JP2002340440A - Heat pump hot-water supplier - Google Patents

Heat pump hot-water supplier

Info

Publication number
JP2002340440A
JP2002340440A JP2001149072A JP2001149072A JP2002340440A JP 2002340440 A JP2002340440 A JP 2002340440A JP 2001149072 A JP2001149072 A JP 2001149072A JP 2001149072 A JP2001149072 A JP 2001149072A JP 2002340440 A JP2002340440 A JP 2002340440A
Authority
JP
Japan
Prior art keywords
water
temperature
hot water
reducing device
boiling
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.)
Pending
Application number
JP2001149072A
Other languages
Japanese (ja)
Inventor
Masahiro Ohama
昌宏 尾浜
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP2001149072A priority Critical patent/JP2002340440A/en
Publication of JP2002340440A publication Critical patent/JP2002340440A/en
Pending legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To provide a hot water storage type heat pump hot-water supplier that is improved in operational efficiency and is contrived to effectively utilize the hot-water capacity of a hot-water storage tank. SOLUTION: This heat pump hot-water supplier is provided with a flow rate control means 10 which controls a flow regulating valve 11 for fixing a boiling temperature which is the temperature of water at the water-side outlet of a refrigerant-water heat exchanger 2, a detecting means 13 which detects the completion of the boiling of all hot water stored in the hot-water storage tank 5 just before the completion, and a control means 12 which changes the valve travel of the valve of a pressure reducing device 3 when the signal from the detecting means 13 becomes a prescribed one. Since the valve travel of the valve of the pressure reducing device 3 is changed when the boiling of the hot water is near completion and the discharge pressure of a compressor 1 rises, this hot-water supplier can be operated for heating hot water to a high feed water temperature. Consequently, the supplier can effectively utilize the hot-water capacity of the tank 5 and, in addition, can be operated highly efficiently for heating hot water.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は貯湯式のヒートポン
プ給湯機に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hot water supply type heat pump water heater.

【0002】[0002]

【従来の技術】従来のこの種のヒートポンプ給湯機は特
開昭60−164157号公報に示すようなものがあ
る。図22は従来のヒートポンプ給湯機の構成図であ
る。図22において、圧縮機1、冷媒対水熱交換器2、
減圧装置3、蒸発器4からなる冷媒循環回路と、貯湯槽
5、循環ポンプ6、前記冷媒対水熱交換器2、補助加熱
器7を接続した給湯回路ならなり、前記圧縮機1より吐
出された高温高圧の過熱ガス冷媒は前記冷媒対水熱交換
器2に流入し、ここで前記循環ポンプ6から送られてき
た水を加熱する。そして、凝縮液化した冷媒は前記減圧
装置3で減圧され、前記蒸発器4に流入し、ここで大気
熱を吸熱して蒸発ガス化し、前記圧縮機1に戻る。一
方、前記冷媒対水熱交換器2で加熱された湯は前記貯湯
槽5の上部に流入し、上から次第に貯湯されていく。そ
して、前記冷媒対水熱交換器2の入口水温が設定値に達
すると給水温度検出手段8が検知し、前記圧縮機1によ
るヒートポンプ運転を停止して、前記補助加熱器7の単
独運転に切り換えるものである。
2. Description of the Related Art A conventional heat pump water heater of this kind is disclosed in Japanese Patent Application Laid-Open No. 60-164157. FIG. 22 is a configuration diagram of a conventional heat pump water heater. In FIG. 22, a compressor 1, a refrigerant-to-water heat exchanger 2,
A refrigerant circulation circuit including a decompression device 3 and an evaporator 4 and a hot water supply circuit connecting a hot water storage tank 5, a circulation pump 6, the refrigerant-to-water heat exchanger 2, and an auxiliary heater 7 are discharged from the compressor 1. The high-temperature, high-pressure superheated gas refrigerant flows into the refrigerant-to-water heat exchanger 2, where it heats the water sent from the circulation pump 6. Then, the condensed and liquefied refrigerant is decompressed by the decompression device 3 and flows into the evaporator 4 where it absorbs atmospheric heat to evaporate and return to the compressor 1. On the other hand, the hot water heated by the refrigerant / water heat exchanger 2 flows into the upper portion of the hot water storage tank 5 and is gradually stored from above. Then, when the inlet water temperature of the refrigerant-to-water heat exchanger 2 reaches a set value, the feedwater temperature detecting means 8 detects it, stops the heat pump operation by the compressor 1 and switches to the independent operation of the auxiliary heater 7. Things.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
ような従来例の構成では、沸き上げ運転時間の経過とと
もに貯湯槽5内の湯と水の接する部分で湯水混合層が生
じ、その層は次第に拡大していく。図23は貯湯槽5内
の湯の温度分布を示す。同図中において、T1は沸き上
げ温度(高温湯)であり、T2は市水温度(低温湯)で
ある。前述の湯水混合層は、高温湯と低温湯の熱伝導お
よび対流により発生するものであり、高温湯から低温湯
へ伝熱されその境界部分で高温湯は温度低下し、逆に低
温湯は温度上昇する。従って、貯湯槽5の沸き上げ完了
近くになると、前記冷媒対水熱交換器2に流入する給水
温度は高くなるため、前記圧縮機1の吐出圧力は上昇し
て、モータの巻線温度の上昇など圧縮機1の耐久性が課
題となってくる。
However, in the above-described configuration of the prior art, as the boiling operation time elapses, a hot-water mixed layer is formed at a portion where hot water and water in the hot-water storage tank 5 come into contact with each other, and the layer is gradually formed. Expand. FIG. 23 shows a temperature distribution of hot water in hot water storage tank 5. In the figure, T1 is the boiling temperature (high-temperature hot water), and T2 is the city water temperature (low-temperature hot water). The above-mentioned hot-water mixture layer is generated by heat conduction and convection between the high-temperature hot water and the low-temperature hot water, and is transferred from the high-temperature hot water to the low-temperature hot water. To rise. Therefore, when the boiling of the hot water storage tank 5 is nearly completed, the temperature of the feedwater flowing into the refrigerant-to-water heat exchanger 2 increases, so that the discharge pressure of the compressor 1 increases and the winding temperature of the motor increases. For example, durability of the compressor 1 becomes an issue.

【0004】図24は横軸に前記冷媒対水熱交換器2に
流入する給水温度をとり、縦軸にその時の圧縮機1の吐
出圧力をとって、給水温度に対する圧縮機1の吐出圧力
の関係を示したグラフである。同図中の圧力Pは常用上
限圧力であり、圧縮機1の耐久性を保証するためには、
通常運転ではこの圧力以下で運転する必要がある。圧力
Pの時の給水温度は同図中よりT3となる。また、有効
な湯温の下限をTu(例えば45℃)とし、前述のT3
とTuを図23に示す。同図の左側に示す貯湯槽5の断
面図において、湯温T3以下の領域は沸き上げ可能な領
域であり、Tu以上の領域は有効な湯として使用できる
領域である。しかし、湯温T3とTuの間の領域(斜線
の部分)は有効な湯として利用できない領域である。
In FIG. 24, the horizontal axis indicates the feed water temperature flowing into the refrigerant-to-water heat exchanger 2, and the vertical axis indicates the discharge pressure of the compressor 1 at that time. It is a graph showing the relationship. The pressure P in the figure is a normal upper limit pressure, and in order to guarantee the durability of the compressor 1,
In normal operation, it is necessary to operate at or below this pressure. The supply water temperature at the time of the pressure P is T3 from the figure. Further, the lower limit of the effective hot water temperature is Tu (for example, 45 ° C.), and the above-mentioned T3
And Tu are shown in FIG. In the cross-sectional view of the hot water storage tank 5 shown on the left side of the figure, a region below the hot water temperature T3 is a region that can be boiled, and a region above Tu is a region that can be used as effective hot water. However, the area between the hot water temperatures T3 and Tu (shaded area) is an area that cannot be used as effective hot water.

【0005】このように従来例の構成では、前記冷媒対
水熱交換器2に流れる水温が低い状態で運転を停止せざ
るをえないので、前記貯湯槽5の下部が低温の水の状態
で停止することになり、前記貯湯槽5の湯容量を有効に
利用できない。そのため、貯湯熱量は減少し、給湯負荷
を満足することができない。これを解決する方法の一つ
として、貯湯槽5の容量を大きくすることが考えられ
る。しかし、この場合には、貯湯槽5の設置面積が大き
くなり、設置の自由度が制限され、かつ、コストが高く
なるという課題がある。また、他の方法として、ヒート
ポンプ運転を停止した後、補助加熱器7の単独運転で貯
湯熱量を増加する方法がある。しかし、この場合には、
ヒータなどで加熱するため、消費電力が大きくなり、効
率が悪くなるという課題がある。
As described above, in the conventional configuration, the operation must be stopped in a state where the water temperature flowing through the refrigerant-to-water heat exchanger 2 is low, so that the lower part of the hot water storage tank 5 is in a state of low-temperature water. As a result, the hot water capacity of the hot water storage tank 5 cannot be used effectively. Therefore, the amount of hot water stored decreases, and the hot water supply load cannot be satisfied. As one method for solving this, it is conceivable to increase the capacity of the hot water storage tank 5. However, in this case, there is a problem that the installation area of the hot water tank 5 is increased, the degree of freedom of installation is limited, and the cost is increased. Further, as another method, there is a method of increasing the amount of stored hot water by operating the auxiliary heater 7 alone after stopping the heat pump operation. But in this case,
Since heating is performed by a heater or the like, there is a problem that power consumption is increased and efficiency is deteriorated.

【0006】本発明は、上記従来の課題を解決するもの
で、圧縮機の異常温度上昇ならびに異常圧力上昇もな
く、低消費電力量で貯湯槽の下部まで高温湯を貯湯し、
湯容量を有効に利用可能としたヒートポンプ給湯機の提
供を目的とする。
The present invention solves the above-mentioned conventional problems, and stores high-temperature hot water up to the lower portion of a hot water storage tank with low power consumption without an abnormal rise in temperature and abnormal pressure of a compressor.
It is an object of the present invention to provide a heat pump water heater capable of effectively utilizing a hot water capacity.

【0007】[0007]

【課題を解決するための手段】前記従来の課題を解決す
るために、本発明のヒートポンプ給湯機は、貯湯槽全体
が沸き上がる直前を検出する沸き上げ完了直前検出手段
と、沸き上げ完了に近づいたことを検出したときに、減
圧装置の弁開度を開くように制御する制御手段とを設け
たものである。だから、沸き上げ完了に近づき、圧縮機
の吐出圧力が上昇する場合に、減圧装置の弁開度を開く
ように制御し、吐出圧力を低く押さえるので、高温の給
水温度まで給湯加熱運転が可能となるものである。
In order to solve the above-mentioned conventional problems, a heat pump water heater according to the present invention has a means for detecting immediately before the completion of boiling of the entire hot water storage tank, and a means for immediately before the completion of boiling. And control means for controlling so as to open the valve opening of the pressure reducing device when it is detected. Therefore, when the discharge pressure of the compressor nears the completion of boiling and the discharge pressure of the compressor rises, the valve opening of the pressure reducing device is controlled to open, and the discharge pressure is kept low, so that hot water supply heating operation can be performed up to a high supply water temperature. It becomes.

