JP2806109B2 - Heat transfer device - Google Patents

Heat transfer device

Info

Publication number
JP2806109B2
JP2806109B2 JP31579691A JP31579691A JP2806109B2 JP 2806109 B2 JP2806109 B2 JP 2806109B2 JP 31579691 A JP31579691 A JP 31579691A JP 31579691 A JP31579691 A JP 31579691A JP 2806109 B2 JP2806109 B2 JP 2806109B2
Authority
JP
Japan
Prior art keywords
refrigerant
liquid
gas
combustion
heat transfer
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
JP31579691A
Other languages
Japanese (ja)
Other versions
JPH05149555A (en
Inventor
茂 岩永
達規 桜武
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 Corp
Panasonic Holdings Corp
Original Assignee
Panasonic Corp
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 Panasonic Corp, Matsushita Electric Industrial Co Ltd filed Critical Panasonic Corp
Priority to JP31579691A priority Critical patent/JP2806109B2/en
Publication of JPH05149555A publication Critical patent/JPH05149555A/en
Application granted granted Critical
Publication of JP2806109B2 publication Critical patent/JP2806109B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、冷媒を加熱する時の圧
力上昇を利用して、熱を暖房などに利用する熱搬送装置
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat transfer apparatus for utilizing heat for heating or the like by utilizing a pressure increase when a refrigerant is heated.

【0002】[0002]

【従来の技術】従来の熱搬送装置は、例えば特開平3−
51631号公報に示されるように、図3のような構成
になっている。
2. Description of the Related Art A conventional heat transfer device is disclosed in, for example,
As shown in Japanese Patent No. 51631, the configuration is as shown in FIG.

【0003】すなわち、気液セパレータ1は、冷媒加熱
器2の上方に配置されるとともに冷媒加熱器2の入口管
3と冷媒加熱器2の出口管4とで連結され環状の管路で
接続されている。また、受液器5は気液セパレータ1の
上方に配置され、第1逆止弁6を有する落込み管7で気
液セパレータ1へ接続され、さらに開閉弁8を有する均
圧管9により出口管4を介して気液セパレータ1に接続
されている。気液セパレータ1と利用側として室内側に
配置される放熱器10は、ガス冷媒往き管11で接続さ
れ、放熱器10と受液器5は、第2逆止弁12を有する
液冷媒戻り管13で接続されている。以上のように、気
液セパレータ1、放熱器10、第2逆止弁12、受液器
5、第1逆止弁6は順次配管接続された環状の循環路を
形成している。14は冷媒加熱器2の出口管4に設けた
温度検知器であり、15は温度検知器14の検知する温
度により、開閉弁8の開閉時間を制御する制御装置であ
る。16は冷媒加熱器2に設けたバーナであり、バーナ
16により冷媒を加熱する。17は放熱器10に設けた
送風機である。
[0003] That is, the gas-liquid separator 1 is disposed above the refrigerant heater 2 and connected by an inlet pipe 3 of the refrigerant heater 2 and an outlet pipe 4 of the refrigerant heater 2 and connected by an annular pipe. ing. The liquid receiver 5 is disposed above the gas-liquid separator 1, is connected to the gas-liquid separator 1 by a drop pipe 7 having a first check valve 6, and is further connected to an outlet pipe by a pressure equalizing pipe 9 having an on-off valve 8. 4 is connected to the gas-liquid separator 1. The gas-liquid separator 1 and a radiator 10 arranged on the indoor side as a utilization side are connected by a gas refrigerant outflow pipe 11, and the radiator 10 and the liquid receiver 5 are connected to a liquid refrigerant return pipe having a second check valve 12. 13 are connected. As described above, the gas-liquid separator 1, the radiator 10, the second check valve 12, the liquid receiver 5, and the first check valve 6 form an annular circulation path that is sequentially connected to the pipe. Reference numeral 14 denotes a temperature detector provided in the outlet pipe 4 of the refrigerant heater 2, and reference numeral 15 denotes a control device that controls the opening / closing time of the on-off valve 8 based on the temperature detected by the temperature detector 14. Reference numeral 16 denotes a burner provided in the refrigerant heater 2, and the refrigerant is heated by the burner 16. 17 is a blower provided in the radiator 10.

