JPH044512B2 - - Google Patents
Info
- Publication number
- JPH044512B2 JPH044512B2 JP15096585A JP15096585A JPH044512B2 JP H044512 B2 JPH044512 B2 JP H044512B2 JP 15096585 A JP15096585 A JP 15096585A JP 15096585 A JP15096585 A JP 15096585A JP H044512 B2 JPH044512 B2 JP H044512B2
- Authority
- JP
- Japan
- Prior art keywords
- hot water
- refrigerant
- water supply
- temperature
- heat exchanger
- 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.)
- Expired
Links
- 239000003507 refrigerant Substances 0.000 claims description 91
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 80
- 238000009835 boiling Methods 0.000 claims description 31
- 239000000203 mixture Substances 0.000 claims description 21
- 238000004378 air conditioning Methods 0.000 claims description 11
- 239000008236 heating water Substances 0.000 claims description 10
- 239000007788 liquid Substances 0.000 description 16
- 238000001816 cooling Methods 0.000 description 8
- 230000007423 decrease Effects 0.000 description 8
- 238000010586 diagram Methods 0.000 description 5
- 230000005855 radiation Effects 0.000 description 4
- 238000009833 condensation Methods 0.000 description 3
- 230000005494 condensation Effects 0.000 description 3
- 238000005057 refrigeration Methods 0.000 description 3
- 238000001514 detection method Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
Landscapes
- Domestic Hot-Water Supply Systems And Details Of Heating Systems (AREA)
- Central Air Conditioning (AREA)
- Steam Or Hot-Water Central Heating Systems (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
(産業上の利用分野)
本発明は冷暖房給湯機、詳しくは、室外側熱交
換器、室内側熱交換器及び給湯側熱交換器と圧縮
機とを切換機構を介して接続してなる冷媒回路
に、高沸点冷媒と低沸点冷媒との混合冷媒を封入
すると共に、循環冷媒の組成比を変更可能とする
手段を設けて、給湯運転時に、前記冷媒回路の循
環冷媒の組成比を変更し、該冷媒中の高沸点冷媒
の組成比を高くし(以下、高沸点冷媒リツチとい
う)給湯温度を高くできるようにした冷暖房給湯
機に関する。
(従来技術)
本出願人は、特願昭59−177189号において、こ
の種冷暖房給湯機(冷媒回路に関しては、本発明
に係る図面である第2図参照)を提案した。
しかして、第2図に示す冷暖房給湯機は、圧縮
機4への吸入冷媒の状態を、液管8に介装する電
動膨張弁9または10により湿り状態と過熱状態
とに変更制御して、前記吸入冷媒を湿り状態に制
御することにより、該冷媒中に残存する高沸点冷
媒リツチの未蒸発液冷媒を前記圧縮機4の流入側
に設ける気液分離器12に貯留し、また、逆に前
記吸入冷媒を過熱状態に制御することにより、前
記気液分離器12に貯留された高沸点冷媒リツチ
の液冷媒を蒸発させて循環回路に戻してやること
により、前記循環冷媒における高沸点冷媒と低沸
点冷媒との組成比を変更するようにしている。
尚、1は室外側熱交換器、2は室内側熱変換
器、3は給湯側熱交換器、7は四路切換弁からな
る冷媒回路の切換機構であり、また、一点鎖線矢
印ハは給湯サイクルを示している。
そして、給湯運転時においては、高温給湯を可
能とするために、循環冷媒の組成比を高沸点冷媒
リツチ側に調節して、比較的低い高圧圧力で凝縮
温度を高く設定できるようにしている。
ところで、所定容量の前記給湯側熱交換器3に
おいて、単位時間に一定の熱量を放熱させるに
は、前記熱交換器3内の凝縮冷媒と被加熱対象で
ある貯湯水との間にある温度以上の温度差が必要
である。
従つて、一般に、設定給湯温度を高くすると、
それだけ凝縮温度、従つて、凝縮圧力が上昇する
ことになる。
そこで、従来、設定給湯温度の上限値は、過負
荷運転を防止の観点から前記圧縮機4に定められ
ている許容高圧圧力(許容凝縮温度)と、所定の
放熱量により定まる前記所要温度差とを考慮して
設定していたのである。
換言すると、設定給湯温度の上限値は、前記許
容凝縮温度より前記所要温度差分だけ低い温度に
制限されていたのである。
(発明が解決しようとする問題点)
ところで、上記冷暖房給湯機において、冷媒回
路に、高沸点冷媒の組成比の高い混合冷媒を封入
してやれば、それだけ低い高圧圧力で高い給湯温
度から得られるのであるが、換言すると、前記設
定給湯温度の上限値を高くできるのであるが、か
くした場合にはその反面、冷房、暖房運転時の冷
凍能力が小さくなる欠点を生じるのである。
しかして、本発明は、所定容量の前記給湯側熱
交換器においても、単位時間に放熱させる放熱量
を少なくすれば、この放熱に必要な凝縮冷媒と貯
湯水との所要温度差もそれに応じて小さくなるこ
とに着目して発明したもので、その目的は、前記
設定給湯温度を高くする場合には、前記圧縮機の
能力を積極的に減少させて前記給湯熱交換器での
放熱量を少なくし、前記冷媒回路に殊更に高沸点
冷媒の組成比の高い混合冷媒を封入しなくても、
かつ、凝縮圧力を従来に比して高くすることな
く、給湯温度(設定給湯温度の上限値)を高くで
きるようにする点にある。
(問題点を解決するための手段)
本発明の構成を第1図及び第2図に基づいて説
明すると、室外側熱交換器1、室内側熱交換器2
及び給湯側熱交換器3と圧縮機4とを切換機構7
を介して接続して冷媒回路を形成し、この冷媒回
路に高沸点冷媒と低沸点冷媒との混合冷媒を封入
している。更に、液管8に介装する電動膨張弁
9,10の弁開度制御の変更により循環冷媒の組
成比を変更可能とし、給湯運転時には循環冷媒の
組成比を変更して、該冷媒中の高沸点冷媒の組成
比を高くする如くしている。
更に、前記圧縮機4に、該圧縮機4の部分容量
運転を可能とする容量制御手段を設ける一方、給
湯運転における設定給湯温度を高低に切換える切
換手段15、該切換手段15が高温側の設定給湯
温度に切換えられた時に、前記容量制御手段をオ
ン動作して前記圧縮機4を部分容量運転させる制
御手段とを設けたのである。
(作用)
給湯運転時であつて、前記切換手段15を高温
側の設定給湯温度側に切換えると、このことによ
つて、前記圧縮機4が部分容量運転させられるか
ら、冷凍能力が低下し、前記給湯側熱交換器での
放熱量が積極的に減少させられるのである。
このため、この減少した放熱量を放熱させるた
めに必要な凝縮冷媒と貯湯水との温度差も従来の
全容量運転時に比して減少するから、この所容温
度差の減少分だけ凝縮温度(高圧圧力)を上昇さ
せることなく、前記設定給湯温度の上限値を高く
設定できるのである。
(実施例)
第2図に示すものは、冷房、暖房、給湯及び冷
房給湯運転を可能とした冷暖房給湯機である。
即ち、室外側熱交換器1、室内側熱交換器2及
び給湯側熱交換器3と、圧縮機4とを、2個の第
1及び第2四路切換弁5,6から成る切換機構7
を介して接続して冷媒回路を形成している。
そして、この冷媒回路に高沸点冷媒R22と低
沸点冷媒R12とを混合してなる混合冷媒を封入
している。
更に、前記室外側熱交換器1と前記室内側熱交
換器2とを接続する被管8に、任意に弁開度制御
を行えるようにした第1及び第2電動膨張弁9,
10を介装する一方、前記圧縮機4の吸入ガス管
11に、吸入冷媒中の未蒸発液冷媒を分離して貯
留可能とした気液分離器12を介装している。
尚、13は受液器、14はアキユムレータであ
