JPH0373793B2 - - Google Patents
Info
- Publication number
- JPH0373793B2 JPH0373793B2 JP61160538A JP16053886A JPH0373793B2 JP H0373793 B2 JPH0373793 B2 JP H0373793B2 JP 61160538 A JP61160538 A JP 61160538A JP 16053886 A JP16053886 A JP 16053886A JP H0373793 B2 JPH0373793 B2 JP H0373793B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- refrigerant
- hot water
- compressor
- water supply
- 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 - Lifetime
Links
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- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Description
【発明の詳細な説明】
(産業上の利用分野)
この発明は、空調及び給湯機能を有するヒート
ポンプシステムに関するものである。DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to a heat pump system having air conditioning and hot water supply functions.
(従来の技術)
異なる負荷の冷凍サイクルを一装置内に有する
ヒートポンプシステムにおいて、各冷凍サイクル
時のそれぞれの効率を向上する具体的な方式とし
て、例えば、特開昭60−162159号公報には、冷・
暖房兼用の空気調和機において、冷房時と暖房時
との冷媒量を可変する装置が示されている。第3
図に上記装置の冷媒回路図を示しており、同図に
おいて、圧縮機41は冷暖切換えのための四路切
換弁42に接続され、この四路切換弁42に室内
熱交換器43、膨張弁44、室外熱交換器45が
順次配管接続されている。そして、上記四路切換
弁42と室内熱交換器43とを接続する配管に、
冷凍器油46を入れた容器47が介設されてい
る。上記装置は、冷凍機油に対する溶解度が、圧
力と温度により異なる混合冷媒を使用して、循環
冷媒量を変化させようとするものであり、図中実
線矢印方向に冷媒を循環させる室内暖房運転時に
は、圧縮機41から吐出される高温高圧のガス冷
媒は、まず上記容器47内に流入し、その後室内
熱交換器43、膨張弁44、室外熱交換器45と
循環する。一方、図中破線矢印方向に冷媒を循環
させる室内冷房運転時には、上記容器47へは、
室内熱交換器45を経由して低温低圧となつたガ
ス冷媒が流入するのである。このとき、例えば冷
凍機油としてスニソ(SUNISO)4GS(商品名)
を用い、冷媒としてR13B1とR12との非共沸混合
冷媒を用いた場合、スニソ4GSに対する溶解度
は、高温高圧時には、R13B1は小さく、R12は大
きなものであるため、R12がスニソ4GSに多く溶
け込み、したがつて、循環冷媒は低沸点冷媒であ
るR13B1濃度の高い組成となる。一方、低温低
圧時には、R13B1とR12との溶解度に高温高圧時
程の差はなくなり、循環冷媒は高沸点冷媒である
R12の特性が強い混合冷媒となるのである。一般
に、低沸点冷媒ほど圧縮機の吸入比容積が小さく
なつて冷媒循環量が多くなり、能力が増加してく
ることから、暖房運転時には低沸点冷媒R13B1
の多い冷媒組成となつて暖房能力を上昇し、一
方、冷房運転時には高沸点冷媒R12の作用によつ
て冷房能力を減少することにより、各冷暖運転時
の効率を向上しようとするものである。(Prior Art) In a heat pump system having refrigeration cycles with different loads in one device, as a specific method for improving the efficiency of each refrigeration cycle, for example, Japanese Patent Application Laid-Open No. 162159/1982 discloses cold·
In an air conditioner for both heating and heating, a device is shown that varies the amount of refrigerant during cooling and heating. Third
The figure shows a refrigerant circuit diagram of the above device. In the figure, a compressor 41 is connected to a four-way switching valve 42 for switching between cooling and heating, and an indoor heat exchanger 43 and an expansion valve are connected to the four-way switching valve 42. 44 and an outdoor heat exchanger 45 are sequentially connected by piping. Then, in the piping connecting the four-way switching valve 42 and the indoor heat exchanger 43,
A container 47 containing refrigerator oil 46 is interposed. The above device attempts to change the amount of circulating refrigerant by using a mixed refrigerant whose solubility in refrigeration oil varies depending on pressure and temperature.During indoor heating operation in which the refrigerant is circulated in the direction of the solid arrow in the figure, The high-temperature, high-pressure gas refrigerant discharged from the compressor 41 first flows into the container 47, and then circulates through the indoor heat exchanger 43, the expansion valve 44, and the outdoor heat exchanger 45. On the other hand, during indoor cooling operation in which the refrigerant is circulated in the direction of the dashed arrow in the figure, the refrigerant flows into the container 47.
The low-temperature, low-pressure gas refrigerant flows through the indoor heat exchanger 45. At this time, for example, SUNISO 4GS (trade name) is used as refrigerating machine oil.
When using a non-azeotropic mixed refrigerant of R13B1 and R12 as a refrigerant, the solubility in Suniso 4GS is that at high temperature and high pressure, R13B1 is small and R12 is large, so R12 dissolves in a large amount in Suniso 4GS, Therefore, the circulating refrigerant has a composition with a high concentration of R13B1, which is a low boiling point refrigerant. On the other hand, at low temperature and low pressure, the difference in solubility between R13B1 and R12 disappears compared to at high temperature and high pressure, and the circulating refrigerant is a high boiling point refrigerant.
This results in a mixed refrigerant with strong R12 characteristics. In general, the lower the boiling point refrigerant, the smaller the compressor's suction specific volume, the larger the refrigerant circulation amount, and the higher the capacity.
The refrigerant composition has a high refrigerant composition, increasing the heating capacity, while during cooling operation, the cooling capacity is reduced by the action of the high boiling point refrigerant R12, thereby improving efficiency during each cooling/heating operation.
