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JPH0827006B2 - Heat carrier - Google Patents
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JPH0827006B2 - Heat carrier - Google Patents

Heat carrier

Info

Publication number
JPH0827006B2
JPH0827006B2 JP62291045A JP29104587A JPH0827006B2 JP H0827006 B2 JPH0827006 B2 JP H0827006B2 JP 62291045 A JP62291045 A JP 62291045A JP 29104587 A JP29104587 A JP 29104587A JP H0827006 B2 JPH0827006 B2 JP H0827006B2
Authority
JP
Japan
Prior art keywords
liquid
receiver
gas
refrigerant
check valve
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
Application number
JP62291045A
Other languages
Japanese (ja)
Other versions
JPH01134130A (en
Inventor
達規 桜武
茂 岩永
紘一郎 山口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP62291045A priority Critical patent/JPH0827006B2/en
Publication of JPH01134130A publication Critical patent/JPH01134130A/en
Publication of JPH0827006B2 publication Critical patent/JPH0827006B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Central Heating Systems (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は無動力熱搬送方式で冷媒を介し暖房を行なう
熱搬送機に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat transfer machine for heating by a non-powered heat transfer method via a refrigerant.

従来の技術 冷媒を用いた暖房装置で低外気温時暖房能力の低下防
止及び低ランニングコストを達成するため冷媒加熱器を
設け液ポンプ搬送方式の暖房装置が従来からある。この
方式は冷媒加熱器で冷媒を蒸発させ室内熱交換器で凝縮
液化させ、その液冷媒をポンプで再び冷媒加熱器へ送る
ものである。しかしながら上記方式においてもポンプの
運転費が必要であるため、このポンプ機能を冷媒の圧力
差で行なうものが従来ある。(例えは実開昭61-43679号
公報) この種の暖房装置は第2図に示すように冷媒加熱器1
より上方に位置した受液器2の中間位置に気液分離器3
を配設し前記受液器2と前記気液分離器3の間に両者を
均圧させる開閉弁4を有しさらにく受液器2と気液分離
器3の間に逆止弁5を有する構成を有し、冷媒加熱器1
で蒸発した冷媒は接続配管7を通り放熱器6で凝縮し受
液器2へ接続配管8を通り流入する。受液器2へ液冷媒
が溜ると開閉弁4を開き受液器2と気液分離器3とを均
圧化し受液器2の液冷媒を気液分離器3へ流入させる。
流入し終わると開閉弁4を閉じ逆止弁5も閉じるため再
び放熱器6から凝縮した液冷媒が受液器2へ圧送され流
入する。このような動作を繰り返して熱搬送を行ない暖
房運転を行なうようになっていた。
2. Description of the Related Art Conventionally, there is a liquid pump transfer type heating device provided with a refrigerant heater in order to prevent a decrease in heating capacity at low outside air temperature and a low running cost in a heating device using a refrigerant. In this system, the refrigerant heater evaporates the refrigerant, the indoor heat exchanger condenses it into liquid, and the liquid refrigerant is pumped again to the refrigerant heater. However, even in the above-mentioned method, since the operation cost of the pump is required, there is a conventional one that performs this pump function by the pressure difference of the refrigerant. (For example, Japanese Utility Model Laid-Open No. 61-43679) A heating device of this type has a refrigerant heater 1 as shown in FIG.
The gas-liquid separator 3 is located at an intermediate position of the receiver 2 which is located higher.
And a check valve 5 for equalizing the pressure between the liquid receiver 2 and the gas-liquid separator 3, and a check valve 5 between the liquid receiver 2 and the gas-liquid separator 3. Refrigerant heater 1 having a configuration having
The refrigerant that has evaporated in 2 passes through the connecting pipe 7 and is condensed by the radiator 6 and flows into the liquid receiver 2 through the connecting pipe 8. When the liquid refrigerant collects in the liquid receiver 2, the on-off valve 4 is opened and the liquid receiver 2 and the gas-liquid separator 3 are pressure-equalized so that the liquid refrigerant in the liquid receiver 2 flows into the gas-liquid separator 3.
When the inflow is completed, the on-off valve 4 is closed and the check valve 5 is also closed, so that the liquid refrigerant condensed from the radiator 6 is pumped to the liquid receiver 2 and flows in again. By repeating such operations, heat transfer is performed to perform heating operation.

