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JPH0631717B2 - Method and apparatus for controlling low temperature fluid in heat exchanger - Google Patents

Method and apparatus for controlling low temperature fluid in heat exchanger

Info

Publication number
JPH0631717B2
JPH0631717B2 JP59271904A JP27190484A JPH0631717B2 JP H0631717 B2 JPH0631717 B2 JP H0631717B2 JP 59271904 A JP59271904 A JP 59271904A JP 27190484 A JP27190484 A JP 27190484A JP H0631717 B2 JPH0631717 B2 JP H0631717B2
Authority
JP
Japan
Prior art keywords
heat exchanger
temperature
temperature fluid
engine
low
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP59271904A
Other languages
Japanese (ja)
Other versions
JPS61149796A (en
Inventor
秀樹 中島
晃 吉田
啓友 綱島
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.)
TSUCHA SEISAKUSHO KK
Original Assignee
TSUCHA SEISAKUSHO KK
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 TSUCHA SEISAKUSHO KK filed Critical TSUCHA SEISAKUSHO KK
Priority to JP59271904A priority Critical patent/JPH0631717B2/en
Publication of JPS61149796A publication Critical patent/JPS61149796A/en
Publication of JPH0631717B2 publication Critical patent/JPH0631717B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F27/00Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、熱交換器特に内燃機関の排気ガスから熱回
収を行なう熱交換器の低温流体制御方法及びその装置に
関連する。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat exchanger, and more particularly to a cryogenic fluid control method and apparatus for a heat exchanger that recovers heat from exhaust gas of an internal combustion engine.

従来技術 従来の熱交換器は,例えば第4図に示されるように、内
燃機関の排気ガスから熱を回収するため使用される。即
ち熱交換器10は第1通路となる管12によりガスエン
ジン11に接続され、その間に触媒コンバータ13が配
置される。又、熱交換器10の第1通路出口側には消音
器14が接続される。ガスエンジン11は点線16で示
されるように、コンプレツサ15に作動連結され、コン
プレツサ15は管17と18を通じて空調器等の冷媒を
圧縮する。ガスエンジン11の冷却水は管19を通り貯
湯槽20に送られ、そこで管21と22を通る他の流体
と熱交換が行なわれる。冷却水は貯湯槽20から管23
を通りポンプ24、管25と26を経て再びガスエンジ
ン11に送られる。管25の冷却水は、又、管27を通
り熱交換器10に送られる。
PRIOR ART A conventional heat exchanger is used to recover heat from the exhaust gas of an internal combustion engine, for example as shown in FIG. That is, the heat exchanger 10 is connected to the gas engine 11 by the pipe 12 serving as the first passage, and the catalytic converter 13 is arranged therebetween. Further, a silencer 14 is connected to the heat exchanger 10 on the outlet side of the first passage. The gas engine 11 is operatively connected to a compressor 15, as indicated by the dotted line 16, which compresses refrigerant, such as air conditioners, through tubes 17 and 18. The cooling water of the gas engine 11 is sent to the hot water storage tank 20 through the pipe 19 and exchanges heat with other fluids passing through the pipes 21 and 22. The cooling water is supplied from the hot water storage tank 20 to the pipe 23.
Through the pump 24 and the pipes 25 and 26, and is again sent to the gas engine 11. The cooling water of the pipe 25 is also sent to the heat exchanger 10 through the pipe 27.

発明が解決しようとする問題点 第4図の装置では、高温流体であるガスエンジン11の
排気ガスは管12により触媒コンバータ13、熱交換器
10及び消音器14を通じて外部に放出される。熱交換
器10では管12を通る高温の排気ガスの熱は、管27
を通る冷却水により回収される。この装置では、熱交換
器10を通過する排気ガスが一般に150゜〜200℃以下に
なると排気ガス中に含まれる水蒸気が凝縮水となる凝結
現象が発生する。即ち、熱交換器内壁により排気ガスは
露点以下の温度に冷却される。排気ガス中には水蒸気、
硫黄又は窒素が含まれ、この冷却により水蒸気圧力が飽
和蒸気圧以下に減圧されるので熱交換器10内では内壁
に水蒸気が凝結し硫酸又は硝酸等の腐食性成分を含む凝
縮水が生成される。
Problems to be Solved by the Invention In the apparatus shown in FIG. 4, the exhaust gas of the gas engine 11 which is a high temperature fluid is discharged to the outside through the pipe 12 through the catalytic converter 13, the heat exchanger 10 and the silencer 14. In the heat exchanger 10, the heat of the hot exhaust gas passing through the pipe 12 is
Recovered by cooling water passing through. In this device, when the exhaust gas passing through the heat exchanger 10 is generally below 150 ° to 200 ° C, a condensation phenomenon occurs in which the water vapor contained in the exhaust gas becomes condensed water. That is, the exhaust gas is cooled to a temperature below the dew point by the inner wall of the heat exchanger. Water vapor in the exhaust gas,
Since sulfur or nitrogen is contained and the steam pressure is reduced to a saturated steam pressure or less by this cooling, steam is condensed on the inner wall of the heat exchanger 10 to generate condensed water containing corrosive components such as sulfuric acid or nitric acid. .

