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JP3718055B2 - Operation control method of ozone circulation cleaning device - Google Patents
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JP3718055B2 - Operation control method of ozone circulation cleaning device - Google Patents

Operation control method of ozone circulation cleaning device Download PDF

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Publication number
JP3718055B2
JP3718055B2 JP15939998A JP15939998A JP3718055B2 JP 3718055 B2 JP3718055 B2 JP 3718055B2 JP 15939998 A JP15939998 A JP 15939998A JP 15939998 A JP15939998 A JP 15939998A JP 3718055 B2 JP3718055 B2 JP 3718055B2
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Prior art keywords
water
ozone
circulation
valve
circulation loop
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JP15939998A
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Japanese (ja)
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JPH11351794A (en
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賢久 深堀
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Kubota Corp
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Kubota Corp
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Description

【0001】
【発明の属する技術分野】
本発明は、オゾン循環洗浄装置の運転制御方法に係り、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運転制御方法に関する。
【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6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。また、オゾン分解器17のオゾン分解機能が喪失していなくても、オゾン洗浄処理後の熱交換の再開時に、循環ループ11内の溶存残留オゾンが給水管4から排水管5に流下して、場合によっては給排水管系に悪影響を及ぼすおそれがある。
【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とともに、オゾン洗浄処理後の熱交換の再開時に、循環ループ内の溶存残留オゾンが給水管から排水管に流下するのを防止することができるオゾン循環洗浄装置の運転制御方法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、本発明に係るオゾン循環洗浄装置の運転制御方法は、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、前記通水遮断弁を弁閉したのち、逃がし弁を弁開して前記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た後に逃がし弁を弁閉し、ついで前記循環弁を弁開することによって循環ループを形成し、給水タンクから循環ループに水を補給したのち循環ポンプを運転し、ついでオゾン発生源の運転で発生したオゾンを循環ループに供給して、オゾン溶存水の循環によるオゾン循環洗浄を行ったのちオゾン発生源の運転を停止し、該オゾン発生源の運転停止後にオゾン溶存水の循環を継続して溶存残留オゾンを分解し、ついで循環ポンプの運転を停止し、かつ給水タンクから循環ループへの給水を止めた状態で循環ループに設けられているドレン弁を弁開して循環ループ内の汚れた水を排出し、つぎにドレン弁を弁閉して給水タンクから循環ループに給水したのち、前記循環弁を弁閉しかつ前記通水遮断弁を弁開して熱交換の可能な状態に復帰させる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、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すことで、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、オゾン溶存水の循環によるオゾン循環洗浄を行ったのち、オゾン発生源の運転を停止し、該オゾン発生源の運転停止後にオゾン溶存水の循環を継続して溶存残留オゾンを分解するので、循環ループ内の溶存残留オゾンが給水管から排水管に流下するのを防止することができる。
【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は本発明の実施に適用可能な構成図の一例を示す。なお、図6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。給水タンク21は、給水管22を介して連通管8における循環ポンプ12の吐出側に連通しており、給水管22には給水タンク21側から給水弁23と、連通管8方向への流れのみを許容し、連通管8から給水弁23への流れを遮断する逆止弁24が直列に介設されている。また、連通管8にドレン弁25を介設した排水管26が分岐して設けられている。図中27は気液分離器、28はエアー抜き弁を示す。
【0014】
つぎに、本発明の制御方法について説明する。図1のように、通水遮断弁6、7を弁開し、第1循環弁9、逃がし弁20、給水弁23およびドレン弁25を弁閉した状態で、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を通過させることにより、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オゾン洗浄を実行したい場合には、洗浄開始信号を出力する。出力された洗浄開始信号に基づいて、図2のように通水遮断弁6,7を弁閉したのち、逃がし弁20を弁開して熱交換器本体3の内圧により熱交換器本体3が膨脹していた体積分の水を所定時間(T1)内で逃がす。これにより、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の機能喪失を回避することができる。
【0016】
所定時間(T1)経過時に、図3のように逃がし弁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を形成するとともに、給水弁23を弁開して、給水タンク21から循環ループ11に水を補給し、所定時間(T2)内で循環ループ11に水を充満させ、所定時間(T2)経過時に循環ポンプ12を運転する。循環ポンプ12の運転による吐出圧の影響で、たとえ給水弁23が弁開していても給水タンク21から循環ループ11への給水は遮断される。
【0017】
