JP2021079361A - Purifier and purification method of cleaning fluid - Google Patents

Purifier and purification method of cleaning fluid Download PDF

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JP2021079361A
JP2021079361A JP2019211581A JP2019211581A JP2021079361A JP 2021079361 A JP2021079361 A JP 2021079361A JP 2019211581 A JP2019211581 A JP 2019211581A JP 2019211581 A JP2019211581 A JP 2019211581A JP 2021079361 A JP2021079361 A JP 2021079361A
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cleaning liquid
liquid
cleaning
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metal
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JP7442301B2 (en
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正浩 上野
Masahiro Ueno
正浩 上野
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JATCO Ltd
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Abstract

To provide a purifier of a cleaning fluid capable of surely purifying a polluted cleaning fluid even though a matter obtained by strongly combining metal components with oil content remains in the polluted cleaning fluid.SOLUTION: A purifier of a cleaning fluid includes a liquid atomization device 3 for atomizing a molecule group of a liquid by circulating a polluted cleaning fluid polluted by cleaning a metal processed article, a centrifuge 4 for performing centrifugal separation treatment of a cleaning fluid obtained by atomizing a molecule group by the liquid atomization device 3 to recover and remove metal sludge in the cleaning fluid, and a floating oil recovery device 5 for performing floating recovery of the oil content in the cleaning fluid treated by the centrifuge 4.SELECTED DRAWING: Figure 1

Description

本発明は、特にアルミ加工品の洗浄に用いる洗浄液の浄化に適した洗浄液の浄化装置及び浄化方法に関するものである。 The present invention relates to a cleaning liquid purification device and a purification method particularly suitable for purifying a cleaning liquid used for cleaning aluminum processed products.

金属加工品(製品)を製造する場合、一般に、製品を加工し(加工工程)、加工した製品を洗浄し(洗浄工程)、洗浄後の製品を検査して(検査工程)、出荷する。洗浄工程では、洗浄液を用いて製品を洗浄するが、洗浄に用いられて汚濁した洗浄液は浄化処理をしたうえで循環して使用する。そこで、汚濁洗浄液を浄化する技術が開発されている。 When manufacturing a processed metal product (product), generally, the product is processed (processing process), the processed product is washed (cleaning process), the cleaned product is inspected (inspection process), and then shipped. In the cleaning process, the product is washed with a cleaning liquid, and the cleaning liquid used for cleaning and polluted is circulated after being purified. Therefore, a technique for purifying a pollutant cleaning liquid has been developed.

一般的な汚濁洗浄液の浄化手法としては、ダーティタンク内に回収された汚濁洗浄液をダーティタンク内から取り出してバグフィルタを通過させて浄化し、クリーンタンク内に回収する。その後、浄化された洗浄液をジェットポンプで吸引しノズルから吐出して製品を洗浄し、汚濁した洗浄液をダーティタンク内に回収する。 As a general method for purifying a pollutant cleaning liquid, the pollutant cleaning liquid collected in a dirty tank is taken out from the dirty tank, passed through a bug filter to be purified, and then collected in a clean tank. After that, the purified cleaning liquid is sucked by a jet pump and discharged from a nozzle to clean the product, and the polluted cleaning liquid is collected in a dirty tank.

しかし、汚濁洗浄液を単にバグフィルタに通過させるだけでは汚濁洗浄液中のスラッジや油分が残存し、汚濁洗浄液を十分に浄化することができない。特許文献1には、この点に着目して、洗浄に用いられて汚濁した洗浄液を、貯液槽で油水分離するともに浮遊スラジを遠心分離機で除去して汚濁洗浄液を浄化する技術が開示されている。 However, simply passing the pollutant cleaning liquid through the bag filter leaves sludge and oil in the pollutant cleaning liquid, and the pollutant cleaning liquid cannot be sufficiently purified. Focusing on this point, Patent Document 1 discloses a technique for purifying a polluted cleaning liquid by separating oil and water in a liquid storage tank and removing floating sludge with a centrifuge to purify the polluted cleaning liquid used for cleaning. ing.

実公昭58−8398号公報Jikken Sho 58-8398 Gazette

しかしながら、金属成分と油分とが分子間結合によって強固に結合されることがある。特にアルミ加工品(アルミニウム加工品)を洗浄した後の洗浄液では、アルミ成分と油分とが強固に結合される(分子間結合)傾向がある。このように金属成分と油分とが強固に結合されたものは、洗浄液の水分に近い比重となり洗浄液中に浮遊するため遠心分離機では十分に分離できないことがある。 However, the metal component and the oil component may be strongly bonded by an intermolecular bond. In particular, in the cleaning liquid after cleaning the processed aluminum product (processed aluminum product), the aluminum component and the oil component tend to be strongly bonded (intermolecular bond). Such a tightly bonded metal component and oil may not be sufficiently separated by a centrifuge because the specific density is close to that of the water content of the cleaning liquid and the metal component and the oil content are suspended in the cleaning liquid.

