Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP3594804B2 - Ozone circulation cleaning equipment for plate heat exchanger - Google Patents
[go: Go Back, main page]

JP3594804B2 - Ozone circulation cleaning equipment for plate heat exchanger - Google Patents

Ozone circulation cleaning equipment for plate heat exchanger Download PDF

Info

Publication number
JP3594804B2
JP3594804B2 JP15939898A JP15939898A JP3594804B2 JP 3594804 B2 JP3594804 B2 JP 3594804B2 JP 15939898 A JP15939898 A JP 15939898A JP 15939898 A JP15939898 A JP 15939898A JP 3594804 B2 JP3594804 B2 JP 3594804B2
Authority
JP
Japan
Prior art keywords
water
heat exchanger
ozone
pipe
heat
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
JP15939898A
Other languages
Japanese (ja)
Other versions
JPH11351793A (en
Inventor
賢久 深堀
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP15939898A priority Critical patent/JP3594804B2/en
Publication of JPH11351793A publication Critical patent/JPH11351793A/en
Application granted granted Critical
Publication of JP3594804B2 publication Critical patent/JP3594804B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、プレート式熱交換器のオゾン循環洗浄装置に係り、さらに詳しくは、熱交換プレートの伝熱面への微生物の付着および増殖を確実に抑制するのに好適なプレート式熱交換器のオゾン循環洗浄装置に関する。
【0002】
【従来の技術】
従来のプレート式熱交換器のオゾン循環洗浄装置は、図3に示すように構成されている。すなわち、複数の熱交換プレート1,1の集合体によってなる熱交換ユニット2が熱交換器本体3に装入され、熱交換ユニット2の入口2Aから各熱交換プレート1,1内に熱媒体Fを順次導入して通過させ、出口2Bから熱交換ユニット2の外部に熱媒体Fを導出させるとともに、熱交換器本体3の内部で下水や河川水あるいは海水などの水Wを通過させ、この通過水Wと各熱交換プレート1,1内を通過する熱媒体Fとが各熱交換プレート1,1の伝熱面を介して間接熱交換される。
【0003】
熱交換器本体3の入口3Aに給水管4が接続され、出口3Bに排水管5が接続されており、給水管4に通水遮断弁6が介設され、排水管5に通水遮断弁7が介設されている。給水管4における通水遮断弁6の直下流位置と排水管5における通水遮断弁7の直上流位置とは、連通管8を介して互いに連通している。連通管8には、第1循環弁9と連通管8から給水管4への流れのみを許容し、給水管4から連通管8への流れを遮断する逆止弁によってなる第2循環弁10が介設されている。したがって、通水遮断弁6、7を弁閉し、第1循環弁9を弁開することで、給水管4、熱交換器本体3の内部、排水管5および連通管8からなる循環ループ11を構成できる。また、連通管8に循環ポンプ12が介設されている。
【0004】
一方、オゾン発生源14は、オゾン供給管15およびオゾン注入用エゼクター13を介して連通管8内に連通している。このため、循環ループ11の形成状態で循環ポンプ12およびオゾン発生源14を運転することにより、循環ループ11内にオゾンが注入(供給)され、オゾン溶存水を循環させることができる。
【0005】
他方、オゾンを注入することによって、循環ループ11内の見かけ上の体積が増すため、連通管8から膨脹タンク16と活性炭を充填したオゾン分解器17とを直列に介設した排出管18を分岐して設け、膨脹タンク16で体積増加分を吸収するとともに、余剰ガスを膨脹タンク16の頂部からオゾン分解器17に導いて排出するようになっている。このような構成によって循環ループ11は大気に開放される。
【0006】
ところで、通水遮断弁6、7を弁開し、第1循環弁9を弁閉して、熱交換器本体3の内部で下水や河川水あるいは海水などの水Wを通過させ、この通過水Wと各熱交換プレート1,1内を通過する熱媒体Fとを各熱交換プレート1,1の伝熱面を介して間接熱交換していると、経時により下水や河川水あるいは海水などの水Wに含まれている微生物が各熱交換プレート1,1の表面、つまり伝熱面に付着して増殖しスライムと称される微生物汚れを生じることがあり、微生物汚れの発生によって伝熱性能が低下して熱交換効率を低下させる。
【0007】
そこで、通水遮断弁6、7を弁閉し、第1循環弁9を弁開して循環ポンプ12およびオゾン発生源14を運転することにより、循環ループ11内にオゾンを注入して、オゾン溶存水を循環させるオゾン処理により、スライムと称される微生物汚れを除去するとともに、伝熱面への微生物の付着および増殖を抑制している。
【0008】
プレート式熱交換器のオゾン循環洗浄装置によれば、分解洗浄やCIPと称される化学薬品を使用した定置洗浄あるいは温水を使用した定置洗浄などと比較して、手間を省いて比較的簡単にスライムと称される微生物汚れを除去するとともに、伝熱面への微生物の付着および増殖を抑制することができる。
【0009】
【発明が解決しようとする課題】
このオゾン循環洗浄装置では、通水遮断弁6、7を弁開し、第1循環弁9を弁閉して熱交換器本体3の内部で下水や河川水あるいは海水などの水Wを通過させて熱交換している状態において、熱交換器本体3内には使用条件に応じた圧力がかかっており、僅かではあるが内圧で熱交換器本体3が膨脹している。オゾン循環洗浄を行う場合、まず、通水遮断弁6、7を弁閉し、つぎに第1循環弁9を弁開して循環ループ11を形成するが、第1循環弁9を弁開した瞬間、熱交換器本体3の膨脹分に相当する水が膨脹タンク16とオゾン分解器17を通って溢れ出て、膨脹タンク16の満水による機能喪失およびオゾン分解器17への浸水によるオゾン分解機能の喪失を招くおそれを有している。
【0010】
そこで、本発明は、循環ループの形成時に熱交換器本体の膨脹していた体積分に相当する水が膨脹タンクとオゾン分解器を通って溢れ出るのを防止して、膨脹タンクの機能喪失およびオゾン分解器の機能喪失を回避することができるとともに、循環ループの形成時における熱交換器本体への循環流体の流入を均等化して、洗浄能力を向上させることができるプレート式熱交換器のオゾン循環洗浄装置を提供することを目的としている。
【0011】
【課題を解決するための手段】
