JPS62142964A - heating device - Google Patents
heating deviceInfo
- Publication number
- JPS62142964A JPS62142964A JP60283562A JP28356285A JPS62142964A JP S62142964 A JPS62142964 A JP S62142964A JP 60283562 A JP60283562 A JP 60283562A JP 28356285 A JP28356285 A JP 28356285A JP S62142964 A JPS62142964 A JP S62142964A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- refrigerant
- gas
- liquid receiver
- receiver
- 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.)
- Granted
Links
Landscapes
- Central Heating Systems (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- General Preparation And Processing Of Foods (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
本発明はヒートポンプ式暖房装置の性能向上に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to improving the performance of heat pump type heating devices.
従来の技術
従来のヒートポンプ式暖房装置は外気温度が低下するに
つれて冷媒の蒸発温度が低下し、その結果、凝縮器への
冷媒循環量が減少し暖房能力が低下するという欠点があ
った。この暖房能力の低下を補うため第2図に示すよう
に圧縮機1.凝縮器2、減圧装置3.蒸発器4からなる
暖房主循環回路の液化冷媒を第1逆止弁6を介し受液器
5へ送り、制御開閉弁7の開閉により、すなわち制御開
閉弁7が開のときは前記受液器5へ溜っている液冷媒を
第2逆上弁8を通って加熱器9へ重力により供給し、こ
のときは前記受液器5と加熱器9とは均圧されているた
め第1逆上弁6により受液器5へは暖房主従ち回路から
液冷媒は流入せす、受液器5の液冷媒がなくなると前記
制御開閉弁7を閉じ、受液器5へ暖房主循環回路から液
冷媒を第1逆止弁6を通って流入させ(このとき加熱器
圧力は受液器圧力より高いので受液器5への流入液冷媒
は第2逆上弁8により加熱器9へは流れ込まない。)
受液器5へ液冷媒が溜ると再び制御開閉弁7を開にし加
熱器9へ液冷媒を供給する。すなわち加熱器9へは受液
器5から間欠的に液冷媒が供給され、加熱器9で吸熱蒸
発した冷媒ガスは圧縮機1の吐出ガスと共に凝縮器2へ
送られ低外気温時における凝縮能力低下の防止を図って
いる。BACKGROUND OF THE INVENTION Conventional heat pump heating systems have had the disadvantage that the evaporation temperature of the refrigerant decreases as the outside air temperature decreases, resulting in a decrease in the amount of refrigerant circulated to the condenser and a decrease in heating capacity. In order to compensate for this decrease in heating capacity, the compressor 1. Condenser 2, pressure reducing device 3. The liquefied refrigerant in the heating main circulation circuit consisting of the evaporator 4 is sent to the liquid receiver 5 via the first check valve 6, and when the control on-off valve 7 is opened or closed, that is, when the control on-off valve 7 is open, the liquid refrigerant is sent to the liquid receiver 5 through the first check valve 6. The liquid refrigerant accumulated in the liquid refrigerant 5 is supplied by gravity to the heater 9 through the second reverse valve 8. At this time, since the liquid receiver 5 and the heater 9 are pressure equalized, The liquid refrigerant flows into the liquid receiver 5 from the heating main circulation circuit by the valve 6. When the liquid refrigerant in the liquid receiver 5 runs out, the control on-off valve 7 is closed, and the liquid refrigerant flows into the liquid receiver 5 from the heating main circulation circuit. The refrigerant is caused to flow through the first check valve 6 (at this time, the heater pressure is higher than the liquid receiver pressure, so the liquid refrigerant flowing into the liquid receiver 5 is caused to flow into the heater 9 by the second check valve 8). do not have.)
