JP2548933B2 - Cleaning method of tube heat exchanger heat transfer tube - Google Patents

Cleaning method of tube heat exchanger heat transfer tube

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Publication number
JP2548933B2
JP2548933B2 JP62070935A JP7093587A JP2548933B2 JP 2548933 B2 JP2548933 B2 JP 2548933B2 JP 62070935 A JP62070935 A JP 62070935A JP 7093587 A JP7093587 A JP 7093587A JP 2548933 B2 JP2548933 B2 JP 2548933B2
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JP
Japan
Prior art keywords
cooling water
cleaning medium
heat exchanger
heat transfer
separator
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP62070935A
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Japanese (ja)
Other versions
JPS63238398A (en
Inventor
伊弘 友保
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Individual
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Individual
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Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は冷却水を使用する冷凍機、空調機器、化学装
置、復水器などの管式熱交換器の伝熱管内の汚れを清掃
するための管式熱交換器伝熱管の清掃方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention cleans dirt in heat transfer tubes of tubular heat exchangers such as refrigerators, air conditioners, chemical devices, and condensers that use cooling water. Method for cleaning a heat transfer tube of a tube heat exchanger for

〔従来の技術〕[Conventional technology]

冷凍機、空調機器、化学装置、復水器などの関式熱交
換器においては、多数の直管状伝熱器を配列した管式熱
交換器が利用されており、高温流体との熱交換のために
冷却水を使用している。冷却水の種類としては淡水や海
水などがある。
In Seki-type heat exchangers such as refrigerators, air conditioners, chemical devices, and condensers, tubular heat exchangers in which a large number of straight tubular heat exchangers are arranged are used, and heat exchange with high-temperature fluid is possible. Uses cooling water for this. Types of cooling water include fresh water and seawater.

熱交換器に冷却水を使用して運転を行っている場合
に、冷却水中の固形物などが作用して伝熱管内の汚れを
進行させて汚れの程度に応じて熱交換器の熱通過率の低
下にともなう冷凍機などの能力の低下をもたらし、ま
た、真空度の低下、伝熱管内水頭損失の増加などが現れ
る。このために、伝熱管内の汚れの程度に応じて伝熱管
内を清掃することが行われていた。
When the cooling water is used for the heat exchanger, solids in the cooling water act to promote the dirt inside the heat transfer tube and the heat transfer rate of the heat exchanger according to the degree of dirt. As a result, the capacity of the refrigerator and the like is reduced, and the degree of vacuum is reduced and the head loss in the heat transfer tube is increased. For this reason, the inside of the heat transfer tube has been cleaned according to the degree of contamination in the heat transfer tube.

従来の管式熱交換器伝熱管の清掃方法としては、管式
熱交換器の運転中に、熱交換器の多数の伝熱管内を冷却
水とともに伝熱管の断面一杯にスポンジゴムボールなど
の清掃媒体を通過させるように循環させて連続的に伝熱
管内を清掃する方法が用いられている。
The conventional method for cleaning the heat exchanger tubes is to clean the inside of many heat exchanger tubes of the heat exchanger together with cooling water while the tube heat exchanger is in operation to clean the cross section of the heat exchanger tubes such as sponge rubber balls. A method is used in which the medium is circulated so as to pass through and the inside of the heat transfer tube is continuously cleaned.

また、清掃媒体も回分的に伝熱管内を通過させて清掃
する方法も提案されており、回分的清掃方法により、多
数の伝熱管のそれぞれに対する清掃媒体の分散を良好に
させて清掃効果を改善するようにすることが出来る。
In addition, a method has also been proposed in which the cleaning medium is also batchwise passed through the heat transfer tube to be cleaned, and the batchwise cleaning method improves the cleaning effect by improving the dispersion of the cleaning medium in each of the multiple heat transfer tubes. You can do it.

