JPH10311699A - Sterilizing-washing device of running water part of running water system and attached piping - Google Patents

Sterilizing-washing device of running water part of running water system and attached piping

Info

Publication number
JPH10311699A
JPH10311699A JP12076197A JP12076197A JPH10311699A JP H10311699 A JPH10311699 A JP H10311699A JP 12076197 A JP12076197 A JP 12076197A JP 12076197 A JP12076197 A JP 12076197A JP H10311699 A JPH10311699 A JP H10311699A
Authority
JP
Japan
Prior art keywords
water
running water
valve
pipe
piping
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP12076197A
Other languages
Japanese (ja)
Other versions
JP3671101B2 (en
Inventor
Masahisa Fukahori
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 JP12076197A priority Critical patent/JP3671101B2/en
Publication of JPH10311699A publication Critical patent/JPH10311699A/en
Application granted granted Critical
Publication of JP3671101B2 publication Critical patent/JP3671101B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To ensure that the adhesion of micro-organism to a heat transfer surface and the proliferation of the micro-organism are suppressed easily, to eliminate problems of environmental protection, and to sterilize and wash a running water part and attached piping on the conditions that are also economically advantageous. SOLUTION: Piping 3A and 3B are connected to an inlet and outlet 2B and 2A of a running water part 2 which is indirectly heat exchanged with a heat medium F passing through a heat medium passage 1 in a heat exchanger. There is provided with a communicating pipe 5 which communicates the piping 3A to 3B between the first running water cutoff valve 4A and 4B that are interposed in these pipings 3A and 3B and the inlet and outlet 2B and 2A, so that a circulation loop 6 is formed of a running water part 2, the piping 3A, 3B, and the communicating pipe 5. In the communicating pipe 5, the second running water cutoff valve 7, a gas-liquid separator 8, a drain valve 9, a circulation pump 11, and a water supply system 14 provided with a tapping valve 12 and a water supply tank 13 are interposed, and the communicating pipe 5 is equipped with an ozone generator 15 which supplies ozone gases, so as to supply the ozone gases to the clean water from the water supply tank 3 circulating in a circulation loop 6 to perform sterilization.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、通水系の通水部お
よび付設配管の殺菌洗浄装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for sterilizing and cleaning a water passage of a water passage system and an attached pipe.

【0002】[0002]

【従来の技術】たとえば、図4に示す熱媒体通路1を通
る熱媒体Fと間接熱交換される通水部2が設けられ、こ
の通水部2に水を流す配管3A,3Bが通水部2の入口
2Aと出口2Bに接続されている熱交換器において、配
管3Aから比較的多くの微生物を含む汚水や河川水を通
水部2に供給するように構成した場合、経時により汚水
や河川水に含まれている微生物が通水部2や配管3A,
3Bの内面、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、熱交換効率を低下さ
せることになる。また、食品用の熱交換器のように、配
管3Aから通水部2に清水供給するように構成した場合
でも、大腸菌などのが通水部2や配管3A,3Bの内部
で増殖する虞れも有り得る。
2. Description of the Related Art For example, a water passage 2 for indirect heat exchange with a heat medium F passing through a heat medium passage 1 shown in FIG. 4 is provided, and pipes 3A and 3B for flowing water through the water passage 2 are provided with water passages. In the heat exchanger connected to the inlet 2A and the outlet 2B of the section 2, when the sewage or river water containing a relatively large amount of microorganisms is supplied to the water section 2 from the pipe 3A, the sewage or Microorganisms contained in the river water are used to pass water 2 and pipes 3A,
In some cases, the microorganisms adhere to the inner surface of 3B, that is, the heat transfer surface, proliferate, and generate microbial dirt called slime. The generation of microbial dirt lowers the heat transfer performance and lowers the heat exchange efficiency. Further, even in the case where fresh water is supplied from the pipe 3A to the water passage section 2 like a food heat exchanger, Escherichia coli and the like may grow inside the water passage section 2 and the pipes 3A and 3B. Is also possible.

