JP2007167767A - Fluid passage-washing method, washing device, and washing liquid - Google Patents

Fluid passage-washing method, washing device, and washing liquid Download PDF

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JP2007167767A
JP2007167767A JP2005368947A JP2005368947A JP2007167767A JP 2007167767 A JP2007167767 A JP 2007167767A JP 2005368947 A JP2005368947 A JP 2005368947A JP 2005368947 A JP2005368947 A JP 2005368947A JP 2007167767 A JP2007167767 A JP 2007167767A
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liquid
cleaning
cleaning liquid
pipe
fluid passage
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Seiichiro Deguchi
征一郎 出口
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NIKKAN SETSUBI KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a fluid passage-washing method which solves the problem that an abrasive precipitates and separates from a washing liquid, has an excellent washing effect, and washes a fluid passage without clogging a pipe with an abrasive even if the pipe is small in inner diameter, and to provide a device therefor. <P>SOLUTION: In the fluid passage-washing method and device 1, 10, when a fluid passage 9a having an inner diameter of at least 10 mm is washed, a washing liquid 6 is used, which is obtained by mixing a high specific gravity liquid having a specific gravity of 1.18-1.28 with an abrasive of 50-60 mesh in particle size. When a fluid passage 19a having an inner diameter of at most 10 mm is washed, a washing liquid 16 is used, which is obtained by dissolving SiO<SB>2</SB>and B<SB>2</SB>O<SB>3</SB>in warm water which passes through a laminated layer 23 of silica gel and tourmaline. Then, these washing liquids 6 and 16 are each fed into the fluid passages 9a and 19a, respectively. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、給排水用の配管、蒸気用の配管、空気輸送用の配管、ボイラーや冷却装置などの熱交換器の配管、金型の水冷用の水路などの流体通路の洗浄方法、洗浄装置及び洗浄液に係り、無公害の洗浄液を使用して効率的に管内を洗浄することを可能とした流体通路の洗浄に関するものである。   The present invention relates to a method for cleaning a fluid passage such as a pipe for water supply / drainage, a pipe for steam, a pipe for pneumatic transportation, a pipe for a heat exchanger such as a boiler or a cooling device, a water channel for water cooling of a mold, a cleaning apparatus, and the like The present invention relates to a cleaning liquid, and relates to cleaning of a fluid passage that can efficiently clean the inside of a pipe using a non-polluting cleaning liquid.

流体通路には、スケールや錆が発生したり、水あかやスライムやゴミなどの汚れが付着する。流体通路にこれらの付着物が付着すると、流体の流れが悪くなる問題や、空気輸送量が低下する問題や、熱交換器の熱交換の効率を低下させる問題や金型を冷却する機能が低下する問題などが生じるため、時々流体通路を洗浄する作業が行われている。
従来には、給水管内に圧縮空気を間欠的に送り込んで管内の汚れや錆を剥離させる給水管洗浄装置の発明があった(例えば、特許文献1参照)、しかし管内に不規則な周期で空気及び水の衝撃を生じさせるだけでは洗浄効果に限界があり、短時間の間に高度の洗浄効果を得ることはできない問題を有していた。
また、過酸化水素の稀釈液を洗浄液として循環させつつパルスエアーを給気する配管洗浄装置の発明があった(例えば、特許文献2参照)、しかし過酸化水素は有害であるため、管内を洗浄液で洗浄した後に多量の水で濯ぎ洗浄しなければならない問題と、洗浄液を無害化する処理を必要とする問題を有していた。
また、配管の供給口と吐出口に主タンクと副タンクを設け、主タンクから副タンクに洗浄液を流す工程と、副タンクから主タンクに洗浄液を逆流させる工程とを有する配管洗浄装置の発明があった(例えば、特許文献3参照)、しかし係る発明は主タンクと副タンクの2個のタンクを必要とするため装置が過大となる問題を有していた。
Scale, rust, or dirt such as water, slime or dust adheres to the fluid passage. If these deposits adhere to the fluid passage, problems such as poor fluid flow, reduced air transportation, reduced heat exchange efficiency of the heat exchanger, and reduced mold cooling function Therefore, the work of cleaning the fluid passage is sometimes performed.
Conventionally, there has been an invention of a water supply pipe cleaning device that intermittently sends compressed air into a water supply pipe to peel off dirt and rust in the pipe (see, for example, Patent Document 1), but the air has an irregular cycle in the pipe. Moreover, there is a limit to the cleaning effect only by causing an impact of water, and there is a problem that a high cleaning effect cannot be obtained in a short time.
Further, there has been an invention of a pipe cleaning device that supplies pulsed air while circulating a diluted solution of hydrogen peroxide as a cleaning solution (see, for example, Patent Document 2). However, since hydrogen peroxide is harmful, the inside of the pipe is cleaned. After washing with, there was a problem that it had to be rinsed with a large amount of water and a problem that required a treatment for detoxifying the washing liquid.
Further, an invention of a pipe cleaning apparatus having a main tank and a sub tank at a supply port and a discharge port of a pipe, a step of flowing a cleaning liquid from the main tank to the sub tank, and a step of returning the cleaning liquid from the sub tank to the main tank is provided. However, since the invention requires two tanks, a main tank and a sub tank, there is a problem that the apparatus becomes excessive.

さらに、水、水溶性研磨剤が添加された水、酸性液又は粒径0.1mm以上の硬質研磨粒子が添加された酸性液の内のいずれかを洗浄液として用い、ダイヤフラムポンプにより洗浄液を脈動させつつ液体通路を通過させる洗浄システムの発明があった(例えば、特許文献4参照)。
しかし、単なる水や、水溶性研磨剤が添加された水を洗浄液として使用した場合には短時間の間に高度の洗浄効果を得ることはできない問題を有していた。また、酸性液は有害であるため、管内を洗浄液で洗浄した後に水で濯ぎ洗浄しなければならない問題と、洗浄液を無害化する処理を必要とする問題を有していた。
そこで、非水溶性の研磨剤を混入した洗浄液を使用した流体通路の洗浄方法を試行錯誤したが、研磨剤が沈殿して洗浄液から分離してしまう問題があった。
また、粉体や粒体の研磨剤を混入してなる洗浄液を使用すると、配管の内径が小さな場合は管内に研磨剤が詰まってしまう問題があった。
特開2004−321842号公報 特開2003−24892号公報 特開2000−126707号公報 特開平7−275822号公報
Furthermore, the cleaning liquid is pulsated by a diaphragm pump using either water, water to which a water-soluble abrasive is added, acidic liquid or acidic liquid to which hard abrasive particles having a particle size of 0.1 mm or more are added as a cleaning liquid. There has been an invention of a cleaning system that allows a liquid passage to pass therethrough (see, for example, Patent Document 4).
However, when simple water or water to which a water-soluble abrasive is added is used as a cleaning liquid, there is a problem that a high cleaning effect cannot be obtained in a short time. Further, since the acidic liquid is harmful, it has a problem that the inside of the tube must be rinsed with water and then rinsed with water, and a problem that requires a treatment for rendering the cleaning liquid harmless.
Therefore, although a trial and error was performed on the fluid passage cleaning method using a cleaning liquid mixed with a non-water-soluble abrasive, there was a problem that the abrasive precipitated and separated from the cleaning liquid.
Further, when a cleaning liquid in which a powder or granular abrasive is mixed is used, there is a problem that the abrasive is clogged in the pipe when the inner diameter of the pipe is small.
JP 2004-321842 A JP 2003-24892 A JP 2000-126707 A JP 7-275822 A