詳述すれば、ガスエンジン11には、都市ガス又はLP
G等のガス燃料が用いられる。これらの燃料はSH基で構
成されるメルカプタンを含み、このメルカプタンは燃焼
時に水蒸気と反応して硫酸を生ずる。又、燃焼時に酸素
を与えるため供給される空気中には、窒素が含まれ、こ
の窒素は、水蒸気と反応して硝酸となる。前記硫酸又は
硝酸は、弱酸性ながら熱交換器内の温度が高いため、活
性に富み、このため熱交換器内面を腐食する時間当りの
腐食減量は大きい。
More specifically, the gas engine 11 includes city gas or LP.
Gas fuel such as G is used. These fuels include mercaptans composed of SH groups, which react with steam to produce sulfuric acid during combustion. Further, the air supplied to give oxygen during combustion contains nitrogen, and this nitrogen reacts with water vapor to form nitric acid. Although the sulfuric acid or nitric acid is weakly acidic, the temperature inside the heat exchanger is high, so it is highly active, and therefore the corrosion weight loss per unit time that corrodes the inner surface of the heat exchanger is large.

そこで腐食性成分を含む凝縮水を生じない熱交換器を開
発する必要が生ずる。従来の熱交換器では、低温流体の
出口温度を測定して低温流体の流量を制御する方法が提
案されたが、この方法では、熱交換器の再稼動時に低温
流体が充分に冷却されていないと流量制御装置が所期の
機能を行わないため、上記凝縮水が発生する欠点があっ
た。
Therefore, it becomes necessary to develop a heat exchanger that does not generate condensed water containing corrosive components. In the conventional heat exchanger, a method of measuring the outlet temperature of the cryogenic fluid and controlling the flow rate of the cryogenic fluid has been proposed, but in this method, the cryogenic fluid is not sufficiently cooled when the heat exchanger is restarted. Since the flow rate control device does not perform the intended function, there is a drawback that the condensed water is generated.

この発明は、従来の熱交換器の構造を変更せず実施でき
る熱交換器の低温流体制御方法及びその装置を提供する
ことを目的とする。
It is an object of the present invention to provide a low temperature fluid control method for a heat exchanger and an apparatus thereof that can be implemented without changing the structure of a conventional heat exchanger.

発明の概要 この発明による熱交換器の低温流体制御方法は、機関か
ら排出される排気ガスと、循環低温流体との間で熱交換
する装置の低温流体制御方法において、循環低温流体の
一部を、機関へ流入させる前に分流させ、これを機関の
排気管に設けた熱交換器に流入させ、排気ガスの温度が
所定値以上になるように上記分流させる低温流体の流量
を制御させるようにしたものであり、また、本発明の装
置は、機関と貯湯槽との間に、ポンプを介して、循環低
温流体路を設け、機関の排気管に熱交換器を設け、機関
とポンプとの間の循環低温流体路と機関と貯湯槽との間
の循環低温流体路を管で連結し、該管の途中に上記熱交
換器を介在させるとともに排気ガス温度に応じて該管内
を流通する低温流体量を制御する流量制御装置を設けた
ものである。
SUMMARY OF THE INVENTION A cryogenic fluid control method for a heat exchanger according to the present invention is a cryogenic fluid control method for a device for exchanging heat between exhaust gas discharged from an engine and a circulating cryogenic fluid, wherein a part of the circulating cryogenic fluid is , The flow is divided before it is made to flow into the engine, it is made to flow into a heat exchanger provided in the exhaust pipe of the engine, and the flow rate of the low-temperature fluid is divided so that the temperature of the exhaust gas becomes a predetermined value or more. In addition, the device of the present invention provides a circulating low temperature fluid path between the engine and the hot water storage tank via a pump, and provides a heat exchanger in the exhaust pipe of the engine to connect the engine and the pump. A low temperature fluid circulating between the engine and the hot water storage tank is connected by a pipe, the heat exchanger is interposed in the middle of the pipe, and the low temperature fluid flows in the pipe in accordance with the exhaust gas temperature. With a flow control device that controls the amount of fluid is there.