When the liquid refrigerant accumulates in the liquid receiver 5, the control valve 7 is opened again to supply the liquid refrigerant to the heater 9. In other words, the liquid refrigerant is intermittently supplied to the heater 9 from the liquid receiver 5, and the refrigerant gas that has absorbed heat and evaporated in the heater 9 is sent to the condenser 2 together with the discharge gas of the compressor 1 to improve the condensation capacity at low outside temperatures. Efforts are being made to prevent this decline.
(例えば特開昭60−89627号公報)発明が解決し
ようとする問題点
しかしながら第2図のような構成では、受液器5に溜っ
た液冷媒を加熱器9へ供給する際、開状態の制御開閉弁
7を通って加熱器9で吸熱ガス化した冷媒が受液器5へ
流入し受液器5の温度が上昇し、制御開閉弁7の閉時暖
房主循環回路から第1逆止弁6を通って受液器5へ液冷
媒を流入させる時、受液器5のガス部容積が液部の増加
により圧縮されて、受液器5への液冷媒流入量が減少し
、その結果加熱器9の液冷媒量が不足し加熱器9内の冷
媒ガス温度が上昇し、冷媒の熱安定性が損われるという
間m点を有していた。またさらに暖房主循環回路の凝縮
器2出口の液冷媒を円滑に受液器5へ流入させるために
前記受液器5のガス冷媒を暖房主循環回路の氏圧側へ逃
がしてやる方法もあるが(例えば特開昭60−9323
7号公報)冷媒回路が複雑になる間m点を有していた。(For example, Japanese Unexamined Patent Publication No. 60-89627) Problems to be Solved by the Invention However, in the configuration as shown in FIG. The refrigerant that has been endothermically gasified by the heater 9 passes through the control on-off valve 7 and flows into the liquid receiver 5, and the temperature of the liquid receiver 5 rises. When liquid refrigerant flows into the liquid receiver 5 through the valve 6, the volume of the gas part of the liquid receiver 5 is compressed due to the increase in the liquid part, and the amount of liquid refrigerant flowing into the liquid receiver 5 decreases. As a result, the amount of liquid refrigerant in the heater 9 was insufficient, the temperature of the refrigerant gas in the heater 9 rose, and the thermal stability of the refrigerant was impaired. Furthermore, in order to smoothly flow the liquid refrigerant at the outlet of the condenser 2 of the heating main circulation circuit into the liquid receiver 5, there is a method in which the gas refrigerant in the liquid receiver 5 is released to the pressure side of the heating main circulation circuit. (For example, JP-A-60-9323
Publication No. 7) The refrigerant circuit had m points while becoming complicated.
本発明はかかる従来の問題点を解決するもので、機器の
信頼性向上をはかると共に榔器のコンパクト化をはかる
目的のものである。The present invention is intended to solve these conventional problems, and aims to improve the reliability of the device and make the shank more compact.
問題点を解決するための手段
上記間m点を解決するために本発明の暖房装置は、圧縮
機、アキュムレータ、凝縮器、減圧装置。Means for Solving the Problems In order to solve the above problems, the heating device of the present invention includes a compressor, an accumulator, a condenser, and a pressure reducing device.
蒸発器とからなるヒートポンプサイクルと、前記ヒート
ポンプサイクルの高圧液部から第1逆上弁を介し連結し
た受液器、前記受液器の下方に第2逆止弁を介して連結
した気液分離器、前記気液分離器からガス戻し管を前記
圧縮機の吐出管と、開閉弁を有する均圧管を前記受液器
と各々連結すると共に前記気液分離器の液管と戻り管を
冷媒加熱器と連結したサイクルとからなり、仕切り板に
より2つの空間を形成する容器の一方を前記アキュムレ
ータ、他方を前記受液器とし、アキュムレータと受液器
とを一体化構成としたものである。a heat pump cycle consisting of an evaporator; a liquid receiver connected from the high-pressure liquid section of the heat pump cycle via a first reverse valve; and a gas-liquid separation unit connected below the liquid receiver via a second check valve. A gas return pipe from the gas-liquid separator is connected to the discharge pipe of the compressor, and a pressure equalization pipe having an on-off valve is connected to the liquid receiver, and the liquid pipe and return pipe of the gas-liquid separator are heated with refrigerant. One of the containers is the accumulator and the other is the liquid receiver, and the accumulator and the liquid receiver are integrated.