本発明は、上記した各問題を解決するためになされたものでその目的とするところは、給水管内に圧縮空気を間欠的に送り込んで管内の汚れや錆を剥離させる給水管洗浄装置の発明や、水又は水溶性研磨剤が添加された水を洗浄液として用いダイヤフラムポンプにより洗浄液を脈動させつつ液体通路を通過させる洗浄システムの発明の有する、洗浄効果に限界があり短時間の間に高度の洗浄効果を得ることはできない問題をなくし、短時間の間に高度の洗浄効果の得られる流体通路の洗浄方法及び洗浄装置を提供することにある。
また、過酸化水素の稀釈液を洗浄液として循環させつつパルスエアーを給気する配管洗浄装置の発明や、酸性液を洗浄液として用いダイヤフラムポンプにより洗浄液を脈動させつつ液体通路を通過させる洗浄システムの発明の有する、管内を洗浄液で洗浄した後に多量の水で濯ぎ洗浄しなければならない問題と洗浄液を無害化する処理を必要とする問題をなくし、簡易な濯ぎ洗浄ですみ洗浄液をそのまま廃棄することが可能な流体通路の洗浄方法及び洗浄装置を提供することにある。
また、配管の供給口と吐出口に主タンクと副タンクを設け、主タンクから副タンクに洗浄液を流す工程と、副タンクから主タンクに洗浄液を逆流させる工程とを有する配管洗浄装置の発明の有する、装置が過大となる問題をなくし単純で小型な装置で流体通路の洗浄を可能とした洗浄方法及び洗浄装置を提供することにある。
また、研磨剤が沈殿してしまい洗浄液から分離してしまう問題のない、流体通路の洗浄に適した洗浄液を使用することにより、最も洗浄効果が高い流体通路の洗浄方法及び洗浄装置を提供することにある。
さらに、配管の内径が小さな場合においても管内に研磨剤が詰まることなく、流体通路の洗浄を可能とした洗浄液を使用することにより、洗浄効果の高い流体通路の洗浄方法及び洗浄装置を提供することにある。
The present invention has been made to solve the above-described problems, and the object of the present invention is to provide an invention for a water supply pipe cleaning device that intermittently sends compressed air into a water supply pipe to remove dirt and rust in the pipe. The cleaning system has a limited cleaning effect and has a high degree of cleaning within a short period of time. The cleaning system has a cleaning effect that uses water or water with a water-soluble abrasive added as a cleaning liquid and pulsates the cleaning liquid with a diaphragm pump and passes through the liquid passage. It is an object of the present invention to provide a fluid passage cleaning method and a cleaning device that can eliminate a problem in which an effect cannot be obtained and can obtain a high cleaning effect in a short time.
Also, an invention of a pipe cleaning apparatus that supplies pulsed air while circulating a diluted solution of hydrogen peroxide as a cleaning liquid, and an invention of a cleaning system that uses an acidic liquid as a cleaning liquid and pulsates the cleaning liquid with a diaphragm pump while passing through the liquid passage The problem of having to rinse and wash with a large amount of water after washing the inside of the tube and the problem of requiring the treatment to make the washing liquid harmless is eliminated, and the washing liquid can be discarded as it is with simple rinsing. It is an object to provide a cleaning method and a cleaning device for a fluid passage.
Also, an invention of a pipe cleaning apparatus comprising a main tank and a sub tank at a supply port and a discharge port of a pipe, a step of flowing a cleaning liquid from the main tank to the sub tank, and a step of returning the cleaning liquid from the sub tank to the main tank. It is an object of the present invention to provide a cleaning method and a cleaning apparatus that eliminates the problem that the apparatus is excessive and that allows the fluid passage to be cleaned with a simple and small apparatus.
Further, the present invention provides a fluid passage cleaning method and a cleaning device having the highest cleaning effect by using a cleaning liquid suitable for cleaning a fluid passage without causing a problem that an abrasive is precipitated and separated from the cleaning liquid. It is in.
Furthermore, the present invention provides a fluid passage cleaning method and a cleaning device having a high cleaning effect by using a cleaning liquid that can clean the fluid passage without clogging the abrasive in the pipe even when the inner diameter of the pipe is small. It is in.

内径10mm以上の径の流体通路を洗浄する場合は、比重1.18〜1.28の水溶液(以下単に「高比重液」という。)に粒度50〜60メッシュの研磨剤の粒子を混入した洗浄液を流体通路に送り込み、流体通路の管内を洗浄液により洗浄し、流体通路を通過した後の洗浄液を液槽に回収する流体通路の洗浄方法及び洗浄装置とする。
また内径10mm以下の流体通路を洗浄する場合は、シリカゲルとトルマリンの積層に温水を通過させて得た、SiOとBを溶かしてなる洗浄液を流体通路に送り込み、流体通路の管内を洗浄液により洗浄し、流体通路を通過した後の洗浄液を液槽に回収する流体通路の洗浄方法及び洗浄装置とする。
When cleaning a fluid passage having an inner diameter of 10 mm or more, a cleaning liquid in which abrasive particles having a particle size of 50 to 60 mesh are mixed in an aqueous solution having a specific gravity of 1.18 to 1.28 (hereinafter simply referred to as “high specific gravity liquid”). Is supplied to the fluid passage, the inside of the pipe of the fluid passage is cleaned with the cleaning liquid, and the cleaning method and the cleaning device for the fluid passage are used to collect the cleaning liquid after passing through the fluid passage in the liquid tank.
When cleaning a fluid passage having an inner diameter of 10 mm or less, a cleaning liquid obtained by dissolving SiO 2 and B 2 O 3 obtained by passing warm water through a laminate of silica gel and tourmaline is sent to the fluid passage, and the inside of the pipe of the fluid passage is A cleaning method and a cleaning device for a fluid passage for cleaning with a cleaning fluid and collecting the cleaning fluid after passing through the fluid passage in a liquid tank.

高比重液に粒度50〜60メッシュの研磨剤の粒子を混入した洗浄液を内径10mm以上の流体通路の管内に、またSiOとBを溶かした洗浄液を内径10mm以下の流体通路の管内に、それぞれ通過させることにより高度の洗浄効果が得られた。
また内径10mm以上の配管に対しては、高比重液に研磨剤を混入させてなる洗浄液を使用したので、研磨剤が沈殿して洗浄液から分離してしまう問題がなくなった。
また内径10mm以下の配管に対しては、水にSiOとBを溶かしてなる洗浄液を使用したので、管内に研磨剤が詰まる問題がなくなった。
また本発明は酸化水素や酸性液を洗浄液として使用しないので、洗浄後の流体通路を多量の水で濯ぎ洗浄する必要がなくなり、さらに、使用後の洗浄液をそのまま廃棄することが可能なため、洗浄作業が楽で自然環境を汚染することがない。
また、配管の供給口と吐出口に主タンクと副タンクを設ける発明の有する設備が過大となる問題をなくし、単一の液槽で流体通路に洗浄液を供給し使用後の洗浄液を回収する装置としたので、単純で小型な設備で可能な流体通路の洗浄方法及び洗浄装置を提供することができた。
また、流体通路の洗浄に最適な研磨剤を使用し、液槽内の洗浄液を攪拌する攪拌装置を設けたので、最も洗浄効果が高い状態を維持することができる、流体通路の洗浄方法及び洗浄装置を提供することができた。
さらに、消石灰や珪砂やソフトセラミックや貝殻の粒子やSiOやBなど自然環境を汚染しないものを研磨剤として使用したため、流体通路を洗浄した後に行う作業であって、流体通路を清浄水で洗う濯ぎ洗浄作業を簡便なものとすることができた。
A cleaning solution in which abrasive particles having a particle size of 50 to 60 mesh are mixed in a high specific gravity solution is placed in a fluid passage tube having an inner diameter of 10 mm or more, and a cleaning solution in which SiO 2 and B 2 O 3 are dissolved is placed in a fluid passage tube having an inner diameter of 10 mm or less. In addition, a high cleaning effect was obtained by passing each of them.
Further, for the pipe having an inner diameter of 10 mm or more, since the cleaning liquid in which the abrasive is mixed into the high specific gravity liquid is used, there is no problem that the abrasive is precipitated and separated from the cleaning liquid.
Also with respect to the inner diameter 10mm or less of the pipe, so it was used cleaning liquid comprising dissolving SiO 2 and B 2 O 3 in water, no longer the problem of abrasive clogging the tube.
In addition, since the present invention does not use hydrogen oxide or acidic liquid as a cleaning liquid, there is no need to rinse and clean the fluid passage after cleaning with a large amount of water, and the cleaning liquid after use can be discarded as it is. Work is easy and does not pollute the natural environment.
Further, the apparatus having the main tank and the sub-tank at the supply port and the discharge port of the piping eliminates the problem that the invention has an excessive problem, and supplies the cleaning liquid to the fluid passage in a single liquid tank and collects the used cleaning liquid Therefore, it was possible to provide a fluid passage cleaning method and a cleaning device that are possible with a simple and small facility.
In addition, since a polishing agent that is optimal for cleaning the fluid passage is used and a stirring device that stirs the cleaning liquid in the liquid tank is provided, the fluid passage cleaning method and cleaning that can maintain the highest cleaning effect The equipment could be provided.
In addition, slaked lime, silica sand, soft ceramic, shell particles, SiO 2 and B 2 O 3 and other materials that do not pollute the natural environment are used as abrasives. The rinsing and washing operation with water was simplified.