さらに、管式熱交換器の入口冷却水管路および出口冷
却水管路とは別に、管路口径が異なるとともに清掃媒体
の上記管路への導入ならびに上記管路から分離,回収の
ための循環する等の循環管路が上記管路の中間部に設け
られており、清掃媒体は上記循環管路より上記入口冷却
水管路へ導入され、また、上記出口冷却水管路より上記
循環管路に循環されて分離,回収が行われる。
Further, in addition to the inlet cooling water pipeline and the outlet cooling water pipeline of the pipe heat exchanger, the diameter of the pipeline is different and the cleaning medium is introduced into the pipeline and circulated for separation and recovery from the pipeline. Is provided in the middle part of the pipeline, the cleaning medium is introduced from the circulation pipeline to the inlet cooling water pipeline, and is circulated from the outlet cooling water pipeline to the circulation pipeline. Separation and recovery are performed.

(例えば、Douglas J.Smith,POWER ENGINEERING",Jul
y,1985,P42および特公昭39−594号公報など。) 〔発明が解決しようとする課題〕 しかしながら、上記従来の管式熱交換器の清掃方法で
は、比較的冷却水量の少い小規模の管式熱交換器に適用
するにあたり、入口冷却水管路および出口冷却水管路の
管路口径が小径となるのにしたがい、上記入口冷却水管
路および出口冷却水管路の管路口径と清掃媒体との直径
比率が著しく減少して上記入口、出口冷却水管路、循環
管路ならびに機器内における清掃媒体の円滑な移動が阻
害されるため分離器への充分な移動が行われず伝熱管内
の清掃を円滑に行うことができないという問題があっ
た。しかも、上記の問題は管式熱交換器の規模が小規模
となるにしたがい著しい困難性を呈していた。
(For example, Douglas J. Smith, POWER ENGINEERING ", Jul
y, 1985, P42 and Japanese Patent Publication No. 39-594. ) [Problems to be Solved by the Invention] However, in the above-described conventional method for cleaning a tubular heat exchanger, when applied to a small-scale tubular heat exchanger with a relatively small amount of cooling water, an inlet cooling water pipe and As the diameter of the outlet cooling water pipeline becomes smaller, the diameter ratio between the diameter of the inlet cooling water pipeline and the diameter of the outlet cooling water pipeline and the cleaning medium is significantly reduced, and the inlet, the outlet cooling water pipeline, Since the smooth movement of the cleaning medium in the circulation pipe and the equipment is obstructed, the movement to the separator is not sufficiently performed, and the heat transfer pipe cannot be smoothly cleaned. In addition, the above problems have been extremely difficult as the size of the tubular heat exchanger is reduced.

さらに、清掃媒体の入口冷却水への混合、伝熱管内の
清掃に引続き、清掃媒体の出口冷却水からの分離、回収
など上記入口、出口冷却水管路、循環管路ならびに機器
内における清掃媒体の円滑な移動を行うために格別のポ
ンプによる強制流動のもとで行うことが発明者によって
提案されたが、前記ポンプを用いることにより配管装置
の密集をはじめとして運転操作を複雑にさせてしまい、
さらに経済性を減少させると言う問題もあった。
Further, following the mixing of the cleaning medium with the inlet cooling water and the cleaning of the inside of the heat transfer tube, the separation and recovery of the cleaning medium from the outlet cooling water, such as the above-mentioned inlet, the outlet cooling water pipeline, the circulation pipeline and the cleaning medium in the equipment. It was proposed by the inventor to perform the movement under forced flow by a special pump for smooth movement, but the use of the pump complicates the operation including the congestion of the piping device,
There was also the problem of reducing economic efficiency.

