JPH01117909A - Cooling water controller of heat-exchanger - Google Patents
Cooling water controller of heat-exchangerInfo
- Publication number
- JPH01117909A JPH01117909A JP62274668A JP27466887A JPH01117909A JP H01117909 A JPH01117909 A JP H01117909A JP 62274668 A JP62274668 A JP 62274668A JP 27466887 A JP27466887 A JP 27466887A JP H01117909 A JPH01117909 A JP H01117909A
- Authority
- JP
- Japan
- Prior art keywords
- cooling water
- flow rate
- temperature
- humidity
- heat exchanger
- 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
Links
- 239000000498 cooling water Substances 0.000 title claims abstract 16
- 229920006395 saturated elastomer Polymers 0.000 claims abstract 6
- 238000001816 cooling Methods 0.000 abstract 2
- 238000005259 measurement Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Exhaust-Gas Circulating Devices (AREA)
- Exhaust Gas After Treatment (AREA)
Abstract
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、特にエンジンの排気管に接続さ
れた熱交換器の劣化防止に関連する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to the prevention of deterioration of heat exchangers, particularly heat exchangers connected to the exhaust pipe of an engine.
灸米叫挟権
従来のガスエンジン用熱交換器を第4図について説明す
る。熱交換器10は、ガスエンジン等のエンジン11の
排気管12と、エンジン11から冷却管13を流れる冷
却水(−次冷却水)との間で熱交換を行う、エンジン1
1及び熱交換器1゜で加熱された冷却管13内の冷却水
は、更に第二の熱交換器14に接続される。第二の熱交
換器14では、冷却管13内を流れる冷却水と、第二の
冷却管16を流れる冷却水との間で熱交換を行う。A conventional heat exchanger for a gas engine will be explained with reference to FIG. The heat exchanger 10 exchanges heat between an exhaust pipe 12 of an engine 11 such as a gas engine and cooling water (subcooling water) flowing through a cooling pipe 13 from the engine 11.
1 and the cooling water in the cooling pipe 13 heated by the heat exchanger 1° is further connected to a second heat exchanger 14. In the second heat exchanger 14, heat exchange is performed between the cooling water flowing in the cooling pipe 13 and the cooling water flowing in the second cooling pipe 16.
冷却管13には、サーモスタット封切り換え弁15が設
けられ、冷却管13を通る冷却水が第二の熱交換器14
を通りエンジン11へ供給する通路又は第二の熱交換器
14を通らずに直接エンジン11に流入する通路を形成
する。The cooling pipe 13 is provided with a thermostatically sealed switching valve 15, and the cooling water passing through the cooling pipe 13 is transferred to the second heat exchanger 14.
A passage through which the heat exchanger passes through and supplies the engine 11, or a passage which flows directly into the engine 11 without passing through the second heat exchanger 14 is formed.
上記構成において、熱交換器10は、エンジン11から
排出・されかつ排気管12を通る排気ガスの熱を、冷却
管1:うを通る冷却水により受熱する。In the above configuration, the heat exchanger 10 receives the heat of the exhaust gas discharged from the engine 11 and passing through the exhaust pipe 12 by the cooling water passing through the cooling pipe 1.
この熱は第二の熱交換器14に供給され、第二の冷却管
16から熱が回収される。第二の冷却管16の加熱され
た高温冷却水は空気調和装置用の温水又は給湯等に利用
される。排気管12を通る排気ガスは、第一の熱交換器
10に流入し、ここで、冷却管13の冷却水に熱を奪わ
れた後、大気中に放出される。This heat is supplied to the second heat exchanger 14 and is recovered from the second cooling pipe 16. The heated high-temperature cooling water of the second cooling pipe 16 is used for hot water or hot water for an air conditioner. The exhaust gas passing through the exhaust pipe 12 flows into the first heat exchanger 10, where heat is removed by the cooling water of the cooling pipe 13, and then released into the atmosphere.
冷却管13を通る一次冷却水は、ポンプ(図示せず)に
より循環されるが、熱交換器10内を通過した後、サー
モスタット封切り換え弁15により流れ方向が制御され
る。サーモスタット封切り換え弁15は、例えば80℃
以上の温度に設定され、−次冷却水が水温80℃以下の
時は第二の熱交換器14を通らずガスエンジン11に直
接戻される。しかし、−次冷却水の水温が80℃を超え
るときは、−次冷却水の第二の熱交換器14を通りガス
エンジン11に戻る流路が形成される。The primary cooling water passing through the cooling pipe 13 is circulated by a pump (not shown), and after passing through the heat exchanger 10, the flow direction is controlled by a thermostatic seal switching valve 15. The thermostatic seal switching valve 15 is, for example, 80°C.