請求項1の発明は、流体通路の管内に洗浄液を通過させることにより、前記管内を洗浄する方法であって洗浄液が、高比重液に粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液、または、水にSiOとBを溶かしてなる洗浄液、のいずれかの洗浄液である流体通路の洗浄方法とする。
内径10mm以上の配管については、高比重液に粒度50〜60メッシュの研磨剤の粒
子を混入してなる洗浄液を使用することが好ましい。比重1.18〜1.28の高比重液に粒度50〜60メッシュの研磨剤を混入させると、高比重液の中における研磨剤の沈降速度が遅くなり、研磨剤が長時間にわたり高比重液の中に浮遊する効果が得られるからである。また、60メッシュの篩を通過し50メッシュの篩に乗った粒度の研磨剤を使用した洗浄試験において、高い洗浄効果が得られたからである。
一方、内径10mm以下の配管については、水にSiOとBを溶かしてなる洗浄液を使用することが好ましい。管路の途中で詰まるおそれのない洗浄液であって、高い洗浄効果の得られる洗浄液について洗浄試験した結果、水にSiOとBを溶かした洗浄液を使用した場合に、高い洗浄効果が得られたからである。
請求項2の発明は、流体通路の管内に洗浄液を通過させることにより、前記管内を洗浄する方法であって洗浄液が、水に消石灰を混ぜて得た高比重液に粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液、または、水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液、のいずれかの洗浄液である流体通路の洗浄方法とする。
消石灰は水溶性があり、安価であってそのまま廃棄しても自然環境を汚染することがないため、水を高比重化する材料として好ましいからである。
また、水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液を使用した洗浄試験の結果、高い洗浄効果が得られたからである。
請求項3の発明は、流体通路の配管の管内に洗浄液を通過させることにより、前記管内を洗浄する方法であって洗浄液が、水に5μmのサイズの消石灰を混ぜて得た高比重液に、重量比で5〜20%の量の研磨剤の粒子であって、粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液、または、水にSiOを65〜75ppm含み、かつ、Bを25〜33ppm含む洗浄液、のいずれかの洗浄液である流体通路の洗浄方法とする。 5μmのサイズの消石灰は水を高比重化することに適していて、5μmのサイズまでは紙フィルタを使用して濾過することができる。濾過することにより洗浄液から消石灰を取り出して再使用することができると共に、使用後に廃棄する洗浄液に消石灰が含まれないため、さらに自然環境に優しく経済的だからである。
また、水にSiOを65〜75ppm含み、かつ、Bを25〜33ppm含む洗浄液を使用した洗浄試験の結果、さらに高い洗浄効果が得られたからである。
The invention according to claim 1 is a method of cleaning the inside of the pipe by passing the cleaning liquid through the pipe of the fluid passage, and the cleaning liquid is mixed with abrasive particles having a particle size of 50 to 60 mesh in the high specific gravity liquid. A fluid path cleaning method is a cleaning liquid or a cleaning liquid obtained by dissolving SiO 2 and B 2 O 3 in water.
For piping having an inner diameter of 10 mm or more, it is preferable to use a cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh in a high specific gravity liquid. When an abrasive having a particle size of 50 to 60 mesh is mixed in a high specific gravity liquid having a specific gravity of 1.18 to 1.28, the settling rate of the abrasive in the high specific gravity liquid is slowed down, and the abrasive becomes a high specific gravity liquid for a long time. It is because the effect which floats in is obtained. In addition, a high cleaning effect was obtained in a cleaning test using an abrasive having a particle size that passed through a 60-mesh sieve and mounted on a 50-mesh sieve.
On the other hand, for a pipe having an inner diameter of 10 mm or less, it is preferable to use a cleaning liquid obtained by dissolving SiO 2 and B 2 O 3 in water. As a result of a cleaning test on a cleaning liquid that does not clog in the middle of a pipeline and has a high cleaning effect, a high cleaning effect is obtained when a cleaning liquid in which SiO 2 and B 2 O 3 are dissolved in water is used. Because it was obtained.
The invention of claim 2 is a method of cleaning the inside of the pipe by passing the cleaning liquid through the pipe of the fluid passage. The cleaning liquid is polished to a high specific gravity liquid obtained by mixing slaked lime with water and having a particle size of 50 to 60 mesh. A cleaning method for a fluid passage which is either a cleaning liquid obtained by mixing agent particles or a cleaning liquid containing 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water.
This is because slaked lime is water-soluble, is inexpensive, and does not pollute the natural environment even if discarded as it is, and therefore is preferred as a material for increasing the specific gravity of water.
Also it includes 50~80ppm the SiO 2 in water, and, B 2 O 3 cleaning test results using a cleaning solution containing 20~35ppm a is because high cleaning effect was obtained.
The invention of claim 3 is a method of cleaning the inside of the pipe by passing the cleaning liquid through the pipe of the fluid passage pipe. The cleaning liquid is a high specific gravity liquid obtained by mixing slaked lime having a size of 5 μm with water. a particle of 5-20% of the amount of abrasive by weight, the washing solution made by mixing the particles of particle size 50 to 60 mesh abrasives or comprises 65~75ppm the SiO 2 in water, and, B A cleaning method for a fluid passage which is a cleaning liquid of any one of 25 to 33 ppm of 2 O 3 is used. Slaked lime with a size of 5 μm is suitable for increasing the specific gravity of water, and up to a size of 5 μm can be filtered using a paper filter. This is because slaked lime can be taken out from the cleaning liquid by filtration and reused, and since the slaked lime is not contained in the cleaning liquid discarded after use, it is further friendly to the natural environment and economical.
Further, as a result of a cleaning test using a cleaning liquid containing 65 to 75 ppm of SiO 2 and 25 to 33 ppm of B 2 O 3 in water, a higher cleaning effect was obtained.