る。
かくして、前記切換機構7を切換操作して、実
線矢印イで示すごとく冷凍サイクルをロのごとく
形成することにより暖房運転を、一点鎖線矢印ハ
に示すごとく形成することにより給湯運転を、更
に、二点鎖線矢印ニのごとく形成することにより
冷房給湯運転を行えるようにしている。これと同
時に、各運転に応じて前記第1及び第2電動膨張
弁9,10のいずれか一方を第1表に示すごとく
通電して弁開度制御し、または非通電として開放
し、前記圧縮機4の吸入冷媒の過熱度を制御する
ごとくしている。
尚、前記切換機構7を各四路切換弁5,6は通
電により実線側に切換えられるもので、各運転時
における通電状態は前記第1表に示す通りであ
る。
(Industrial Application Field) The present invention relates to an air-conditioning/heating water heater, and more specifically, a refrigerant circuit formed by connecting an outdoor heat exchanger, an indoor heat exchanger, a hot water supply side heat exchanger, and a compressor via a switching mechanism. A mixed refrigerant of a high boiling point refrigerant and a low boiling point refrigerant is sealed in the refrigerant, and a means is provided for changing the composition ratio of the circulating refrigerant, so that the composition ratio of the circulating refrigerant in the refrigerant circuit is changed during hot water supply operation, The present invention relates to an air-conditioning/heating water heater in which the composition ratio of a high-boiling point refrigerant in the refrigerant is increased (hereinafter referred to as "high-boiling point refrigerant rich") to increase the hot water supply temperature. (Prior Art) The present applicant proposed this type of air-conditioning/heating water heater (for the refrigerant circuit, see FIG. 2, which is a drawing related to the present invention) in Japanese Patent Application No. 177189/1989. Thus, the air conditioning/heating water heater shown in FIG. 2 controls the state of the refrigerant sucked into the compressor 4 into a wet state and a superheated state by using an electric expansion valve 9 or 10 installed in the liquid pipe 8. By controlling the suction refrigerant to a wet state, the unevaporated liquid refrigerant rich in high boiling point refrigerant remaining in the refrigerant is stored in the gas-liquid separator 12 provided on the inflow side of the compressor 4, and vice versa. By controlling the suction refrigerant to a superheated state, the high boiling point refrigerant rich liquid refrigerant stored in the gas-liquid separator 12 is evaporated and returned to the circulation circuit, thereby separating the high boiling point refrigerant and the low boiling point refrigerant in the circulation refrigerant. The composition ratio with the boiling point refrigerant is changed. In addition, 1 is an outdoor heat exchanger, 2 is an indoor heat exchanger, 3 is a hot water supply side heat exchanger, 7 is a refrigerant circuit switching mechanism consisting of a four-way switching valve, and the dashed line arrow C is a hot water supply side heat exchanger. It shows the cycle. During hot water supply operation, in order to enable high temperature hot water supply, the composition ratio of the circulating refrigerant is adjusted to be rich in high boiling point refrigerant, so that the condensing temperature can be set high at a relatively low high pressure. By the way, in order to radiate a constant amount of heat per unit time in the hot water supply side heat exchanger 3 having a predetermined capacity, the temperature must be higher than a temperature between the condensed refrigerant in the heat exchanger 3 and the stored hot water to be heated. temperature difference is required. Therefore, in general, if the set hot water temperature is increased,
The condensing temperature and therefore the condensing pressure will increase accordingly. Therefore, conventionally, the upper limit value of the set hot water supply temperature is determined by the allowable high pressure (allowable condensing temperature) set for the compressor 4 from the viewpoint of preventing overload operation and the required temperature difference determined by the predetermined amount of heat radiation. It was set with this in mind. In other words, the upper limit value of the set hot water supply temperature is limited to a temperature lower than the allowable condensing temperature by the required