前記目的を達成するために、本発明に係るプレート式熱交換器のオゾン循環洗浄装置は、複数の熱交換プレートの集合体によってなる熱交換ユニットが熱交換器本体に装入され、前記熱交換ユニットの入口から各熱交換プレート内に熱媒体を順次導入して通過させ、出口から熱交換ユニットの外部に前記熱媒体を導出させるとともに、前記熱交換器本体の内部で水を通過させ、この通過水と前記各熱交換プレート内を通過する熱媒体とが各熱交換プレートの伝熱面を介して間接熱交換され、前記熱交換器本体の入口に接続される給水管と、該熱交換器本体の出口に接続される排水管と、これら給水管と排水管のそれぞれに介設した通水遮断弁と、通水遮断弁下流側の前記給水管と通水遮断弁上流側の前記排水管とを互いに連通させた連通管とを備え、前記各通水遮断弁を弁閉し、かつ前記連通管に介設した循環弁を弁開することで、前記給水管、前記熱交換器本体の内部、前記排水管および前記連通管からなる循環ループを形成し、循環ポンプを運転し、かつオゾン発生源で発生させたオゾンを循環ループに供給して、オゾン溶存水を循環させるとともに、該循環ループに膨脹タンクとオゾン分解器を直列に介設した排出管が分岐して設けられているプレート式熱交換器のオゾン循環洗浄装置において、前記各通水遮断弁弁閉時の熱交換器本体の内圧により本体が膨脹していた体積分の水を逃がす逃がし弁を設けるとともに、前記連通管の出口が前記給水管に偏心して接続されて該連通管から給水管に流入した流体に給水管の軸周りの旋回流を発生させるように構成したことを特徴としている。
【0012】
本発明によれば、通水遮断弁を弁閉したのち、まず逃がし弁を弁開して熱交換器本体の内圧により本体が膨脹していた体積分の水を逃がし、つぎに逃がし弁を弁閉し、循環弁を弁開することによって循環ループを形成し、循環ポンプを運転し、かつオゾン発生源で発生させたオゾンを循環ループ供給して、オゾン溶存水を循環させることにより、前記膨脹していた体積分に相当する水が膨脹タンクとオゾン分解器を通って溢れ出るのを防止して、膨脹タンクの機能喪失およびオゾン分解器の機能喪失を回避することができる。また、循環ループの形成時においては、給水管内で軸周りの旋回流が発生し、この旋回流が熱交換器本体に導かれるので、熱交換器本体への循環流体の流入を均等化して洗浄能力を向上させることができる。
【0013】
【発明の実施の形態】
以下、本発明の一実施の形態を図面に基づいて説明する。図1は本発明の一実施の形態を示す構成図、図2は連通管と給水管との関係を示す拡大断面図である。なお、図3に示す従来例と同一もしくは相当部分には、同一符号を付して詳しい説明は省略する。図1および図3において、連通管8における第1循環弁9の直上流位置に膨脹逃がし管19を分岐して設け、この膨脹逃がし管19に逃がし弁20を介設してある。また、連通管8の出口が給水管4に偏心して接続されて連通管8から給水管4に流入した流体に給水管4の軸周りの旋回流Sを発生させるように構成されている。
【0014】
このような構成であれば、通水遮断弁6、7を弁開し、第1循環弁9を弁閉して、熱交換器本体3の内部で下水や河川水あるいは海水などの水Wを通過させることで、この通過水Wと各熱交換プレート1,1内を通過する熱媒体Fとを各熱交換プレート1,1の伝熱面を介して間接熱交換することができる。
【0015】
一方、定時的もしくは定期的に通水遮断弁6、7を弁閉したのち、まず、逃がし弁20を弁開して熱交換器本体3の内圧により本体が膨脹していた体積分の水を膨脹逃がし管19から逃がし、つぎに逃がし弁20を弁閉し、第1循環弁9を弁開することによって循環ループ11を形成し、循環ポンプ12を運転する。ついでオゾン発生源14で発生させたオゾンを循環ループ11に供給して、オゾン溶存水を循環させることにより、前記膨脹していた体積分に相当する水が膨脹タンク16とオゾン分解器17を通って溢れ出るのを防止して、膨脹タンク16の機能喪失およびオゾン分解器17の機能喪失を回避した状態でオゾン溶存水を循環させるオゾン循環洗浄処理を実行して、スライムと称される微生物汚れを除去するとともに、伝熱面への微生物の付着および増殖を抑制することができる。
【0016】
また、循環ループ11の形成時においては、給水管4内で軸周りの旋回流Sが発生し、この旋回流Sが熱交換器本体3に導かれるので、熱交換器本体3への循環流体の流入を均等化して洗浄能力を向上させることができる。
【0017】
なお、前記実施の形態では、連通管8における第1循環弁9の直上流位置に膨脹逃がし管19を分岐して設け、この膨脹逃がし管19に逃がし弁20を介設して説明しているが、図1の仮想線で示すように、排水管5における通水遮断弁7に膨脹逃がし管19を分岐して設け、この膨脹逃がし管19に逃がし弁20を介設してもよい。
【0018】
【発明の効果】
以上説明したように、本発明は、通水遮断弁を弁閉したのち、まず逃がし弁を弁開して熱交換器本体の内圧により本体が膨脹していた体積分の水を逃がし、つぎに逃がし弁を弁閉し、循環弁を弁開することによって循環ループを形成できるので、循環ループの形成時に熱交換器本体の膨脹していた体積分に相当する水が膨脹タンクとオゾン分解器を通って溢れ出るのを防止して、膨脹タンクの機能喪失およびオゾン分解器の機能喪失を回避した状態でオゾン溶存水を循環させることにより、スライムと称される微生物汚れを除去するとともに、伝熱面への微生物の付着および増殖を抑制することができる。また、循環ループの形成時においては、給水管内で軸周りの旋回流を発生させて熱交換器本体に導くようにしているので、熱交換器本体への循環流体の流入を均等化して洗浄能力を向上させることができる。
【図面の簡単な説明】
【図1】本発明の一実施の形態を示す構成図である。
【図2】連通管と給水管との関係を示す拡大断面図である。
【図3】従来例の構成図である。
【符号の説明】
1 熱交換プレート
2 熱交換ユニット
2A 熱交換ユニットの入口
2B 熱交換ユニットの出口
3 熱交換器本体
3A 熱交換器本体の入口
3B 熱交換器本体の出口
4 給水管
5 排水管
6 通水遮断弁
7 通水遮断弁
8 連通管
9 第1循環弁
10 逆止弁(第2循環弁)
11 循環ループ
12 循環ポンプ
14 オゾン発生源
15 オゾン供給管
16 膨脹タンク
17 オゾン分解器
20 逃がし弁
F 熱媒体
W 水
S 旋回流
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to an ozone circulation cleaning device for a plate heat exchanger, and more particularly, to a plate heat exchanger suitable for reliably suppressing the growth and adhesion of microorganisms to the heat transfer surface of a heat exchange plate. The present invention relates to an ozone circulation cleaning device.
[0002]
[Prior art]
A conventional ozone circulation cleaning device for a plate heat exchanger is configured as shown in FIG. That is, the heat exchange unit 2 composed of an aggregate of the plurality of heat exchange plates 1 and 1 is inserted into the heat exchanger body 3 and the heat medium F is introduced into each heat exchange plate 1 and 1 from the inlet 2A of the heat exchange unit 2. The heat medium F is led out of the heat exchange unit 2 from the outlet 2B, and the water W such as sewage, river water, or seawater passes through the heat exchanger main body 3 and passes through the outlet 2B. Indirect heat exchange is performed between the water W and the heat medium F passing through each heat exchange plate 1, 1 via the heat transfer surface of each heat exchange plate 1, 1.