作 用
本発明は上記した構成によって受液器はヒートポンプサ
イクルの低圧部であるアキュムレータと仕切り板を介し
て一体化構成としであるので伝熱効果により開閉弁が開
時気液分離器から流入してきたガス冷媒を凝縮させ、開
閉弁が閉時、ヒートポンプサイクル側の高圧液冷媒が受
液器へ流入することが円滑に行なわれる作用があり、そ
の結果気液分離器には受液器から液冷媒が不足すること
なく供給され冷媒加熱器へ供給される液冷媒も不足する
ことはないから冷媒が熱分解することなくサイクルの信
頼性の向上2機器のコンパクト化が得られる。Function The present invention has the above-described structure, and the liquid receiver is integrated with the accumulator, which is the low-pressure part of the heat pump cycle, via the partition plate, so due to the heat transfer effect, when the on-off valve is open, inflow from the gas-liquid separator is prevented. When the on-off valve closes, the high-pressure liquid refrigerant on the heat pump cycle side flows smoothly into the liquid receiver, and as a result, the gas-liquid separator has the effect of condensing the liquid refrigerant from the liquid receiver to the liquid receiver. Since there is no shortage of refrigerant and there is no shortage of liquid refrigerant supplied to the refrigerant heater, the refrigerant does not undergo thermal decomposition, improving cycle reliability and making equipment more compact.
実施例
以下、本発明の実施例を添付図面にもとづいて説明する
。Embodiments Hereinafter, embodiments of the present invention will be described based on the accompanying drawings.
第1図において、10は圧縮機、11は凝縮器、12は
減圧装置、13は蒸発器、14は仕切り板16により受
液器15と一体化構成となっているアキュムレータで、
ヒートポンプサイクルを構成している。17は前記受液
器15とヒートポンプサイクル高圧液部とを接続する管
に配設しである第1逆止弁、18は前記受液器15の下
方に配設しである気液分離器で、前記受液器15とは第
2逆止弁19を介して接続されている。20は前記気液
分離器18と前記圧縮機1の吐出管とを接続するガス戻
し管、21は前記気液分離器18と受液器15とを連結
する均圧管22に配設しである開閉弁、23.24はそ
れぞれ前記気液分離器18に配設しである液管と戻り管
で冷媒加熱器25と連結している。In FIG. 1, 10 is a compressor, 11 is a condenser, 12 is a pressure reducing device, 13 is an evaporator, 14 is an accumulator that is integrated with a liquid receiver 15 by a partition plate 16,
It constitutes a heat pump cycle. 17 is a first check valve disposed in a pipe connecting the liquid receiver 15 and the heat pump cycle high-pressure liquid section; 18 is a gas-liquid separator disposed below the liquid receiver 15; , and is connected to the liquid receiver 15 via a second check valve 19. 20 is a gas return pipe that connects the gas-liquid separator 18 and the discharge pipe of the compressor 1, and 21 is installed in a pressure equalization pipe 22 that connects the gas-liquid separator 18 and the liquid receiver 15. The on-off valves 23 and 24 are connected to the refrigerant heater 25 through a liquid pipe and a return pipe, respectively, which are disposed in the gas-liquid separator 18.