temperature difference. (Problems to be Solved by the Invention) By the way, in the above-mentioned air-conditioning/heating water heater, if a mixed refrigerant with a high composition ratio of high boiling point refrigerant is filled in the refrigerant circuit, a high hot water temperature can be obtained at a lower high pressure. However, in other words, the upper limit value of the set hot water supply temperature can be increased, but in this case, on the other hand, there is a drawback that the refrigerating capacity during cooling and heating operations becomes smaller. Therefore, even in the hot water supply side heat exchanger having a predetermined capacity, if the amount of heat radiated per unit time is reduced, the required temperature difference between the condensed refrigerant and the stored hot water required for this heat radiation will be reduced accordingly. This was invented with a focus on reducing the heat exchanger's size, and its purpose is to actively reduce the capacity of the compressor to reduce the amount of heat released by the hot water heat exchanger when the set hot water temperature is increased. However, even if the refrigerant circuit is not particularly filled with a mixed refrigerant having a high composition ratio of high boiling point refrigerants,
Another point is that the hot water supply temperature (the upper limit value of the set hot water supply temperature) can be increased without increasing the condensing pressure higher than in the past. (Means for Solving the Problems) The configuration of the present invention will be explained based on FIGS. 1 and 2. The outdoor heat exchanger 1, the indoor heat exchanger 2
and a mechanism 7 for switching between the hot water supply side heat exchanger 3 and the compressor 4
are connected to form a refrigerant circuit, and a mixed refrigerant of a high boiling point refrigerant and a low boiling point refrigerant is sealed in this refrigerant circuit. Furthermore, the composition ratio of the circulating refrigerant can be changed by changing the valve opening control of the electric expansion valves 9 and 10 installed in the liquid pipe 8. During hot water supply operation, the composition ratio of the circulating refrigerant can be changed to The composition ratio of the high boiling point refrigerant is increased. Furthermore, the compressor 4 is provided with a capacity control means that enables partial capacity operation of the compressor 4, and a switching means 15 that switches the set hot water temperature during hot water supply operation between high and low, and the switching means 15 is set on the high temperature side. A control means is provided which turns on the capacity control means and causes the compressor 4 to operate at a partial capacity when the temperature is changed to the hot water supply temperature. (Function) During hot water supply operation, when the switching means 15 is switched to the high temperature set hot water supply temperature side, the compressor 4 is thereby operated at partial capacity, so that the refrigerating capacity is reduced. The amount of heat released by the hot water supply side heat exchanger is actively reduced. Therefore, the temperature difference between the condensed refrigerant and the stored hot water, which is necessary to radiate this reduced amount of heat radiation, is also reduced compared to the conventional full capacity operation, so the condensation temperature ( The upper limit value of the set hot water supply temperature can be set high without increasing the high pressure (high pressure). (Example) What is shown in FIG. 2 is an air-conditioning/heating water heater that is capable of cooling, heating, hot water supply, and cooling hot water supply operations. That is, the outdoor heat exchanger 1, the indoor heat exchanger 2, the hot water supply side heat exchanger 3, and the compressor 4 are connected to each other by a switching mechanism 7 consisting of two first and second four-way switching valves 5 and 6.
