JPH057632B2 - - Google Patents
Info
- Publication number
- JPH057632B2 JPH057632B2 JP60161272A JP16127285A JPH057632B2 JP H057632 B2 JPH057632 B2 JP H057632B2 JP 60161272 A JP60161272 A JP 60161272A JP 16127285 A JP16127285 A JP 16127285A JP H057632 B2 JPH057632 B2 JP H057632B2
- Authority
- JP
- Japan
- Prior art keywords
- antifreeze
- heating
- heat
- air
- heat 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
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- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Steam Or Hot-Water Central Heating Systems (AREA)
- Compressor (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は空気熱源ヒートポンプの着霜、着氷防
止装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a frosting and icing prevention device for an air source heat pump.
各種空気調和用熱源機器の中でヒートポンプの
省エネルギー性が再認識されつつある。
Among various air-conditioning heat source devices, the energy-saving properties of heat pumps are being rediscovered.
圧縮式ヒートポンプの中では、無限にある空気
を熱源とした空気熱源ヒートポンプが製品として
販売されているが、厳冬期などには空気からの取
熱部に着氷、着霜が生じ、能力の低下、動力の上
昇が生じるため、各種デフロスト法が開発されて
いる。 Among compression heat pumps, air source heat pumps are sold as products that use the infinite amount of air as a heat source, but during the harsh winter months, ice and frost build up on the heat extraction section from the air, resulting in a decrease in capacity. , various defrosting methods have been developed because of the increase in power.
然し、此のデフロスト期間中は暖房能力の中
断、低下が生じ、また一般にはデフロストに要す
る無駄なエネルギーの投入があるために、総合的
な効率は低いのが一般である。 However, during this defrosting period, the heating capacity is interrupted or reduced, and there is generally a waste of energy required for defrosting, so the overall efficiency is generally low.
此の欠点をとり除く手段として、外気側空気熱
交換器部分に不凍液を散布し、着霜、着氷を生じ
させない手法が考案されているが、外気湿度の低
い気象条件では不凍液は濃縮する傾向にあり、逆
に外気湿度の高い気象条件、例えば雨天あるいは
降雪時には次第に不凍液が空気中の水分を吸収し
て濃度低下が生じ、やがては着氷を生じる欠点が
あつた。不凍液濃度の低下に応じ、濃い不凍液を
補充する事はその一つの解決策で此れは既存の技
術という事が出来る。然し単に不凍液を補充する
だけでは空気熱交換器部分の不凍液槽の液位は上
昇する一方であり、場合によつては不凍液がオー
バフローし、不凍液が損耗するのみならず環境に
悪影響を与える。 As a means to eliminate this drawback, a method has been devised to prevent frost and icing by spraying antifreeze on the outside air side air heat exchanger, but antifreeze tends to concentrate in weather conditions with low outside air humidity. On the other hand, in weather conditions where the outside air humidity is high, such as rain or snowfall, the antifreeze solution gradually absorbs moisture from the air, resulting in a decrease in concentration, which eventually leads to icing. Replenishing concentrated antifreeze in response to a decrease in antifreeze concentration is one solution, and this can be said to be an existing technology. However, if the antifreeze solution is simply replenished, the liquid level in the antifreeze tank in the air heat exchanger section will continue to rise, and in some cases, the antifreeze solution may overflow, which not only causes the antifreeze solution to be wasted, but also has a negative impact on the environment.
本発明は外気側熱交換要素に不凍液を散布する
手段及び外部熱源により不凍液中の水分を蒸発さ
せる手段を備えた空気熱源ヒートポンプにおい
て、不凍液中の水分を蒸発させる手段における熱
の有効利用をはかり、もつて加熱に要する熱エネ
ルギーの節約をはかろうとするものである。
The present invention aims to effectively utilize heat in the means for evaporating moisture in the antifreeze in an air source heat pump equipped with a means for distributing antifreeze to an outside air side heat exchange element and a means for evaporating moisture in the antifreeze using an external heat source. The aim is to save the thermal energy required for heating.
以下、本発明の実施例を図面により説明する。 Embodiments of the present invention will be described below with reference to the drawings.
