the non-liquid heat exchangers 1A and 1B on the non-operating side are cooled. It promotes temperature recovery.
【0060】以上、対液熱交換器1(1A,1B)で冷
媒Rと熱交換させる熱源側熱媒液に採熱源としての水W
を直接使用する本第2実施形態において、制御器14′
は、(イ)又は(ロ)の負荷対応運転の実施で対空気熱
交換器2に着霜した霜を除去する除霜運転の必要時に、
熱源側熱媒液としての水Wの温度tw及び負荷側熱媒液
Lfの温度tfに応じて(ニ)の主除霜運転と(ホ)の
補助除霜運転とを自動的に選択実施する除霜制御手段を
構成する。As described above, the water W as a heat source is added to the heat source side heat transfer fluid to be exchanged with the refrigerant R in the liquid heat exchanger 1 (1A, 1B).
In the second embodiment in which the controller 14 'is used directly, the controller 14'
When the defrosting operation for removing the frost formed on the air heat exchanger 2 in the execution of the load corresponding operation (a) or (b) is necessary,
The main defrosting operation (d) and the auxiliary defrosting operation (e) are automatically selected and executed according to the temperature tw of the water W as the heat source side heat medium liquid and the temperature tf of the load side heat medium liquid Lf. It constitutes a defrost control means.
【0061】また、この制御器14′は、対液熱交換器
1を冷媒蒸発器Eとして機能させ、かつ、対負荷熱交換
器3又は対空気熱交換器2を冷媒凝縮器Cとして機能さ
せる(ロ),(ハ),(ニ)の運転(液熱源運転)にお
いて、冷媒Rを水Wと熱交換させる複数の対液熱交換器
1A,1Bのうち冷媒Rを器内通過させるものを、冷媒
Rと水Wとの熱交換状態に応じて自動的に切り換える凍
結防止制御手段を構成する。The controller 14 'causes the liquid heat exchanger 1 to function as a refrigerant evaporator E, and causes the load heat exchanger 3 or the air heat exchanger 2 to function as a refrigerant condenser C. In the operations (b), (c), and (d) (liquid heat source operation), one of the plurality of liquid heat exchangers 1A and 1B for exchanging the refrigerant R with the water W, the refrigerant R passing through the inside of the heat exchangers. The anti-freezing control means automatically switches according to the heat exchange state between the refrigerant R and the water W.
【0062】なお、本第2実施形態の融雪設備でも、第
1実施形態の融雪設備と同様、上記(イ)〜(ホ)の運
転の他、必要に応じて前述の(へ)〜(チ)の運転を選
択実施でき、そして、これら(へ)〜(チ)の運転につ
いても、水Wからの採熱を伴うことに対し、制御器1
4′は、(ロ),(ハ),(ニ)の運転と同様、センサ
S5′,S6′の検出温度t1′,t2′に基づく前述
の如き第1及び第2対液熱交換器1A,1Bの自動交互
使用を行なう。In the snow melting equipment of the second embodiment, similarly to the snow melting equipment of the first embodiment, in addition to the above-mentioned operations (a) to (e), if necessary, the above-mentioned (f) to (h) are used. ) Operation can be selected and performed, and the operations of (h) to (h) also involve the controller 1
Reference numeral 4 'denotes the first and second liquid heat exchangers 1A based on the detected temperatures t1' and t2 'of the sensors S5' and S6 'as in (b), (c) and (d). , 1B.
【0063】〔別実施形態〕次に別実施形態を列記す
る。[Another Embodiment] Next, another embodiment will be described.