請求項4の発明は、高比重液に粒度が50〜60メッシュの研磨剤の粒子を混入してなる洗浄液を液槽に貯蔵し、ダイヤフラムポンプを使用して前記洗浄液を流体通路の管内に送り、前記管内を通過した洗浄液を再び前記液槽に回収するようにし、前記流体通路の管内に前記洗浄液を循環させることにより、前記管内を洗浄する流体通路の洗浄方法とする。 高比重液の中では粒度50〜60メッシュの研磨剤の沈降速度が遅く、長時間にわたり研磨剤が高比重液の中に浮遊するため、高い洗浄効果が得られるからである。
また、粒度の大きな研磨剤を含んだ洗浄剤を配管に送り込むためにはダイヤフラムポンプが適しており、ダイヤフラムポンプを使用すると洗浄剤が配管通路の中で間欠的に脈動するため、高い洗浄効果が得られるため好ましいからである。
請求項5の発明は、水に5μmのサイズの消石灰を混ぜて得た高比重液に、重量比で5〜20%の量の研磨剤の粒子であって、粒度が50〜60メッシュの研磨剤の粒子を混入してなる洗浄液を液槽に貯蔵し、ダイヤフラムポンプを使用して前記洗浄液を流体通路の管内に送り、前記管内を通過した洗浄液を再び前記液槽に回収するようにし、前記流体通路の管内に前記洗浄液を循環させることにより、前記管内を洗浄する流体通路の洗浄方法とする。
消石灰は水溶性があり安価であって自然環境を汚染することもない。また、5μmのサイズの消石灰は水を高比重化することに適していて、紙フィルタを使用して濾過することにより洗浄液から取り出すことができるからである。
研磨剤の混入量としては、高比重液に対して重量比で5〜20%の研磨剤を混入することが好ましく、さらには10〜20%の研磨剤を混入すると高い洗浄効果が得られる。
請求項6の発明は、洗浄液を貯蔵可能な液槽と、前記液槽に貯蔵した洗浄液であって、高比重液に粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液と、前記洗浄液を流体通路の管内に送りさらに前記管内を通過した洗浄液を前記液槽まで回収するダイヤフラムポンプとを有する流体通路の洗浄装置とする。
液槽は洗浄液の貯蔵に適していればよい。ダイヤフラムポンプはスプールの移動に伴いダイヤフラムが動いて、2つの材料室を順次加減圧して洗浄液の吸引と圧送を繰り返し行うものである。ダイヤフラムポンプは粒度の大きな研磨剤を含んだ洗浄剤を間欠的に送ることに適しているため使用したものである。
液槽とダイヤフラムポンプの2つの材料室の間及びダイヤフラムポンプの吐出口と流体通路の入り口の間を配管で接続し、さらに流体通路の出口と液槽とを配管で接続する構成とする。
According to a fourth aspect of the present invention, a cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh with a high specific gravity liquid is stored in a liquid tank, and the cleaning liquid is sent into a pipe of a fluid passage using a diaphragm pump. The cleaning liquid that has passed through the pipe is again collected in the liquid tank, and the cleaning liquid is circulated in the pipe of the fluid path, thereby cleaning the inside of the pipe. This is because, in the high specific gravity liquid, the settling speed of the abrasive having a particle size of 50 to 60 mesh is slow and the abrasive floats in the high specific gravity liquid for a long time, so that a high cleaning effect can be obtained.
In addition, diaphragm pumps are suitable for sending cleaning agents containing abrasives with a large particle size into the pipes. When diaphragm pumps are used, the cleaning agent pulsates intermittently in the pipe passages, so it has a high cleaning effect. This is because it is preferable.
The invention according to claim 5 is a high specific gravity liquid obtained by mixing slaked lime having a size of 5 μm with water, and abrasive particles having an amount of 5 to 20% by weight and having a particle size of 50 to 60 mesh. The cleaning liquid in which the agent particles are mixed is stored in the liquid tank, and the cleaning liquid is sent into the pipe of the fluid passage using a diaphragm pump, and the cleaning liquid that has passed through the pipe is again collected in the liquid tank, A fluid passage cleaning method for cleaning the inside of the pipe by circulating the cleaning liquid in the pipe of the fluid path.
Slaked lime is water-soluble, inexpensive and does not pollute the natural environment. Further, slaked lime having a size of 5 μm is suitable for increasing the specific gravity of water, and can be taken out from the cleaning liquid by filtering using a paper filter.
As the amount of the abrasive mixed, it is preferable to mix 5 to 20% of the abrasive in a weight ratio with respect to the high specific gravity liquid. Further, when 10 to 20% of the abrasive is mixed, a high cleaning effect can be obtained.
The invention of claim 6 is a liquid tank capable of storing a cleaning liquid, a cleaning liquid stored in the liquid tank, wherein the cleaning liquid is formed by mixing abrasive particles having a particle size of 50 to 60 mesh in a high specific gravity liquid, The fluid passage cleaning device includes a diaphragm pump that sends the cleaning liquid into the pipe of the fluid passage and collects the cleaning liquid that has passed through the pipe to the liquid tank.
The liquid tank only needs to be suitable for storing the cleaning liquid. In the diaphragm pump, the diaphragm moves as the spool moves, and the two material chambers are sequentially pressurized and depressurized to repeatedly suck and pump the cleaning liquid. The diaphragm pump is used because it is suitable for intermittently sending a cleaning agent containing a polishing agent having a large particle size.
The two material chambers of the liquid tank and the diaphragm pump, the discharge port of the diaphragm pump and the inlet of the fluid passage are connected by piping, and the outlet of the fluid passage and the liquid tank are connected by piping.

請求項7の発明は、洗浄液を貯蔵可能な液槽と、前記液槽に貯蔵した洗浄液であって、水に5μmのサイズの消石灰を混ぜて得た高比重液に、重量比で5〜20%の量の研磨剤の粒子であって、粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液と、前記洗浄液を流体通路の管内に送りさらに前記管内を通過した洗浄液を前記液槽まで回収するダイヤフラムポンプと、前記液槽に貯蔵した洗浄液を攪拌する攪拌装置とを有する流体通路の洗浄装置とする。
消石灰は水溶性があり、安価であって、自然環境を汚染することもない。また、5μmのサイズの消石灰は水を高比重化することに適しており、紙フィルタを使用して濾過することにより、洗浄液から取り出すことができるからである。
高比重液の中であっても長時間経過するに従い徐々に研磨剤などの混入物が沈降して洗浄液から分離してしまうため、液槽に洗浄液を攪拌する攪拌装置を設けて研磨剤などの混入物が沈降することを防ぐようにしたものである。
攪拌装置としては、洗浄液の中で板や棒を機械的に回転させる構成や、洗浄液の中で板や棒を往復移動させる構成や、洗浄液の下部から圧縮空気などを吹き出させて洗浄液に上昇流を発生させる構成などが好ましい。
このとき、高比重液に対して重量比で5〜20%の研磨剤を混入することが好ましく、さらに10〜20%の研磨剤を混入すると高い洗浄効果が得られる。
請求項8の発明は、高比重液に粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液とする。
試験の結果60メッシュの篩を通過し50メッシュの篩に乗った粒度の研磨剤を混入した洗浄液が、高い洗浄効果が得られる洗浄液であることが得られたからである。
請求項9の発明は、水に消石灰を混ぜて得た高比重液に、粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液とする。
消石灰は水溶性があり、安価であってそのまま廃棄しても自然環境を汚染することがないため使用したものである。
Invention of Claim 7 is the liquid tank which can store a washing | cleaning liquid, and the washing | cleaning liquid stored in the said liquid tank, Comprising: It is 5-20 by weight ratio in the high specific gravity liquid obtained by mixing slaked lime of the size of 5 micrometers into water. % Of abrasive particles containing 50 to 60 mesh of abrasive particles, and the cleaning liquid sent to the pipe of the fluid passage and further passed through the pipe. The fluid passage cleaning device includes a diaphragm pump that collects the cleaning liquid and a stirring device that stirs the cleaning liquid stored in the liquid tank.
Slaked lime is water-soluble, inexpensive, and does not pollute the natural environment. Moreover, slaked lime having a size of 5 μm is suitable for increasing the specific gravity of water, and can be taken out from the cleaning liquid by filtering using a paper filter.
Even in high specific gravity liquids, contaminants such as abrasives gradually settle and separate from the cleaning liquid over a long period of time, so a stirring device for stirring the cleaning liquid is provided in the liquid tank. It is intended to prevent the contaminants from settling.
As a stirring device, a structure in which a plate or a rod is mechanically rotated in the cleaning liquid, a structure in which the plate or the rod is reciprocated in the cleaning liquid, or a compressed air is blown out from the lower part of the cleaning liquid to flow upward to the cleaning liquid. The structure etc. which generate | occur | produce are preferable.
At this time, it is preferable to mix 5-20% of abrasive | polishing agent by weight ratio with respect to high specific gravity liquid, and when 10-20% of abrasive | polishing agent is further mixed, a high cleaning effect will be acquired.
The invention of claim 8 is a cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh in a high specific gravity liquid.
This is because, as a result of the test, it was found that the cleaning liquid mixed with the abrasive having a particle size that passed through the 60-mesh sieve and placed on the 50-mesh sieve was a cleaning liquid with a high cleaning effect.
The invention according to claim 9 is a cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh in a high specific gravity liquid obtained by mixing slaked lime with water.
Slaked lime is used because it is water-soluble, is inexpensive, and does not contaminate the natural environment when discarded as it is.