実施例 以下この発明の実施例を図面について説明する。前記第
4図及び第1図ないし第3図では、同一部分には、同一
符号を付する。
Embodiments Embodiments of the present invention will be described below with reference to the drawings. In FIG. 4 and FIGS. 1 to 3, the same parts are designated by the same reference numerals.

この発明の実施例を示す第1図は、基本的には前記第4
図に示される装置と同一の装置を有する。従つて同一装
置については、説明を省略する。
FIG. 1 showing an embodiment of the present invention is basically the same as the fourth embodiment.
It has the same device as that shown in the figure. Therefore, description of the same device is omitted.

この発明では、ガスエンジン11や内燃機関などの機関と
貯湯槽20との間がポンプ24を介して管19、23、25により
連結されて循環低温流体路が形成されており、ポンプ24
と熱交換器10とを接続する管27に流量制御装置28が
取付けられ、又、例えば機関の排気管に設けられた熱交
換器10の高温流体の出口部12aに、感温素子31が取付
けられる。感温素子31は、高温流体の温度を電気信号
に変換する温度センサ30の1部で、サーミスタ、特に
負特性サーミスタ(NTCサーミスタ)又はクロメル−
アルメル(CA)熱電対等種々の側温素子が使用される。温
度センサ30は、感温素子31からの信号を高温流体の
出口温度に対応する信号に変換し、これを制御回路32
に供給する。感温素子31の取付け位置は、上記出口部
12a以外でもよい。例えば入口部又は入口と出口の中間
部に取付けてもよいが、いずれにしても感温素子31の
出力は、高温流体温度に対し一定の関係が与えられ、高
温流体温度を表わすレベルを含む。制御回路32は、温
度センサ30の信号を受け出口温度のレベルを電気的に
決定し、このレベルに対応する駆動信号を発生する。こ
の駆動信号は、流量制御装置28に送出され、流量制御
装置28は、上記駆動信号に対応する流量で低温流体を
管29を通り熱交換器10に供給する。即ち、熱交換器
10から排出される排気ガスの出口温度が例えば約150゜
〜200℃以上のとき、流量制御装置28は、出口温度に
比例した流量で低温流体を熱交換器10へ供給する。換
言すれば、出口温度が高いときは、熱交換器10への低温
流体の流量は多く、逆に出口温度が低いときはこの流量
は少ない。しかし、ガスエンジンの性能上、管12を通
る排気ガスの温度上限及び最大吐出流量が設定されるた
め、排気ガスの出口温度が、一定温度例えば400℃から
上限温度までは、流量制御装置28は、一定の最大流量
で低温流体を熱交換器10へ供給することもある。逆
に、排気ガスの出口温度が約120℃以下の下限温度のと
きは、制御装置32は駆動信号を生ずることがなく流量
制御装置28の作動は停止される。上記排気ガスの上限
及び下限温度は、ガスエンジンの性能に応じて決定され
る。これらの上限及び下限温度は、感温素子31が熱交
換器10の入口部に取付けられたときは、出口部の場合
より、非常に高くなる。
In the present invention, the engine such as the gas engine 11 or the internal combustion engine and the hot water storage tank 20 are connected by the pipes 19, 23 and 25 via the pump 24 to form a circulating low temperature fluid passage.
A flow rate control device 28 is attached to a pipe 27 that connects the heat exchanger 10 with the heat exchanger 10, and a temperature sensitive element 31 is attached to an outlet portion 12a of the high temperature fluid of the heat exchanger 10 provided in the exhaust pipe of the engine, for example. To be The temperature sensitive element 31 is a part of the temperature sensor 30 that converts the temperature of a high temperature fluid into an electric signal, and is a thermistor, particularly a negative characteristic thermistor (NTC thermistor) or chromel-.
Various side temperature devices such as alumel (CA) thermocouples are used. The temperature sensor 30 converts the signal from the temperature sensitive element 31 into a signal corresponding to the outlet temperature of the high temperature fluid, and converts this into a control circuit 32.
Supply to. The temperature sensitive element 31 is mounted at the above-mentioned outlet portion.
It may be other than 12a. For example, the output of the temperature sensing element 31 may be attached to the inlet portion or an intermediate portion between the inlet and the outlet, but in any case, the output of the temperature sensitive element 31 has a constant relationship with the hot fluid temperature and includes a level representing the hot fluid temperature. The control circuit 32 receives the signal from the temperature sensor 30 and electrically determines the level of the outlet temperature, and generates a drive signal corresponding to this level. This drive signal is sent to the flow rate control device 28, and the flow rate control device 28 supplies the low temperature fluid to the heat exchanger 10 through the pipe 29 at a flow rate corresponding to the drive signal. That is, when the outlet temperature of the exhaust gas discharged from the heat exchanger 10 is, for example, about 150 ° to 200 ° C. or higher, the flow rate control device 28 supplies the low temperature fluid to the heat exchanger 10 at a flow rate proportional to the outlet temperature. . In other words, when the outlet temperature is high, the flow rate of the low temperature fluid to the heat exchanger 10 is high, and conversely, when the outlet temperature is low, this flow rate is low. However, due to the performance of the gas engine, the temperature upper limit and the maximum discharge flow rate of the exhaust gas passing through the pipe 12 are set, so that the flow rate control device 28 does not operate until the exhaust gas outlet temperature reaches a constant temperature, for example, 400 ° C. to the upper limit temperature. The low temperature fluid may be supplied to the heat exchanger 10 at a constant maximum flow rate. On the contrary, when the outlet temperature of the exhaust gas is the lower limit temperature of about 120 ° C. or less, the control device 32 does not generate a drive signal and the operation of the flow rate control device 28 is stopped. The upper limit and the lower limit temperature of the exhaust gas are determined according to the performance of the gas engine. These upper and lower temperatures are much higher when the temperature sensitive element 31 is attached to the inlet of the heat exchanger 10 than when it is at the outlet.