When the temperature is set above and the secondary cooling water has a water temperature of 80° C. or lower, it is directly returned to the gas engine 11 without passing through the second heat exchanger 14. However, when the temperature of the secondary cooling water exceeds 80° C., a flow path is formed for the secondary cooling water to pass through the second heat exchanger 14 and return to the gas engine 11.
ガスエンジン11の排気管12内では、冷却水との間で
熱交換を行うとき、排気ガスが過度に冷えるため、排気
中の水分やスス等の付着が促進され、熱交換器10の排
気側の通路に腐食又は目詰まり等の劣化が生じた。即ち
、熱交換器10を通過する排気ガスが一般に150℃〜
zOO℃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生ずる。熱交換器10の内壁に
より、排気ガスは露点以下の温度に冷却される。In the exhaust pipe 12 of the gas engine 11, when heat is exchanged with the cooling water, the exhaust gas cools down excessively, which promotes the adhesion of moisture, soot, etc. Deterioration such as corrosion or clogging has occurred in the passages. That is, the exhaust gas passing through the heat exchanger 10 generally has a temperature of 150°C to
When the temperature is below zOO°C, a phenomenon of condensation occurs in which water vapor contained in the exhaust gas becomes condensed water. The exhaust gas is cooled to a temperature below the dew point by the inner wall of the heat exchanger 10.
排気ガス中には、水蒸気、硫黄又は窒素が含まれ、この
冷却により水へ気圧力が飽和蒸気圧以下に減圧されると
、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。The exhaust gas contains water vapor, sulfur, or nitrogen, and when the air pressure is reduced to below the saturated vapor pressure, the water vapor condenses on the inner wall of the heat exchanger 10 and becomes sulfuric acid or nitric acid. , condensate water containing corrosive components such as acids is produced.
ガスエンジン11には、都市ガス又はLPG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、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。また。The gas engine 11 uses gas fuel such as city gas or LPG. These fuels contain mercaptans composed of SH groups, which upon combustion react with water vapor to produce sulfuric acid. Also.
燃焼時に酸素を供給する空気中には窒素が含まれ。Nitrogen is included in the air that provides oxygen during combustion.
窒素は水蒸気と反応して硝酸となる。生成される硫酸又
は硝酸は弱酸性であるが、熱交換器10内の温度が高い
ため、活性に富み、このため熱交換器10の内面を腐食
する時間当りの腐食減量は大きい。更に、排気管の温度
が低いと、排気ガス中に含まれるカーボンが排気管の内
壁に付着して、排気管に目詰まりが発生した。Nitrogen reacts with water vapor to form nitric acid. Although the generated sulfuric acid or nitric acid is weakly acidic, since the temperature inside the heat exchanger 10 is high, it is highly active, and therefore the corrosion loss per unit of time during which it corrodes the inner surface of the heat exchanger 10 is large. Furthermore, when the temperature of the exhaust pipe was low, carbon contained in the exhaust gas adhered to the inner wall of the exhaust pipe, causing clogging of the exhaust pipe.
このような欠点を解消するため、特開昭61−1497
96号公報に示されるように、排気ガスの温度を測定し
て、この温度レベルに対応して冷却水を流す方法が提案
されている。この公報に示されるように、ガスエンジン
用の排気熱回収用熱交換器を流れる排気ガスの温度を検
出し、この温度に対応して熱交換器を流れる冷却水の流
量を制御する低温流体制御法は公知である。In order to eliminate such drawbacks, Japanese Patent Application Laid-Open No. 61-1497
As shown in Japanese Patent No. 96, a method has been proposed in which the temperature of exhaust gas is measured and cooling water is caused to flow in accordance with the temperature level. As shown in this publication, low-temperature fluid control detects the temperature of exhaust gas flowing through a heat exchanger for exhaust heat recovery for gas engines and controls the flow rate of cooling water flowing through the heat exchanger in accordance with this temperature. The law is known.