【0004】上記構成において、その動作を以下に説明
する。冷媒加熱器2において、バーナ16の燃焼熱で加
熱された冷媒は、ガスと液の2相状態で出口管4を通
り、気液セパレータ1へ流入し、液冷媒は入口管3から
再び冷媒加熱器2に流入する。一方、気液セパレータ1
へ流入した2相状態の冷媒のうちガス冷媒は、ガス冷媒
往き管11から放熱器10へ入り、送風機17で送られ
た室内空気と熱交換し、放熱凝縮し過冷却液化する。
The operation of the above configuration will be described below. In the refrigerant heater 2, the refrigerant heated by the combustion heat of the burner 16 passes through the outlet pipe 4 in the two-phase state of gas and liquid, flows into the gas-liquid separator 1, and the liquid refrigerant heats again from the inlet pipe 3. Into the vessel 2. On the other hand, the gas-liquid separator 1
Of the two-phase refrigerant flowing into the gas refrigerant, the gas refrigerant enters the radiator 10 through the gas refrigerant outflow pipe 11, exchanges heat with the room air sent by the blower 17, radiates and condenses, and turns into supercooled liquid.

【0005】ここで、開閉弁8が閉のときには、放熱器
10で凝縮液化した過冷却液冷媒は、液冷媒戻り管13
から第2逆止弁12を介して、ガス冷媒を凝縮させるこ
とにより受液器5内へ流入する。このとき受液器5内の
圧力は気液セパレータ1内の圧力より低くなっているた
め、第1逆止弁6は閉状態となっている。この状態で、
開閉弁8を開とすると、受液器5と気液セパレータ1と
は均圧管9により連通して均圧状態となり、受液器5内
の液冷媒は重力により第1逆止弁6を通り気液セパレー
タ1内へ流入する。
When the on-off valve 8 is closed, the supercooled liquid refrigerant condensed and liquefied by the radiator 10 is supplied to the liquid refrigerant return pipe 13.
Then, the gas refrigerant flows into the liquid receiver 5 through the second check valve 12 by condensing the gas refrigerant. At this time, since the pressure in the liquid receiver 5 is lower than the pressure in the gas-liquid separator 1, the first check valve 6 is in a closed state. In this state,
When the on-off valve 8 is opened, the liquid receiver 5 and the gas-liquid separator 1 communicate with each other by the pressure equalizing pipe 9 to be in a pressure equalized state, and the liquid refrigerant in the liquid receiver 5 passes through the first check valve 6 due to gravity. The gas flows into the gas-liquid separator 1.

【0006】次に、開閉弁8を再び閉にすると、第1逆
止弁6は閉状態となり、受液器5内へ放熱器10の凝縮
過冷却液冷媒が、受液器内の急減圧により吸引され受液
器5が液冷媒で満たされるサイクルを繰り返す。このよ
うに、気液セパレータ1と冷媒加熱器2間は蒸発した冷
媒圧による自然循環サイクルであり、受液器5から気液
セパレータ1および冷媒加熱器2への液冷媒の供給は開
閉弁8の開閉周期による間欠動作サイクルである。
Next, when the on-off valve 8 is closed again, the first check valve 6 is closed, and the condensed supercooled liquid refrigerant of the radiator 10 flows into the receiver 5 and the pressure in the receiver is rapidly reduced. , And the cycle in which the receiver 5 is filled with the liquid refrigerant is repeated. As described above, a natural circulation cycle is performed between the gas-liquid separator 1 and the refrigerant heater 2 by the evaporated refrigerant pressure, and the supply of the liquid refrigerant from the receiver 5 to the gas-liquid separator 1 and the refrigerant heater 2 is performed by the on-off valve 8. Is an intermittent operation cycle based on the opening / closing cycle.