(発明が解決しようとする問題点)
ところで、最近は、上記の様な空調機能と共
に、貯湯槽の中に熱交換器を設置して湯を加熱す
る給湯機能をも有するヒートポンプシステムが現
れており、この場合、空調冷凍サイクルに適合し
た冷媒量及び冷媒種のままで給湯サイクルに切換
えると、圧縮機の吐出圧力が異常に昇圧するとい
う問題があつた。それは、貯湯槽内の湯温の上昇
と共に凝縮器として作用する給湯熱交換器での熱
交換量が低下し、このことによつて、凝縮温度の
上昇、すなわち凝縮圧力の増加が生じるためであ
る。そこで、空調サイクル時の冷媒種よりも、液
化し易い高沸点冷媒種に切り換えることにより上
記のような異常発生の防止が可能となる。しかし
ながら、上記異常昇圧の発生は、貯湯槽の湯温が
ある程度上昇している場合には、給湯サイクルへ
の切換え後短時間のうちに生ずる現象であるの
で、これを防止するためには、上記冷媒種の切換
えが迅速になされることが必要である。前記の従
来装置においては、冷凍機油への冷媒の溶解度を
利用して冷媒組成を可変するものであるが、所要
の冷媒組成に達する迄には長時間を要するもので
ある。それは、冷凍機油46の入つた容器47内
に流入するガス冷媒の溶け込み或いは放出は、上
記冷媒機油46の液面を介して行なわれ、したが
つて、平衡状態に達する迄の時間は、ガス相及び
液中の濃度差による拡散速度に依存するからであ
る。さらに、所定の溶解量を得るためには、冷凍
機油46がその溶解度を与え得る温度になつてい
ることが必要であるが、容器47及び冷凍機油4
6はそれ自体熱容量を有し、したがつて、例えば
暖房から冷房に切換えた場合に、高温にあつた容
器47と冷凍機油46とが、これに流入してくる
低温のガス冷媒によつて所定の低温状態になる迄
には長時間を要するからである。(Problems to be Solved by the Invention) Recently, heat pump systems have appeared that have not only the above-mentioned air conditioning function but also a hot water supply function that heats hot water by installing a heat exchanger in a hot water storage tank. In this case, when switching to the hot water supply cycle with the amount and type of refrigerant that are compatible with the air conditioning refrigeration cycle, there was a problem that the discharge pressure of the compressor would abnormally increase. This is because as the water temperature in the hot water storage tank rises, the amount of heat exchanged in the hot water heat exchanger, which acts as a condenser, decreases, resulting in an increase in the condensing temperature and therefore the condensing pressure. . Therefore, by switching to a refrigerant with a higher boiling point that is more likely to liquefy than the refrigerant used during the air conditioning cycle, it is possible to prevent the above-mentioned abnormalities from occurring. However, the occurrence of the abnormal pressure increase described above occurs within a short time after switching to the hot water supply cycle if the water temperature in the hot water storage tank has risen to a certain extent, so in order to prevent this, the above It is necessary to quickly change the type of refrigerant. In the conventional apparatus described above, the refrigerant composition is varied by utilizing the solubility of the refrigerant in the refrigerating machine oil, but it takes a long time to reach the desired refrigerant composition. This is because the gas refrigerant flowing into the container 47 containing the refrigerant oil 46 is dissolved or released through the liquid level of the refrigerant oil 46, and therefore the time required to reach an equilibrium state is the gas phase. This is because it depends on the diffusion rate due to the difference in concentration in the liquid. Furthermore, in order to obtain a predetermined amount of dissolution, it is necessary that the refrigerating machine oil 46 is at a temperature that can provide the solubility.
6 itself has a heat capacity. Therefore, when switching from heating to cooling, for example, the container 47 and the refrigerating machine oil 46, which are at a high temperature, are heated to a predetermined level by the low temperature gas refrigerant flowing into them. This is because it takes a long time to reach the low temperature state.
この発明は、上記した点に鑑みなされたもので
あつて、その目的は、空調及び給湯機能を有する
ヒートポンプシステムにおいて、空調サイクルか
ら給湯サイクルに切換えられた時に、圧縮機の吐
出ガス圧の異常昇圧の発生を防止し得るように迅
速に冷媒組成の変化を生じ得るヒートポンプシス
テムを提供することにある。 The present invention has been made in view of the above-mentioned points, and its purpose is to prevent an abnormal increase in the discharge gas pressure of the compressor when switching from the air conditioning cycle to the hot water supply cycle in a heat pump system having air conditioning and hot water supply functions. It is an object of the present invention to provide a heat pump system that can quickly change the refrigerant composition so as to prevent the occurrence of.
(問題点を解決するための手段)
そこで、この発明のヒートポンプシステムは、
液管11で互いに接続された室外及び室内熱交換
器10,20,21,22の一方の熱交換器を第
1ガス管3に介して圧縮機1の吐出配管2に接続
すると共に、他方の熱交換機を上記圧縮機1の吸
込配管6に接続し、さらに上記液管11に接続さ
れた給湯用熱交換器28を上記第1ガス管3と吐
出配管2との間に接続された切換手段25に接続
することより、上記圧縮機1の吐出配管2を第1
ガス管3に連通させた空調運転と、上記圧縮機1
の吐出配管2を給湯用熱交換器28に連通させた
給湯運転とを切換可能とする一方、これら配管内
を流れる冷媒を、高温高圧側と低温低圧側との二
状態の冷凍機油に対する各溶解度の差が低沸点側
冷媒よりも高沸点側冷媒の方が大きい非共沸混合
冷媒で構成して成るヒートポンプシステムであつ
て、上記第1ガス管3には、上記圧縮機1からの
吐出ガス冷媒が上記第1ガス管3へと供給される
空調運転時に上記吐出ガス冷媒に混入した冷凍機
油を溜め込む液溜器26を介設すると共に、上記
液溜器26と上記吸込配管6との間は吸出管35
で接続し、この吸出管35には、給湯運転時に上
記液溜器26内の液を圧縮機1の吸込圧力によつ
て吸込配管6へと放出するため上記切換手段25
と連動して開となる一方、空調運転時に閉となる
遮断弁25を介設したことを特徴としている。(Means for solving the problem) Therefore, the heat pump system of this invention is
One of the outdoor and indoor heat exchangers 10, 20, 21, 22 connected to each other by a liquid pipe 11 is connected to the discharge pipe 2 of the compressor 1 via the first gas pipe 3, and the other one is connected to the discharge pipe 2 of the compressor 1 via the first gas pipe 3. A heat exchanger is connected to the suction pipe 6 of the compressor 1, and a hot water supply heat exchanger 28 connected to the liquid pipe 11 is connected between the first gas pipe 3 and the discharge pipe 2. 25, the discharge pipe 2 of the compressor 1 is connected to the first
Air conditioning operation connected to the gas pipe 3 and the compressor 1
It is possible to switch between the hot water supply operation in which the discharge piping 2 is connected to the hot water supply heat exchanger 28, and the refrigerant flowing in these piping is controlled to have different solubility in the refrigerating machine oil in two states: high temperature high pressure side and low temperature low pressure side. The heat pump system is composed of a non-azeotropic mixed refrigerant in which the difference between the high boiling point refrigerant and the low boiling point refrigerant is larger, and the first gas pipe 3 is connected to the discharge gas from the compressor 1. A liquid reservoir 26 for storing refrigerating machine oil mixed in the discharged gas refrigerant during air conditioning operation in which refrigerant is supplied to the first gas pipe 3 is interposed, and a liquid reservoir 26 is provided between the liquid reservoir 26 and the suction pipe 6. is suction pipe 35
The switching means 25 is connected to the suction pipe 35 in order to discharge the liquid in the liquid reservoir 26 to the suction pipe 6 by the suction pressure of the compressor 1 during hot water supply operation.
