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JPH058360B2 - - Google Patents
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JPH058360B2 - - Google Patents

Info

Publication number
JPH058360B2
JPH058360B2 JP24321084A JP24321084A JPH058360B2 JP H058360 B2 JPH058360 B2 JP H058360B2 JP 24321084 A JP24321084 A JP 24321084A JP 24321084 A JP24321084 A JP 24321084A JP H058360 B2 JPH058360 B2 JP H058360B2
Authority
JP
Japan
Prior art keywords
heat exchanger
cleaning
cleaning liquid
condensed water
container
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
JP24321084A
Other languages
Japanese (ja)
Other versions
JPS61122497A (en
Inventor
Takeji Yoko
Akizuna Nakagaki
Akio Myazawa
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 JP24321084A priority Critical patent/JPS61122497A/en
Publication of JPS61122497A publication Critical patent/JPS61122497A/en
Publication of JPH058360B2 publication Critical patent/JPH058360B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G9/00Cleaning by flushing or washing, e.g. with chemical solvents

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Cleaning By Liquid Or Steam (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 この発明は、熱交換器の洗浄方法及び洗浄装置
に関連する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application This invention relates to a method and apparatus for cleaning a heat exchanger.

従来の技術 一般に熱交換器は、互いに熱交換を行う第1流
体及び第2流体を別々に通過する第1通路及び第
2通路を有する。多管式熱交換器では、第1通路
及び第2通路のうち一方は、他方の通路中に配置
された複数の金属管で構成され、これらの管の前
後に入口と出口とが設けられる。
2. Description of the Related Art Generally, a heat exchanger has a first passage and a second passage through which a first fluid and a second fluid that exchange heat with each other pass separately. In a multi-tubular heat exchanger, one of the first passage and the second passage is composed of a plurality of metal tubes arranged in the other passage, and an inlet and an outlet are provided before and after these tubes.

第1流体にガスを使用し、第2流体に水を使用
して高温ガスから水で熱を吸収する場合、ガス
は、水中に配置された多数の管の中を通過する。
このガスが内燃機関から排出されるガスの場合、
排気ガス中には、炭酸ガスのほか水蒸気、硫黄
等、種々の成分が含有される。排気ガスと水との
間で熱交換を行うと、排気ガスは水で冷却される
ため排気ガス中の水蒸気が凝結し、凝縮水は管の
内壁に水滴となつて付着する。この水滴は、排気
ガス中の硫黄と反応して硫酸が生成され、金属製
管の内壁は、硫酸によつて腐食する。このため熱
交換器の寿命が短縮された。従来では、管内壁の
腐食を防止するため、種々の対策が講じられた。
第1に、凝縮水の発生しない状態を確保するこ
と、即ち出口での排気ガス温度をより高温に保持
する対策が提案された。この方法では、排気ガス
から十分に熱を回収できないため、熱交換効率が
著しく低下した。第2に、耐食性材料で管を形成
するか又はこの材料で管内壁を処理する方法が提
案された。しかしこの方法も、製造された管が高
価なため、実用的ではない、別法として、管の肉
厚を大きくする方法もあるが、重量の増加により
熱交換器を車両に用いることは適当ではない。更
に、一定時間毎に清掃員が洗浄する方法がある。
この方法も、短時間毎に洗浄しなければならない
ため、非常に煩瑣であり、又、熱交換器へ取付位
置によつては、洗浄できないことがある。
When a gas is used as the first fluid and water is used as the second fluid to absorb heat from the hot gas with water, the gas passes through a number of tubes that are placed underwater.
If this gas is emitted from an internal combustion engine,
Exhaust gas contains various components such as water vapor and sulfur in addition to carbon dioxide gas. When heat is exchanged between the exhaust gas and water, the exhaust gas is cooled by the water, so water vapor in the exhaust gas condenses, and the condensed water adheres to the inner wall of the pipe as water droplets. These water droplets react with sulfur in the exhaust gas to produce sulfuric acid, and the inner wall of the metal pipe is corroded by the sulfuric acid. This shortened the life of the heat exchanger. Conventionally, various measures have been taken to prevent corrosion of the inner walls of pipes.
First, measures have been proposed to ensure that no condensed water is generated, that is, to maintain the exhaust gas temperature at the outlet at a higher temperature. With this method, heat exchange efficiency was significantly reduced because sufficient heat could not be recovered from the exhaust gas. Secondly, methods have been proposed for forming the tubes from corrosion-resistant materials or for treating the inner walls of the tubes with this material. However, this method is also not practical because the manufactured tubes are expensive.Alternatively, there is a method of increasing the wall thickness of the tubes, but due to the increased weight, it is not appropriate to use heat exchangers in vehicles. do not have. Furthermore, there is a method in which cleaning staff clean the area at regular intervals.
This method is also very cumbersome as it requires cleaning every short period of time, and cleaning may not be possible depending on the mounting position on the heat exchanger.