[0003]
A water supply pipe 4 is connected to an inlet 3A of the heat exchanger body 3, a drain pipe 5 is connected to an outlet 3B, a water cutoff valve 6 is interposed in the water supply pipe 4, and a water cutoff valve is connected to the drain pipe 5. 7 are interposed. The position of the water supply pipe 4 immediately downstream of the water cutoff valve 6 and the position of the drainage pipe 5 immediately upstream of the water cutoff valve 7 are in communication with each other via a communication pipe 8. The communication pipe 8 has a first circulation valve 9 and a second circulation valve 10 composed of a check valve that allows only the flow from the communication pipe 8 to the water supply pipe 4 and blocks the flow from the water supply pipe 4 to the communication pipe 8. Is interposed. Therefore, by closing the water cutoff valves 6 and 7 and opening the first circulation valve 9, the circulation loop 11 including the water supply pipe 4, the inside of the heat exchanger body 3, the drainage pipe 5, and the communication pipe 8 is formed. Can be configured. A circulation pump 12 is provided in the communication pipe 8.
[0004]
On the other hand, the ozone generation source 14 communicates with the inside of the communication pipe 8 via the ozone supply pipe 15 and the ozone injecting ejector 13. Therefore, by operating the circulation pump 12 and the ozone generation source 14 in the state where the circulation loop 11 is formed, ozone is injected (supplied) into the circulation loop 11 and the ozone-dissolved water can be circulated.
[0005]
On the other hand, by injecting ozone, the apparent volume in the circulation loop 11 increases, so that the discharge pipe 18 in which the expansion tank 16 and the ozone decomposer 17 filled with activated carbon are interposed in series from the communication pipe 8. The expansion tank 16 absorbs the increased volume, and the excess gas is guided to the ozone decomposer 17 from the top of the expansion tank 16 and discharged. With such a configuration, the circulation loop 11 is opened to the atmosphere.
[0006]
By the way, the water cutoff valves 6 and 7 are opened, the first circulation valve 9 is closed, and the water W such as sewage, river water, or seawater passes inside the heat exchanger body 3. When W and the heat medium F passing through the heat exchange plates 1 and 1 are indirectly heat-exchanged via the heat transfer surfaces of the heat exchange plates 1 and 1, the sewage, river water, seawater, or the like over time. Microorganisms contained in the water W may adhere to the surfaces of the heat exchange plates 1 and 1, that is, heat transfer surfaces, and proliferate to produce microbial dirt called slime. And the heat exchange efficiency decreases.
[0007]
Then, the water shutoff valves 6 and 7 are closed, the first circulation valve 9 is opened, and the circulation pump 12 and the ozone generation source 14 are operated, so that ozone is injected into the circulation loop 11 and ozone is injected. Ozone treatment for circulating dissolved water removes microbial dirt called slime and suppresses the attachment and growth of microorganisms on the heat transfer surface.
[0008]