【0007】[0007]

【発明が解決しようとする課題】上記従来の構成におい
て、冷媒加熱による熱搬送を行なうため開閉弁8の開閉
周期を温度検知器14で検出した冷媒の蒸発温度とバー
ナ16での燃焼量に応じて適正に制御している。図4は
この定常燃焼時の開閉弁8の閉時間TOFと開時間TON
した開閉周期TS (TS =TOF+TON)での運転状況を
示し、時間t1 において開状態から閉状態に切替るとと
もに減圧開始遅れ時間Tl を伴なったあと受液器5内が
過冷却液冷媒によって冷却凝縮されて減圧時間Tr で減
圧による液冷媒の流入が完了する(TOF=Tl
r )。受液器5に流入し終った液冷媒は次の開閉弁8
の開時間TONで冷媒加熱器2側へ落込まれると共に、開
閉の繰返しで熱搬送が続行される。
In the above-mentioned conventional construction, in order to carry out heat transfer by heating the refrigerant, the opening / closing cycle of the on-off valve 8 depends on the evaporation temperature of the refrigerant detected by the temperature detector 14 and the amount of combustion in the burner 16. Is properly controlled. Figure 4 shows the operating conditions of this between closing the steady combustion time of the on-off valve 8 T OF and closing period T S which is opened time T ON (T S = T OF + T ON), from the open state at time t 1 inflow of the liquid refrigerant by decompression in later receiver 5 entailed a vacuum start delay time T l with switched to the closed state is cooled and condensed by the supercooled liquid refrigerant pressure reducing time T r is completed (T oF = T l +
Tr ). The liquid refrigerant that has flowed into the receiver 5 is supplied to the next on-off valve 8.
At the opening time T ON of the above, the heat is transferred to the refrigerant heater 2 side, and the heat transfer is continued by repeating the opening and closing.

【0008】以上のように定常燃焼時における熱搬送を
安定して継続させることには何ら問題はない。しかし、
この熱搬送を暖房に利用する場合などでは、利用側とな
る室内側の温度(室温)が上昇し設定値に達したことに
よる燃焼停止時(以下サーモOFFと呼ぶ)および室温
が設定値を下回ることによる燃焼開始(以下サーモON
と呼ぶ)などの冷媒加熱量が大巾に変化する時におい
て、液冷媒の挙動が不安定となって受液器5内への液冷
媒の流入が不確実となり、冷媒加熱器において異常過熱
を生じ、ひどい時は空焼きによる機器停止を招くなど過
渡変化時における安定加熱運転に課題があった。
As described above, there is no problem in stably continuing the heat transfer during the steady combustion. But,
In the case where this heat transfer is used for heating, for example, when the temperature of the indoor side (room temperature) on the user side rises and reaches a set value, combustion stops (hereinafter referred to as thermo-OFF) and the room temperature falls below the set value. Start of combustion (hereinafter thermo ON)
), The behavior of the liquid refrigerant becomes unstable, the flow of the liquid refrigerant into the receiver 5 becomes uncertain, and abnormal overheating occurs in the refrigerant heater. There is a problem in the stable heating operation at the time of a transient change, such as causing the equipment to stop due to empty baking when it is severe.

【0009】本発明は上記課題を解決するもので、冷媒
加熱熱搬送における過渡変化時の冷媒循環を改善し、安
定加熱運転を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and has as its object to provide a stable heating operation by improving the circulation of the refrigerant at the time of a transient change in the heat transfer by heating the refrigerant.

【0010】[0010]

【課題を解決するための手段】本発明は上記目的を達成
するため、バーナを有する冷媒加熱器と気液セパレータ
を環状管路に接続し、前記気液セパレータの上方に設け
た受液器を、第1逆止弁を有する落込み管と開閉弁を有
する均圧管とで前記環状管路に接続した熱搬送部と、前
記気液セパレータ、送風機を有する放熱器、第2逆止
弁、前記受液器を順次配管接続した環状の循環路と、前
記バーナの燃焼停止時は前記送風機の風量を所定値まで
低減し、燃焼開始時は風量を所定値まで増加させ、かつ
風量の増減変化速度は風量低減時を大きくする制御装置
を設けた構成としている。
SUMMARY OF THE INVENTION In order to achieve the above object, the present invention provides a liquid receiver having a refrigerant heater having a burner and a gas-liquid separator connected to an annular conduit, and provided above the gas-liquid separator. A heat transfer unit connected to the annular conduit with a dropping pipe having a first check valve and a pressure equalizing pipe having an on-off valve, the gas-liquid separator, a radiator having a blower, a second check valve, An annular circulation path in which liquid receivers are sequentially connected to a pipe, and when the combustion of the burner is stopped, the air volume of the blower is reduced to a predetermined value, at the start of combustion, the air volume is increased to a predetermined value, and the rate of change of the air volume is increased or decreased. Has a configuration in which a control device for increasing the amount of air flow reduction is provided.