循環ポンプ12の運転を所定時間(T3)継続することによって、気液分離器27とエアー抜き弁28の経路から循環ループ11内のエアー抜きがなされる。
【0018】
所定時間(T3)経過時にオゾン発生源14の運転を開始して、オゾン発生源14で発生したオゾンを所定時間(T4)内で循環ループ11に供給し、オゾン溶存水を循環させながらオゾン循環洗浄を行う。
【0019】
所定時間(T4)経過時にオゾン発生源14の運転を停止し、循環ポンプ12のみの運転によりオゾン溶存水を所定時間(T5)循環ループ11内で循環させる。これによって、循環ループ11内の溶存残留オゾンを分解する。所定時間(T5)経過時に循環ポンプ12の運転を停止する。
【0020】
所定時間(T5)経過時には、前述のように循環ポンプ12の運転を停止するとともに、図4のように所定時間(T6)給水弁23を弁閉し、かつドレン弁25を弁開する。これにより、循環ループ11内の洗浄済みの汚れた水を排出する。
【0021】
所定時間(T6)経過時に、図5に示すようにドレン弁25を弁閉し、かつ所定時間(T7)給水弁23を弁開して、循環ループ11に水を補給する。
【0022】
所定時間(T7)経過時に、第1循環弁9および給水弁23を弁閉し、通水遮断弁6、7を弁開することで、図1に示す状態、つまり、熱交換器本体3の内部通過水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状態に復帰させることができる。
【0023】
このように、通水遮断弁6、7を弁閉したのち、逃がし弁20を弁開して熱交換器本体3の内圧により熱交換器本体3が膨脹していた体積分の水を逃がすことで、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の機能喪失を回避することができる。また、オゾン溶存水の循環によるオゾン循環洗浄を行ったのち、オゾン発生源14の運転を停止して、オゾン溶存水の循環を継続しつつ溶存残留オゾンを分解するので、循環ループ内の溶存残留オゾンが給水管4から排水管5に流下するのを防止することができるため、給排水管系に悪影響を及ぼすことはない。
【0024】
【発明の効果】
以上説明したように、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、オゾン発生源の運転を停止して、オゾン溶存水の循環を継続しつつ溶存残留オゾンを分解するので、循環ループ内の溶存残留オゾンが給水管から排水管に流下するのを防止することができるため、給排水管系に悪影響を及ぼすことはない。
【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】膨脹弁の弁開による膨脹分逃がし時の状態を示す構成図である。
【図3】循環ループの形成状態と循環ループへの給水状態を示す構成図である。
【図4】循環ループ内の洗浄済み汚水の排出状態を示す構成図である。
【図5】循環ループへの水の補給状態を示す構成図である。
【図6】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
3 熱交換器本体
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
21 給水タンク
22 ドレン弁
F 熱媒体
W 水
S 旋回流
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an operation control method for an ozone circulation cleaning apparatus, and more particularly to an operation control method suitable for reliably suppressing the adhesion and growth of microorganisms on a heat transfer surface of a heat exchange plate.
[0002]
[Prior art]
A conventional ozone circulation cleaning device for a plate heat exchanger is configured as shown in FIG. That is, a heat exchange unit 2 composed of an assembly of a plurality of heat exchange plates 1, 1 is inserted into the heat exchanger body 3, and the heat medium F enters the heat exchange plates 1, 1 from the inlet 2 A of the heat exchange unit 2. Are introduced and passed through, and the heat medium F is led out of the heat exchange unit 2 from the outlet 2B, and water W such as sewage, river water or seawater is passed inside the heat exchanger body 3, and this passage is performed. The water 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.
[0003]
A water supply pipe 4 is connected to the inlet 3 </ b> A of the heat exchanger body 3, a drain pipe 5 is connected to the outlet 3 </ b> B, 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 is interposed. The position immediately downstream of the water shutoff valve 6 in the water supply pipe 4 and the position immediately upstream of the water shutoff valve 7 in the drain pipe 5 are communicated with each other via the communication pipe 8. The communication pipe 8 is allowed to flow only from the first circulation valve 9 and the communication pipe 8 to the water supply pipe 4, and the second circulation valve 10 is constituted by a check valve that blocks the flow from the water supply pipe 4 to the communication pipe 8. Is installed. Accordingly, the circulation loop 11 including the water supply pipe 4, the inside of the heat exchanger body 3, the drain pipe 5 and the communication pipe 8 is formed by closing the water cutoff valves 6 and 7 and opening the first circulation valve 9. Can be configured. A circulation pump 12 is interposed in the communication pipe 8.