According to the ozone circulation cleaning device of the plate type heat exchanger, it is relatively simple and requires less labor than disassembly cleaning, stationary cleaning using a chemical called CIP, or stationary cleaning using warm water. Microbial stains called slime can be removed, and adhesion and growth of microorganisms on the heat transfer surface can be suppressed.
[0009]
[Problems to be solved by the invention]
In this ozone circulation cleaning device, the water cutoff valves 6 and 7 are opened, the first circulation valve 9 is closed, and water W such as sewage, river water, or seawater passes inside the heat exchanger body 3. In the state where the heat exchange is performed, a pressure corresponding to the use condition is applied in the heat exchanger main body 3, and the heat exchanger main body 3 is expanded with a slight internal pressure. When performing ozone circulation cleaning, first, the water cutoff valves 6 and 7 are closed, and then the first circulation valve 9 is opened to form a circulation loop 11, but the first circulation valve 9 is opened. At the moment, the water equivalent to the expansion of the heat exchanger body 3 overflows through the expansion tank 16 and the ozone decomposer 17, and the function of the expansion tank 16 is lost due to its fullness and the ozone decomposing function is immersed in the ozone decomposer 17. There is a risk of causing the loss.
[0010]
Therefore, the present invention prevents water corresponding to the expanded volume of the heat exchanger body from overflowing through the expansion tank and the ozone decomposer at the time of forming the circulation loop, so that the function of the expansion tank is lost. The ozone of the plate type heat exchanger which can avoid loss of the function of the ozone decomposer and can equalize the flow of the circulating fluid into the heat exchanger body at the time of forming the circulation loop to improve the cleaning ability. It is an object to provide a circulation cleaning device.
[0011]
[Means for Solving the Problems]
In order to achieve the above object, in the ozone circulation cleaning apparatus for a plate heat exchanger according to the present invention, a heat exchange unit including an aggregate of a plurality of heat exchange plates is inserted into a heat exchanger body, and the heat exchange A heat medium is sequentially introduced and passed into each heat exchange plate from the inlet of the unit, and the heat medium is led out of the heat exchange unit from the outlet, and water is passed inside the heat exchanger body. A water supply pipe connected to an inlet of the heat exchanger main body, wherein the passing water and a heat medium passing through each of the heat exchange plates are indirectly heat-exchanged through a heat transfer surface of each heat exchange plate; A drain pipe connected to the outlet of the vessel body, a water cutoff valve interposed in each of the water supply pipe and the drain pipe, the water supply pipe on the downstream side of the water cutoff valve, and the drainage on the upstream side of the water cutoff valve. A communication pipe that connects the pipes to each other The water supply pipe, the inside of the heat exchanger body, the drain pipe and the communication pipe are provided by closing the respective water cutoff valves and opening the circulation valve interposed in the communication pipe. A circulation loop is formed, a circulation pump is operated, and ozone generated by an ozone generation source is supplied to the circulation loop to