【0064】前述の第1実施形態では、採熱用熱交換器
8A,8Bに通過させる熱源側熱媒液Lbの検出温度t
bと、負荷装置としての融雪熱交換器11に通過させる
負荷側熱媒液Lfの検出温度tfとに基づき、主除霜運
転と補助除霜運転との自動選択を行なようにしたが、主
除霜運転と補助除霜運転との自動選択の判断に用いる熱
源側熱媒液Lbの温度は、採熱用熱交換器8A,8Bか
ら送出される熱源側熱媒液Lbの温度であってもよく、
また同様に、主除霜運転と補助除霜運転との自動選択の
判断に用いる負荷側熱媒液Lfの温度も、負荷装置から
送出される負荷側熱媒液Lfの温度であってもよい。In the first embodiment, the detected temperature t of the heat-source-side heat transfer fluid Lb passed through the heat-exchanger heat exchangers 8A and 8B.
b, the automatic selection between the main defrosting operation and the auxiliary defrosting operation is performed based on the detected temperature tf of the load-side heat medium liquid Lf passed through the snow melting heat exchanger 11 as a load device. The temperature of the heat-source-side heat medium liquid Lb used to determine the automatic selection between the main defrosting operation and the auxiliary defrosting operation is the temperature of the heat-source-side heat medium liquid Lb sent from the heat collecting heat exchangers 8A and 8B. May be
Similarly, the temperature of the load-side heat transfer fluid Lf used for determining the automatic selection between the main defrosting operation and the auxiliary defrosting operation may be the temperature of the load-side heat transfer liquid Lf sent from the load device. .
【0065】また、前述の第2実施形態では、対液熱交
換器1(1A,1B)に熱源側熱媒液として通過させる
水Wの検出温度twと、負荷装置としての融雪熱交換器
11に通過させる負荷側熱媒液Lfの検出温度tfとに
基づき、主除霜運転と補助除霜運転との自動選択を行な
ようにしたが、対液熱交換器1で冷媒Rと熱交換させる
熱源側熱媒液に水Wを使用する形態において、主除霜運
転と補助除霜運転との自動選択の判断に用いる水Wの温
度は、対液熱交換器1A,1Bから送出される水Wの温
度であってもよく、また同様に、主除霜運転と補助除霜
運転との自動選択の判断に用いる負荷側熱媒液Lfの温
度も、負荷装置から送出される負荷側熱媒液Lfの温度
であってもよい。In the second embodiment, the detected temperature tw of the water W passed through the liquid heat exchanger 1 (1A, 1B) as the heat source side heat transfer fluid, and the snow melting heat exchanger 11 as the load device Automatic selection between the main defrosting operation and the auxiliary defrosting operation is performed based on the detected temperature tf of the load-side heat transfer fluid Lf passed through the heat exchanger. In a mode in which water W is used as the heat-source-side heat transfer medium to be heated, the temperature of water W used to determine the automatic selection between the main defrosting operation and the auxiliary defrosting operation is sent from the liquid heat exchangers 1A and 1B. The temperature of the water W may be the same, and similarly, the temperature of the load-side heat transfer fluid Lf used to determine the automatic selection between the main defrosting operation and the auxiliary defrosting operation is also the load-side heat medium liquid Lf sent from the load device. The temperature of the medium Lf may be used.
【0066】熱源側熱媒液Lb,W(水Wを熱源側熱媒
液に直接使用する場合を含む)の温度と負荷側熱媒液L
fの温度とに基づく主除霜運転と補助除霜運転との自動
選択で用いる選択基準は、熱源側熱媒液Lb,Wの側で
の凍結トラブル、及び、負荷側での凍結トラブルを防止
する機能を生じるものであれば、具体的には、どのよう
な形態の選択基準であってもよい。The temperature of the heat-source-side heat transfer fluid Lb, W (including the case where water W is used directly as the heat-source-side heat transfer fluid) and the load-side heat transfer fluid L
The selection criterion used in the automatic selection between the main defrosting operation and the auxiliary defrosting operation based on the temperature of f prevents freezing trouble on the heat source side heat transfer fluids Lb and W and freezing trouble on the load side. Specifically, any type of selection criterion may be used as long as the selection function is provided.