[0004]
On the other hand, the ozone generation source 14 communicates with the communication pipe 8 through the ozone supply pipe 15 and the ozone injection ejector 13. For this reason, by operating the circulation pump 12 and the ozone generation source 14 in a 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, since the apparent volume in the circulation loop 11 is increased by injecting ozone, the discharge pipe 18 in which the expansion tank 16 and the ozone decomposer 17 filled with activated carbon are connected in series from the communication pipe 8 is branched. The expansion tank 16 absorbs the volume increase, and the excess gas is led from the top of the expansion tank 16 to the ozonolysis device 17 and discharged. With such a configuration, the circulation loop 11 is opened to the atmosphere.
[0006]
By the way, the water shutoff valves 6 and 7 are opened, the first circulation valve 9 is closed, and water W such as sewage, river water or seawater is allowed to pass through the heat exchanger main body 3, and this passing water 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, sewage, river water, seawater, etc. Microorganisms contained in the water W may grow on the surface of each heat exchange plate 1, 1, that is, the heat transfer surface, to produce microbial dirt called slime. Lowers the heat exchange efficiency.
[0007]
Accordingly, 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 to inject ozone into the circulation loop 11, Ozone treatment that circulates dissolved water removes microbial soil called slime and suppresses the adhesion 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 easy to save time and effort compared to the disinfecting cleaning, the stationary cleaning using chemicals called CIP or the stationary cleaning using hot water. In addition to removing microbial soil called slime, it is possible to suppress the adhesion and growth of microorganisms on the heat transfer surface.
[0009]
[Problems to be solved by the invention]
In this ozone circulation cleaning apparatus, the water shutoff valves 6 and 7 are opened, the first circulation valve 9 is closed, and water W such as sewage, river water or seawater is allowed to pass inside the heat exchanger body 3. In the state where heat is exchanged, a pressure corresponding to the use conditions is applied in the heat exchanger main body 3, and the heat exchanger main body 3 expands with a slight internal pressure. When performing ozone circulation cleaning, first, the water shutoff valves 6 and 7 are closed, then the first circulation valve 9 is opened to form the circulation loop 11, but the first circulation valve 9 is opened. Instantly, the water corresponding 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 the full water and the ozone decomposition function due to the flooding of the ozone decomposer 17. There is a risk of causing loss. Moreover, even if the ozonolysis function of the ozonolysis device 17 is not lost, the dissolved residual ozone in the circulation loop 11 flows down from the water supply pipe 4 to the drain pipe 5 when the heat exchange after the ozone cleaning process is resumed. In some cases, it may adversely affect the water supply and drainage pipe system.
[0010]
Therefore, the present invention prevents the water corresponding to the volume of the heat exchanger body that has been expanded when the circulation loop is formed from overflowing through the expansion tank and the ozonolysis device, An ozone circulating cleaning device that avoids loss of function of the ozone decomposer and prevents dissolved residual ozone in the circulation loop from flowing from the water supply pipe to the drain pipe when resuming heat exchange after the ozone cleaning treatment. The object is to provide an operation control method.