It is characterized by interposing a shutoff valve 25 that opens in conjunction with the air conditioner and closes during air conditioning operation.
(作用)
上記のように構成されたヒートポンプシステム
においては、切換手段25を非給湯運転、すなわ
ち空調サイクルの切換位置で運転しているときに
は、液溜器26は圧縮機1の吐出ガス冷媒が流通
する箇所に位置し、冷媒に混入して配管内を循環
する冷凍機油は、徐々にこの液溜器26中に溜ま
つてくることとなる。この間に溜まつた冷凍機油
及び液溜器26は、吐出ガス冷媒の作用を受けて
高温高圧の状態にある。一方、この状態から、切
換手段25を給湯運転に切換え、遮断弁25を開
作動すると、上記液溜器26は上記圧縮機1の吸
込配管6側へ吸出管35を介して接続されること
となり、上記圧縮機1の吸込圧力の作用を受け
て、液溜器26中の冷凍機油は急速に吸込配管6
側へ吸出されるのである。この吸込配管6は常時
低温低圧のガス冷媒が流通しているので、液溜器
26から吸込配管6側へ放出された冷凍機油は急
速に低温低圧状態に変化する。このとき配管内を
流れる冷媒を、上記高温高圧及び低温低圧の二状
態の冷凍機油に対する溶解度の差が、低沸点側冷
媒よりも高沸点側冷媒の方が大きい非共沸混合冷
媒で構成してあるため、空調サイクル時には液溜
器26中の高温高圧の冷凍機油に高沸点冷媒が多
く溶け込むので、この高沸点冷媒の少ない組成の
冷媒が配管を循環することとなり、一方給湯サイ
クル切換後には、上記冷凍機油は急速に低温低圧
状態に変化するので、これに溶け込んでいた高沸
点冷媒は短時間のうちに放出されることになる。
このことにより、給湯運転切換時、配管を循環す
る冷媒は、短時間のうちに高沸点冷媒の多い組成
になるので、前述のような凝縮圧力の上昇するこ
とがなくなり、圧縮機1の吐出ガス圧の異常昇圧
の発生を防止することが可能となるのである。(Function) In the heat pump system configured as described above, when the switching means 25 is operated in a non-hot water supply operation, that is, in the switching position of the air conditioning cycle, the liquid reservoir 26 is configured such that the gas refrigerant discharged from the compressor 1 flows through the switching means 25. The refrigerating machine oil, which is located at a location where the refrigerant is mixed with the refrigerant and circulates within the piping, gradually accumulates in the liquid reservoir 26. The refrigerating machine oil and liquid reservoir 26 that have accumulated during this period are in a high temperature and high pressure state due to the action of the discharged gas refrigerant. On the other hand, from this state, when the switching means 25 is switched to hot water supply operation and the cutoff valve 25 is opened, the liquid reservoir 26 is connected to the suction pipe 6 side of the compressor 1 via the suction pipe 35. Under the action of the suction pressure of the compressor 1, the refrigerating machine oil in the liquid reservoir 26 rapidly flows into the suction pipe 6.
It is sucked out to the side. Since a low-temperature, low-pressure gas refrigerant always flows through the suction pipe 6, the refrigerating machine oil discharged from the liquid reservoir 26 to the suction pipe 6 side rapidly changes to a low-temperature, low-pressure state. At this time, the refrigerant flowing in the pipe is composed of a non-azeotropic mixed refrigerant in which the difference in solubility in the refrigerating machine oil in the two states of high temperature and high pressure and low temperature and low pressure is larger in the high boiling point refrigerant than in the low boiling point refrigerant. Therefore, during the air conditioning cycle, a large amount of high-boiling point refrigerant dissolves in the high-temperature, high-pressure refrigerating machine oil in the liquid reservoir 26, so a refrigerant with a composition containing less high-boiling point refrigerant circulates through the pipes.On the other hand, after the hot water supply cycle is switched, Since the refrigerating machine oil rapidly changes to a low temperature and low pressure state, the high boiling point refrigerant dissolved therein will be released within a short period of time.
As a result, when the hot water supply operation is switched, the refrigerant circulating through the pipes quickly becomes a composition with a high boiling point refrigerant, so the condensation pressure does not increase as described above, and the discharge gas of the compressor 1 This makes it possible to prevent abnormal pressure increases from occurring.
(実施例)
次に、この発明のヒートポンプシステムの具体
的な実施例について、図面を参照しつつ詳細に説
明する。(Example) Next, a specific example of the heat pump system of the present invention will be described in detail with reference to the drawings.