本発明は、このような課題に着目して創案されたもので、金属成分と油分とが強固に結合されたものが汚濁洗浄液に残存していても汚濁洗浄液を確実に浄化することができるようにした洗浄液の浄化装置及び浄化方法を提供することを目的としている。 The present invention has been devised in view of such a problem, so that the pollutant cleaning liquid can be reliably purified even if the metal component and the oil are strongly bonded to each other and remain in the pollutant cleaning liquid. It is an object of the present invention to provide a purification device and a purification method for the cleaning liquid.

本発明の洗浄液の浄化装置は、金属加工品を洗浄して汚濁した汚濁洗浄液を流通させることにより液体の分子集団を微細化する液体微細化装置と、前記液体微細化装置により分子集団を微細化された洗浄液を遠心分離処理して前記洗浄液中の金属スラッジを回収し除去する遠心分離機と、前記遠心分離機により処理された洗浄液中の油分を浮上回収する浮上油回収装置と、を備えていることを特徴としている。
前記液体微細化装置は、前記汚濁洗浄液が流通する流路の上流側に配置され複数の金属製メッシュが装備された金属製メッシュ層と、前記流路の前記金属製メッシュ層よりも下流側に配置され複数のセラミックボールが装備されたセラミックボール層とが内装された処理容器と、前記処理容器内に前記汚濁洗浄液を所定圧以上且つ所定速度以上で通過させる洗浄液圧送装置と、を有していることが好ましい。
前記液体微細化装置の上流側に、前記汚濁洗浄液を一次処理するバグフィルタが配置されていることが好ましい。
さらに、前記浮上油回収装置により処理された浄化洗浄液を貯留する浄化洗浄液タンクと、前記浄化洗浄液タンク内の前記浄化洗浄液を使用して前記金属加工品を洗浄して汚濁した前記汚濁洗浄液を貯留する汚濁洗浄液タンクと、を備え、洗浄液の循環経路が形成されていることが好ましい。
The cleaning liquid purification device of the present invention is a liquid micronization device that purifies a metal processed product and distributes a polluted polluted cleaning liquid to miniaturize a liquid molecular group, and the liquid micronization device that miniaturizes the molecular group. A centrifuge that centrifuges the cleaned liquid to collect and removes metal sludge in the cleaning liquid, and a floating oil recovery device that floats and collects oil in the cleaning liquid treated by the centrifuge. It is characterized by being.
The liquid micronization device is arranged on the upstream side of the flow path through which the pollutant cleaning liquid flows and is equipped with a plurality of metal meshes, and on the downstream side of the metal mesh layer of the flow path. It has a processing container in which a ceramic ball layer provided with a plurality of ceramic balls is arranged, and a cleaning liquid pumping device for passing the polluted cleaning liquid through the processing container at a predetermined pressure or higher and a predetermined speed or higher. It is preferable to have.
It is preferable that a bug filter for primary treatment of the pollutant cleaning liquid is arranged on the upstream side of the liquid miniaturization apparatus.
Further, a purification cleaning liquid tank for storing the purification cleaning liquid processed by the floating oil recovery device and the pollution cleaning liquid that has been polluted by cleaning the metal processed product using the purification cleaning liquid in the purification cleaning liquid tank are stored. It is preferable that a pollutant cleaning liquid tank is provided and a circulation route for the cleaning liquid is formed.

本発明の洗浄液の浄化方法は、金属加工品を洗浄して汚濁した洗浄液を液体微細化装置に流通させて液体の分子集団を微細化する液体微細化工程と、前記液体微細化工程により分子集団を微細化された洗浄液を遠心分離処理して前記洗浄液中の金属スラッジを回収し除去する遠心分離工程と、前記遠心分離工程により処理された洗浄液中の油分を浮上回収する浮上油回収工程と、を備えていることを特徴としている。 The cleaning liquid purification method of the present invention includes a liquid micronization step of cleaning a metal processed product and distributing a polluted cleaning liquid to a liquid micronization device to miniaturize a liquid molecular group, and a molecular group by the liquid micronization step. A centrifugal separation step of centrifuging the finely divided cleaning liquid to recover and remove metal sludge in the cleaning liquid, and a floating oil recovery step of floating and recovering the oil content in the cleaning liquid treated by the centrifugation step. It is characterized by having.

本発明によれば、金属成分と油分とが強固に結合されたものが汚濁洗浄液に残存していても、金属成分と油分との結合を効率的に分離させ、汚濁洗浄液を確実に浄化することができる。 According to the present invention, even if a material in which a metal component and an oil are strongly bonded remains in the pollutant cleaning liquid, the bond between the metal component and the oil is efficiently separated and the polluted cleaning liquid is reliably purified. Can be done.

一実施形態に係る洗浄液の浄化装置の構成を示すブロック図である。It is a block diagram which shows the structure of the purification apparatus of the cleaning liquid which concerns on one Embodiment. 一実施形態に係る洗浄液の浄化装置の液体微細化装置を示す図であり、(a)は全体構成図、(b)は処理容器内の構成を示す断面図である。It is a figure which shows the liquid miniaturization apparatus of the cleaning liquid purification apparatus which concerns on one Embodiment, (a) is the whole block diagram, (b) is the sectional view which shows the structure in the processing container. 一実施形態にかかる洗浄液の浄化装置の遠心分離機の構成を示す断面図である。It is sectional drawing which shows the structure of the centrifuge of the purification apparatus of the cleaning liquid which concerns on one Embodiment. 一実施形態にかかる洗浄液の浄化装置の浮上油回収装置の構成を示す断面図である。It is sectional drawing which shows the structure of the floating oil recovery apparatus of the purification apparatus of the cleaning liquid which concerns on one Embodiment.