【0003】そこで、従来は、機械的手段による分解洗
浄やCIPと称される化学薬品および温水を使用した定
置洗浄によってスライムの除去を図っている。しかし、
機械的手段による分解洗浄は、複雑な構造の伝熱面を有
するプレート式熱交換器では、作業が困難な上に有効な
スライムの除去を期待できない。一方、CIPと称され
る化学薬品および温水を使用した定置洗浄は、薬品処理
の問題や温水を確保するためのエネルギー源が必要にな
るので経済的に不利である。しかも、環境への影響を考
慮する必要があるため煩雑であるとともに、有効なスラ
イムの除去を期待できない。また、これら機械的手段と
化学的手段の両者ともに、伝熱面への微生物の付着およ
び微生物の増殖を抑制する効果を期待できない。
Therefore, conventionally, slime has been removed by disassembly cleaning by mechanical means or stationary cleaning using a chemical called CIP and hot water. But,
The disassembly and cleaning by mechanical means is difficult to perform in a plate heat exchanger having a heat transfer surface having a complicated structure, and effective slime removal cannot be expected. On the other hand, stationary cleaning using a chemical called CIP and hot water is economically disadvantageous because of the problem of chemical treatment and the necessity of an energy source for securing hot water. In addition, since it is necessary to consider the effect on the environment, the method is complicated, and effective slime removal cannot be expected. In addition, neither the mechanical means nor the chemical means can be expected to have the effect of suppressing the attachment of microorganisms to the heat transfer surface and the growth of microorganisms.

【0004】[0004]

【発明が解決しようとする課題】すなわち、従来の機械
的手段や化学的手段では、作業が困難で手間がかかる上
に有効なスライムの除去を期待できず、微生物の付着お
よび微生物の増殖を抑制する効果も期待できない。しか
も、化学的手段の場合は、薬品処理の問題や温水を確保
するためのエネルギー源が必要になるので経済的に不利
であり、かつ環境への影響を考慮する必要があるため煩
雑な難点を有している。そこで、本発明は、微生物の付
着および微生物の増殖を容易かつ確実に抑制し、環境保
全上の問題をなくして通水部および付設配管の殺菌洗浄
を行うことができるとともに、経済的にも有利な通水系
の通水部および付設配管の殺菌洗浄装置を提供すること
を目的としている。
That is, conventional mechanical means and chemical means are difficult and time-consuming to work with, and effective slime removal cannot be expected, so that adhesion of microorganisms and growth of microorganisms are suppressed. It cannot be expected to be effective. In addition, chemical means is economically disadvantageous because of the problem of chemical treatment and the necessity of an energy source to secure hot water, and it is necessary to consider the impact on the environment. Have. Therefore, the present invention can easily and surely suppress the adhesion of microorganisms and the growth of microorganisms, and can sterilize and wash the water passage section and the attached piping without the problem of environmental conservation, and are economically advantageous. It is an object of the present invention to provide a sterilization and cleaning device for a water-flowing section of a water-flow system and an attached pipe.

【0005】[0005]