circulate ozone-dissolved water. An expansion tank and an ozone decomposer are connected in series to the circulation loop. In the plate-type heat exchanger ozone circulating cleaning device provided with a branching discharge pipe interposed in the main body, the volume of the main body expanded by the internal pressure of the heat exchanger main body when each of the water cutoff valves is closed. In addition to providing a relief valve for releasing water, the outlet of the communication pipe is eccentrically connected to the water supply pipe so that the fluid flowing into the water supply pipe from the communication pipe generates a swirling flow around the axis of the water supply pipe. Characterized by comprising It is.
[0012]
According to the present invention, after closing the water cutoff valve, first, the relief valve is opened to release the volume of water in which the main body has expanded due to the internal pressure of the heat exchanger main body, and then the release valve is opened. The expansion is performed by closing and opening a circulation valve to form a circulation loop, operating a circulation pump, and supplying ozone generated by an ozone generation source in a circulation loop to circulate ozone-dissolved water. It is possible to prevent the water corresponding to the volume that has been flowing out from flowing through the expansion tank and the ozone decomposer, thereby preventing the loss of the function of the expansion tank and the function of the ozone decomposer. Further, when the circulation loop is formed, a swirling flow around the axis is generated in the water supply pipe, and the swirling flow is guided to the heat exchanger main body, so that the inflow of the circulating fluid into the heat exchanger main body is equalized and washed. The ability can be improved.
[0013]
BEST MODE FOR CARRYING OUT THE INVENTION
An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram showing an embodiment of the present invention, and FIG. 2 is an enlarged sectional view showing a relationship between a communication pipe and a water supply pipe. The same or corresponding parts as those of the conventional example shown in FIG. 1 and 3, an expansion relief pipe 19 is provided at a position immediately upstream of the first circulation valve 9 in the communication pipe 8, and a relief valve 20 is provided in the expansion relief pipe 19. Further, the outlet of the communication pipe 8 is eccentrically connected to the water supply pipe 4 so as to generate a swirling flow S around the axis of the water supply pipe 4 in the fluid flowing into the water supply pipe 4 from the communication pipe 8.
[0014]
With such a configuration, the water cutoff valves 6 and 7 are opened, the first circulation valve 9 is closed, and water W such as sewage, river water, or seawater is discharged inside the heat exchanger body 3. The passage allows the indirect heat exchange between the passing water W and the heat medium F passing through the heat exchange plates 1, 1 via the heat transfer surfaces of the heat exchange plates 1, 1.
[0015]