are connected to form a refrigerant circuit. A mixed refrigerant formed by mixing a high boiling point refrigerant R22 and a low boiling point refrigerant R12 is sealed in this refrigerant circuit. Further, first and second electric expansion valves 9, which can arbitrarily control the valve opening degree, are provided in the tube sheath 8 connecting the outdoor heat exchanger 1 and the indoor heat exchanger 2.
On the other hand, a gas-liquid separator 12 is installed in the suction gas pipe 11 of the compressor 4, which is capable of separating and storing unevaporated liquid refrigerant in the suction refrigerant. In addition, 13 is a liquid receiver, and 14 is an accumulator. Thus, by switching the switching mechanism 7, the refrigeration cycle is formed as shown by the solid line arrow A, as shown in B, and the hot water supply operation is formed as shown in the dashed line arrow C. By forming it as shown by the dotted chain arrow D, cooling hot water supply operation can be performed. At the same time, depending on each operation, one of the first and second electric expansion valves 9, 10 is energized as shown in Table 1 to control the valve opening, or is de-energized and opened to The degree of superheating of the refrigerant sucked into the machine 4 is controlled. The four-way switching valves 5 and 6 of the switching mechanism 7 are switched to the solid line side by energization, and the energization state during each operation is as shown in Table 1 above.
【表】
更に、前記冷媒回路の循環混合冷媒の組成比を
後記するごとく変更可能として、冷暖房運転時に
おいては、循環冷媒中の高沸点冷媒の組成比を高
低に変更して、冷凍能力を大小に変更制御する一
方、給湯運転時には循環冷媒中の高沸点冷媒の組
成比を高くして、高圧圧力に対する凝縮温度を高
く、従つて、温度の高い給湯が行えるようにして
いる(尚、この場合冷凍能力は低下する)。
以下、冷房運転時における能力調整について説
明すると、冷凍能力を大きくする場合には、前記
第1電動膨張弁9の弁開度を前記吸入冷媒が湿り
状態となるように開きぎみに制御するのであつ
て、かくすると前記吸入ガス管11を流通する吸
入冷媒に残存する高沸点冷媒リツチの未蒸発液冷
媒が前記気液分離器12で分離されて該分離器1
2に貯留されていくのである。
このようにして高沸点冷媒リツチの液冷媒が前
記気液分離器12に貯留されていくと、循環冷媒
中の高沸点冷媒の組成比が低下し、換言すると、
低沸点冷媒の組成比が上昇するので能力が増大す
るのである。
また、前記第1電動膨張弁9の弁開度を前記吸
入冷媒が過熱状態となるように制御すると、前記
気液分離12に貯留されていた高沸点冷媒リツチ
の液冷媒が前記吸入冷媒に蒸発していき、前記気
液分離器12から放出されるので、循環冷媒中の
高沸点冷媒の組成比が再び上昇して能力が低下す
るのである。
一方、給湯、または、冷房給湯運転時には、前
記第2または第1電動膨張弁10,9を、前記吸
入冷媒が過熱状態となるように制御して、前記冷
房運転時における能力低下時と同様に循環冷媒中
の高沸点冷媒の組成比を高くするのである。かく
すると、冷凍能力は低下するが、高圧圧力に対す
る凝縮温度が高くなり、従つて、高温給湯が可能
となるのである。
以上のごとく構成する冷暖房給湯機において、
前記圧縮機4に容量を2段階に調節可能とした容
量制御手段を設けると共に、
前記設定給湯温度を高低に切換える切換手段1
5(第3図参照)と、
給湯または冷房給湯運転時に前記切換手段15
の信号を入力して、前記容量制御手段を動作させ
て前記圧縮機1を部分容量運転させる制御手段と
を設けるのである。
前記圧縮機4はステーシヨナリーベーン形の回
転圧縮機で、前記容量制御手段を次のようにして
設けている。即ち、シリンダ(図示せず)に、吸
入側にバイパス通路41を介して連通する中間吐
出孔42を開口すると共に、該中間吐出孔42を
開閉する中間吐出弁43を設ける一方、この中間
吐出弁43の背面側に高圧または低圧ガスを作用
させて、該弁43を開閉動作させる3方電磁弁4
4を設けている。
かくして、前記3方電磁弁44への通電を遮断