【0067】また、前述の図8や図10に示す如き選択
基準D2,D2′を用いる場合、熱源側熱媒液Lb,W
の側について設定する凍結危険温度tb1,tw1や凍
結注意温度tb2,tw2、並びに、負荷側について設
定する凍結危険温度tf1や凍結注意温度tf2は、夫
々、使用する熱源側熱媒液Lb,Wや負荷側熱媒液Lf
の種類、あるいはまた、主除霜運転と補助除霜運転との
自動選択の判断に用いる熱源側熱媒液Lb,Wや負荷側
熱媒液Lfの温度の検出位置、さらにまた、採熱源種や
負荷装置の用途など、装置の設計条件に応じて、適当な
値を選定すればよい。When the selection criteria D2, D2 'as shown in FIGS. 8 and 10 are used, the heat source side heat transfer fluids Lb, W
The freezing dangerous temperatures tb1 and tw1 and the caution freezing temperatures tb2 and tw2 set for the side and the freezing dangerous temperature tf1 and the caution freezing temperature tf2 set for the load side are respectively used for the heat source side heat transfer fluids Lb and W, Load side heat transfer fluid Lf
Or the detection positions of the temperatures of the heat source side heat transfer fluids Lb and W and the load side heat transfer fluid Lf used to determine the automatic selection between the main defrosting operation and the auxiliary defrosting operation, and furthermore, the heat collection source type An appropriate value may be selected according to the design conditions of the device, such as the application of the load device and the like.
【0068】前述の第1実施形態では、第1及び第2の
採熱用熱交換器8A,8Bのうち熱源側熱媒液Lbを器
内通過させるものを、熱源側熱媒液Lbと水Wとの熱交
換状態に応じて自動的に切り換えるのに、熱源側熱媒液
Lb及び水Wの通過状態にある採熱用熱交換器8A,8
Bからの送出水温度t1,t2が設定下限温度txまで
低下するごとに切り換えを実施するようにしたが、2器
ないしそれ以上の複数の採熱用熱交換器のうち熱源側熱
媒液Lbを器内通過させるものの自動切り換えの判断に
用いる熱源側熱媒液Lbと水Wとの熱交換状態の具体的
な状態情報としては、種々のものを採用でき、例えば、
熱源側熱媒液Lb及び水Wの通過状態にある採熱用熱交
換器8A,8Bの器内通過後の熱源側熱媒液Lbと器内
通過後の水Wとの温度差が設定値よりも小さくなるごと
に切り換えを行なうようにしてもよい。In the first embodiment, one of the first and second heat-exchanging heat exchangers 8A and 8B that allows the heat-source-side heat transfer fluid Lb to pass through the inside of the heat-exchanger is replaced with the heat-source-side heat transfer fluid Lb and water. In order to automatically switch in accordance with the state of heat exchange with W, the heat-collecting heat exchangers 8A, 8 in a state in which the heat source side heat transfer fluid Lb and the water W pass.
The switching is performed each time the temperature t1, t2 of the water discharged from B decreases to the set lower limit temperature tx. However, the heat source side heat transfer fluid Lb of the two or more heat collecting heat exchangers is used. As the specific state information of the heat exchange state between the heat source side heat transfer fluid Lb and the water W used for the determination of the automatic switching of the one that passes through the inside of the vessel, various kinds of information can be adopted.
The temperature difference between the heat-source-side heat transfer liquid Lb after passing through the heat-collecting heat exchangers 8A and 8B and the water W after passing through the inside of the heat-collecting heat exchangers 8A and 8B in a state where the heat-source-side heat transfer liquid Lb and water W pass. The switching may be performed every time it becomes smaller.