第1図〜第5図は空気熱源ヒートポンプのフロ
ーシートで空気熱源ヒートポンプの外気側熱交換
器の周辺を示すものである。第5図は、従来の外
部加熱源を用いた不凍液濃縮方法を示すものであ
り、第1図〜第4図は本発明の実施例を示すもの
である。 FIGS. 1 to 5 are flow sheets for an air source heat pump, showing the vicinity of the outside air side heat exchanger of the air source heat pump. FIG. 5 shows a conventional antifreeze concentration method using an external heating source, and FIGS. 1 to 4 show embodiments of the present invention.
先づ第5図に基いて従来の技術について説明す
る。 First, the conventional technique will be explained based on FIG.
ヒートポンプの外気側熱交換器1はヒートポン
プの冷媒配管2,29が減圧弁3を介して容器状
の外皮4内部に導かれており、冷媒配管2,29
は熱交換要素6に連通している。外皮4の上部開
口にはフアン7を備え、フアン7は雨除け8によ
り蔽われている。フアン7は雨除け8と外皮4上
部の開口間から外気を吸込み熱交換要素6を介し
て内部冷媒を冬期は加熱するものである。そして
外気は図示矢印イのように外皮4に設けたルーバ
9を通じて外気側に戻るようになつている。外皮
4の底部は不凍液11の溜りとなつており、該不
凍液は主として配管24、吸込管10をとおり不
凍液散布用ポンプ(以下ポンプと称する)12よ
り吸引されるが一部は配管13、制止弁14を通
じて加温器15中に入る。 In the outside air side heat exchanger 1 of the heat pump, the refrigerant pipes 2 and 29 of the heat pump are guided into the inside of the container-shaped outer skin 4 via the pressure reducing valve 3.
is in communication with the heat exchange element 6. A fan 7 is provided at the upper opening of the outer skin 4, and the fan 7 is covered by a rain shield 8. The fan 7 sucks in outside air from between the rain shield 8 and the opening at the top of the outer skin 4 and heats the internal refrigerant through the heat exchange element 6 during the winter. The outside air then returns to the outside air side through a louver 9 provided on the outer skin 4 as shown by arrow A in the figure. The bottom of the outer skin 4 is a reservoir of antifreeze 11, and the antifreeze mainly passes through a pipe 24 and a suction pipe 10 and is sucked by an antifreeze spraying pump (hereinafter referred to as pump) 12, but some of it passes through a pipe 13 and a stop valve. It enters the warmer 15 through 14.
尚、不凍液の溜りは、外皮4の底部のみと限ら
ず、別に並設されるタンクであつても良い。 Note that the antifreeze reservoir is not limited to the bottom of the outer skin 4, but may be a separate tank installed in parallel.
加温濃縮器15は密閉容器中に電気ヒータ16
を備えるものでこゝで不凍液は加温濃縮され、且
つ含有水分は蒸発し上部の排気管17から水蒸気
となつて排出される。加温濃縮器15で加温され
た不凍液は配管18に出て加温濃縮器15中に不
凍液を充満させるようにオリフイス19で絞ら
れ、ついで制止弁20を介して配管24を流れる
不凍液の本流に合流して吸込管10をとおりポン
プ12に吸込まれる。 The heating concentrator 15 has an electric heater 16 in a closed container.
Here, the antifreeze liquid is heated and concentrated, and the water content is evaporated and discharged as water vapor from the upper exhaust pipe 17. The antifreeze heated in the heating concentrator 15 exits to the pipe 18 and is throttled by the orifice 19 so as to fill the heating concentrator 15 with antifreeze.Then, the main stream of antifreeze flows through the pipe 24 via the stop valve 20. The water flows through the suction pipe 10 and is sucked into the pump 12.
ポンプ12で吐出された不凍液は吐出管21を
とおり、外皮4内の上部に配した散布器22によ
り熱交換要素6に散布され、熱交換要素6の表面
に附着して結霜、着氷を防止する一方餘分の不凍
液は下部の溜部にたまるようになつている。 The antifreeze discharged by the pump 12 passes through the discharge pipe 21 and is sprayed onto the heat exchange element 6 by the sprayer 22 disposed in the upper part of the outer skin 4, and adheres to the surface of the heat exchange element 6 to cause frost formation and icing. On the other hand, the antifreeze solution is designed to accumulate in a reservoir at the bottom.
