JPH0245101B2 - REIDANBOSOCHI - Google Patents
REIDANBOSOCHIInfo
- Publication number
- JPH0245101B2 JPH0245101B2 JP16706984A JP16706984A JPH0245101B2 JP H0245101 B2 JPH0245101 B2 JP H0245101B2 JP 16706984 A JP16706984 A JP 16706984A JP 16706984 A JP16706984 A JP 16706984A JP H0245101 B2 JPH0245101 B2 JP H0245101B2
- Authority
- JP
- Japan
- Prior art keywords
- refrigerant
- heating
- gas
- liquid
- pump
- 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
- 239000003507 refrigerant Substances 0.000 claims description 131
- 238000010438 heat treatment Methods 0.000 claims description 46
- 239000007788 liquid Substances 0.000 claims description 37
- 238000001816 cooling Methods 0.000 claims description 3
- 229920006395 saturated elastomer Polymers 0.000 description 8
- 238000004378 air conditioning Methods 0.000 description 7
- 230000007423 decrease Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000005494 condensation Effects 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000002159 abnormal effect Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Landscapes
- 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
本発明は補助熱源により高圧液冷媒を加熱する
冷媒加熱器を有し、その熱エネルギを暖房時の低
圧蒸発器で得られた主熱源からの暖房出力に加え
る事でヒートポンプ暖房能力の増加をはかる冷暖
房装置において、冷媒加熱器内を流れる冷媒の流
量制御手段に関するものである。Detailed Description of the Invention: Industrial Application Field The present invention has a refrigerant heater that heats a high-pressure liquid refrigerant with an auxiliary heat source, and the thermal energy is used for heating from the main heat source obtained by a low-pressure evaporator during heating. This invention relates to a means for controlling the flow rate of refrigerant flowing within a refrigerant heater in a heating and cooling system that increases the heating capacity of a heat pump by adding it to the output.
従来例の構成とその問題点
従来、空気熱源ヒートポンプ式の冷暖房装置で
は低外気温時の暖房能力不足や暖房運転開始時の
暖房効果の立ち上り特性の改善を図るため、例え
ば第2図で示されるような冷媒加熱器を有した冷
暖房装置が提案されている。第3図はその動作を
表わしたモリエル線図である。Conventional configurations and their problems Conventionally, air-source heat pump type air-conditioning and heating systems have been designed to improve heating performance due to lack of heating capacity at low outside temperatures and the rising characteristics of the heating effect at the start of heating operation, for example, as shown in Figure 2. A heating and cooling device having such a refrigerant heater has been proposed. FIG. 3 is a Mollier diagram showing the operation.
第2図において、1は屋外ユニツト部分、2お
よび2′は屋内ユニツト部分で、これらのユニツ
トはそれぞれ2本の冷媒配管3,4および3′,
4′により接続されている。屋外ユニツト部分1
において、5は圧縮機、6は四方弁、7は屋外熱
交換器、8は絞り装置である。9は暖房時に高圧
冷媒液の回路となる配管4および4′から絞り装
置8への系路に設けられた受液器であり、受液器
9からは冷媒ポンプ10、冷媒加熱器11および
逆止弁12を直列に介して圧縮機5の吐出冷媒ガ
ス配管13と接続される冷媒回路14が設けられ
ている。15および16は屋内ユニツト2を使用
する時に開動作する電磁弁、15′および16′は
屋内ユニツト2′を使用する時に開動作する電磁
弁である。電磁弁15,15′は分岐回路17を
介して四方弁6と、電磁弁16,16′を分岐回
路18を介して受液器9とそれぞれ接続されてい
る。 In Fig. 2, 1 is an outdoor unit part, 2 and 2' are indoor unit parts, and these units have two refrigerant pipes 3, 4 and 3', respectively.