【0069】また、前述の第2実施形態では、第1及び
第2の対液熱交換器1A,1Bのうち冷媒Rを器内通過
させるものを、冷媒Rと水Wとの熱交換状態に応じて自
動的に切り換えるのに、冷媒R及び水Wの通過状態にあ
る対液熱交換器1A,1Bからの送出水温度t1′,t
2′が設定下限温度txまで低下するごとに切り換えを
実施するようにしたが、対液熱交換器1A,1Bで冷媒
Rと熱交換させる熱源側熱媒液に水Wを使用する場合に
おいても同様に、2器ないしそれ以上の複数の対液熱交
換器のうち冷媒Rを器内通過させるものの自動切り換え
の判断に用いる冷媒Rと水Wとの熱交換状態の具体的な
状態情報としては、種々のものを採用でき、冷媒R及び
水Wの通過状態にある対液熱交換器1A,1Bの器内通
過後の冷媒Rと器内通過後の水Wとの温度差が設定値よ
りも小さくなるごとに切り換えを行なうようにしてもよ
い。In the above-described second embodiment, one of the first and second liquid-to-liquid heat exchangers 1A and 1B that allows the refrigerant R to pass through the inside of the heat exchanger 1A and 1B is set in a heat exchange state between the refrigerant R and the water W. Automatically switched according to the temperature T1 ′, t1 of the water sent from the liquid heat exchangers 1A, 1B in the passing state of the refrigerant R and the water W.
The switching is performed every time 2 ′ falls to the set lower limit temperature tx. However, even in the case where water W is used as the heat source side heat transfer fluid for exchanging heat with the refrigerant R in the liquid heat exchangers 1A and 1B. Similarly, specific state information of the heat exchange state between the refrigerant R and the water W used for the determination of automatic switching of the two or more plural liquid heat exchangers that pass the refrigerant R inside the liquid heat exchanger is as follows. The temperature difference between the refrigerant R after passing through the inside of the liquid heat exchangers 1A and 1B and the water W after passing through the inside of the liquid heat exchangers 1A and 1B in a state where the refrigerant R and water W pass is larger than the set value. The switching may be performed each time is smaller.
【0070】さらに、このように採熱用熱交換器8A,
8Bの切り換えを熱源側熱媒液Lbと水Wとの熱交換状
態に応じて行なったり、対液熱交換器1A,1Bの切り
換えを冷媒Rと水Wとの熱交換状態に応じて行なうに代
え、これら採熱用熱交換器の切り換えや対液熱交換器の
切り換えを設定時間毎に行なうようにしてもよい。Further, as described above, the heat collecting heat exchanger 8A,
8B is switched according to the heat exchange state between the heat source side heat transfer fluid Lb and the water W, or the liquid heat exchangers 1A and 1B are switched according to the heat exchange state between the refrigerant R and the water W. Alternatively, the switching of the heat exchanger for heat collection and the switching of the liquid heat exchanger may be performed at set time intervals.
【0071】そしてまた、請求項1に係る発明の実施に
あたり、場合によっては、上記の如き採熱用熱交換器の
自動切り換えや対液熱交換器の自動切り換えを行なわな
い形態を採ってもよい。Further, in implementing the invention according to claim 1, depending on the case, a mode may be adopted in which the automatic switching of the heat exchanger for heat collection and the automatic switching of the liquid heat exchanger are not performed as described above. .
【0072】負荷側熱媒液Lfには熱源側熱媒液Lb,
Wと同様、ブラインや水など、種々の液体を使用でき、
また、対負荷熱交換器3での発生温熱の用途は、前述の
如き融雪に限られるものではなく、凍結防止や暖房ある
いは物品加熱など、どのようなものであってもよい。The load-side heat transfer fluid Lf includes a heat-source-side heat transfer fluid Lb,
Like W, various liquids such as brine and water can be used,
Further, the application of the generated heat in the anti-load heat exchanger 3 is not limited to snow melting as described above, but may be any application such as prevention of freezing, heating or heating of articles.
【図1】第1実施形態を示す設備構成図FIG. 1 is a configuration diagram showing a first embodiment.
【図2】空気熱源の負荷対応運転における冷媒の流れを
示す図FIG. 2 is a diagram showing a flow of a refrigerant in a load operation of an air heat source.
【図3】2熱源の負荷対応運転における冷媒の流れを示
す図FIG. 3 is a diagram illustrating a flow of a refrigerant in a load corresponding operation of two heat sources.
【図4】水熱源の負荷対応運転における冷媒の流れを示
す図FIG. 4 is a diagram showing a flow of a refrigerant in a load operation of a water heat source.
【図5】主除霜運転における冷媒の流れを示す図FIG. 5 is a diagram showing a flow of a refrigerant in a main defrosting operation.