【課題を解決するための手段】前記目的を達成するため
に、本発明は、通水部に水を流す配管が該通水部の出入
口にそれぞれ接続されている通水系において、前記各配
管のそれぞれに第1通水遮断弁が設けられ、この第1通
水遮断弁と前記通水部の出入口の間から前記各配管を連
通させる連通管が設けられて、前記通水部、前記各配管
および連通管により循環ループが形成され、前記連通管
に第2通水遮断弁、気液分離器、排水弁、循環ポンプ、
注水弁と補水槽を設けた補水系が介設されているととも
に、該連通管にオゾンガスを供給するオゾン発生装置を
備え、前記気液分離器の上部に膨脹吸収タンクを連通し
て配置したことを特徴としている。本発明によれば、通
常は、第1通水遮断弁の弁開、第2通水遮断弁と排水弁
および注水弁の弁閉によって行える。一方、第1通水遮
断弁の弁閉、第2通水遮断弁と排水弁の弁開によって、
循環ループ内の水を排出したのち、排水弁を弁閉し、注
水弁を弁開することで、補水系の清水を循環ループ内に
送り込んで、循環ループ内を清水の満水状態にして、注
水弁を弁閉する。ついで循環ポンプを運転して、循環ル
ープ内で清水を循環させるとともに、オゾン発生装置の
運転により循環ループ内にオゾンガスを供給する。循環
ループ内に気泡として供給されたオゾンガスの一部は、
清水に溶け込んで循環しながら殺菌を行う。また、清水
に溶け込まないオゾンガスは気泡の状態で循環しながら
殺菌を行い、通水系の通水部および付設配管のへの微生
物の付着および微生物の増殖を抑制する。他方、オゾン
発生装置の運転により循環ループ内へは連続的にオゾン
ガスが供給される。しかし、余分なオゾンガスおよび空
気は気液分離器によって清水から分離して排出できるの
で、連続的なオゾンガスの供給が可能になる。
In order to achieve the above object, the present invention relates to a water flow system in which pipes for flowing water to a water flow section are respectively connected to inlets and outlets of the water flow section. A first water cutoff valve is provided for each, and a communication pipe for connecting the pipes between the first water cutoff valve and an inlet / outlet of the water passage section is provided, and the water passage section and the pipes are provided. A circulation loop is formed by the communication pipe and a second water cutoff valve, a gas-liquid separator, a drain valve, a circulation pump,
A water replenishment system having a water injection valve and a water refill tank is interposed, an ozone generator for supplying ozone gas to the communication pipe is provided, and an expansion absorption tank is disposed in communication with an upper part of the gas-liquid separator. It is characterized by. According to the present invention, it can be normally performed by opening the first water cutoff valve and closing the second water cutoff valve, the drain valve, and the water injection valve. On the other hand, by closing the first water cutoff valve and opening the second water cutoff valve and the drain valve,
After draining the water in the circulation loop, close the drain valve and open the water injection valve to send fresh water from the rehydration system into the circulation loop, fill the circulation loop with fresh water, and inject water. Close the valve. Then, the circulation pump is operated to circulate fresh water in the circulation loop, and the ozone generator is operated to supply ozone gas into the circulation loop. Part of the ozone gas supplied as bubbles in the circulation loop
Dissolve in clear water and sterilize while circulating. In addition, ozone gas which is not dissolved in fresh water is sterilized while circulating in the form of air bubbles, thereby suppressing the attachment of microorganisms to the water passage section and the attached piping of the water passage system and the growth of microorganisms. On the other hand, the operation of the ozone generator continuously supplies ozone gas into the circulation loop. However, since excess ozone gas and air can be separated and discharged from fresh water by the gas-liquid separator, continuous supply of ozone gas becomes possible.

【0006】[0006]

【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
示す熱交換時の構成図である。なお、図4に示す従来例
と同一もしくは相当部分には、同一符号を付して説明す
る。図1において、熱交換器には、熱媒体通路1を通る
熱媒体Fと間接熱交換される通水部2が設けられ、この
通水部2に水を流す配管3A,3Bが通水部2の入口2
Aと出口2Bに接続されている。配管3Aには第1通水
遮断弁4Aが設けられ、配管3Bには第1通水遮断弁4
Bが設けられている。
An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram at the time of heat exchange showing an embodiment of the present invention. The same or corresponding parts as those in the conventional example shown in FIG. In FIG. 1, the heat exchanger is provided with a water passage 2 for indirect heat exchange with the heat medium F passing through the heat medium passage 1, and pipes 3 </ b> A and 3 </ b> B for flowing water through the water passage 2 are provided with water passages. 2 entrance 2
A and outlet 2B. The pipe 3A is provided with a first water cutoff valve 4A, and the pipe 3B is provided with a first water cutoff valve 4A.
B is provided.