発明が解決しようとする問題点 この発明は、上記欠点を解消したもので、高熱
交換効率を維持しつつ自動的に洗浄できる熱交換
器の洗浄法及び洗浄装置を提供するものである。
この発明の洗浄装置は、比較的安価かつ軽量に製
造できる。
Problems to be Solved by the Invention The present invention solves the above-mentioned drawbacks, and provides a method and apparatus for cleaning a heat exchanger that can be automatically cleaned while maintaining high heat exchange efficiency.
The cleaning device of the present invention can be manufactured relatively inexpensively and lightweight.

発明の概要 この発明による熱交換器の洗浄方法は、熱交換
器内で得られた凝縮水を容器内に導入し、その凝
縮水に含まれる特定成分の濃度が測定される。こ
の濃度が所定レベル以上か否かが検出され、所定
レベル以上のときは、熱交換器内に洗浄液が供給
される。
Summary of the Invention In the heat exchanger cleaning method according to the present invention, condensed water obtained within the heat exchanger is introduced into a container, and the concentration of a specific component contained in the condensed water is measured. It is detected whether this concentration is above a predetermined level, and when it is above the predetermined level, the cleaning liquid is supplied into the heat exchanger.

この発明による熱交換器の洗浄装置は、上記洗
浄方法の実施に直接使用する装置で、この装置
は、容器内に収容された凝縮水中に含まれる特定
成分に応答して電気信号を生ずるセンサと、この
センサの電気信号が所定レベル以上のとき駆動信
号を生ずる比較回路と、比較回路の駆動信号を受
け熱交換器内に洗浄液を供給する洗浄液供給手段
とを有する。
The heat exchanger cleaning device according to the present invention is a device that is directly used to carry out the above cleaning method, and this device includes a sensor that generates an electrical signal in response to a specific component contained in condensed water contained in a container. , a comparison circuit that generates a drive signal when the electric signal from the sensor is at a predetermined level or higher, and a cleaning liquid supply means that receives the drive signal from the comparison circuit and supplies cleaning liquid into the heat exchanger.

実施例 以下、この発明の実施例を図面について説明す
る。第1図に示される通り、熱交換器10は、排
気ガス等の第1流体が通過する第1通路11と、
水等の第2流体が通過する第2通路12とを有す
る。第1通路11には、入口13と、この入口1
3に連結しかつ徐々に拡大する大きさを有する膨
張室14と、該膨張室14に連絡する多数の金属
管15と、金属管15の出口に連絡しかつ前記膨
張室14とほぼ同形の収縮室16の後方に連絡す
る出口17とが設けられる。金属管15の両端に
は、一対の仕切板18,19が固着され、その間
に冷却室20が形成される。冷却室20には、第
2通路の入口21と出口22が設けられる。
Embodiments Hereinafter, embodiments of the present invention will be described with reference to the drawings. As shown in FIG. 1, the heat exchanger 10 includes a first passage 11 through which a first fluid such as exhaust gas passes;
It has a second passage 12 through which a second fluid such as water passes. The first passage 11 has an inlet 13 and an inlet 1
an expansion chamber 14 connected to the expansion chamber 3 and having a size that gradually expands; a large number of metal tubes 15 connected to the expansion chamber 14; and a contraction chamber connected to the outlet of the metal tube 15 and having a substantially same shape as the expansion chamber 14. An outlet 17 communicating with the rear of the chamber 16 is provided. A pair of partition plates 18 and 19 are fixed to both ends of the metal tube 15, and a cooling chamber 20 is formed between them. The cooling chamber 20 is provided with an inlet 21 and an outlet 22 of the second passage.