以下、図面を参照して本発明にかかる洗浄液の浄化装置及び洗浄液の浄化方法の実施形態を説明する。なお、以下に示す実施形態はあくまでも例示に過ぎず、以下の実施形態で明示しない種々の変形や技術の適用を排除する意図はない。かかる実施形態を部分的に用いて実施したり、一部を変更して実施したり、同等の機能を有する他の機構や装置に置き換えて実施したりすることができるものである。 Hereinafter, embodiments of a cleaning liquid purification device and a cleaning liquid purification method according to the present invention will be described with reference to the drawings. It should be noted that the embodiments shown below are merely examples, and there is no intention of excluding the application of various modifications and techniques not specified in the following embodiments. Such an embodiment can be partially used, partially modified, or replaced with another mechanism or device having the same function.

〔洗浄液の浄化装置の全体構成〕
本実施形態にかかる洗浄液の浄化装置は、アルミ加工品等の金属加工品(以下、製品ともいう)を製造する際に、製品を加工する加工工程と、製品を検査する検査工程との間で、加工した製品を洗浄する洗浄工程で使用するもので、金属加工品を洗浄して汚濁した汚濁洗浄液を浄化して再利用できるようにするものである。なお、洗浄液は、例えば水に所要の洗浄剤を溶解させたものである。
[Overall configuration of cleaning liquid purification device]
The cleaning liquid purification device according to the present embodiment is used between a processing process for processing a product and an inspection process for inspecting the product when manufacturing a metal processed product (hereinafter, also referred to as a product) such as an aluminum processed product. It is used in the cleaning process for cleaning processed products, and is used to clean metal processed products to purify polluted polluted cleaning liquids so that they can be reused. The cleaning liquid is, for example, a solution in which a required cleaning agent is dissolved in water.

図1に示すように、この浄化装置10は、汚濁洗浄液タンク(ダーティタンクともいう)1と、バグフィルタ2と、液体微細化装置(微細水装置ともいう)3と、遠心分離機4と、浮上油回収装置5と、浄化洗浄液タンク(クリーンタンクともいう)6とを、洗浄液の処理経路9の上流側から下流側へ向けてこの順で配備されており、洗浄液の循環経路が形成されている。図1では、ダーティタンク1からクリーンタンク6に至る浄化装置10における洗浄液の処理経路9を太線矢印で示している。 As shown in FIG. 1, the purification device 10 includes a pollutant cleaning liquid tank (also referred to as a dirty tank) 1, a bag filter 2, a liquid miniaturization device (also referred to as a fine water device) 3, a centrifuge 4. The floating oil recovery device 5 and the purification cleaning liquid tank (also referred to as a clean tank) 6 are arranged in this order from the upstream side to the downstream side of the cleaning liquid treatment path 9, and a cleaning liquid circulation path is formed. There is. In FIG. 1, the cleaning liquid treatment path 9 in the purification device 10 from the dirty tank 1 to the clean tank 6 is indicated by a thick arrow.

クリーンタンク6に貯留された浄化洗浄液は、ジェットポンプ7によって吸い上げられて洗浄ノズル8から製品に向けて噴射されて、製品の洗浄に用いられる。
洗浄に用いられた浄化洗浄液は、製品の金属加工時に付着した油や金属バリ等の金属クズが混入して汚濁する。この汚濁した洗浄液(汚濁洗浄液)はダーティタンク1に回収されて本浄化装置10によって処理される。
なお、図1では、クリーンタンク6からダーティタンク1に至る製品の洗浄にかかる洗浄液の移動経路11を細線矢印で示している。
以下、浄化装置10の要部構成を説明する。
The purifying cleaning liquid stored in the clean tank 6 is sucked up by the jet pump 7 and injected from the cleaning nozzle 8 toward the product to be used for cleaning the product.
The purifying cleaning liquid used for cleaning becomes polluted by being mixed with metal debris such as oil and metal burrs that adhered during metal processing of the product. This polluted cleaning liquid (polluted cleaning liquid) is collected in the dirty tank 1 and processed by the present purification device 10.
In FIG. 1, the moving path 11 of the cleaning liquid for cleaning the product from the clean tank 6 to the dirty tank 1 is indicated by a thin arrow.
Hereinafter, the main configuration of the purification device 10 will be described.

〔バグフィルタ〕
バグフィルタ2は、公知のものであり、所定の粗さ(ここでは10μ)のフィルタエレメントを備えており、ダーティタンク1内の汚濁洗浄液をこのバグフィルタ2に通過させてろ過することで、汚濁洗浄液中の一定以上のサイズの固形分を除去することができる。このバグフィルタ2による処理を一次処理という。
[Bug filter]
The bug filter 2 is a known one, and is provided with a filter element having a predetermined roughness (here, 10 μ), and the pollutant cleaning liquid in the dirty tank 1 is passed through the bug filter 2 to be filtered to pollute. It is possible to remove solid content of a certain size or more in the cleaning liquid. The processing by this bug filter 2 is called primary processing.

