JPH05340550A - Controller of refrigerant heater - Google Patents

Controller of refrigerant heater

Info

Publication number
JPH05340550A
JPH05340550A JP4145369A JP14536992A JPH05340550A JP H05340550 A JPH05340550 A JP H05340550A JP 4145369 A JP4145369 A JP 4145369A JP 14536992 A JP14536992 A JP 14536992A JP H05340550 A JPH05340550 A JP H05340550A
Authority
JP
Japan
Prior art keywords
refrigerant
temperature
heat
heat exchange
exchange section
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP4145369A
Other languages
Japanese (ja)
Other versions
JP2921264B2 (en
Inventor
Katsuzo Konakawa
勝蔵 粉川
Ryuta Kondo
龍太 近藤
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 JP4145369A priority Critical patent/JP2921264B2/en
Publication of JPH05340550A publication Critical patent/JPH05340550A/en
Application granted granted Critical
Publication of JP2921264B2 publication Critical patent/JP2921264B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/0008Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one medium being in heat conductive contact with the conduits for the other medium
    • F28D7/0025Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one medium being in heat conductive contact with the conduits for the other medium the conduits for one medium or the conduits for both media being flat tubes or arrays of tubes

Abstract

PURPOSE:To provide a controller of a refrigerant heater used for an air conditioning device by heating refrigerant with high temperature gas such as combustion gas, wherein when the refrigerant is overheated because of an insufficient refrigerant in a refrigerant heating portion, that can be immediately detected to normalize the operation of the system. CONSTITUTION:A controller 29 outputs an overheating signal when the temperature output of an overheating temperature detecting means 25 is more than the fixed value. And the controller 29 inputs the temperature output from the overheating temperature detecting means 25 for every fixed times, computes the difference of the before and after outputs in the controller 29, and outputs the overheating signal when the computed value is more than the fixed value. Accordingly, the device can be operated without any response delay because the controller 29 stops the drive of a burner 8 by outputting the overheating signal, and the protection of the device and the system operation can be normalized, moreover heat decomposition and deterioration of refrigerant do not occur, and a system having high reliability can be obtained.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は燃焼ガス等の高温ガスに
より水、コロン等の冷媒を加熱し冷暖房装置に利用する
冷媒加熱器の制御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 control device for a refrigerant heater which heats a refrigerant such as water or cologne by a high temperature gas such as a combustion gas and uses the refrigerant in a cooling and heating device.

【0002】[0002]

【従来の技術】従来の被加熱側流体に冷媒を用いて、燃
焼ガスにより加熱して液状冷媒を蒸発気化させて潜熱に
より熱を運び暖房を行うものに図3に示すような冷媒加
熱暖房機がある。これは燃焼ガスと冷媒との熱交換を行
う熱交換器1と放熱器2を循環用の密閉管路3で連結す
ると共に、密閉管路3中に設けた冷媒搬送機4により冷
媒を強制循環するように構成されている。図4は、上記
熱交換器1の従来例を示したもので(特開昭59−10
7167号公報)、水平方向に延びる円筒状の筒体の内
周面に長手方向に沿い多数のフィン5を設け、外周面の
軸方向にはパイプ保持部6及び冷媒が内部を流れるパイ
プ7を設け、そして、バーナ8からの燃焼ガスを筒体内
面に沿い水平横方向に流して、冷媒搬送機4により送ら
れ、パイプ7内を流れる冷媒を加熱するものである。9
は温度検知器であり、前記パイプ保持部6の間の表面に
取り付け、冷媒が異常に温度上昇した場合、温度検知器
9が一定の温度以上になると加熱を停止するように制御
している。
2. Description of the Related Art A conventional refrigerant heating / heating machine as shown in FIG. 3 is used in which a refrigerant is used as a fluid to be heated and is heated by combustion gas to evaporate a liquid refrigerant to carry heat by latent heat for heating. There is. This connects the heat exchanger 1 for exchanging heat between the combustion gas and the refrigerant with the radiator 2 by the closed pipe 3 for circulation, and forcibly circulates the refrigerant by the refrigerant carrier 4 provided in the closed pipe 3. Is configured to. FIG. 4 shows a conventional example of the heat exchanger 1 (Japanese Patent Application Laid-Open No. 59-10).
No. 7167), a large number of fins 5 are provided on the inner peripheral surface of a cylindrical body extending in the horizontal direction along the longitudinal direction, and a pipe holding portion 6 and a pipe 7 through which a refrigerant flows in the axial direction of the outer peripheral surface. The combustion gas from the burner 8 is provided to flow horizontally in the horizontal direction along the inner surface of the cylinder, and is sent by the refrigerant carrier 4 to heat the refrigerant flowing in the pipe 7. 9
Is a temperature detector, which is attached to the surface between the pipe holding portions 6 and controls so that the heating is stopped when the temperature of the refrigerant is abnormally increased and the temperature detector 9 reaches a certain temperature or higher.

【0003】[0003]

【発明が解決しようとする課題】しかし、この暖房シス
テムでは冷媒搬送に外部動力としての冷媒搬送機4が必
要であり、そこで暖房運転時のランニングコストを低減
することが望まれている。
However, in this heating system, the refrigerant carrier 4 as an external power is required to carry the refrigerant, and therefore it is desired to reduce the running cost during the heating operation.