外皮4下部の溜部の不凍液11の規定液面は液
位コントローラ30により検出され、その信号に
より電気ヒータのスイツチを入切するようになつ
ている。 A specified liquid level of the antifreeze liquid 11 in the reservoir at the bottom of the outer skin 4 is detected by a liquid level controller 30, and the electric heater is turned on and off in response to a signal from the liquid level controller 30.
電気ヒータ16の制御はコントローラ30によ
り検出された外皮4の溜り中の不凍液11の水位
が規定水位以上に上昇した場合液位コントローラ
30により電気ヒータのスイツチを入れ、外皮4
の溜り中の不凍液の液位低下により電気ヒータの
スイツチを切るようになつている。 The electric heater 16 is controlled by turning on the electric heater by the liquid level controller 30 when the water level of the antifreeze liquid 11 in the reservoir of the outer skin 4 rises above the specified water level, which is detected by the controller 30.
When the level of antifreeze in the tank drops, the electric heater is turned off.
第1図は、本発明の実施例を示す。 FIG. 1 shows an embodiment of the invention.
加温濃縮器15内で蒸発した不凍液中の水分
は、排気管17を介し、回収熱交換器31へ入
り、負荷側流体の温水を加熱するとともに、凝縮
液化する。液化したドレン39は、ドレン配管3
2により、回収熱交換器外部に排出される。 The water in the antifreeze that evaporated in the heating concentrator 15 enters the recovery heat exchanger 31 via the exhaust pipe 17, heats the hot water of the load side fluid, and condenses and liquefies it. The liquefied drain 39 is transferred to the drain pipe 3
2, the heat is discharged to the outside of the recovery heat exchanger.
第2図は他の実施例を示す。 FIG. 2 shows another embodiment.
加温濃縮器15の内圧を大気圧以下に保持する
よう、不凍液配管13にオリフイス19不凍液配
管18に加温濃縮用不凍液ポンプ36を設け、不
凍液を循環させる。一方、加温濃縮器15内にた
まつた不凝縮ガス(たとえば空気など)を外部に
連続的にあるいは定期的に排出するようガス排気
管33及び排気ポンプ34を設ける。回収熱交換
器31内で凝縮液化したドレン39は、回収熱交
換器31の内圧と外気圧との圧力差分だけ液柱を
かけるためのドレン配管32を経て、温水槽41
に排出する。この、ドレン39は、負荷側温水と
して利用できる。 In order to keep the internal pressure of the heating concentrator 15 below atmospheric pressure, an orifice 19 is provided in the antifreeze pipe 13 and an antifreeze pump 36 for heating and concentration is provided in the antifreeze pipe 18 to circulate the antifreeze. On the other hand, a gas exhaust pipe 33 and an exhaust pump 34 are provided to continuously or periodically exhaust the non-condensable gas (for example, air) accumulated in the heating concentrator 15 to the outside. The drain 39 condensed and liquefied in the recovery heat exchanger 31 passes through a drain pipe 32 for applying a liquid column by the pressure difference between the internal pressure of the recovery heat exchanger 31 and the outside pressure, and then flows to the hot water tank 41.
to be discharged. This drain 39 can be used as load-side hot water.
第3図は他の実施例を示す。 FIG. 3 shows another embodiment.
不凍液配管13及び23に不凍液熱交換器37
をもうけ、加熱器に出入する不凍液を互いに熱交
換する。一方、回収熱交換器31内で凝縮したド
レン39は、ドレン配管32を介して、ドレンポ
ンプ35により外部に排出する。 Antifreeze heat exchanger 37 is installed in antifreeze pipes 13 and 23.
The antifreeze flowing in and out of the heater exchanges heat with each other. On the other hand, the drain 39 condensed within the recovery heat exchanger 31 is discharged to the outside by the drain pump 35 via the drain pipe 32.
第4図は加温濃縮器15内の不凝縮ガスを排出
するために、ドレンポンプの一次側ドレン配管3
2にエジエクタ40を設け、ドレンポンプ35に
より、ドレン39と共に不凝縮ガスを外部に排出
する。 FIG. 4 shows the primary side drain piping 3 of the drain pump in order to discharge the non-condensable gas in the heating concentrator 15.
2 is provided with an ejector 40, and a drain pump 35 discharges non-condensable gas to the outside together with a drain 39.
次に本発明の作用をのべる。 Next, the effects of the present invention will be described.