〔液体微細化装置〕
液体微細化装置3は、公知のものであり、図2に示すように、処理容器30と、上流側タンク31と、上流側タンク31内の汚濁洗浄液を吸引して処理容器30に圧送するポンプ(洗浄液圧送装置)32と、処理容器30で処理された洗浄液を一時貯留する下流側タンク33とを備えている。なお、上流側タンク31内の汚濁洗浄液は、ダーティタンク1内の汚濁洗浄液をバグフィルタ2で一次処理されたものである。
[Liquid miniaturization device]
The liquid miniaturization device 3 is a known one, and as shown in FIG. 2, a pump that sucks the processing container 30, the upstream tank 31, and the pollutant cleaning liquid in the upstream tank 31 and pumps them to the processing container 30. A (cleaning liquid pumping device) 32 and a downstream tank 33 for temporarily storing the cleaning liquid treated in the processing container 30 are provided. The pollutant cleaning liquid in the upstream tank 31 is a primary treatment of the pollutant cleaning liquid in the dirty tank 1 with the bug filter 2.

処理容器30内には、汚濁洗浄液が流通する流路30aの上流側に配置され複数の金属製メッシュ(ここでは、ステンレス鋼(SUS)製のメッシュ)が装備された金属製メッシュ層34と、流路30aの金属製メッシュ層34よりも下流側に配置され複数のセラミックボールが装備されたセラミックボール層35とが内装されている。 In the processing container 30, a metal mesh layer 34 arranged on the upstream side of the flow path 30a through which the pollutant cleaning liquid flows and equipped with a plurality of metal meshes (here, a mesh made of stainless steel (SUS)), and a metal mesh layer 34. A ceramic ball layer 35, which is arranged on the downstream side of the metal mesh layer 34 of the flow path 30a and is equipped with a plurality of ceramic balls, is installed.

ポンプ32による圧送によって、一定以上の圧力と速度をもって処理容器30内に液体を通過させると、液体が通過する際に、SUSメッシュ及びセラミックボールの周りでキャビテーションやコアンダ効果が繰り返し発生し、この結果として液体中に大量のナノバブル(ナノレベルの気泡)が発生する。なお、この装置によって発生したナノバブルは、空気を強制的に液体に溶け込ませる方式の通常のナノバブルよりも長く液体中に留まって効果を発揮する特性がある。 When the liquid is passed through the processing container 30 with a pressure and speed above a certain level by pumping by the pump 32, cavitation and Coanda effect are repeatedly generated around the SUS mesh and the ceramic balls when the liquid passes, and as a result, the cavitation and the Coanda effect are repeatedly generated. As a result, a large amount of nanobubbles (nanolevel bubbles) are generated in the liquid. It should be noted that the nanobubbles generated by this device have the property of staying in the liquid for a longer time than the normal nanobubbles of the method of forcibly dissolving air in the liquid and exerting an effect.

こうして発生したナノバブルは、液体の分子集団を微細化する作用を発揮する。これは、セラミックボールが励起されて特殊な波長の微弱電位を発生し、分子間結合の分離が促進されるものと考えられる。例えば液体としての水を処理容器30内に流通させてナノバブルが発生すると、水の分子集団を微細化する。このため、液体微細化装置3を微細水装置ともいう。 The nanobubbles generated in this way exert the effect of refining the molecular population of the liquid. It is considered that this is because the ceramic ball is excited to generate a weak potential having a special wavelength, and the separation of intermolecular bonds is promoted. For example, when water as a liquid is circulated in the processing container 30 to generate nanobubbles, the molecular population of water is refined. Therefore, the liquid miniaturization device 3 is also referred to as a fine water device.

液体微細化装置3で処理される汚濁洗浄液には、バグフィルタ2では除去できなかったスラッジや油分が残存し、スラッジの中には、金属成分と油分とが強固に結合(分子間結合)された状態で残存したものがある。特に、アルミ成分と油分とは分子間結合によってより強固に結合される傾向がある。金属成分と油分とが強固に結合するとこれらを容易に分解することはできないため、汚濁洗浄液の浄化の妨げになっている。 Sludge and oil that could not be removed by the bag filter 2 remain in the pollutant cleaning liquid treated by the liquid miniaturization apparatus 3, and the metal component and the oil are firmly bonded (intermolecular bond) in the sludge. There is something that remains in the state. In particular, the aluminum component and the oil tend to be more strongly bonded by intermolecular binding. If the metal component and the oil are strongly bonded, they cannot be easily decomposed, which hinders the purification of the pollutant cleaning liquid.