On the other hand, after closing the water cutoff valves 6 and 7 regularly or periodically, first, the relief valve 20 is opened to discharge water of a volume that has been expanded by the internal pressure of the heat exchanger main body 3. A circulation loop 11 is formed by releasing the expansion relief pipe 19, then closing the relief valve 20 and opening the first circulation valve 9 to operate the circulation pump 12. Then, the ozone generated by the ozone generating source 14 is supplied to the circulation loop 11 to circulate the ozone-dissolved water, so that the water corresponding to the expanded volume passes through the expansion tank 16 and the ozone decomposer 17. Ozone circulating washing treatment for circulating ozone-dissolved water in a state where loss of function of the expansion tank 16 and loss of function of the ozone decomposer 17 is prevented by preventing overflow and overflow is performed, and microbial contamination called slime is performed. , And adhesion and growth of microorganisms on the heat transfer surface can be suppressed.
[0016]
When the circulation loop 11 is formed, a swirling flow S around the axis is generated in the water supply pipe 4, and the swirling flow S is guided to the heat exchanger main body 3. And the cleaning ability can be improved by equalizing the inflow of water.
[0017]
In the above-described embodiment, an expansion relief pipe 19 is provided at a position immediately upstream of the first circulation valve 9 in the communication pipe 8, and the expansion relief pipe 19 is provided with a relief valve 20 interposed therebetween. However, as shown by an imaginary line in FIG. 1, an expansion relief pipe 19 may be branched from the water cutoff valve 7 in the drain pipe 5, and a relief valve 20 may be provided in the expansion relief pipe 19.
[0018]
【The invention's effect】
As described above, after closing the water cutoff valve, the present invention first opens the relief valve to release water of the volume in which the main body has expanded due to the internal pressure of the heat exchanger main body, A circulation loop can be formed by closing the relief valve and opening the circulation valve, so that the water corresponding to the expanded volume of the heat exchanger body when the circulation loop is formed passes through the expansion tank and the ozone decomposer. By circulating the ozone-dissolved water in a state where it is prevented from overflowing and avoiding the loss of function of the expansion tank and the function of the ozone decomposer, microbial dirt called slime is removed and heat transfer is performed. Adhesion and growth of microorganisms on the surface can be suppressed. Further, when the circulation loop is formed, a swirling flow around the axis is generated in the water supply pipe to guide the swirling flow to the heat exchanger main body, so that the inflow of the circulating fluid into the heat exchanger main body is equalized and the cleaning capacity is increased. Can be improved.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an embodiment of the present invention.
FIG. 2 is an enlarged sectional view showing a relationship between a communication pipe and a water supply pipe.
FIG. 3 is a configuration diagram of a conventional example.
[Explanation of symbols]
REFERENCE SIGNS LIST 1 heat exchange plate 2 heat exchange unit 2A heat exchange unit inlet 2B heat exchange unit outlet 3 heat exchanger body 3A heat exchanger body inlet 3B heat exchanger body outlet 4 water supply pipe 5 drain pipe 6 water cutoff valve 7 water cutoff valve 8 communication pipe 9 first circulation valve 10 check valve (second circulation valve)
DESCRIPTION OF SYMBOLS 11 Circulation loop 12 Circulation pump 14 Ozone generation source 15 Ozone supply pipe 16 Expansion tank 17 Ozone decomposer 20 Relief valve F Heat medium W Water S Swirling flow