【0004】暖房運転時のランニングコスト低減には冷
媒搬送用の外部動力を無くして無動力で熱搬送すること
が有効である。無動力熱搬送により冷媒加熱暖房を行う
場合、液状冷媒が加熱されて発生する気体冷媒の浮力に
よる自然循環力が重要となる。
In order to reduce the running cost during the heating operation, it is effective to transfer heat without power by eliminating the external power for transferring the refrigerant. When performing refrigerant heating and heating by non-powered heat transfer, the natural circulation force due to the buoyancy of the gaseous refrigerant generated by heating the liquid refrigerant is important.

【0005】しかしながら上記従来の構成で、冷媒加熱
の熱交換機1は、冷媒は水平方向に延びるパイプ7内を
流れるため、加熱されて気液二相混合状態の冷媒の気体
成分がスムーズに出口に向かって流れないため冷媒の淀
みを生じ、局部的な異常過熱を発生する。また筒体内の
燃焼室と熱交換部が一体であるため熱交換量が燃焼状態
により不均一となり、局部過熱を生じ冷媒の熱分解ある
いは機器の異常温度上昇など、機器の信頼性能上、課題
があった。また、冷媒が異常温度上昇する時、冷媒が潜
熱変化した後顕熱変化するため、この時、冷媒は急激に
温度上昇し、温度検知器の熱容量による応答が遅れが生
じた。そのため、冷媒が高温に過熱され熱分解を発生
し、性能劣化や腐食等機器の信頼性で問題であった。
However, in the above-described conventional structure, in the heat exchanger 1 for heating the refrigerant, the refrigerant flows in the pipe 7 extending in the horizontal direction, so that the gas component of the refrigerant which is heated and is in the gas-liquid two-phase mixed state smoothly exits. Since it does not flow toward the interior, stagnation of the refrigerant occurs, causing localized abnormal overheating. In addition, since the combustion chamber and heat exchange part in the cylinder are integrated, the amount of heat exchange becomes uneven depending on the combustion state, causing local overheating, thermal decomposition of the refrigerant, abnormal temperature rise of the device, etc. there were. In addition, when the temperature of the refrigerant rises to an abnormal temperature, the temperature of the refrigerant rapidly rises because the latent heat of the refrigerant changes and then the sensible heat of the refrigerant changes. Therefore, the response due to the heat capacity of the temperature detector is delayed. Therefore, the refrigerant is overheated to a high temperature to cause thermal decomposition, which causes a problem in reliability of equipment such as performance deterioration and corrosion.

【0006】本発明は上記課題を解決するため、バーナ
等で加熱する冷媒加熱器の自然循環サイクルの自然循環
力を増進させて、円滑に冷媒を循環させて無動力熱搬送
を確実におこなわせ、高温燃焼ガスを燃焼室から均一に
熱交換部に導き冷媒の均一温度の維持とにより冷媒の熱
分解を生じなく信頼性の高いシステムとし、さらに冷媒
加熱器に冷媒が不足した場合等、冷媒が過熱された時、
直ちにこれを検知し機器の保護とシステムの動作を正常
化する。
In order to solve the above problems, the present invention enhances the natural circulation force of the natural circulation cycle of a refrigerant heater heated by a burner or the like to smoothly circulate the refrigerant to ensure unpowered heat transfer. , A high-temperature combustion gas is uniformly introduced from the combustion chamber to the heat exchange section to maintain a uniform temperature of the refrigerant, and a highly reliable system does not cause thermal decomposition of the refrigerant, and when the refrigerant heater lacks the refrigerant, etc. When is overheated,
Immediately detect this and protect equipment and normalize system operation.

【0007】[0007]

【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、冷媒入口部と冷媒出口部に連通した熱交換部
と、前記熱交換部を加熱する熱源部と、前記熱交換部に
設けた過熱温度検知手段と、前記過熱温度検知手段の温
度出力が一定値以上である時は過熱信号を出力する制御
部とを備え、前記制御部は前記過熱温度検知手段の温度
出力を一定の時間毎に入力し、この前後の温度出力の差
を演算し、この値が所定の値以上である時は過熱信号を
出力する構成としてある。
In order to achieve the above object, the present invention includes a heat exchange section communicating with a refrigerant inlet section and a refrigerant outlet section, a heat source section for heating the heat exchange section, and a heat exchange section. An overheat temperature detecting means is provided, and a control section that outputs an overheat signal when the temperature output of the overheat temperature detecting means is a certain value or more, and the control section keeps the temperature output of the overheat temperature detecting means constant. It is inputted every time, the difference between the temperature output before and after this is calculated, and when this value is equal to or more than a predetermined value, an overheat signal is output.

【0008】[0008]

【作用】本発明は上記構成によって、通常時、冷媒は、
冷媒入口部から熱交換部にはいり、熱源部により熱交換
部で加熱され、高温冷媒ガスとなって冷媒出口部から出
て循環する。この時、冷媒は蒸発による潜熱で熱を搬送
する。このため、熱交換部は熱源部から加熱される熱量
と冷媒に放出する熱量でバランスしており、運転中に冷
媒が外部に洩れる等、充填量の減少あるいは循環量が減
少した時等の、熱を冷媒に正常に放出できない時は、熱
交換部が急激に過熱し高温となって冷媒並びに冷凍機油
が高温劣化する。また、異常時として、運転開始時に熱
交換部に冷媒が無い時は、熱源部により熱交換部が過熱
され過熱温度検知手段の温度出力は急激に上昇する。そ
こで、過熱温度検知手段の温度出力が一定値以上になる
と過熱信号を制御部に出力し、機器の保護とシステムの
動作を正常化する。
According to the present invention, the refrigerant is
The refrigerant enters the heat exchange section, is heated by the heat source section in the heat exchange section, becomes high-temperature refrigerant gas, and exits from the refrigerant exit section and circulates. At this time, the refrigerant transfers heat by latent heat due to evaporation. Therefore, the heat exchange section balances the amount of heat that is heated from the heat source and the amount of heat that is released to the refrigerant, such as when the refrigerant leaks to the outside during operation, such as when the filling amount decreases or the circulation amount decreases, When the heat cannot be normally released to the refrigerant, the heat exchange section rapidly overheats to a high temperature, and the refrigerant and the refrigerating machine oil deteriorate at a high temperature. Further, as an abnormal condition, when there is no refrigerant in the heat exchanging portion at the start of operation, the heat exchanging portion is overheated by the heat source portion, and the temperature output of the overheat temperature detecting means rapidly rises. Therefore, when the temperature output of the overheat temperature detecting means exceeds a certain value, an overheat signal is output to the control section to normalize the protection of the equipment and the operation of the system.