制御回路32及び流量制御装置28の詳細の1例は、第
2図に示される。制御回路32は、温度センサ30に接
続された増幅器33と、増幅器33の出力を受けこの出力
が所定レベル以上か否かを判断する差動増幅器34とを
有する。差動増幅器34は、増幅器33に接続された非
反転入力端子40と、定電圧電源36に接続された反転
入力端子41を有する。
An example of the details of the control circuit 32 and the flow control device 28 is shown in FIG. The control circuit 32 includes an amplifier 33 connected to the temperature sensor 30, and a differential amplifier 34 that receives the output of the amplifier 33 and determines whether the output is equal to or higher than a predetermined level. The differential amplifier 34 has a non-inverting input terminal 40 connected to the amplifier 33 and an inverting input terminal 41 connected to the constant voltage power supply 36.

流量制御装置28は、差動増幅器34の駆動信号を受け
るトルクモータ35及びトルクモータ35のフラツパ(図
示せず)で作動される可変流量制御弁であるサーボ弁28
aを有する。上記トルクモータ35とサーボ弁28aは、公
知型式の装置を使用できる。
The flow rate control device 28 is a servo valve 28 that is a variable flow rate control valve that is operated by a torque motor 35 that receives a drive signal of a differential amplifier 34 and a flapper (not shown) of the torque motor 35.
have a. For the torque motor 35 and the servo valve 28a, known type devices can be used.