【0008】[0008]

【発明の実施の形態】請求項1に記載の発明は、圧縮
機、冷媒対水熱交換器、減圧装置、蒸発器を順次接続し
た冷媒循環回路と、貯湯槽、循環ポンプ、前記冷媒対水
熱交換器を順次接続した給湯回路と、貯湯槽全体が沸き
上がる直前を検出する沸き上げ完了直前検出手段と、前
記沸き上げ完了直前検出手段からの信号が所定の信号に
なった時に、前記減圧装置の弁開度を変更する制御手段
とを備えたことにより、沸き上げ完了に近づき、圧縮機
の吐出圧力が上昇する場合に、減圧装置の弁開度を開く
ように制御し、吐出圧力を低く押さえ、高温の給水温度
まで給湯加熱運転が可能となり、貯湯槽の湯容量を有効
に利用できるものである。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The invention according to claim 1 is a refrigerant circulation circuit in which a compressor, a refrigerant-to-water heat exchanger, a decompression device, and an evaporator are sequentially connected, a hot water tank, a circulation pump, and the refrigerant-to-water. A hot water supply circuit to which a heat exchanger is sequentially connected; a heating completion detecting means for detecting immediately before the whole hot water tank is heated; and a pressure reducing device when a signal from the heating completion detecting means becomes a predetermined signal. Control means for changing the valve opening of the compressor, when the boiling is approaching completion and the discharge pressure of the compressor rises, the valve opening of the pressure reducing device is controlled to be opened, and the discharge pressure is lowered. The hot water supply heating operation can be performed up to the holding water temperature and the high supply water temperature, and the hot water capacity of the hot water storage tank can be effectively used.

【0009】請求項2に記載の発明は、減圧装置の弁開
度の変更幅は外気温度を検出する外気温度検出手段から
得た外気温度に応じて決定する制御手段を備えたことに
より、外気温度に応じた最適な減圧装置の弁開度の変更
を行うので、貯湯槽の湯容量を有効に利用でき、かつ、
効率の良い給湯加熱運転ができるものである。
According to a second aspect of the present invention, there is provided a control device for determining the change width of the valve opening of the pressure reducing device in accordance with the outside air temperature obtained from the outside air temperature detecting means for detecting the outside air temperature. Since the valve opening of the decompression device is changed optimally according to the temperature, the hot water capacity of the hot water tank can be used effectively, and
An efficient hot water supply heating operation can be performed.

【0010】請求項3に記載の発明は、予め決められた
複数の給水温度毎に前記減圧装置の弁開度の変更を行う
制御手段を備えたことにより、給水温度に応じた最適な
減圧装置の弁開度の変更を行うので、有効な湯として利
用できない無駄な領域がより少なくなるため、貯湯槽の
湯容量を有効に利用でき、かつ、効率の良い給湯加熱運
転ができるものである。
According to a third aspect of the present invention, an optimal pressure reducing device according to the water supply temperature is provided by providing control means for changing a valve opening of the pressure reducing device for each of a plurality of predetermined water temperatures. Since the valve opening degree is changed, the wasteful area that cannot be used as effective hot water is reduced, so that the hot water capacity of the hot water storage tank can be effectively used, and an efficient hot water supply heating operation can be performed.

【0011】請求項4に記載の発明は、給水温度が高い
ほど減圧装置の弁開度の変更量を大きくした制御手段を
備えたことにより、吐出圧力の上昇が大きい高給水温度
時に減圧装置の弁開度の変更量を大きくして吐出圧力を
大きく低下させ、給水温度に応じた最適な減圧装置の弁
開度の変更を行うので、貯湯槽の湯容量を有効に利用で
き、かつ、効率の良い給湯加熱運転ができるものであ
る。
According to a fourth aspect of the present invention, there is provided a control means for increasing the amount of change in the valve opening of the pressure reducing device as the temperature of the water supply increases, so that the pressure reducing device is operated at a high temperature of the water supply where the rise in discharge pressure is large. Since the discharge pressure is greatly reduced by increasing the amount of change in the valve opening and the valve opening of the decompression device is optimally changed according to the supply water temperature, the hot water capacity of the hot water storage tank can be used effectively and the efficiency can be improved. A good hot water supply heating operation is possible.

【0012】請求項5に記載の発明は、予め設定された
時間間隔ごとに減圧装置の弁開度の変更を行う制御手段
を備えたことにより、沸き上げ完了直前時に最適な減圧
装置の弁開度の変更を行うので、貯湯槽の湯容量を有効
に利用でき、かつ、効率の良い給湯加熱運転ができるも
のである。
According to a fifth aspect of the present invention, the control means for changing the valve opening of the pressure reducing device at predetermined time intervals is provided, so that the valve opening of the pressure reducing device is optimized just before the completion of boiling. Since the degree is changed, the hot water capacity of the hot water storage tank can be effectively used, and an efficient hot water supply heating operation can be performed.

【0013】請求項6に記載の発明は、減圧装置の弁開
度の変更を行う時間間隔を沸き上げ完了に近づくほど小
さくした制御手段を備えたことにより、沸き上げ完了に
近づくほど吐出圧力の上昇が大きい時に減圧装置の弁開
度の変更を多くして吐出圧力を大きく低下させ、最適な
減圧装置の弁開度の変更を行うので、貯湯槽の湯容量を
有効に利用でき、かつ、効率の良い給湯加熱運転ができ
るものである。
According to a sixth aspect of the present invention, there is provided control means for shortening the time interval for changing the valve opening of the pressure reducing device as the boiling is completed, so that the discharge pressure is reduced as the boiling is completed. When the rise is large, the change in the valve opening of the decompression device is increased to greatly reduce the discharge pressure, and the optimum valve opening of the decompression device is changed, so that the hot water capacity of the hot water storage tank can be used effectively, and An efficient hot water supply heating operation can be performed.

【0014】請求項7に記載の発明は、沸き上げ完了直
前検出手段として、流量調整弁を通過する流量が最大流
量になった時に、最大流量になっている時間を計測する
時間計測手段を備えたことにより、沸き上げ流量が、所
定の時間の間、最大になったことを検出して減圧装置の
弁開度の変更を行い、吐出圧力を低く押さえ、加熱運転
を続けるので、高温の給水温度まで給湯加熱運転が可能
となり、貯湯槽の湯容量を有効に利用できるものであ
る。
According to a seventh aspect of the present invention, as the detecting means immediately before the completion of the boiling, the time measuring means for measuring the time of the maximum flow rate when the flow rate passing through the flow regulating valve reaches the maximum flow rate is provided. As a result, it is detected that the boiling flow rate has reached a maximum for a predetermined time, the valve opening of the pressure reducing device is changed, the discharge pressure is kept low, and the heating operation is continued. The hot water supply heating operation can be performed up to the temperature, and the hot water capacity of the hot water storage tank can be used effectively.

【0015】請求項8に記載の発明は、沸き上げ完了直
前検出手段として吐出圧力検出手段を用い、設定された
基準圧力になれば、減圧装置の弁開度を開くように制御
する制御手段を備えたことにより、貯湯槽の湯容量を有
効に利用でき、かつ、直接圧力で制御するので、圧縮機
のより確実な耐久性の向上になるものである。
The invention according to claim 8 uses a discharge pressure detecting means as a means for detecting immediately before the completion of boiling, and a control means for controlling the valve opening of the pressure reducing device to be opened when the set reference pressure is reached. With this arrangement, the hot water capacity of the hot water storage tank can be effectively used, and the pressure is directly controlled, so that the durability of the compressor can be more reliably improved.

【0016】請求項9に記載の発明は、沸き上げ完了直
前検出手段として貯湯槽の下部温度検出する貯湯槽温度
検出手段を用い、所定の貯湯槽温度になれば、減圧装置
の弁開度を開くように制御する制御手段を備えたことに
より、貯湯槽の湯容量を有効に利用でき、かつ、直接貯
湯槽の温度を検出して制御するので、圧縮機のより確実
な耐久性の向上になるものである。
According to a ninth aspect of the present invention, a hot water tank temperature detecting means for detecting a lower temperature of the hot water tank is used as a means for detecting immediately before completion of boiling, and when a predetermined hot water tank temperature is reached, the valve opening of the pressure reducing device is increased. By providing a control means to control the opening, the hot water capacity of the hot water tank can be used effectively, and the temperature of the hot water tank is directly detected and controlled. It becomes.

【0017】[0017]

【実施例】以下、本発明の実施例について、図面を参照
しながら説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0018】(実施例1)図1は本発明の実施例1のヒ
ートポンプ給湯機の構成図、図2は同ヒートポンプ給湯
機の運転時間に対する圧縮機の運転状態と減圧装置の弁
開度と吐出圧力と給水温度とを示すグラフ、図3は同ヒ
ートポンプ給湯機の貯湯槽の温度分布を示す説明図であ
る。なお、従来例で説明した図22と同じ構成部材には
同一符号を用い説明を省略する。
(Embodiment 1) FIG. 1 is a block diagram of a heat pump water heater according to Embodiment 1 of the present invention, and FIG. 2 is an operating state of a compressor with respect to an operation time of the heat pump water heater, a valve opening degree and discharge of a pressure reducing device. FIG. 3 is a graph showing pressure and water supply temperature, and FIG. 3 is an explanatory diagram showing a temperature distribution of a hot water tank of the heat pump water heater. Note that the same reference numerals are used for the same components as those in FIG.

【0019】図1において、冷媒対水熱交換器2の水側
出口に設けられた沸き上げ温度検出手段9からの信号で
流量制御手段10は流量調整弁11の開度を制御して、
冷媒対水熱交換器2の出口水温(沸き上げ温度)をほぼ
一定になるように沸き上げる。また、制御手段12は、
沸き上げ完了の直前を検出する沸き上げ完了直前検出手
段13からの信号で、減圧装置3の弁開度を制御するも
のである。前記流量調整弁11としては、ステッピング
モータで駆動する電動バルブなどがある。
In FIG. 1, a flow rate control means 10 controls an opening degree of a flow rate control valve 11 by a signal from a boiling temperature detection means 9 provided at a water side outlet of the refrigerant-to-water heat exchanger 2.
The outlet water temperature (boiling temperature) of the refrigerant-to-water heat exchanger 2 is raised to be substantially constant. Further, the control means 12
The opening degree of the pressure reducing device 3 is controlled by a signal from the detection unit 13 immediately before the completion of the boiling, which detects immediately before the completion of the boiling. Examples of the flow control valve 11 include an electric valve driven by a stepping motor.

【0020】なお、沸き上げ完了直前検出手段13とし
て、ここでは一例として、冷媒対水熱交換器2の水側入
口水温である給水温度を検出する給水温度検出手段8を
用いる。また、減圧装置3として電動膨張弁(図示せ
ず)等がある。
As the means 13 for detecting immediately before the completion of boiling, for example, a feedwater temperature detecting means 8 for detecting a feedwater temperature which is a water-side inlet water temperature of the refrigerant-to-water heat exchanger 2 is used. The pressure reducing device 3 includes an electric expansion valve (not shown) and the like.