第1図は、この発明の一実施例における全体構
成を示す冷媒回路図であり、一基の室外熱交換器
10と三基の室内熱交換器20,21,22及び
一基の給湯用熱交換器28を有する三室空調及び
給湯用ヒートポンプシステムとして構成されてい
る。同図において、室外熱交換器10は液管11
によつて、各室にそれぞれ配置された室内熱交換
器20,21,22に接続されている。この液管
11には、上記室外熱交換器10側より主管膨張
弁12、レシーバタンク13、液閉鎖弁14が順
次介設されており、またこの液閉鎖弁14と上記
各室内熱交換器20,21,22との間は、それ
ぞれ支管膨張弁201,211,221の介設さ
れた三本の分岐液管202,212,222に分
岐されている。そして、上記各室内熱交換器2
0,21,22にはそれぞれ分岐ガス管203,
213,223が接続されており、これらの分岐
ガス管203,213,223の合流点はガス閉
鎖弁15の介設された室内側ガス管16によつ
て、また、上記室外熱交換器10は室外側ガス管
17によつて、それぞれ冷暖切換用の四路切換弁
(以下、冷暖切換弁という。)18に接続されてい
る。一方、圧縮機1の吐出配管2は四路切換弁2
5に接続されており、この四路切換弁25の上記
吐出配管2との連通可能な一方の接続ポートと、
上記冷暖切換弁18の一方の接続ポートとが、液
溜器26の介設された第1ガス管3により接続さ
れると共に、上記冷暖切換弁18の他方の接続ポ
ートは、2箇のアキユームレータ4,5の介設さ
れた吸込配管6に接続されて、空調用冷媒循環回
路を構成している。 FIG. 1 is a refrigerant circuit diagram showing the overall configuration in an embodiment of the present invention, including one outdoor heat exchanger 10, three indoor heat exchangers 20, 21, 22, and one hot water supply heat exchanger. It is configured as a three-chamber air conditioning and hot water heat pump system with an exchanger 28. In the figure, the outdoor heat exchanger 10 is a liquid pipe 11
are connected to indoor heat exchangers 20, 21, and 22 arranged in each room, respectively. In this liquid pipe 11, a main pipe expansion valve 12, a receiver tank 13, and a liquid closing valve 14 are sequentially installed from the outdoor heat exchanger 10 side, and this liquid closing valve 14 and each of the indoor heat exchangers 20 , 21, 22 are branched into three branch liquid pipes 202, 212, 222 with branch pipe expansion valves 201, 211, 221 interposed therein, respectively. And each of the above indoor heat exchangers 2
0, 21, and 22 have branch gas pipes 203 and 22, respectively.
213, 223 are connected, and the confluence of these branch gas pipes 203, 213, 223 is connected by an indoor gas pipe 16 in which a gas shutoff valve 15 is interposed, and the outdoor heat exchanger 10 is Each of them is connected by an outdoor gas pipe 17 to a four-way switching valve (hereinafter referred to as a heating/cooling switching valve) 18 for switching between cooling and heating. On the other hand, the discharge pipe 2 of the compressor 1 is connected to the four-way switching valve 2.
5, one connection port of the four-way switching valve 25 that can communicate with the discharge pipe 2;
One connection port of the heating/cooling switching valve 18 is connected to the first gas pipe 3 in which a liquid reservoir 26 is interposed, and the other connecting port of the heating/cooling switching valve 18 is connected to two AC pipes. It is connected to the suction pipe 6 in which the multors 4 and 5 are interposed, thereby forming an air conditioning refrigerant circulation circuit.
上記四路切換弁25は、空調と給湯とを切換え
る切換手段となるものであつて、上記吐出配管2
と連通可能な他方の接続ポートには、貯湯槽27
内に設置されている給湯用熱交換器28が、ガス
閉鎖弁29の介設された給湯用ガス管30によつ
て接続されている。またこの給湯用熱交換器28
は、前記液管11に介設されているレシーバタン
ク13に、液閉鎖弁31の介設された給湯用液管
32により接続されている。さらに、この給湯用
液管32には、給湯用熱交換器28側から液管1
1側へ向かう冷媒流れを許容する方向の逆止弁3
3と、この逆止弁33に並列接続され、デフロス
ト運転以外は閉成される電磁弁34とが介設され
ている。そして前記四路切換弁25において、上
記給湯用ガス管30及び前記第1ガス管3との連
通が可能な接続ポートは、吸込配管6の前記冷暖
切換弁18とアキユームレータ5との間に、吸出
管35により接続されている。したがつて、上記
四路切換弁25は、上記吸出管35が第1ガス管
3と連通する位置においては、第1ガス管3側か
ら吸出管35側への冷媒流れが生じ、一方、給湯
用ガス管30と連通する位置では、後述するよう
に、これらの配管を通しての冷媒流れは生じず、
吸出管35に介設した遮断弁としての機能を有す
るものでもある。 The four-way switching valve 25 serves as a switching means for switching between air conditioning and hot water supply, and serves as a switching means for switching between air conditioning and hot water supply.
The other connection port that can communicate with the hot water tank 27
A heat exchanger 28 for hot water supply installed inside is connected to a hot water supply gas pipe 30 in which a gas shutoff valve 29 is interposed. In addition, this hot water supply heat exchanger 28
is connected to a receiver tank 13 provided in the liquid pipe 11 through a hot water supply liquid pipe 32 provided with a liquid shutoff valve 31 . Further, a liquid pipe 1 is connected to the hot water supply liquid pipe 32 from the hot water supply heat exchanger 28 side.
Check valve 3 in a direction that allows refrigerant flow toward the 1 side
3, and a solenoid valve 34 which is connected in parallel to the check valve 33 and is closed except during defrost operation. In the four-way switching valve 25, a connection port that can communicate with the hot water supply gas pipe 30 and the first gas pipe 3 is located between the cooling/heating switching valve 18 of the suction pipe 6 and the accumulator 5. , are connected by a suction pipe 35. Therefore, in the four-way switching valve 25, at a position where the suction pipe 35 communicates with the first gas pipe 3, a refrigerant flow occurs from the first gas pipe 3 side to the suction pipe 35 side, and on the other hand, the hot water supply At the position communicating with the gas pipe 30, no refrigerant flow occurs through these pipes, as will be described later.
It also has a function as a shutoff valve provided in the suction pipe 35.