本発明はこのような従来の問題を解決するものであ
り、小規模の管式熱交換器に適用し得て、入口冷却水管
路および出口冷却水管路内の水流を直接利用して上記入
口、出口冷却水管路、分離器、容器などの機器への清掃
媒体の移動を円滑となし、管式熱交換器の熱交換能力を
向上できるとともに、上記入口、出口冷却水管路以外の
格別の管路およびポンプの使用を省略し得る優れた管式
熱交換器伝熱管の清掃方法を提供することを目的とする
ものである。
The present invention is to solve such a conventional problem, can be applied to a small-scale tubular heat exchanger, the inlet by directly utilizing the water flow in the inlet cooling water pipeline and the outlet cooling water pipeline, The cleaning medium can be smoothly moved to the equipment such as the outlet cooling water pipeline, the separator, and the container, and the heat exchange capacity of the pipe heat exchanger can be improved, and special pipelines other than the above inlet and outlet cooling water pipelines. Another object of the present invention is to provide an excellent method for cleaning a heat transfer tube of a tubular heat exchanger that can omit the use of a pump.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は上記目的を達成するために、管式熱交換器の
伝熱管内に加圧された入口冷却水とともに清掃媒体を通
過させて伝熱管内を清掃する方法において、管式熱交換
器と接続された分離器は、分離器の内部には中間分離材
を有し、分離器の下部には第1の遮断弁を介した第1の
容器と、第1の容器の下部には第2の遮断弁を介した第
2の容器と、を直列に備え、加圧された入口冷却水とと
もに清掃媒体は、上記伝熱管内を通過して付着した汚れ
を清掃した後、上記伝熱管からの加圧された出口冷却水
および清掃媒体との混合流は、上記分離器に導かれ、上
記中間分離財を通過して出口冷却水と清掃媒体とに分離
され、出口冷却水は上記分離器から排出されるととも
に、分離された清掃媒体は第1の遮断弁と第2の遮断弁
との交互開閉作動により形成される上記入口冷却水の上
記分離器への通水遮断状態のもとで移動して、第1の容
器および第2の容器内に順次、下降受容された後、加圧
された上記入口冷却水が清掃部材の受容されている第2
の容器内に混入され、上記入口冷却水および清掃媒体と
の混合流が上記管式熱交換器に直接に導かれるようにし
たものである。
In order to achieve the above object, the present invention provides a method for cleaning the inside of a heat transfer tube by passing a cleaning medium together with inlet cooling water pressurized in the heat transfer tube of the tube heat exchanger, and The connected separator has an intermediate separating material inside the separator, a first container through a first shutoff valve in the lower part of the separator, and a second container in the lower part of the first container. And a second container via a shutoff valve in series, and the cleaning medium together with the pressurized inlet cooling water passes through the inside of the heat transfer tube to clean the adhered dirt, and then from the heat transfer tube. The mixed flow of the pressurized outlet cooling water and the cleaning medium is guided to the separator, passes through the intermediate separation material and is separated into the outlet cooling water and the cleaning medium, and the outlet cooling water is discharged from the separator. The cleaning medium that is discharged and separated is generated by the alternating opening / closing operation of the first shutoff valve and the second shutoff valve. The inlet that is formed is moved under the condition of blocking the passage of the cooling water to the separator, and is sequentially received in the first container and the second container, and then is pressurized. Second cooling water is received by the cleaning member
The mixed flow of the inlet cooling water and the cleaning medium is introduced directly into the tubular heat exchanger.

〔作用〕[Action]

本発明は上記のような構成により次のような作用を有
する。
The present invention has the following effects due to the above-mentioned configuration.

すなわち、清掃媒体は加圧された入口冷却水の水流を
直接利用して強制流動のもとで管式熱交換器の伝熱管内
を通過して清掃が行われて、上記伝熱管内を通過した清
掃媒体は出口冷却水の水流を直接利用して強制流動のも
とで分離器に導かれて出口冷却水と清掃媒体とに分離さ
れて、上記出口冷却水は分離器から排出される。分離さ
れた上記清掃媒体は第1の遮断弁と第2の遮断弁との交
互開閉作動により形成される上記入口冷却水の上記分離
器への通水遮断状態のもとで移動して、第1の容器およ
び第2の容器内に順次、下降受容された後、加圧された
上記入口冷却水が清掃部材の受容されている第2の容器
内に混入され、上記入口冷却水および清掃媒体との混合
流が上記管式熱交換器に直接に導かれて伝熱管内の清掃
が行われる。
That is, the cleaning medium passes through the inside of the heat transfer tube of the tubular heat exchanger under forced flow by directly using the pressurized inlet cooling water flow to be cleaned, and then passes through the inside of the heat transfer tube. The cleaning medium is directly guided to the separator by using the water flow of the outlet cooling water under forced flow to be separated into the outlet cooling water and the cleaning medium, and the outlet cooling water is discharged from the separator. The separated cleaning medium moves under the condition where the inlet cooling water formed by the alternating opening and closing operation of the first shutoff valve and the second shutoff valve is cut off to the separator, After being successively received in the first container and the second container, the pressurized inlet cooling water is mixed into the second container in which the cleaning member is received, and the inlet cooling water and the cleaning medium are received. The mixed flow of and is directly guided to the tube heat exchanger to clean the inside of the heat transfer tube.