4'. Outdoor unit part 1
, 5 is a compressor, 6 is a four-way valve, 7 is an outdoor heat exchanger, and 8 is a throttle device. Reference numeral 9 denotes a liquid receiver installed in the system from pipes 4 and 4' to the expansion device 8, which forms a high-pressure refrigerant liquid circuit during heating. A refrigerant circuit 14 is provided which is connected to a discharge refrigerant gas pipe 13 of the compressor 5 via a stop valve 12 in series. 15 and 16 are solenoid valves that are opened when the indoor unit 2 is used, and 15' and 16' are solenoid valves that are opened when the indoor unit 2' is used. The solenoid valves 15 and 15' are connected to the four-way valve 6 through a branch circuit 17, and the solenoid valves 16 and 16' are connected to the liquid receiver 9 through a branch circuit 18, respectively.
冷媒加熱器11に設けられる補助熱源としては
何でもよいが第2図の従来例では2個の電気ヒー
タ19および19′を用いた例を示している。各
電気ヒータは電源20に対して並列に接続され、
それぞれスイツチ21および21′を有している。
各スイツチは屋内ユニツト2を暖房運転している
時にスイツチ21がONし、屋内ユニツト2′を
暖房運転している時にスイツチ21′がONとな
るよう構成されている。 Although any auxiliary heat source may be used as the auxiliary heat source provided in the refrigerant heater 11, the conventional example shown in FIG. 2 shows an example using two electric heaters 19 and 19'. Each electric heater is connected in parallel to a power source 20,
Each has a switch 21 and 21'.
Each switch is configured such that the switch 21 is turned on when the indoor unit 2 is in heating operation, and the switch 21' is turned on when the indoor unit 2' is in heating operation.
以上の従来の構成において、暖房2室運転時の
動作を第3図に併用して説明する。屋内熱交換器
22および22′で凝縮した高圧冷媒液は受液器
9へ流入し(第3図d点)、二方向に分岐される。
一方は絞り装置8で減圧され屋外熱交換器7へ流
入し(第3図e点)、外気より吸熱気化し圧縮機
5に吸入後(第3図a点)圧縮され、高圧冷媒ガ
スとして吐出される。他方は、冷媒ポンプ10に
より冷媒加熱器11に流入し(第3図f点)、電
気ヒータ19および19′により加熱気化された
後、逆止弁12を経て、圧縮機5から出た吐出冷
媒ガスと混合し(第3図c点)四方弁6を経て再
び屋内熱交換器22および22′で凝縮液化され
る。 In the conventional configuration described above, the operation during two-room heating operation will be described with reference to FIG. 3. The high-pressure refrigerant liquid condensed in the indoor heat exchangers 22 and 22' flows into the liquid receiver 9 (point d in FIG. 3) and is branched into two directions.
One side is depressurized by the expansion device 8 and flows into the outdoor heat exchanger 7 (point e in Figure 3), where it absorbs heat from the outside air and vaporizes, is sucked into the compressor 5 (point a in Figure 3), is compressed, and is discharged as high-pressure refrigerant gas. be done. The other refrigerant flows into the refrigerant heater 11 by the refrigerant pump 10 (point f in Figure 3), is heated and vaporized by the electric heaters 19 and 19', passes through the check valve 12, and is discharged from the compressor 5. The mixture is mixed with gas (point c in Figure 3), passes through the four-way valve 6, and is again condensed and liquefied in the indoor heat exchangers 22 and 22'.
以上の説明でわかるように、
GM;圧縮機5の冷媒流量
GP;冷媒ポンプ10の冷媒流量
GC;屋内熱交換器22および22′を流れる合計
の冷媒流量
QH;暖房能力
とすれば
GC=GM+GC
となり、QHは
QH=GC(ic−id)=GM(ic−id)
+GP(ic−id)
すなわち、冷媒加熱器11の加熱能力QRH
QRH=GP(ic−id)
ぶんだけ暖房能力が増加する事になり、低外気
温時の暖房能力不足や暖房運転開始時の暖房効果
の立ち上り特性の改善を図る手段として用いられ
ていた。しかしこのような従来の冷暖房装置で暖
房1室運転を行なうため冷媒加熱器11の電気ヒ
ータ19又は19′のいずれかをOFFして加熱量
QRHを半減させようとした場合には次のような欠
点があつた。 As can be seen from the above explanation, G M ; refrigerant flow rate G P of the compressor 5; refrigerant flow rate G C of the refrigerant pump 10; total refrigerant flow rate Q H flowing through the indoor heat exchangers 22 and 22'; For example, G C = G M + G C , and Q H is Q H = G C (i c − i d ) = G M (i c − i d ) + G P (i c − i d ) In other words, the refrigerant heater 11 Heating capacity Q RH Q RH = G P (i c − i d ) This increases the heating capacity by an amount of It was used as a means of achieving However, in order to perform single-room heating operation in such a conventional air-conditioning system, either the electric heater 19 or 19' of the refrigerant heater 11 is turned off to reduce the heating amount.