発明が解決しようとする問題点 しかしながら上記のような構成では冷媒加熱器1の上
方に気液分離器3、さらにその上方に逆止弁5と受液器
2を配設するため機器の高さ方向の大きさが大きくなる
という問題点を有していた。さらに受液器2が単に容器
のみの密閉容器構成では、受液器2へ放熱器6から液冷
媒が流入する際、受液器2内には高圧ガスが存在してお
り、それを流入液冷媒で冷却凝縮させ受液器内部圧力を
低下させる作用が十分でなく、その結果熱搬送量の低下
や、受液器2流入液冷媒の過冷却度を十分にとる必要が
生じ放熱器6が大きくなりサイクル内の冷媒量が多くな
る問題点を有していた。又開閉弁4の抵抗が大きい場合
は、受液器2から気液分離器3へ重力差で液冷媒を完全
に流出する開閉弁を開しておく時間が長くかかり、その
結果 G=V×γ/T G :能力に必要な冷媒循環量(g/sec) V :受液器容積(cc) γ :受液器内液冷媒密度(g/cc) T :開閉弁の周期(開時間+閉時間)(sec) から分かるようにTが大きくなるためGが小さくなり、
熱搬送量が大きくとれず、直動型電磁弁ではポート径を
大きくし抵抗を減らすと最高作動圧力差が小さくなり確
実に開閉弁を開閉させる動作に信頼性が欠けるという問
題点を有していた。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention However, in the above configuration, the gas-liquid separator 3 is arranged above the refrigerant heater 1, and the check valve 5 and the liquid receiver 2 are arranged above the gas heater 3 so that the height of the device is high. There is a problem that the size of the direction becomes large. Further, in the closed container configuration in which the liquid receiver 2 is only a container, when the liquid refrigerant flows into the liquid receiver 2 from the radiator 6, high-pressure gas exists in the liquid receiver 2 and the high pressure gas The action of cooling and condensing with the refrigerant to lower the internal pressure of the receiver is not sufficient, and as a result, it is necessary to reduce the amount of heat transfer and to obtain a sufficient degree of supercooling of the liquid refrigerant flowing into the receiver 2. There was a problem that the amount of refrigerant in the cycle became large and the amount of refrigerant in the cycle increased. Further, when the resistance of the on-off valve 4 is large, it takes a long time to open the on-off valve which completely discharges the liquid refrigerant from the liquid receiver 2 to the gas-liquid separator 3 due to the gravity difference, and as a result, G = V × γ / T G: Refrigerant circulation amount required for capacity (g / sec) V: Liquid receiver volume (cc) γ: Liquid refrigerant density in receiver (g / cc) T: Open / close valve cycle (open time + As can be seen from (closing time) (sec), T increases and G decreases,
Since the heat transfer amount cannot be large and the direct-acting solenoid valve has a problem that the maximum operating pressure difference decreases when the port diameter is increased and the resistance is reduced, the operation to reliably open and close the on-off valve is unreliable. It was