【0009】また、別の異常時として、運転開始時に熱
交換部に冷媒が有りかつ冷媒の循環が停止した時は、最
初、熱源部により熱交換部が受けた熱はこの冷媒の蒸発
潜熱に変わるため、過熱温度検知手段の温度出力の応答
が遅くなる。そこで、熱交換部に有る冷媒が全て蒸発す
るのを予知することにより、機器を停止する。すなわ
ち、過熱温度検知手段の温度出力を一定の時間毎に入力
し、この前後の温度出力を演算し、この値が所定の値以
上である時は過熱信号を出力することにより、熱交換器
の冷媒が液相状態で無くなり気相のみで顕熱による急激
な上昇を検知でき、機器の保護とシステムの動作を正常
化する。そのため、冷媒加熱器に冷媒が不足した場合等
冷媒が過熱する時、直ちに冷媒の温度を検知し機器の保
護とシステムの動作を正常化でき、冷媒の熱分解、劣化
が生じ無く信頼性の高いシステムになる。
Further, as another abnormal condition, when there is a refrigerant in the heat exchange section at the start of operation and the circulation of the refrigerant is stopped, the heat received by the heat exchange section by the heat source section is first converted to latent heat of vaporization of this refrigerant. Therefore, the response of the temperature output of the overheat temperature detecting means becomes slow. Therefore, the equipment is stopped by predicting that all the refrigerant in the heat exchange section will evaporate. That is, the temperature output of the overheat temperature detecting means is input at regular intervals, the temperature output before and after this is calculated, and when this value is equal to or greater than a predetermined value, an overheat signal is output, thereby The refrigerant disappears in the liquid phase, and a sudden rise due to sensible heat can be detected only in the gas phase, thus protecting the equipment and normalizing the system operation. Therefore, when the refrigerant overheats, such as when the refrigerant heater runs short, the temperature of the refrigerant can be immediately detected to normalize the equipment protection and system operation, and the thermal decomposition and deterioration of the refrigerant do not occur and are highly reliable. Become a system.

【0010】[0010]

【実施例】以下、本発明の実施例を添付図面を参照して
説明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

【0011】図1から図2において、10は内面に断熱
材23を設けて燃焼室10aを形成した円筒状の燃焼室
ケースで、底部にバーナ8を臨ませている。この燃焼室
ケース10は先端の開口面を、多数の縦方向の高温ガス
通路12を有する高温ガス通路体12aの外面に接合さ
せている。高温ガス通路体12aは上下に2分割して両
者間に、各高温ガス通路12が燃焼室10aのガス出口
13へ連通するように横長の入口12bを形成してい
る。そして、高温ガス通路体12aは伝熱隔壁11に接
合して、これに高温ガス通路12の熱及び多数の伝熱フ
ィン22を通じて熱を均一に伝える。14aは燃焼室ケ
ース10の先端を延長して、高温ガス通路体12aの各
高温ガス通路12の上下の出口側および高温ガス通路体
12aの左右側を囲んで排気室14bを形成した排気ケ
ースで、上部に排気路14を有する。15は伝熱隔壁1
1の外面に熱的に接合させた熱交換部であり、縦方向の
冷媒通路16が多数設けられている。17は熱交換部1
5の下端に設けた入口ヘッダー管、18は熱交換部15
の上端に設けた出口ヘッダー管であり、それぞれ冷媒入
口管19、冷媒出口管20を接続し、この各々により冷
媒回路と接続しており、入口ヘッダー管17の他端には
下方に曲折しオイル抜き管21を設けてある。入口ヘッ
ダー管17と出口ヘッダー管18はそれぞれ縦方向の冷
媒通路16により連通している。22は伝熱隔壁11の
内側に熱的に接した伝熱フィンであり、多数枚としてあ
る。燃焼室10aはその高温ガス通路12と接しない残
りの外面を覆う断熱材23を燃焼ケース10の内部に設
けてある。高温ガス通路12の伝熱隔壁11の一部に、
この伝熱隔壁11に密着して伝熱具24を設け、この伝
熱具24に対抗する位置の熱交換部15に、過熱温度検
知手段として温度サーミスタ25を取り付けた構成とし
たものである。
In FIGS. 1 and 2, reference numeral 10 denotes a cylindrical combustion chamber case in which a heat insulating material 23 is provided on the inner surface to form a combustion chamber 10a, and a burner 8 faces the bottom. The combustion chamber case 10 has an open end surface joined to the outer surface of a high temperature gas passage body 12a having a large number of vertical high temperature gas passages 12. The high temperature gas passage body 12a is vertically divided into two, and a horizontally long inlet 12b is formed between the two so that each high temperature gas passage 12 communicates with the gas outlet 13 of the combustion chamber 10a. Then, the high temperature gas passage body 12a is joined to the heat transfer partition wall 11, and the heat of the high temperature gas passage 12 and the heat are uniformly transferred to the heat transfer partition wall 11 through the large number of heat transfer fins 22. Reference numeral 14a denotes an exhaust case in which the tip of the combustion chamber case 10 is extended to form an exhaust chamber 14b surrounding the upper and lower outlet sides of each high temperature gas passage 12 of the high temperature gas passage body 12a and the left and right sides of the high temperature gas passage body 12a. The exhaust path 14 is provided at the upper part. 15 is a heat transfer partition 1
1 is a heat exchange part that is thermally joined to the outer surface of 1, and is provided with a large number of longitudinal refrigerant passages 16. 17 is a heat exchange unit 1
5, an inlet header pipe provided at the lower end of 5, a heat exchange section 15
Is an outlet header pipe provided at the upper end of the inlet header pipe 19 and the refrigerant outlet pipe 20 are respectively connected to the refrigerant circuit, and the other end of the inlet header pipe 17 is bent downward to form an oil. A vent pipe 21 is provided. The inlet header pipe 17 and the outlet header pipe 18 are communicated with each other by a vertical refrigerant passage 16. Reference numeral 22 is a heat transfer fin that is in thermal contact with the inside of the heat transfer partition wall 11, and is a large number. The combustion chamber 10a is provided with a heat insulating material 23 inside the combustion case 10 for covering the remaining outer surface which is not in contact with the high temperature gas passage 12. In a part of the heat transfer partition wall 11 of the high temperature gas passage 12,
A heat transfer tool 24 is provided in close contact with the heat transfer partition wall 11, and a temperature thermistor 25 as an overheat temperature detecting means is attached to the heat exchange section 15 at a position opposed to the heat transfer tool 24.