上記構成において圧縮機10で高温高圧になった冷媒は
凝縮器11で凝縮液化し減圧装置12で減圧膨張し蒸発
器13でガス化しアキュムレータ14をへて圧縮機9へ
戻る。一方、前記ヒートポンプサイクルの高圧液部から
分流した液冷媒は開閉弁21が閉のとき第1逆止弁17
を通って受液器15へ溜る。このとき気液分離器18の
圧力は受液器15の圧力よりも高いため第2逆止弁19
により受液器15に流入する液冷媒は気液分離器18へ
流れ込まない。次に受液器15に液冷媒が溜り込むと開
閉弁21を開とし受液器15の圧力は気液分離器18の
圧力と均圧管22により等しくなり、気液分離器18は
受液器15より下方に配設しであるため重力により受液
器15に溜っていた液冷媒は気液分離器18へ流入する
。このとき受液器15の圧力は気液分離器18の圧力と
等しいため第1逆止弁17は閉となりヒートポンプサイ
クル高圧液部から受液器15へ液冷媒は流入しない。気
液分離器18へ流入した液冷媒は自然循環で液管23か
ら冷媒加熱器25へ流入し吸熱蒸発し二相状態で戻り管
24を通り再び気液分離器18へ戻りガス冷媒のみがガ
ス戻し管20を通って圧縮機10の吐出ガスと合流し凝
縮器11へ流入する。又、二相状態で戻り管24を通り
気液分子a器18へ戻ってきた液冷媒は再び冷媒加熱器
25へ流入する。以上のように開閉弁21の開閉により
受液器15ヘヒ一トポンプサイクル高圧液部から溜り込
んだ液冷媒を間欠的に気液分離器18へ供給してやり気
液分離器1日と冷媒加熱器25の二相自然循環サイクル
を行なわせることにより連続的に冷媒加熱器25で吸熱
蒸発したガス冷媒を圧縮機1の吐出ガスと合流させ凝縮
器2へ搬送するものである。ここで冷媒加熱器25から
の吸熱を冷媒が熱分解することなく二相状態で行なわせ
るためには受液器15ζこ円滑に液冷媒を溜め込むこと
が必要であるが本実施例ではヒートポンプサイクルの低
圧側であるアキュムレータ14と仕切り板16を介して
受液器15を一体化しであるため、開閉弁21が開時、
気液分陰器18から均圧管22を通って流入するガス冷
媒がアキュムレータ14の低温部に接し凝縮し、開閉弁
21が閉時高圧液冷媒が受液器15流人時ガス部容積を
圧縮することがなく、円滑に受液器15ヘヒートポンプ
サイクル側から液冷媒が溜り込む。したがって受液器1
5から気液分離器18への冷媒供給量も不足することな
くその結果冷媒加熱器25での冷媒の熱分解が防止でき
サイクルの信頼性が向上すると共に機器のコンパクト化
が可能となる効果がある。In the above configuration, the refrigerant that has become high temperature and high pressure in the compressor 10 is condensed and liquefied in the condenser 11, expanded under reduced pressure in the pressure reducing device 12, gasified in the evaporator 13, and returned to the compressor 9 through the accumulator 14. On the other hand, when the on-off valve 21 is closed, the liquid refrigerant branched from the high-pressure liquid part of the heat pump cycle flows through the first check valve 17.