問題点を解決するための手段 上記問題点を解決するために本発明の熱搬送機は、冷
媒加熱器と前記冷媒加熱器の上方に配設した気液分離器
とをループ状に接続する一方、前記気液分離器、放熱
器、第1逆止弁、前記気液分離器より上方に配設した受
液器、第2逆止弁を順次ループ状に接続した冷媒回路を
有し、前記受液器上部には前記気液分離器の圧力と均圧
する均圧管を有する開閉弁出口管と、前記第1逆止弁を
接続するU字管を設け、前記第2逆止弁は前記受液器の
外殻内で構成すると共に、前記受液器内の上方部にパン
チングメタルを設け、開閉弁には通路抵抗が少なく最高
差動圧力差も大きいパイロット式電磁弁を備えたもので
ある。
Means for Solving the Problems In order to solve the above problems, the heat carrier of the present invention has a refrigerant heater and a gas-liquid separator arranged above the refrigerant heater connected in a loop. A gas-liquid separator, a radiator, a first check valve, a liquid receiver disposed above the gas-liquid separator, and a second check valve, which are connected in a loop in sequence to form a refrigerant circuit, An on-off valve outlet pipe having a pressure equalizing pipe for equalizing the pressure of the gas-liquid separator and a U-shaped pipe connecting the first check valve are provided in the upper part of the liquid receiver, and the second check valve is the receiving pipe. In addition to being constructed within the outer shell of the liquid container, punching metal is provided in the upper part inside the liquid receiver, and the opening / closing valve is equipped with a pilot type solenoid valve with a small passage resistance and a large maximum differential pressure difference. .

本発明は、上記した構成によって第2逆止弁は、受液
器を構成する同じ外殻内で構成する為、第2逆止弁と受
液器とのろう付け作業が省略でき、第2逆止弁の受液器
側のろう付け時の熱的影響をさけるための銅パイプ部を
長くとる必要がなく小型コンパクトに加工することがで
きる。また第1逆止弁から流入した凝縮液冷媒はパンチ
ングメタルに当たり液冷媒は飛散し、液冷媒がガス冷媒
と接触する面積が増大し、気液物質移動が促進され、大
きな過冷却度は必要なく少ない過冷却度で受液器内部圧
力を低下させることができ、さらに開閉弁にパイロット
式電磁弁を設けている為、流路抵抗が少なくかつ最高作
動圧差が大きい為受液器から気液分離器へ液冷媒を完全
に流出させる時間が短くなり熱搬送量の増大が図れると
共に、確実に開閉させる動作の信頼性向上が図れる。
According to the present invention, since the second check valve is configured in the same outer shell that configures the liquid receiver by the above-described configuration, the brazing work between the second check valve and the liquid receiver can be omitted, and the second check valve can be omitted. Since it is not necessary to lengthen the copper pipe portion for avoiding the thermal influence at the time of brazing on the receiver side of the check valve, it is possible to process it in a small and compact size. Further, the condensed liquid refrigerant flowing from the first check valve hits the punching metal and the liquid refrigerant scatters, the area where the liquid refrigerant contacts the gas refrigerant increases, the gas-liquid mass transfer is promoted, and a large degree of supercooling is not required. The internal pressure of the receiver can be reduced with a small degree of supercooling, and the pilot solenoid valve is installed on the on-off valve, so the flow resistance is small and the maximum operating pressure difference is large, so gas-liquid separation from the receiver The time required for the liquid refrigerant to completely flow out to the container can be shortened, the amount of heat transfer can be increased, and the reliability of the operation for opening and closing the liquid refrigerant can be improved.

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。なお第2図と同一部には同一番号を付している。第
1図において1は気液分離器3より下方に配設してある
冷媒加熱器、7,8は放熱器6の入口接続配管、出口接続
配管、9は第1逆止弁で順方向出口側はU字管10で受液
器2の上部に接続してある。弁座11、弁体12、スプリン
グ13から成る第2逆止弁5は受液器外径から弁座11の外
径迄絞り加工した受液器2の外殻にコーキング加工して
あり、受液器2の上部にはパンチングメタルを挿入して
ある。又、4は入口側に前記入口接続配管7から分岐し
てある均圧管17を有し、出口管15を前記受液器2の上方
に接続してあるパイロット式電磁弁であり16は前記パイ
ロット式電磁弁の開閉動作を制御する制御装置、18は冷
媒加熱器1を加熱するバーナである。
Embodiments Embodiments of the present invention will be described below with reference to the accompanying drawings. The same parts as those in FIG. 2 are designated by the same reference numerals. In FIG. 1, 1 is a refrigerant heater disposed below the gas-liquid separator 3, 7 and 8 are inlet connection pipes and outlet connection pipes of the radiator 6, and 9 is a first check valve which is a forward outlet. The side is connected to the upper part of the receiver 2 by a U-shaped tube 10. The second check valve 5 including the valve seat 11, the valve body 12 and the spring 13 is caulked on the outer shell of the receiver 2 which is drawn from the outer diameter of the receiver to the outer diameter of the valve seat 11. A punching metal is inserted in the upper part of the liquid container 2. Further, 4 is a pilot type solenoid valve having an equalizing pipe 17 branched from the inlet connecting pipe 7 on the inlet side, and an outlet pipe 15 is connected above the liquid receiver 2, and 16 is a pilot solenoid valve. A control device for controlling the opening / closing operation of the solenoid valve, and a burner 18 for heating the refrigerant heater 1.