【0012】本実施例では、伝熱具24、伝熱フィン2
2、伝熱隔壁11をアルミ材とし、伝熱具24は伝熱フ
ィン22に嵌合した状態で伝熱隔壁11にブレージング
ロー付けすることにより、伝熱隔壁11と伝熱フィン2
2に伝熱具24を密着して設けてある。この伝熱具24
のほぼ中央に伝熱隔壁11を貫通し、熱交換部15の冷
媒通路16の近傍に至る穴を設け、この穴に温度サーミ
スタ25を熱伝導材を塗布して挿入し固定具26で保持
している。温度サーミスタ25の温度感温部は、先端に
設けてあり冷媒通路16の近くに位置する。28は冷媒
温度検知手段であり、出口管20の外壁面に保持具27
で咬めて取り付けた温度サーミスタである。29は制御
部であり、温度サーミスタ24と温度サーミスタ28の
検出出力を入力と演算し、その結果の出力によりシステ
ムを制御するマイコン等で構成した制御部である。温度
サーミスタ28の検出出力によりバーナ8の燃焼量を制
御する。
In this embodiment, the heat transfer tool 24 and the heat transfer fin 2 are used.
2. The heat transfer partition wall 11 and the heat transfer fin 2 are made of aluminum, and the heat transfer tool 24 is brazed to the heat transfer partition wall 11 while being fitted to the heat transfer fins 22.
A heat transfer tool 24 is provided in close contact with the second member 2. This heat transfer tool 24
A hole that penetrates through the heat transfer partition wall 11 and reaches the vicinity of the refrigerant passage 16 of the heat exchange section 15 is provided at approximately the center of the heat transfer section 15. The temperature thermistor 25 is coated with a heat conductive material and is inserted and held by the fixture 26. ing. The temperature sensitive portion of the temperature thermistor 25 is provided at the tip and is located near the refrigerant passage 16. Reference numeral 28 is a refrigerant temperature detecting means, and a holder 27 is provided on the outer wall surface of the outlet pipe 20.
It is a temperature thermistor bitten and attached by. Reference numeral 29 denotes a control unit, which is a control unit configured by a microcomputer or the like for controlling the system by calculating the detection outputs of the temperature thermistor 24 and the temperature thermistor 28 as inputs and controlling the system by the output of the results. The combustion output of the burner 8 is controlled by the detection output of the temperature thermistor 28.

【0013】熱交換部の冷媒が減少した時の動作を図5
に示す。温度サーミスタ25の検出出力が一定値以上9
0℃である時は、過熱信号を制御部29が出力し、ま
た、制御部29にて、温度サーミスタ25の検出出力を
一定の時間毎(例えば30秒)に入力し、この前後の温
度出力の差を演算し、この値が所定の値以上(例えば1
0deg)である時は過熱信号を出力する。そして、冷
媒回路は、往管30から、復管31に至る間に放熱用の
熱交換器等(図示せず)を接続する。往管30、復管3
1は冷媒入口管19、冷媒出口管20と冷媒受タンク3
2を介して接続されている。
FIG. 5 shows the operation when the refrigerant in the heat exchange section is reduced.
Shown in. The detection output of the temperature thermistor 25 is a certain value or more 9
When the temperature is 0 ° C., the control unit 29 outputs an overheat signal, and the control unit 29 inputs the detection output of the temperature thermistor 25 at regular intervals (for example, 30 seconds), and outputs the temperature before and after this. Is calculated, and this value is greater than or equal to a predetermined value (for example, 1
When it is 0 deg), an overheat signal is output. Then, in the refrigerant circuit, a heat exchanger or the like (not shown) for heat radiation is connected between the outward pipe 30 and the return pipe 31. Outgoing pipe 30, return pipe 3
1 is a refrigerant inlet pipe 19, a refrigerant outlet pipe 20 and a refrigerant receiving tank 3
2 are connected.