The liquid passes through and accumulates in the liquid receiver 15. At this time, since the pressure in the gas-liquid separator 18 is higher than the pressure in the liquid receiver 15, the second check valve 19
Therefore, the liquid refrigerant flowing into the liquid receiver 15 does not flow into the gas-liquid separator 18. Next, when the liquid refrigerant accumulates in the liquid receiver 15, the on-off valve 21 is opened, and the pressure in the liquid receiver 15 becomes equal to the pressure in the gas-liquid separator 18 through the pressure equalization pipe 22, and the gas-liquid separator 18 becomes equal to the pressure in the liquid receiver 18. Since the liquid refrigerant is disposed below the liquid receiver 15, the liquid refrigerant accumulated in the liquid receiver 15 flows into the gas-liquid separator 18 due to gravity. At this time, the pressure in the liquid receiver 15 is equal to the pressure in the gas-liquid separator 18, so the first check valve 17 is closed, and liquid refrigerant does not flow into the liquid receiver 15 from the high-pressure liquid section of the heat pump cycle. The liquid refrigerant that has flowed into the gas-liquid separator 18 flows through the liquid pipe 23 into the refrigerant heater 25 through natural circulation, absorbs heat, evaporates, passes through the return pipe 24 in a two-phase state, returns to the gas-liquid separator 18, and only the gas refrigerant becomes a gas. It passes through the return pipe 20, merges with the discharge gas of the compressor 10, and flows into the condenser 11. Further, the liquid refrigerant that has returned to the gas-liquid molecular a device 18 through the return pipe 24 in a two-phase state flows into the refrigerant heater 25 again. As described above, by opening and closing the on-off valve 21, the liquid refrigerant accumulated in the liquid receiver 15 is intermittently supplied from the high-pressure liquid section to the gas-liquid separator 18 and the refrigerant heater 25. By performing a two-phase natural circulation cycle, the gas refrigerant that has been endothermically evaporated in the refrigerant heater 25 is combined with the discharge gas of the compressor 1 and conveyed to the condenser 2. In order to absorb heat from the refrigerant heater 25 in a two-phase state without thermally decomposing the refrigerant, it is necessary to smoothly store the liquid refrigerant in the liquid receiver 15ζ. Since the accumulator 14 on the low pressure side and the liquid receiver 15 are integrated through the partition plate 16, when the on-off valve 21 is opened,
The gas refrigerant flowing from the gas-liquid separator 18 through the pressure equalization pipe 22 contacts the low-temperature part of the accumulator 14 and condenses, and when the on-off valve 21 is closed, the high-pressure liquid refrigerant compresses the volume of the gas part of the liquid receiver 15 when flowing. The liquid refrigerant smoothly accumulates in the liquid receiver 15 from the heat pump cycle side without any problems. Therefore, receiver 1
5 to the gas-liquid separator 18, and as a result, thermal decomposition of the refrigerant in the refrigerant heater 25 is prevented, cycle reliability is improved, and the equipment can be made more compact. be.
発明の効果
以上のように本発明の暖房装置によれば、ヒートポンプ
サイクルのアキュムレーターと受液器とを一体化しであ
るため気液分離器へ受液器から液冷媒を供給する際、均
圧管を通って気液分離器から受液器へ流入するガス冷媒
をアキュムレータの低温部で凝縮させ受液器ヘヒートポ
ンプサイクル高圧液冷媒が流入する際、受液器のガス部
容積減少に伴なう受液器圧力上昇を防止し受液器への液
冷媒流入が円滑となり、その結果気液分離器への受液器
からの液冷媒供給が不足することなく冷媒加熱器での冷
媒熱分解が防止できシステムの信頼性が向上すると共に
機器のコンパクト化が可能となり、外気温度の影響の少
ない快適な暖房装置が得られるものである。Effects of the Invention As described above, according to the heating device of the present invention, since the accumulator of the heat pump cycle and the liquid receiver are integrated, when supplying liquid refrigerant from the liquid receiver to the gas-liquid separator, the pressure equalizing pipe is used. The gas refrigerant flowing from the gas-liquid separator to the liquid receiver is condensed in the low-temperature part of the accumulator, and when the high-pressure liquid refrigerant flows into the heat pump cycle, the volume of the gas part of the liquid receiver decreases. Preventing pressure rise in the liquid receiver, the flow of liquid refrigerant into the liquid receiver becomes smooth, and as a result, refrigerant thermal decomposition in the refrigerant heater can be performed without running out of liquid refrigerant supply from the liquid receiver to the gas-liquid separator. This can improve the reliability of the system, make the equipment more compact, and provide a comfortable heating system that is less affected by outside temperature.