請求項10の発明は、水に5μmのサイズの消石灰を混ぜて得た高比重液に、重量比で5〜20%の量の研磨剤の粒子であって、粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液とする。
5μmのサイズの消石灰は水を高比重化することに適しており、紙フィルタを使用して濾過することにより洗浄液から取り出すことができるからである。
請求項11の発明は、請求項1〜請求項10のいずれかに記載した発明において、珪砂の粒子又はソフトセラミックの粒子又は貝殻を砕いた粒子の内のいずれかを、研磨剤として使用した発明とする。
珪砂は市販されている珪砂を、ソフトセラミックは粘土(カオリン)を摂氏1200度程度の温度で焼いたものを砕いた粒子を、貝殻としてはホタテの貝殻を砕いた粒子をそれぞれ使用することが好ましい。
それぞれの研磨剤の硬度は、珪砂>ソフトセラミック>貝殻の順で硬いが、管内の付着物が硬い場合は柔らかい研磨剤を使用し、管内の付着物の硬度が柔らかい場合は硬い研磨剤を使用すると高い洗浄効果が得られることが試験の結果得られている。
請求項12の発明は、水にSiOとBを溶かした洗浄液を液槽に貯蔵し、ポンプを使用して前記洗浄液を流体通路の管内に送り、前記管内を通過した洗浄液を再び前記液槽に回収するようにし、前記記流体通路の管内に前記洗浄液を循環させることにより、前記管内を洗浄する流体通路の洗浄方法とする。
シリカゲルとトルマリンを容器の中に入れ、シリカゲルとトルマリンの層に摂氏35〜45度の温水を通過させると、徐々にSiOとBが溶け出す。何回も繰り返し温水を循環させて、シリカゲルとトルマリンの層に温水を通過させることにより使用する洗浄液が得られる。
The invention of claim 10 is a high specific gravity liquid obtained by mixing slaked lime with a size of 5 μm in water, and abrasive particles having a particle size of 50 to 60 mesh in an amount of 5 to 20% by weight. The cleaning liquid is made by mixing the particles.
This is because slaked lime having a size of 5 μm is suitable for increasing the specific gravity of water and can be taken out from the cleaning liquid by filtering using a paper filter.
The invention of claim 11 is the invention according to any one of claims 1 to 10, wherein any one of silica sand particles, soft ceramic particles or shell crushed particles is used as an abrasive. And
It is preferable to use commercially available silica sand, crushed particles of clay (kaolin) baked at a temperature of about 1200 degrees Celsius, and crushed scallop shells as the shell. .
The hardness of each abrasive is hard in the order of silica sand> soft ceramic> shell, but if the deposit in the tube is hard, use a soft abrasive, and if the deposit in the tube is soft, use a hard abrasive Then, as a result of the test, a high cleaning effect is obtained.
In the invention of claim 12, the cleaning liquid in which SiO 2 and B 2 O 3 are dissolved in water is stored in a liquid tank, the cleaning liquid is sent into the pipe of the fluid passage using a pump, and the cleaning liquid that has passed through the pipe is again supplied. The fluid passage is cleaned in the pipe by collecting the liquid in the liquid tank and circulating the cleaning liquid in the pipe of the fluid passage.
When silica gel and tourmaline are put in a container and warm water of 35 to 45 degrees Celsius is passed through the silica gel and tourmaline layer, SiO 2 and B 2 O 3 are gradually dissolved. A washing solution to be used is obtained by repeatedly circulating hot water many times and passing the hot water through a layer of silica gel and tourmaline.

請求項13の発明は、水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液を液槽に貯蔵し、ポンプを使用して前記洗浄液を流体通路の管内に送り、前記管内を通過した洗浄液を再び前記液槽に回収するようにし、前記流体通路の管内に前記洗浄液を循環させることにより、前記管内を洗浄する流体通路の洗浄方法とする。 水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液を使用すると高い洗浄効果が得られるからである。また、水にSiOを65〜75ppm含み、かつ、Bを25〜33ppm含む洗浄液を使用するとさらに高い洗浄効果が得られる。
請求項14の発明は、洗浄液を貯蔵可能な液槽と、前記液槽に貯蔵した洗浄液であって、水にSiOとBを溶かしてなる洗浄液と、前記洗浄液を流体通路の管内に送りさらに前記管内を通過させた洗浄液を前記液槽まで回収するポンプとを有する流体通路の洗浄装置とする。
液槽は洗浄液を貯蔵することに適した容器であればよい。ポンプについてはその形式について特にこだわるものではない。液槽とポンプの間及びポンプの吐出口と流体通路の入り口の間を配管で接続し、さらに流体通路の出口と液槽とを配管で接続する構成とすることが好ましい。
請求項15の発明は、洗浄液を貯蔵可能な液槽と、前記液槽に貯蔵した洗浄液であって、水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液と、前記洗浄液を流体通路の管内に送りさらに前記管内を通過させた洗浄液を前記液槽まで回収するポンプとを有する流体通路の洗浄装置とする。
水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液を使用することにより、高い洗浄効果が得られる流体通路の洗浄装置を提供することができるからである。また、水にSiOを65〜75ppm含み、かつ、Bを25〜33ppm含む洗浄液を使用することはさらに好ましい。
請求項16の発明は、水にSiO及びBを溶かしてなる洗浄液とする。本発明は、内径10mm以下の流体通路を洗浄することに適した洗浄液であって洗浄効果の高い洗浄液を提供したものである。
請求項17の発明は、水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液とする。本発明は、内径10mm以下の流体通路を洗浄することに適した洗浄液であって洗浄効果の高い洗浄液を提供したものである。また、水にSiOを65〜75ppm含み、かつ、Bを25〜35ppm含む洗浄液はさらに好ましい。
In the invention of claim 13, the cleaning liquid containing 50-80 ppm of SiO 2 and 20-35 ppm of B 2 O 3 in water is stored in the liquid tank, and the cleaning liquid is sent into the pipe of the fluid passage using a pump. The cleaning liquid that has passed through the pipe is again collected in the liquid tank, and the cleaning liquid is circulated in the pipe of the fluid path, thereby cleaning the inside of the pipe. This is because a high cleaning effect can be obtained by using a cleaning solution containing 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water. Further, when a cleaning solution containing 65 to 75 ppm of SiO 2 and 25 to 33 ppm of B 2 O 3 is used in water, a higher cleaning effect can be obtained.
The invention of claim 14 is a liquid tank capable of storing a cleaning liquid, a cleaning liquid stored in the liquid tank, wherein the cleaning liquid is obtained by dissolving SiO 2 and B 2 O 3 in water, and the cleaning liquid is placed in a pipe of a fluid passage. And a pump that recovers the cleaning liquid that has passed through the pipe to the liquid tank.
The liquid tank may be any container suitable for storing the cleaning liquid. The pump is not particularly concerned about its type. It is preferable that a pipe is connected between the liquid tank and the pump, a discharge port of the pump and the inlet of the fluid passage, and an outlet of the fluid passage and the liquid tank are connected by a pipe.
The invention of claim 15 is a liquid tank capable of storing a cleaning liquid, a cleaning liquid stored in the liquid tank, wherein the cleaning liquid contains 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water. The fluid passage cleaning device includes a pump that sends the cleaning liquid into the pipe of the fluid passage and collects the cleaning liquid that has passed through the pipe to the liquid tank.
This is because by using a cleaning liquid containing 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water, it is possible to provide a fluid passage cleaning device that can provide a high cleaning effect. Further, it is more preferable to use a cleaning liquid containing 65 to 75 ppm of SiO 2 and 25 to 33 ppm of B 2 O 3 in water.
The invention according to claim 16 is a cleaning liquid obtained by dissolving SiO 2 and B 2 O 3 in water. The present invention provides a cleaning liquid suitable for cleaning a fluid passage having an inner diameter of 10 mm or less and having a high cleaning effect.
The invention of claim 17 is a cleaning liquid containing 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water. The present invention provides a cleaning liquid suitable for cleaning a fluid passage having an inner diameter of 10 mm or less and having a high cleaning effect. Further, a cleaning solution containing 65 to 75 ppm of SiO 2 and 25 to 35 ppm of B 2 O 3 in water is more preferable.