このように、管式熱交換器の入口冷却水管路および出
口冷却水管路の管路口径が小径であっても清掃媒体は加
圧された入口冷却水の水流を直接利用して強制流動のも
とで移動させるため、清掃媒体を混合している上記入
口、出口冷却水管路、分離器、容器などにおける滞留な
どを発生させることなく円滑に移動される。
As described above, even if the inlet cooling water pipeline and the outlet cooling water pipeline of the pipe heat exchanger have small diameters, the cleaning medium is forced to flow directly by using the pressurized inlet water flow. Since the cleaning medium is moved, the smooth movement can be achieved without causing retention in the inlet and outlet cooling water pipes, the separator, the container, etc. where the cleaning medium is mixed.

そして、清掃媒体の上記管路への導入ならびに上記管
路からの分離、回収および容器への受容などの操作にお
いては、清掃媒体の移動のための上記入口、出口冷却水
管路以外の格別の循環管路やポンプの使用を省略してい
る。
Then, in operations such as introduction of the cleaning medium into the pipe line, separation from the pipe line, recovery and reception in the container, special circulation other than the inlet and outlet cooling water pipe lines for moving the cleaning medium. The use of pipelines and pumps is omitted.

〔実施例〕〔Example〕

第1図は本発明の一実施例をしめすフローシートであ
る。10は管式熱交換器をしめし、器内には多数の直管状
伝熱管が配列されている。12は入口冷却水管路、16は出
口冷却水管路をそれぞれしめし、入口冷却水が管式熱交
換器10に供給され、熱交換を行った後排出される。13は
入口冷却水管路12の入口部をしめし、また、14は入口冷
却水を加圧し流動させるためのポンプである。伝熱管の
清掃媒体はスポンジゴムボールなどが用いられ、必要に
応じて硬度などの性質の異なるものなどを用いることが
できる。
FIG. 1 is a flow sheet showing an embodiment of the present invention. Reference numeral 10 denotes a tubular heat exchanger, in which a large number of straight tubular heat transfer tubes are arranged. Reference numeral 12 denotes an inlet cooling water pipeline, and 16 denotes an outlet cooling water pipeline. The inlet cooling water is supplied to the pipe heat exchanger 10, and heat is exchanged and then discharged. Reference numeral 13 denotes an inlet portion of the inlet cooling water pipe line 12, and 14 is a pump for pressurizing and flowing the inlet cooling water. As a cleaning medium for the heat transfer tube, a sponge rubber ball or the like is used, and if necessary, those having different properties such as hardness can be used.

入口冷却水は入口部13よりポンプ14を用いて所要の水
頭に加圧されて流れ、後記の第2の容器36内に受容され
ている清掃媒体が入口冷却水管路12中に直接に混入され
て、清掃媒体が分散した流れとなって管式熱交換器10に
導かれ、上記冷却水の流れとともに伝熱管の断面一杯に
清掃媒体が内面に摩擦させながら通過して伝熱管内に付
着した汚れを清掃して出口冷却水として出口冷却水管路
16に排出される。このさい、管式熱交換器10では伝熱管
内の清掃が行われると同時に熱交換作用が継続され、そ
の運転が中断されることがない。
The inlet cooling water flows under pressure from the inlet portion 13 to the required head using the pump 14, and the cleaning medium received in the second container 36 described later is directly mixed into the inlet cooling water pipe line 12. Then, the cleaning medium becomes a dispersed flow and is guided to the tube heat exchanger 10, and the cleaning medium passes through the cross section of the heat transfer tube along with the flow of the cooling water while rubbing against the inner surface and adheres to the inside of the heat transfer tube. Clean the dirt and use it as the outlet cooling water.
Emitted to 16. At this time, in the tube heat exchanger 10, the inside of the heat transfer tube is cleaned, and at the same time, the heat exchange action is continued and the operation thereof is not interrupted.