【0011】[0011]

【作用】本発明は上記構成により、サーモOFFなどの
燃焼停止時では放熱器の送風機風量を急速に低減して冷
媒圧力の低下速度を遅くし冷媒圧力の急低下時に生じる
液冷媒の過冷却度の急低下に伴なう液冷媒の受液器への
流入停止を防止する。さらに、サーモONなどの燃焼開
始時では送風機風量を徐々に増加して冷媒圧力を急速に
上げて液冷媒の過冷却度を高めるとともに放熱器への液
冷媒の急速な滞留量の増加による冷媒量分布のアンバラ
ンスを防ぎ受液器への液冷媒の流入を促進する。
According to the present invention, the supercooling degree of the liquid refrigerant generated when the refrigerant pressure suddenly decreases by rapidly reducing the blower air volume of the radiator to slow down the refrigerant pressure when the combustion is stopped such as when the thermostat is turned off. To prevent the liquid refrigerant from flowing into the receiver due to the rapid decrease in the temperature. Furthermore, at the start of combustion such as thermo-ON, the blower air volume is gradually increased to rapidly increase the refrigerant pressure to increase the degree of supercooling of the liquid refrigerant, and the amount of refrigerant due to the rapid increase in the amount of liquid refrigerant retained in the radiator. Prevents imbalance in distribution and promotes the flow of liquid refrigerant into the receiver.

【0012】以上のようにして、燃焼停止時および燃焼
開始時において受液器へ液冷媒が流入し易い状態を生み
出し、冷媒循環を改善して冷媒加熱器での異常過熱の発
生を防止できる。
As described above, when the combustion is stopped and when the combustion is started, a state in which the liquid refrigerant easily flows into the liquid receiver is created, the refrigerant circulation is improved, and the occurrence of abnormal overheating in the refrigerant heater can be prevented.

【0013】[0013]

【実施例】以下本発明の実施例を図1で説明する。FIG. 1 shows an embodiment of the present invention.

【0014】図1において、図3と同一符号は同一部材
を示し同一機能を有しているので詳細な説明は省略し、
異なる点を中心に説明する。
In FIG. 1, the same reference numerals as those in FIG. 3 denote the same members, and have the same functions.
The different points will be mainly described.

【0015】18はバーナ16と対向して設けた冷媒加
熱器2と気液セパレータ1を環状管路に接続し、気液セ
パレータ1の上方に設けた受液器5を、第1逆止弁6を
有する落込み管7と開閉弁8を有する均圧管9とで前記
環状管路に接続した熱搬送部である。19は気液セパレ
ータ1、送風機17を有する放熱器10、第2逆止弁1
2、受液器5を順次配管接続した環状の循環路である。
20は放熱器10に設けた室温検知器であり、放熱器1
0に対して流入する空気の温度を検知する。21はバー
ナ16の燃焼量を可変する燃焼量可変装置である。
A refrigerant heater 2 and a gas-liquid separator 1 provided opposite to the burner 16 are connected to an annular conduit, and a liquid receiver 5 provided above the gas-liquid separator 1 is connected to a first check valve. 6 is a heat transfer section connected to the annular pipe by a drop pipe 7 having an opening 6 and a pressure equalizing pipe 9 having an on-off valve 8. 19 is a gas-liquid separator 1, a radiator 10 having a blower 17, and a second check valve 1.
2. An annular circulation path in which the liquid receivers 5 are sequentially connected by piping.
Reference numeral 20 denotes a room temperature detector provided on the radiator 10, and the radiator 1
For 0, the temperature of the air flowing in is detected. Reference numeral 21 denotes a combustion amount varying device that varies the combustion amount of the burner 16.

【0016】22は開閉弁8、温度検知器14、送風機
17、室温検知器20、燃焼量可変装置21に電気的に
接続されるとともにバーナ16の燃焼停止時は送風機1
7の風量を所定値まで低減し、燃焼開始時は風量を所定
値まで増加させ、かつ風量の増減変化速度は風量低減時
を大きくする制御装置である。
Numeral 22 is electrically connected to the on-off valve 8, the temperature detector 14, the blower 17, the room temperature detector 20, and the variable combustion amount device 21, and is connected to the blower 1 when the burner 16 stops burning.
7 is a control device for reducing the air flow to a predetermined value, increasing the air flow to a predetermined value at the start of combustion, and increasing or decreasing the rate of increase or decrease of the air flow when the air flow is reduced.