この発明の洗浄装置では、収縮室16の下方に
容器23に連絡する管24が取付けられる。容器
23の下部には、弁25に連絡する管26が接続
される。弁25に接続された管27は、公知の排
水管に接続される。容器23内には、センサ28
が固定される。このセンサは、酸又はアルカリ濃
度を測定するガラス電極等のPHメータ用センサ又
は他の腐食性物質の濃度を測定する装置で利用さ
れる公知のセンサが使用される。
In the cleaning device of the present invention, a pipe 24 communicating with a container 23 is attached below the contraction chamber 16. A pipe 26 communicating with a valve 25 is connected to the lower part of the container 23 . A pipe 27 connected to the valve 25 is connected to a known drain pipe. Inside the container 23, a sensor 28 is installed.
is fixed. This sensor may be a PH meter sensor such as a glass electrode that measures acid or alkali concentration, or a known sensor used in devices that measure the concentration of other corrosive substances.

このセンサ28は、制御回路30に電気的に接
続される。制御回路30は、第1電磁弁29を構
成するソレノイド31と、第2電磁弁32を構成
するソレノイド33と、ポンプ34を駆動するモ
ータ35にも電気的に接続される。弁25がソレ
ノイド31によつて作動されるのと同様に、ポン
プ34に接続された弁36はソレノイド33によ
つて作動される。弁25と36は、ノーマルクロ
ーズ型で、それぞれ、ソレノイド31又は33が
付勢されたときのみ開放される。ポンプ34は、
洗浄液37が貯蔵されたタンク38に接続され、
又、弁36を通じて噴水口40に接続される。ソ
レノイド33、弁36、ポンプ34及びモータ3
5は洗浄液供給手段49を構成する。噴水口40
は、熱交換器10の入口13に突出して固定さ
れ、金属管15に向つて洗浄液を噴出できるよう
にセツトされる。図示の例では、熱交換器10は
一定角度θだけ傾斜して固定される。
This sensor 28 is electrically connected to a control circuit 30. The control circuit 30 is also electrically connected to a solenoid 31 forming the first electromagnetic valve 29 , a solenoid 33 forming the second electromagnetic valve 32 , and a motor 35 driving the pump 34 . Just as valve 25 is actuated by solenoid 31, valve 36 connected to pump 34 is actuated by solenoid 33. Valves 25 and 36 are normally closed and open only when solenoids 31 or 33, respectively, are energized. The pump 34 is
connected to a tank 38 in which a cleaning liquid 37 is stored;
It is also connected to a water fountain 40 through a valve 36. Solenoid 33, valve 36, pump 34 and motor 3
5 constitutes a cleaning liquid supply means 49. fountain 40
is fixed so as to protrude from the inlet 13 of the heat exchanger 10, and is set so as to be able to spray cleaning liquid toward the metal tube 15. In the illustrated example, the heat exchanger 10 is tilted and fixed by a certain angle θ.

第2図は、制御回路30の詳細が示される。こ
の制御回路30は、センサ28に接続された増幅
器41と、ORゲート42を通じて増幅器41の
出力を受ける非反転入力端子43を有する差動増
幅器44と、差動増幅器44の出力を増幅するト
ランジスタ45とを有する。差動増幅器44とト
ランジスタ45は比較回路39を構成する。OR
ゲート42の他の入力端子は手動スイツチ46に
接続され、差動増幅器44の反転入力端子47
は、基準レベルを決定する定電圧電源48に接続
される。トランジスタ45のコレクタは、電源に
接続され、エミツタは、制限抵抗50,51,5
2を通じてそれぞれ、ソレノイド31と33及び
モータ35に接続される。
FIG. 2 shows details of the control circuit 30. This control circuit 30 includes an amplifier 41 connected to the sensor 28, a differential amplifier 44 having a non-inverting input terminal 43 that receives the output of the amplifier 41 through an OR gate 42, and a transistor 45 that amplifies the output of the differential amplifier 44. and has. The differential amplifier 44 and the transistor 45 constitute a comparison circuit 39. OR
The other input terminal of the gate 42 is connected to a manual switch 46 and an inverting input terminal 47 of the differential amplifier 44.
is connected to a constant voltage power supply 48 that determines the reference level. The collector of the transistor 45 is connected to the power supply, and the emitter is connected to the limiting resistors 50, 51, 5.
2 to solenoids 31 and 33 and a motor 35, respectively.