【0014】上記構成において、燃料の供給装置により
供給した燃料をバーナ8で燃焼させ、燃焼室10aに発
生した高温ガスは燃焼ガス出口13から入口12bを通
り高温ガス通路体12aの上下に2分割した各々に流れ
て高温ガス通路12と伝熱フィン22の間の通路を通
り、高温ガス通路12の上の出口から排気室14bに流
れる高温ガスと、高温ガス通路12の下の出口から高温
ガス通路体12aの左右側を囲んだ排気室14bに流れ
る高温ガスは上の排気室14bで合流し排気路14に流
れる。
In the above structure, the fuel supplied by the fuel supply device is burned by the burner 8, and the high temperature gas generated in the combustion chamber 10a is divided into two parts, that is, from the combustion gas outlet 13 to the inlet 12b and above and below the high temperature gas passage body 12a. The hot gas flowing through each of the hot gas passages 12 and the heat transfer fins 22 and flowing from the upper outlet of the hot gas passage 12 to the exhaust chamber 14b, and the hot gas from the lower outlet of the hot gas passage 12 The high temperature gas flowing in the exhaust chamber 14b that surrounds the left and right sides of the passage body 12a merges in the upper exhaust chamber 14b and flows into the exhaust passage 14.

【0015】一方、冷媒入口管19を通って入口ヘッダ
ー管17に入った液冷媒は、熱交換部15の下部より多
数の縦方向の冷媒通路16に分流して流れ、高温ガス通
路12内を流れる燃焼ガスおよび伝熱フィン22から伝
熱隔壁11を介して熱を熱交換部15に伝熱する。した
がって、この熱交換部15の縦方向の冷媒通路16内の
冷媒を入口ヘッダー17に近い下部より十分に加熱す
る。そこで加熱された液状冷媒は気化蒸発を開始し液の
中に気泡を生じる気液二相状態となる。発生した気泡は
浮力効果で縦方向に設けた冷媒通路16内を下方から上
方に上昇する。特に燃焼ガスは燃焼室10aから燃焼ガ
ス出口13を出たのち高温ガス通路12より伝熱隔壁1
1を介し冷媒に伝熱するために、燃焼ガスの温度と流れ
が均一となり、熱交換部15の各部を均一に加熱できス
ムーズかつ均一に冷媒を蒸発させ、かつ冷媒を局部過熱
させることがなく無動力熱搬送を確実におこなわせ冷媒
の熱分解を生じない。そして、熱交換部15の冷媒通路
16を均一加熱できることにより冷媒通路16の各々の
流量が均等となり全体としての抵抗を低減させ、気泡上
昇力は強められ自然循環力が強くなり上部へ冷媒を送る
気泡ポンプ作用が発生する。
On the other hand, the liquid refrigerant that has passed through the refrigerant inlet pipe 19 and entered the inlet header pipe 17 is divided into a plurality of vertical refrigerant passages 16 from the lower portion of the heat exchange portion 15 and flows into the high temperature gas passage 12. Heat is transferred from the flowing combustion gas and the heat transfer fins 22 to the heat exchange section 15 via the heat transfer partition wall 11. Therefore, the refrigerant in the longitudinal refrigerant passage 16 of the heat exchange portion 15 is sufficiently heated from the lower portion near the inlet header 17. Then, the heated liquid refrigerant starts vaporization and evaporation, and becomes a gas-liquid two-phase state in which bubbles are generated in the liquid. Due to the buoyancy effect, the generated bubbles rise upward from below in the refrigerant passage 16 provided in the vertical direction. Particularly, the combustion gas leaves the combustion gas outlet 13 from the combustion chamber 10a, and then the heat transfer partition wall 1 from the high temperature gas passage 12.
Since the heat is transferred to the refrigerant via 1, the temperature and flow of the combustion gas are uniform, each part of the heat exchange section 15 can be uniformly heated, and the refrigerant is evaporated smoothly and uniformly, and the refrigerant is not locally overheated. The non-powered heat transfer is reliably performed, and the thermal decomposition of the refrigerant does not occur. Further, since the refrigerant passage 16 of the heat exchange section 15 can be uniformly heated, the flow rate of each of the refrigerant passages 16 becomes uniform and the resistance as a whole is reduced, the bubble rising force is strengthened and the natural circulation force is strengthened and the refrigerant is sent to the upper part. Bubble pump action occurs.

【0016】冷媒通路16の上端に達した冷媒は出口ヘ
ッダー管18に流入し冷媒出口管20より気液分離タン
ク32に流れ、分離したガス冷媒は往管30から放熱用
の熱交換器(図示せず)に向かって流出する。この熱交
換器の放熱量の変動に対して、冷媒の温度を温度センサ
28で常に検知し、一定の温度になるようにバーナ8の
燃焼量を制御部29でコントロールする。
The refrigerant reaching the upper end of the refrigerant passage 16 flows into the outlet header pipe 18 and flows from the refrigerant outlet pipe 20 into the gas-liquid separation tank 32, and the separated gas refrigerant is discharged from the outward pipe 30 for heat dissipation (see FIG. It flows out toward (not shown). The temperature of the refrigerant is constantly detected by the temperature sensor 28 in response to the fluctuation of the heat radiation amount of the heat exchanger, and the combustion amount of the burner 8 is controlled by the control unit 29 so that the temperature becomes constant.