液体微細化装置3は、このような金属成分と油分とを分離させる作用も有している。これは、上記同様にセラミックボールが励起されて特殊な波長の微弱電位を発生し、分子間結合の分離が促進されるものと考えられる。金属成分と油分とが分離すると、遠心分離によって汚濁洗浄液から金属成分を分離して回収することができ、浮上回収によって汚濁洗浄液中の油分を分離して回収することができる。 The liquid miniaturization device 3 also has an action of separating such a metal component and an oil component. It is considered that this is because the ceramic ball is excited to generate a weak potential having a special wavelength in the same manner as described above, and the separation of the intermolecular bond is promoted. When the metal component and the oil component are separated, the metal component can be separated and recovered from the pollutant cleaning solution by centrifugation, and the oil component in the pollutant cleaning solution can be separated and recovered by floating recovery.

〔遠心分離機〕
遠心分離機4は、公知のものであり、図3に示すように、略円筒状で縦長の処理容器40を備えている。処理容器40の上部には、拡径した旋回室41が設けられ、旋回室41の外周には、旋回室41の軸心から偏心した位置に液体(ここでは、液体微細化装置3で処理された洗浄液)を高速で圧送する入口部42が設けられている。これにより、旋回室41内では、供給された液体が高速旋回しながら、液体(水分及び油分)と、液体に対して比重の大きい金属スラッジ等の固形分とが分離されるようになっている。
〔centrifuge〕
The centrifuge 4 is a known one, and as shown in FIG. 3, the centrifuge 4 includes a substantially cylindrical and vertically long processing container 40. A swivel chamber 41 having an enlarged diameter is provided in the upper part of the processing container 40, and a liquid (here, treated by the liquid miniaturizing device 3) is provided on the outer periphery of the swirl chamber 41 at a position eccentric from the axis of the swivel chamber 41. An inlet portion 42 for pumping the cleaning liquid) at high speed is provided. As a result, in the swirl chamber 41, the supplied liquid swirls at high speed, and the liquid (moisture and oil) and the solid content such as metal sludge having a large specific gravity with respect to the liquid are separated. ..

処理容器40の上下方向中間部には、固形分が沈降していく空間である沈降空間43が設けられ、沈降空間43の下方の処理容器40の下部には、固形分が沈殿する空間である沈殿室44が設けられる。
また、処理容器40の下端部には沈殿室44内に沈殿した固形分を回収する下部回収出口45が設けられ、処理容器40の上端部には旋回室41内で固形分を除去された液体成分(水分及び油分)を回収する上部回収口46が設けられている。
こうして、液体微細化装置3で処理された洗浄液を遠心分離機4に導入することで、洗浄液から金属スラッジ等の固形分を除去することができる。
A settling space 43, which is a space for solids to settle, is provided in the middle portion in the vertical direction of the processing container 40, and a space for solids to settle is provided in the lower part of the processing container 40 below the settling space 43. A settling chamber 44 is provided.
Further, a lower collection outlet 45 for collecting the solid content settled in the settling chamber 44 is provided at the lower end of the processing container 40, and a liquid from which the solid content has been removed in the swirl chamber 41 is provided at the upper end of the processing container 40. An upper collection port 46 for collecting components (moisture and oil) is provided.
By introducing the cleaning liquid treated by the liquid miniaturizing device 3 into the centrifuge 4 in this way, solid content such as metal sludge can be removed from the cleaning liquid.

〔浮上油回収装置〕
浮上油回収装置5は、公知のものであり、図4に示すように、洗浄液〔固形分を除去された液体成分(水分及び油分)〕が貯留される処理タンク51と、処理タンク51内の洗浄液中の液面付近に回収口52aを配置された油回収ダクト52と、油回収ダクト52に接続されて回収口52aから洗浄液中の液面付近に浮上した油分を吸引回収する吸引ポンプ53と、回収した油分が貯留される油回収タンク54とを備えている。油回収ダクト52はフレキシブルであり、回収口52aにはフロート52bが装備され、回収口52aが常時、洗浄液の液面直下に位置するようになっている。
[Floating oil recovery device]
The floating oil recovery device 5 is a known one, and as shown in FIG. 4, a processing tank 51 in which a cleaning liquid [a liquid component from which solids have been removed (moisture and oil)] is stored, and a processing tank 51 in the processing tank 51. An oil recovery duct 52 in which a recovery port 52a is arranged near the liquid level in the cleaning liquid, and a suction pump 53 connected to the oil recovery duct 52 and sucking and recovering oil floating near the liquid level in the cleaning liquid from the recovery port 52a. It is provided with an oil recovery tank 54 for storing the recovered oil. The oil recovery duct 52 is flexible, and the recovery port 52a is equipped with a float 52b so that the recovery port 52a is always located directly below the liquid level of the cleaning liquid.

また、処理容器51内の底部付近に吸引口55aを配置された洗浄液吸引ダクト55と、洗浄液吸引ダクト55に接続されて吸引口55aから、処理容器51内で油分を分離された洗浄液を吸引する吸引ポンプ56と、吸引した洗浄液が貯留される回収タンク57とを備えている。回収タンク57にはクリーンタンク6を直接用いてもよい。
このように浮上油回収装置5では、洗浄液の液体成分のうちの油分を分離して残存した水分(洗浄剤を含む)を回収する。
Further, the cleaning liquid suction duct 55 in which the suction port 55a is arranged near the bottom of the processing container 51 and the cleaning liquid whose oil content is separated in the processing container 51 are sucked from the suction port 55a connected to the cleaning liquid suction duct 55. It includes a suction pump 56 and a recovery tank 57 in which the sucked cleaning liquid is stored. A clean tank 6 may be directly used for the recovery tank 57.
In this way, the floating oil recovery device 5 separates the oil component of the liquid component of the cleaning liquid and recovers the remaining water (including the cleaning agent).