上記洗浄装置の作動について以下説明する。熱
交換器10の第1通路11を通る高温排気ガス
は、金属管15内を通過するとき、冷却室20内
を循環する水によつて冷却される。金属管15内
では、排気ガス中に含まれる水蒸気は冷却され多
数の水滴となつて金属管15の内壁に付着する。
この水滴は排気ガス中に含まれる硫黄等の無機物
質又は有機物質と反応し硫酸又はアルカリ等の腐
食性物質を形成する。熱交換器10が一定角度傾
斜して固定されるため、金属管15の内壁に付着
した水滴はある程度の大きさまで成長したのち、
出口17へ向つて流れ始め、収縮室16内で下方
に落下する。この凝縮水は、管24を通り、容器
23内に集められる。
The operation of the above cleaning device will be explained below. The high temperature exhaust gas passing through the first passage 11 of the heat exchanger 10 is cooled by water circulating in the cooling chamber 20 as it passes through the metal tube 15 . Inside the metal tube 15, the water vapor contained in the exhaust gas is cooled and becomes a large number of water droplets that adhere to the inner wall of the metal tube 15.
These water droplets react with inorganic substances such as sulfur or organic substances contained in the exhaust gas to form corrosive substances such as sulfuric acid or alkali. Since the heat exchanger 10 is fixed at a fixed angle, the water droplets attached to the inner wall of the metal tube 15 grow to a certain size, and then
It begins to flow towards the outlet 17 and falls downward within the contraction chamber 16. This condensed water passes through tube 24 and is collected in container 23.

容器28内に取付けられたセンサ28は、接触
する凝縮水に含まれる腐食性物質濃度に対応する
電圧を発生する。この電圧は、増幅器41で増幅
された後、ORゲート42を通じて差動増幅器4
4の非反転入力端子43に印加される。ORゲー
ト42は、増幅器41からのアナログ信号を非反
転入力端子43へ伝達する。差動増幅器44は、
非反転入力端子43と反転入力端子47とに印加
される電圧を比較して、非反転入力端子43の電
圧レベルの方が高いとき出力を生じトランジスタ
45を導通させる。トランジスタ45の導通状態
の間、抵抗50,51,52を通じて電圧がソレ
ノイド31と33及びモータ35に印加される。
A sensor 28 mounted within the vessel 28 generates a voltage corresponding to the concentration of corrosive material contained in the condensate it contacts. This voltage is amplified by an amplifier 41 and then passed through an OR gate 42 to a differential amplifier 4.
It is applied to the non-inverting input terminal 43 of No. 4. OR gate 42 transmits the analog signal from amplifier 41 to non-inverting input terminal 43. The differential amplifier 44 is
The voltages applied to the non-inverting input terminal 43 and the inverting input terminal 47 are compared, and when the voltage level of the non-inverting input terminal 43 is higher, an output is generated and the transistor 45 is made conductive. While transistor 45 is conductive, voltage is applied to solenoids 31 and 33 and motor 35 through resistors 50, 51, and 52.

従つて、弁25と36がオープン即ち開放さ
れ、ポンプ34の駆動によつてタンク38内の洗
浄液が弁36と噴水口40を通じて熱交換器10
の膨張室14内に供給される。このため、金属管
15の内部が洗浄され、この洗浄液は腐食性物質
と共に収縮室16へ流れ、管24を通じて容器2
3内へ流入する。弁25は、既に開放されている
ので、凝縮水と洗浄水は弁25を通じて外部へ排
出される。容器23内の腐食性物質濃度が所定レ
ベル以下となると、差動増幅器44の非反転入力
端子43に印加される電圧は、反転入力端子47
の電圧より低くなるため、差動増幅器44の出力
が停止され、トランジスタ45が非導通状態とな
る。従つて、ソレノイド31,33及びモータ3
5が消勢され、弁25と36が閉鎖されると共に
ポンプ34による洗浄液の熱交換器10内への供
給が終了する。
Therefore, the valves 25 and 36 are opened, and the cleaning liquid in the tank 38 is supplied to the heat exchanger 10 through the valve 36 and the spout 40 by driving the pump 34.
is supplied into the expansion chamber 14 of. For this reason, the inside of the metal tube 15 is cleaned, and this cleaning liquid flows into the shrinkage chamber 16 together with the corrosive substances and passes through the tube 24 to the container 2.
Flow into 3. Since the valve 25 is already open, the condensed water and cleaning water are discharged to the outside through the valve 25. When the corrosive substance concentration in the container 23 falls below a predetermined level, the voltage applied to the non-inverting input terminal 43 of the differential amplifier 44 changes to the inverting input terminal 47.
Since the voltage becomes lower than the voltage of , the output of the differential amplifier 44 is stopped and the transistor 45 becomes non-conductive. Therefore, the solenoids 31, 33 and the motor 3
5 is deenergized, valves 25 and 36 are closed, and supply of the cleaning liquid into the heat exchanger 10 by the pump 34 ends.