【0017】また、高温ガス通路12を高温ガス通路体
12aで形成し、かつ伝熱隔壁11と密着した熱交換部
15で構成した二重壁構成により、前記内壁から伝熱フ
ィン22を通じて冷媒通路16に伝熱するため、伝熱効
率が上昇しまた多孔管構成の熱交換部15で構成した二
重壁構成による冷媒の燃焼ガス部への洩れ防止と高温の
燃焼室10aと冷媒通路16を高温ガス通路体12aで
完全に分離したため局部過熱による冷媒の熱分解、劣化
が生じ無く信頼性の高いシステムである。燃焼室10a
の高温ガス通路12と接しない燃焼室ケース10の内面
は断熱材23で覆い放熱を防止する。
Further, the high temperature gas passage 12 is formed by the high temperature gas passage body 12a, and the double wall structure is constituted by the heat exchange portion 15 which is in close contact with the heat transfer partition wall 11, so that the refrigerant passage is formed from the inner wall through the heat transfer fins 22. Since the heat is transferred to the heat exchanger 16, heat transfer efficiency is increased, and the double wall structure constituted by the heat exchange section 15 having a perforated pipe structure prevents the refrigerant from leaking to the combustion gas portion, and the high temperature combustion chamber 10a and the refrigerant passage 16 are heated to a high temperature. Since the gas passage body 12a is completely separated, the refrigerant is not thermally decomposed or deteriorated due to local overheating, and the system has high reliability. Combustion chamber 10a
The inner surface of the combustion chamber case 10 that is not in contact with the high temperature gas passage 12 is covered with a heat insulating material 23 to prevent heat radiation.

【0018】そして、通常運転中、冷媒は戻り管31、
冷媒入口管19から入口ヘッダ管17から熱交換部15
の冷媒通路部材16にはいり、熱源部であるバーナ8に
より熱交換部15で加熱され、高温冷媒ガスとなって冷
媒出口管20から往管30に流出し循環する。冷媒は蒸
発による潜熱で搬送するため、冷媒の圧力に応じて常に
一定温度であり、冷媒出口管20に設けた温度サーミス
タ28により検知した熱交換部15から出る冷媒温度と
熱交換部15に設けた温度サーミスタ25により検知し
た熱交換部の温度はほぼ同じ温度となり、熱交換部は熱
源部から加熱される熱量と冷媒に放出する熱量でバラン
スして一定の温度に平衡し保っている。
During normal operation, the refrigerant returns to the return pipe 31,
From the refrigerant inlet pipe 19 to the inlet header pipe 17 to the heat exchange section 15
The refrigerant passage member 16 is heated by the burner 8 which is a heat source in the heat exchanging portion 15, becomes high-temperature refrigerant gas, flows out from the refrigerant outlet pipe 20 to the outward pipe 30, and circulates. Since the refrigerant is transported by latent heat due to evaporation, the temperature is always constant according to the pressure of the refrigerant, and the temperature of the refrigerant discharged from the heat exchange section 15 detected by the temperature thermistor 28 provided in the refrigerant outlet pipe 20 and the heat exchange section 15 are provided. The temperature of the heat exchange section detected by the temperature thermistor 25 becomes almost the same temperature, and the heat exchange section balances the heat quantity heated from the heat source section and the heat quantity released to the refrigerant to keep a constant temperature.