【0017】上記構成において、開閉弁8の開閉動作と
バーナ16の燃焼、送風機17の運転により冷媒加熱に
よる熱搬送の暖房運転を行なうが、サーモOFF/ON
による燃焼停止および燃焼開始する時の動作について図
2で説明する。
In the above configuration, the heating operation of the heat transfer by the refrigerant heating is performed by the opening / closing operation of the on-off valve 8, the combustion of the burner 16, and the operation of the blower 17, but the thermo OFF / ON.
The operation at the time of stopping the combustion and starting the combustion will be described with reference to FIG.

【0018】冷媒加熱の熱搬送運転により利用側の室温
が上昇し、室温検知器20があらかじめ設定した所定値
に達したことを検知すると、制御装置22でサーモOF
Fとして時間t0 で燃焼停止する。燃焼停止後も開閉弁
8は開閉動作している。放熱器10の送風機17はV1
の風量で動作していたが、燃焼停止とともに所定値V 0
まで風量を急速に低減させる。
[0018] Room temperature on the user side by heat transfer operation of refrigerant heating
Rises, and the room temperature detector 20 sets a predetermined value
When the control device 22 detects that the
Time t as F0To stop the combustion. Open / close valve even after stopping combustion
8 is opening and closing operation. The blower 17 of the radiator 10 has V1
Operating at the air volume of 0
To rapidly reduce the air flow.

【0019】この風量低下速度は変化時間Δt0 の間に
風量変化量ΔVを生じるようにここではタイマー制御し
ている。
[0019] The air flow rate of decrease in this case to produce a flow rate change amount ΔV between the change time Delta] t 0 are timer controlled.

【0020】次にサーモONにより時間tS で燃焼開始
とともに送風機17は所定値V1 まで風量を徐々に増加
させる。
[0020] Then the blower 17 together with the combustion initiated at the time t S by thermo ON gradually increase the air volume to a predetermined value V 1.

【0021】この風量増加速度は変化時間ΔtS の間に
風量変化量ΔVを生じるようここではタイマー制御して
いる。
Here, the timer is controlled so that the rate of increase of the air flow produces an air flow change amount ΔV during the change time Δt S.

【0022】しかも風量の増減変化速度は風量低減時を
大きくするので変化時間はΔt0 <ΔtS としている。
In addition, since the speed of change of the air flow is increased when the air flow is reduced, the change time is set to Δt 0 <Δt S.

【0023】以上のように、送風機風量を燃焼停止時は
低減し燃焼開始時は増加せしめるとともに、その風量変
化速度を風量低減時は早く風量増加時は遅くすることに
より、燃焼停止時では冷媒の蒸発圧力の低下を遅くして
液冷媒の過冷却度の低下を遅くし、開閉弁閉成時の受液
器圧力の減圧による液冷媒の受液器への流入を継続させ
冷媒加熱器の残熱を利用側へ回収して異常過熱の発生を
防止し、燃焼開始時では冷媒の蒸発圧力の上昇を早くし
て液冷媒の過冷却度を高めるとともに放熱能力の過大時
に生じる放熱器への液冷媒の一時的な急増による冷媒量
分布のアンバランスを防止し、受液器圧力の減圧による
受液器への液冷媒の流入を促進して冷媒循環を改善し、
異常過熱の発生を防止した安定立上げ運転を実現する。
As described above, the air flow rate of the blower is reduced when the combustion is stopped and increased when the combustion is started, and the rate of change of the air flow is reduced when the air flow is reduced and the speed is increased when the air flow is increased. Slowing down the evaporation pressure and slowing down the degree of supercooling of the liquid refrigerant, continuing the flow of the liquid refrigerant into the receiver due to the pressure reduction of the receiver when the on-off valve is closed, and leaving the remaining refrigerant heater Heat is recovered to the user side to prevent the occurrence of abnormal overheating, and at the start of combustion, the evaporation pressure of the refrigerant is quickly increased to increase the degree of supercooling of the liquid refrigerant and to the radiator that occurs when the heat radiation capacity is excessive. Prevents imbalance in refrigerant volume distribution due to temporary sudden increase in refrigerant, promotes inflow of liquid refrigerant into the receiver due to reduced pressure of the receiver, and improves refrigerant circulation,
Realizes stable start-up operation that prevents abnormal overheating.