【0007】第1通水遮断弁4A,4Bと通水部2の出
入口2A,2Bの間から配管3A,3Bを連通させる連
通管5が設けられている。したがって、通水部2、配管
3A,3Bおよび連通管5により循環ループ6が形成さ
れる。また、連通管5には、第2通水遮断弁7、気液分
離器8および循環ポンプ11が直列に介設されていると
ともに、気液分離器8と循環ポンプ11の吸込側の間の
連通管5に排水配管3A弁9を介設した排水管10が介
設され、循環ポンプ11の吐出側と配管3Aの間の連通
管5に注水弁12と補水槽13を設けた補水系14が介
設されている。さらに、連通管5にオゾンガスを供給す
るオゾン発生装置15を備えている。このオゾン発生装
置15におけるオゾンガス供給管15Aの先端は、補水
系14と循環ポンプ11の吸込側の間の連通管5に形成
した絞り部5Aに開口している。
A communication pipe 5 is provided between the first water cutoff valves 4A and 4B and the inlets and outlets 2A and 2B of the water flow section 2 to communicate the pipes 3A and 3B. Therefore, a circulation loop 6 is formed by the water passage section 2, the pipes 3A and 3B, and the communication pipe 5. A second water cutoff valve 7, a gas-liquid separator 8, and a circulation pump 11 are provided in series with the communication pipe 5, and a gas passage between the gas-liquid separator 8 and the suction side of the circulation pump 11 is provided. A drainage pipe 10 having a drainage pipe 3A valve 9 inserted in the communication pipe 5 and a water supply system 14 having a water injection valve 12 and a water tank 13 in the communication pipe 5 between the discharge side of the circulation pump 11 and the pipe 3A. Is interposed. Further, an ozone generator 15 for supplying ozone gas to the communication pipe 5 is provided. The end of the ozone gas supply pipe 15A in the ozone generator 15 is open to a throttle 5A formed in the communication pipe 5 between the water supply system 14 and the suction side of the circulation pump 11.

【0008】気液分離器8の上部に膨脹吸収タンク16
が連通して配置されている。この膨脹吸収タンク16の
底部またはその付近のレベルLLと補水槽13の満水水
位HWLとを同じ位置に設定するように、膨脹吸収タン
ク16と補水槽13とを位置決めしてある。補水槽13
の水位は、満水水位HWLは、図示していない水位制御
手段の作動により、常時、満水水位HWLに保持され
る。また、膨脹吸収タンク16の上端部に連通して自動
排気弁17が設けられ、この自動排気弁17の出口は、
排オゾン分解器18を介して系外に通じている。図中、
19、20は逆止弁を示す。
The expansion absorption tank 16 is provided above the gas-liquid separator 8.
Are arranged in communication. The expansion absorption tank 16 and the water refill tank 13 are positioned so that the level LL at or near the bottom of the expansion absorption tank 16 and the full water level HWL of the water refill tank 13 are set at the same position. Water tank 13
The full water level HWL is always maintained at the full water level HWL by the operation of the water level control means (not shown). An automatic exhaust valve 17 is provided in communication with the upper end of the expansion absorption tank 16, and the outlet of the automatic exhaust valve 17 is
It communicates with the outside of the system via a waste ozone decomposer 18. In the figure,
19 and 20 indicate check valves.

【0009】このような構成であれば、図1のように、
第1通水遮断弁4A,4Bを弁開し、第2通水遮断弁7
と排水弁9および注水弁12を弁閉することによって、
実線矢印で示すように、配管3A→通水部2→配管3B
の経路で水を流して、熱交換を実行することができる。
With such a configuration, as shown in FIG.
The first water cutoff valves 4A and 4B are opened, and the second water cutoff valve 7 is opened.
And the drain valve 9 and the water injection valve 12 are closed,
As shown by the solid arrow, pipe 3A → water passage 2 → pipe 3B
The heat exchange can be performed by flowing water through the path.