【0021】次に動作、作用について説明する。図2は
横軸に運転時間をとり、縦軸に圧縮機の運転状態と減圧
装置の弁開度と吐出圧力と給水温度とをとって、運転時
間に対する圧縮機の運転状態と減圧装置の弁開度と吐出
圧力と給水温度との関係を示したものである。従来例で
説明したように、貯湯槽5の沸き上げ完了近くになる
と、冷媒対水熱交換器2に流入する給水温度は高くな
る。つまり、冷媒対水熱交換器2に流入する水が前述し
た湯水混合層の部分になると、同図に示すように、運転
時間とともに給水温度が上昇する。そして、沸き上げ完
了直前検出手段13である給水温度検出手段8が(沸き
上げ温度T1よりも低い温度である)沸き上げ完了直前
検出温度Thを検出すると、制御手段12は、減圧装置
3の弁開度を大きくする(開く)。この時、吐出圧力は
P1からP2に減少する。その後、運転時間の経過とと
もに給水温度が更に上昇し、それに従って吐出圧力が上
昇する。そして、給水温度検出手段8が、常用上限圧力
Pになる給水温度T3aを検出すると、圧縮機を停止
し、加熱運転を終了する。なお、同図中の太い点線は、
減圧装置3の弁開度の制御を行わない従来例の場合であ
る。運転限界の給水温度がT3からT3aへと高くな
り、運転範囲が大きくなることがわかる。
Next, the operation and operation will be described. In FIG. 2, the horizontal axis indicates the operating time, and the vertical axis indicates the operating state of the compressor, the valve opening degree of the pressure reducing device, the discharge pressure, and the feedwater temperature. It shows the relationship between the opening degree, the discharge pressure, and the feedwater temperature. As described in the conventional example, when the boiling of the hot water storage tank 5 is nearly completed, the temperature of the supply water flowing into the refrigerant-to-water heat exchanger 2 increases. That is, when the water flowing into the refrigerant-to-water heat exchanger 2 becomes the portion of the hot water mixture layer described above, as shown in FIG. When the feed water temperature detecting means 8 as the detecting means 13 immediately before the completion of the boiling detects the detected temperature Th immediately before the completion of the boiling (which is lower than the boiling temperature T1), the control means 12 sets the valve of the pressure reducing device 3 to Increase the opening (open). At this time, the discharge pressure decreases from P1 to P2. Thereafter, as the operation time elapses, the feedwater temperature further rises, and the discharge pressure rises accordingly. Then, when the feedwater temperature detecting means 8 detects the feedwater temperature T3a at which the normal upper limit pressure P is reached, the compressor is stopped and the heating operation is ended. The thick dotted line in FIG.
This is a case of a conventional example in which the valve opening of the pressure reducing device 3 is not controlled. It can be seen that the water supply temperature at the operation limit increases from T3 to T3a, and the operation range increases.

【0022】図3は貯湯槽5内の湯の温度分布を示す。
同図の左側に示す貯湯槽5の断面図において、湯温T3
a以下の領域は沸き上げ可能な領域であり、Tu以上の
領域は有効な湯として使用できる領域である。有効な湯
として利用できない領域は図23で示した従来例の場合
には湯温T3とTuの間の領域であったが、本実施例の
場合は湯温T3aとTuの間の領域(斜線の部分)であ
る。つまり、湯温T3とT3aの間の領域(点線による
斜線の部分)が、本実施例によって、有効になった湯の
領域である。
FIG. 3 shows the temperature distribution of the hot water in the hot water storage tank 5.
In the sectional view of the hot water storage tank 5 shown on the left side of FIG.
The region below a is a region that can be boiled, and the region above Tu is a region that can be used as effective hot water. The area that cannot be used as effective hot water is the area between the hot water temperatures T3 and Tu in the case of the conventional example shown in FIG. 23, but the area between the hot water temperatures T3a and Tu (the hatched area) in the present embodiment. Part). In other words, the area between the hot water temperatures T3 and T3a (the shaded area indicated by the dotted line) is the hot water area that has become effective according to the present embodiment.

【0023】以上のように、本実施例においては、圧縮
機、冷媒対水熱交換器、減圧装置、蒸発器を順次接続し
た冷媒循環回路と、貯湯槽、循環ポンプ、前記冷媒対水
熱交換器を順次接続した給湯回路と、貯湯槽全体が沸き
上がる直前を検出する沸き上げ完了直前検出手段と、前
記沸き上げ完了直前検出手段からの信号が所定の信号に
なった時に、前記減圧装置の弁開度を開くように制御す
る制御手段とを備えたことにより、沸き上げ完了に近づ
き、圧縮機の吐出圧力が上昇する場合に、減圧装置の弁
開度を開くように制御し、吐出圧力を低く押さえ、高温
の給水温度まで給湯加熱運転が可能となり、貯湯槽の湯
容量を有効に利用できるものである。
As described above, in this embodiment, the refrigerant circulation circuit in which the compressor, the refrigerant-to-water heat exchanger, the pressure reducing device, and the evaporator are sequentially connected, the hot water tank, the circulation pump, and the refrigerant-to-water heat exchange A hot water supply circuit to which water heaters are sequentially connected, a means for detecting immediately before the boiling of the entire hot water storage tank is completed, and a valve for the pressure reducing device when the signal from the means for immediately before the boiling becomes a predetermined signal. Control means for controlling the opening degree, by controlling the opening degree of the valve of the pressure reducing device when the boiling pressure is close to completion and the discharge pressure of the compressor increases, thereby controlling the discharge pressure. It is possible to perform the hot water supply heating operation up to a high supply water temperature by holding the supply water low, so that the hot water capacity of the hot water storage tank can be effectively used.

【0024】なお、本実施例において、循環ポンプ6を
冷媒対水熱交換器2の水側入口と貯湯槽5との間に設
け、流量調整弁11を循環ポンプ6と冷媒対水熱交換器
2の水側入口との間に設けたが、流量調整弁11の位置
としては、循環ポンプ6の入口と貯湯槽5との間に設け
ても、冷媒対水熱交換器2の水側出口と貯湯槽5との間
に設けも、図1の実施例と同様の作用、効果が得られ
る。
In this embodiment, the circulation pump 6 is provided between the water-side inlet of the refrigerant-to-water heat exchanger 2 and the hot water storage tank 5, and the flow control valve 11 is provided with the circulation pump 6 and the refrigerant-to-water heat exchanger. 2 is provided between the inlet of the circulating pump 6 and the hot water storage tank 5, but the position of the flow control valve 11 may be provided between the water-side outlet of the refrigerant and the water heat exchanger 2. The same operation and effect as those in the embodiment of FIG.

【0025】また、冷凍サイクルとしては、図22の従
来例で説明したように、冷媒対水熱交換器2を凝縮器と
して使用する吐出圧力が臨界点より低い通常のヒートポ
ンプサイクルであってもよいし、冷媒対水熱交換器2を
ガスクーラとして使用する吐出圧力が臨界点より高い超
臨界ヒートポンプサイクルであってもよい。
The refrigeration cycle may be a normal heat pump cycle in which the refrigerant-to-water heat exchanger 2 is used as a condenser and the discharge pressure is lower than the critical point, as described in the conventional example of FIG. However, a supercritical heat pump cycle in which the refrigerant-to-water heat exchanger 2 is used as a gas cooler and the discharge pressure is higher than the critical point may be used.

【0026】(実施例2)図4は本発明の実施例2のヒ
ートポンプ給湯機の構成図、図5は同ヒートポンプ給湯
機の減圧装置の弁開度に対する吐出圧力を示すグラフ、
図6は同ヒートポンプ給湯機の外気温度に対する減圧装
置の弁開度の変更量と沸き上げ完了直前検出温度とを示
すグラフである。
(Embodiment 2) FIG. 4 is a block diagram of a heat pump water heater according to Embodiment 2 of the present invention, and FIG. 5 is a graph showing discharge pressure with respect to valve opening degree of a pressure reducing device of the heat pump water heater.
FIG. 6 is a graph showing the change amount of the valve opening of the pressure reducing device with respect to the outside air temperature of the heat pump water heater and the detected temperature immediately before the completion of boiling.

【0027】本実施例において、実施例1と異なる点
は、外気温度を検出する外気温度検出手段14と、外気
温度に対する減圧装置3の弁開度の変更量を記憶してい
る第一の記憶手段15とを設けた構成としていることで
ある。なお、実施例1と同符号の部分は同一構成を有
し、説明は省略する。
The present embodiment is different from the first embodiment in that an outside air temperature detecting means 14 for detecting an outside air temperature and a first storage which stores a change amount of the valve opening of the pressure reducing device 3 with respect to the outside air temperature. And means 15 are provided. Note that the portions denoted by the same reference numerals as those in the first embodiment have the same configuration, and description thereof will be omitted.

【0028】次に動作、作用について説明する。図5は
横軸に減圧装置3の弁開度をとり、外気温度をパラメー
タ(冬は例えば5℃、中間期は例えば18℃、夏は例え
ば29℃)にして、縦軸に吐出圧力をとって、ある給水
温度の場合の減圧装置3の弁開度に対する吐出圧力の関
係を示したものである。同図に示すように、減圧装置3
の弁開度が大きくなれば、吐出圧力が減少する。そこ
で、吐出圧力をP1からP2に減少させるための減圧装
置3の弁開度の変更量を求めれば、冬(例えば5℃)で
は△S1、中間期(例えば18℃)では△S2、夏(例
えば29℃)では△S3となる。
Next, the operation and operation will be described. In FIG. 5, the horizontal axis indicates the valve opening of the pressure reducing device 3, the outside air temperature is set as a parameter (for example, 5 ° C. in winter, 18 ° C. in the middle period, 29 ° C. in summer, for example), and the discharge pressure is plotted on the vertical axis. 7 shows the relationship between the valve opening of the pressure reducing device 3 and the discharge pressure at a certain feedwater temperature. As shown in FIG.
When the valve opening degree becomes large, the discharge pressure decreases. Therefore, if the amount of change in the valve opening of the pressure reducing device 3 for reducing the discharge pressure from P1 to P2 is obtained, ΔS1 in winter (for example, 5 ° C.), ΔS2 in the intermediate period (for example, 18 ° C.), and summer ( At 29 ° C., for example, ΔS3 is obtained.

【0029】図6は横軸に外気温度をとり、縦軸に減圧
装置3の弁開度の変更量と沸き上げ完了直前検出温度と
をとって、外気温度に対する減圧装置3の弁開度の変更
量と沸き上げ完了直前検出温度との関係を示したもので
ある。外気温度に対する減圧装置3の弁開度の変更量の
関係は、図5で求めた外気温度(冬は5℃、中間期は1
8℃、夏は29℃)に対する変更量(冬は△S1、中間
期は△S2、夏は△S3)の関係である。また、外気温
度に対する沸き上げ完了直前検出温度の関係は、各外気
温度(冬は例えば5℃、中間期は例えば18℃、夏は例
えば29℃)において吐出圧力がP1になる給水温度
(沸き上げ完了直前検出温度Th)を求めることによっ
て決定できる。そして、これらの関係をあらわしたもの
が図6であり、この図6の関係を第一の記憶手段15に
記憶させる。
FIG. 6 shows the outside air temperature on the horizontal axis, and the change amount of the valve opening of the pressure reducing device 3 and the detected temperature immediately before the completion of boiling on the vertical axis, and shows the valve opening of the pressure reducing device 3 with respect to the outside air temperature. 9 shows the relationship between the change amount and the detected temperature immediately before the completion of boiling. The relationship between the outside air temperature and the amount of change in the valve opening of the pressure reducing device 3 is determined by the outside air temperature (5 ° C. in winter, 1
The change amount (△ S1 in winter, △ S2 in the interim period, △ S3 in summer) relative to 8 ° C. and 29 ° C. in summer. The relationship between the outside air temperature and the detected temperature immediately before the completion of boiling is as follows: at each outside air temperature (for example, 5 ° C. in winter, 18 ° C. in the intermediate period, and 29 ° C. in summer, for example), the feedwater temperature (boiling up) at which the discharge pressure is P1 It can be determined by obtaining the detected temperature immediately before completion Th). FIG. 6 shows these relationships, and the relationships in FIG. 6 are stored in the first storage unit 15.