【0024】以上のように、燃焼停止時および燃焼開始
時での冷媒加熱器の異常過熱を防止して冷媒の熱分解あ
るいは冷媒加熱器の熱劣化などの発生を防止し、システ
ムの信頼性、耐久性を向上できる。
As described above, the abnormal overheating of the refrigerant heater at the time of stopping the combustion and at the start of the combustion is prevented, thereby preventing the thermal decomposition of the refrigerant or the deterioration of the refrigerant heater from occurring. Durability can be improved.

【0025】さらに、燃焼停止時に残熱を利用側である
室内側に回収できるため、エネルギーのムダを省き経済
性が向上できる。
Furthermore, since the residual heat can be recovered to the indoor side, which is the utilization side, at the time of stopping the combustion, waste of energy can be saved and the economic efficiency can be improved.

【0026】また、風量低減時はタイマー制御とすれ
ば、冷媒温度を検知して風量制御する場合の熱容量など
による応答遅れの発生がなく、圧力低下が比較的早い減
圧時に対して応答遅れがなく追従できて有効であり、簡
便で実用性が向上する。
Further, if the air flow is reduced by using timer control, there is no response delay due to heat capacity or the like when the refrigerant temperature is detected and the air flow is controlled, and there is no response delay when the pressure is reduced relatively quickly. It is effective because it can follow, and is simple and practical.

【0027】[0027]

【発明の効果】以上のように本発明の熱搬送装置は、バ
ーナ、冷媒加熱器、気液セパレータ、受液器、第1逆止
弁、開閉弁を有する熱搬送部と、気液セパレータ、送風
機を有する放熱器、第2逆止弁、受液器を順次接続した
循環路と、バーナの燃焼停止時は送風機の風量を所定値
まで低減し、燃焼開始時は風量を所定値まで増加させ、
かつ風量の増減変化速度は風量低減時を大きくする制御
装置を設けた構成としているので、燃焼停止時および燃
焼開始時での冷媒加熱器の異常過熱が防止でき、熱搬送
装置の信頼性、耐久性を向上できるという効果がある。
また、燃焼停止時に冷媒加熱器の残熱を利用側である室
内側に回収でき、経済性が向上するという利点もある。
As described above, the heat transfer apparatus according to the present invention comprises a heat transfer section having a burner, a refrigerant heater, a gas-liquid separator, a liquid receiver, a first check valve, an on-off valve, a gas-liquid separator, A radiator having a blower, a second check valve, a circulation path in which a liquid receiver is sequentially connected, and when the burner stops burning, the air volume of the blower is reduced to a predetermined value, and when the combustion starts, the air volume is increased to a predetermined value. ,
In addition, a control device that increases the rate of change of the air flow to increase when the air flow is reduced is provided, so that abnormal overheating of the refrigerant heater at the time of combustion stop and start of combustion can be prevented, and the reliability and durability of the heat transfer device The effect is that the performance can be improved.
Further, there is also an advantage that the residual heat of the refrigerant heater can be recovered to the indoor side, which is the use side, when the combustion is stopped, and the economic efficiency is improved.

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

【図1】本発明の一実施例の熱搬送装置のシステム構成
FIG. 1 is a system configuration diagram of a heat transfer device according to an embodiment of the present invention.

【図2】本発明の実施例の制御動作図FIG. 2 is a control operation diagram according to the embodiment of the present invention.

【図3】従来の熱搬送装置のシステム構成図FIG. 3 is a system configuration diagram of a conventional heat transfer device.

【図4】従来の熱搬送装置の開閉弁動作説明図FIG. 4 is an explanatory diagram of an on-off valve operation of a conventional heat transfer device.