この発明で使用される洗浄液供給手段の他の実
施例として、ベンチユリ管53を使用する例が第
3図に示される。この例では、第1通路11の入
口13に縮小断面部54が形成されこの縮小断面
部54には、弁36に連通する管55が接続され
る。従つて排気ガスは、縮小断面部54では高速
度で流れ、低圧力状態となる。この状態でソレノ
イド33が付勢され、弁36が開放されると、タ
ンク38内の洗浄液37は、ポンプ34を使用せ
ずに自動的に熱交換器10の縮小断面部54に吸
引され、排気ガスと共に膨張室14内に噴霧さ
れ、金属管15内が洗浄される。
As another embodiment of the cleaning liquid supply means used in the present invention, an example in which a bench lily tube 53 is used is shown in FIG. In this example, a reduced cross-section portion 54 is formed at the inlet 13 of the first passage 11, and a pipe 55 communicating with the valve 36 is connected to the reduced cross-section portion 54. Therefore, the exhaust gas flows at a high velocity in the reduced cross-section portion 54 and is in a low pressure state. In this state, when the solenoid 33 is energized and the valve 36 is opened, the cleaning liquid 37 in the tank 38 is automatically sucked into the reduced section section 54 of the heat exchanger 10 without using the pump 34, and is exhausted. It is sprayed into the expansion chamber 14 together with the gas, and the inside of the metal tube 15 is cleaned.

上記自動洗浄とは別に適宜洗浄するときは、ス
イツチ46が手動で押圧される。このため、非反
転入力端子43に印加される電圧が高くなり、差
動増幅器44の出力により上記と同様に熱交換器
が洗浄される。
When performing appropriate cleaning in addition to the automatic cleaning described above, the switch 46 is manually pressed. Therefore, the voltage applied to the non-inverting input terminal 43 increases, and the output of the differential amplifier 44 cleans the heat exchanger in the same manner as described above.

この発明の装置では、種々の変更が可能であ
る。例えば、管24を二分路に分けて、凝縮水と
洗浄液とを別の管路で放出することもできる。ま
た、膨張室14の下部には、ドレン抜きを設けて
もよい。
Various modifications can be made to the device of this invention. For example, the pipe 24 can be divided into two branches so that the condensed water and the cleaning liquid can be discharged in separate pipes. Further, a drain may be provided at the bottom of the expansion chamber 14.

更にトランジスタ45とソレノイド31,33
又はモータ35との間に個別タイマを接続して、
又は別の電源スイツチに接続してこれらの作動時
間を任意に選択してもよい。更にORゲート42
を省略して、増幅器41の出力を直接差動増幅器
44の非反転入力端子43へ接続すると共に、ス
イツチ46をトランジスタ45と並列に接続し
て、スイツチ46の出力を直接、抵抗50,5
1,52に印加してもよい。
Furthermore, a transistor 45 and solenoids 31, 33
Or by connecting an individual timer between the motor 35 and
Alternatively, these operating times may be arbitrarily selected by connecting to another power switch. Furthermore, OR gate 42
is omitted, the output of the amplifier 41 is directly connected to the non-inverting input terminal 43 of the differential amplifier 44, the switch 46 is connected in parallel with the transistor 45, and the output of the switch 46 is directly connected to the resistors 50, 5.
1,52 may be applied.

洗浄液と共に熱交換器10内に、スケール又は
ゴミ等の異物が入ることを防止するため、タンク
38とポンプ34との間にフイルタを設けること
もできる。又、排液を再利用するため、管27に
フイルタ、中和槽又は洗剤混合槽等の処理装置を
設けてこのような装置を経てタンク38に浄化液
を戻す循環管路を使用することもできる。
A filter may be provided between the tank 38 and the pump 34 to prevent foreign matter such as scale or dirt from entering the heat exchanger 10 together with the cleaning liquid. In addition, in order to reuse the waste liquid, a circulation pipe line may be used in which the pipe 27 is equipped with a processing device such as a filter, a neutralization tank, or a detergent mixing tank, and the purified liquid is returned to the tank 38 through such a device. can.