出口冷却水管路16には分岐器18が設けられており、清
掃媒体が混合されている出口冷却水が分岐器18を通過し
て、清掃媒体を混合している出口冷却水の主流が管路16
の弁50を経て下流側に流れる。
The outlet cooling water pipe 16 is provided with a branching device 18, and the outlet cooling water mixed with the cleaning medium passes through the branching device 18, and the main flow of the outlet cooling water mixed with the cleaning medium is the pipeline. 16
Flows downstream via valve 50.

上記分岐器18は、T字状をなし、内部には図示されな
い分離材を備えており、出口冷却水管路16を管路16aと
後述するバイパス管路17とに分岐させている。
The branching device 18 has a T shape and is provided with a separating member (not shown) inside thereof, and branches the outlet cooling water pipeline 16 into a pipeline 16a and a bypass pipeline 17 described later.

20は出口冷却水の管路16aの端部に設けられた分離器
であり、22,28は分離器20の入口、出口をそれぞれをし
めす。分離器20の内部には中間分離材24を備え、26は中
間部をしめす。また、分離器20は、その下部には第1の
遮断弁30を介した第1の容器32ならびに第1の容器32の
下部には第2の遮断弁34を介した第2の容器36が、順
次、分離器20に直列に接続されていて、垂直円筒状の一
体構造に形成されている。また、第1の遮断弁30および
第2の遮断弁34は相互に交互開閉作動するごとなされて
いる。
Reference numeral 20 denotes a separator provided at the end of the outlet cooling water pipe 16a, and reference numerals 22 and 28 denote an inlet and an outlet of the separator 20, respectively. An intermediate separator 24 is provided inside the separator 20, and 26 indicates an intermediate portion. Further, the separator 20 has a first container 32 via a first shutoff valve 30 at the lower part thereof and a second container 36 via a second shutoff valve 34 at the lower part of the first container 32. .. are sequentially connected in series to the separator 20 and are formed into a vertical cylindrical integral structure. Further, the first shutoff valve 30 and the second shutoff valve 34 are arranged so that they are alternately opened and closed.

前記の出口冷却水は所要の水頭を有して管路16aを流
れ分離器20に導入される。分離器20では中間部26から中
間分離材24を通過し、篩上である清掃媒体と篩下である
出口冷却水とを分離して、出口28より管路16bを通り弁5
2を介して排出され、上記出口冷却水は管路16cを経て系
外の工程に接続される。
The outlet cooling water having the required head is introduced into the separator 20 through the pipe 16a. In the separator 20, the intermediate portion 26 passes through the intermediate separating material 24 to separate the cleaning medium on the sieve from the outlet cooling water under the sieve, and from the outlet 28 through the pipe 16b to the valve 5
The water is discharged via 2 and the outlet cooling water is connected to a process outside the system via a pipe 16c.