以上のように構成された上記実施例の作動状態
について、次に説明する。まず室内を冷房又は暖
房する空調運転時には、図中実線及び破線矢印で
示す冷媒流れが生ずるように四路切換弁25を切
換えする。すなわち、圧縮機1から吐出される高
温高圧のガス冷媒は、吐出配管2、四路切換弁2
5を経由して、第1ガス管3に流入し、これに介
設してある液溜器26を通つて冷暖切換弁18へ
と供給される。そしてこの冷暖切換弁18の切換
位置により、実線矢印方向に室内熱交換器20,
21,22側から室外熱交換器10側へ循環する
暖房サイクル循環が、また破線矢印方向に室外熱
交換器10側から室内熱交換器20,21,22
側へ循環する冷房サイクル循環がそれぞれ行なわ
れ、冷暖切換弁18に戻つた低温低圧のガス冷媒
は、吸込配管6を通して圧縮機1に返流されるの
である。このとき給湯用熱交換器28に接続され
ている給湯用ガス管30は、四路切換弁25、吸
出管35を介して低圧が作用している吸込配管6
に連通しており、したがつて、給湯用液管32に
介設されている逆止弁33には流れ阻止方向の圧
力差がかかるので、給湯用熱交換器28には冷媒
流れは生じず、給湯加熱停止状態にある。また、
このとき、循環冷媒に混入して配管内を循環して
いる冷凍機油はアキユームレータ4,5におい
て、ガス冷媒より分離されて、それらのアキユー
ムレータ4,5に溜まつていくとともに、図中ア
キユームレータ5の内部を模式的に示すように、
圧縮機1側の内部連通管7は、底部まで伸びて更
に上方に向かう鉤状のパイプで構成されると共
に、その底部位置には小孔8が設けられており、
したがつて、このアキユームレータ4,5に溜ま
る冷凍機油は、上記小孔8を通して適量吸い出さ
れ、ガス冷媒と共に、圧縮機1に流入していくの
である。一方、圧縮機1からは油が混入したガス
冷媒が吐出配管2を通して吐出されており、この
吐出ガス冷媒に含まれる冷凍機油量と、上記アキ
ユームレータ4,5より流入される冷凍機油量と
がバランスした状態で、圧縮機1内の冷凍機油量
が保持されているのである。そして、上記吐出配
管2へ吐出されたガス冷媒は第1ガス管3に介設
している液溜器26を経由して冷暖切換弁18に
供給される。この液溜器26は、第1図中、その
内部構造を模式的に示しているように、例えば、
四路切換弁25側の内部連通管36は底部に近接
して開口する直管で構成され、他方の冷暖切換弁
18側の内部連通管37は短管で構成されている
ような、ガス−液分離機能を有しており、したが
つて、冷凍機油が混入されたガス冷媒がこの液溜
器26を流通するときには、冷凍機油は分離され
て、次第にこの液溜器26内に溜まつていくこと
となる。以上のことにより、上記空調運転時に、
アキユームレータ4,5に溜まつていた冷凍機油
は次第に液溜器26へと移し換えられることとな
る。この移し換えられる冷凍機油は、移し換え前
は低温低圧であるが、移し換え後は圧縮機1の吐
出ガス冷媒にさらされているので、高温かつ高圧
状態である。 The operating state of the above-described embodiment configured as described above will be explained next. First, during air conditioning operation to cool or heat the room, the four-way selector valve 25 is switched so that the refrigerant flows as shown by solid lines and broken line arrows in the figure. That is, the high temperature and high pressure gas refrigerant discharged from the compressor 1 is transferred to the discharge pipe 2 and the four-way switching valve 2.
5, flows into the first gas pipe 3, and is supplied to the cooling/heating switching valve 18 through a liquid reservoir 26 provided therein. Then, depending on the switching position of the heating/cooling switching valve 18, the indoor heat exchanger 20,
The heating cycle circulates from the 21, 22 side to the outdoor heat exchanger 10 side, and the heating cycle circulates from the outdoor heat exchanger 10 side to the indoor heat exchanger 20, 21, 22 in the direction of the broken line arrow.
The cooling cycle circulation to the side is performed, and the low-temperature, low-pressure gas refrigerant that returns to the cooling/heating switching valve 18 is returned to the compressor 1 through the suction pipe 6. At this time, the hot water supply gas pipe 30 connected to the hot water supply heat exchanger 28 is connected to the suction pipe 6 on which low pressure is applied via the four-way switching valve 25 and the suction pipe 35.
Therefore, a pressure difference in the flow blocking direction is applied to the check valve 33 interposed in the hot water supply liquid pipe 32, so no refrigerant flow occurs in the hot water supply heat exchanger 28. , hot water heating is stopped. Also,
At this time, the refrigerating machine oil mixed with the circulating refrigerant and circulating in the pipes is separated from the gas refrigerant in the accumulators 4 and 5, and accumulates in the accumulators 4 and 5, and as shown in FIG. As schematically shown inside the medium storage unit 5,
The internal communication pipe 7 on the compressor 1 side is composed of a hook-shaped pipe that extends to the bottom and goes further upward, and a small hole 8 is provided at the bottom position.
Therefore, an appropriate amount of the refrigerating machine oil accumulated in the accumulators 4 and 5 is sucked out through the small hole 8 and flows into the compressor 1 together with the gas refrigerant. On the other hand, a gas refrigerant mixed with oil is discharged from the compressor 1 through a discharge pipe 2, and the amount of refrigerating machine oil contained in this discharged gas refrigerant and the amount of refrigerating machine oil flowing in from the accumulators 4 and 5 are The amount of refrigerating machine oil in the compressor 1 is maintained in a balanced state. The gas refrigerant discharged to the discharge pipe 2 is supplied to the cooling/heating switching valve 18 via the liquid reservoir 26 interposed in the first gas pipe 3. As the internal structure of this liquid reservoir 26 is schematically shown in FIG. 1, for example,
The internal communication pipe 36 on the four-way switching valve 25 side is a straight pipe that opens close to the bottom, and the internal communication pipe 37 on the other cooling/heating switching valve 18 side is a short pipe. It has a liquid separation function, so when the gas refrigerant mixed with refrigerating machine oil flows through this liquid reservoir 26, the refrigerating machine oil is separated and gradually accumulates in this liquid reservoir 26. I have to go. Due to the above, during the above air conditioning operation,
The refrigerating machine oil accumulated in the accumulators 4 and 5 is gradually transferred to the liquid reservoir 26. The refrigerating machine oil to be transferred is at a low temperature and low pressure before being transferred, but after being transferred, it is exposed to the discharge gas refrigerant of the compressor 1, so it is in a high temperature and high pressure state.