〔作用及び効果〕
本実施形態にかかる洗浄液の浄化装置10は、上記のように構成されているので、金属加工品を洗浄して汚濁した汚濁洗浄液(つまり、洗浄液(洗浄剤を含んだ水)に油分と金属スラッジ等の固定分とが含有した液体)を流通させることにより、洗浄液を確実に浄化して再利用することができるようになる(効果1)。
[Action and effect]
Since the cleaning liquid purifying device 10 according to the present embodiment is configured as described above, oil and metal sludge are added to the polluted cleaning liquid (that is, the cleaning liquid (water containing a cleaning agent)) that has been polluted by cleaning the metal processed product. By circulating the liquid containing a fixed amount such as, etc., the cleaning liquid can be reliably purified and reused (effect 1).

つまり、汚濁洗浄液をバグフィルタ2に通過させてろ過することで、汚濁洗浄液中の一定以上のサイズの固形分を除去する(一次処理)。この段階では、一次処理した洗浄液には、水分および油分からなる液体成分に微小なサイズの固形分(金属スラッジ)が含まれる。また、固形分には、金属成分と油分とが強固に結合(分子間結合)された状態で残存した結合体(特に、アルミ成分と油分とが分子間結合によってより強固に結合された結合体)が含まれる。 That is, by passing the pollutant cleaning liquid through the bag filter 2 and filtering it, solid content having a certain size or larger in the pollutant cleaning liquid is removed (primary treatment). At this stage, the primary-treated cleaning liquid contains fine-sized solids (metal sludge) in the liquid component consisting of water and oil. Further, in the solid content, a bond remaining in a state where the metal component and the oil component are strongly bonded (intermolecular bond) (in particular, a bond in which the aluminum component and the oil component are more strongly bonded by the intermolecular bond). ) Is included.

次に、一次処理した洗浄液を液体微細化装置3に流通させて液体の分子集団を微細化する(液体微細化工程)。つまり、液体微細化装置3は、SUSメッシュを有する金属製メッシュ層34とセラミックボールを有するセラミックボール層35とが内装された処理容器30と、洗浄液圧送装置32とを有しているので、一定以上の圧力と速度をもって処理容器30内に液体を通過させると、液体が通過する際に、SUSメッシュ及びセラミックボールの周りでキャビテーションやコアンダ効果が繰り返し発生し、この結果として液体中に大量のナノバブルが発生する。液体微細化装置3により液体中に発生するこのナノバブルによって洗浄液中の液体同士や液体と固体との分子間の結合を分離する。これにより、金属成分と油分とが強固に結合された状態で残存した結合体(特に、アルミ成分と油分との結合体)を分解することができる(効果2)。 Next, the primary-treated cleaning liquid is circulated to the liquid miniaturization apparatus 3 to miniaturize the molecular group of the liquid (liquid miniaturization step). That is, the liquid micronizing device 3 has a processing container 30 in which a metal mesh layer 34 having a SUS mesh and a ceramic ball layer 35 having ceramic balls are contained, and a cleaning liquid pumping device 32, and is therefore constant. When the liquid is passed through the processing container 30 with the above pressure and speed, cavitation and coranda effects are repeatedly generated around the SUS mesh and the ceramic balls when the liquid passes, and as a result, a large amount of nanobubbles are generated in the liquid. Occurs. The nanobubbles generated in the liquid by the liquid miniaturizing device 3 separate the bonds between the liquids in the cleaning liquid and between the molecules of the liquid and the solid. Thereby, the bond (particularly, the bond between the aluminum component and the oil) remaining in the state where the metal component and the oil are firmly bonded can be decomposed (effect 2).

次に、こうして液体微細化工程で金属成分と油分との結合体が分解された洗浄液を遠心分離機4により遠心分離処理して前記洗浄液中の金属スラッジを回収し除去する(遠心分離工程)。
遠心分離工程では、洗浄液から金属スラッジ等の固形分(金属スラッジ)が除去される。金属成分と油分との結合体は、比重が水に近く、遠心分離のみでは、この結合体の金属成分を洗浄液(洗浄剤を含んだ水)から分離することが困難であるが、本装置では予め金属成分と油分との結合体が分解されているのでこのようなことはない。
Next, the cleaning liquid in which the combination of the metal component and the oil is decomposed in the liquid miniaturization step is centrifuged by the centrifuge 4 to collect and remove the metal sludge in the cleaning liquid (centrifuge step).
In the centrifugation step, solids (metal sludge) such as metal sludge are removed from the cleaning liquid. The specific gravity of the combination of the metal component and the oil is close to that of water, and it is difficult to separate the metal component of this combination from the cleaning liquid (water containing a detergent) only by centrifugation. This does not happen because the combination of the metal component and the oil is decomposed in advance.