分離器20の中間部26に残留された清掃媒体は第1の遮
断弁30の開放と第2の遮断弁34の閉止との交互開閉作動
により、第1の容器32に下降移動、受容され、さらに前
記第1の遮断弁30および第2の遮断弁34の作動切換えに
より、清掃媒体は第1の容器32から第2の容器36に下降
移動、受容される。このさい、ポンプ14を用いて入口冷
却水路12内の加圧された入口冷却水の流れが第1の容器
32および第2の容器36にそれぞれ作用するが第1の遮断
弁30および第2の遮断弁34の交互開閉作用によって分離
器20への通水遮断状態を形成できて、かかる状態のもと
で清掃媒体の第1および第2の容器32,36への受容が行
われる。
The cleaning medium remaining in the intermediate portion 26 of the separator 20 is moved downwardly and received in the first container 32 by the alternating opening / closing operation of opening the first shutoff valve 30 and closing the second shutoff valve 34, Further, by switching the operation of the first shutoff valve 30 and the second shutoff valve 34, the cleaning medium is moved down and received from the first container 32 to the second container 36. At this time, the flow of the pressurized inlet cooling water in the inlet cooling water passage 12 using the pump 14 is changed to the first container.
Although it acts on 32 and the second container 36, respectively, it is possible to form a water cutoff state to the separator 20 by the alternate opening and closing action of the first shutoff valve 30 and the second shutoff valve 34. The cleaning medium is received in the first and second containers 32,36.

40,38は第2の容器36の入口および出口をそれぞれし
めし、弁42,43は入口冷却水管路12において第2の容器3
6の入口40,出口38側に夫々設けられており、また、15は
入口冷却水管路12のバイパス管路をしめし、バイパス管
路15において弁46を備えている。かくして前記の弁42,4
3および46の作動によって入口冷却水は第1および第2
の容器32,36をバイパスされて管式熱交換器10へ導くこ
とができる。
Reference numerals 40 and 38 respectively indicate an inlet and an outlet of the second container 36, and valves 42 and 43 are provided in the inlet cooling water line 12 for the second container 3 respectively.
6 are provided on the inlet 40 side and the outlet 38 side, respectively, and 15 indicates a bypass line of the inlet cooling water line 12, and a valve 46 is provided in the bypass line 15. Thus said valves 42,4
By the operation of 3 and 46, the inlet cooling water becomes the first and second
It is possible to bypass the vessels 32 and 36 of the above and lead them to the tube heat exchanger 10.

さらに上述したように、17は分岐器18を介して出口冷
却水管路16のバイパス管路をしめし、バイパス管路17に
おいて弁57を備えている。上記弁50の閉止と弁57の開放
とにより、分岐器18の分離材によりバイパス管路17には
清掃媒体を含まぬ出口冷却水が分離器20、第1および第
2の容器32,36をバイパスされ、管路16c側と合流されて
系外の工程に接続される。
Further, as described above, 17 indicates the bypass pipe of the outlet cooling water pipe 16 via the branch device 18, and the bypass pipe 17 is provided with the valve 57. Due to the closing of the valve 50 and the opening of the valve 57, the outlet cooling water containing no cleaning medium flows through the separator 20 and the first and second containers 32, 36 in the bypass line 17 due to the separating material of the branching device 18. It is bypassed, merged with the side of the conduit 16c, and connected to a process outside the system.

このようにして、清掃媒体の入口冷却水への混合、伝
熱管内の清掃、清掃媒体の出口冷却水からの分離、回
収、および容器への下降受容などの操作が繰返えされ
る。かくして、管式熱交換器の入口冷却水管路および出
口冷却水管路以外の別の管路を有せず、上記管路口が小
径であっても清掃媒体は加圧された入口冷却水の水流を
直接利用して強制流動のもとで移動されるため、清掃媒
体を混合している上記入口、出口冷却水管路、分離器、
容器などにおける滞留や閉塞などを発生させることなく
その移動を円滑することができる。また、清掃部材は上
記分離器20、第1および第2の容器32,36などの一体構
造内を順次、下降受容して移動されるので、上述の移動
と同様にその移動を円滑にすることができる。したがっ
て、管熱交換器の伝熱管内の清掃を確実に行うことがで
きて、その熱交換能力、冷凍機などの能力を著しく向上
することができる。
In this way, operations such as mixing the cleaning medium with the inlet cooling water, cleaning the inside of the heat transfer tube, separating the cleaning medium from the outlet cooling water, collecting, and receiving the descending medium into the container are repeated. Thus, there is no separate pipeline other than the inlet cooling water pipeline and the outlet cooling water pipeline of the tubular heat exchanger, and even if the pipeline mouth has a small diameter, the cleaning medium can flow the pressurized inlet cooling water flow. Since it is directly used and moved under forced flow, the above-mentioned inlet and outlet cooling water pipes, separators, which are mixing the cleaning medium,
The movement can be facilitated without causing retention or blockage in the container or the like. Further, since the cleaning member is sequentially received and moved downward in the integrated structure of the separator 20, the first and second containers 32, 36, etc., it is possible to smoothly move the cleaning member in the same manner as the above-mentioned movement. You can Therefore, the inside of the heat transfer tube of the tube heat exchanger can be reliably cleaned, and the heat exchange capacity and the capacity of the refrigerator and the like can be significantly improved.