次に、給湯運転の作動状態について説明する。
第1図中、一点鎖線の矢印で示す方向に冷媒を循
環させることによつて、給湯加熱が行なわれる。
すなわち、圧縮機1から吐出される高温高圧のガ
ス冷媒は、吐出配管2、四路切換弁25、給湯用
ガス管30、給湯用熱交換器28、給湯用液管3
2を経由して、液管11に介設しているレシーバ
タンク13に流入する。そして、冷暖切換弁18
を室外熱交換器10が吸込配管6に連通する位置
に切換えておくことにより、上記給湯用熱交換器
28からレシーバタンク13に流入した冷媒は、
室外熱交換器10、室外側ガス管17、冷暖切換
弁18、吸込配管6を経由して圧縮機1に返流さ
れ、このとき上記給湯用熱交換器28は凝縮器と
して作用し、湯の加熱が行なわれる。なお、この
とき室内熱交換器20,21,22は、室内側ガ
ス管16、冷暖切換弁18、第1ガス管3、四路
切換弁25、吐出管35を介して吸込配管6に連
通しており、したがつて、支管膨張弁201,2
11,221を適宜開制御することにより、室内
側の同時冷房運転も可能である。 Next, the operating state of hot water supply operation will be explained.
In FIG. 1, hot water is heated by circulating the refrigerant in the direction indicated by the dashed-dotted arrow.
That is, the high-temperature, high-pressure gas refrigerant discharged from the compressor 1 is transferred to the discharge pipe 2, the four-way switching valve 25, the gas pipe 30 for hot water supply, the heat exchanger 28 for hot water supply, and the liquid pipe 3 for hot water supply.
2, it flows into the receiver tank 13 interposed in the liquid pipe 11. And the cooling/heating switching valve 18
By switching the outdoor heat exchanger 10 to a position where it communicates with the suction pipe 6, the refrigerant flowing from the hot water supply heat exchanger 28 into the receiver tank 13 is
The water is returned to the compressor 1 via the outdoor heat exchanger 10, the outdoor gas pipe 17, the cooling/heating switching valve 18, and the suction pipe 6. At this time, the hot water supply heat exchanger 28 acts as a condenser, and the hot water is Heating takes place. Note that at this time, the indoor heat exchangers 20, 21, and 22 are communicated with the suction pipe 6 via the indoor gas pipe 16, the cooling/heating switching valve 18, the first gas pipe 3, the four-way switching valve 25, and the discharge pipe 35. Therefore, the branch pipe expansion valves 201, 2
11 and 221, it is also possible to perform simultaneous indoor cooling operation.
上記のように、四路切換弁25の切換えによつ
て、空調運転からの給湯運転へと切換えられる
が、この四路切換弁25の切換えと同時に、上記
第1ガス管3に介設していた液溜器26は、吐出
配管2との連通状態から、吸出管35を介して吸
込配管6へ連通する状態に切換わり、圧縮機1の
吸込圧力が作用することとなる。したがつて、先
に述べたように、液溜器35の底部まで伸びた内
部連通管36の開口位置を越える冷凍機油は急速
に吸込配管6側へ吸出されることとなる。吸出さ
れた冷凍機油は、アキユームレータ4,5の介設
されている吸込配管6側に移し換えられると略同
時に、低温低圧状態となる。 As mentioned above, by switching the four-way switching valve 25, the air conditioning operation is switched to the hot water supply operation, but at the same time as the switching of the four-way switching valve 25, the The liquid reservoir 26 is switched from communicating with the discharge pipe 2 to communicating with the suction pipe 6 via the suction pipe 35, and the suction pressure of the compressor 1 is applied thereto. Therefore, as described above, the refrigerating machine oil that exceeds the opening position of the internal communication pipe 36 extending to the bottom of the liquid reservoir 35 is rapidly sucked out to the suction pipe 6 side. The sucked-out refrigerating machine oil is brought into a low-temperature, low-pressure state almost at the same time as it is transferred to the suction pipe 6 side where the accumulators 4 and 5 are interposed.
以上の説明のように、上記実施例においては、
圧縮機1の作動に必要な適正量の冷凍機油以外の
余剰の冷凍機油が、非給湯運転(空調運転)時に
は、液溜器26内に高温高圧の状態で次第に溜め
込まれ、一方給湯運転への切換えと略同時に、上
記高温高圧の冷凍機油が吸込配管6側へ吸い出さ
れて、低温低圧状態となるのである。そして、上
記実施例においては、冷媒として沸点の異なる、
例えばR22とR114との混合冷媒を用い、冷凍機
油としてスニソ4GSを用いている。第2図a,b
にはR22及びR114のスニソ4GSに対する溶解度特
性を、それぞれ示しているが、低沸点側の冷媒
R22は、同図aのように、上記装置の作動条件で
ある圧力20Kg/cm2以下、油温120℃以下の範囲で
は殆ど溶解度に差はなく、一方、高沸点側の冷媒
R114においては、同図bのA,Bで示すように、
上記装置において得られる高温高圧と、低温低圧
の二状態に対して、溶解度が大きく異なるもので
ある。すなわち、高温高圧の冷凍機油には多量の
R114が吸収され、そしてこの冷凍機油が低温低
圧になると吸収していたR114が放出される。し
たがつて、前記したように、非給湯運転時には液
等器26に溜め込まれた冷凍機油中に、R114は
多量に吸収されていくので、空調冷媒循環サイク
ルには、高沸点冷媒R114の少ない組成の冷媒が
循環して、従来通りの空調能力を維持し得る。一
方、給湯運転時には、その切換えと略同時に上記
R114が冷凍機油中から放出され、したがつて、
高沸点冷媒R114の多い組成の冷媒が循環するこ
ととなる。このことから、従来装置において生じ
ていたような圧縮機1からの吐出ガス圧の異常昇
圧が防止できることとなるのである。 As explained above, in the above embodiment,
Surplus refrigerating machine oil other than the appropriate amount of refrigerating machine oil required for the operation of the compressor 1 is gradually stored in the liquid reservoir 26 at high temperature and pressure during non-hot water supply operation (air conditioning operation), while during hot water supply operation. At approximately the same time as the switching, the high-temperature, high-pressure refrigerating machine oil is sucked out to the suction pipe 6 side, resulting in a low-temperature, low-pressure state. In the above embodiment, the refrigerant has different boiling points.