【0030】制御手段12は、定期的に、沸き上げ完了
直前検出手段13である給水温度検出手段8から給水温
度を検出し、さらに、外気温度検出手段14から外気温
度を検出する。そして、第一の記憶手段15に記憶させ
ている、外気温度に対する減圧装置3の弁開度の変更量
と沸き上げ完了直前検出温度Thとを求める。そして、
給水温度検出手段8から求めた給水温度が沸き上げ完了
直前検出温度Thより低ければ、減圧装置3の弁開度は
変更せず、逆に、給水温度が沸き上げ完了直前検出温度
Thより高ければ第一の記憶手段15から求めた減圧装
置3の弁開度の変更量だけ減圧装置3の弁開度を変更す
る(開く)。減圧装置3の弁開度を変更すると吐出圧力
はP1からP2に減少する。その後、実施例1で説明し
たように、運転時間の経過とともに給水温度が更に上昇
し、それに従って吐出圧力が上昇する。そして、給水温
度検出手段8が、常用上限圧力Pになる給水温度T3a
を検出すると、圧縮機を停止し、加熱運転を終了する。
The control means 12 periodically detects the supply water temperature from the supply water temperature detection means 8, which is the detection means 13 immediately before the completion of boiling, and further detects the outside air temperature from the outside air temperature detection means 14. Then, the amount of change of the valve opening of the pressure reducing device 3 with respect to the outside air temperature and the detected temperature Th immediately before the completion of boiling, which are stored in the first storage means 15, are obtained. And
If the feedwater temperature obtained from the feedwater temperature detecting means 8 is lower than the detected temperature Th immediately before the completion of boiling, the valve opening of the pressure reducing device 3 is not changed. Conversely, if the feedwater temperature is higher than the detected temperature Th immediately before the completion of boiling. The valve opening of the pressure reducing device 3 is changed (opened) by the change amount of the valve opening of the pressure reducing device 3 obtained from the first storage means 15. When the valve opening of the pressure reducing device 3 is changed, the discharge pressure decreases from P1 to P2. Thereafter, as described in the first embodiment, the feedwater temperature further increases with the elapse of the operation time, and the discharge pressure increases accordingly. Then, the feedwater temperature detecting means 8 detects that the feedwater temperature T3a becomes the normal upper limit pressure P.
Is detected, the compressor is stopped and the heating operation is terminated.

【0031】以上のように、本実施例においては、減圧
装置の弁開度の変更量は外気温度を検出する外気温度検
出手段から得た外気温度に応じて決定する制御手段を備
えたことにより、外気温度に応じた最適な減圧装置の弁
開度の変更を行うので、貯湯槽の湯容量を有効に利用で
き、かつ、効率の良い給湯加熱運転ができるものであ
る。
As described above, in the present embodiment, the control means for determining the amount of change in the valve opening of the pressure reducing device in accordance with the outside air temperature obtained from the outside air temperature detecting means for detecting the outside air temperature is provided. Since the valve opening of the decompression device is optimally changed in accordance with the outside air temperature, the hot water capacity of the hot water tank can be effectively used, and the efficient hot water supply heating operation can be performed.

【0032】(実施例3)図7は本発明の実施例3のヒ
ートポンプ給湯機の構成図、図8は同ヒートポンプ給湯
機の運転時間に対する給水温度と吐出圧力と減圧装置の
弁開度と圧縮機の運転状態とを示すグラフである。
(Embodiment 3) FIG. 7 is a block diagram of a heat pump water heater according to Embodiment 3 of the present invention, and FIG. 8 is a diagram showing a water supply temperature, a discharge pressure, a valve opening degree and a compression of a pressure reducing device with respect to an operation time of the heat pump water heater. It is a graph which shows the driving | running state of a machine.

【0033】本実施例において、実施例1と異なる点
は、給水温度記憶手段16を設けた構成としていること
である。なお、実施例1と同符号の部分は同一構成を有
し、説明は省略する。
This embodiment is different from the first embodiment in that a water supply temperature storage means 16 is provided. Note that the portions denoted by the same reference numerals as those in the first embodiment have the same configuration, and description thereof will be omitted.

【0034】次に動作、作用について説明する。図8は
横軸に運転時間をとり、縦軸に給水温度と吐出圧力と減
圧装置の弁開度と圧縮機の運転状態とをとって、運転時
間に対する給水温度と吐出圧力と減圧装置の弁開度と圧
縮機の運転状態との関係を示したものである。同図中に
示すTh1、Th2(Th1<Th2)は、沸き上げ完
了直前検出温度Thで、それぞれ第一の沸き上げ完了直
前検出温度、第二の沸き上げ完了直前検出温度である。
この第一の沸き上げ完了直前検出温度Th1と第二の沸
き上げ完了直前検出温度Th2とを給水温度記憶手段1
6に記憶させる。
Next, the operation and operation will be described. FIG. 8 shows the operation time on the horizontal axis, the feed water temperature, discharge pressure, the valve opening degree of the pressure reducing device, and the operating state of the compressor on the vertical axis. 4 shows a relationship between the opening degree and the operating state of the compressor. Th1 and Th2 (Th1 <Th2) shown in the figure are detected temperatures Th immediately before the completion of boiling, and are a detected temperature immediately before the completion of the first boiling and a detected temperature immediately before the completion of the second boiling, respectively.
The first detected temperature Th1 immediately before the completion of boiling and the second detected temperature Th2 immediately before the completion of boiling are stored in the water supply temperature storage means 1.
6 is stored.

【0035】前述したように、貯湯槽5の沸き上げ完了
近くになると、冷媒対水熱交換器2に流入する給水温度
は高くなる。制御手段12は、定期的に、沸き上げ完了
直前検出手段13である給水温度検出手段8から給水温
度を検出し、さらに、給水温度記憶手段16に記憶させ
ている第一の沸き上げ完了直前検出温度Th1を求め
る。そして、給水温度検出手段8から求めた給水温度が
第一の沸き上げ完了直前検出温度Th1より低ければ、
減圧装置3の弁開度は変更せず、逆に、給水温度が第一
の沸き上げ完了直前検出温度Th1より高ければ減圧装
置3の弁開度を変更する(開く)。減圧装置3の弁開度
を変更すると吐出圧力は減少する。その後も、制御手段
12は、定期的に、沸き上げ完了直前検出手段13であ
る給水温度検出手段8から給水温度を検出し、さらに、
給水温度記憶手段16に記憶させている第二の沸き上げ
完了直前検出温度Th2を求める。そして、給水温度検
出手段8から求めた給水温度が第二の沸き上げ完了直前
検出温度Th2より低ければ、減圧装置3の弁開度は変
更せず、逆に、給水温度が第二の沸き上げ完了直前検出
温度Th2より高ければ減圧装置3の弁開度を変更する
(開く)。減圧装置3の弁開度を変更した時は同様に、
吐出圧力は減少する。その後、実施例1で説明したよう
に、運転時間の経過とともに給水温度が更に上昇し、そ
れに従って吐出圧力が上昇する。そして、給水温度検出
手段8が、常用上限圧力Pになる給水温度T3aを検出
すると、圧縮機を停止し、加熱運転を終了する。
As described above, when the boiling of the hot water storage tank 5 is nearly completed, the temperature of the supply water flowing into the refrigerant-to-water heat exchanger 2 increases. The control means 12 periodically detects the feed water temperature from the feed water temperature detection means 8 which is the detection means 13 immediately before the completion of the boiling, and further detects the temperature immediately before the completion of the first boiling stored in the feed water temperature storage means 16. The temperature Th1 is obtained. And if the feed water temperature obtained from the feed water temperature detecting means 8 is lower than the detected temperature Th1 immediately before the completion of the first boiling,
The valve opening of the pressure reducing device 3 is not changed. Conversely, if the feedwater temperature is higher than the first detected temperature Th1 just before the completion of boiling, the valve opening of the pressure reducing device 3 is changed (opened). When the valve opening of the pressure reducing device 3 is changed, the discharge pressure decreases. After that, the control means 12 periodically detects the feed water temperature from the feed water temperature detecting means 8 which is the detecting means 13 immediately before the completion of boiling, and further,
The second detected temperature Th2 immediately before completion of the boiling stored in the water supply temperature storage means 16 is obtained. If the feed water temperature obtained from the feed water temperature detecting means 8 is lower than the second detected temperature immediately before the completion of boiling, the valve opening of the pressure reducing device 3 is not changed. If it is higher than the detection temperature Th2 just before completion, the valve opening of the pressure reducing device 3 is changed (opened). Similarly, when the valve opening of the pressure reducing device 3 is changed,
The discharge pressure decreases. Thereafter, as described in the first embodiment, the feedwater temperature further increases with the elapse of the operation time, and the discharge pressure increases accordingly. Then, when the feedwater temperature detecting means 8 detects the feedwater temperature T3a at which the normal upper limit pressure P is reached, the compressor is stopped and the heating operation is ended.

【0036】以上のように、本実施例においては、予め
決められた複数の給水温度毎に前記減圧装置の弁開度の
変更を行う制御手段を備えたことにより、給水温度に応
じた最適な減圧装置の弁開度の変更を行うので、有効な
湯として利用できない無駄な領域がより少なくなるた
め、貯湯槽の湯容量を有効に利用でき、かつ、効率の良
い給湯加熱運転ができるものである。
As described above, in the present embodiment, the control means for changing the valve opening of the pressure reducing device for each of a plurality of predetermined supply water temperatures is provided, so that the optimum value corresponding to the supply water temperature is provided. Since the valve opening of the decompression device is changed, there is less wasteful area that cannot be used as effective hot water, so that the hot water capacity of the hot water storage tank can be used effectively, and an efficient hot water supply heating operation can be performed. is there.

【0037】また、本実施例では、沸き上げ完了直前検
出温度Thとして2つの給水温度を設定したが、3つ以
上の給水温度を設定しても、本実施例と同様の作用、効
果が得られる。
In this embodiment, two feed water temperatures are set as the detected temperature Th immediately before the completion of boiling. However, even if three or more feed water temperatures are set, the same operation and effect as those of the present embodiment can be obtained. Can be

【0038】(実施例4)図9は本発明の実施例4のヒ
ートポンプ給湯機の構成図、図10は同ヒートポンプ給
湯機の給水温度に対する吐出圧力と減圧装置の弁開度を
示すグラフ、図11は同ヒートポンプ給湯機の給水温度
に対する減圧装置の弁開度の変更量を示すグラフであ
る。
(Embodiment 4) FIG. 9 is a block diagram of a heat pump water heater according to a fourth embodiment of the present invention, and FIG. 10 is a graph showing a discharge pressure and a valve opening of a pressure reducing device with respect to a water supply temperature of the heat pump water heater. 11 is a graph showing the amount of change in the valve opening of the pressure reducing device with respect to the feed water temperature of the heat pump water heater.

【0039】本実施例において、実施例3と異なる点
は、給水温度に対する減圧装置の弁開度の変更量を記憶
する第二の記憶手段17を設けた構成としていることで
ある。なお、実施例3と同符号の部分は同一構成を有
し、説明は省略する。
The present embodiment is different from the third embodiment in that a second storage means 17 for storing the amount of change of the valve opening of the pressure reducing device with respect to the feed water temperature is provided. Note that the portions denoted by the same reference numerals as in the third embodiment have the same configuration, and description thereof will be omitted.