して、前記中間吐出弁43の背面に高圧を作用さ
せることによつて、前記中間吐出孔42を閉鎖し
て全容量運転し、また、前記3方電磁弁44に通
電して、前記中間吐出弁43の背面に低圧を作用
させると、該弁43がリターンばね45により開
動作して、部分容量運転が行えるようにしてい
る。
また、前記圧縮機4には、過負荷運転防止用の
高圧制御スイツチ(図示せず)を設けており、高
圧圧力が設定圧力に達すると前記圧縮機4を停止
するようにしている。従つて、凝縮温度の上限は
前記設定圧力に対応したい凝縮温度の上限は前記
設定圧力に対応した凝縮温度tpに制限されてい
る。
また、前記切換手段は後記するマイクロコンピ
ユータの入力側に接続するスイツチ15からなる
ものである。
更に、前記制御手段は前記マイクロコンピユー
タに組込むプログラムにより達成するものであ
る。
以下、電気回路につい概略説明すると、マイク
ロコンピユータCの入力側に、運転モードを切換
える運転モード選択手段16と、前記切換スイツ
チ15とを接続する一方、
前記マイクロコンピユータCの出力側には、前
記容量制御手段の前記3方電磁弁44、前記各四
路切換弁5,6及び前記各電動膨張弁9,10を
接続している。
尚、給湯運転時には前記したごとく設定給湯温
度を高低に切換えられるようにしているが、これ
ら高温側の設定給湯温度及び低温側の設定給湯温
度はいずれも前記マイクロコンピユータのROM
に予めインプツトされている。
尚、図示していないが、前記給湯側熱交換器3
側には貯湯水の温度を検出する検出手段を設けて
おり、該検出手段による検出温度と前記設定給湯
温度とを基に、前記マイクロコンピユータによ
り、前記圧縮機1を発停制御するようにしてい
る。
次に、上記冷暖房給湯機の給湯運転について説
明する。
前記運転モード選択手段16により給湯運転を
選択すると、前記第1及び第2四路切換弁5,6
が切換えられて第2図に示す給湯サイクルが形成
されると同時に、前記第1電動膨張弁9が前記吸
入冷媒を過熱状態とするように制御される。この
結果、循環冷媒が高沸点冷媒リツチ(封入当初)
の組成比となり、低い高圧圧力で高い凝縮温度が
得られるのである。即ち、全体に高温の給湯水が
得られるのである。
しかして、前記切換スイツチ15を低温側の設
定給湯温度t1側に切換えると、前記3方電磁弁
44の通電が遮断されて、前記中間吐出弁43の
背面に高圧が作用して前記中間吐出孔42が閉鎖
され、前記圧縮機4が全容量運転されるのであ
る。
この結果、第4図に示すように、前記給湯側熱
交換器3における放熱量が前記圧縮機4の全容量
運転に見合う大熱量Q1となるのである。かくし
て、大きな放熱量で迅速に貯湯水を加熱できるの
であり、この貯湯水が前記低温側設定給湯温度t
1に達すると、前記圧縮機1が停止されるのであ
る。
一方、前記切換スイツチ15を高温側の設定給
湯温度t2側に切換えると、前記3方電磁弁44
が励磁されて、前記中間吐出弁43が開放され、
前記圧縮機1が部分容量運転に切換えられるので
ある。
そうすると、前記圧縮機1の能力が低下するか
ら、それに応じて前記給湯側熱交換器3での放熱
量も減少するのである(熱量Q2)。かくして、
この熱量Q2を単位時間に放熱するために必要な
凝縮冷媒と前記貯湯水との温度差Δt2は、放熱
量がQ1の場合の所要温度差Δt1よりも小さく
なるのである。
このよう前記所要温度差が小さくなるから、高
温側設定給湯温度t2の設定上限温度を低温側設
定給湯温度t1に対して、(t1−t2)だけ高
く設定できるのである。換言すると、高温側設定
給湯温度(t1)を(t1−t2)だけ前記圧縮
機4の高圧制御に規定されて定まる上限の前記凝
縮温度t0に近付けて高温側に設定することがで
きるのである。
かくして、給湯能力は低下するが、従来に比し
て更に高温の給湯が行えるのである。
尚、この場合も、貯湯水の温度が前記設定給湯
温度t2に達すると、前記圧縮機4は停止され
る。
尚、上記実施例においては、前記制御手段をマ
イクロコンピユータを用いて構成したが、第5図
に示すように、サーモスタツトから成る前記切換
スイツチ15の高温側切換接点aに、高温側設定
給湯温度で動作するサーモスタツト30と前記圧
縮機4駆動用の電磁開閉器31との直列回路と、
前記3方電磁弁44のとの並列回路を接続する一
方、
前記切換スイツチ15の低温側切換接点bに、
低温側接点温度で動作するサーモスタツト32と
前記電磁開閉器31との直列回路に接続するごと
くして、シーケンス回路により構成してもよい。
また、循環冷媒の組成比を変更するための手段
は上記した実施例のものに限定されるものではな
い。
また、前記圧縮機4は回転圧縮機に限ることな
くあらゆるタイプの圧縮機を用いるこができる。
また、容量制御手段も前記した手段に限られるも
のではない。
(発明の効果)
以上のごとく、本発明においては、給湯運転時
に、高温給湯を行う場合には積極的に前記圧縮機
4の能力を低下させて、前記給湯側熱交換器での
放熱量を減少させるようにしたから、冷媒回路に
封入する混合冷媒に高沸点冷媒の組成比が殊更に
高いものを用いなくても、設定給湯温度をより高
く設定でき、従来に比してより温度の高い給湯が