【0019】異常時の熱交換部の温度を図5に示す。運
転中に冷媒が外部に洩れるなど充填量の減少あるいは循
環量が減少した時等、熱を冷媒に正常に放出できない
時、熱交換部15は、冷媒が潜熱変化から顕熱変化に移
行し、冷媒の温度が急激に温度上昇するため、過熱温度
検知手段の温度サーミスタ25は急速に上昇し応答遅れ
無く検知し、制御部は動作する。また、異常時として、
運転開始時に熱交換部の冷媒通路部材15に冷媒が無い
時は、同様に、バーナ8により熱交換部15が過熱され
温度サーミスタ25の温度出力は急激に上昇する。そこ
で、温度サーミスタ25の出力が一定値以上になると過
熱信号を制御部29に出力し、制御部29はただちに燃
焼を停止するように動作して機器の保護とシステムの動
作を正常化する。そして、別の異常時として、運転開始
時に熱交換部15に冷媒が有りかつ冷媒の循環が停止し
た時は、図5に示すように、最初、バーナ8により熱交
換部15が受けた熱はこの冷媒の蒸発潜熱に変わるた
め、過熱温度検知手段の温度サーミスタ25の出力の応
答が遅くなる。そこで、熱交換部15に有る冷媒が全て
蒸発するのを予知することにより、機器を停止する。す
なわち、バーナ8により加熱を始め熱交換部15の冷媒
が蒸発し始めると、同時に、熱交換部15に取付けた温
度サーミスタ25の出力は少しづつ上昇する。温度サー
ミスタ25の最初の温度上昇は、熱交換部15の各部分
の熱容量や周囲の温度の影響を受けてその温度上昇カー
ブは多少は変化する。温度サーミスタ25の出力を一定
の時間毎(30秒)に制御部29に入力し、この前後の
温度出力の差を演算する。そして、熱交換部15に有る
冷媒が全て蒸発して冷媒が液相状態で無くなり気相のみ
で顕熱による熱搬送を開始する時、温度サーミスタ25
の出力が急激に上昇するため、演算した前後の温度出力
の差の値が急激に大きくなる(10deg)。そこで、
熱交換部15の冷媒が完全に無くなる前にこの異常を予
知することが可能となり、図5に示す破線の温度とな
る。このため応答遅れによる熱交換部15の異常な高温
になることがなく、機器の保護とシステムの動作を正常
化する。前述の冷媒が無い時の運転開始時に上記制御を
行なうと図5に示す様に熱交換部15の熱ストレスを小
さくできる。それによって、冷媒加熱器に冷媒が不足し
た場合等冷媒が過熱する時、直ちに冷媒の温度を検知し
機器の保護とシステムの動作を正常化でき、冷媒の熱分
解、劣化が生じ無く信頼性の高いシステムにできる。
FIG. 5 shows the temperature of the heat exchange section at the time of abnormality. When heat cannot be normally released to the refrigerant, such as when the filling amount decreases or the circulation amount decreases such as the refrigerant leaking to the outside during operation, the heat exchange unit 15 causes the refrigerant to change from latent heat change to sensible heat change. Since the temperature of the refrigerant rapidly rises, the temperature thermistor 25 of the overheat temperature detecting means rapidly rises and detects without a response delay, and the control unit operates. Also, in the event of an abnormality,
Similarly, when there is no refrigerant in the refrigerant passage member 15 of the heat exchange section at the start of operation, the heat exchange section 15 is overheated by the burner 8 and the temperature output of the temperature thermistor 25 rapidly increases. Therefore, when the output of the temperature thermistor 25 exceeds a certain value, an overheat signal is output to the control unit 29, and the control unit 29 operates so as to immediately stop combustion, thereby protecting the equipment and normalizing the operation of the system. Then, as another abnormal condition, when the heat exchange section 15 has a refrigerant at the start of operation and the circulation of the refrigerant is stopped, as shown in FIG. 5, the heat received by the heat exchange section 15 by the burner 8 is initially Since it changes to the latent heat of vaporization of the refrigerant, the response of the output of the temperature thermistor 25 of the overheat temperature detecting means becomes slow. Therefore, the equipment is stopped by predicting that all the refrigerant in the heat exchange section 15 will evaporate. That is, when heating is started by the burner 8 and the refrigerant in the heat exchange section 15 begins to evaporate, at the same time, the output of the temperature thermistor 25 attached to the heat exchange section 15 gradually increases. The initial temperature rise of the temperature thermistor 25 is affected by the heat capacity of each part of the heat exchange section 15 and the ambient temperature, and the temperature rise curve changes slightly. The output of the temperature thermistor 25 is input to the control unit 29 at regular intervals (30 seconds), and the difference in temperature output before and after this is calculated. Then, when all the refrigerant in the heat exchange section 15 evaporates and the refrigerant disappears in the liquid phase state and heat transfer by sensible heat is started only in the gas phase, the temperature thermistor 25
Since the output of 1 increases sharply, the value of the difference between the temperature output before and after the calculation increases rapidly (10 deg). Therefore,
This abnormality can be predicted before the refrigerant in the heat exchange section 15 is completely consumed, and the temperature becomes the temperature shown by the broken line in FIG. Therefore, the heat exchange section 15 does not become abnormally high temperature due to the response delay, and the equipment is protected and the system operation is normalized. If the above control is performed at the start of operation when there is no refrigerant as described above, the heat stress of the heat exchange section 15 can be reduced as shown in FIG. As a result, when the refrigerant overheats, such as when the refrigerant heater runs short, the temperature of the refrigerant can be immediately detected to protect the equipment and normalize the operation of the system, and thermal decomposition and deterioration of the refrigerant do not occur and reliability is improved. It can be a high system.

【0020】また、バーナ8の加熱する入力量を、加熱
開始からすくなくとも、一定時間は一定の入力量とする
ことにより加熱量を一定に保ち、バーナ8により加熱を
始め熱交換部15の冷媒が蒸発し始める時に、熱交換部
15の温度サーミスタ25の出力の温度上昇は、安定し
た温度上昇カーブとなり、温度サーミスタ25の出力差
による判定する所定の値を小さく設定しても誤動作が生
じない。このため、より早く異常を検知することが可能
となり、機器の異常による過熱をより少なくなり、熱交
換器、冷媒等に加わる熱的ストレスを小さく、耐久的性
に信頼性が向上する。
The heating input amount of the burner 8 is kept constant by keeping the input amount constant for a certain period of time even if the input amount to be heated is at least from the start of heating. When vaporization starts, the temperature rise of the output of the temperature thermistor 25 of the heat exchange section 15 becomes a stable temperature rise curve, and malfunction does not occur even if the predetermined value determined by the output difference of the temperature thermistor 25 is set small. Therefore, it becomes possible to detect an abnormality more quickly, less overheat due to an abnormality of the device, less thermal stress applied to the heat exchanger, the refrigerant, etc., and reliability is improved in durability.

【0021】[0021]