【0010】一方、定期的に、図2のように、第1通水
遮断弁4A,4Bを弁閉し、第2通水遮断弁7と排水弁
9の弁開によって、循環ループ6内の水を排出したの
ち、図3のように排水弁9を弁閉し、注水弁12を弁開
することで、補水系14の補水槽13に貯留されている
清水を循環ループ6内に送り込んで、循環ループ6内を
清水の満水状態にして、注水弁12を弁閉する。
On the other hand, as shown in FIG. 2, the first water cutoff valves 4A and 4B are periodically closed, and the second water cutoff valve 7 and the drain valve 9 are opened to periodically open the circulation loop 6 as shown in FIG. After discharging the water, the drainage valve 9 is closed and the water injection valve 12 is opened as shown in FIG. 3, whereby the fresh water stored in the water refill tank 13 of the water refill system 14 is sent into the circulation loop 6. Then, the circulation loop 6 is filled with fresh water, and the water injection valve 12 is closed.

【0011】ついで循環ポンプ11を運転して、循環ル
ープ6内で清水を循環させるとともに、オゾン発生装置
15の運転によりオゾンガス供給管15Aから循環ルー
プ6内にオゾンガスを供給する。循環ループ6へのオゾ
ンガスの供給は、オゾンガス供給管15Aの先端を補水
系14と循環ポンプ11の吸込側の間の連通管5に形成
した絞り部5Aに開口していることにより、ここでのエ
ゼクター作用により可能である。また、循環ポンプ11
の吸込側にオゾンガスが供給されることにより、循環ポ
ンプ11内でオゾンガスが攪拌され、オゾン気泡が小さ
くなるため、清水に溶け込み易くなる。
Next, the circulation pump 11 is operated to circulate fresh water in the circulation loop 6, and the ozone generator 15 is operated to supply ozone gas into the circulation loop 6 from the ozone gas supply pipe 15 A. The supply of the ozone gas to the circulation loop 6 is performed by opening the tip of the ozone gas supply pipe 15A to a throttle portion 5A formed in the communication pipe 5 between the water refilling system 14 and the suction side of the circulation pump 11. This is possible by the ejector action. The circulation pump 11
When ozone gas is supplied to the suction side of, the ozone gas is agitated in the circulation pump 11 and ozone bubbles are reduced, so that the ozone gas is easily dissolved in fresh water.

【0012】循環ループ6内に気泡として供給されたオ
ゾンガスの一部は、清水に溶け込んで循環しながら殺菌
を行う。また、清水に溶け込まないオゾンガスは気泡の
状態で循環しながら殺菌を行い、通水部2、配管3A,
3Bの内面への微生物の付着および微生物の増殖を抑制
する殺菌洗浄が実行できる。
A part of the ozone gas supplied as bubbles into the circulation loop 6 is sterilized while being dissolved in fresh water and circulated. In addition, ozone gas which does not dissolve in fresh water is sterilized while circulating in the state of air bubbles, and the water passing part 2, the pipe 3A,
Sterilization and cleaning can be performed to suppress the adhesion of microorganisms to the inner surface of 3B and the growth of microorganisms.

【0013】他方、オゾン発生装置15の運転により循
環ループ6内へは連続的にオゾンガスが供給される。し
かし、余分なオゾンガスは気液分離器8によって清水か
ら分離して、自動排気弁16→排オゾン分解器18の経
路で系外に排出できるので、連続的なオゾンガスの供給
が可能になる。
On the other hand, the operation of the ozone generator 15 continuously supplies ozone gas into the circulation loop 6. However, excess ozone gas can be separated from fresh water by the gas-liquid separator 8 and discharged out of the system through the path from the automatic exhaust valve 16 to the exhaust ozone decomposer 18, so that continuous ozone gas supply becomes possible.