ポンプ12により、外皮4の溜り中の不凍液の
うち配管13に出て行く分は配管13→制止弁1
4→加温濃縮器15→配管18→制止弁20→と
流れ、外皮4の溜り中の不凍液11を吸出する配
管24からの不凍液の主流と合流して、吸込管1
0→ポンプ12→吐出管21→散布器22→熱交
換要素6→外皮4の不凍液11の溜りと循環す
る。そして不凍液は散布器22→熱交換要素6→
外皮4の不凍液11の溜りと流れる間に散布器2
2に附着している水分及び空気中の水分によりう
すめられ、不凍液の容積は増加する。 The amount of antifreeze in the pool of the outer skin 4 that goes out to the piping 13 by the pump 12 is transferred from the piping 13 to the stop valve 1.
4 → heating concentrator 15 → piping 18 → stop valve 20 →, and merges with the main flow of antifreeze from piping 24 that sucks out antifreeze 11 in the pool of outer skin 4, and then flows into suction pipe 1.
0→pump 12→discharge pipe 21→spreader 22→heat exchange element 6→reservoir of antifreeze 11 in outer skin 4. And the antifreeze is distributed by the sprayer 22 → the heat exchange element 6 →
Spreader 2 is installed between the pool and flow of antifreeze 11 in outer skin 4.
The volume of the antifreeze increases as it is diluted by the moisture attached to the antifreeze and the moisture in the air.
液位コントローラ30が液位上昇を検知すると
液位コントローラ30は電気ヒータのスイツチを
入れ、加温濃縮器15にて不凍液と水との蒸発温
度の差を利用して水分を蒸発させ水分は排気管1
7から排出され、濃度が上昇し容積の減少した不
凍液が加温濃縮器15の出口側配管18に送り出
される。従つて配管24から流入する不凍液と配
管18から流入する濃度の濃くなつた不凍液は吸
込管10では配管24からの不凍液よりは濃度の
濃い不凍液となつており、ポンプ12に吸込まれ
吐出されるので散布器22からは濃度を回復され
た不凍液が散布される。 When the liquid level controller 30 detects a rise in the liquid level, the liquid level controller 30 turns on the electric heater, and uses the difference in evaporation temperature between antifreeze and water to evaporate water in the heating concentrator 15, and the water is exhausted. tube 1
7, the antifreeze liquid whose concentration has increased and whose volume has decreased is sent to the outlet side piping 18 of the heating concentrator 15. Therefore, the antifreeze fluid flowing in from the pipe 24 and the highly concentrated antifreeze fluid flowing in from the pipe 18 have a higher concentration in the suction pipe 10 than the antifreeze fluid flowing from the pipe 24, and are sucked into the pump 12 and discharged. The antifreeze solution whose concentration has been restored is sprayed from the sprayer 22.
外皮4の溜りの不凍液11の液位はかくして次
第に液位が低下し、該液位の低下を液位コントロ
ーラが検知して電気ヒータのスイツチを切る。 The liquid level of the antifreeze liquid 11 in the reservoir of the outer skin 4 thus gradually decreases, and the liquid level controller detects this decrease in the liquid level and switches off the electric heater.
液位コントローラ30が検知する外皮4の溜り
中の不凍液11の液位の上下は不凍液の濃度の淡
濃に照応している。 The rise and fall of the liquid level of the antifreeze liquid 11 in the pool of the outer skin 4 detected by the liquid level controller 30 corresponds to the concentration of the antifreeze liquid.
また、熱交換器37を使用し、加温濃縮器15
に出入する不凍液を互いに熱交換すれば、外皮4
の下部不凍液は加温濃縮器15導出された高温の
不凍液によつて加熱され、加温濃縮器で蒸発する
温度に近い温度まで上昇し、加温濃縮器15では
ほぼ不凍液の含有水分が蒸発する潜熱分だけを入
力してやればよい。ここで、加熱手段としては多
くのものが考えられるが、安全で取扱いが簡便で
あり、又、設備費用の大きくならない電熱ヒータ
が最も好ましい。電気ヒータは濃度検出又は不凍
液槽の液位検出のいずれかもしくは併せて動作作
させても良く、自動的に運転される事が最も良い
が勿論人為的にヒータを投入する方法も可能であ
る。又、この加熱源は電気ヒータ16に限られる
ものではなく、ガス燃焼等一般に加熱源であれば
よいのである。 In addition, a heat exchanger 37 is used, and a heating concentrator 15 is used.