When trying to reduce Q RH by half, there were the following drawbacks.
冷媒ポンプ10の冷媒流量GPは所要の最大能
力、すなわち暖房2室運転時の冷媒加熱能力QRH
に合わせて設計されており、電気ヒータ19,1
9′が共にONになつた時に冷媒加熱器11を出
た冷媒の状態が適性な過熱ガス域となるように設
計される。その理由は、圧縮機5から出た吐出ガ
スと合流して4第2図c点)、四方弁6、冷媒配
管3を経て屋内熱交換器22および22′の入口
に至る経路中の冷媒ガス状態を過熱ガス状態に保
つためである。もし冷媒加熱器11の出口の出口
冷媒状態が飽和状態に近いと、圧縮機5との合流
点(第3図c点)は飽和ガス領域に近づく事にな
り、屋内熱交換器22および22′の入口に至る
前に、経路中での放熱により飽和域に達してしま
い、本来は暖房能力に100%利用すべき凝縮潜熱
の一部が失われてしまい、暖房効率の低下を招く
事になる。 The refrigerant flow rate G P of the refrigerant pump 10 is the required maximum capacity, that is, the refrigerant heating capacity Q RH when operating two heating rooms.
Electric heater 19,1
It is designed so that the state of the refrigerant exiting the refrigerant heater 11 when both 9' are turned on is in an appropriate superheated gas region. The reason for this is that the refrigerant gas in the path that merges with the discharge gas from the compressor 5 (point c in Figure 2), passes through the four-way valve 6, and the refrigerant pipe 3, and reaches the inlets of the indoor heat exchangers 22 and 22'. This is to maintain the state of superheated gas. If the outlet refrigerant state at the outlet of the refrigerant heater 11 is close to the saturated state, the confluence point with the compressor 5 (point c in Figure 3) will approach the saturated gas region, and the indoor heat exchanger 22 and 22' Before reaching the inlet, the saturation region is reached due to heat dissipation in the path, and a part of the condensed latent heat that should originally be used 100% for heating capacity is lost, leading to a decrease in heating efficiency. .
しかしながら、暖房1室運転時は電気ヒータ1
9,19′の一方をOFFにする事は、屋内熱交換
器の台数減少による冷媒回路の高圧異常上昇を防
ぐ点からは必要不可欠である。したがつて冷媒加
熱能力QRHを半減させた場合は、冷媒ポンプ10
の冷媒流量GPが暖房2室時と同一であれば冷媒
加熱器11の出口冷媒状態は飽和域に入つてしま
い(第3図g点)、前述の暖房効率の低下を招く
という欠点を生じてくる。これを防止するために
冷媒ポンプ10の流量GPを加熱量QRHの変化に合
わせて変化させ、冷媒加熱器11の出口冷媒状態
を一定の過熱ガス状態に保つ必要があつた。この
ため冷媒ポンプ10の流量可変手段を設ける必要
がある。具体的には冷媒ポンプ10の回転数を変
化させる方法や冷媒ポンプ10の出口または入口
側に流量調整弁を設ける方法があつたが、前者は
電気的な制御回路が必要であり、後者は弁を駆動
する可動部分が必要であるなど、共にコストアツ
プや複雑化の要因となつていた。 However, when operating one heating room, electric heater 1
Turning off one of 9 and 19' is essential from the point of view of preventing an abnormal rise in high pressure in the refrigerant circuit due to a reduction in the number of indoor heat exchangers. Therefore, if the refrigerant heating capacity Q RH is halved, the refrigerant pump 10
If the refrigerant flow rate G P is the same as when heating two rooms, the refrigerant state at the outlet of the refrigerant heater 11 will enter the saturated region (point g in Figure 3), resulting in the aforementioned drawback of decreasing heating efficiency. It's coming. In order to prevent this, it was necessary to change the flow rate G P of the refrigerant pump 10 in accordance with the change in the heating amount Q RH to maintain the refrigerant state at the outlet of the refrigerant heater 11 in a constant superheated gas state. For this reason, it is necessary to provide a flow rate variable means for the refrigerant pump 10. Specifically, there are methods of changing the rotation speed of the refrigerant pump 10 and methods of providing a flow rate adjustment valve at the outlet or inlet side of the refrigerant pump 10, but the former requires an electrical control circuit, and the latter requires a valve. Both of these factors increased cost and complexity, such as the need for moving parts to drive the motor.