第2図の装置の作動について説明すると、差動増幅器3
4は、温度センサ30からの出力が電源36より高いか
否かを判断し、この出力が高いときには、この出力に対
応する駆動信号を生じトルクモータ35のフラツパを対
応位置まで移動させ、サーボ弁28aの開放量を増大す
る。従つて、ポンプ24から管25,27、サーボ弁28
a及び管29を通る低温流体の流量は増加する。高温流体
の温度が高いが上限温度に満たないときは温度センサ3
0から非反転入力端子40に与えられる出力はその最大
レベルよりは低いが、電源36より高いので、差動増幅
器34は、比較的低レベルの駆動信号を生ずる。このた
めトルクモータ35のフラツパ移動量は小さく、サーボ
弁28aの開放量も小さい。従つてサーボ弁28aを通る低温
流体流量は少ない。
The operation of the apparatus shown in FIG. 2 will be described. The differential amplifier 3
Reference numeral 4 determines whether or not the output from the temperature sensor 30 is higher than that of the power supply 36. When this output is high, a drive signal corresponding to this output is generated to move the flapper of the torque motor 35 to the corresponding position, and the servo valve Increase the opening amount of 28a. Therefore, from the pump 24 to the pipes 25 and 27, the servo valve 28
The flow rate of cryogenic fluid through a and tube 29 is increased. If the temperature of the high temperature fluid is high but the temperature does not reach the upper limit temperature, the temperature sensor 3
The output provided from 0 to the non-inverting input terminal 40 is below its maximum level but above the power supply 36 so that the differential amplifier 34 produces a relatively low level drive signal. Therefore, the amount of movement of the flapper of the torque motor 35 is small, and the amount of opening of the servo valve 28a is also small. Therefore, the low temperature fluid flow rate through the servo valve 28a is low.

排気ガスの出口温度が一定温度以下の場合は、温度セン
サ30から非反転入力端子40に与えられる信号は電源
36より低い。このため、差動増幅器34は駆動信号を
生じないので、トルクモータ35は作動せず、サーボ弁
28aも開放されない。
When the exhaust gas outlet temperature is equal to or lower than a certain temperature, the signal supplied from the temperature sensor 30 to the non-inverting input terminal 40 is lower than that of the power source 36. Therefore, since the differential amplifier 34 does not generate a drive signal, the torque motor 35 does not operate and the servo valve
28a is not released either.

第3図は、流量制御装置28の他の実施例を示す。流量
制御装置28は、差動増幅器34の出力を受ける加減速
度モータ37と、このモータ37で駆動されるポンプ28
bとを有する。ポンプ28bは、管27と29とに接続され
るが管27を貯湯槽20に直接接続してもよい。モータ
37は、排気ガスの温度に対応する差動増幅器34の駆
動信号で作動され、モータ37に作動連結されたポンプ
28bは、上記温度に対応する流量で低温流体を熱交換器
10に供給する。
FIG. 3 shows another embodiment of the flow rate control device 28. The flow rate control device 28 includes an acceleration / deceleration motor 37 that receives the output of the differential amplifier 34 and a pump 28 that is driven by the motor 37.
with b and. The pump 28b is connected to the pipes 27 and 29, but the pipe 27 may be directly connected to the hot water storage tank 20. The motor 37 is driven by a drive signal of the differential amplifier 34 corresponding to the temperature of the exhaust gas, and is a pump operatively connected to the motor 37.
28b supplies the low temperature fluid to the heat exchanger 10 at a flow rate corresponding to the above temperature.

上記低温流体制御装置は、ガスエンジンの排気ガスから
熱を回収する熱交換器の例として説明されたが、この発
明の実施例は、種々の変更が可能である。例えば、この
発明は車両に取付けられた内燃機関の排気ガスから熱を
回収する熱交換器にも実施できる。制御回路32では、
差動増幅器34の代りにA/D変換器を接続し、一定時間毎
に駆動信号をデイジタルで発生し、このデイジタル信号
トルクモータ35又は加減速度モータ37を作動するこ
ともよい。又、差動増幅器とA/D変換器を組合わせてこ
れらを作動することもできる。
The cryogenic fluid control device has been described as an example of the heat exchanger that recovers heat from the exhaust gas of the gas engine, but the embodiment of the present invention can be variously modified. For example, the present invention can be implemented in a heat exchanger that recovers heat from the exhaust gas of an internal combustion engine mounted on a vehicle. In the control circuit 32,
It is also possible to connect an A / D converter instead of the differential amplifier 34, generate a drive signal digitally at regular time intervals, and operate the digital signal torque motor 35 or the acceleration / deceleration motor 37. It is also possible to operate these by combining a differential amplifier and an A / D converter.