[0011]
[Means for Solving the Problems]
In order to achieve the above object, an operation control method of the ozone circulation cleaning apparatus according to the present invention includes a heat exchange unit including a plurality of heat exchange plates assembled in a heat exchanger body, The heat medium is sequentially introduced into and passed through each heat exchange plate from the inlet, and the heat medium is led out of the heat exchange unit from the outlet, and water is passed through the heat exchanger body. And a heat medium passing through the heat exchange plates are indirectly heat exchanged via the heat transfer surfaces of the heat exchange plates, and a water supply pipe connected to the inlet of the heat exchanger body, and the heat exchanger body A drain pipe connected to the outlet of the water supply pipe, a water cutoff valve interposed in each of the water supply pipe and the drain pipe, the water supply pipe downstream of the water cutoff valve and the drain pipe upstream of the water cutoff valve, And communication pipes that communicate with each other Circulating the water supply pipe, the inside of the heat exchanger body, the drain pipe, and the communication pipe by closing each water cutoff valve and opening a circulation valve interposed in the communication pipe A loop is formed, the circulation pump is operated, and ozone generated from an ozone generation source is supplied to the circulation loop to circulate ozone-dissolved water, and an expansion tank and an ozone decomposer are provided in series in the circulation loop. In the ozone circulation cleaning device for a plate heat exchanger provided with a branched discharge pipe, the water shutoff valve is closed, the relief valve is opened, and the internal pressure of the heat exchanger main body is opened. After releasing the volume of water that had been expanded, the relief valve was closed and then the circulation valve was opened to form a circulation loop. After the water was supplied from the water supply tank to the circulation loop, the circulation pump was turned on. Drive The ozone generated by the operation of the ozone source is supplied to the circulation loop, and after the ozone circulation cleaning by circulating the ozone-dissolved water is performed, the operation of the ozone source is stopped, and the ozone dissolved after the operation of the ozone source is stopped Continue to circulate water to decompose dissolved residual ozone, then stop the operation of the circulation pump, and open the drain valve provided in the circulation loop with the water supply from the water supply tank to the circulation loop stopped. After draining dirty water in the circulation loop, the drain valve is then closed and water is supplied from the water tank to the circulation loop, and then the circulation valve is closed and the water shutoff valve is opened. It is characterized by returning to a replaceable state.
[0012]
According to the present invention, after the water shutoff valve is closed, the relief valve is opened to release the volume of water that has been expanded by the internal pressure of the heat exchanger body, thereby expanding the volume. Water corresponding to a minute can be prevented from overflowing through the expansion tank and the ozonolysis device, and loss of function of the expansion tank and ozonolysis device can be avoided. In addition, after performing ozone circulation cleaning by circulation of ozone-dissolved water, the operation of the ozone generation source is stopped, and after the operation of the ozone generation source is stopped, the circulation of ozone-dissolved water is continued to decompose dissolved residual ozone. It is possible to prevent the dissolved residual ozone in the circulation loop from flowing down from the water supply pipe to the drain pipe.
[0013]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows an example of a configuration diagram applicable to the implementation of the present invention. In addition, the same code | symbol is attached | subjected to the part which is the same as that of the prior art example shown in FIG. 6, or an equivalent, and detailed description is abbreviate | omitted. In FIG. 1, an expansion relief pipe 19 is branched and provided at a position immediately upstream of the first circulation valve 9 in the communication pipe 8, and a relief valve 20 is interposed in the expansion relief pipe 19. The water supply tank 21 communicates with the discharge side of the circulation pump 12 in the communication pipe 8 through the water supply pipe 22, and the water supply pipe 22 only flows from the water supply tank 21 side to the water supply valve 23 and the communication pipe 8. And a check valve 24 that interrupts the flow from the communication pipe 8 to the water supply valve 23 is provided in series. Further, a drain pipe 26 provided with a drain valve 25 is branched from the communication pipe 8. In the figure, 27 indicates a gas-liquid separator, and 28 indicates an air vent valve.
[0014]
Next, the control method of the present invention will be described. As shown in FIG. 1, the water shutoff valves 6 and 7 are opened and the first circulation valve 9, the relief valve 20, the water supply valve 23 and the drain valve 25 are closed, and the heat exchanger main body 3 is opened. By passing water W such as sewage, river water or seawater, the passing water W and the heat medium F passing through the heat exchange plates 1 and 1 are passed through the heat transfer surfaces of the heat exchange plates 1 and 1. Indirect heat exchange.
[0015]
On the other hand, when it is desired to perform ozone cleaning regularly or periodically, a cleaning start signal is output. Based on the output cleaning start signal, the water shutoff valves 6 and 7 are closed as shown in FIG. 2, the relief valve 20 is opened, and the heat exchanger body 3 is moved by the internal pressure of the heat exchanger body 3. The expanded volume of water is allowed to escape within a predetermined time (T1). This prevents the water corresponding to the volume which has been expanded from overflowing through the expansion tank 16 and the ozonolysis device 17, thereby avoiding the loss of function of the expansion tank 16 and the loss of function of the ozonolysis device 17. be able to.