【符号の説明】[Explanation of symbols]

1 気液セパレータ 2 冷媒加熱器 5 受液器 6 第1逆止弁 7 落込み管 8 開閉弁 9 均圧管 10 放熱器 12 第2逆止弁 16 バーナ 17 送風機 18 熱搬送部 19 循環路 22 制御装置 REFERENCE SIGNS LIST 1 gas-liquid separator 2 refrigerant heater 5 liquid receiver 6 first check valve 7 drop pipe 8 on-off valve 9 equalizing pipe 10 radiator 12 second check valve 16 burner 17 blower 18 heat transfer section 19 circulation path 22 control apparatus

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.6,DB名) F24D 7/00──────────────────────────────────────────────────続 き Continued on front page (58) Field surveyed (Int.Cl. 6 , DB name) F24D 7/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】バーナを有する冷媒加熱器と気液セパレー
タを環状管路に接続し、前記気液セパレータの上方に設
けた受液器を、第1逆止弁を有する落込み管と開閉弁を
有する均圧管とで前記環状管路に接続した熱搬送部と、
前記気液セパレータ、送風機を有する放熱器、第2逆止
弁、前記受液器を順次配管接続した環状の循環路と、前
記バーナの燃焼停止時は前記送風機の風量を所定値まで
低減し、燃焼開始時は風量を所定値まで増加させ、かつ
風量の増減変化速度は風量低減時を大きくする制御装置
を設けた熱搬送装置。
A refrigerant heater having a burner and a gas-liquid separator are connected to an annular conduit, and a receiver provided above the gas-liquid separator is provided with a dropping pipe having a first check valve and an on-off valve. A heat transfer unit connected to the annular conduit with an equalizing pipe having
The gas-liquid separator, a radiator having a blower, a second check valve, an annular circulation path in which the liquid receiver is sequentially connected with a pipe, and reducing the air volume of the blower to a predetermined value when combustion of the burner is stopped, A heat transfer device provided with a control device for increasing the air volume to a predetermined value at the start of combustion and increasing or decreasing the air volume at a rate of increasing or decreasing the air volume.
【請求項2】風量の低減時はタイマー制御とした請求項
1記載の熱搬送装置。
2. The heat transfer device according to claim 1, wherein timer control is performed when the air volume is reduced.
JP31579691A 1991-11-29 1991-11-29 Heat transfer device Expired - Fee Related JP2806109B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31579691A JP2806109B2 (en) 1991-11-29 1991-11-29 Heat transfer device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31579691A JP2806109B2 (en) 1991-11-29 1991-11-29 Heat transfer device

Publications (2)

Publication Number Publication Date
JPH05149555A JPH05149555A (en) 1993-06-15
JP2806109B2 true JP2806109B2 (en) 1998-09-30

Family

ID=18069659

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31579691A Expired - Fee Related JP2806109B2 (en) 1991-11-29 1991-11-29 Heat transfer device

Country Status (1)

Country Link
JP (1) JP2806109B2 (en)

Also Published As

Publication number Publication date
JPH05149555A (en) 1993-06-15

Similar Documents

Publication Publication Date Title
JP2806109B2 (en) Heat transfer device
JP2780546B2 (en) Heat transfer device
JP2792289B2 (en) Heat transfer device
JP2924381B2 (en) Heat transfer device
JP2806108B2 (en) Heat transfer device
JP2783024B2 (en) Heat transfer device
JP2806110B2 (en) Heat transfer device
JP2783025B2 (en) Heat transfer device
JP2792288B2 (en) Heat transfer device
JP3240344B2 (en) Refrigerant temperature controller for gas absorption heat source equipment
JP3399025B2 (en) Heat transfer device
JP2689663B2 (en) Heating system
JP3407181B2 (en) Absorption type cold heat generator
JP3044868B2 (en) Heat transfer device
JP3594426B2 (en) Air conditioner
JP2692968B2 (en) Heat transfer device
JP3289235B2 (en) Absorption type cold heat generator
JP3446159B2 (en) Absorption type cold heat generator
JP2692969B2 (en) Heat transfer device
JP2692967B2 (en) Heat transfer device
JPS604040Y2 (en) Separate air conditioner/heater
JPH0327826B2 (en)
JPH0814686A (en) Refrigerant heating type heater cooler
JPS649535B2 (en)
JPH02150651A (en) Heating apparatus

Legal Events

Date Code Title Description
LAPS Cancellation because of no payment of annual fees