発明が解決しようとする間1.a
しかし、従来の低温流体制御装置では、エンジンの排気
ガス温度を検出して熱交換器への冷却水の流量を制御す
るので、排気ガス中の水分の凝縮及びカーボンの付着を
十分に防止することができなかった。即ち、排気管の内
壁に水滴及びカーボンが付着する条件は、排気ガスの温
度のみではなく、飽和湿度が主要因である。排気管の温
度が低くても、排気ガス中の湿度が飽和湿度に達しない
ときは、排気管の内壁に水滴は付着しない、逆に、排気
管の温度が高い場合に、排気ガス中の湿度が飽和湿度を
超えているとき、排気管の内壁に水滴が付着する。排気
ガス中のカーボンは、排気管の内壁に付着する水滴と共
に排気管の内壁に付着して、エンジンの稼動と共に堆積
する。While the invention is trying to solve 1. a However, with conventional low-temperature fluid control devices, the flow rate of cooling water to the heat exchanger is controlled by detecting the engine exhaust gas temperature, which sufficiently prevents moisture condensation and carbon adhesion in the exhaust gas. I couldn't do that. That is, the conditions for water droplets and carbon to adhere to the inner wall of the exhaust pipe are mainly caused by not only the temperature of the exhaust gas but also the saturated humidity. Even if the temperature of the exhaust pipe is low, if the humidity in the exhaust gas does not reach the saturated humidity, water droplets will not adhere to the inner wall of the exhaust pipe. Conversely, if the temperature of the exhaust pipe is high, the humidity in the exhaust gas will not reach the saturated humidity. When the humidity exceeds the saturated humidity, water droplets adhere to the inner wall of the exhaust pipe. Carbon in the exhaust gas adheres to the inner wall of the exhaust pipe along with water droplets that adhere to the inner wall of the exhaust pipe, and accumulates as the engine operates.
このような現象が現実に発生している以上、従来のよう
に、単に排気ガスの温度のみを測定しても、熱交換器の
腐食及び目詰まりを十分に防止することができない。Since such a phenomenon actually occurs, it is not possible to sufficiently prevent corrosion and clogging of the heat exchanger by simply measuring the temperature of the exhaust gas as in the past.
そこで、この発明は、従来の上記欠点を解消して、排気
ガス中の湿度及び排気管の温度における飽和湿度に対応
して冷却水の流量を制御できる熱交換器の冷却水制御装
置を提供することを目的とする。SUMMARY OF THE INVENTION Accordingly, the present invention provides a cooling water control device for a heat exchanger that can eliminate the above-mentioned conventional drawbacks and control the flow rate of cooling water in accordance with the humidity in exhaust gas and the saturated humidity at the temperature of the exhaust pipe. The purpose is to
奥漠2点J」1伏するための手段 この発明による熱交換器の冷却水制御装置は。Depth 2 points J” 1 means to fall prone A cooling water control device for a heat exchanger according to the present invention is a cooling water control device for a heat exchanger.
エンジンの排気管に接続されかつエンジンの排気ガスと
冷却水との間で熱交換を行う熱交換器と、熱交換器の冷
却水の流量を制御する流量制御装置と、排気ガスの湿度
を測定する湿度測定装置と、排気管の温度を測定する温
度測定装置と、温度測定装置により測定された排気管の
温度に対応する飽和湿度に対して湿度測定装置により測
定された排気ガスの湿度が高いとき、流量制御装置を制
御して熱交換器への冷却水の流量を制御する流量制御回
路とを設けた構成を有する。A heat exchanger that is connected to the engine exhaust pipe and exchanges heat between engine exhaust gas and cooling water, a flow control device that controls the flow rate of the cooling water in the heat exchanger, and measures the humidity of the exhaust gas. a humidity measuring device that measures the temperature of the exhaust pipe; and a temperature measuring device that measures the temperature of the exhaust pipe; and a temperature measuring device that measures the temperature of the exhaust pipe; At this time, the heat exchanger has a configuration including a flow rate control circuit that controls the flow rate control device to control the flow rate of cooling water to the heat exchanger.
作用
流量制御回路は、温度測定装置により測定された排気管
の温度に対応する飽和湿度に対して湿度測定装置により
測定された排気ガスの湿度が高いとき、流量制御装置を
制御して冷却水の流量を制御し、排気管の温度に対応す
る飽和湿度に対して排気ガスの湿度が低いときは、冷却
水の流量制御を行わない。The operating flow rate control circuit controls the flow rate control device to control the cooling water when the humidity of the exhaust gas measured by the humidity measuring device is higher than the saturated humidity corresponding to the temperature of the exhaust pipe measured by the temperature measuring device. The flow rate of the cooling water is controlled, and when the humidity of the exhaust gas is lower than the saturated humidity corresponding to the temperature of the exhaust pipe, the flow rate of the cooling water is not controlled.