[0016]
When a predetermined time (T1) has elapsed, the relief valve 20 is closed as shown in FIG. 3 and the first circulation valve 9 is opened to form a circulation loop 11 and the water supply valve 23 is opened to supply water. Water is supplied from the tank 21 to the circulation loop 11 to fill the circulation loop 11 with water within a predetermined time (T2), and the circulation pump 12 is operated when the predetermined time (T2) has elapsed. The water supply from the water supply tank 21 to the circulation loop 11 is shut off even if the water supply valve 23 is open due to the influence of the discharge pressure due to the operation of the circulation pump 12.
[0017]
By continuing the operation of the circulation pump 12 for a predetermined time (T3), the air in the circulation loop 11 is vented from the path of the gas-liquid separator 27 and the air vent valve 28.
[0018]
When the predetermined time (T3) elapses, the operation of the ozone generation source 14 is started, ozone generated by the ozone generation source 14 is supplied to the circulation loop 11 within the predetermined time (T4), and ozone circulation is performed while circulating the ozone-dissolved water. Wash.
[0019]
When the predetermined time (T4) elapses, the operation of the ozone generation source 14 is stopped, and the ozone-dissolved water is circulated in the circulation loop 11 by the operation of only the circulation pump 12 for the predetermined time (T5). Thereby, the dissolved residual ozone in the circulation loop 11 is decomposed. When the predetermined time (T5) has elapsed, the operation of the circulation pump 12 is stopped.
[0020]
When the predetermined time (T5) has elapsed, the operation of the circulation pump 12 is stopped as described above, the water supply valve 23 is closed for a predetermined time (T6), and the drain valve 25 is opened as shown in FIG. Thereby, the cleaned dirty water in the circulation loop 11 is discharged.
[0021]
When the predetermined time (T6) has elapsed, the drain valve 25 is closed as shown in FIG. 5 and the water supply valve 23 is opened for a predetermined time (T7) to supply water to the circulation loop 11.
[0022]
When the predetermined time (T7) elapses, the first circulation valve 9 and the water supply valve 23 are closed, and the water cutoff valves 6 and 7 are opened, so that the state shown in FIG. The internal passing water W and the heat medium F passing through each heat exchange plate 1, 1 can be returned to a state where heat exchange is performed indirectly through the heat transfer surface of each heat exchange plate 1, 1.
[0023]
In this way, after closing the water shutoff valves 6 and 7, the relief valve 20 is opened to release the volume of water that the heat exchanger body 3 has expanded due to the internal pressure of the heat exchanger body 3. Thus, it is possible to prevent the water from overflowing through the expansion tank 16 and the ozonolysis device 17, thereby avoiding the loss of the function of the expansion tank 16 and the loss of the function of the ozonolysis device 17. In addition, after performing ozone circulation cleaning by circulation of ozone-dissolved water, the operation of the ozone generation source 14 is stopped, and the dissolved residual ozone is decomposed while continuing the circulation of the ozone-dissolved water. Since ozone can be prevented from flowing down from the water supply pipe 4 to the drain pipe 5, it does not adversely affect the water supply / drain pipe system.
[0024]
【The invention's effect】
As described above, the present invention prevents the water corresponding to the volume of the heat exchanger body that has been expanded when the circulation loop is formed from overflowing through the expansion tank and the ozonolysis device, By circulating the ozone-dissolved water in a state where the loss of the function of the ozone and the function of the ozonolysis device is avoided, the microbial soil called slime is removed, and the operation of the ozone source is stopped and the ozone-dissolved water is stopped. Since the dissolved residual ozone is decomposed while continuing the circulation, the dissolved residual ozone in the circulation loop can be prevented from flowing down from the water supply pipe to the drain pipe, so that the supply / drain pipe system is not adversely affected.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an embodiment of the present invention.
FIG. 2 is a configuration diagram showing a state when an expansion component is released by opening the expansion valve.
FIG. 3 is a configuration diagram showing a formation state of a circulation loop and a water supply state to the circulation loop.
FIG. 4 is a configuration diagram showing a discharged state of cleaned sewage in the circulation loop.