【発明の効果】以上説明したように本発明は、冷媒入口
部と冷媒出口部に連通した熱交換部と、前記熱交換部を
加熱する熱源部と、前記熱交換部に設けた過熱温度検知
手段と、前記過熱温度検知手段の温度出力が一定値以上
である時は過熱信号を出力する制御部を備え、前記制御
部は前記過熱温度検知手段の温度出力を一定の時間毎に
入力し、この前後の温度出力の差を演算し、この値が所
定の値以上である時は過熱信号を出力するものであるか
ら、次の効果が得られる。 (1)運転中に冷媒が外部に洩れるあるいは循環量が減
少した時は、過熱温度検知手段の温度出力が一定値以上
になると過熱信号を制御部から出力することにより、機
器の保護とシステムの動作を正常化できる。また、運転
開始時に熱交換部に冷媒が有り、かつ冷媒の循環が停止
した時も、応答遅れなく直ちに冷媒の温度を検知し機器
の保護とシステムの動作を正常化でき、冷媒の熱分解、
劣化が生じ無く信頼性の高いシステムにできる。 (2)制御部は熱源部の加熱するための入力量を、加熱
開始らかすくなくとも、一定時間は一定の入力量とする
ことにより、冷媒加熱温度検知手段の出力の所定の値を
高精度に設定でき、より早く異常を検知できる。
As described above, according to the present invention, the heat exchange section communicating with the refrigerant inlet section and the refrigerant outlet section, the heat source section for heating the heat exchange section, and the overheat temperature detection provided in the heat exchange section are provided. And a control unit that outputs an overheat signal when the temperature output of the overheat temperature detection unit is equal to or higher than a constant value, and the control unit inputs the temperature output of the overheat temperature detection unit at constant time intervals, The difference between the temperature outputs before and after this is calculated, and when this value is equal to or greater than a predetermined value, an overheat signal is output, so that the following effects can be obtained. (1) When the refrigerant leaks to the outside during operation or the circulation amount decreases, when the temperature output of the overheat temperature detecting means exceeds a certain value, an overheat signal is output from the control unit to protect the equipment and prevent the system from operating. The operation can be normalized. Also, when there is a refrigerant in the heat exchange section at the start of operation, and even when the circulation of the refrigerant is stopped, the temperature of the refrigerant can be immediately detected without delay in response to normalize the protection of the equipment and the operation of the system, thermal decomposition of the refrigerant,
A highly reliable system can be obtained without deterioration. (2) The control unit sets the predetermined value of the output of the refrigerant heating temperature detection unit with high accuracy by setting the input amount for heating the heat source unit to a constant input amount for a certain period of time even if the heating is not started. It can be set and the abnormality can be detected earlier.

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

【図1】本発明の一実施例におけるす熱交換器の要部断
面の斜視図
FIG. 1 is a perspective view of a cross section of a main part of a chair heat exchanger according to an embodiment of the present invention.

【図2】同熱交換器の熱交換部部分の断面図FIG. 2 is a cross-sectional view of a heat exchange part of the heat exchanger.

【図3】従来の冷媒加熱機の回路構成図FIG. 3 is a circuit configuration diagram of a conventional refrigerant heater.

【図4】従来の冷媒加熱機の外観斜視図FIG. 4 is an external perspective view of a conventional refrigerant heater.

【図5】熱交換器の冷媒が減少した時の温度変化図FIG. 5 is a temperature change diagram when the refrigerant in the heat exchanger decreases.

【符号の説明】[Explanation of symbols]

8 バーナ(熱源部) 15 熱交換部 17 入口ヘッダ管(冷媒入口部) 18 出口ヘッダ管(冷媒出口部) 25 過熱温度検知手段 29 制御部 8 burner (heat source part) 15 heat exchange part 17 inlet header pipe (refrigerant inlet part) 18 outlet header pipe (refrigerant outlet part) 25 overheat temperature detecting means 29 control part

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】冷媒入口部と冷媒出口部に連通した熱交換
部と、前記熱交換部を加熱する熱源部と、前記熱交換部
に設けた過熱温度検知手段と、前記過熱温度検知手段の
温度出力が一定値以上である時は過熱信号を出力する制
御部を備え、前記制御部は前記過熱温度検知手段の温度
出力を一定の時間毎に入力し、この前後の温度出力の差
を演算し、この値が所定の値以上である時は過熱信号を
出力する冷媒加熱器の制御装置。
1. A heat exchange section communicating with a refrigerant inlet section and a refrigerant outlet section, a heat source section for heating the heat exchange section, an overheat temperature detection means provided in the heat exchange section, and an overheat temperature detection means. A control unit that outputs an overheat signal when the temperature output is equal to or higher than a certain value is provided, and the control unit inputs the temperature output of the overheat temperature detecting means at regular time intervals and calculates a difference between the temperature output before and after the temperature output. The control device for the refrigerant heater, which outputs an overheat signal when this value is equal to or greater than a predetermined value.
【請求項2】熱源部の加熱するための入力量を、加熱開
始からすくなくとも、一定時間は一定の入力量とした請
求項1記載の冷媒加熱器の制御装置。
2. The control device for a refrigerant heater according to claim 1, wherein the input amount for heating the heat source unit is a constant input amount for a certain period of time at least from the start of heating.
JP4145369A 1992-06-05 1992-06-05 Refrigerant heater controller Expired - Lifetime JP2921264B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4145369A JP2921264B2 (en) 1992-06-05 1992-06-05 Refrigerant heater controller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4145369A JP2921264B2 (en) 1992-06-05 1992-06-05 Refrigerant heater controller

Publications (2)

Publication Number Publication Date
JPH05340550A true JPH05340550A (en) 1993-12-21
JP2921264B2 JP2921264B2 (en) 1999-07-19

Family

ID=15383630

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4145369A Expired - Lifetime JP2921264B2 (en) 1992-06-05 1992-06-05 Refrigerant heater controller

Country Status (1)

Country Link
JP (1) JP2921264B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013179466A1 (en) * 2012-05-31 2013-12-05 トヨタ自動車株式会社 Exhaust-heat recovery apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013179466A1 (en) * 2012-05-31 2013-12-05 トヨタ自動車株式会社 Exhaust-heat recovery apparatus
CN104350252A (en) * 2012-05-31 2015-02-11 丰田自动车株式会社 Exhaust-heat recovery apparatus
JP5835479B2 (en) * 2012-05-31 2015-12-24 トヨタ自動車株式会社 Exhaust heat recovery device

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