【0014】さらに、循環ループ6内を循環している清
水には、オゾンガスが小さな気泡として混入しているの
で、見かけの清水体積は膨脹により大きくなるが、膨脹
分を膨脹吸収タンク16によって吸収できる。このた
め、循環ループ6の水位は、膨脹吸収タンク6の底部ま
たはその付近のレベルLLより僅かに上昇したレベルで
安定し、この状態を維持して余分なオゾンガスは自動排
気弁16→排オゾン分解器18の経路で系外に排出され
る。
Furthermore, since the ozone gas is mixed as small bubbles into the fresh water circulating in the circulation loop 6, the apparent volume of the fresh water increases due to the expansion, but the expansion can be absorbed by the expansion absorption tank 16. . For this reason, the water level of the circulation loop 6 is stabilized at a level slightly higher than the level LL at or near the bottom of the expansion absorption tank 6, and in this state, the excess ozone gas is removed from the automatic exhaust valve 16 → the exhaust ozone decomposition. It is discharged out of the system through the path of the vessel 18.

【0015】前述の通水部2および付設配管3A,3B
の殺菌洗浄を所定時間実行したのち、循環ポンプ11お
よびオゾン発生装置15の運転を停止し、第2通水遮断
弁7を弁閉したのち、第1通水遮断弁4A,4Bを弁開
することで、図1に示す熱交換可能な状態を得ることが
できる。
The above-mentioned water passage section 2 and attached pipes 3A, 3B
After the germicidal washing is performed for a predetermined time, the operations of the circulation pump 11 and the ozone generator 15 are stopped, the second water cutoff valve 7 is closed, and the first water cutoff valves 4A and 4B are opened. Thus, the heat exchangeable state shown in FIG. 1 can be obtained.

【0016】なお、前記実施の形態では、熱交換器の通
水部2の入口2Aと出口2Bに付設配管3A,3Bを接
続し、配管3Aに第1通水遮断弁4Aを設け、配管3B
に第1通水遮断弁4Bを設けているが、図4に示すよう
に、容器やタンクなどによってなる通水部2を設け、こ
の通水部2の入口2Aと出口2Bに付設配管3A,3B
を接続し、配管3Aに第1通水遮断弁4Aを設け、配管
3Bに第1通水遮断弁4Bを設けてもよい。
In the above embodiment, the attached pipes 3A and 3B are connected to the inlet 2A and the outlet 2B of the water passage 2 of the heat exchanger, and the first water cutoff valve 4A is provided in the pipe 3A, and the pipe 3B
Is provided with a first water cutoff valve 4B, as shown in FIG. 4, a water passage 2 composed of a container, a tank or the like is provided, and attached pipes 3A and 3A are provided at an inlet 2A and an outlet 2B of the water passage 2. 3B
And a first water cutoff valve 4A may be provided in the pipe 3A, and a first water cutoff valve 4B may be provided in the pipe 3B.

【0017】[0017]

【発明の効果】以上説明したように、本発明は、微生物
の付着および微生物の増殖を容易かつ確実に抑制し、環
境保全上の問題をなくして通水部および付設配管の殺菌
洗浄を行うことができるとともに、従来の化学的手段で
必要とされていた薬品処理の問題や温水を確保するため
のエネルギー源が不要になるので経済的にも有利であ
る。
As described above, according to the present invention, the adhesion of microorganisms and the growth of microorganisms can be easily and reliably suppressed, and the sterilization and cleaning of the water passage and the attached pipes can be performed without environmental conservation problems. This is economically advantageous because it eliminates the problem of chemical treatment required by conventional chemical means and the need for an energy source to secure hot water.

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

【図1】本発明の一実施の形態を示す構成図である。FIG. 1 is a configuration diagram showing an embodiment of the present invention.

【図2】循環ループ内の水を排出する時の構成図であ
る。
FIG. 2 is a configuration diagram when water in a circulation loop is discharged.

【図3】循環ループ内を清水にオゾンガスを供給してい
る殺菌時の構成図である。
FIG. 3 is a configuration diagram at the time of sterilization in which ozone gas is supplied to fresh water in a circulation loop.

【図4】本発明の他の実施の形態を示す構成図である。FIG. 4 is a configuration diagram showing another embodiment of the present invention.

【図5】従来例の構成図である。FIG. 5 is a configuration diagram of a conventional example.