上記実施例は、多管式熱交換器の例を示すが、
多板式熱交換器にも実施できる。
The above embodiment shows an example of a shell-and-tube heat exchanger,
It can also be applied to multi-plate heat exchangers.

発明の効果 この発明は、上記の通り構成したので、熱交換
器を自動的に洗浄でき、熱交換器の効率は低下さ
れない。また、熱交換器を軽量かつ比較的安価に
製造できる。更に清掃員による洗浄作業を省略で
きかつ熱交換器を細部まで充分に洗浄できる。こ
のため、熱交換器の修理に要する時間も大幅に減
少し熱交換器の寿命も長期化することができる。
Effects of the Invention Since the present invention is configured as described above, the heat exchanger can be automatically cleaned and the efficiency of the heat exchanger is not reduced. Moreover, the heat exchanger can be manufactured lightweight and relatively inexpensively. Furthermore, cleaning work by cleaning personnel can be omitted, and the heat exchanger can be thoroughly cleaned in detail. Therefore, the time required for repairing the heat exchanger is significantly reduced, and the life of the heat exchanger can be extended.

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

第1図はこの発明による熱交換器の洗浄装置の
断面図;第2図は、制御回路の詳細を示す電気回
路図で;第3図は、洗浄液供給手段の他の実施例
の断面図を示す。 10……熱交換器、11……第1通路、12…
…第2通路、23……容器、28……センサ、3
9……比較回路、49……洗浄液供給手段。
Fig. 1 is a sectional view of a heat exchanger cleaning device according to the present invention; Fig. 2 is an electric circuit diagram showing details of the control circuit; Fig. 3 is a sectional view of another embodiment of the cleaning liquid supply means. show. 10... Heat exchanger, 11... First passage, 12...
...Second passageway, 23...Container, 28...Sensor, 3
9... Comparison circuit, 49... Cleaning liquid supply means.

Claims (1)