さらに、清掃媒体の上記入口冷却水管路への導入なら
びに上記出口冷却水管路からの分離、回収、および容器
への受容などの操作においては、清掃媒体の移動のため
の上記入口冷却水、出口冷却水管路以外の格別な管路や
ポンプの使用を省略できるため、配管装置の密集をはじ
めとして運転操作を複雑とすることを回避することがで
き、経済的な効果をもたらすことができる。
Further, in the operations such as introduction of the cleaning medium into the inlet cooling water pipeline, separation from the outlet cooling water pipeline, collection, and reception in the container, the inlet cooling water and the outlet cooling water for moving the cleaning medium are used. Since it is possible to omit the use of special pipes or pumps other than the water pipe, it is possible to avoid complicated operation such as crowding of piping devices, and it is possible to bring about an economical effect.

とくに、小規模の管式熱交換器が複数基設置される設
備などにおいては、上記配管やポンプの使用の省略によ
る設備の著しい簡易化を可能とし、経済的効果をさらに
著しく増進させることができる。
In particular, in the case where a small number of pipe-type heat exchangers are installed in a plurality of units, it is possible to remarkably simplify the facilities by omitting the use of the above pipes and pumps, and to further improve the economic effect. .

本発明の実施態様は前記実施例のみ限定されることな
く多くの態様が採用可能であることは勿論である。
Needless to say, the embodiment of the present invention is not limited to the above-mentioned embodiment, and many embodiments can be adopted.

〔発明の効果〕〔The invention's effect〕

本発明は上記実施例より明らかなように、管式熱交換
器の伝熱管内に冷却水とともに清掃媒体を通過させて伝
熱管内を清掃するにあたり、とくに小規模の管式熱交換
器に適用し得て、入口冷却水、出口冷却水管路ならびに
分離器、容器など機器への清掃媒体の移動を円滑にする
ことができて伝熱管内の清掃を確実となし管式熱交換器
の熱交換能力、冷凍機などの能力を向上でき、また、入
口冷却水管路および出口冷却水管路以外に格別な循環管
路やポンプの使用を省略できるため、経済的な効果をも
たらすことができる。
INDUSTRIAL APPLICABILITY As is apparent from the above-described embodiment, the present invention is applied to a small-sized tubular heat exchanger in cleaning the inside of the tubular heat exchanger by passing the cleaning medium together with the cooling water into the tubular heat exchanger. Therefore, it is possible to smoothly move the cleaning medium to the equipment such as the inlet cooling water, the outlet cooling water pipeline and the separator, the container, etc., and the inside of the heat transfer tube is not reliably cleaned. The capacity, the capacity of the refrigerator, etc. can be improved, and the use of a special circulation conduit or pump other than the inlet cooling water conduit and the outlet cooling water conduit can be omitted, so that an economic effect can be brought about.

とくに、小規模の管式熱交換器が複数基設置される設
備などにあっては、上記循環管路やポンプの使用の省略
による設備の著しい簡易化を可能とし、経済的効果をさ
らに著しく増進させることができる。
Especially for equipment with multiple small-scale tubular heat exchangers installed, it is possible to significantly simplify the equipment by omitting the use of the above circulation pipelines and pumps, and to further improve the economic effect. Can be made.