FIG. 5 is a configuration diagram showing a state of supplying water to the circulation loop.
FIG. 6 is a configuration diagram of a conventional example.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Heat exchange plate 2 Heat exchange unit 3 Heat exchanger main body 4 Water supply pipe 5 Drain pipe 6 Water shutoff valve 7 Water shutoff 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 21 Water supply tank 22 Drain valve F Heat medium W Water S Swirl

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、前記通水遮断弁を弁閉したのち、逃がし弁を弁開して前記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た後に逃がし弁を弁閉し、ついで前記循環弁を弁開することによって循環ループを形成し、給水タンクから循環ループに水を補給したのち循環ポンプを運転し、ついでオゾン発生源の運転で発生したオゾンを循環ループに供給して、オゾン溶存水の循環によるオゾン循環洗浄を行ったのちオゾン発生源の運転を停止し、該オゾン発生源の運転停止後にオゾン溶存水の循環を継続して溶存残留オゾンを分解し、ついで循環ポンプの運転を停止し、かつ給水タンクから循環ループへの給水を止めた状態で循環ループに設けられているドレン弁を弁開して循環ループ内の汚れた水を排出し、つぎにドレン弁を弁閉して給水タンクから循環ループに給水したのち、前記循環弁を弁閉しかつ前記通水遮断弁を弁開して熱交換の可能な状態に復帰させることを特徴とするオゾン循環洗浄装置の運転制御方法。A heat exchange unit composed of an assembly of a plurality of heat exchange plates is inserted into the heat exchanger body, and a heat medium is sequentially introduced and passed through each heat exchange plate from the inlet of the heat exchange unit, and heat exchange is performed from the outlet. The heat medium is led out to the outside of the unit, and water is allowed to pass inside the heat exchanger body, and the passing water and the heat medium passing through the heat exchange plates are heat transfer surfaces of the heat exchange plates. Indirect heat exchange via a water supply pipe connected to the inlet of the heat exchanger body, a drain pipe connected to the outlet of the heat exchanger body, and each of these water supply pipe and drain pipe A water shutoff valve, and a communication pipe communicating the water supply pipe on the downstream side of the water shutoff valve and the drain pipe on the upstream side of the water shutoff valve, and closing each of the water shutoff valves, And by opening the circulation valve provided in the communication pipe A circulation loop composed of the water supply pipe, the heat exchanger main body, the drain pipe and the communication pipe is formed, a circulation pump is operated, and ozone generated from an ozone generation source is supplied to the circulation loop to generate ozone. In the ozone circulation cleaning apparatus for a plate heat exchanger, in which the dissolved water is circulated and a discharge pipe in which an expansion tank and an ozone decomposer are connected in series is branched in the circulation loop, After the valve is closed, the relief valve is opened, and after the water of the volume that the body has expanded due to the internal pressure of the heat exchanger body is released, the relief valve is closed, and then the circulation valve is opened. Then, a circulation loop is formed, water is supplied from the water supply tank to the circulation loop, and then the circulation pump is operated. Then, ozone generated by the operation of the ozone generation source is supplied to the circulation loop, and ozone dissolved water is supplied. After performing ozone circulation cleaning by circulation, stop the operation of the ozone generation source, continue the circulation of the ozone dissolved water after the operation of the ozone generation source to decompose the dissolved residual ozone, and then stop the operation of the circulation pump With the water supply from the water supply tank to the circulation loop stopped, the drain valve provided in the circulation loop is opened to discharge dirty water in the circulation loop, and then the drain valve is closed to supply water. An operation control method for an ozone circulation cleaning apparatus, wherein water is supplied from a tank to a circulation loop, and then the circulation valve is closed and the water cutoff valve is opened to return to a heat exchangeable state.
JP15939998A 1998-06-08 1998-06-08 Operation control method of ozone circulation cleaning device Expired - Fee Related JP3718055B2 (en)

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JP15939998A JP3718055B2 (en) 1998-06-08 1998-06-08 Operation control method of ozone circulation cleaning device

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Application Number Priority Date Filing Date Title
JP15939998A JP3718055B2 (en) 1998-06-08 1998-06-08 Operation control method of ozone circulation cleaning device

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JP3718055B2 true JP3718055B2 (en) 2005-11-16

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