【図6】補助除霜運転における冷媒の流れを示す図FIG. 6 is a diagram showing a flow of a refrigerant in an auxiliary defrosting operation.
【図7】負荷対応運転の選択基準を示す図FIG. 7 is a diagram showing selection criteria for load-adaptive operation.
【図8】第1実施形態での除霜運転の選択基準を示す図FIG. 8 is a diagram showing selection criteria for a defrosting operation in the first embodiment.
【図9】第2実施形態を示す設備構成図FIG. 9 is a diagram illustrating a configuration of a second embodiment.
【図10】第2実施形態での除霜運転の選択基準を示す
図FIG. 10 is a diagram showing selection criteria for a defrosting operation in the second embodiment.
1,1A,1B 対液熱交換器 2 対空気熱交換器 3 対負荷熱交換器 8A,8B 採熱用熱交換器 14,14′ 除霜制御手段,凍結防止制御手段 A 空気 C 冷媒凝縮器 E 冷媒蒸発器 Lb 熱源側熱媒液 Lf 負荷側熱媒液 R 冷媒 tb,tw 熱源側熱媒液の温度 tf 負荷側熱媒液の温度 W 水,熱源側熱媒液 1, 1A, 1B Heat exchanger for liquid 2 Heat exchanger for air 3 Heat exchanger for load 8A, 8B Heat exchanger for heat collection 14, 14 'Defrosting control means, antifreezing control means A Air C refrigerant condenser E Refrigerant evaporator Lb Heat source side heat medium liquid Lf Load side heat medium liquid R Refrigerant tb, tw Heat source side heat medium liquid temperature tf Load side heat medium liquid temperature W Water, heat source side heat medium liquid
Claims (3)
交換器と、冷媒を熱源側熱媒液と熱交換させる対液熱交
換器と、冷媒を負荷側熱媒液と熱交換させる対負荷熱交
換器とを設け、 前記対空気熱交換器を冷媒蒸発器として機能させ、か
つ、前記対負荷熱交換器を冷媒凝縮器として機能させる
負荷対応運転と、 前記対液熱交換器を冷媒蒸発器として機能させ、かつ、
前記対空気熱交換器を冷媒凝縮器として機能させる主除
霜運転と、 前記対負荷熱交換器を冷媒蒸発器として機能させ、か
つ、前記対空気熱交換器を冷媒凝縮器として機能させる
補助除霜運転との切り換えを可能にし、 前記負荷対応運転の実施で前記対空気熱交換器に着霜し
た霜を除去する除霜運転の必要時に、前記熱源側熱媒液
の温度及び前記負荷側熱媒液の温度に応じて前記主除霜
運転と前記補助除霜運転とを自動的に選択実施する除霜
制御手段を設けてあるヒートポンプ装置。An air heat exchanger for exchanging heat between a refrigerant and atmospheric air, a liquid heat exchanger for exchanging heat between a refrigerant and a heat source liquid, and a pair for exchanging heat between the refrigerant and a load heat liquid. A load heat exchanger, wherein the air-to-air heat exchanger functions as a refrigerant evaporator, and the load-to-load heat exchanger functions as a refrigerant condenser. Function as an evaporator, and
A main defrosting operation in which the air heat exchanger functions as a refrigerant condenser; and an auxiliary defrosting function in which the load heat exchanger functions as a refrigerant evaporator, and the air heat exchanger functions as a refrigerant condenser. When the defrosting operation for removing the frost formed on the air heat exchanger by performing the load corresponding operation is necessary, the temperature of the heat source side heat transfer fluid and the load side heat can be switched. A heat pump device provided with defrost control means for automatically selecting and executing the main defrost operation and the auxiliary defrost operation according to the temperature of the medium.