If the antifreeze flowing in and out of the
The lower antifreeze liquid is heated by the high-temperature antifreeze liquid discharged from the heating concentrator 15, and is raised to a temperature close to the evaporation temperature in the heating concentrator 15, and almost all the water contained in the antifreeze liquid is evaporated in the heating concentrator 15. All you have to do is input the latent heat. Although many heating means are conceivable, an electric heater is most preferable because it is safe, easy to handle, and does not require large equipment costs. The electric heater may be operated either by detecting the concentration or by detecting the liquid level in the antifreeze tank, or in combination. Automatic operation is best, but of course it is also possible to manually turn on the heater. Further, this heating source is not limited to the electric heater 16, but may be any general heating source such as gas combustion.
一方、加温濃縮器15で発生した蒸気は、回収
熱交換器31内で負荷側流体の温水を加熱し、凝
縮する。従つて不凍液の加温濃縮に使用されたエ
ネルギのほとんどを、負荷側温水の加熱に利用し
得るため、従来例のごとく、蒸気を単に排出する
ものと比較し、不凍液の加熱濃縮と負荷温水の加
熱の2重の効果を有する。さらに、加温濃縮器1
5及び回収熱交換器31を大気圧以下の真空に保
つことにより、容器としての製作が容易となり、
安全性も増す。 On the other hand, the steam generated in the heating condenser 15 heats and condenses the load-side fluid hot water in the recovery heat exchanger 31. Therefore, most of the energy used to heat and concentrate the antifreeze liquid can be used to heat the load-side hot water. It has a double heating effect. Furthermore, heating concentrator 1
By keeping 5 and the recovery heat exchanger 31 in a vacuum below atmospheric pressure, it is easy to manufacture the container.
It also increases safety.
以上のように、本発明はヒートポンプ装置で外
気側熱交換器に不凍液散布装置を備えたものにお
いて散布する不凍液を加温して不凍液中の水分を
除くように加温手段を設けたので、不凍液の濃度
低下による熱交換要素への着水、着霜が防止でき
る。更に、不凍液を加温するに要する熱エネルギ
を負荷側流体の加熱に利用したので、エネルギの
有効な活用がはかれた。
As described above, the present invention is a heat pump device equipped with an antifreeze spraying device on the outside air side heat exchanger, and is provided with a heating means to heat the antifreeze to be sprayed to remove moisture from the antifreeze. It is possible to prevent water from landing on the heat exchange element and frost formation due to a decrease in the concentration of water. Furthermore, since the thermal energy required to heat the antifreeze liquid is used to heat the load-side fluid, effective use of energy is achieved.
第1図、第2図、第3図及び第4図は、本発明
の空気熱源ヒートポンプの外気熱交換器周辺の
夫々異なる実施例を説明するためのフローシー
ト、第5図は従来の空気熱源ヒートポンプの外気
熱交換器周辺の装置を説明するためのフローシー
トである。
1…外気側熱交換器、2…冷媒配管、3…減圧
弁、4…外皮、6…熱交換要素、7…フアン、1
1…不凍液、13…配管、14…制止弁、15…
加温濃縮器、16…電気ヒータ、17…排気管、
18…配管、19…オリフイス、20…制止弁、
21…吐出管、22…散布器、25…圧縮機、2
6…負荷側熱交換器、27…負荷側温水ポンプ、
31…回収熱交換器、32…ドレン配管、33…
ガス排気管、34…排気ポンプ、35…ドレンポ
ンプ、37…不凍液熱交換器、38…不凍液熱交
換器コイル、39…ドレン、40…エジエクタ。
FIGS. 1, 2, 3, and 4 are flow sheets for explaining different embodiments of the outside air heat exchanger and the surrounding area of the air heat source heat pump of the present invention, and FIG. 5 is a flow sheet of the conventional air heat source heat pump. This is a flow sheet for explaining devices around an outside air heat exchanger of a heat pump. 1... Outside air side heat exchanger, 2... Refrigerant piping, 3... Pressure reducing valve, 4... Outer skin, 6... Heat exchange element, 7... Fan, 1
1... Antifreeze, 13... Piping, 14... Stop valve, 15...