For example, a mixed refrigerant of R22 and R114 is used, and Suniso 4GS is used as the refrigerating machine oil. Figure 2 a, b
shows the solubility characteristics of R22 and R114 in Suniso 4GS, respectively.
As shown in Figure a, there is almost no difference in the solubility of R22 under the operating conditions of the above device, that is, the pressure is below 20 kg/cm 2 and the oil temperature is below 120°C.
In R114, as shown by A and B in the same figure b,
The solubility differs greatly between the two states of high temperature and high pressure obtained in the above device and low temperature and low pressure. In other words, there is a large amount of high temperature and high pressure refrigeration oil.
R114 is absorbed, and when this refrigerating machine oil becomes low temperature and pressure, the absorbed R114 is released. Therefore, as mentioned above, during non-hot water supply operation, a large amount of R114 is absorbed into the refrigerating machine oil stored in the liquid equalizer 26, so in the air conditioning refrigerant circulation cycle, a high boiling point refrigerant with a composition that is low in R114 is used. The refrigerant is circulated to maintain the same air conditioning capacity as before. On the other hand, during hot water supply operation, the above-mentioned
R114 is released from the refrigeration oil and therefore
A refrigerant having a composition with a high boiling point refrigerant R114 will be circulated. This makes it possible to prevent an abnormal increase in the discharge gas pressure from the compressor 1, which occurs in conventional devices.
以上の説明のように、上記実施例においては、
給湯運転切換時に、高沸点冷媒の多い組成に短時
間で変化するので、圧力の異常昇圧を防止でき、
さらには、この圧力上昇度が低減されることか
ら、従来に比べて沸き上げ湯温を上昇させること
も可能となる。また、従来は空調と給湯とのそれ
ぞれの運転に共に使用し得る冷媒を選定し、その
結果各能力を抑えざるを得ない状態で装置構成が
成されていたが、上記実施例によれば、それぞれ
の空調サイクル、及び給湯サイクルに略適合した
冷媒組成へと自動的に変化するので、各能力の向
上が図れることとなる。また上記実施例の説明の
中で、液溜器26の内部流通管36を底部に開口
する直管で構成したが、このとき、空調サイクル
時に流入するガス冷媒は、冷凍機油中をバブリン
グしながら流通する状態となり、このことにより
ガス冷媒の冷凍機油中への溶解がより速やかに行
なわれるという効果を有している。 As explained above, in the above embodiment,
When switching hot water supply operation, the composition quickly changes to a high-boiling refrigerant-rich composition, which prevents abnormal pressure increases.
Furthermore, since the degree of pressure rise is reduced, it is also possible to raise the temperature of boiling water compared to the conventional method. Furthermore, in the past, a refrigerant that could be used for both air conditioning and hot water supply operations was selected, and as a result, the equipment configuration was configured in such a way that each capacity had to be suppressed, but according to the above embodiment, Since the refrigerant composition is automatically changed to suit each air conditioning cycle and hot water supply cycle, each capacity can be improved. In addition, in the description of the above embodiment, the internal flow pipe 36 of the liquid reservoir 26 is configured as a straight pipe that opens at the bottom, but at this time, the gas refrigerant that flows in during the air conditioning cycle bubbles through the refrigerating machine oil. This has the effect of dissolving the gas refrigerant into the refrigerating machine oil more quickly.
なお、上記実施例においては、一例として、
R22とR112、スニソ4GSを挙げたが、上記説明の
ように、高沸点側の冷媒により大きな溶解度の差
が生じる組合せであれば、他の冷媒、冷凍機油の
使用することができる。また、切換手段及び遮断
弁として、それらの機能を兼用する四路切換弁2
5で構成したが、例えば、吐出配管2を第1ガス
管3と給湯用ガス管30とに切換え可能であれ
ば、三方弁やその他の弁で構成することが可能で
あり、またこのとき、吸出管35は独自の遮断弁
を介設すると共に、直接液溜器26に接続する構
成とすることもできる。さらに、吸込配管6に介
設したアキユームレータ4,5は、上記吸込配管
6に液溜の機能を有するように、例えば配管径の
大きな領域を付加すれば、上記アキユームレータ
4,5は省略することもできる。 In addition, in the above embodiment, as an example,
Although R22, R112, and Suniso 4GS are mentioned, as explained above, other refrigerants and refrigerating machine oil can be used as long as the combination causes a large difference in solubility depending on the refrigerant on the high boiling point side. In addition, a four-way switching valve 2 that serves both functions as a switching means and a shutoff valve.
5, but for example, if the discharge pipe 2 can be switched between the first gas pipe 3 and the hot water supply gas pipe 30, it can be constructed with a three-way valve or other valves, and in this case, The suction pipe 35 may be provided with its own cutoff valve and may also be configured to be directly connected to the liquid reservoir 26. Furthermore, the accumulators 4 and 5 interposed in the suction pipe 6 can be modified by adding, for example, a region with a large pipe diameter to the suction pipe 6 so as to have a liquid storage function. It can also be omitted.