発明の目的
本発明は、冷媒加熱器出口と圧縮機吐出ガス配
管との間に冷媒気液分離器を設け、その気液分離
器の液溜り部と冷媒ポンプ吸い込み側とを絞り抵
抗を介して連絡するバイパス回路を設けるという
安価な簡単な構成で冷媒ポンプの流量制御を行な
い、冷媒加熱器の加熱量が暖房2室時から暖房1
室時へと大きく変化しても、冷媒加熱器出口の冷
媒状態を最低限、飽和ガス状態に保つ冷媒流量制
御手段を提供する事を目的とするものである。Purpose of the Invention The present invention provides a refrigerant gas-liquid separator between the refrigerant heater outlet and the compressor discharge gas pipe, and connects the liquid reservoir of the gas-liquid separator and the refrigerant pump suction side through a throttling resistor. The flow rate of the refrigerant pump is controlled using an inexpensive and simple configuration that includes a connecting bypass circuit, and the heating amount of the refrigerant heater changes from heating 2 rooms to heating 1 room.
It is an object of the present invention to provide a refrigerant flow rate control means that maintains the refrigerant state at the outlet of a refrigerant heater to a saturated gas state at the minimum even if the room temperature changes significantly.
発明の構成
この目的を達成するために本発明は、高圧冷媒
凝縮熱交換器と、低圧蒸発熱交換器および圧縮機
により構成されるヒートポンプ暖房サイクルに、
前記高圧冷媒凝縮熱交換器を出た高圧液冷媒を冷
媒ポンプ、冷媒加熱器および冷媒気液分離器を介
して圧縮機吐出冷媒回路へ導く冷媒回路を設け、
さらに前記冷媒気液分離器の液溜り部分と前記冷
媒ポンプ吸い込み側とを絞り抵抗を介して連絡す
るバイパス回路を設けたものである。Structure of the Invention To achieve this object, the present invention provides a heat pump heating cycle composed of a high-pressure refrigerant condensing heat exchanger, a low-pressure evaporative heat exchanger, and a compressor.
A refrigerant circuit is provided for guiding the high-pressure liquid refrigerant exiting the high-pressure refrigerant condensing heat exchanger to a compressor discharge refrigerant circuit via a refrigerant pump, a refrigerant heater, and a refrigerant gas-liquid separator,
Furthermore, a bypass circuit is provided that connects the liquid reservoir portion of the refrigerant gas-liquid separator and the suction side of the refrigerant pump via a throttling resistor.
この構成により、冷媒加熱器の加熱量が変化し
ても冷媒加熱器出口の冷媒状態を最低限の飽和ガ
ス状態に保つことができる。 With this configuration, even if the heating amount of the refrigerant heater changes, the state of the refrigerant at the outlet of the refrigerant heater can be maintained at the minimum saturated gas state.