【0040】次に動作、作用について説明する。図10
は横軸に給水温度をとり、縦軸に吐出圧力と減圧装置の
弁開度とをとって、給水温度に対する吐出圧力と減圧装
置の弁開度との関係を示したものである。同図におい
て、点線は減圧装置3の弁開度を一定とした場合であ
る。同図からわかるように、給水温度が高くなればなる
ほど急激に吐出圧力が高くなる。また、同図中に示すT
h1、Th2、Th3、Th4、Th5(Th1<Th
2<Th3<Th4<Th5)は、沸き上げ完了直前検
出温度Thを示す給水温度で、それぞれ第一、第二、第
三、第四、第五の沸き上げ完了直前検出温度である。こ
の第一から第五の沸き上げ完了直前検出温度を給水温度
記憶手段16に記憶させる。そして、沸き上げ完了直前
検出手段13である給水温度検出手段8から検出した給
水温度が、給水温度記憶手段16に記憶させている沸き
上げ完了直前検出温度Th(Th1、Th2、Th3、
Th4、Th5)以上になれば、減圧装置3の弁開度を
変更(それぞれ△S1、△S2、△S3、△S4、△S
5)する(開く)。この時の減圧装置3の弁開度の変更
量を、同図に示すように、沸き上げ完了直前検出温度の
高い方がより大きくする。つまり、沸き上げ完了直前検
出温度Th1<Th2<Th3<Th4<Th5の時、
減圧装置3の弁開度の変更量を△S1<△S2<△S3
<△S4<△S5とする。このようにすれば、同図の実
線で示すように、吐出圧力の急激な上昇はなくなる。ま
た、図11は横軸に給水温度をとり、縦軸に減圧装置3
の弁開度の変更量をとって、給水温度に対する減圧装置
3の弁開度の変更量の関係を示したものであり、この関
係を第二の記憶手段17に記憶させる。
Next, the operation and operation will be described. FIG.
Shows the relationship between the discharge pressure and the valve opening of the pressure reducing device with respect to the water supply temperature by taking the feed water temperature on the horizontal axis and the discharge pressure and the valve opening of the pressure reducing device on the vertical axis. In the figure, the dotted line indicates a case where the valve opening of the pressure reducing device 3 is constant. As can be seen from the figure, the higher the feedwater temperature, the more rapidly the discharge pressure increases. Further, T shown in FIG.
h1, Th2, Th3, Th4, Th5 (Th1 <Th
2 <Th3 <Th4 <Th5) is the feedwater temperature indicating the detected temperature Th immediately before the completion of the boiling, and is the first, second, third, fourth, and fifth detected temperatures immediately before the completion of the boiling, respectively. The first to fifth detected temperatures immediately before the completion of boiling are stored in the feedwater temperature storage means 16. Then, the feed water temperature detected from the feed water temperature detecting means 8 which is the detecting means 13 immediately before the completion of the boiling is stored in the feed water temperature storing means 16 and the detected temperature Th immediately before the completion of the boiling Th (Th1, Th2, Th3,
Th4, Th5) or more, the valve opening of the pressure reducing device 3 is changed ((S1, △ S2, △ S3, △ S4, △ S, respectively).
5) Do (open). As shown in the figure, the change amount of the valve opening degree of the pressure reducing device 3 at this time is made larger when the detected temperature immediately before the completion of boiling is higher. That is, when the detected temperature immediately before the completion of boiling is Th1 <Th2 <Th3 <Th4 <Th5,
The change amount of the valve opening degree of the pressure reducing device 3 is set to △ S1 <△ S2 <△ S3
<△ S4 <△ S5. In this way, as shown by the solid line in FIG. FIG. 11 shows the feedwater temperature on the horizontal axis and the pressure reducing device 3 on the vertical axis.
The relationship between the amount of change in the valve opening of the pressure reducing device 3 and the supply water temperature is shown by taking the amount of change in the valve opening of the second embodiment, and this relationship is stored in the second storage means 17.

【0041】制御手段12は、定期的に、沸き上げ完了
直前検出手段13である給水温度検出手段8から給水温
度を検出する。そして、給水温度記憶手段16に記憶さ
せている沸き上げ完了直前検出温度Th(Th1、Th
2、Th3、Th4、Th5)を求める。そして、給水
温度検出手段8から求めた給水温度が沸き上げ完了直前
検出温度Thより低ければ、減圧装置3の弁開度は変更
せず、逆に、給水温度が沸き上げ完了直前検出温度Th
より高ければ、第二の記憶手段17に記憶している給水
温度に対する減圧装置の弁開度の変更量(それぞれ△S
1、△S2、△S3、△S4、△S5)だけ減圧装置3
の弁開度を変更する(開く)。
The control means 12 periodically detects the feed water temperature from the feed water temperature detecting means 8 which is the detecting means 13 immediately before the completion of boiling. Then, the detected temperature Th (Th1, Th1) immediately before the completion of the boiling stored in the water supply temperature storage means 16 is stored.
2, Th3, Th4, Th5). If the feed water temperature obtained from the feed water temperature detecting means 8 is lower than the detected temperature Th immediately before the completion of boiling, the valve opening of the pressure reducing device 3 is not changed.
If it is higher, the change amount of the valve opening of the pressure reducing device with respect to the feed water temperature stored in the second storage means 17 (each of ΔS
1, ΔS2, ΔS3, ΔS4, ΔS5)
Change the valve opening (open).

【0042】以上のように、本実施例においては、給水
温度が高いほど減圧装置の弁開度の変更量を大きくした
制御手段を備えたことにより、吐出圧力の上昇が大きい
高給水温度時に減圧装置の弁開度の変更量を大きくして
吐出圧力を大きく低下させ、給水温度に応じた最適な減
圧装置の弁開度の変更を行うので、貯湯槽の湯容量を有
効に利用でき、かつ、効率の良い給湯加熱運転ができる
ものである。
As described above, in the present embodiment, the control means for increasing the change amount of the valve opening of the pressure reducing device as the water supply temperature becomes higher is provided. Since the discharge pressure is greatly reduced by increasing the amount of change in the valve opening of the device, and the valve opening of the decompression device is optimally changed according to the supply water temperature, the hot water capacity of the hot water tank can be used effectively, and In addition, an efficient hot water supply heating operation can be performed.

【0043】また、本実施例では、沸き上げ完了直前検
出温度Thとして5つの給水温度を設定したが、6つ以
上の給水温度を設定しても、本実施例と同様の作用、効
果が得られる。
In this embodiment, five feed water temperatures are set as the detected temperature Th immediately before the completion of boiling. However, even if six or more feed water temperatures are set, the same operation and effect as those of this embodiment can be obtained. Can be

【0044】(実施例5)図12は本発明の実施例5の
ヒートポンプ給湯機の構成図、図13は同ヒートポンプ
給湯機の運転時間に対する給水温度と減圧装置の弁開度
と吐出圧力とを示すグラフである。
(Embodiment 5) FIG. 12 is a block diagram of a heat pump water heater according to a fifth embodiment of the present invention, and FIG. 13 shows the relationship between the water supply temperature, the valve opening degree of the pressure reducing device, and the discharge pressure with respect to the operation time of the heat pump water heater. It is a graph shown.

【0045】本実施例において、実施例1と異なる点は
タイマー18を設けた構成としていることである。な
お、実施例1と同符号の部分は同一構成を有し、説明は
省略する。
The present embodiment is different from the first embodiment in that a timer 18 is provided. Note that the portions denoted by the same reference numerals as those in the first embodiment have the same configuration, and description thereof will be omitted.

【0046】次に動作、作用について説明する。図13
は横軸に運転時間度をとり、縦軸に給水温度と減圧装置
の弁開度と吐出圧力とをとって、運転時間に対する給水
温度と減圧装置の弁開度と吐出圧力との関係を示したも
のである。前述したように、湯水混合層の部分になると
運転時間とともに給水温度が上昇する。同図において、
点線は減圧装置3の弁開度を一定とした場合であり、運
転時間が経過して給水温度が高くなればなるほど急激に
吐出圧力が高くなる。そこで、給水温度が、沸き上げ完
了直前検出温度Thになれば、予め設定された所定の時
間間隔△T毎に、減圧装置3の弁開度を大きくする。こ
のようにすれば、同図のように、減圧装置3の弁開度が
一定の場合に比べて、吐出圧力を低くすることができ
る。
Next, the operation and operation will be described. FIG.
The horizontal axis shows the degree of operation time, and the vertical axis shows the relationship between the feed water temperature, the valve opening of the pressure reducing device, and the discharge pressure with respect to the operating time, taking the feed water temperature, the valve opening of the pressure reducing device, and the discharge pressure. It is a thing. As described above, the feedwater temperature rises with the operation time in the hot water / water mixture layer. In the figure,
The dotted line shows the case where the valve opening of the pressure reducing device 3 is fixed, and the discharge pressure increases rapidly as the operation time elapses and the feedwater temperature increases. Therefore, when the supply water temperature becomes equal to the detected temperature Th immediately before the completion of boiling, the valve opening of the pressure reducing device 3 is increased at predetermined preset time intervals ΔT. By doing so, the discharge pressure can be reduced as compared with the case where the valve opening of the pressure reducing device 3 is constant as shown in FIG.

【0047】すなわち、制御手段12は、定期的に、沸
き上げ完了直前検出手段13である給水温度検出手段8
から給水温度を検出する。そして、給水温度検出手段8
から求めた給水温度が沸き上げ完了直前検出温度Thよ
り高ければ、タイマー18からの信号によって、所定の
時間間隔△T毎に減圧装置3の弁開度を開く。
That is, the control means 12 periodically supplies the feedwater temperature detecting means 8 which is the detecting means 13 immediately before the completion of boiling.
From the water supply temperature. Then, the water supply temperature detecting means 8
If the feed water temperature obtained from the above is higher than the detected temperature Th immediately before the completion of boiling, the valve opening of the pressure reducing device 3 is opened at predetermined time intervals ΔT by a signal from the timer 18.

【0048】以上のように、本実施例においては、予め
設定された時間間隔ごとに減圧装置3の弁開度の変更を
行う制御手段12を備えたことにより、沸き上げ完了直
前時に最適な減圧装置3の弁開度の変更を行うので、貯
湯槽5の湯容量を有効に利用でき、かつ、効率の良い給
湯加熱運転ができるものである。
As described above, in the present embodiment, the control means 12 for changing the valve opening of the pressure reducing device 3 at predetermined time intervals is provided, so that the optimum pressure reduction immediately before the completion of boiling is provided. Since the opening degree of the valve of the device 3 is changed, the hot water capacity of the hot water storage tank 5 can be effectively used, and an efficient hot water supply heating operation can be performed.

【0049】(実施例6)図14は本発明の実施例6の
ヒートポンプ給湯機の構成図、図15は同ヒートポンプ
給湯機の運転時間に対する給水温度と減圧装置の弁開度
と吐出圧力とを示すグラフである。
(Embodiment 6) FIG. 14 is a block diagram of a heat pump water heater according to Embodiment 6 of the present invention, and FIG. 15 is a graph showing the relationship between the water supply temperature, the valve opening degree of the pressure reducing device, and the discharge pressure with respect to the operation time of the heat pump water heater. It is a graph shown.

【0050】本実施例において、実施例5と異なる点は
時間間隔記憶手段19を設けた構成としていることであ
る。なお、実施例5と同符号の部分は同一構成を有し、
説明は省略する。
The present embodiment is different from the fifth embodiment in that a time interval storage means 19 is provided. Note that the portions denoted by the same reference numerals as those of the fifth embodiment have the same configuration,
Description is omitted.