発明の効果 以上のように、本発明の方法および装置によれば循環低
温流体は所定温度以上に制御されるとともに、その一部
が機関に戻される前に分流されて熱交換器により加熱さ
れ、また残部が加熱されずに機関に流入されるようにな
っているから、機関の冷却作用を損うことなく、熱交換
器内に腐食の原因となる凝縮水が生成するのを防止す
る。
As described above, according to the method and apparatus of the present invention, the circulating low temperature fluid is controlled to a predetermined temperature or higher, and a part of the low temperature fluid is divided and heated by the heat exchanger before being returned to the engine, Further, since the remaining portion is not heated but is allowed to flow into the engine, it prevents generation of condensed water causing corrosion in the heat exchanger without impairing the cooling action of the engine.

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

第1図は、この発明による熱交換器の低温流体制御装置
のブロツク図;第2図は第1図の装置に使用する制御回
路及び流量制御装置の詳細を示すブロツク図;第3図は
第2図と同様の他の実施例を示すブロツク図で;第4図
は従来の低温流体制御装置のブロツク図を示す。 10……熱交換器、28……流量制御装置、30……温度セン
サ、32……制御回路
FIG. 1 is a block diagram of a cryogenic fluid control device for a heat exchanger according to the present invention; FIG. 2 is a block diagram showing details of a control circuit and a flow rate control device used in the device of FIG. 1; FIG. 4 is a block diagram showing another embodiment similar to FIG. 2; FIG. 4 shows a block diagram of a conventional cryogenic fluid control device. 10: Heat exchanger, 28: Flow control device, 30: Temperature sensor, 32: Control circuit

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】機関から排出される排気ガスと、循環低温
流体との間で熱交換する装置の低温流体制御方法におい
て、循環低温流体の一部を、機関へ流入させる前に分流
させ、これを機関の排気管に設けた熱交換器に流入さ
せ、排気ガスの温度が所定値以上になるように上記分流
させる低温流体の流量を制御させるようにした熱交換器
の低温流体制御方法。
1. A low-temperature fluid control method for an apparatus for exchanging heat between an exhaust gas discharged from an engine and a circulating low-temperature fluid, wherein a part of the circulating low-temperature fluid is split before flowing into an engine. A method for controlling a low temperature fluid in a heat exchanger, wherein the flow rate of the low temperature fluid is controlled so that the temperature of the exhaust gas is equal to or higher than a predetermined value.
【請求項2】機関と貯湯槽との間にポンプを介して、循
環低温流体路を設け、機関の排気管に熱交換器を設け、
機関とポンプとの間の循環低温流体路と、機関と貯湯槽
との間の循環低温流体路とを管で連結し、該管の途中に
上記熱交換器を介在させるとともに排気ガス温度に応じ
て該管内を流通する低温流体の流量を制御する流量制御
装置を設けて成る熱交換器の低温流体制御装置。
2. A circulating low-temperature fluid path is provided between the engine and the hot water storage tank via a pump, and a heat exchanger is provided in the exhaust pipe of the engine.
A circulating low-temperature fluid path between the engine and the pump and a circulating low-temperature fluid path between the engine and the hot water tank are connected by a pipe, and the heat exchanger is interposed in the middle of the pipe and the temperature of the exhaust gas is adjusted according to the exhaust gas temperature. A low temperature fluid control device for a heat exchanger, which is provided with a flow rate control device for controlling the flow rate of the low temperature fluid flowing in the pipe.
JP59271904A 1984-12-25 1984-12-25 Method and apparatus for controlling low temperature fluid in heat exchanger Expired - Lifetime JPH0631717B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59271904A JPH0631717B2 (en) 1984-12-25 1984-12-25 Method and apparatus for controlling low temperature fluid in heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59271904A JPH0631717B2 (en) 1984-12-25 1984-12-25 Method and apparatus for controlling low temperature fluid in heat exchanger

Publications (2)

Publication Number Publication Date
JPS61149796A JPS61149796A (en) 1986-07-08
JPH0631717B2 true JPH0631717B2 (en) 1994-04-27

Family

ID=17506506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59271904A Expired - Lifetime JPH0631717B2 (en) 1984-12-25 1984-12-25 Method and apparatus for controlling low temperature fluid in heat exchanger

Country Status (1)

Country Link
JP (1) JPH0631717B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009031557A1 (en) 2009-03-02 2010-09-09 Sms Siemag Ag Energy recovery in hot strip mills by converting the cooling heat of the continuous casting plant and the residual heat of slabs and coils into electrical energy or other use of the captured process heat

Also Published As

Publication number Publication date
JPS61149796A (en) 1986-07-08

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