行えるのである。[Table] Furthermore, the composition ratio of the circulating mixed refrigerant in the refrigerant circuit can be changed as described below, and during air conditioning operation, the composition ratio of the high boiling point refrigerant in the circulating refrigerant can be changed to a higher or lower value to increase or decrease the refrigerating capacity. At the same time, during hot water supply operation, the composition ratio of the high boiling point refrigerant in the circulating refrigerant is increased to increase the condensation temperature for high pressure, and therefore hot water can be supplied at a high temperature (in this case, refrigeration capacity will decrease). In the following, capacity adjustment during cooling operation will be explained. When increasing the refrigeration capacity, the valve opening degree of the first electric expansion valve 9 is controlled to be as small as possible so that the suction refrigerant becomes wet. In this way, the unevaporated liquid refrigerant rich in high-boiling point refrigerant remaining in the suction refrigerant flowing through the suction gas pipe 11 is separated by the gas-liquid separator 12 and transferred to the separator 1.
It will be stored in 2. As the liquid refrigerant rich in high boiling point refrigerant is stored in the gas-liquid separator 12 in this way, the composition ratio of the high boiling point refrigerant in the circulating refrigerant decreases, in other words,
The capacity increases because the composition ratio of the low boiling point refrigerant increases. Furthermore, when the valve opening degree of the first electric expansion valve 9 is controlled so that the suction refrigerant is in a superheated state, the high boiling point refrigerant-rich liquid refrigerant stored in the gas-liquid separator 12 evaporates into the suction refrigerant. Then, as the refrigerant is discharged from the gas-liquid separator 12, the composition ratio of the high-boiling refrigerant in the circulating refrigerant rises again, and the capacity decreases. On the other hand, during hot water supply or cooling hot water supply operation, the second or first electric expansion valve 10, 9 is controlled so that the suction refrigerant is in a superheated state, similar to when the capacity decreases during the cooling operation. The composition ratio of the high boiling point refrigerant in the circulating refrigerant is increased. In this way, although the refrigerating capacity decreases, the condensing temperature for high pressure increases, and therefore high temperature hot water supply becomes possible. In the air conditioning/heating water heater configured as above,
The compressor 4 is provided with a capacity control means capable of adjusting the capacity in two stages, and a switching means 1 for switching the set hot water supply temperature between high and low.
5 (see Figure 3), and the switching means 15 during hot water supply or cooling hot water supply operation.