【0051】次に動作、作用について説明する。図15
は横軸に運転時間度をとり、縦軸に給水温度と減圧装置
の弁開度と吐出圧力とをとって、運転時間に対する給水
温度と減圧装置の弁開度と吐出圧力との関係を示したも
のである。前述したように、湯水混合層の部分になると
運転時間とともに給水温度が上昇する。同図において、
点線は減圧装置3の弁開度を一定とした場合であり、運
転時間が経過して給水温度が高くなればなるほど急激に
吐出圧力が高くなる。そこで、給水温度が、第一の沸き
上げ完了直前検出温度Th1になれば、予め設定された
所定の第一の時間間隔△T1毎に、減圧装置3の弁開度
を大きくする。そして、給水温度が上昇し、給水温度が
第二の沸き上げ完了直前検出温度Th2になれば、前記
第一の時間間隔△T1より小さい所定の第二の時間間隔
△T2(△T2<△T1)毎に、減圧装置3の弁開度を
大きくする。このように、吐出圧力が急激に上昇する高
給水温度時に、減圧装置3の弁開度を修正する時間間隔
を短くすれば、同図のように、減圧装置3の弁開度が一
定の場合に比べて、吐出圧力を低くすることができ、特
に、急激な吐出圧力の上昇をなくすことができるため、
給湯加熱運転の範囲を広げることができる。ところで、
前述した第一の時間間隔△T1と第二の時間間隔△T2
とを時間間隔記憶手段19に記憶させておく。
Next, the operation and operation will be described. FIG.
The horizontal axis shows the degree of operation time, and the vertical axis shows the relationship between the feed water temperature, the valve opening of the pressure reducing device, and the discharge pressure with respect to the operating time, taking the feed water temperature, the valve opening of the pressure reducing device, and the discharge pressure. It is a thing. As described above, the feedwater temperature rises with the operation time in the hot water / water mixture layer. In the figure,
The dotted line shows the case where the valve opening of the pressure reducing device 3 is fixed, and the discharge pressure increases rapidly as the operation time elapses and the feedwater temperature increases. Therefore, when the feedwater temperature becomes the detected temperature Th1 immediately before the completion of the first boiling, the valve opening of the pressure reducing device 3 is increased at every predetermined first time interval ΔT1. Then, when the feed water temperature rises and the feed water temperature becomes the detected temperature Th2 immediately before the completion of the second boiling, a predetermined second time interval ΔT2 (ΔT2 <ΔT1) smaller than the first time interval ΔT1. ), The valve opening of the pressure reducing device 3 is increased. As described above, if the time interval for correcting the valve opening of the pressure reducing device 3 is shortened at the time of high supply water temperature at which the discharge pressure rises rapidly, as shown in FIG. As compared with, the discharge pressure can be reduced, and in particular, since a sharp increase in the discharge pressure can be eliminated,
The range of the hot water supply heating operation can be expanded. by the way,
The above-mentioned first time interval ΔT1 and second time interval ΔT2
Are stored in the time interval storage means 19.

【0052】すなわち、制御手段12は、定期的に、沸
き上げ完了直前検出手段13である給水温度検出手段8
から給水温度を検出する。そして、給水温度検出手段8
から求めた給水温度が第一の沸き上げ完了直前検出温度
Th1より高ければ、時間間隔記憶手段19からの信号
によって、第一の時間間隔△T1を検出する。そして、
タイマー18からの信号によって、第一の時間間隔△T
1毎に減圧装置3の弁開度を開く。さらに、給水温度が
上昇し、給水温度検出手段8から求めた給水温度が第二
の沸き上げ完了直前検出温度Th2より高ければ、時間
間隔記憶手段19からの信号によって、第二の時間間隔
△T2を検出する。そして、タイマー18からの信号に
よって、第二の時間間隔△T2毎に減圧装置3の弁開度
を開く。
That is, the control means 12 periodically supplies the feedwater temperature detecting means 8 which is the detecting means 13 immediately before the completion of boiling.
From the water supply temperature. Then, the water supply temperature detecting means 8
If the feed water temperature obtained from the above is higher than the first detected temperature Th1 immediately before the completion of boiling, the first time interval ΔT1 is detected by the signal from the time interval storage means 19. And
According to the signal from the timer 18, the first time interval ΔT
The valve opening of the pressure reducing device 3 is opened every one. Further, if the feed water temperature rises and the feed water temperature obtained from the feed water temperature detecting means 8 is higher than the second detected temperature immediately before the completion of the boiling Th2, the second time interval ΔT2 Is detected. Then, in response to a signal from the timer 18, the valve opening of the pressure reducing device 3 is opened at every second time interval ΔT2.

【0053】以上のように、本実施例においては、減圧
装置の弁開度の変更を行う時間間隔を沸き上げ完了に近
づくほど小さくした制御手段を備えたことにより、沸き
上げ完了に近づくほど吐出圧力の上昇が大きい時に減圧
装置の弁開度の変更を多くして吐出圧力を大きく低下さ
せ、最適な減圧装置の弁開度の変更を行うので、貯湯槽
の湯容量を有効に利用でき、かつ、効率の良い給湯加熱
運転ができるものである。
As described above, in this embodiment, by providing the control means for reducing the time interval for changing the valve opening of the pressure reducing device as the boiling is completed, the discharging is performed as the boiling is completed. When the pressure rise is large, the change in the valve opening of the pressure reducing device is increased to greatly reduce the discharge pressure, and the optimal valve opening of the pressure reducing device is changed, so that the hot water capacity of the hot water tank can be used effectively, In addition, an efficient hot water supply heating operation can be performed.

【0054】また、本実施例では、減圧装置の弁開度の
変更を行う時間間隔として2つの時間間隔(△T1、△
T2)を設定したが、3つ以上の時間間隔を設定して
も、本実施例と同様の作用、効果が得られる。
Further, in this embodiment, two time intervals ({T1 and {T1}) are used as time intervals for changing the valve opening of the pressure reducing device.
Although T2) is set, the same operation and effect as in the present embodiment can be obtained even if three or more time intervals are set.

【0055】(実施例7)図16は本発明の実施例7の
ヒートポンプ給湯機の構成図、図17は同ヒートポンプ
給湯機の運転時間に対する給水温度と流量調整弁の開度
と流量と吐出圧力と減圧装置の弁開度とを示すグラフで
ある。本実施例において、実施例1と異なる点は、沸上
げ完了直前検出手段13として、流量調整弁11を通過
する流量が最大流量になっている時間を計測する時間計
測手段20を設けた構成としていることである。なお、
実施例1と同符号の部分は同一構成を有し、説明は省略
する。
(Embodiment 7) FIG. 16 is a block diagram of a heat pump water heater according to Embodiment 7 of the present invention, and FIG. 17 is a diagram showing the water supply temperature, the opening degree of the flow regulating valve, the flow rate, and the discharge pressure with respect to the operation time of the heat pump water heater. It is a graph which shows the valve opening degree of a pressure reducing device. The present embodiment is different from the first embodiment in that a time measuring means 20 for measuring the time when the flow passing through the flow regulating valve 11 is the maximum flow is provided as the detecting means 13 immediately before the completion of boiling. It is that you are. In addition,
Portions denoted by the same reference numerals as in the first embodiment have the same configuration, and description thereof will be omitted.

【0056】次に動作、作用について説明する。図17
は横軸に運転時間度をとり、縦軸に給水温度と流量調整
弁11の開度と流量と吐出圧力と減圧装置3の弁開度と
をとって、運転時間に対する給水温度と流量調整弁11
の開度と流量と吐出圧力と減圧装置3の弁開度との関係
を示したものである。前述したように、冷媒対水熱交換
器2の水側出口に設けられた沸き上げ温度検出手段9か
らの信号で流量制御手段10は流量調整弁11の開度を
制御して、冷媒対水熱交換器2の出口水温(沸き上げ温
度)をほぼ一定になるように沸き上げる。今、湯水混合
層の部分になると運転時間とともに給水温度が上昇する
ので、冷媒対水熱交換器2の水側流量が大きくなるよう
に流量調整弁11の開度を大きくさせていく。ところ
が、流量調整弁11の開度が最大開度に達してもなお給
水温度が上昇する場合がある。この場合には、冷媒対水
熱交換器2の出口水温である沸き上げ温度が上昇し、か
つ、吐出圧力も急激に上昇する。そこで、流量調整弁1
1の開度が所定の運転時間続けて最大開度になれば、減
圧装置3の弁開度を開くように制御すれば、図17に示
すように、吐出圧力が低下し、給湯加熱運転を続けるこ
とが可能となる。
Next, the operation and operation will be described. FIG.
Takes the operation time degree on the horizontal axis, the feed water temperature, the opening degree and flow rate of the flow control valve 11, the discharge pressure, and the valve opening degree of the pressure reducing device 3 on the vertical axis. 11
The relationship between the opening degree, the flow rate, the discharge pressure, and the valve opening degree of the pressure reducing device 3 is shown. As described above, the flow control means 10 controls the opening degree of the flow control valve 11 by the signal from the boiling temperature detecting means 9 provided at the water-side outlet of the refrigerant-to-water heat exchanger 2, and The outlet water temperature (boiling temperature) of the heat exchanger 2 is raised so as to be substantially constant. Now, in the part of the hot and cold water mixing layer, the feed water temperature rises with the operation time, so the opening degree of the flow control valve 11 is increased so that the water flow rate of the refrigerant to the water heat exchanger 2 increases. However, even when the opening of the flow control valve 11 reaches the maximum opening, the supply water temperature may still rise. In this case, the boiling temperature, which is the outlet water temperature of the refrigerant-to-water heat exchanger 2, rises, and the discharge pressure also rises sharply. Therefore, the flow control valve 1
If the opening degree of No. 1 reaches the maximum opening degree continuously for a predetermined operation time, if the opening degree of the valve of the pressure reducing device 3 is controlled, the discharge pressure is reduced as shown in FIG. It is possible to continue.

【0057】すなわち、制御手段12は、定期的に、沸
き上げ完了直前検出手段13である時間計測手段20か
ら流量調整弁11の開度が最大開度になっている時間を
検出する。そして、この検出した時間が予め設定された
所定の運転時間より長ければ、時間計測手段20からの
信号によって、減圧装置3の弁開度を開く。
That is, the control means 12 periodically detects the time when the opening of the flow regulating valve 11 is at the maximum opening from the time measuring means 20 which is the detecting means 13 immediately before completion of boiling. If the detected time is longer than a predetermined operation time set in advance, the valve opening of the pressure reducing device 3 is opened by a signal from the time measuring means 20.

【0058】以上のように、本実施例においては、沸き
上げ完了直前検出手段として、流量調整弁11の開度が
最大になった時に時間を計測する時間計測手段を備えた
ことにより、所定の時間の間、流量調整弁11を通過す
る流量が最大流量になったことを検出して減圧装置の弁
開度の変更を行い、吐出圧力を低く押さえ、加熱運転を
続けるので、高温の給水温度まで給湯加熱運転が可能と
なり、貯湯槽の湯容量を有効に利用できるものである。
As described above, the present embodiment is provided with the time measuring means for measuring the time when the opening of the flow regulating valve 11 is maximized as the detecting means immediately before the completion of boiling, so that the predetermined time can be obtained. During a period of time, it detects that the flow passing through the flow control valve 11 has reached the maximum flow, changes the valve opening of the pressure reducing device, keeps the discharge pressure low, and continues the heating operation. The hot water supply heating operation is possible up to this, and the hot water capacity of the hot water storage tank can be used effectively.