実施例の説明
以下、本発明の一実施例について添付図面の第
1図を参考に説明する。DESCRIPTION OF THE EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. 1 of the accompanying drawings.
同図において、第2図の従来例と同一部品は同
一番号にて示してある。従来例と異なる構成部分
は、冷媒加熱器11の出口側と逆止弁12との間
に冷媒気液分離器23を設け、前記冷媒気液分離
器23の液溜り部24と冷媒ポンプ10の吸込み
側とを絞り抵抗25を介して連絡するバイパス回
路26を設けている点である。前記絞り抵抗25
は毛細管で構成されているが、所要の流通抵抗が
得られるものであれば、どのような構成でもよ
い。 In the figure, parts that are the same as those in the conventional example of FIG. 2 are designated by the same numbers. Components different from the conventional example include a refrigerant gas-liquid separator 23 provided between the outlet side of the refrigerant heater 11 and the check valve 12, and a liquid reservoir 24 of the refrigerant gas-liquid separator 23 and the refrigerant pump 10. The main feature is that a bypass circuit 26 is provided which communicates with the suction side via a throttle resistor 25. The aperture resistor 25
is composed of a capillary tube, but any structure may be used as long as the required flow resistance can be obtained.
次に本発明の動作を説明する。 Next, the operation of the present invention will be explained.
暖房2室運転時、冷媒加熱器11の加熱能力
QRHは電気ヒータ19,19′が共にONされて供
給されており、冷媒加熱器11の出口冷媒状態も
適性な過熱ガス状態を維持しているとする。した
がつて冷媒気液分離器23内には液冷媒は存在し
ない。この時、冷媒ポンプ10の吸込み側には絞
り抵抗25を通つて冷媒気液分離器23内の冷媒
ガスの一部が流入している(破線矢印)。したが
つて冷媒ポンプ10には受液器9から来た高圧の
液冷媒だけでなくバイパス回路17を通つて来た
ガス冷媒が気泡の状態で混入する。しかし、絞り
抵抗25の入口がガス冷媒であるため、そのバイ
パス流路抵抗が大であり、バイパス流量は少なく
する事ができ、冷媒気液分離器23から圧縮器へ
向かう冷媒流量は十分に確保する事ができる。 Heating capacity of refrigerant heater 11 when operating two heating rooms
It is assumed that Q RH is supplied with both the electric heaters 19 and 19' turned on, and the refrigerant state at the outlet of the refrigerant heater 11 maintains an appropriate superheated gas state. Therefore, no liquid refrigerant exists in the refrigerant gas-liquid separator 23. At this time, a part of the refrigerant gas in the refrigerant gas-liquid separator 23 flows into the suction side of the refrigerant pump 10 through the throttle resistor 25 (dashed line arrow). Therefore, not only the high-pressure liquid refrigerant coming from the liquid receiver 9 but also the gas refrigerant coming through the bypass circuit 17 is mixed into the refrigerant pump 10 in the form of bubbles. However, since the inlet of the throttle resistor 25 is a gas refrigerant, its bypass flow path resistance is large, and the bypass flow rate can be reduced, ensuring a sufficient refrigerant flow rate from the refrigerant gas-liquid separator 23 to the compressor. I can do that.
次に暖房1室運転時の動作について説明する。
暖房1室時一方の屋内ユニツト、例えば2′は停
止されるから、冷媒加熱器11内の電気ヒータ1
9′もOFFとなり冷媒加熱能力QRHは減少する。
この時、冷媒ポンプ10の流量はポンプ回転数が
一定回転であるのでほとんど減少しない。 Next, the operation during single room heating operation will be explained.
When heating one room, one indoor unit, for example 2', is stopped, so the electric heater 1 in the refrigerant heater 11
9' is also turned off, and the refrigerant heating capacity QRH decreases.
At this time, the flow rate of the refrigerant pump 10 hardly decreases because the pump rotation speed is constant.