Claims (1)

複数の熱交換プレートの集合体によってなる熱交換ユニットが熱交換器本体に装入され、前記熱交換ユニットの入口から各熱交換プレート内に熱媒体を順次導入して通過させ、出口から熱交換ユニットの外部に前記熱媒体を導出させるとともに、前記熱交換器本体の内部で水を通過させ、この通過水と前記各熱交換プレート内を通過する熱媒体とが各熱交換プレートの伝熱面を介して間接熱交換され、前記熱交換器本体の入口に接続される給水管と、該熱交換器本体の出口に接続される排水管と、これら給水管と排水管のそれぞれに介設した通水遮断弁と、通水遮断弁下流側の前記給水管と通水遮断弁上流側の前記排水管とを互いに連通させた連通管とを備え、前記各通水遮断弁を弁閉し、かつ前記連通管に介設した循環弁を弁開することで、前記給水管、前記熱交換器本体の内部、前記排水管および前記連通管からなる循環ループを形成し、循環ポンプを運転し、かつオゾン発生源で発生させたオゾンを循環ループに供給して、オゾン溶存水を循環させるとともに、該循環ループに膨脹タンクとオゾン分解器を直列に介設した排出管が分岐して設けられているプレート式熱交換器のオゾン循環洗浄装置において、前記各通水遮断弁の弁閉時に熱交換器本体の内圧により本体が膨脹していた体積分の水を逃がす逃がし弁を設けるとともに、前記連通管の出口が前記給水管に偏心して接続されて該連通管から給水管に流入した流体に給水管の軸周りの旋回流を発生させるように構成したことを特徴とするプレート式熱交換器のオゾン循環洗浄装置。A heat exchange unit composed of an aggregate of a plurality of heat exchange plates is inserted into the heat exchanger body, a heat medium is sequentially introduced and passed through each heat exchange plate from an inlet of the heat exchange unit, and heat exchange is performed from an outlet. The heat medium is led out of the unit, water is passed inside the heat exchanger body, and the passing water and the heat medium passing through each heat exchange plate are connected to the heat transfer surface of each heat exchange plate. Is indirectly heat-exchanged via a water supply pipe connected to an inlet of the heat exchanger main body, a drain pipe connected to an outlet of the heat exchanger main body, and provided in each of the water supply pipe and the drain pipe. A water cutoff valve, a communication pipe that connects the water supply pipe on the downstream side of the water cutoff valve and the drainage pipe on the upstream side of the water cutoff valve with each other, and closes each of the water cutoff valves, And by opening the circulation valve interposed in the communication pipe The water supply pipe, the inside of the heat exchanger body, forming a circulation loop consisting of the drainage pipe and the communication pipe, operating a circulation pump, and supplying ozone generated by an ozone generation source to the circulation loop, In the ozone circulation cleaning device of the plate type heat exchanger, the ozone-dissolved water is circulated, and a discharge pipe having an expansion tank and an ozone decomposer arranged in series is branched and provided in the circulation loop. When the shut-off valve is closed, a relief valve is provided to release the volume of water expanded by the internal pressure of the heat exchanger main body due to the internal pressure of the heat exchanger main body. An ozone circulation cleaning apparatus for a plate-type heat exchanger, wherein a swirling flow around an axis of a water supply pipe is generated in a fluid flowing into the water supply pipe.
JP15939898A 1998-06-08 1998-06-08 Ozone circulation cleaning equipment for plate heat exchanger Expired - Fee Related JP3594804B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15939898A JP3594804B2 (en) 1998-06-08 1998-06-08 Ozone circulation cleaning equipment for plate heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15939898A JP3594804B2 (en) 1998-06-08 1998-06-08 Ozone circulation cleaning equipment for plate heat exchanger