次に、遠心分離工程により処理された洗浄液中の油分を浮上油回収装置5によって浮上回収する(浮上油回収工程)。
浮上油回収工程では、洗浄液から油分が除去される。金属成分と油分との結合体は、比重が水に近く、浮上油回収といった静的な比重分離では、結合体を洗浄液(洗浄剤を含んだ水)から分離することが困難であるが、本装置では予め金属成分と油分との結合体が分解されているのでこのようなことはない。
Next, the oil content in the cleaning liquid treated by the centrifugation step is floated and recovered by the floating oil recovery device 5 (floating oil recovery step).
In the floating oil recovery step, oil is removed from the cleaning liquid. The specific gravity of the combination of the metal component and the oil is close to that of water, and it is difficult to separate the combination from the cleaning liquid (water containing a cleaning agent) by static specific gravity separation such as floating oil recovery. This is not the case because the combination of the metal component and the oil is decomposed in advance in the apparatus.

このようにして、本実施形態にかかる洗浄液の浄化装置又は洗浄液の浄化方法によれば、アルミ成分と油分との結合体をはじめとする金属成分と油分との結合体が、汚濁洗浄液に残存していても、液体微細化装置3(液体微細化工程)で金属成分と油分との結合を分離して結合体を分解することができるので、その後の遠心分離機4(遠心分離工程)、浮上油回収装置5(浮上油回収工程)によって汚濁洗浄液を確実に浄化することができる。 In this way, according to the cleaning liquid purifying device or the cleaning liquid purification method according to the present embodiment, the combined metal component and oil content, including the combined aluminum component and oil component, remains in the polluted cleaning liquid. Even so, the liquid micronizer 3 (liquid micronization step) can separate the bond between the metal component and the oil and decompose the bond, so the subsequent centrifuge 4 (centrifuge step) floats. The pollutant cleaning liquid can be reliably purified by the oil recovery device 5 (floating oil recovery step).

また、本実施形態では、液体微細化装置3の上流側にバグフィルタ2が配置され、汚濁洗浄液を、バグフィルタ2に通過させてろ過することで汚濁洗浄液中の一定以上のサイズの固形分を除去(一次処理)してから、液体微細化装置3で処理するので、液体微細化装置3では、結合体を効率よく分解することができる(効果3)。 Further, in the present embodiment, the bag filter 2 is arranged on the upstream side of the liquid miniaturization device 3, and the pollutant cleaning liquid is passed through the bag filter 2 and filtered to remove solid content of a certain size or more in the pollutant cleaning liquid. Since it is removed (primary treatment) and then processed by the liquid miniaturization device 3, the liquid miniaturization device 3 can efficiently decompose the conjugate (effect 3).

さらに、浮上油回収装置5により処理された浄化洗浄液を貯留する浄化洗浄液タンク6と、浄化洗浄液タンク6内の浄化洗浄液を使用して金属加工品を洗浄して汚濁した汚濁洗浄液を貯留する汚濁洗浄液タンク1と、を備え、汚濁洗浄液タンク1と、バグフィルタ2と、液体微細化装置3と、遠心分離機4と、浮上油回収装置5と、浄化洗浄液タンク6とから、洗浄液の循環経路が形成されているので、洗浄液を循環させながら連続的に使用することができる(効果4)。 Further, a purification cleaning liquid tank 6 for storing the purification cleaning liquid processed by the floating oil recovery device 5, and a pollution cleaning liquid for storing the polluted cleaning liquid which is polluted by cleaning the metal processed product using the purification cleaning liquid in the purification cleaning liquid tank 6. A tank 1 is provided, and a cleaning liquid circulation path is provided from the pollutant cleaning liquid tank 1, the bag filter 2, the liquid miniaturization device 3, the centrifuge 4, the floating oil recovery device 5, and the purification cleaning liquid tank 6. Since it is formed, it can be used continuously while circulating the cleaning liquid (effect 4).

〔その他〕
以上本発明の実施形態を説明したが、本発明はその趣旨を逸脱しない範囲でかかる実施形態を種々変更して実施することができる。
例えば、上記の実施形態で説明した液体微細化装置3,遠心分離機4,浮上油回収装置5は一例であり、それぞれの機能を有するものであれば種々の装置を適用することができる。特に、液体微細化装置3は、液体の分子集団を微細化する、すなわち、液体分子間や液体分子と固体分子間の結合(特に、汚濁洗浄液中に含有される金属成分と油分の間の分子結合)を分離することができるものであればよい。
[Other]
Although the embodiments of the present invention have been described above, the present invention can be implemented by variously modifying such embodiments without departing from the spirit of the present invention.
For example, the liquid miniaturization device 3, the centrifuge 4, and the floating oil recovery device 5 described in the above embodiment are examples, and various devices can be applied as long as they have the respective functions. In particular, the liquid micronizing device 3 miniaturizes a liquid molecular group, that is, a bond between liquid molecules or between a liquid molecule and a solid molecule (particularly, a molecule between a metal component and an oil contained in a pollutant cleaning liquid). Anything that can separate the bond) will do.