【0059】(実施例8)図18は本発明の実施例8の
ヒートポンプ給湯機の構成図、図19は同ヒートポンプ
給湯機の運転時間に対する給水温度と吐出圧力と減圧装
置の弁開度とを示すグラフである。本実施例において、
実施例1と異なる点は、沸上げ完了直前検出手段13と
して、吐出圧力を検出する吐出圧力検出手段21を設け
た構成としていることである。なお、実施例1と同符号
の部分は同一構成を有し、説明は省略する。
(Eighth Embodiment) FIG. 18 is a block diagram of a heat pump water heater according to an eighth embodiment of the present invention, and FIG. 19 shows the water supply temperature, discharge pressure, and valve opening degree of the pressure reducing device with respect to the operation time of the heat pump water heater. It is a graph shown. In this embodiment,
The difference from the first embodiment is that the discharge pressure detecting means 21 for detecting the discharge pressure is provided as the detection means 13 immediately before the completion of boiling. Note that the portions denoted by the same reference numerals as those in the first embodiment have the same configuration, and description thereof will be omitted.

【0060】次に動作、作用について説明する。図19
は横軸に運転時間をとり、縦軸に給水温度と吐出圧力と
減圧装置の弁開度とをとって、運転時間に対する給水温
度と吐出圧力と減圧装置の弁開度との関係を示したもの
である。前述したように、湯水混合層の部分になると運
転時間とともに給水温度が上昇すし、これにともなっ
て、吐出圧力も高くなる。そこで、吐出圧力が基準圧力
Pになれば、減圧装置3の弁開度を大きくする。その結
果、吐出圧力を低下させることができる。
Next, the operation and operation will be described. FIG.
The horizontal axis indicates the operation time, and the vertical axis indicates the supply water temperature, the discharge pressure, and the valve opening of the pressure reducing device, and indicates the relationship between the water supply temperature, the discharge pressure, and the valve opening of the pressure reduction device with respect to the operation time. Things. As described above, in the hot and cold water mixing layer, the feed water temperature increases with the operation time, and the discharge pressure also increases accordingly. Therefore, when the discharge pressure reaches the reference pressure P, the valve opening of the pressure reducing device 3 is increased. As a result, the discharge pressure can be reduced.

【0061】すなわち、制御手段12は、定期的に、沸
き上げ完了直前検出手段13である吐出圧力検出手段2
1から吐出圧力を検出する。そして、吐出圧力検出手段
21から求めた吐出圧力が予め設定された基準圧力Pよ
り高ければ、吐出圧力検出手段21からの信号によっ
て、減圧装置3の弁開度を開く。そして、このことを繰
り返す。
That is, the control means 12 periodically controls the discharge pressure detecting means 2 as the detecting means 13 immediately before the completion of boiling.
From 1, the discharge pressure is detected. Then, if the discharge pressure obtained from the discharge pressure detecting means 21 is higher than a preset reference pressure P, the valve opening of the pressure reducing device 3 is opened by a signal from the discharge pressure detecting means 21. And this is repeated.

【0062】以上のように、本実施例においては、沸き
上げ完了直前検出手段として吐出圧力検出手段を用い、
設定された基準圧力になれば、減圧装置の弁開度を開く
ように制御する制御手段を備えたことにより、貯湯槽の
湯容量を有効に利用でき、かつ、直接圧力で制御するの
で、圧縮機のより確実な耐久性の向上になるものであ
る。
As described above, in the present embodiment, the discharge pressure detecting means is used as the detecting means immediately before the completion of boiling,
By providing control means for opening the valve opening of the pressure reducing device when the set reference pressure is reached, the hot water capacity of the hot water storage tank can be used effectively, and the pressure is controlled by direct pressure, so that the compression This will surely improve the durability of the machine.

【0063】(実施例9)図20は本発明の実施例9の
ヒートポンプ給湯機の構成図、図21は同ヒートポンプ
給湯機の運転時間に対する圧縮機の運転状態と減圧装置
の弁開度と吐出圧力と貯湯槽の下部温度とを示すグラフ
である。
(Embodiment 9) FIG. 20 is a block diagram of a heat pump water heater according to a ninth embodiment of the present invention, and FIG. 21 is a diagram showing the operating state of the compressor, the valve opening degree and discharge of the pressure reducing device with respect to the operation time of the heat pump water heater. It is a graph which shows pressure and the lower part temperature of a hot-water storage tank.

【0064】本実施例において、実施例1と異なる点
は、沸き上げ完了直前検出手段として貯湯槽の下部温度
を検出する貯湯槽温度検出手段22を設けた構成として
いることである。なお、実施例1と同符号の部分は同一
構成を有し、説明は省略する。
The present embodiment is different from the first embodiment in that a hot water tank temperature detecting means 22 for detecting a lower temperature of the hot water tank is provided as a means for detecting immediately before the completion of boiling. Note that the portions denoted by the same reference numerals as those in the first embodiment have the same configuration, and description thereof will be omitted.

【0065】次に動作、作用について説明する。図21
は横軸に運転時間をとり、縦軸に圧縮機1の運転状態と
減圧装置3の弁開度と吐出圧力と貯湯槽5の下部温度と
をとって、運転時間に対する圧縮機1の運転状態と減圧
装置3の弁開度と吐出圧力と貯湯槽5の下部温度との関
係を示したものである。前述したように、湯水混合層の
部分になると、運転時間とともに貯湯槽5の下部温度が
上昇する。そして、沸き上げ完了直前検出手段13であ
る貯湯槽温度検出手段22が沸き上げ完了直前検出温度
Thを検出すると、制御手段12は、減圧装置3の弁開
度を大きくする(開く)。この時、吐出圧力はP1から
P2に減少する。その後、運転時間の経過とともに貯湯
槽5の下部温度が更に上昇し、それに従って吐出圧力が
上昇する。そして、貯湯槽温度検出手段22が、常用上
限圧力Pになる貯湯槽5の下部温度T3aを検出する
と、圧縮機を停止し、加熱運転を終了する。なお、同図
中の太い点線は、減圧装置3の弁開度の制御を行わない
従来例の場合である。運転限界の貯湯槽5の下部温度が
T3からT3aへと高くなり、運転範囲が大きくなる。
Next, the operation and operation will be described. FIG.
Takes the operating time on the horizontal axis, the operating state of the compressor 1, the valve opening degree of the pressure reducing device 3, the discharge pressure, and the lower temperature of the hot water tank 5 on the vertical axis, and the operating state of the compressor 1 with respect to the operating time. And the relationship between the valve opening degree of the pressure reducing device 3, the discharge pressure, and the lower temperature of the hot water tank 5. As described above, the temperature of the lower part of the hot water storage tank 5 rises with the operation time when it comes to the hot and cold water mixed layer. Then, when the hot water tank temperature detecting means 22 which is the detecting means 13 immediately before the completion of the boiling detects the detected temperature Th immediately before the completion of the boiling, the control means 12 increases (opens) the valve opening of the pressure reducing device 3. At this time, the discharge pressure decreases from P1 to P2. Thereafter, as the operation time elapses, the lower temperature of the hot water tank 5 further rises, and the discharge pressure rises accordingly. Then, when the hot water tank temperature detecting means 22 detects the lower temperature T3a of the hot water tank 5 at which the normal upper limit pressure P is reached, the compressor is stopped and the heating operation ends. The thick dotted line in the figure is the case of the conventional example in which the valve opening of the pressure reducing device 3 is not controlled. The lower temperature of the hot water storage tank 5 at the operation limit increases from T3 to T3a, and the operation range increases.

【0066】以上のように、本実施例においては、沸き
上げ完了直前検出手段として貯湯槽温度検出手段を用
い、所定の貯湯槽温度以上になれば、減圧装置の弁開度
を開くように制御する制御手段を備えたことにより、貯
湯槽の湯容量を有効に利用でき、かつ、直接貯湯槽の温
度を検出して制御するので、圧縮機のより確実な耐久性
の向上になるものである
As described above, in the present embodiment, the hot-water tank temperature detecting means is used as the detecting means immediately before the completion of boiling, and when the temperature of the hot-water tank exceeds a predetermined value, the valve opening of the pressure reducing device is opened. With the control means, the hot water capacity of the hot water storage tank can be used effectively, and the temperature of the hot water storage tank is directly detected and controlled, so that the durability of the compressor is more reliably improved.

【0067】[0067]

【発明の効果】以上のように、請求項1から請求項9に
記載の発明によれば、沸き上げ完了に近づき、圧縮機の
吐出圧力が上昇する場合に、減圧装置の弁開度を制御
し、吐出圧力を低く押さえ、高温の給水温度まで給湯加
熱運転が可能となるので、有効な湯として利用できない
無駄な領域がより少なくなるため、貯湯槽の湯容量を有
効に利用できる。その結果、従来と同じ大きさの貯湯槽
でより大きな給湯負荷を満足し、逆に、従来と同じ大き
さの給湯負荷を満足するためには従来より小形の貯湯槽
でよいので、設置の自由度が大きく、コスト低減にもな
る。さらに、効率の良い給湯加熱運転ができるものであ
る。
As described above, according to the first to ninth aspects of the present invention, the valve opening of the pressure reducing device is controlled when the discharge pressure of the compressor rises near the completion of boiling. In addition, since the discharge pressure is kept low and the hot water supply heating operation can be performed up to a high supply water temperature, a wasteful area that cannot be used as effective hot water is reduced, and the hot water capacity of the hot water storage tank can be effectively used. As a result, a hot water tank of the same size as the conventional one can satisfy a larger hot water supply load, and conversely, to satisfy a hot water supply load of the same size as the conventional one, a smaller hot water tank can be used. The degree is large and the cost is reduced. Furthermore, an efficient hot water supply heating operation can be performed.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施例1のヒートポンプ給湯機を示す
構成図
FIG. 1 is a configuration diagram illustrating a heat pump water heater according to a first embodiment of the present invention.

【図2】同ヒートポンプ給湯機の運転時間に対する圧縮
機の運転状態と減圧装置の弁開度と吐出圧力と給水温度
とを示すグラフ
FIG. 2 is a graph showing an operating state of a compressor, a valve opening degree of a pressure reducing device, a discharge pressure, and a feed water temperature with respect to an operation time of the heat pump water heater.

【図3】同ヒートポンプ給湯機の貯湯槽の温度分布を示
す説明図
FIG. 3 is an explanatory diagram showing a temperature distribution of a hot water storage tank of the heat pump water heater.

【図4】本発明の実施例2のヒートポンプ給湯機を示す
構成図
FIG. 4 is a configuration diagram illustrating a heat pump water heater according to a second embodiment of the present invention.

【図5】同ヒートポンプ給湯機の減圧装置の弁開度に対
する吐出圧力を示すグラフ
FIG. 5 is a graph showing a discharge pressure with respect to a valve opening degree of a pressure reducing device of the heat pump water heater.

【図6】同ヒートポンプ給湯機の外気温度に対する減圧
装置の弁開度の変更量と沸き上げ完了直前検出温度とを
示すグラフ
FIG. 6 is a graph showing a change amount of a valve opening of a pressure reducing device with respect to an outside air temperature of the heat pump water heater and a detected temperature immediately before completion of boiling.

【図7】本発明の実施例3のヒートポンプ給湯機を示す
構成図
FIG. 7 is a configuration diagram illustrating a heat pump water heater according to a third embodiment of the present invention.

【図8】同ヒートポンプ給湯機の運転時間に対する給水
温度と吐出圧力と減圧装置の弁開度と圧縮機の運転状態
とを示すグラフ
FIG. 8 is a graph showing a feed water temperature, a discharge pressure, a valve opening degree of a pressure reducing device, and an operating state of a compressor with respect to an operation time of the heat pump water heater.

【図9】本発明の実施例4のヒートポンプ給湯機を示す
構成図
FIG. 9 is a configuration diagram illustrating a heat pump water heater according to a fourth embodiment of the present invention.