図1に示した実施例1は、洗浄装置1の構成と、洗浄装置1により金型9の流体通路9aを洗浄する状態を表したものである。洗浄装置1は洗浄液6を貯蔵する液槽4と、液槽4の下部に設置した多数の図示しない穴を有する吹出管4aと、空気圧駆動式のダイヤフラムポンプ3及びコンプレッサ7を有している。
また、ダイヤフラムポンプ3の、エア供給口3cとコンプレッサ7とを給気配管8dでつなぎ、エア排気口3dと吹出管4aとを排気配管8eでつなぎ、吸込口3aに連結する吸込配管8aの他端が洗浄液6の液層に浸かるようにし、吐出口3bと流体通路9aの入口9bとを輸送配管8bでつないだ。
また、流体通路9aは10mm以上の内径を有する管路とし、流体通路9aの出口9cに連結する回収配管8cの他端は液槽4の上部に開放する構成にした。
そして水にサイズ5μmの消石灰を混ぜて比重1.2の高比重液を製造し、ホタテ貝を砕いた粒子であって粒度50〜60メッシュに篩い分けた粒子を研磨剤とし、高比重液に対して重量比で20%の量の研磨剤の粒子を混入したものを洗浄液6として使用した。
The first embodiment shown in FIG. 1 shows a configuration of the cleaning device 1 and a state in which the fluid passage 9 a of the mold 9 is cleaned by the cleaning device 1. The cleaning device 1 includes a liquid tank 4 for storing the cleaning liquid 6, a blow-out pipe 4 a having a number of holes (not shown) installed in the lower part of the liquid tank 4, a pneumatically driven diaphragm pump 3 and a compressor 7.
In addition, the air supply port 3c and the compressor 7 of the diaphragm pump 3 are connected by an air supply pipe 8d, the air exhaust port 3d and the outlet pipe 4a are connected by an exhaust pipe 8e, and the suction pipe 8a connected to the suction port 3a. The end was immersed in the liquid layer of the cleaning liquid 6, and the discharge port 3b and the inlet 9b of the fluid passage 9a were connected by the transport pipe 8b.
The fluid passage 9 a is a pipe having an inner diameter of 10 mm or more, and the other end of the recovery pipe 8 c connected to the outlet 9 c of the fluid passage 9 a is opened to the top of the liquid tank 4.
Then, a high specific gravity liquid with a specific gravity of 1.2 is manufactured by mixing slaked lime with a size of 5 μm in water, and particles obtained by crushing scallop shells and sieved to a particle size of 50 to 60 mesh are used as abrasives. On the other hand, a mixture of abrasive particles in an amount of 20% by weight was used as the cleaning liquid 6.

実施例1の考案は以上のように構成されており、以下その作用について説明する。コンプレッサ7から供給された圧縮空気は給気配管8dを通りエア供給口3cからダイヤフラムポンプ3に入る。
圧縮空気によりダイヤフラムポンプ3内のバルブのスプールを材料室A側に押すと材料室Aのダイヤフラムに押されて材料室Aは圧縮され、材料室A内の洗浄液は加圧され吐出口3bから輸送配管8bに押し出される。このとき、材料室Bの空気は減圧され液槽4内の洗浄液6は吸込配管8aを通って吸込口3aから材料室Bに吸引される。
次に、圧縮空気によりダイヤフラムポンプ3内のバルブのスプールを材料室B側に押すと材料室Bのダイヤフラムに押されて材料室Bは圧縮され、材料室B内の洗浄液は加圧され吐出口3bから輸送配管8bに押し出される。このとき、材料室Aの空気は減圧され液槽4内の洗浄液6は吸込配管8aを通って吸込口3aから材料室Aに吸引される。
このようにして、液層4内の洗浄液6は交互に材料室A又は材料室Bに吸引され、材料室A又は材料室Bから交互に輸送配管8bに押し出されることになり、洗浄液6は間欠的に金型9の入口9bを経由して流体通路9aに送られる。
金型9の流体通路9a内を通過するときに洗浄液は脈動しながら流体通路9aの内面を洗浄し、その後金型9の出口9cを経由して回収配管8cに流れ、回収配管8cを通り液槽4の上部から落下して液槽4に回収される。
ダイヤフラムポンプ3のエア排気口3dから排出された圧縮空気は排気配管8eを通過して吹出管4aの多数の穴から洗浄液6の液層に噴出する。かかる圧縮空気の噴出により洗浄液6の液層に上昇流が発生して洗浄液6は攪拌される。
また流体通路を洗浄した後には、貝殻の粒子及びサイズ5μmの消石灰を紙フィルタにより濾過して洗浄液から分離して取り出すことができる。さらに、貝殻の粒子とサイズ5μmの消石灰は篩を使用して篩い分けることにより再利用することができる。
流体通路の付着物に自然を汚染する物質が含まれている場合を除き、貝殻の粒子及びサイズ5μmの消石灰を分離した洗浄液に自然を汚染するような物質が含まれていないので、濾過した後の洗浄液を希釈することなくそのまま廃棄することができる。
The device of the first embodiment is configured as described above, and the operation thereof will be described below. The compressed air supplied from the compressor 7 passes through the air supply pipe 8d and enters the diaphragm pump 3 from the air supply port 3c.
When the spool of the valve in the diaphragm pump 3 is pushed to the material chamber A side by compressed air, the material chamber A is compressed by being pushed by the diaphragm in the material chamber A, and the cleaning liquid in the material chamber A is pressurized and transported from the discharge port 3b. It is pushed out to the pipe 8b. At this time, the air in the material chamber B is depressurized, and the cleaning liquid 6 in the liquid tank 4 is sucked into the material chamber B from the suction port 3a through the suction pipe 8a.
Next, when the spool of the valve in the diaphragm pump 3 is pushed to the material chamber B side by the compressed air, the material chamber B is compressed by being pushed by the diaphragm in the material chamber B, and the cleaning liquid in the material chamber B is pressurized and discharged. It is pushed out from 3b to the transport pipe 8b. At this time, the air in the material chamber A is depressurized, and the cleaning liquid 6 in the liquid tank 4 is sucked into the material chamber A from the suction port 3a through the suction pipe 8a.
In this way, the cleaning liquid 6 in the liquid layer 4 is alternately sucked into the material chamber A or the material chamber B, and is alternately pushed out from the material chamber A or the material chamber B to the transport pipe 8b. Thus, the fluid is sent to the fluid passage 9a via the inlet 9b of the mold 9.
When passing through the fluid passage 9a of the mold 9, the cleaning liquid pulsates and cleans the inner surface of the fluid passage 9a, then flows to the recovery pipe 8c via the outlet 9c of the mold 9, and passes through the recovery pipe 8c. It drops from the upper part of the tank 4 and is collected in the liquid tank 4.
The compressed air discharged from the air exhaust port 3d of the diaphragm pump 3 passes through the exhaust pipe 8e and is jetted into the liquid layer of the cleaning liquid 6 from the numerous holes of the blow-out pipe 4a. As the compressed air is ejected, an upward flow is generated in the liquid layer of the cleaning liquid 6 and the cleaning liquid 6 is stirred.
After washing the fluid passage, shell particles and slaked lime having a size of 5 μm can be filtered through a paper filter and separated from the washing solution. Furthermore, shell particles and slaked lime having a size of 5 μm can be reused by sieving using a sieve.
Since the substance that pollutes nature is not contained in the cleaning liquid from which shell particles and slaked lime with a size of 5 μm are separated, except after the substance that pollutes nature is included in the deposits of the fluid passage, after filtration The cleaning solution can be discarded as it is without being diluted.