(発明の効果)
以上の説明のように、この発明のヒートポンプ
システムにおいては、空調運転時には液溜器に高
温高圧で冷凍機油を溜め込む一方、給湯運転時に
は上記液溜器内の冷凍機油を圧縮機の吸込配管側
へと吸出して急速に低温低圧とするようにしてあ
るので、高沸点冷媒が迅速に放出され、この高沸
点冷媒を多く含んだ冷媒組成に速やかに変化する
ため、貯湯槽の湯温が上昇していても凝縮圧力が
上昇せず、したがつて、圧縮機からの吐出ガス圧
の異常昇圧を防止することができる。(Effects of the Invention) As described above, in the heat pump system of the present invention, refrigerating machine oil is stored in the reservoir at high temperature and pressure during air conditioning operation, while refrigerating machine oil in the reservoir is stored in the compressor during hot water supply operation. Since the high boiling point refrigerant is quickly discharged and the refrigerant composition quickly changes to include a large amount of this high boiling point refrigerant, the hot water in the hot water storage tank is Even if the temperature rises, the condensing pressure does not rise, and therefore, it is possible to prevent the pressure of the gas discharged from the compressor from increasing abnormally.
第1図はこの発明のヒートポンプシステムの一
実施例における全体構成を示す冷媒回路図、第2
図a,bはスニソ4GS中へのR22とR114の溶解度
を示すグラフ、第3図は従来の空調機の冷媒回路
図である。
1……圧縮機、2……吐出配管、3……第1ガ
ス管、6……吸込配管、10……室外熱交換器、
11……液管、20,21,22……室内熱交換
器、25……四路切換弁(切換手段)(遮断弁)、
26……液溜器、28……給湯用熱交換器、35
……吸出管。
FIG. 1 is a refrigerant circuit diagram showing the overall configuration of an embodiment of the heat pump system of the present invention, and FIG.
Figures a and b are graphs showing the solubility of R22 and R114 in Suniso 4GS, and Figure 3 is a refrigerant circuit diagram of a conventional air conditioner. 1...Compressor, 2...Discharge pipe, 3...First gas pipe, 6...Suction pipe, 10...Outdoor heat exchanger,
11... Liquid pipe, 20, 21, 22... Indoor heat exchanger, 25... Four-way switching valve (switching means) (shutoff valve),
26...Liquid reservoir, 28...Hot water supply heat exchanger, 35
...Suction tube.
Claims (1)
交換器10,20,21,22の一方の熱交換器
を第1ガス管3を介して圧縮機1の吐出配管2に
接続すると共に、他方の熱交換器を上記圧縮機1
の吸込配管6に接続し、さらに上記液管11に接
続された給湯用熱交換器28を上記第1ガス管3
と吐出配管2との間に接続された切換手段25に
接続することにより、上記圧縮機1の吐出配管2
を第1ガス管3に連通させた空調運転と、上記圧
縮機1の吐出配管2を給湯用熱交換器28に連通
させた給湯運転とを切換可能とする一方、これら
配管内を流れる冷媒を、高温高圧側と低温低圧側
との二状態の冷凍機油に対する各溶解度の差が低
沸点側冷媒よりも高沸点側冷媒の方が大きい非共
沸混合冷媒で構成して成るヒートポンプシステム
であつて、上記第1ガス管3には、上記圧縮機1
からの吐出ガス冷媒が上記第1ガス管3へと供給
される空調運転時に上記吐出ガス冷媒に混入した
冷凍機油を溜め込む液溜器26を介設すると共
に、上記液溜器26と上記吸込配管6との間は吸
出管35で接続し、この吸出管35には、給湯運
転時に上記液溜器26内の液を圧縮機1の吸込圧
力によつて吸込配管6へと放出するため上記切換
手段25と連動して開となる一方、空調運転時に
閉となる遮断弁25を介設したことを特徴とする
ヒートポンプシステム。1 One of the outdoor and indoor heat exchangers 10, 20, 21, 22 connected to each other by the liquid pipe 11 is connected to the discharge pipe 2 of the compressor 1 via the first gas pipe 3, and the other The heat exchanger of the above compressor 1
The hot water supply heat exchanger 28 connected to the suction pipe 6 and the liquid pipe 11 is connected to the first gas pipe 3.
By connecting to the switching means 25 connected between the discharge pipe 2 and the discharge pipe 2 of the compressor 1,
It is possible to switch between an air conditioning operation in which the compressor 1 is connected to the first gas pipe 3 and a hot water supply operation in which the discharge pipe 2 of the compressor 1 is connected to the hot water supply heat exchanger 28, and the refrigerant flowing in these pipes is , a heat pump system comprising a non-azeotropic mixed refrigerant in which the difference in solubility in two states of refrigerating machine oil, high-temperature, high-pressure side and low-temperature, low-pressure side, is larger for the high-boiling point refrigerant than for the low-boiling point side refrigerant; , the compressor 1 is connected to the first gas pipe 3.
A liquid reservoir 26 is provided to store refrigerating machine oil mixed in the discharged gas refrigerant during air conditioning operation in which the discharged gas refrigerant is supplied to the first gas pipe 3, and the liquid reservoir 26 and the suction pipe 6 is connected by a suction pipe 35, and this suction pipe 35 is equipped with the above-mentioned switching switch in order to discharge the liquid in the liquid reservoir 26 to the suction pipe 6 by the suction pressure of the compressor 1 during hot water supply operation. A heat pump system characterized by interposing a shutoff valve 25 which opens in conjunction with means 25 and closes during air conditioning operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16053886A JPS6315047A (en) | 1986-07-07 | 1986-07-07 | heat pump system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16053886A JPS6315047A (en) | 1986-07-07 | 1986-07-07 | heat pump system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6315047A JPS6315047A (en) | 1988-01-22 |
| JPH0373793B2 true JPH0373793B2 (en) | 1991-11-22 |
Family
ID=15717143
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16053886A Granted JPS6315047A (en) | 1986-07-07 | 1986-07-07 | heat pump system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6315047A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01222729A (en) * | 1988-03-01 | 1989-09-06 | Shiitex:Kk | High-production marine ranch creation system |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6155562A (en) * | 1984-08-24 | 1986-03-20 | ダイキン工業株式会社 | Refrigeration equipment using mixed refrigerant |
-
1986
- 1986-07-07 JP JP16053886A patent/JPS6315047A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6315047A (en) | 1988-01-22 |
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