【図10】同ヒートポンプ給湯機の給水温度に対する吐
出圧力と減圧装置の弁開度を示すグラフ
FIG. 10 is a graph showing a discharge pressure and a valve opening of a pressure reducing device with respect to a water supply temperature of the heat pump water heater.

【図11】同ヒートポンプ給湯機の給水温度に対する減
圧装置の弁開度の変更量を示すグラフ
FIG. 11 is a graph showing a change amount of a valve opening degree of a pressure reducing device with respect to a water supply temperature of the heat pump water heater.

【図12】本発明の実施例5のヒートポンプ給湯機を示
す構成図
FIG. 12 is a configuration diagram illustrating a heat pump water heater according to a fifth embodiment of the present invention.

【図13】同ヒートポンプ給湯機の運転時間に対する給
水温度と減圧装置の弁開度と吐出圧力とを示すグラフ
FIG. 13 is a graph showing a feed water temperature, a valve opening degree of a pressure reducing device, and a discharge pressure with respect to an operation time of the heat pump water heater.

【図14】本発明の実施例6のヒートポンプ給湯機を示
す構成図
FIG. 14 is a configuration diagram showing a heat pump water heater according to Embodiment 6 of the present invention.

【図15】同ヒートポンプ給湯機の運転時間に対する給
水温度と減圧装置の弁開度と吐出圧力とを示すグラフ
FIG. 15 is a graph showing a feed water temperature, a valve opening degree of a pressure reducing device, and a discharge pressure with respect to an operation time of the heat pump water heater.

【図16】本発明の実施例7のヒートポンプ給湯機を示
す構成図
FIG. 16 is a configuration diagram showing a heat pump water heater according to a seventh embodiment of the present invention.

【図17】同ヒートポンプ給湯機の運転時間に対する給
水温度と流量調整弁の開度と流量と吐出圧力と減圧装置
の弁開度とを示すグラフ
FIG. 17 is a graph showing the feed water temperature, the opening degree of the flow control valve, the flow rate, the discharge pressure, and the opening degree of the pressure reducing device with respect to the operation time of the heat pump water heater.

【図18】本発明の実施例8のヒートポンプ給湯機を示
す構成図
FIG. 18 is a configuration diagram illustrating a heat pump water heater according to an eighth embodiment of the present invention.

【図19】同ヒートポンプ給湯機の運転時間に対する給
水温度と吐出圧力と減圧装置の弁開度とを示すグラフ
FIG. 19 is a graph showing a feed water temperature, a discharge pressure, and a valve opening degree of a pressure reducing device with respect to an operation time of the heat pump water heater.

【図20】本発明の実施例9のヒートポンプ給湯機を示
す構成図
FIG. 20 is a configuration diagram showing a heat pump water heater according to a ninth embodiment of the present invention.

【図21】同ヒートポンプ給湯機の運転時間に対する圧
縮機の運転状態と減圧装置の弁開度と吐出圧力と貯湯槽
の下部温度とを示すグラフ
FIG. 21 is a graph showing the operation state of the compressor, the valve opening degree of the pressure reducing device, the discharge pressure, and the lower temperature of the hot water tank with respect to the operation time of the heat pump water heater.

【図22】従来例におけるヒートポンプ給湯機を示す構
成図
FIG. 22 is a configuration diagram showing a heat pump water heater in a conventional example.

【図23】同ヒートポンプ給湯機の貯湯槽の温度分布を
示す説明図
FIG. 23 is an explanatory diagram showing a temperature distribution of a hot water storage tank of the heat pump water heater.

【図24】同ヒートポンプ給湯機の給水温度に対する吐
出圧力を示すグラフ
FIG. 24 is a graph showing discharge pressure with respect to feed water temperature of the heat pump water heater.

【符号の説明】[Explanation of symbols]

1 圧縮機 2 冷媒対水熱交換器 3 減圧装置 4 蒸発器 5 貯湯槽 6 循環ポンプ 10 流量制御手段 11 流量調整弁 12 制御手段 13 沸き上げ完了直前検出手段 DESCRIPTION OF SYMBOLS 1 Compressor 2 Refrigerant-water heat exchanger 3 Decompression device 4 Evaporator 5 Hot water storage tank 6 Circulation pump 10 Flow control means 11 Flow control valve 12 Control means 13 Detecting means just before completion of boiling

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 圧縮機、冷媒対水熱交換器、冷媒の流量
を制御する減圧装置、蒸発器を順次接続した冷媒循環回
路と、貯湯槽、循環ポンプ、前記冷媒対水熱交換器を順
次接続した給湯回路と、前記給湯回路において前記冷媒
対水熱交換器の水側出口水温である沸き上げ温度を一定
にするために前記冷媒対水熱交換器の水側入口と前記貯
湯槽との間に、または、前記冷媒対水熱交換器の水側出
口と前記貯湯槽との間に設けられた流量調節弁を制御す
る流量制御手段と、前記貯湯槽全体が沸き上がる直前を
検出する沸き上げ完了直前検出手段と、前記沸き上げ完
了直前検出手段からの信号が所定の信号になった時に前
記減圧装置の弁開度を変更する制御手段とを備えたヒー
トポンプ給湯機。
1. A refrigerant circuit in which a compressor, a refrigerant-to-water heat exchanger, a pressure reducing device for controlling the flow rate of refrigerant, and an evaporator are sequentially connected, a hot water tank, a circulation pump, and the refrigerant-water heat exchanger are sequentially arranged. A connected hot water supply circuit, and a water side inlet of the refrigerant / water heat exchanger and the hot water storage tank in order to make a boiling temperature that is a water side exit water temperature of the refrigerant / water heat exchanger in the hot water supply circuit constant. A flow control means for controlling a flow control valve provided between the water-side outlet of the refrigerant-to-water heat exchanger and the hot water storage tank, and a boiler for detecting immediately before the entire hot water storage tank is heated A heat pump water heater comprising: immediately before completion detection means; and control means for changing a valve opening of the pressure reducing device when a signal from the immediately before boiling completion detection means becomes a predetermined signal.
【請求項2】 減圧装置の弁開度の変更量は外気温度を
検出する外気温度検出手段から得た外気温度に応じて決
定する制御手段を備えたことを特徴とする請求項1記載
のヒートポンプ給湯機。
2. The heat pump according to claim 1, further comprising control means for determining the amount of change in the valve opening of the pressure reducing device in accordance with the outside air temperature obtained from the outside air temperature detecting means for detecting the outside air temperature. Water heater.
【請求項3】 沸き上げ完了直前検出手段として冷媒対
水熱交換器の水側入口水温である給水温度を検出する給
水温度検出手段を設け、前記給水温度検出手段が予め決
められた複数の給水温度を検出する毎に、減圧装置の弁
開度を開くように制御する制御手段を備えたことを特徴
とする請求項1記載のヒートポンプ給湯機。
3. A water supply temperature detection means for detecting a water supply temperature which is a water-side inlet water temperature of a refrigerant-to-water heat exchanger as a detection means immediately before the completion of boiling, wherein the water supply temperature detection means comprises a plurality of predetermined water supply waters. 2. The heat pump water heater according to claim 1, further comprising control means for controlling so as to open the valve opening of the pressure reducing device every time the temperature is detected.
【請求項4】 減圧装置の弁開度の変更量は、給水温度
が高いほど大きくしたことを特徴とする請求項3記載の
ヒートポンプ給湯機。
4. The heat pump water heater according to claim 3, wherein the amount of change of the valve opening of the pressure reducing device is increased as the water supply temperature is higher.
【請求項5】予め設定された時間間隔ごとに減圧装置の
弁開度を変更する制御手段を備えたことを特徴とする請
求項1記載のヒートポンプ給湯機。
5. The heat pump water heater according to claim 1, further comprising control means for changing a valve opening of the pressure reducing device at predetermined time intervals.
【請求項6】 減圧装置の弁開度の変更の時間間隔は、
沸き上げ完了に近づくほど小さくすることを特徴とする
請求項5記載のヒートポンプ給湯機。
6. The time interval for changing the valve opening of the pressure reducing device is as follows:
6. The heat pump water heater according to claim 5, wherein the heat pump water heater is reduced as the boiling is completed.
【請求項7】 沸き上げ完了直前検出手段として、流量
調整弁を通過する流量が最大流量になった時に、最大流
量になっている時間を計測する時間計測手段を備えたこ
とを特徴とする請求項1記載のヒートポンプ給湯機。
7. As a means for detecting immediately before the completion of boiling, a time measuring means for measuring a time during which the maximum flow rate is reached when the flow rate passing through the flow regulating valve reaches the maximum flow rate is provided. Item 2. The heat pump water heater according to item 1.
【請求項8】 沸き上げ完了直前検出手段として吐出圧
力を検出する吐出圧力検出手段を備えたことを特徴とす
る請求項1記載のヒートポンプ給湯機。
8. The heat pump water heater according to claim 1, further comprising a discharge pressure detecting means for detecting a discharge pressure as a means for detecting immediately before the completion of boiling.
【請求項9】 沸き上げ完了直前検出手段として貯湯槽
の下部温度を検出する貯湯槽温度検出手段を備えたこと
を特徴とする請求項1記載のヒートポンプ給湯機。
9. The heat pump water heater according to claim 1, further comprising a hot water tank temperature detecting means for detecting a lower temperature of the hot water tank as a means for detecting immediately before the completion of boiling.
JP2001149072A 2001-05-18 2001-05-18 Heat pump hot-water supplier Pending JP2002340440A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001149072A JP2002340440A (en) 2001-05-18 2001-05-18 Heat pump hot-water supplier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001149072A JP2002340440A (en) 2001-05-18 2001-05-18 Heat pump hot-water supplier

Publications (1)

Publication Number Publication Date
JP2002340440A true JP2002340440A (en) 2002-11-27

Family

ID=18994288

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001149072A Pending JP2002340440A (en) 2001-05-18 2001-05-18 Heat pump hot-water supplier

Country Status (1)

Country Link
JP (1) JP2002340440A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7127905B2 (en) 2003-12-19 2006-10-31 Carrier Corporation Vapor compression system startup method
US7458418B2 (en) 2003-01-13 2008-12-02 Carrier Corporation Storage tank for hot water systems
JP2009008379A (en) * 2007-05-25 2009-01-15 Denso Corp Refrigerating cycle device
JP2009121704A (en) * 2007-11-12 2009-06-04 Corona Corp Heat pump type water heater
JP2013160485A (en) * 2012-02-08 2013-08-19 Hitachi Appliances Inc Heat pump type liquid heating device
JP2016121818A (en) * 2014-12-24 2016-07-07 株式会社デンソー Control method of heat pump cycle, and heating system

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7458418B2 (en) 2003-01-13 2008-12-02 Carrier Corporation Storage tank for hot water systems
US7127905B2 (en) 2003-12-19 2006-10-31 Carrier Corporation Vapor compression system startup method
US7490481B2 (en) 2003-12-19 2009-02-17 Carrier Corporation Vapor compression system startup method
JP2009008379A (en) * 2007-05-25 2009-01-15 Denso Corp Refrigerating cycle device
JP4725592B2 (en) * 2007-05-25 2011-07-13 株式会社デンソー Refrigeration cycle equipment
JP2009121704A (en) * 2007-11-12 2009-06-04 Corona Corp Heat pump type water heater
JP2013160485A (en) * 2012-02-08 2013-08-19 Hitachi Appliances Inc Heat pump type liquid heating device
JP2016121818A (en) * 2014-12-24 2016-07-07 株式会社デンソー Control method of heat pump cycle, and heating system

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