【符号の説明】[Explanation of symbols]

1 熱媒体通路 2 通水部 2A 通水部の入口 2B 通水部の出口 3A 配管 3B 配管 4A 第1通水遮断弁 4B 第1通水遮断弁 5 連通管 6 循環ループ 7 第2通水遮断弁 8 気液分離器 9 排水弁 11 循環ポンプ 12 注水弁 13 補水槽 14 補水系 15 オゾン発生装置 16 膨脹吸収タンク F 熱媒体 REFERENCE SIGNS LIST 1 heat medium passage 2 water passage 2A inlet of water passage 2B outlet of water passage 3A pipe 3B pipe 4A first water cutoff valve 4B first water cutoff valve 5 communication pipe 6 circulation loop 7 second water cutoff Valve 8 Gas-liquid separator 9 Drain valve 11 Circulation pump 12 Water injection valve 13 Refill tank 14 Refill system 15 Ozone generator 16 Expansion absorption tank F Heat medium

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 通水部に水を流す配管が該通水部の出入
口にそれぞれ接続されている通水系において、前記各配
管のそれぞれに第1通水遮断弁が設けられ、この第1通
水遮断弁と前記通水部の出入口の間から前記各配管を連
通させる連通管が設けられて、前記通水部、前記各配管
および連通管により循環ループが形成され、前記連通管
に第2通水遮断弁、気液分離器、排水弁、循環ポンプ、
注水弁と補水槽を設けた補水系が介設されているととも
に、該連通管にオゾンガスを供給するオゾン発生装置を
備え、前記気液分離器の上部に膨脹吸収タンクを連通し
て配置したことを特徴とする通水系の通水部および付設
配管の殺菌洗浄装置。
A first water cutoff valve is provided for each of said pipes in a water flow system in which pipes for flowing water to said water flow section are respectively connected to inlets and outlets of said water flow section. A communication pipe is provided for communicating the pipes from between the water shutoff valve and the inlet / outlet of the water communication section, and a circulation loop is formed by the water communication section, the respective pipes, and the communication pipe. Water cutoff valve, gas-liquid separator, drain valve, circulation pump,
A water replenishment system having a water injection valve and a water refill tank is interposed, an ozone generator for supplying ozone gas to the communication pipe is provided, and an expansion absorption tank is disposed in communication with an upper part of the gas-liquid separator. A disinfection and cleaning device for a water passage part and an attached pipe of a water passage system, characterized in that:
JP12076197A 1997-05-12 1997-05-12 Sterilization and cleaning equipment for water flow system and attached piping Expired - Fee Related JP3671101B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12076197A JP3671101B2 (en) 1997-05-12 1997-05-12 Sterilization and cleaning equipment for water flow system and attached piping

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12076197A JP3671101B2 (en) 1997-05-12 1997-05-12 Sterilization and cleaning equipment for water flow system and attached piping

Publications (2)

Publication Number Publication Date
JPH10311699A true JPH10311699A (en) 1998-11-24
JP3671101B2 JP3671101B2 (en) 2005-07-13

Family

ID=14794346

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12076197A Expired - Fee Related JP3671101B2 (en) 1997-05-12 1997-05-12 Sterilization and cleaning equipment for water flow system and attached piping

Country Status (1)

Country Link
JP (1) JP3671101B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013171090A1 (en) * 2012-05-14 2013-11-21 BSH Bosch und Siemens Hausgeräte GmbH Device for the temporary storage of an operating liquid
JP2017219305A (en) * 2017-07-28 2017-12-14 水野ストレーナー工業株式会社 Plate type heat exchanger

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013171090A1 (en) * 2012-05-14 2013-11-21 BSH Bosch und Siemens Hausgeräte GmbH Device for the temporary storage of an operating liquid
JP2017219305A (en) * 2017-07-28 2017-12-14 水野ストレーナー工業株式会社 Plate type heat exchanger

Also Published As

Publication number Publication date
JP3671101B2 (en) 2005-07-13

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