数の採熱用熱交換器を設け、 前記対液熱交換器を冷媒蒸発器として機能させ、かつ、
前記対負荷熱交換器又は前記対空気熱交換器を冷媒凝縮
器として機能させる液熱源運転において、複数の前記採
熱用熱交換器のうち前記熱源側熱媒液を器内通過させる
ものを、前記熱源側熱媒液と水との熱交換状態に応じ
て、又は、設定時間毎に自動的に切り換える凍結防止制
御手段を設けてある請求項1記載のヒートポンプ装置。2. A plurality of heat collecting heat exchangers for exchanging the heat source side heat transfer medium with water, wherein the liquid heat exchanger functions as a refrigerant evaporator, and
In the liquid heat source operation in which the heat-to-load heat exchanger or the air-to-air heat exchanger functions as a refrigerant condenser, one of the plurality of heat-collecting heat exchangers that allows the heat-source-side heat transfer medium to pass therethrough, The heat pump device according to claim 1, further comprising a freeze prevention control unit that automatically switches according to a heat exchange state between the heat source side heat transfer fluid and water or at set time intervals.
に、前記対液熱交換器を複数設け、 前記対液熱交換器を冷媒蒸発器として機能させ、かつ、
前記対負荷熱交換器又は前記対空気熱交換器を冷媒凝縮
器として機能させる液熱源運転において、複数の前記対
液熱交換器のうち冷媒を器内通過させるものを、冷媒と
水との熱交換状態に応じて、又は、設定時間毎に自動的
に切り換える凍結防止制御手段を設けてある請求項1記
載のヒートポンプ装置。3. Using water as the heat source side heat transfer fluid, providing a plurality of the liquid heat exchangers, making the liquid heat exchanger function as a refrigerant evaporator, and
In the liquid heat source operation in which the load-to-load heat exchanger or the air-to-air heat exchanger functions as a refrigerant condenser, one of the plurality of liquid-to-liquid heat exchangers that allows the refrigerant to pass through the inside of the heat exchanger is used for heat transfer between the refrigerant and water. 2. The heat pump device according to claim 1, further comprising a freeze prevention control unit that automatically switches according to a replacement state or at set time intervals.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000257392A JP2002071245A (en) | 2000-08-28 | 2000-08-28 | Heat pump equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000257392A JP2002071245A (en) | 2000-08-28 | 2000-08-28 | Heat pump equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2002071245A true JP2002071245A (en) | 2002-03-08 |
Family
ID=18745856
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000257392A Pending JP2002071245A (en) | 2000-08-28 | 2000-08-28 | Heat pump equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2002071245A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006250438A (en) * | 2005-03-10 | 2006-09-21 | Yanmar Co Ltd | Engine driven heat pump |
| WO2008111149A1 (en) | 2007-03-12 | 2008-09-18 | Hoshizaki Denki Kabushiki Kaisha | Cooling storage building |
| WO2014091548A1 (en) * | 2012-12-11 | 2014-06-19 | 三菱電機株式会社 | Air conditioning hot water supply composite system |
-
2000
- 2000-08-28 JP JP2000257392A patent/JP2002071245A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006250438A (en) * | 2005-03-10 | 2006-09-21 | Yanmar Co Ltd | Engine driven heat pump |
| WO2008111149A1 (en) | 2007-03-12 | 2008-09-18 | Hoshizaki Denki Kabushiki Kaisha | Cooling storage building |
| US8365543B2 (en) | 2007-03-12 | 2013-02-05 | Hoshizaki Denki Kabushiki Kaisha | Cooling storage |
| WO2014091548A1 (en) * | 2012-12-11 | 2014-06-19 | 三菱電機株式会社 | Air conditioning hot water supply composite system |
| CN104813121A (en) * | 2012-12-11 | 2015-07-29 | 三菱电机株式会社 | Air conditioner hot water supply composite system |
| CN104813121B (en) * | 2012-12-11 | 2016-08-24 | 三菱电机株式会社 | Air-conditioning and water-heating complex system |
| JP5984965B2 (en) * | 2012-12-11 | 2016-09-06 | 三菱電機株式会社 | Air conditioning and hot water supply complex system |
| US9631826B2 (en) | 2012-12-11 | 2017-04-25 | Mistubishi Electric Corporation | Combined air-conditioning and hot-water supply system |
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