Publications (2)

Publication Number Publication Date
JPH11351793A JPH11351793A (en) 1999-12-24
JP3594804B2 true JP3594804B2 (en) 2004-12-02

Family

ID=15692912

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15939898A Expired - Fee Related JP3594804B2 (en) 1998-06-08 1998-06-08 Ozone circulation cleaning equipment for plate heat exchanger

Country Status (1)

Country Link
JP (1) JP3594804B2 (en)

Also Published As

Publication number Publication date
JPH11351793A (en) 1999-12-24

Similar Documents

Publication Publication Date Title
JP3594804B2 (en) Ozone circulation cleaning equipment for plate heat exchanger
JP2015134338A (en) Backwash type filtration device and plate heat exchanger
JP3718057B2 (en) Ozone circulation cleaning system for plate heat exchanger
TWI468234B (en) Washing method of water supply piping for water treatment plant
JP4649667B2 (en) Heat recovery type purification system for ballast water
JP3718055B2 (en) Operation control method of ozone circulation cleaning device
JP2000220992A (en) Ozone circulation cleaning equipment for heat exchanger
CN212222621U (en) Circulating filtering system
CN110207368A (en) Soft water water heater
JP3240248B2 (en) Rust removal device and rust removal method for mold cooling section
JP2000220991A (en) Ozone circulation cleaning equipment for heat exchanger
JPS5832320B2 (en) condenser protection device
CN217082985U (en) Backwashing device for water taking end of surface water source heat pump system
JP2011252627A (en) Water heating device
KR100473683B1 (en) Scale removal apparatus for plate heat changers
JP2000065495A (en) Cleaning method in the pipeline
JPH10311699A (en) Sterilization and cleaning device for water passage and attached piping in water passage system
JPH07294184A (en) Ozone sterilizer in plate heat exchanger
JPH11248373A (en) Heat exchange equipment
CN222159901U (en) Descaling device for water dissolving system
CN215295919U (en) Heat exchange device for landfill leachate treatment
JP3499937B2 (en) Slime stripping method for heat exchanger and slime stripping structure
JP3837211B2 (en) Bathtub cleaning equipment
JP3800489B2 (en) Corrosion prevention device for water circulation system
JP2000234893A (en) Operation control method in ozone circulation cleaning device of heat exchanger

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040816

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040824

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20040901

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

LAPS Cancellation because of no payment of annual fees