実施例
以下、この発明による熱交換器の冷却水制御装置の実施
例を第1図〜第3図について説明する。EXAMPLE Hereinafter, an example of a cooling water control device for a heat exchanger according to the present invention will be described with reference to FIGS. 1 to 3.
これらの図面では第4図に示す箇所と同一の部分につい
ては同一符号を付し、説明を省略する。In these drawings, the same parts as shown in FIG. 4 are designated by the same reference numerals, and their explanation will be omitted.
この発明による熱交換器の冷却水制御装置2゜は、排気
管12内を流れる排気ガスの湿度を測定する湿Jf1測
定装置21と、排気管の温度を測定する温度測定装v:
122と、熱交換器の冷却水の流量を制御する流量制御
装置23と、温度測定装置により測定された排気管の温
度に対応する飽和湿度に対して湿度測定装置により測定
された排気ガスの湿度が高いとき、流量制御装置を制御
して熱交換器への冷却水の流量を制御する流量制御回路
24とが設けられる。The cooling water control device 2 for a heat exchanger according to the present invention includes a humidity Jf1 measuring device 21 that measures the humidity of exhaust gas flowing in the exhaust pipe 12, and a temperature measuring device v that measures the temperature of the exhaust pipe.
122, a flow rate control device 23 that controls the flow rate of the cooling water of the heat exchanger, and a humidity of the exhaust gas measured by the humidity measuring device relative to the saturated humidity corresponding to the temperature of the exhaust pipe measured by the temperature measuring device. A flow control circuit 24 is provided which controls the flow rate control device to control the flow rate of cooling water to the heat exchanger when the temperature is high.
湿度測定装置21は、乾湿計、露点計、毛髪湿度計、赤
外線吸収湿度計、電気抵抗式湿度計等種々の湿度測定装
置を使用することができる。赤外線吸収湿度計は、特定
の赤外線が水蒸気に吸収されることを利用したものであ
る。また、電気抵抗式湿度計は、吸湿性物質(主にLi
C1)の薄層の電気抵抗が湿度によって変化する特性を
利用したものである。As the humidity measuring device 21, various humidity measuring devices such as a psychrometer, a dew point meter, a hair hygrometer, an infrared absorption hygrometer, and an electrical resistance hygrometer can be used. Infrared absorption hygrometers utilize the fact that specific infrared rays are absorbed by water vapor. In addition, electrical resistance hygrometers use hygroscopic substances (mainly Li)
This method utilizes the characteristic that the electrical resistance of the thin layer C1) changes depending on humidity.
温度測定装置22は、熱電対、負特性又は正特性のサー
ミスタ、バイメタル等種々の温度測定装置を使用できる
。As the temperature measuring device 22, various temperature measuring devices such as a thermocouple, a negative or positive thermistor, or a bimetal can be used.
流量制御装置23は、冷却管13を流れる冷却水を循環
するポンプ、流量制御弁又は熱交換器10への流量を制
限してエンジン11又は第二の熱交換器14へ戻す切り
換え弁である。The flow rate control device 23 is a pump that circulates the cooling water flowing through the cooling pipe 13, a flow rate control valve, or a switching valve that limits the flow rate to the heat exchanger 10 and returns it to the engine 11 or the second heat exchanger 14.
流量制御回路24は、マイクロコンピュータ等の集積回
路を使用して作成することができる。何れにしても、流
量制御回路24は、温度測定装置22に接続されかつ飽
和湿度を演算する飽和湿度決定手段と、飽和湿度決定手
段及び湿度測定装置21に接続されかつ飽和湿度決定手
段の出力より湿度測定手段の出力が大きいとき、流量制
御装置に制御出力を与えて冷却水の流量を制御比較手段
を有する。この動作を第2図のフローチャートについて
説明する。The flow rate control circuit 24 can be created using an integrated circuit such as a microcomputer. In any case, the flow rate control circuit 24 includes a saturated humidity determining means that is connected to the temperature measuring device 22 and calculates the saturated humidity, and a saturated humidity determining means that is connected to the saturated humidity determining means and the humidity measuring device 21 and uses the output of the saturated humidity determining means. When the output of the humidity measuring means is large, a control output is provided to the flow rate control device to control and compare the flow rate of the cooling water. This operation will be explained with reference to the flowchart of FIG.