Heating concentrator, 16... electric heater, 17... exhaust pipe,
18... Piping, 19... Orifice, 20... Stop valve,
21...Discharge pipe, 22...Spreader, 25...Compressor, 2
6...Load side heat exchanger, 27...Load side hot water pump,
31...Recovery heat exchanger, 32...Drain piping, 33...
Gas exhaust pipe, 34...exhaust pump, 35...drain pump, 37...antifreeze heat exchanger, 38...antifreeze heat exchanger coil, 39...drain, 40...ejector.
Claims (1)
する外気より熱を奪う外気側熱交換器1と、前記
熱交換要素中で加熱蒸発した冷媒を圧縮機25で
圧縮した後該圧縮機からの吐出ガスにより負荷流
体を加熱するための負荷側熱交換器26と、前記
不凍液を加温濃縮する加温濃縮器15を備えた空
気熱源ヒートポンプにおいて、加温濃縮の際に不
凍液より蒸発分離された蒸気で、前記負荷側熱交
換器に導入される負荷流体を加熱するようにした
ことを特徴とする空気熱源ヒートポンプ。 2 加温濃縮器を大気圧以下で運転すると共に、
不凍液より蒸発分離された蒸気で、負荷流体を加
熱する際に凝縮したドレンを、大気圧の外部に放
出する手段を有する特許請求の範囲第1項記載の
空気熱源ヒートポンプ。 3 加温濃縮器に、ガス排出手段を付属させた特
許請求の範囲第1項又は第2項記載の空気熱源ヒ
ートポンプ。 4 ドレン排出手段とガス排出手段とが共用でき
るものである特許請求の範囲第3項記載の空気熱
源ヒートポンプ。 5 加温濃縮器に出入する不凍液間で熱交換させ
る特許請求の範囲第1項、第2項、第3項または
第4項記載の空気熱源ヒートポンプ。[Scope of Claims] 1. An outside air side heat exchanger 1 which takes away heat from outside air and has a means for dispersing antifreeze onto a heat exchange element 6, and a compressor 25 which compresses the refrigerant heated and evaporated in the heat exchange element. In an air source heat pump equipped with a load-side heat exchanger 26 for heating a load fluid with gas discharged from the compressor, and a heating concentrator 15 for heating and concentrating the antifreeze liquid, during heating and concentration. An air source heat pump characterized in that a load fluid introduced into the load-side heat exchanger is heated with steam evaporated and separated from antifreeze. 2. Operate the heating concentrator below atmospheric pressure,
2. The air source heat pump according to claim 1, further comprising means for discharging condensate condensed when heating a load fluid with vapor evaporated and separated from antifreeze to the outside at atmospheric pressure. 3. The air heat source heat pump according to claim 1 or 2, wherein the heating concentrator is provided with a gas exhaust means. 4. The air source heat pump according to claim 3, wherein the drain discharge means and the gas discharge means can be used in common. 5. The air source heat pump according to claim 1, 2, 3, or 4, wherein heat is exchanged between antifreeze flowing in and out of a heating concentrator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16127285A JPS6222972A (en) | 1985-07-23 | 1985-07-23 | Air heat-source heat pump |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16127285A JPS6222972A (en) | 1985-07-23 | 1985-07-23 | Air heat-source heat pump |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6222972A JPS6222972A (en) | 1987-01-31 |
| JPH057632B2 true JPH057632B2 (en) | 1993-01-29 |
Family
ID=15731950
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16127285A Granted JPS6222972A (en) | 1985-07-23 | 1985-07-23 | Air heat-source heat pump |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6222972A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08104327A (en) * | 1994-10-04 | 1996-04-23 | Akira Kono | Can with back lid |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5252277U (en) * | 1975-10-14 | 1977-04-14 | ||
| JPS553739Y2 (en) * | 1976-06-30 | 1980-01-29 | ||
| JPS56137100U (en) * | 1980-03-17 | 1981-10-17 | ||
| JPS6053764A (en) * | 1983-09-05 | 1985-03-27 | 株式会社荏原製作所 | Air heat source heat pump |
-
1985
- 1985-07-23 JP JP16127285A patent/JPS6222972A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08104327A (en) * | 1994-10-04 | 1996-04-23 | Akira Kono | Can with back lid |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6222972A (en) | 1987-01-31 |
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