したがつて、冷媒加熱器11の出口暖房状態は
冷媒エンタルピが減少し、飽和域内に入つて来る
事になり、冷媒気液分離器23内には液冷媒が溜
め始め、前記絞り抵抗25の入口側には液冷媒が
存在するようになる。この結果、絞り抵抗25の
バイパス流路抵抗は大巾に減少し、バイパス流量
を増大させる。絞り抵抗25の流路抵抗を適切に
選べば、冷媒気液分離器23内の液冷媒はバイパ
ス回路26を介して冷媒ポンプ10の吸い込み側
へ返し、ガス冷媒は飽和ガスの状態で圧縮機5の
吐出ガスとの合流点(c点)に送る事ができる。 Therefore, in the heating state at the exit of the refrigerant heater 11, the refrigerant enthalpy decreases and enters the saturated region, and liquid refrigerant begins to accumulate in the refrigerant vapor-liquid separator 23, and the inlet of the throttle resistor 25 There will be liquid refrigerant on the side. As a result, the bypass flow path resistance of the throttle resistor 25 is greatly reduced, increasing the bypass flow rate. If the flow path resistance of the throttle resistor 25 is appropriately selected, the liquid refrigerant in the refrigerant gas-liquid separator 23 is returned to the suction side of the refrigerant pump 10 via the bypass circuit 26, and the gas refrigerant is returned to the compressor 5 in a saturated gas state. can be sent to the confluence point (point c) with the discharged gas.
この結果、圧縮機5からでた吐出冷媒ガスとの
合流点(第1図c点)の過熱度は暖房2室時より
は少ないが、依然として保たれ、四方弁6、冷媒
配管3を経て屋内熱交換器2の入口に至る経路中
の冷媒ガス状態を過熱ガス状態に保つ事ができ、
その経路中では放熱による冷媒の凝縮を防止で
き、屋内熱交換器2内で凝縮潜熱を有効に使用で
き、暖房効率の低下を防止できる。 As a result, the degree of superheating at the confluence point (point c in Figure 1) with the discharged refrigerant gas from the compressor 5 is lower than when heating two rooms, but it is still maintained, and it is passed through the four-way valve 6 and the refrigerant pipe 3 into the room. The state of the refrigerant gas in the path leading to the inlet of the heat exchanger 2 can be maintained in a superheated gas state,
In the path, condensation of the refrigerant due to heat radiation can be prevented, and the latent heat of condensation can be effectively used within the indoor heat exchanger 2, thereby preventing a decrease in heating efficiency.
発明の効果
以上述べたように本発明は、ヒートポンプ暖房
サイクルにおいて、高圧冷媒凝縮熱交換器を出た
高圧冷媒液を分岐させ、低圧蒸発熱交換器および
圧縮機への冷媒回路の他に、前記高圧液冷媒を冷
媒ポンプ、冷媒加熱器および冷媒気流分離器を介
して、圧縮機吐出冷媒回路へ導く冷媒回路を設
け、前記冷媒気液分離器の液溜り部分と前記冷媒
ポンプ吸い込み側とを絞り抵抗を介して連絡する
バイパス回路を設けるという安価で簡単な構成に
より、冷媒加熱器の加熱能力が変化する事による
冷媒加熱器出口冷媒の状態変化を利用し、バイパ
ス回路のバイパス流量を調整し、圧縮機の吐出ガ
スとの合流点に向かう冷媒流量を制御する事がで
きる。その結果、冷媒気液分離器出口の冷媒の状
態を最低限、略一定の飽和ガス状態に保つ事がで
き、屋内熱交換器入口前で冷媒ガスが凝縮してし
まい、暖房効率が低下するのを防止する事ができ
る。なお、本発明の実施例では2室冷暖房装置に
ついて述べたが、屋内ユニツトが各1台の1室冷
暖房装置で本発明を実施しても、冷媒加熱能力の
変化に対しては同様の効果を有する事は言うまで
もない。Effects of the Invention As described above, the present invention branches the high-pressure refrigerant liquid exiting the high-pressure refrigerant condensing heat exchanger in a heat pump heating cycle, and in addition to the refrigerant circuit to the low-pressure evaporative heat exchanger and compressor, A refrigerant circuit is provided that guides high-pressure liquid refrigerant to a compressor discharge refrigerant circuit via a refrigerant pump, a refrigerant heater, and a refrigerant air flow separator, and the liquid reservoir portion of the refrigerant gas-liquid separator and the refrigerant pump suction side are throttled. By using a simple and inexpensive configuration that includes a bypass circuit that communicates through a resistor, the bypass flow rate of the bypass circuit can be adjusted by utilizing changes in the state of the refrigerant at the outlet of the refrigerant heater due to changes in the heating capacity of the refrigerant heater. It is possible to control the flow rate of refrigerant heading to the confluence point with the discharge gas of the compressor. As a result, the state of the refrigerant at the outlet of the refrigerant gas-liquid separator can be maintained at a minimum, almost constant saturated gas state, which prevents refrigerant gas from condensing before the inlet of the indoor heat exchanger and reducing heating efficiency. can be prevented. In the embodiment of the present invention, a two-room air-conditioning system has been described, but even if the present invention is implemented with a single-room air-conditioning system in which each indoor unit has one unit, the same effect can be obtained with respect to changes in refrigerant heating capacity. Needless to say, I have one.