まず、ステップ30では、湿度測定装置21からの信号
を受信して、排気管12を流れる排気ガスの湿度を検出
する0次に、ステップ31では、温度測定装置22から
の信号を受信して、排気管12の温度を検出する。流量
制御回路24内には。First, in step 30, a signal from the humidity measuring device 21 is received to detect the humidity of the exhaust gas flowing through the exhaust pipe 12.Next, in step 31, a signal is received from the temperature measuring device 22, and the humidity of the exhaust gas flowing through the exhaust pipe 12 is detected. The temperature of the exhaust pipe 12 is detected. In the flow control circuit 24.
演算回路が設けられ、ステップ32では、排気管12の
温度での飽和湿度を決定する。この飽和湿度は、湿り空
気線図を利用して容易に求めることができる。ステップ
33では、比較手段によって排気ガスの湿度が飽和湿度
より大きいか否か判断する。排気ガスの湿度が飽和湿度
より大きい又は等しいとき、ステップ34に進み、流量
制御装置23により冷却水の流量が制御される。この流
量制御は、冷却管13を流れる冷却水を循環するポンプ
、流量制御弁又は切り換え弁により熱交換器10への冷
却水の流量を減少状態、零流斌状態又は非増加状態にす
ることにより行われる。しかし。An arithmetic circuit is provided, and in step 32, the saturated humidity at the temperature of the exhaust pipe 12 is determined. This saturated humidity can be easily determined using a psychrometric diagram. In step 33, the comparing means determines whether the humidity of the exhaust gas is higher than the saturated humidity. When the humidity of the exhaust gas is greater than or equal to the saturated humidity, the process proceeds to step 34, where the flow rate control device 23 controls the flow rate of the cooling water. This flow rate control is performed by reducing the flow rate of the cooling water to the heat exchanger 10 by using a pump, a flow control valve, or a switching valve that circulates the cooling water flowing through the cooling pipe 13, reducing the flow rate to a zero flow state, or reducing the flow rate to a zero flow state or a non-increasing state. It will be done. but.
排気ガスの湿度が飽和湿度に満たないときは、ステップ
35において冷却水の流量は制御されない。When the humidity of the exhaust gas is less than the saturated humidity, the flow rate of the cooling water is not controlled in step 35.
ステップ34及び35において冷却水の流量を制御した
後又は非制御後、ステップ33に戻り、エンジン11の
稼!Fll中、常に排気ガス中の湿度と飽和湿度とが比
鮫される。After controlling or not controlling the flow rate of the cooling water in steps 34 and 35, the process returns to step 33 to check whether the engine 11 is running or not. During Fll, the humidity in the exhaust gas and the saturated humidity are always compared.
第3図は、流量制御回路24の具体的な回路を示す。排
気管12内を流れる排気ガスの湿度を測定する湿度al
ll定装置21は、増幅器25を介して差動増幅器28
の反転入力端子に接続される。また、排気管の温度を測
定する温度測定装置22は。FIG. 3 shows a specific circuit of the flow rate control circuit 24. Humidity al that measures the humidity of exhaust gas flowing inside the exhaust pipe 12
The ll determining device 21 is connected to a differential amplifier 28 via an amplifier 25.
is connected to the inverting input terminal of Also, a temperature measuring device 22 that measures the temperature of the exhaust pipe.
増幅器26を介して演算増幅器27の非反転入力端子に
接続される。演算増幅器27の反転入力端子は適当な電
源に接続される。演算増幅器27は排気管12の温度で
の飽和湿度を演算する。演算増幅器27の出力は、差動
増幅器28の非反転入力端子に供給される。作動増幅器
2Bの出力は、トランジスタ等のドライバ回路29に送
出される。It is connected to a non-inverting input terminal of an operational amplifier 27 via an amplifier 26 . The inverting input terminal of operational amplifier 27 is connected to a suitable power supply. The operational amplifier 27 calculates the saturated humidity at the temperature of the exhaust pipe 12. The output of operational amplifier 27 is supplied to a non-inverting input terminal of differential amplifier 28. The output of the operational amplifier 2B is sent to a driver circuit 29 such as a transistor.
ドライバ回路29は、そのオン時に、熱交換器の熱交換
器への冷却水の流量を制御する流量制御装置23を作動
する。When the driver circuit 29 is turned on, it operates the flow control device 23 that controls the flow rate of cooling water to the heat exchanger.