上記構成においてバーナ18の燃焼熱で冷媒加熱器1で
加熱された冷媒は2相状態で気液分離器3内に流入し液
冷媒は再び冷媒加熱器1へ流入する。一方気液分離器3
内に冷媒加熱器1から流入した2相冷媒のガス冷媒は入
口接続配管7を通り放熱器6で凝縮液化する。この時パ
イロット式電磁弁4が閉の時は第2逆止弁5は閉状態で
受液器2へ放熱器6からの凝縮液冷媒が第1逆止弁9、
U字管10を通り圧送され受液器2内のパンチングメタル
14に当り受液器2内のガス冷媒と気液物質移動が促進さ
れ受液器2内の圧力が低下し受液器2内に凝縮液冷媒が
溜る。この状態でパイロット式電磁弁4を開にすると受
液器2と気液分離器3とは均圧状態となり受液器2内の
液冷媒は第2逆止弁5を通り気液分離器3内へ流入す
る。この時第1逆止弁9は閉状態である。次にパイロッ
ト式電磁弁を閉とすると第2逆止弁5は閉となり再び受
液器2へ放熱器6から凝縮液冷媒が流入し受液器2を凝
縮液冷媒で満たしパイロット式電磁弁4を開にするとい
うサイクルを繰返す。すなわち気液分離器3と冷媒加熱
器1の間は自然循環サイクル、気液分離器3、放熱器
6、第1逆止弁9、受液器2、第2逆止弁5のサイクル
は、受液器2へ放熱器6からの液冷媒を溜めてそれを間
欠的に気液分離器3へ供給するという間欠動作サイクル
である。したがって受液器2、パイロット式電磁弁4、
第2逆止弁5、第1逆止弁9で熱搬送機として作用し、
受液器2と第2逆止弁は受液器2の外径から弁座11の外
径迄絞り加工した受液器2の外殻に弁座11をコーキング
加工しており第2逆止弁5の受液器2側のろう付け時の
熱的影響をさけるための銅パイプ部を長くとる必要がな
く、ろう付け作業も省略でき、第1逆止弁9出口側をU
字管で受液器上部と接続していることと合わせて熱搬送
機部を小型コンパクトに加工することができる効果があ
る。又、第1逆止弁9から流入した凝縮液冷媒はパンチ
ングメタル14に当り気液物質移動が促進され少ない過冷
却度で受液器2内部圧力を低下させることができ、放熱
器6の小型化というこの種の熱搬送機を使用したシステ
ムの小型コンパクト化ができ、さらに開閉弁にパイロッ
ト式電磁弁を使用することにより前記電磁弁ポート径を
大きくし抵抗を小さくしかつ最高差動圧力差を大きく設
定できるため、受液器2から気液分離器3へ液冷媒を供
給する際の前記電磁弁開時間を短かくすることができ熱
搬送量の増大化が図れ、前記電磁弁の開閉動作も確実に
行なわれ、この種の熱搬送機の性能、信頼性が向上する
効果がある。
In the above structure, the refrigerant heated by the refrigerant heater 1 by the combustion heat of the burner 18 flows into the gas-liquid separator 3 in a two-phase state, and the liquid refrigerant again flows into the refrigerant heater 1. On the other hand, gas-liquid separator 3
The gas refrigerant of the two-phase refrigerant flowing in from the refrigerant heater 1 passes through the inlet connection pipe 7 and is condensed and liquefied by the radiator 6. At this time, when the pilot type solenoid valve 4 is closed, the second check valve 5 is closed and the condensed liquid refrigerant from the radiator 6 to the liquid receiver 2 is transferred to the first check valve 9,
Punching metal in the receiver 2 that is pumped through the U-tube 10
At 14, the gas refrigerant and gas-liquid mass transfer in the liquid receiver 2 are promoted, the pressure in the liquid receiver 2 drops, and the condensed liquid refrigerant accumulates in the liquid receiver 2. When the pilot type solenoid valve 4 is opened in this state, the liquid receiver 2 and the gas-liquid separator 3 are in a pressure equalizing state, and the liquid refrigerant in the liquid receiver 2 passes through the second check valve 5 and the gas-liquid separator 3 Flows in. At this time, the first check valve 9 is closed. Next, when the pilot type solenoid valve is closed, the second check valve 5 is closed and the condensed liquid refrigerant flows into the receiver 2 from the radiator 6 again to fill the receiver 2 with the condensed liquid refrigerant. Repeat the cycle of opening. That is, the natural circulation cycle between the gas-liquid separator 3 and the refrigerant heater 1, the cycle of the gas-liquid separator 3, the radiator 6, the first check valve 9, the liquid receiver 2 and the second check valve 5 is: This is an intermittent operation cycle in which the liquid refrigerant from the radiator 6 is accumulated in the liquid receiver 2 and is intermittently supplied to the gas-liquid separator 3. Therefore, the receiver 2, the pilot type solenoid valve 4,
The second check valve 5 and the first check valve 9 function as a heat carrier,
The receiver 2 and the second check valve are processed by caulking the valve seat 11 on the outer shell of the receiver 2 which is drawn from the outer diameter of the receiver 2 to the outer diameter of the valve seat 11 It is not necessary to lengthen the copper pipe part for avoiding the thermal influence at the time of brazing of the liquid receiver 2 side of the valve 5, the brazing work can be omitted, and the outlet side of the first check valve 9 is U-shaped.
In addition to the fact that it is connected to the upper part of the receiver by a character tube, there is an effect that the heat carrier unit can be processed into a small size and a compact size. Further, the condensed liquid refrigerant flowing from the first check valve 9 hits the punching metal 14 to promote the gas-liquid mass transfer, so that the internal pressure of the receiver 2 can be reduced with a small degree of supercooling, and the radiator 6 can be made compact. A system using this type of heat carrier can be made smaller and more compact, and by using a pilot type solenoid valve for the on-off valve, the solenoid valve port diameter can be increased to reduce the resistance and the maximum differential pressure difference. Can be set to a large value, the opening time of the solenoid valve when the liquid refrigerant is supplied from the liquid receiver 2 to the gas-liquid separator 3 can be shortened, the heat transfer amount can be increased, and the solenoid valve can be opened and closed. The operation is surely performed, and the performance and reliability of this type of heat carrier are improved.

発明の効果 以上のように本発明の熱搬送機によれば次の効果が得
られる。
Effects of the Invention As described above, according to the heat carrier of the present invention, the following effects are obtained.

(1)受液器外殻内で第2逆止弁を構成し、第1逆止弁
出口側をU字管で受液器上部と接続しているので熱搬送
機を小型コンパクトに加工することができる。
(1) Since the second check valve is configured in the outer shell of the receiver and the outlet of the first check valve is connected to the upper part of the receiver with a U-shaped pipe, the heat transfer machine can be made compact and compact. be able to.

(2)受液器内に設けたパンチングメタルにより受液器
内の気液物質移動が促進され少ない過冷却度で受液器内
圧力を低下させることができこの種の熱搬送機を用いた
放熱器の小型化が可能となる。
(2) The punching metal provided in the receiver allows the gas-liquid mass transfer in the receiver to be promoted and the pressure inside the receiver to be lowered with a small degree of supercooling. It is possible to downsize the radiator.

(3)開閉弁に最高差動圧力差が大きくとれ、かつポー
ト径を大きくしたパイロット式電磁弁を用いることによ
り受液器から液冷媒を加熱部に供給する時間が短縮化で
きその結果熱搬送量の増加が図れると共に確実に開閉動
作する性能、信頼性共にすぐれた熱搬送機を提供するこ
とができる。
(3) By using a pilot type solenoid valve with a large maximum differential pressure difference and a large port diameter for the on-off valve, the time to supply the liquid refrigerant from the receiver to the heating section can be shortened, resulting in heat transfer. It is possible to provide a heat carrier having an increased amount and an excellent opening / closing performance and reliability.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の一実施例による熱搬送機を用いたシス
テム回路構成図、第2図は従来のこの種の熱搬送機を用
いたシステム回路構成図である。 2……受液器、4……開閉弁(パイロット式電磁弁)、
5……第2逆止弁、9……第1逆止弁、10……U字管、
14……パンチングメタル。
FIG. 1 is a system circuit block diagram using a heat carrier according to an embodiment of the present invention, and FIG. 2 is a system circuit block diagram using a conventional heat carrier of this type. 2 ... Liquid receiver, 4 ... Open / close valve (pilot type solenoid valve),
5 ... Second check valve, 9 ... First check valve, 10 ... U-tube,
14 ... punching metal.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】冷媒加熱器と前記冷媒加熱器の上方に配設
した気液分離器とをループ状に接続する一方、前記気液
分離器、放熱器、第1逆止弁、前記気液分離器より上方
に配設した気液器、第2逆止弁を順次ループ状に接続し
た冷媒回路を有し、前記受液器上部には前記気液分離器
の圧力と均圧する均圧管を有する開閉弁出口管と、前記
第1逆止弁を接続するU字管を設け、前記第2逆止弁は
前記受液器の外殻内で構成すると共に、前記受液器内の
上方部にパンチングメタルを設けた熱搬送機。
1. A refrigerant heater and a gas-liquid separator disposed above the refrigerant heater are connected in a loop, while the gas-liquid separator, a radiator, a first check valve, and the gas-liquid separator. A gas-liquid device arranged above the separator and a refrigerant circuit in which a second check valve is sequentially connected in a loop shape are provided, and a pressure equalizing pipe for equalizing the pressure of the gas-liquid separator is provided above the liquid receiver. A U-shaped pipe that connects the on-off valve outlet pipe and the first check valve is provided, and the second check valve is formed in the outer shell of the liquid receiver, and an upper portion in the liquid receiver. Heat transfer machine equipped with punching metal.
【請求項2】開閉弁はパイロット式電磁弁である特許請
求の範囲第1項記載の熱搬送機。
2. The heat carrier according to claim 1, wherein the on-off valve is a pilot type solenoid valve.
JP62291045A 1987-11-18 1987-11-18 Heat carrier Expired - Lifetime JPH0827006B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62291045A JPH0827006B2 (en) 1987-11-18 1987-11-18 Heat carrier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62291045A JPH0827006B2 (en) 1987-11-18 1987-11-18 Heat carrier

Publications (2)

Publication Number Publication Date
JPH01134130A JPH01134130A (en) 1989-05-26
JPH0827006B2 true JPH0827006B2 (en) 1996-03-21

Family

ID=17763727

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62291045A Expired - Lifetime JPH0827006B2 (en) 1987-11-18 1987-11-18 Heat carrier

Country Status (1)

Country Link
JP (1) JPH0827006B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007078269A (en) * 2005-09-14 2007-03-29 Yanmar Co Ltd Cooling and heating simultaneous operation- corresponding engine driven type heat pump

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007078269A (en) * 2005-09-14 2007-03-29 Yanmar Co Ltd Cooling and heating simultaneous operation- corresponding engine driven type heat pump

Also Published As

Publication number Publication date
JPH01134130A (en) 1989-05-26

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