第1図は本発明の冷暖房装置の一実施例を示す
冷媒回路図、第2図は従来の冷暖房装置の冷媒回
路図、第3図は第2図の冷暖房装置の動作を表わ
すモリエル線図である。
5……圧縮機、7……屋外熱交換器、10……
冷媒ポンプ、11……冷媒加熱器、22,22′
……屋内熱交換器、23……冷媒気液分離器、2
5……絞り抵抗、26……バイパス回路。
Fig. 1 is a refrigerant circuit diagram showing an embodiment of the air conditioning system of the present invention, Fig. 2 is a refrigerant circuit diagram of a conventional air conditioning system, and Fig. 3 is a Mollier diagram showing the operation of the air conditioning system shown in Fig. 2. be. 5...Compressor, 7...Outdoor heat exchanger, 10...
Refrigerant pump, 11... Refrigerant heater, 22, 22'
... Indoor heat exchanger, 23 ... Refrigerant gas-liquid separator, 2
5...Aperture resistance, 26...Bypass circuit.
Claims (1)
および圧縮機により構成されるヒートポンプ暖房
サイクルに、前記高圧冷媒凝縮熱交換器を出た高
圧液冷媒を冷媒ポンプ、冷媒加熱器および冷媒気
液分離器を介して圧縮機吐出冷媒回路へ導く冷媒
回路を設け、さらに前記冷媒気液分離器の液溜り
部分と前記冷媒ポンプ吸い込み側とを絞り抵抗を
介して連絡するバイパス回路を設けた冷暖房装
置。1. The high-pressure liquid refrigerant that has exited the high-pressure refrigerant condensing heat exchanger is passed through a refrigerant pump, a refrigerant heater, and a refrigerant gas-liquid to a heat pump heating cycle composed of a high-pressure refrigerant condensing heat exchanger, a low-pressure evaporative heat exchanger, and a compressor. A heating and cooling system comprising a refrigerant circuit that leads to a compressor discharge refrigerant circuit via a separator, and a bypass circuit that connects a liquid reservoir portion of the refrigerant gas-liquid separator and the suction side of the refrigerant pump via a throttling resistor. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16706984A JPH0245101B2 (en) | 1984-08-09 | 1984-08-09 | REIDANBOSOCHI |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16706984A JPH0245101B2 (en) | 1984-08-09 | 1984-08-09 | REIDANBOSOCHI |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6144256A JPS6144256A (en) | 1986-03-03 |
| JPH0245101B2 true JPH0245101B2 (en) | 1990-10-08 |
Family
ID=15842827
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16706984A Expired - Lifetime JPH0245101B2 (en) | 1984-08-09 | 1984-08-09 | REIDANBOSOCHI |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0245101B2 (en) |
-
1984
- 1984-08-09 JP JP16706984A patent/JPH0245101B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6144256A (en) | 1986-03-03 |
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