第3図の構成において、温度測定装置22の出力に基づ
いて演算増幅器27は、飽和湿度を表す出力を作動増幅
器28の非反転入力端子に供給する。また、湿度測定装
置21は、差動増幅器28の反転入力端子に出力を与え
る。差動増幅器28は、演算増幅器27の出力が増幅器
25の出力より小さいとき、ドライバ回路29に出力を
供給して流量制御装置23を作動して冷却水を循環する
。In the configuration of FIG. 3, based on the output of temperature measuring device 22, operational amplifier 27 provides an output representative of saturated humidity to a non-inverting input terminal of operational amplifier 28. Furthermore, the humidity measuring device 21 provides an output to the inverting input terminal of the differential amplifier 28. When the output of the operational amplifier 27 is smaller than the output of the amplifier 25, the differential amplifier 28 supplies an output to the driver circuit 29 to operate the flow control device 23 and circulate the cooling water.
しかし、演算増幅器27の出力が増幅器25の出゛力よ
り大きいとき又は等しいとき、流量制御装置23を制御
して冷却水の流量を減少状態、零流量状態又は非増加状
態にする。However, when the output of the operational amplifier 27 is greater than or equal to the output of the amplifier 25, the flow control device 23 is controlled to reduce the flow rate of the cooling water, to a zero flow state, or to a non-increasing state.
上記のように、流量制御回路24は、温度測定装置22
により測定された排気管の温度に対応する飽和湿度に対
して湿度測定装置21により測定された排気ガスの湿度
が高いとき、流量制御装置を制御して冷却水の流量を制
御し、排気管の温度に対応する飽和湿度に対して排気ガ
スの湿度が低いときは、冷却水の流量制御を行わない、
従って、排気管の温度が低く、排気ガス中の湿度が飽和
湿度に達しないは、冷却水が循環される。また、排気管
の温度が高くても、排気ガス中の湿度が飽和湿度を超え
ているときは、冷却水の流量が制限される。このため、
排気管の内壁に水滴が付着する現象及び付着する水滴と
共に排気管の内壁に排気ガス中のカーボンが付着する現
象が生じない。As mentioned above, the flow control circuit 24 controls the temperature measurement device 22
When the humidity of the exhaust gas measured by the humidity measuring device 21 is higher than the saturated humidity corresponding to the temperature of the exhaust pipe measured by When the humidity of the exhaust gas is lower than the saturated humidity corresponding to the temperature, the flow rate of cooling water is not controlled.
Therefore, when the temperature of the exhaust pipe is low and the humidity in the exhaust gas does not reach the saturated humidity, cooling water is circulated. Further, even if the temperature of the exhaust pipe is high, when the humidity in the exhaust gas exceeds the saturated humidity, the flow rate of the cooling water is restricted. For this reason,
A phenomenon in which water droplets adhere to the inner wall of the exhaust pipe and a phenomenon in which carbon in the exhaust gas adheres to the inner wall of the exhaust pipe together with the attached water droplets does not occur.
分明の級呆
この発明では、排気ガスの湿度及び排気管の温度を1l
lll定して、熱交換器へ流れる冷却水の流量が制御さ
れる。冷却水の流量を制御し、排気管の内壁での水滴の
付着を防止することにより、腐食性物質による熱交換器
の排気管の腐食及びカーボンの付着による目詰まりを防
止することができる。In this invention, the humidity of the exhaust gas and the temperature of the exhaust pipe are adjusted to 1 liter.
The flow rate of the cooling water flowing to the heat exchanger is controlled based on the specified temperature. By controlling the flow rate of cooling water and preventing water droplets from adhering to the inner wall of the exhaust pipe, corrosion of the exhaust pipe of the heat exchanger due to corrosive substances and clogging due to adhesion of carbon can be prevented.
このように、熱交換器の劣化を防止すると共に。In this way, the deterioration of the heat exchanger is prevented.
熱交換効率の低下を阻止することが可能となる。It becomes possible to prevent a decrease in heat exchange efficiency.
第1図はこの発明により熱交換器の冷却水制御装置のブ
ロック図、第2図は流量制御回路の動作を示すフローチ
ャート、第3図は流量制御回路の回路図、第4図は従来
の熱交換器のブロック図である。
110.エンジン、 101.熱交換器、 126.