図2に示した実施例2は洗浄装置10の構成と、洗浄装置10により金型19の流体通路19aを洗浄する状態を表したものである。洗浄装置10は洗浄液16を貯蔵する液槽14とポンプ13を有している。
また、液槽14とポンプ13の吸込口との間を吸込配管18bでつなぎ、ポンプ13の吐出口と流体通路19aの入口19bとの間を輸送配管18aでつなぎ、流体通路19aの出口19cに連結する回収配管18cの他端は液槽14の上部に解放する構成とした。実施例2で洗浄する流体通路19aは10mm以下の内径を有する管路とした。
そして、図3に示した洗浄液製造機20を使用して得た洗浄液16を使用した。洗浄液製造機20は温水器21、容器22及び容器22の中に貯蔵した5mmサイズのシリカゲルと5〜10mmサイズのトルマリンを積み上げてなる積層23を有している。
温水器21により摂氏40度の温水を送流管24aを通して容器22に供給し、積層23を通過した温水を還流管24bを通して温水器21に還流させる。この循環作業を長時間連続して行うことにより、SiOを70ppm含み、かつ、Bを30ppm含む洗浄液を得た。
液槽14内の洗浄液16は吸引配管18bを通ってポンプ13に吸引され、輸送配管18aを通って入口19bから金型19の流体通路19aに送られる。洗浄液は流体通路19aの中を通過するときに流体通路19aの内面を洗浄し、金型19の出口19cから回収配管18cに流れ、回収配管18cを通り液槽14の上部から落下して液槽14に回収される。
SiOやBは自然を汚染するような物質ではないので、流体通路の付着物に自然を汚染する物質が含まれている場合を除き、使用後の洗浄液を希釈することなくそのまま廃棄することができる。
2 shows the configuration of the cleaning device 10 and a state in which the fluid passage 19a of the mold 19 is cleaned by the cleaning device 10. The cleaning apparatus 10 includes a liquid tank 14 that stores a cleaning liquid 16 and a pump 13.
Further, the suction pipe 18b connects between the liquid tank 14 and the suction port of the pump 13, the connection between the discharge port of the pump 13 and the inlet 19b of the fluid passage 19a by the transport pipe 18a, and the outlet 19c of the fluid passage 19a. The other end of the recovery pipe 18c to be connected is opened to the upper part of the liquid tank 14. The fluid passage 19a for cleaning in Example 2 was a pipe having an inner diameter of 10 mm or less.
And the cleaning liquid 16 obtained using the cleaning liquid manufacturing machine 20 shown in FIG. 3 was used. The cleaning liquid manufacturing machine 20 has a water heater 21, a container 22, and a laminate 23 formed by stacking 5 mm size silica gel and 5 to 10 mm size tourmaline stored in the container 22.
Hot water at 40 degrees Celsius is supplied to the container 22 through the flow pipe 24a by the water heater 21, and the hot water that has passed through the stack 23 is refluxed to the water heater 21 through the reflux pipe 24b. By performing this circulation operation continuously for a long time, a cleaning liquid containing 70 ppm of SiO 2 and 30 ppm of B 2 O 3 was obtained.
The cleaning liquid 16 in the liquid tank 14 is sucked into the pump 13 through the suction pipe 18b, and is sent from the inlet 19b to the fluid passage 19a of the mold 19 through the transport pipe 18a. When the cleaning liquid passes through the fluid passage 19a, the inner surface of the fluid passage 19a is cleaned, flows from the outlet 19c of the mold 19 to the recovery pipe 18c, passes through the recovery pipe 18c, and falls from the upper part of the liquid tank 14 to fall into the liquid tank. 14 recovered.
Since SiO 2 and B 2 O 3 are not substances that pollute nature, the used cleaning fluid is discarded without being diluted, unless the deposits in the fluid passage contain substances that pollute nature. can do.

本発明は、流体通路の洗浄装置や洗浄液を製造販売する産業で利用されるだけでなく、金型を使用して金属をプレス成形する産業や、真空成形や押出成形などプラスチックを成型する産業や、ボイラや冷却装置など熱交換器を使用する産業などで利用される。   The present invention is not only used in industries that manufacture and sell fluid passage cleaning devices and cleaning liquids, but also in industries that press mold metals using molds, industries that mold plastics such as vacuum molding and extrusion molding, Used in industries that use heat exchangers such as boilers and cooling devices.

実施例1の洗浄装置の構成を表した構成図である。1 is a configuration diagram illustrating a configuration of a cleaning device according to Embodiment 1. FIG. 実施例2の洗浄装置の構成を表した構成図である。It is a block diagram showing the structure of the washing | cleaning apparatus of Example 2. FIG. 洗浄液製造機の構成を表した構成図である。It is a block diagram showing the structure of the washing | cleaning-liquid manufacturing machine.

符号の説明Explanation of symbols

1 :洗浄装置 3 :ダイヤフラムポンプ 3a:吸込口
3b:吐出口 3c:エア供給口 3d:エア排気口
4 :液槽 4a:吹出管 6 :洗浄液
7 :コンプレッサ 8a:吸込配管 8b:輸送配管
8c:回収配管 8d:給気配管 8e:排気配管
9 :金型 9a:流体通路 9b:入口
9c:出口 10 :洗浄装置 13 :ポンプ
14 :液槽 16 :洗浄液 18a:輸送配管
18b:吸引配管 18c:回収配管 19 :金型
19a:流体通路 19b:入口 19c:出口
20 :洗浄液製造機 21 :温水器 22 :容器
23 :積層 24a:送流管 24b:還流管










1: Cleaning device 3: Diaphragm pump 3a: Suction port
3b: Discharge port 3c: Air supply port 3d: Air exhaust port 4: Liquid tank 4a: Blowing pipe 6: Cleaning liquid 7: Compressor 8a: Suction piping 8b: Transportation piping 8c: Recovery piping 8d: Supply piping 8e: Exhaust piping 9 : Mold 9a: Fluid passage 9b: Inlet 9c: Outlet 10: Cleaning device 13: Pump 14: Liquid tank 16: Cleaning liquid 18a: Transport piping 18b: Suction piping 18c: Recovery piping 19: Mold 19a: Fluid passage 19b: Inlet 19c: Outlet 20: Cleaning liquid manufacturing machine 21: Water heater 22: Container 23: Laminate 24a: Flow pipe 24b: Reflux pipe










Claims (17)

流体通路の管内に洗浄液を通過させることにより、前記管内を洗浄する方法であって洗浄液が、
比重1.18〜1.28の水溶液(以下単に「高比重液」という。)に、粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液、
または、水にSiOとBを溶かしてなる洗浄液、のいずれかの洗浄液であることを特徴とする流体通路の洗浄方法。
A method of cleaning the inside of the pipe by passing the cleaning liquid through the pipe of the fluid passage,
A cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh in an aqueous solution having a specific gravity of 1.18 to 1.28 (hereinafter simply referred to as “high specific gravity liquid”);
Alternatively, the cleaning method for a fluid passage is characterized by being a cleaning liquid of any one of a cleaning liquid obtained by dissolving SiO 2 and B 2 O 3 in water.
流体通路の管内に洗浄液を通過させることにより、前記管内を洗浄する方法であって洗浄液が、
水に消石灰を混ぜて得た高比重液に、粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液、
または、水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液、のいずれかの洗浄液であることを特徴とする流体通路の洗浄方法。
A method of cleaning the inside of the pipe by passing the cleaning liquid through the pipe of the fluid passage,
A cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh with a high specific gravity liquid obtained by mixing slaked lime with water,
Alternatively, the cleaning method for a fluid passage is characterized by being a cleaning liquid containing 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water.
流体通路の管内に洗浄液を通過させることにより、前記管内を洗浄する方法であって洗浄液が、
水に5μmのサイズの消石灰を混ぜて得た高比重液に、重量比で5〜20%の量の研磨剤の粒子であって、粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液、
または、水にSiOを65〜75ppm含み、かつ、Bを25〜33ppm含む洗浄液、のいずれかの洗浄液であることを特徴とする流体通路の洗浄方法。
A method of cleaning the inside of the pipe by passing the cleaning liquid through the pipe of the fluid passage,
A high specific gravity liquid obtained by mixing slaked lime with a size of 5 μm in water is mixed with abrasive particles having a particle size of 50 to 60 mesh in an amount of 5 to 20% by weight. Cleaning liquid,
Alternatively, the cleaning method for a fluid passage is characterized by being a cleaning solution containing 65 to 75 ppm of SiO 2 and 25 to 33 ppm of B 2 O 3 in water.
高比重液に粒度が50〜60メッシュの研磨剤の粒子を混入してなる洗浄液を液槽に貯蔵し、ダイヤフラムポンプを使用して前記洗浄液を流体通路の管内に送り、前記管内を通過した洗浄液を再び前記液槽に回収するようにし、前記流体通路の管内に前記洗浄液を循環させることにより、前記管内を洗浄することを特徴とする流体通路の洗浄方法。   A cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh in a high specific gravity liquid is stored in a liquid tank, and the cleaning liquid is sent into a pipe of a fluid passage using a diaphragm pump, and the cleaning liquid passes through the pipe. Is recovered in the liquid tank again, and the cleaning liquid is circulated in the pipe of the fluid path to clean the inside of the pipe. 水に5μmのサイズの消石灰を混ぜて得た高比重液に、重量比で5〜20%の量の研磨剤の粒子であって、粒度が50〜60メッシュの研磨剤の粒子を混入してなる洗浄液を液槽に貯蔵し、ダイヤフラムポンプを使用して前記洗浄液を流体通路の管内に送り、前記管内を通過した洗浄液を再び前記液槽に回収するようにし、前記流体通路の管内に前記洗浄液を循環させることにより、前記管内を洗浄することを特徴とする流体通路の洗浄方法。   A high specific gravity liquid obtained by mixing slaked lime having a size of 5 μm with water is mixed with abrasive particles having an amount of 5 to 20% by weight, and the particle size is 50 to 60 mesh. The cleaning liquid is stored in a liquid tank, and the cleaning liquid is sent into the pipe of the fluid passage using a diaphragm pump, and the cleaning liquid that has passed through the pipe is again collected in the liquid tank, and the cleaning liquid is stored in the pipe of the fluid passage. A method for cleaning a fluid passage, wherein the inside of the pipe is cleaned by circulating the water. 洗浄液を貯蔵可能な液槽と、前記液槽に貯蔵した洗浄液であって、高比重液に粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液と、前記洗浄液を流体通路の管内に送りさらに前記管内を通過した洗浄液を前記液槽まで回収するダイヤフラムポンプとを有することを特徴とする流体通路の洗浄装置。   A liquid tank capable of storing a cleaning liquid, a cleaning liquid stored in the liquid tank, the cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh in a high specific gravity liquid, and the cleaning liquid in a pipe of a fluid passage A fluid passage cleaning apparatus comprising: a diaphragm pump that feeds and recovers the cleaning liquid that has passed through the pipe to the liquid tank. 洗浄液を貯蔵可能な液槽と、前記液槽に貯蔵した洗浄液であって、水に5μmのサイズの消石灰を混ぜて得た高比重液に、重量比で5〜20%の量の研磨剤の粒子であって、粒度50〜60メッシュの研磨剤の粒子を混入してなる洗浄液と、前記洗浄液を流体通路の管内に送りさらに前記管内を通過した洗浄液を前記液槽まで回収するダイヤフラムポンプと、前記液槽に貯蔵した洗浄液を攪拌する攪拌装置とを有することを特徴とする流体通路の洗浄装置。   A liquid tank capable of storing a cleaning liquid, and a cleaning liquid stored in the liquid tank, wherein a high specific gravity liquid obtained by mixing slaked lime having a size of 5 μm with water contains an abrasive having an amount of 5 to 20% by weight. A cleaning liquid in which abrasive particles having a particle size of 50 to 60 mesh are mixed, and a diaphragm pump that sends the cleaning liquid into a pipe of a fluid passage and collects the cleaning liquid that has passed through the pipe to the liquid tank; A fluid passage cleaning device comprising: a stirring device for stirring the cleaning solution stored in the liquid tank. 高比重液に、粒度50〜60メッシュの研磨剤の粒子を混入してなることを特徴とする洗浄液。   A cleaning liquid comprising a high specific gravity liquid mixed with abrasive particles having a particle size of 50 to 60 mesh. 水に消石灰を混ぜて得た高比重液に、粒度50〜60メッシュの研磨剤の粒子を混入してなることを特徴とする洗浄液。   A cleaning liquid obtained by mixing abrasive particles having a particle size of 50 to 60 mesh in a high specific gravity liquid obtained by mixing slaked lime with water. 水に5μmのサイズの消石灰を混ぜて得た高比重液に、重量比で5〜20%の量の研磨剤の粒子であって、粒度50〜60メッシュの研磨剤の粒子を混入してなることを特徴とする洗浄液。   A high specific gravity liquid obtained by mixing slaked lime with a size of 5 μm in water is mixed with abrasive particles having a particle size of 50 to 60 mesh in an amount of 5 to 20% by weight. A cleaning liquid characterized by that. 請求項1〜請求項10のいずれかに記載した発明において、珪砂の粒子又はソフトセラミックの粒子又は貝殻を砕いた粒子の内のいずれかを、研磨剤として使用したことを特徴とする発明。   11. The invention according to any one of claims 1 to 10, wherein any one of silica sand particles, soft ceramic particles or crushed shell particles is used as an abrasive. 水にSiOとBを溶かした洗浄液を液槽に貯蔵し、ポンプを使用して前記洗浄液を流体通路の管内に送り、前記管内を通過した洗浄液を再び前記液槽に回収するようにし、前記流体通路の管内に前記洗浄液を循環させることにより、前記管内を洗浄することを特徴とする流体通路の洗浄方法。 A cleaning solution in which SiO 2 and B 2 O 3 are dissolved in water is stored in a liquid tank, and the cleaning liquid is sent into a pipe of a fluid passage using a pump, and the cleaning liquid that has passed through the pipe is recovered in the liquid tank again. And cleaning the inside of the pipe by circulating the cleaning liquid in the pipe of the fluid path. 水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液を液槽に貯蔵し、ポンプを使用して前記洗浄液を流体通路の管内に送り、前記管内を通過した洗浄液を再び前記液槽に回収するようにし、前記流体通路の管内に前記洗浄液を循環させることにより、前記管内を洗浄することを特徴とする流体通路の洗浄方法。 A cleaning liquid containing 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water is stored in a liquid tank, and the cleaning liquid is sent into the pipe of the fluid passage using a pump, and passes through the pipe. Is recovered in the liquid tank again, and the cleaning liquid is circulated in the pipe of the fluid path to clean the inside of the pipe. 洗浄液を貯蔵可能な液槽と、前記液槽に貯蔵した洗浄液であって、水にSiO
を溶かしてなる洗浄液と、前記洗浄液を流体通路の管内に送りさらに前記管内を通過させた洗浄液を前記液槽まで回収するポンプとを有することを特徴とする流体通路の洗浄装置。
A liquid tank capable of storing a cleaning liquid, a cleaning liquid stored in the liquid tank, wherein the cleaning liquid is obtained by dissolving SiO 2 and B 2 O 3 in water, and the cleaning liquid is sent into a pipe of a fluid passage and further passes through the pipe A fluid passage cleaning apparatus, comprising: a pump that recovers the cleaning liquid to the liquid tank.
洗浄液を貯蔵可能な液槽と、前記液槽に貯蔵した洗浄液であって、水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含む洗浄液と、前記洗浄液を流体通路の管内に送りさらに前記管内を通過させた洗浄液を前記液槽まで回収するポンプとを有することを特徴とする流体通路の洗浄装置。 A liquid tank capable of storing a cleaning liquid, a cleaning liquid stored in the liquid tank, wherein the cleaning liquid contains 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water, and the cleaning liquid is contained in the fluid passage. A fluid passage cleaning apparatus, comprising: a pump for feeding the cleaning liquid that has been fed into the pipe and passing through the pipe to the liquid tank. 水にSiO及びBを溶かしてなる洗浄液。 A cleaning solution obtained by dissolving SiO 2 and B 2 O 3 in water. 水にSiOを50〜80ppm含み、かつ、Bを20〜35ppm含むことを特徴とする洗浄液。















A cleaning liquid comprising 50 to 80 ppm of SiO 2 and 20 to 35 ppm of B 2 O 3 in water.















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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6433042B1 (en) * 2018-08-10 2018-12-05 日本リニューアル株式会社 Flushing device

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58177190A (en) * 1982-04-09 1983-10-17 日本軽金属株式会社 Method of cleaning inner wall of pipe
JPH03112753U (en) * 1990-02-28 1991-11-18
JPH10219923A (en) * 1997-02-07 1998-08-18 Kuraray Co Ltd Material for civil engineering and building
JPH1110543A (en) * 1997-06-27 1999-01-19 Sumitomo Bakelite Co Ltd Manufacture of abrasive material made of thermosetting resin
JP2001090137A (en) * 1999-09-17 2001-04-03 Yamaha Livingtec Corp Bathroom floor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58177190A (en) * 1982-04-09 1983-10-17 日本軽金属株式会社 Method of cleaning inner wall of pipe
JPH03112753U (en) * 1990-02-28 1991-11-18
JPH10219923A (en) * 1997-02-07 1998-08-18 Kuraray Co Ltd Material for civil engineering and building
JPH1110543A (en) * 1997-06-27 1999-01-19 Sumitomo Bakelite Co Ltd Manufacture of abrasive material made of thermosetting resin
JP2001090137A (en) * 1999-09-17 2001-04-03 Yamaha Livingtec Corp Bathroom floor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6433042B1 (en) * 2018-08-10 2018-12-05 日本リニューアル株式会社 Flushing device
JP2020025927A (en) * 2018-08-10 2020-02-20 日本リニューアル株式会社 Flushing device

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