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

第1図は本発明の一実施例における管式熱交換器の伝熱
管の清掃方法のフローシートである。 10……管式熱交換器、12……入口冷却水管路、16……出
口冷却水管路、18……分岐器、20……分離器、30,34…
…第1および第2の遮断弁、32,36……第1および第2
の容器
FIG. 1 is a flow sheet of a method for cleaning a heat transfer tube of a tubular heat exchanger according to an embodiment of the present invention. 10 …… Tube heat exchanger, 12 …… Inlet cooling water pipe, 16 …… Outlet cooling water pipe, 18 …… Brancher, 20 …… Separator, 30,34…
... First and second shutoff valves, 32,36 ... First and second
Container of

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】管式熱交換器の伝熱管内に加圧された入口
冷却水とともに清掃媒体を通過させて伝熱管内を清掃す
る方法において、管式熱交換器と接続された分離器は、
分離器の内部には中間分離材を有し、分離器の下部には
第1の遮断弁を介した第1の容器と、第1の容器の下部
には第2の遮断弁を介した第2の容器と、を直列に備
え、加圧された入口冷却水とともに清掃媒体は、上記伝
熱管内を通過して付着した汚れを清掃した後、上記伝熱
管からの加圧された出口冷却水および清掃媒体との混合
流は、上記分離器に導かれ、上記中間分離材を通過して
出口冷却水と清掃媒体とに分離され、出口冷却水は上記
分離器から排出されるとともに、分離された清掃媒体は
第1の遮断弁と第2の遮断弁との交互開閉作動により形
成される上記入口冷却水の上記分離器への通水遮断状態
のもとで移動して、第1の容器および第2の容器内に順
次、下降受容された後、加圧された上記入口冷却水が清
掃部材の受容されている第2の容器内に混入され、上記
入口冷却水および清掃媒体との混合流が上記管式熱交換
器に直接に導かれることを特徴とする管式熱交換器伝熱
管の清掃方法。
1. A method for cleaning the inside of a heat transfer tube by passing a cleaning medium together with pressurized inlet cooling water into the heat transfer tube of the tube heat exchanger, wherein a separator connected to the tube heat exchanger is ,
The separator has an intermediate separating material, a lower part of the separator has a first container via a first shutoff valve, and a lower part of the first container has a second shutoff valve via a first shutoff valve. 2 container in series, and the cleaning medium together with the pressurized inlet cooling water passes through the heat transfer tube to clean the adhered dirt, and then the pressurized outlet cooling water from the heat transfer tube. And the mixed flow with the cleaning medium is guided to the separator, passes through the intermediate separating material and is separated into the outlet cooling water and the cleaning medium, and the outlet cooling water is discharged from the separator and separated. The cleaning medium moves under the condition where the inlet cooling water is formed by the alternating opening / closing operation of the first shutoff valve and the second shutoff valve to shut off the passage of water to the separator, and the first container And sequentially received in the second container and then the pressurized inlet cooling water is received in the cleaning member. The second is mixed in the vessel, the inlet cooling water and cleaning medium and cleaning method of tube heat exchanger heat transfer tube mixed flow, characterized in that the guided directly to the tube heat exchanger that.
JP62070935A 1987-03-25 1987-03-25 Cleaning method of tube heat exchanger heat transfer tube Expired - Fee Related JP2548933B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62070935A JP2548933B2 (en) 1987-03-25 1987-03-25 Cleaning method of tube heat exchanger heat transfer tube

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62070935A JP2548933B2 (en) 1987-03-25 1987-03-25 Cleaning method of tube heat exchanger heat transfer tube

Publications (2)

Publication Number Publication Date
JPS63238398A JPS63238398A (en) 1988-10-04
JP2548933B2 true JP2548933B2 (en) 1996-10-30

Family

ID=13445862

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62070935A Expired - Fee Related JP2548933B2 (en) 1987-03-25 1987-03-25 Cleaning method of tube heat exchanger heat transfer tube

Country Status (1)

Country Link
JP (1) JP2548933B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN215952338U (en) * 2021-08-02 2022-03-04 山东日照发电有限公司 Disassembly-free backwashing structure and closed water heat exchanger

Also Published As

Publication number Publication date
JPS63238398A (en) 1988-10-04

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