排気管、 20.、冷却水制御装置、21゜、湿度測
定装置、 220.温度測定装置、23゜、流量制御装
置、 240.流量制御回路、第1図
第2図Fig. 1 is a block diagram of a cooling water control device for a heat exchanger according to the present invention, Fig. 2 is a flowchart showing the operation of the flow rate control circuit, Fig. 3 is a circuit diagram of the flow rate control circuit, and Fig. 4 is a conventional heat exchanger cooling water control device. FIG. 2 is a block diagram of an exchanger. 110. Engine, 101. heat exchanger, 126.
Exhaust pipe, 20. , cooling water control device, 21°, humidity measuring device, 220. Temperature measurement device, 23°, flow rate control device, 240. Flow control circuit, Figure 1 Figure 2
Claims (3)
ガスと冷却水との間で熱交換を行う熱交換器と、熱交換
器の冷却水の流量を制御する流量制御装置と、排気ガス
の湿度を測定する湿度測定装置と、排気管の温度を測定
する温度測定装置と、温度測定装置により測定された排
気管の温度に対応する飽和湿度に対して湿度測定装置に
より測定された排気ガスの湿度が高いとき、流量制御装
置を制御して熱交換器への冷却水の流量を制御する流量
制御回路とで構成されることを特徴とする熱交換器の冷
却水制御装置。(1) A heat exchanger connected to the engine exhaust pipe and exchanging heat between engine exhaust gas and cooling water; a flow rate control device controlling the flow rate of the cooling water in the heat exchanger; A humidity measuring device for measuring humidity, a temperature measuring device for measuring the temperature of the exhaust pipe, and a temperature measuring device for measuring the temperature of the exhaust gas measured by the humidity measuring device against the saturated humidity corresponding to the temperature of the exhaust pipe measured by the temperature measuring device. 1. A cooling water control device for a heat exchanger, comprising a flow rate control circuit that controls a flow rate control device to control the flow rate of cooling water to the heat exchanger when humidity is high.
和湿度を演算する飽和湿度決定手段と、飽和湿度決定手
段及び湿度測定装置に接続されかつ飽和湿度決定手段の
出力より湿度測定手段の出力が大きいとき、流量制御装
置に制御出力を与えて熱交換器への冷却水の流量を制御
する比較手段とを有する特許請求の範囲第(1)項記載
の熱交換器の冷却水制御装置。(2) The flow control circuit includes a saturated humidity determining means connected to the temperature measuring device and calculating saturated humidity, and an output of the humidity measuring means connected to the saturated humidity determining means and the humidity measuring device and based on the output of the saturated humidity determining means. A cooling water control device for a heat exchanger according to claim 1, further comprising comparison means for controlling the flow rate of cooling water to the heat exchanger by giving a control output to the flow rate control device when the flow rate is large.
御弁又は切り換え弁である特許請求の範囲第(1)項記
載の熱交換器の冷却水制御装置。(3) The cooling water control device for a heat exchanger according to claim (1), wherein the flow rate control device is a pump, a flow control valve, or a switching valve that circulates the cooling water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62274668A JPH0625541B2 (en) | 1987-10-31 | 1987-10-31 | Cooling water control device for heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62274668A JPH0625541B2 (en) | 1987-10-31 | 1987-10-31 | Cooling water control device for heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01117909A true JPH01117909A (en) | 1989-05-10 |
| JPH0625541B2 JPH0625541B2 (en) | 1994-04-06 |
Family
ID=17544893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62274668A Expired - Lifetime JPH0625541B2 (en) | 1987-10-31 | 1987-10-31 | Cooling water control device for heat exchanger |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0625541B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0579320A (en) * | 1991-09-20 | 1993-03-30 | Hitachi Ltd | Internal combustion engine, operation thereof and automobile |
| CN103498713A (en) * | 2013-09-29 | 2014-01-08 | 宝鸡石油机械有限责任公司 | Energy-saving noise-lowering safety system of large diesel engine |
-
1987
- 1987-10-31 JP JP62274668A patent/JPH0625541B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0579320A (en) * | 1991-09-20 | 1993-03-30 | Hitachi Ltd | Internal combustion engine, operation thereof and automobile |
| CN103498713A (en) * | 2013-09-29 | 2014-01-08 | 宝鸡石油机械有限责任公司 | Energy-saving noise-lowering safety system of large diesel engine |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0625541B2 (en) | 1994-04-06 |
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