1 汚濁洗浄液タンク(ダーティタンク)
2 バグフィルタ
3 液体微細化装置(微細水装置)
4 遠心分離機
5 浮上油回収装置
6 浄化洗浄液タンク(クリーンタンク)
7 ジェットポンプ
8 洗浄ノズル
9 洗浄液の処理経路
10 洗浄液の浄化装置
11 洗浄液の移動経路
30 処理容器
30a 洗浄液の流路
31 上流側タンク
32 ポンプ(洗浄液圧送装置)
33 下流側タンク
34 金属製メッシュ層
35 セラミックボール層
1 Pollution cleaning liquid tank (dirty tank)
2 Bug filter 3 Liquid miniaturization device (fine water device)
4 Centrifuge 5 Floating oil recovery device 6 Purifying and cleaning liquid tank (clean tank)
7 Jet pump 8 Cleaning nozzle 9 Cleaning liquid processing route 10 Cleaning liquid purification device 11 Cleaning liquid movement route 30 Processing container 30a Cleaning liquid flow path 31 Upstream tank 32 Pump (cleaning liquid pumping device)
33 Downstream tank 34 Metal mesh layer 35 Ceramic ball layer

Claims (5)

金属加工品を洗浄して汚濁した汚濁洗浄液を流通させることにより液体の分子集団を微細化する液体微細化装置と、
前記液体微細化装置により分子集団を微細化された洗浄液を遠心分離処理して前記洗浄液中の金属スラッジを回収し除去する遠心分離機と、
前記遠心分離機により処理された洗浄液中の油分を浮上回収する浮上油回収装置と、を備えている
ことを特徴とする洗浄液の浄化装置。
A liquid miniaturization device that miniaturizes a molecular group of liquids by cleaning metal processed products and distributing a polluted cleaning liquid.
A centrifuge that collects and removes metal sludge in the cleaning liquid by centrifuging the cleaning liquid whose molecular population has been refined by the liquid micronizing device.
A cleaning liquid purification device including a floating oil recovery device that floats and recovers oil in the cleaning liquid processed by the centrifuge.
前記液体微細化装置は、
前記汚濁洗浄液が流通する流路の上流側に配置され複数の金属製メッシュが装備された金属製メッシュ層と、前記流路の前記金属製メッシュ層よりも下流側に配置され複数のセラミックボールが装備されたセラミックボール層とが内装された処理容器と、
前記処理容器内に前記汚濁洗浄液を所定圧以上且つ所定速度以上で通過させる洗浄液圧送装置と、を有している
ことを特徴とする請求項1に記載された洗浄液の浄化装置。
The liquid miniaturization device is
A metal mesh layer arranged on the upstream side of the flow path through which the pollutant cleaning liquid flows and equipped with a plurality of metal meshes, and a plurality of ceramic balls arranged on the downstream side of the metal mesh layer of the flow path. A processing container with an equipped ceramic ball layer and
The cleaning liquid purification device according to claim 1, further comprising a cleaning liquid pressure feeding device for passing the polluted cleaning liquid through the processing container at a predetermined pressure or higher and a predetermined speed or higher.
前記液体微細化装置の上流側に、前記汚濁洗浄液を一次処理するバグフィルタが配置されている
ことを特徴とする請求項1又は2に記載された洗浄液の浄化装置。
The cleaning liquid purification device according to claim 1 or 2, wherein a bug filter for primary treatment of the polluted cleaning liquid is arranged on the upstream side of the liquid miniaturization device.
前記浮上油回収装置により処理された浄化洗浄液を貯留する浄化洗浄液タンクと、
前記浄化洗浄液タンク内の前記浄化洗浄液を使用して前記金属加工品を洗浄して汚濁した前記汚濁洗浄液を貯留する汚濁洗浄液タンクと、を備え、
洗浄液の循環経路が形成されている
ことを特徴とする請求項1〜3の何れか1項に記載された洗浄液の浄化装置。
A purification and cleaning liquid tank for storing the purification and cleaning liquid processed by the floating oil recovery device, and
A pollutant cleaning liquid tank for storing the polluted cleaning liquid that has been polluted by cleaning the metal processed product using the purifying cleaning liquid in the purifying cleaning liquid tank is provided.
The cleaning liquid purification device according to any one of claims 1 to 3, wherein a circulation route for the cleaning liquid is formed.
金属加工品を洗浄して汚濁した洗浄液を液体微細化装置に流通させて液体の分子集団を微細化する液体微細化工程と、
前記液体微細化工程により分子集団を微細化された洗浄液を遠心分離処理して前記洗浄液中の金属スラッジを回収し除去する遠心分離工程と、
前記遠心分離工程により処理された洗浄液中の油分を浮上回収する浮上油回収工程と、を備えている
ことを特徴とする洗浄液の浄化方法。
A liquid miniaturization process in which a metal processed product is washed and a polluted cleaning liquid is distributed to a liquid miniaturization device to miniaturize a molecular group of the liquid.
A centrifugal separation step of centrifuging a cleaning liquid whose molecular population has been refined by the liquid refining step to collect and remove metal sludge in the cleaning liquid.
A method for purifying a cleaning liquid, which comprises a floating oil recovery step for floating and recovering oil in the cleaning liquid treated by the centrifugation step.
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