A control means is provided which inputs a signal to operate the capacity control means and cause the compressor 1 to operate at a partial capacity. The compressor 4 is a stationary vane type rotary compressor, and the capacity control means is provided as follows. That is, a cylinder (not shown) is provided with an intermediate discharge hole 42 that communicates with the suction side via a bypass passage 41, and an intermediate discharge valve 43 that opens and closes the intermediate discharge hole 42. A three-way solenoid valve 4 that opens and closes the valve 43 by applying high pressure or low pressure gas to the back side of the valve 43.
There are 4. Thus, by cutting off the power to the three-way solenoid valve 44 and applying high pressure to the back surface of the intermediate discharge valve 43, the intermediate discharge hole 42 is closed and full capacity operation is performed. When the three-way solenoid valve 44 is energized to apply low pressure to the back surface of the intermediate discharge valve 43, the valve 43 is opened by the return spring 45, allowing partial capacity operation. Further, the compressor 4 is provided with a high pressure control switch (not shown) for preventing overload operation, and the compressor 4 is stopped when the high pressure reaches a set pressure. Therefore, the upper limit of the condensing temperature is limited to the condensing temperature t p corresponding to the set pressure. Further, the switching means comprises a switch 15 connected to the input side of a microcomputer to be described later. Furthermore, the control means is achieved by a program built into the microcomputer. Hereinafter, the electric circuit will be briefly explained. On the input side of the microcomputer C, an operation mode selection means 16 for switching the operation mode and the changeover switch 15 are connected, while on the output side of the microcomputer C, the above-mentioned capacitor is connected. The three-way solenoid valve 44, the four-way switching valves 5 and 6, and the electric expansion valves 9 and 10 of the control means are connected. During the hot water supply operation, the hot water supply temperature setting can be switched between high and low as described above, and both the hot water temperature setting on the high temperature side and the setting hot water temperature on the low temperature side are stored in the ROM of the microcomputer.
has been input in advance. Although not shown, the hot water supply side heat exchanger 3
A detection means for detecting the temperature of the stored hot water is provided on the side, and the microcomputer controls the start/stop of the compressor 1 based on the temperature detected by the detection means and the set hot water supply temperature. There is. Next, the hot water supply operation of the above-mentioned air conditioning/heating water heater will be explained. When hot water supply operation is selected by the operation mode selection means 16, the first and second four-way switching valves 5, 6
is switched to form the hot water supply cycle shown in FIG. 2, and at the same time, the first electric expansion valve 9 is controlled to bring the suction refrigerant into a superheated state. As a result, the circulating refrigerant is rich in high boiling point refrigerants (at the time of initial injection).
Therefore, a high condensation temperature can be obtained at a low high pressure. In other words, high-temperature hot water can be obtained throughout. When the changeover switch 15 is switched to the low temperature set water supply temperature t1 side, the energization of the three-way solenoid valve 44 is cut off, and high pressure acts on the back surface of the intermediate discharge valve 43, causing the intermediate discharge hole to 42 is closed and the compressor 4 is operated at full capacity. As a result, as shown in FIG. 4, the amount of heat released in the hot water supply side heat exchanger 3 becomes a large amount of heat Q1 corresponding to the full capacity operation of the compressor 4. In this way, the stored hot water can be quickly heated with a large amount of heat radiation, and this stored hot water reaches the set hot water temperature t on the low-temperature side.
When it reaches 1, the compressor 1 is stopped. On the other hand, when the changeover switch 15 is switched to the set hot water temperature t2 side, which is the high temperature side, the three-way solenoid valve 44
is excited and the intermediate discharge valve 43 is opened,
The compressor 1 is then switched to partial capacity operation. Then, since the capacity of the compressor 1 decreases, the amount of heat released by the hot water supply side heat exchanger 3 also decreases accordingly (amount of heat Q2). Thus,
The temperature difference Δt2 between the condensed refrigerant and the stored hot water required to radiate this amount of heat Q2 per unit time is smaller than the required temperature difference Δt1 when the amount of heat radiated is Q1. Since the required temperature difference is reduced in this manner, the upper limit temperature of the hot water supply temperature t2 set on the high temperature side can be set higher by (t1 - t2) than the set water supply temperature t1 on the low temperature side. In other words, the hot water supply temperature (t1) set on the high temperature side can be set on the high temperature side by (t1 - t2) closer to the upper limit condensing temperature t0 determined by the high pressure control of the compressor 4. Thus, although the hot water supply capacity is reduced, it is possible to supply hot water at a higher temperature than in the past. In this case as well, when the temperature of the stored hot water reaches the set hot water supply temperature t2, the compressor 4 is stopped. In the above embodiment, the control means is configured using a microcomputer, but as shown in FIG. a series circuit of a thermostat 30 operating at 1 and an electromagnetic switch 31 for driving the compressor 4;
While connecting the parallel circuit with the three-way solenoid valve 44, to the low temperature side switching contact b of the switching switch 15,
The thermostat 32, which operates at a low temperature side contact temperature, and the electromagnetic switch 31 may be connected in a series circuit to form a sequence circuit. Further, the means for changing the composition ratio of the circulating refrigerant is not limited to those of the above-described embodiments. Moreover, the compressor 4 is not limited to a rotary compressor, and any type of compressor can be used.