第1図は本発明の一実施例による暖房装置の回路構成図
、第2図は従来の暖房装置なの回路構成図である。
10・・・・・・圧縮機、11・・・・・・凝縮器、1
2・・・・・・減圧装置、13・・・・・・蒸発器、1
4・・・・・・アキュムレータゝ、15・・・・・・受
液器、16・・・・・・仕切り板、17・・・・・・第
1逆止弁、18・・・・・・気液分離器、19・・・・
・・第2逆止弁、20・・・・・・ガス戻し管、21・
・・・・・開閉弁、22・・・・・・均圧管、25・・
・・・・冷媒加熱器。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名IQ
−−−L島風
/J−一一毛禿器
/4−−− 7キユAI/−タ
lσ−史戊各
第2図FIG. 1 is a circuit diagram of a heating device according to an embodiment of the present invention, and FIG. 2 is a circuit diagram of a conventional heating device. 10... Compressor, 11... Condenser, 1
2... Pressure reducing device, 13... Evaporator, 1
4... Accumulator, 15... Liquid receiver, 16... Partition plate, 17... First check valve, 18...・Gas-liquid separator, 19...
...Second check valve, 20...Gas return pipe, 21.
...Opening/closing valve, 22...Pressure equalization pipe, 25...
...Refrigerant heater. Name of agent: Patent attorney Toshio Nakao and one other person IQ
---L Shimakaze/J-11 hairless device/4---7 Kiyu AI/-Talσ-Shiho each 2nd figure
Claims (1)
からなるヒートポンプサイクルを有し、前記ヒートポン
プサイクルの高圧液部から第1逆止弁を介し連結した受
液器、前記受液器の下方に第2逆止弁を介して連結した
気液分離器、前記気液分離器からガス戻し管を前記圧縮
機吐出管と、開閉弁を有する均圧管を前記受液器と各々
連結すると共に、前記気液分離器の液管と戻り管を冷媒
加熱器と連結したサイクルとからなり、仕切り板により
2つの空間を形成する容器の一方を前記アキュムレータ
、他方を前記受液器としてなる暖房装置。It has a heat pump cycle consisting of a compressor, an accumulator, a condenser, a pressure reducer, and an evaporator, and a liquid receiver connected from the high-pressure liquid part of the heat pump cycle via a first check valve, and a liquid receiver below the liquid receiver. A gas-liquid separator connected via a second check valve, a gas return pipe from the gas-liquid separator connected to the compressor discharge pipe, and a pressure equalization pipe having an on-off valve connected to the liquid receiver, respectively; A heating device comprising a cycle in which a liquid pipe and a return pipe of a gas-liquid separator are connected to a refrigerant heater, and in which two spaces are formed by a partition plate, one of which is the accumulator and the other is the liquid receiver.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60283562A JPS62142964A (en) | 1985-12-17 | 1985-12-17 | heating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60283562A JPS62142964A (en) | 1985-12-17 | 1985-12-17 | heating device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62142964A true JPS62142964A (en) | 1987-06-26 |
| JPH0566502B2 JPH0566502B2 (en) | 1993-09-21 |
Family
ID=17667134
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60283562A Granted JPS62142964A (en) | 1985-12-17 | 1985-12-17 | heating device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS62142964A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS553321U (en) * | 1978-06-19 | 1980-01-10 | ||
| JPS6071862A (en) * | 1983-09-28 | 1985-04-23 | 松下電器産業株式会社 | Heat pump device |
| JPS6089627A (en) * | 1983-10-21 | 1985-05-20 | Mitsubishi Electric Corp | Heating device |
-
1985
- 1985-12-17 JP JP60283562A patent/JPS62142964A/en active Granted
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS553321U (en) * | 1978-06-19 | 1980-01-10 | ||
| JPS6071862A (en) * | 1983-09-28 | 1985-04-23 | 松下電器産業株式会社 | Heat pump device |
| JPS6089627A (en) * | 1983-10-21 | 1985-05-20 | Mitsubishi Electric Corp | Heating device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0566502B2 (en) | 1993-09-21 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |