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JPH0827004B2 - Heating system - Google Patents
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JPH0827004B2 - Heating system - Google Patents

Heating system

Info

Publication number
JPH0827004B2
JPH0827004B2 JP13883388A JP13883388A JPH0827004B2 JP H0827004 B2 JPH0827004 B2 JP H0827004B2 JP 13883388 A JP13883388 A JP 13883388A JP 13883388 A JP13883388 A JP 13883388A JP H0827004 B2 JPH0827004 B2 JP H0827004B2
Authority
JP
Japan
Prior art keywords
refrigerant
refrigerant heater
heater
gas
radiator
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 - Fee Related
Application number
JP13883388A
Other languages
Japanese (ja)
Other versions
JPH01306734A (en
Inventor
勝蔵 粉川
克彦 山本
純一 雀堂
達規 桜武
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 JP13883388A priority Critical patent/JPH0827004B2/en
Publication of JPH01306734A publication Critical patent/JPH01306734A/en
Publication of JPH0827004B2 publication Critical patent/JPH0827004B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Central Heating Systems (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は冷媒を加熱し無動力熱搬送方式で暖房運転す
る暖房装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating device that heats a refrigerant and performs heating operation by a non-powered heat transfer system.

従来の技術 従来、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5を有する構成で、冷媒加熱
器1で蒸発した冷媒は放熱器6で凝縮し受液器2へ流入
する。受液器2に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へ流入する。このような動作を繰り返して熱
搬送を行い暖房運転を行うようになっていた。(例えば
実開昭61-43679号公報) 発明が解決しようとする課題 しかしながら、上記従来例の構成では冷媒加熱器1と
気液分離器3の接続配管中を流れる冷媒は比重差による
自然循環である。それを冷媒加熱器をバーナーで加熱す
る場合冷媒が高温となり熱分解するのを防止するために
は、常に飽和ガス状態の気液2相状態で冷媒を冷媒加熱
器から出す必要がある。そのため、 (1)冷媒加熱器1の出口管を気液分離器3の上方から
いれると途中の配管が長くなるために抵抗が大きくなり
それに従って気液分離器内の液面も高くする必要を生じ
装置全体が大きくなる。
2. Description of the Related Art Conventionally, in this type of heating device, as shown in FIG. 2, a gas-liquid separator 3 is arranged at an intermediate position of a liquid receiver 2 located above the refrigerant heater 1 and the liquid receiver 2 is provided. The opening and closing valve 5 for equalizing the pressure between the gas-liquid separator 3 and the gas-liquid separator 3 is provided. The refrigerant evaporated in the refrigerant heater 1 is condensed in the radiator 6 and flows into the liquid receiver 2. 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 again flows into the liquid receiver 2. By repeating such operations, heat transfer is performed to perform heating operation. (For example, Japanese Utility Model Laid-Open No. 61-43679) Problems to be Solved by the Invention However, in the configuration of the conventional example described above, the refrigerant flowing in the connecting pipe of the refrigerant heater 1 and the gas-liquid separator 3 is naturally circulated due to the difference in specific gravity. is there. When the refrigerant heater is heated by a burner, it is necessary to always discharge the refrigerant from the refrigerant heater in a gas-liquid two-phase state in a saturated gas state in order to prevent the refrigerant from becoming hot and thermally decomposing. Therefore, (1) When the outlet pipe of the refrigerant heater 1 is inserted from above the gas-liquid separator 3, the length of the pipe in the middle increases the resistance and accordingly the liquid level in the gas-liquid separator needs to be raised accordingly. As a result, the entire device becomes large.

(2)開閉弁4の開閉により、受液器2から気液分離器
3内に流入する冷媒の温度は放熱器6より冷却した過冷
却液であり気液分離器3のガス温度より低いため、気液
分離器3内のガスはこの過冷却液により凝縮し気液分離
器3内の圧力は低下する。受液器2から気液分離器3に
過冷却液冷媒の流入が停止すると、再び気液分離器3内
の圧力は上昇し、気液分離器3内の圧力は変動する。冷
媒加熱器1と気液分離器3の間を流れる冷媒は比重差を
流れ抵抗によりバランスした自然循環であり、冷媒は冷
媒加熱器1からガスで気液分離器3に流れ気液分離器3
から冷媒加熱器1に液で流れるため冷媒加熱器1から気
液分離器3に流れる抵抗が大きく(ガスは液に比べて比
容積が大きく流速が大きくなるため)なる。そのため、
この冷媒の流量は気液分離器3内の圧力が低くなった時
冷媒加熱器1の入口管から気液分離器3に流れが逆流と
なり、冷媒加熱器1内を低温の液冷媒が循環しなくな
る。このため、冷媒加熱器1内で冷媒が一時的に高温と
なり熱分解を生じる。これを防止するためには、冷媒加
熱器1に対して気液分離器3内の冷媒液面をより大きく
し、自然循環量を確保するかまたは、冷媒加熱器1の熱
容量を大きくする必要があった。このことは、装置全体
が大きくなり、部品のコストも高くなった。
(2) The temperature of the refrigerant flowing from the liquid receiver 2 into the gas-liquid separator 3 by opening and closing the on-off valve 4 is the supercooled liquid cooled by the radiator 6 and is lower than the gas temperature of the gas-liquid separator 3. The gas in the gas-liquid separator 3 is condensed by this supercooled liquid, and the pressure in the gas-liquid separator 3 drops. When the inflow of the supercooled liquid refrigerant from the liquid receiver 2 to the gas-liquid separator 3 is stopped, the pressure inside the gas-liquid separator 3 rises again and the pressure inside the gas-liquid separator 3 fluctuates. The refrigerant flowing between the refrigerant heater 1 and the gas-liquid separator 3 is natural circulation in which the difference in specific gravity is balanced by the flow resistance, and the refrigerant flows from the refrigerant heater 1 to the gas-liquid separator 3 as gas and the gas-liquid separator 3
Since the liquid flows from the refrigerant heater 1 to the refrigerant heater 1, the resistance flowing from the refrigerant heater 1 to the gas-liquid separator 3 is large (because the gas has a larger specific volume and a higher flow velocity than the liquid). for that reason,
When the pressure in the gas-liquid separator 3 becomes low, the flow rate of this refrigerant becomes a reverse flow from the inlet pipe of the refrigerant heater 1 to the gas-liquid separator 3, and the low-temperature liquid refrigerant circulates in the refrigerant heater 1. Disappear. Therefore, the temperature of the refrigerant temporarily rises in the refrigerant heater 1 to cause thermal decomposition. In order to prevent this, it is necessary to make the refrigerant liquid level in the gas-liquid separator 3 larger than that of the refrigerant heater 1 to secure a natural circulation amount or to increase the heat capacity of the refrigerant heater 1. there were. This increases the size of the entire device and increases the cost of parts.

(3)受液器2と気液分離器3とを均圧させる開閉弁4
を直接気液分離器3と接続することは、気液分離器3の
接続口が増え加工コストが高くなる。
(3) Open / close valve 4 for equalizing the pressure between the liquid receiver 2 and the gas-liquid separator 3
The direct connection of the to the gas-liquid separator 3 increases the number of connection ports of the gas-liquid separator 3 and increases the processing cost.

等の課題を有していた。 Had problems such as.

本発明はかかる従来の課題を解消するもので、気液分
離器とバーナー等で加熱する冷媒加熱器の循環を、冷媒
加熱器の上部と放熱器を接続管により接続し、放熱器の
凝縮による凝縮圧力差循環サイクルで冷媒加熱器の冷媒
を循環させることにより、暖房装置の小型コンパクト化
を図り、さらに加工コストの低減化を図ると共に、冷媒
加熱器を流れる冷媒の循環を強制的に促進し、冷媒の過
熱を防止することを目的とする。
The present invention is to solve such conventional problems, the circulation of the refrigerant heater to be heated by a gas-liquid separator and a burner, etc., the upper part of the refrigerant heater and the radiator are connected by a connecting pipe, by condensation of the radiator. By circulating the refrigerant in the refrigerant heater in the condensation pressure differential circulation cycle, the heating device can be made smaller and more compact, the processing cost can be further reduced, and the circulation of the refrigerant flowing through the refrigerant heater can be forcibly promoted. The purpose is to prevent overheating of the refrigerant.

課題を解決するための手段 上記課題を解決するために本発明の暖房装置は、受液
器を冷媒加熱器よりも上方に配設して、放熱器、第1逆
止弁、前記受液器、第2逆止弁、前記冷媒加熱器、を接
続する接続配管と、前記冷媒加熱器の上部と前記放熱器
とを接続する接続管と前記受液器の間に開閉弁を有する
均圧管を設け、さらに前記冷媒加熱器より上方に設けた
冷媒溜り器と、前記冷媒溜り部の下部と前記冷媒加熱器
の下部を接続し、前記冷媒加熱器の上部に設けた出口管
は前記接続管と連通し、前記冷媒加熱器の下部に設けた
入口管は前記第2逆止弁と接続した構成としたものであ
る。
Means for Solving the Problems In order to solve the above problems, in a heating device of the present invention, a liquid receiver is disposed above a refrigerant heater, and a radiator, a first check valve, and the liquid receiver are provided. A connecting pipe connecting the second check valve and the refrigerant heater, and a pressure equalizing pipe having an on-off valve between the connecting pipe connecting the upper part of the refrigerant heater and the radiator and the liquid receiver. Provided, further connecting the refrigerant reservoir provided above the refrigerant heater, the lower portion of the refrigerant reservoir portion and the lower portion of the refrigerant heater, the outlet pipe provided in the upper portion of the refrigerant heater is the connection pipe The inlet pipe provided in the lower part of the refrigerant heater, which is communicated with the refrigerant heater, is connected to the second check valve.

作用 本発明は、上記した構成によって、冷媒加熱器の出口
管を放熱器との接続管と連通し、前記冷媒加熱器の入口
管は前記第2逆止弁と接続し、受液器と出口管を開閉弁
を有する均圧管で接続したため、冷媒加熱器と放熱器は
直接接続でき、冷媒加熱器から出たガス冷媒は放熱器で
凝縮する。放熱器は高温のガス冷媒の熱を放熱し液冷媒
とする為冷媒の圧力が低下する。この凝縮による凝縮圧
力差により冷媒加熱器の高温ガスは冷媒加熱器から放熱
器に吸引される。放熱器に溜った液冷媒は受液器、逆止
弁により受液器の凝縮減圧により受液器に吸引された
後、均圧管の開閉弁の開により冷媒加熱器に落流する。
このため、冷媒加熱器内の冷媒は、運転中は放熱器でガ
ス冷媒が常に凝縮するため一定量以上の冷媒を循環す
る。そして冷媒加熱器の冷媒が加熱されガスとなる量が
多くなると、冷媒加熱器より上方に設けた冷媒溜り器の
下部から冷媒加熱器の下部に液冷媒が流入するため冷媒
加熱器内は常に2相状態で均一温度となる。このため冷
媒及びオイルは過熱する事無く冷媒加熱器の配管スペー
スの小型化が図れ暖房装置の小型コンパクト化が得られ
る。また冷媒加熱器で加熱ガス化した冷媒は直接放熱器
に搬送するため、放熱器に入る冷媒はガス比率が高く過
熱ガスに設定できるため放熱器の熱交換を高効率化出
来、熱交換器を小型コンパクト化が得られ、温風温度は
高くなり暖房感が向上する。さらに冷媒加熱器において
受液器からの低温の冷媒を入口管より流入し、高温の冷
媒は接続管から放熱器に送られるため全体的に冷媒の温
度が低くなり熱交換性能が向上し、局部過熱を生じなく
信頼性が向上する。
Effect of the Invention With the above-described configuration, the present invention allows the outlet pipe of the refrigerant heater to communicate with the connection pipe to the radiator, the inlet pipe of the refrigerant heater to be connected to the second check valve, and the receiver and the outlet. Since the tubes are connected by a pressure equalizing tube having an on-off valve, the refrigerant heater and the radiator can be directly connected, and the gas refrigerant discharged from the refrigerant heater is condensed by the radiator. Since the radiator radiates the heat of the high temperature gas refrigerant and turns it into a liquid refrigerant, the pressure of the refrigerant decreases. Due to the difference in condensation pressure due to this condensation, the high temperature gas in the refrigerant heater is sucked from the refrigerant heater to the radiator. The liquid refrigerant accumulated in the radiator is sucked into the liquid receiver by the liquid receiver and the check valve due to the condensation pressure reduction of the liquid receiver, and then flows into the refrigerant heater by opening the on-off valve of the pressure equalizing pipe.
Therefore, the refrigerant in the refrigerant heater circulates a certain amount or more of refrigerant during operation because the gas refrigerant is always condensed in the radiator. When the amount of the refrigerant heated by the refrigerant heater is increased to gas, the liquid refrigerant flows from the lower part of the refrigerant reservoir provided above the refrigerant heater to the lower part of the refrigerant heater, so that the inside of the refrigerant heater is always 2 A uniform temperature is achieved in the phase state. Therefore, the refrigerant and the oil are not overheated and the piping space of the refrigerant heater can be downsized, and the heating device can be downsized. Also, since the refrigerant heated and gasified by the refrigerant heater is directly conveyed to the radiator, the refrigerant entering the radiator has a high gas ratio and can be set as superheated gas, so the heat exchange of the radiator can be made highly efficient and the heat exchanger A compact size is obtained, and the warm air temperature rises, improving the feeling of heating. Furthermore, in the refrigerant heater, the low-temperature refrigerant from the liquid receiver flows in from the inlet pipe, and the high-temperature refrigerant is sent from the connecting pipe to the radiator, so the temperature of the refrigerant is lowered overall and the heat exchange performance is improved. Reliability is improved without overheating.

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ある。第
1図において、1は冷媒溜り器3、受液器2より下方に
配設してある冷媒加熱器でありバーナー等からの熱を冷
媒に伝熱する様に構成してある(例えば、燃焼室の外周
にアルミ、銅等で冷媒通路を構成する)、7は冷媒加熱
器1の出口から立ち上げている立ち上げ管であり冷媒溜
り部3と密接している(例えば、立ち上げ管7を銅また
はアルミで構成し冷媒溜り部3とロー付け、かしめで取
り付け熱が容易に伝熱する様に構成する。)、8は受液
器2の下端の第2逆止弁5と冷媒加熱器1の入口管とを
接続する入口管、9は前記冷媒溜り部3と前記冷媒加熱
器下部に設けた調節管である。調節管を入口管8途中に
設けても同様の作用がある。そして、10は立ち上げ管7
と放熱器6とを接続する接続配管、11は第1逆止弁、2
は前記冷媒加熱器1より上方に配設してある受液器、5
は第2逆止弁であり、前記冷媒加熱器1、立ち上げ管
7、接続管10、放熱器6、第1逆止弁11、受液器2、第
2逆止弁5は冷媒循環回路を構成しており、前記接続配
管10と受液器2の間に開閉弁4を有する均圧管12を配設
してある。
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, reference numeral 1 is a refrigerant heater disposed below the refrigerant reservoir 3 and the liquid receiver 2 and is configured to transfer heat from a burner or the like to the refrigerant (for example, combustion. A cooling medium passage is made of aluminum, copper, or the like on the outer circumference of the chamber, and 7 is a rising pipe that rises from the outlet of the refrigerant heater 1 and is in close contact with the refrigerant reservoir 3 (for example, the rising pipe 7). Is made of copper or aluminum and is brazed to the refrigerant reservoir 3 and is attached by caulking so that the heat can be transferred easily.), 8 is the second check valve 5 at the lower end of the receiver 2 and the refrigerant heating An inlet pipe connecting the inlet pipe of the container 1 and a reference pipe 9 are provided in the refrigerant reservoir 3 and a lower portion of the refrigerant heater. The same effect can be obtained by providing the adjusting pipe in the middle of the inlet pipe 8. And 10 is a start-up tube 7
And connecting pipe for connecting the radiator 6 with the radiator 6, 11 is a first check valve, 2
Is a liquid receiver 5 disposed above the refrigerant heater 1.
Is a second check valve, and the refrigerant heater 1, start-up pipe 7, connecting pipe 10, radiator 6, first check valve 11, liquid receiver 2, and second check valve 5 are refrigerant circulation circuits. A pressure equalizing pipe 12 having an on-off valve 4 is arranged between the connection pipe 10 and the liquid receiver 2.

上記構成に於て、バーナー等で冷媒加熱器1で加熱さ
れた冷媒は2相状態で立ち上げ管7を通り接続管10に流
入し液冷媒は受液器2から入口管8を通り冷媒加熱器1
へ流入する。また、接続管10内に冷媒加熱器1から流入
した2相冷媒のガス冷媒は放熱器6で凝縮液化する。こ
の時開閉弁4が閉の時は受液器2へ放熱器6からの凝縮
冷媒が第1逆止弁11を通り吸引される。なおこの時は第
2逆止弁5は閉状態であり受液器2内の圧力は吸引され
た凝縮冷媒で圧力が急激に低下し受液器2内は放熱器6
からの凝縮冷媒液で満たされる。この状態で開閉弁4を
開にすると受液器2と冷媒加熱器1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を通り冷媒加熱器1
内へ位置エネルギーによって流入する。この時第1逆止
弁11は閉状態となり冷媒加熱器1から出ているガス冷媒
は放熱器6で凝縮し溜る。次に開閉弁4を閉にすると、
再び受液器2でガス冷媒が凝縮し第2逆止弁は逆圧力の
ため閉となり放熱器6からの冷媒が第1逆止弁11をとお
り吸引されるサイクルを繰り返す。すなわち、冷媒加熱
器1、放熱器6、第1逆止弁11、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冷媒加熱器1へ供給するという間欠
動作サイクルである。ここで、冷媒加熱器1の出口管を
冷媒加熱器1より上方に配設してある接続管10に下端か
ら立ち上げ管7と連通しているため、冷媒加熱器1の出
口を放熱器6に最短距離で接続し管路抵抗を低減でき、
冷媒加熱器1内の冷媒は暖房運転中は一定量の冷媒を循
環する。そして冷媒加熱器1の冷媒が加熱されガスとな
る量が多くなると、冷媒加熱器1より上方に設けた冷媒
溜り器3の下部から冷媒加熱器1の下部に調節管9を通
り、液冷媒が流入するため冷媒加熱器1内は常に2相状
態で均一温度となる。また、冷媒加熱器1内の液冷媒が
多くなると逆に冷媒加熱器1から調節管9を通り冷媒溜
り器3に流れる。このため冷媒及びオイルは過熱する事
無く冷媒加熱器1の配管スペースの小型化が図れ暖房装
置の小型コンパクト化が得られる。また冷媒加熱器で加
熱ガス化した冷媒は直接放熱器6に搬送するため、放熱
器6に入る冷媒はガス比率が高く過熱ガスに設定できる
ため放熱器6の熱交換を高効率化出来、熱交換器を小型
コンパクト化が得られ、温風温度は高くなり暖房感が向
上する。さらに冷媒加熱器1において受液器2からの低
温の冷媒を入口管8より流入し、高温の冷媒は接続管10
から放熱器6に送られるため全体的に冷媒の温度が低く
なり熱交換性能が向上し、局部過熱を生じなく信頼性が
向上する。また、冷媒溜り部3と冷媒加熱器1のガス部
と前記放熱器6とを接続する立ち上げ管7を密接して設
けたことによりこの間で熱伝達が大幅に増加し、冷媒加
熱器1の出口冷媒温度が過熱になるとその熱により冷媒
溜り部3内でガス相が急激に増加し冷媒溜り部3から冷
媒加熱器1に冷媒が速やかに移動する。冷媒加熱器1の
出口温度が低く液相の多い2相となった時は逆に冷媒溜
り部3から立ち上がり管7に熱は流れ、冷媒溜り部3内
のガス相は少なくなり、立ち上がり管7はガス相の多い
冷媒となる。このため放熱器6への熱搬送量は安定し、
循環回路中の冷媒量は自動的に最適に調整でき放熱器6
の放熱熱量が安定し快適性が向上する。
In the above configuration, the refrigerant heated by the refrigerant heater 1 by the burner or the like flows in the two-phase state through the riser pipe 7 into the connecting pipe 10, and the liquid refrigerant flows from the receiver 2 through the inlet pipe 8 to heat the refrigerant. Bowl 1
Flow into. Further, the gas refrigerant of the two-phase refrigerant flowing into the connecting pipe 10 from the refrigerant heater 1 is condensed and liquefied by the radiator 6. At this time, when the open / close valve 4 is closed, the condensed refrigerant from the radiator 6 is sucked into the liquid receiver 2 through the first check valve 11. At this time, the second check valve 5 is in a closed state, and the pressure in the liquid receiver 2 is drastically reduced by the sucked condensed refrigerant, and the heat sink 6 in the liquid receiver 2 is closed.
Filled with condensed refrigerant liquid from. When the on-off valve 4 is opened in this state, the liquid receiver 2 and the refrigerant heater 1 are in a pressure equalizing state, and the liquid refrigerant in the liquid receiver 2 passes through the second check valve 5 and the refrigerant heater 1
It flows in by potential energy. At this time, the first check valve 11 is closed and the gas refrigerant discharged from the refrigerant heater 1 is condensed and accumulated in the radiator 6. Next, when the on-off valve 4 is closed,
The gas refrigerant is condensed again in the liquid receiver 2, the second check valve is closed due to the reverse pressure, and the cycle in which the refrigerant from the radiator 6 is sucked through the first check valve 11 is repeated. That is, in the cycle of the refrigerant heater 1, the radiator 6, the first check valve 11, the liquid receiver 2 and the second check valve 5, the liquid refrigerant from the radiator 6 is accumulated in the liquid receiver 2 and stored therein. This is an intermittent operation cycle in which the refrigerant heater 1 is intermittently supplied. Here, since the outlet pipe of the refrigerant heater 1 communicates with the connection pipe 10 arranged above the refrigerant heater 1 from the lower end to the rising pipe 7, the outlet of the refrigerant heater 1 is connected to the radiator 6 Can be connected in the shortest distance to reduce the pipeline resistance.
The refrigerant in the refrigerant heater 1 circulates a certain amount of refrigerant during the heating operation. When the amount of the refrigerant in the refrigerant heater 1 heated and becoming gas increases, the liquid refrigerant passes from the lower part of the refrigerant reservoir 3 provided above the refrigerant heater 1 to the lower part of the refrigerant heater 1 through the adjusting pipe 9. Because of the inflow, the inside of the refrigerant heater 1 always has a uniform temperature in a two-phase state. Further, when the amount of the liquid refrigerant in the refrigerant heater 1 increases, the refrigerant flows from the refrigerant heater 1 to the refrigerant reservoir 3 through the adjusting pipe 9 conversely. Therefore, the refrigerant and the oil are not overheated and the piping space of the refrigerant heater 1 can be downsized, and the heating device can be downsized and compact. Further, since the refrigerant heated and gasified by the refrigerant heater is directly conveyed to the radiator 6, the refrigerant entering the radiator 6 has a high gas ratio and can be set as a superheated gas, so that the heat exchange of the radiator 6 can be made highly efficient, The exchanger can be made smaller and more compact, and the warm air temperature rises, improving the feeling of heating. Further, in the refrigerant heater 1, the low temperature refrigerant from the liquid receiver 2 flows in through the inlet pipe 8, and the high temperature refrigerant is connected to the connecting pipe 10.
Since it is sent from the heat sink 6 to the radiator 6, the temperature of the refrigerant is lowered as a whole, heat exchange performance is improved, and local overheating does not occur, and reliability is improved. In addition, since the riser pipe 7 that connects the refrigerant reservoir 3 and the gas portion of the refrigerant heater 1 to the radiator 6 is provided in close contact, heat transfer greatly increases during this time, and the refrigerant heater 1 When the outlet refrigerant temperature becomes overheated, the heat causes a rapid increase in the gas phase in the refrigerant reservoir 3, and the refrigerant quickly moves from the refrigerant reservoir 3 to the refrigerant heater 1. When the outlet temperature of the refrigerant heater 1 is low and there are two liquid phases, the heat flows from the refrigerant reservoir 3 to the rising pipe 7 conversely, the gas phase in the refrigerant reservoir 3 decreases, and the rising pipe 7 Is a refrigerant with many gas phases. Therefore, the heat transfer amount to the radiator 6 is stable,
The amount of refrigerant in the circulation circuit can be adjusted automatically and optimally to the radiator 6
The amount of heat radiated is stable and comfort is improved.

さらに、冷媒加熱器1の出口管7から流出する2相冷
媒の流量を強制的に循環させる。このため、液冷媒を気
液分離器内から冷媒加熱器1への自然循環を考えた場合
に比べ、気液分離器内の液面を冷媒加熱器1に対して一
定以上の位置を保つ必要がなくまた、気液分離器と冷媒
加熱器の配管スペースの小型化が図れ暖房装置の小型コ
ンパクト化が得られる作用がある。
Further, the flow rate of the two-phase refrigerant flowing out from the outlet pipe 7 of the refrigerant heater 1 is forcedly circulated. Therefore, it is necessary to keep the liquid level in the gas-liquid separator at a certain level or more with respect to the refrigerant heater 1 as compared with the case where natural circulation of the liquid refrigerant from the gas-liquid separator to the refrigerant heater 1 is considered. In addition, the piping space between the gas-liquid separator and the refrigerant heater can be downsized, and the heating device can be downsized.

発明の効果 以上のように本発明の暖房装置によれば次の効果が得
られる。
Effects of the Invention As described above, the heating device of the present invention has the following effects.

(1)冷媒加熱器の出口管を放熱器との接続管と連通
し、前記冷媒加熱器の入口管は前記第2逆止弁と接続
し、受液器と出口管を開閉弁を有する均圧管で接続した
ため、冷媒加熱器と放熱器は直接接続でき、冷媒加熱器
から出たガス冷媒は放熱器で凝縮する為冷媒の圧力が低
下し、この凝縮による凝縮圧力差により冷媒加熱器の高
温ガスは冷媒加熱器から放熱器に常に吸引されるため、
冷媒加熱器内の冷媒は暖房運転中は一定量の冷媒を循環
する。このため、気液分離器内の液面を冷媒加熱器1に
対して一定以上の位置を保つ必要がなくまた、気液分離
器と冷媒加熱器の配管スペースの小型化が図れ暖房装置
の小型コンパクト化が得られる効果がある。
(1) An outlet pipe of the refrigerant heater communicates with a connecting pipe to the radiator, an inlet pipe of the refrigerant heater is connected to the second check valve, and a receiver and an outlet pipe have an opening / closing valve. Since it is connected by a pressure tube, the refrigerant heater and radiator can be directly connected, and the gas refrigerant discharged from the refrigerant heater is condensed by the radiator, so the pressure of the refrigerant decreases, and due to this condensation pressure difference due to condensation, the temperature of the refrigerant heater rises. Since the gas is always sucked from the refrigerant heater to the radiator,
The refrigerant in the refrigerant heater circulates a certain amount of refrigerant during the heating operation. Therefore, it is not necessary to keep the liquid level in the gas-liquid separator at a certain position or more with respect to the refrigerant heater 1, and the piping space between the gas-liquid separator and the refrigerant heater can be downsized, and the heating device can be downsized. There is an effect that it can be made compact.

(2)そして冷媒加熱器の冷媒が加熱されガスとなる量
が多くなると、冷媒加熱器より上方に設けた冷媒溜り器
の下部から冷媒加熱器の下部に液冷媒が流入するため冷
媒加熱器内は常に2相状態で均一温度となる。このため
冷媒及びオイルは過熱する事無く冷媒加熱器の配管スペ
ースの小型化が図れ暖房装置の小型コンパクト化が得ら
れる。
(2) When the refrigerant in the refrigerant heater is heated and becomes a large amount of gas, the liquid refrigerant flows from the lower part of the refrigerant reservoir provided above the refrigerant heater to the lower part of the refrigerant heater. Always has a uniform temperature in a two-phase state. Therefore, the refrigerant and the oil are not overheated and the piping space of the refrigerant heater can be downsized, and the heating device can be downsized.

(3)また冷媒加熱器で加熱ガス化した冷媒は直接放熱
器に搬送するため、放熱器に入る冷媒はガス比率が高く
過熱ガスに設定できるため放熱器の熱交換を高効率化出
来、熱交換器を小型コンパクト化が得られ、温風温度は
高くなり暖房感が向上する。
(3) Further, since the refrigerant heated and gasified by the refrigerant heater is directly conveyed to the radiator, the refrigerant entering the radiator has a high gas ratio and can be set as superheated gas, so that the heat exchange of the radiator can be made highly efficient, The exchanger can be made smaller and more compact, and the warm air temperature rises, improving the feeling of heating.

(4)さらに冷媒加熱器において受液器からの低温の冷
媒を入口管より流入し、高温の冷媒は接続管から放熱器
に送られるため全体的に冷媒の温度が低くなり熱交換性
能が向上し、局部過熱を生じなく信頼性が向上する。
(4) Further, in the refrigerant heater, the low-temperature refrigerant from the liquid receiver flows in through the inlet pipe, and the high-temperature refrigerant is sent from the connecting pipe to the radiator, so that the temperature of the refrigerant is lowered overall and the heat exchange performance is improved. However, reliability is improved without causing local overheating.

(5)また、冷媒溜り部と冷媒加熱器の上部と前記放熱
器とを接続する立ち上げ管を密接して設けた構成とする
ことによりこの間で熱伝達が大幅に増加し、冷媒加熱器
の出口冷媒温度が過熱になるとその熱により冷媒溜り部
内でガス相が急激に増加し冷媒溜り部から冷媒加熱器に
冷媒が速やかに移動する。冷媒加熱器の出口温度が低く
液相の多い2相となった時は逆に冷媒溜り部から立ち上
がり管に熱は流れ、冷媒溜り部内のガス相は少なくな
り、立ち上がり管はガス相の多い冷媒となる。このため
放熱器への熱搬送量は安定し、循環回路中の冷媒量は自
動的に最適に調整でき放熱器の放熱熱量が安定し快適性
が向上する。
(5) In addition, the heat transfer is significantly increased between the refrigerant reservoir, the upper part of the refrigerant heater, and the riser pipe that connects the radiator to each other. When the outlet refrigerant temperature becomes overheated, the heat causes the gas phase to rapidly increase in the refrigerant reservoir, and the refrigerant quickly moves from the refrigerant reservoir to the refrigerant heater. When the outlet temperature of the refrigerant heater is low and there are two phases with many liquid phases, on the contrary, heat flows from the refrigerant reservoir to the rising pipe, the gas phase in the refrigerant reservoir decreases, and the rising pipe has many gas phases. Becomes For this reason, the amount of heat transferred to the radiator is stable, the amount of refrigerant in the circulation circuit can be automatically and optimally adjusted, and the amount of heat radiated from the radiator is stable, improving comfort.

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

第1図は本発明の一実施例の暖房装置の回路構成図、第
2図は従来の暖房装置の回路構成図である。 1……冷媒加熱器、2……受液器、3……冷媒溜り部、
4……開閉弁、5……第2逆止弁、6……放熱器、7…
…立ち上げ管、8……入口管、9……調節管、10……接
続配管、11……第1逆止弁、12……均圧管。
FIG. 1 is a circuit configuration diagram of a heating device according to an embodiment of the present invention, and FIG. 2 is a circuit configuration diagram of a conventional heating device. 1 ... Refrigerant heater, 2 ... Liquid receiver, 3 ... Refrigerant reservoir,
4 ... on-off valve, 5 ... second check valve, 6 ... radiator, 7 ...
… Startup pipe, 8 …… Inlet pipe, 9 …… Control pipe, 10 …… Connection pipe, 11 …… First check valve, 12 …… Equalization pipe.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 桜武 達規 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 山口 紘一郎 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Tatsunori Sakuratake 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】受液器を冷媒加熱器よりも上方に配設し
て、放熱器、第1逆止弁、前記受液器、第2逆止弁、前
記冷媒加熱器を接続する接続配管と、前記冷媒加熱器の
上部と前記放熱器とを接続する接続配管と、この接続配
管と前記受液器の間に開閉弁を有する均圧管を設け、さ
らに、前記冷媒加熱器より上方に前記冷媒加熱器の下部
に接続して設けた冷媒溜り部と、前記冷媒加熱器の上部
に設けた出口管は前記接続管と連通し、前記冷媒加熱器
の下部に設けた入口管は前記第2逆止弁と接続した暖房
装置。
1. A connection pipe for arranging a liquid receiver above a refrigerant heater to connect the radiator, the first check valve, the liquid receiver, the second check valve, and the refrigerant heater. A connection pipe connecting the upper part of the refrigerant heater and the radiator, and a pressure equalizing pipe having an on-off valve between the connection pipe and the liquid receiver, and further above the refrigerant heater. A refrigerant reservoir provided at a lower portion of the refrigerant heater and an outlet pipe provided at an upper portion of the refrigerant heater communicate with the connection pipe, and an inlet pipe provided at a lower portion of the refrigerant heater is the second pipe. A heating system connected with a check valve.
【請求項2】冷媒溜り部と、冷媒加熱器の上部と放熱器
を接続する接続管とを密接して設けた特許請求の範囲第
1項記載の暖房装置。
2. The heating device according to claim 1, wherein the refrigerant reservoir portion and a connecting pipe connecting the upper portion of the refrigerant heater and the radiator are provided in close contact with each other.
JP13883388A 1988-06-06 1988-06-06 Heating system Expired - Fee Related JPH0827004B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13883388A JPH0827004B2 (en) 1988-06-06 1988-06-06 Heating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13883388A JPH0827004B2 (en) 1988-06-06 1988-06-06 Heating system

Publications (2)

Publication Number Publication Date
JPH01306734A JPH01306734A (en) 1989-12-11
JPH0827004B2 true JPH0827004B2 (en) 1996-03-21

Family

ID=15231286

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13883388A Expired - Fee Related JPH0827004B2 (en) 1988-06-06 1988-06-06 Heating system

Country Status (1)

Country Link
JP (1) JPH0827004B2 (en)

Also Published As

Publication number Publication date
JPH01306734A (en) 1989-12-11

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