Further, the capacity control means is not limited to the above-mentioned means. (Effects of the Invention) As described above, in the present invention, when high-temperature hot water is being supplied during hot water supply operation, the capacity of the compressor 4 is actively reduced to reduce the amount of heat released by the hot water supply side heat exchanger. Since the temperature is reduced, the set hot water temperature can be set higher without using a mixed refrigerant with a particularly high composition ratio of high boiling point refrigerant sealed in the refrigerant circuit, and the temperature is higher than before. Hot water can be supplied.
第1図〜第4図は本発明の一実施例の説明図
で、第1図はクレーム対応図、第2図は冷媒回路
図、第3図は電気回路図、第4図は運転状態説明
図、第5図は他の実施例の電気回路図である。
1……室外側熱交換器、2……室内側熱交換
器、3……給湯側熱交換器、4……圧縮機、7…
…切換機構、15……切換スイツチ。
Figures 1 to 4 are explanatory diagrams of one embodiment of the present invention, where Figure 1 is a complaint response diagram, Figure 2 is a refrigerant circuit diagram, Figure 3 is an electric circuit diagram, and Figure 4 is an explanation of operating conditions. 5 are electrical circuit diagrams of other embodiments. 1...Outdoor heat exchanger, 2...Indoor heat exchanger, 3...Hot water supply side heat exchanger, 4...Compressor, 7...
...Switching mechanism, 15...Switching switch.
Claims (1)
湯側熱交換器3と圧縮機4とを切換機構7を介し
て接続してなる冷媒回路に、高沸点冷媒と低沸点
冷媒との混合冷媒を封入し、給湯運転時に、循環
冷媒の組成比を変更して、該冷媒中の高沸点冷媒
の組成比を高くする如くした冷暖房給湯機であつ
て、前記圧縮機4に、該圧縮機4の部分容量運転
を可能とする容量制御手段を設ける一方、給湯運
転における設定給湯温度を高低に切換える切換手
段15と、該切換手段15が高温側の設定給湯温
度に切換えられた時に、前記容量制御手段をオン
動作して前記圧縮機4を部分容量運転させる制御
手段とを設けたことを特徴とする冷暖房給湯機。1 A refrigerant circuit formed by connecting an outdoor heat exchanger 1, an indoor heat exchanger 2, a hot water supply side heat exchanger 3, and a compressor 4 via a switching mechanism 7 has a high boiling point refrigerant and a low boiling point refrigerant. An air conditioning/heating water heater in which a mixed refrigerant is sealed and the composition ratio of the circulating refrigerant is changed during hot water supply operation to increase the composition ratio of a high boiling point refrigerant in the refrigerant. A capacity control means that enables partial capacity operation of the machine 4 is provided, and a switching means 15 is provided for switching the set hot water supply temperature during hot water supply operation between high and low, and when the switching means 15 is switched to the set hot water temperature on the high temperature side, the above-mentioned An air-conditioning/heating water heater characterized by comprising: a control means for turning on a capacity control means to cause the compressor 4 to operate at a partial capacity.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15096585A JPS6210570A (en) | 1985-07-08 | 1985-07-08 | Air conditioning/heating water heater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15096585A JPS6210570A (en) | 1985-07-08 | 1985-07-08 | Air conditioning/heating water heater |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6210570A JPS6210570A (en) | 1987-01-19 |
| JPH044512B2 true JPH044512B2 (en) | 1992-01-28 |
Family
ID=15508307
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15096585A Granted JPS6210570A (en) | 1985-07-08 | 1985-07-08 | Air conditioning/heating water heater |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6210570A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6383610B2 (en) * | 2014-09-01 | 2018-08-29 | リンナイ株式会社 | Heat pump system |
| JP6357389B2 (en) * | 2014-09-01 | 2018-07-11 | リンナイ株式会社 | Heat pump system |
| JP6389703B2 (en) * | 2014-09-01 | 2018-09-12 | リンナイ株式会社 | Heat pump system |
-
1985
- 1985-07-08 JP JP15096585A patent/JPS6210570A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6210570A (en) | 1987-01-19 |
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