【特許請求の範囲】 1 熱交換器内で得られた凝縮水を容器内に導入
する導水過程; 上記容器内に導入された凝縮水に含まれる特定
成分の濃度を測定する測定過程; 上記特定成分の濃度が所定レベル以上であるこ
とを検出する検出過程;及び 上記検出過程の検出に基いて、熱交換器内に洗
浄液を供給する洗浄過程; とで構成されることを特徴とする熱交換器の洗浄
方法。 2 上記洗浄過程では、上記洗浄液の供給と同時
に凝縮水及び洗浄液の管路が開かれる特許請求の
範囲第1項記載の熱交換器の洗浄方法。 3 上記測定過程、検出過程及び洗浄過程は、電
気的手段により自動的に行われる特許請求の範囲
第1項又は第2項記載の熱交換器の洗浄方法。 4 熱交換を行う第1流体及び第2流体を別々に
通過する第1通路及び第2通路を有する熱交換器
と、 上記第1通路内で得られた凝縮水を収容する容
器と、 該容器内の凝縮水中に含まれる特定成分に応答
して電気信号を生ずるセンサと、 上記センサの電気信号が所定レベル以上のと
き、駆動信号を生ずる比較回路と、 該比較回路の駆動信号を受け熱交換器内に洗浄
液を供給する洗浄液供給手段とで構成されること
を特徴とする熱交換器の洗浄装置。 5 上記センサはPHセンサである特許請求の範囲
第4項記載の熱交換器の洗浄装置。 6 上記比較回路は、差動増幅器を含む特許請求
の範囲第4項記載の熱交換器の洗浄装置。 7 上記洗浄液供給手段は、上記比較器の駆動信
号で付勢されるモータ及び該モータで駆動される
ポンプを含む特許請求の範囲第4項記載の熱交換
器の洗浄装置。 8 上記洗浄液供給手段は、上記熱交換器の第1
流体が流入する入口に形成されたベンチユリ管を
有する特許請求の範囲第4項記載の熱交換器の洗
浄装置。 9 上記洗浄液供給手段は、凝縮水を収容する容
器内の液体の流出を制御する第1電磁弁と熱交換
器への洗浄液の流入を制御する第2電磁弁とを有
し、第1電磁弁及び第2電磁弁は、上記差動増幅
器の出力で制御される特許請求の範囲第6項記載
の熱交換器の洗浄装置。 10 上記熱交換器は、水平に対し一定角度傾斜
している特許請求の範囲第6項ないし第9項のい
ずれかに記載の熱交換器の洗浄装置。
[Claims] 1. A water introduction process for introducing condensed water obtained in a heat exchanger into a container; A measurement process for measuring the concentration of a specific component contained in the condensed water introduced into the container; A heat exchanger characterized by comprising: a detection step of detecting that the concentration of a component is at a predetermined level or higher; and a cleaning step of supplying a cleaning liquid into the heat exchanger based on the detection in the detection step. How to clean the utensils. 2. The heat exchanger cleaning method according to claim 1, wherein in the cleaning process, condensed water and cleaning liquid pipes are opened at the same time as the cleaning liquid is supplied. 3. The heat exchanger cleaning method according to claim 1 or 2, wherein the measurement process, detection process, and cleaning process are automatically performed by electrical means. 4. A heat exchanger having a first passage and a second passage through which a first fluid and a second fluid for heat exchange pass separately; a container for storing condensed water obtained in the first passage; and the container. a sensor that generates an electric signal in response to a specific component contained in the condensed water; a comparison circuit that generates a drive signal when the electric signal of the sensor is above a predetermined level; and a heat exchanger that receives the drive signal of the comparison circuit. 1. A cleaning device for a heat exchanger, comprising a cleaning liquid supply means for supplying cleaning liquid into the vessel. 5. The heat exchanger cleaning device according to claim 4, wherein the sensor is a PH sensor. 6. The heat exchanger cleaning device according to claim 4, wherein the comparison circuit includes a differential amplifier. 7. The heat exchanger cleaning device according to claim 4, wherein the cleaning liquid supply means includes a motor energized by the drive signal of the comparator and a pump driven by the motor. 8 The cleaning liquid supply means is the first one of the heat exchanger.
5. The heat exchanger cleaning device according to claim 4, further comprising a bench lily tube formed at an inlet into which fluid flows. 9 The cleaning liquid supply means has a first solenoid valve that controls the outflow of liquid in the container containing condensed water and a second solenoid valve that controls the inflow of the cleaning liquid into the heat exchanger, and the first solenoid valve 7. The heat exchanger cleaning device according to claim 6, wherein the second electromagnetic valve is controlled by the output of the differential amplifier. 10. The heat exchanger cleaning device according to any one of claims 6 to 9, wherein the heat exchanger is inclined at a certain angle with respect to the horizontal.
JP24321084A 1984-11-20 1984-11-20 Method and device for cleaning heat exchanger Granted JPS61122497A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24321084A JPS61122497A (en) 1984-11-20 1984-11-20 Method and device for cleaning heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24321084A JPS61122497A (en) 1984-11-20 1984-11-20 Method and device for cleaning heat exchanger

Publications (2)

Publication Number Publication Date
JPS61122497A JPS61122497A (en) 1986-06-10
JPH058360B2 true JPH058360B2 (en) 1993-02-01

Family

ID=17100463

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24321084A Granted JPS61122497A (en) 1984-11-20 1984-11-20 Method and device for cleaning heat exchanger

Country Status (1)

Country Link
JP (1) JPS61122497A (en)

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* Cited by examiner, † Cited by third party
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KR100408243B1 (en) * 2001-10-12 2003-12-01 주식회사 엘지이아이 Device for cleaning and corrosion prevention heat exchanger of air conditioner
EP2270414A1 (en) * 2009-07-03 2011-01-05 Aprovis Energy Systems GmbH Water spray in exhaust heat exchanger to reduce efficiency losses
GB201202339D0 (en) * 2012-02-10 2012-03-28 Caterpillar Motoren Gmbh & Co Exhaust gas cooler
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Publication number Priority date Publication date Assignee Title
JP2011505519A (en) * 2007-12-07 2011-02-24 スカニア シーブイ アクチボラグ Structure and method for returning exhaust gas in a combustion engine
JP2012177375A (en) * 2007-12-07 2012-09-13 Scania Cv Ab Structure for returning exhaust gas in combustion engine
JP2012237235A (en) * 2011-05-11 2012-12-06 Toyota Motor Corp Egr system of internal combustion engine
CN105587411A (en) * 2014-11-11 2016-05-18 福特环球技术公司 Method and system for EGR control

Also Published As

Publication number Publication date
JPS61122497A (en) 1986-06-10

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