JP2016140808A - Global environment improvement apparatus - Google Patents

Global environment improvement apparatus Download PDF

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JP2016140808A
JP2016140808A JP2015017353A JP2015017353A JP2016140808A JP 2016140808 A JP2016140808 A JP 2016140808A JP 2015017353 A JP2015017353 A JP 2015017353A JP 2015017353 A JP2015017353 A JP 2015017353A JP 2016140808 A JP2016140808 A JP 2016140808A
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oil
water
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global environment
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健太郎 石栗
Kentaro Ishikuri
健太郎 石栗
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Shinko Japan Co Ltd
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  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
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Abstract

PROBLEM TO BE SOLVED: To achieve separation between oil and water by a liquid electrolyzing technique in first treatment of waste liquid, wastewater, sewage and the like containing oil, and to further detoxify the separated water by, if necessary, applying spray drying, electrolytic separation, or electrolytic sterilization.SOLUTION: A global environment improvement apparatus for detoxifying waste liquid to be treated includes individual devices for treating waste liquid to be treated, in multiple stages. The individual device arranged at a preceding stage is a liquid electrolyzer exhibiting a function for oil-water separation of the waste liquid to be treated, its special electrode comprises a plurality of plate-shaped electrodes arranged to face each other, and a power source supplied to the special electrode is an AC-DC dual-use high-speed electrolytic power source.SELECTED DRAWING: Figure 1

Description

本発明は、主として、油成分と化学物質成分や金属成分と水成分とからなる混合物から構成された廃液の無公害化処理に関する地球環境改善機器の技術分野に属する。   The present invention mainly belongs to the technical field of global environment improvement equipment relating to pollution-free treatment of waste liquid composed of a mixture comprising an oil component and a chemical component, or a metal component and a water component.

廃液、排水や汚水等の無害化処理は地球環境保全の重要な緊急課題の一つであって、改善技術の開発には世界が積極的に取り組んでいるところである。しかし、廃液、排水や汚水の種類や性質は多種多様に亘り、処理技術も画一化されていないのが現況である。 Detoxification treatment of waste liquid, drainage, sewage, etc. is one of the important urgent issues for global environmental conservation, and the world is actively working on the development of improvement technology. However, there are a wide variety of types and properties of waste liquid, drainage and sewage, and the current state of treatment technology is not standardized.

水処理技術やその関連技術は多数存在するところ、特許文献1(特開2005−329380号公報)に記載される発明は、「水系廃液の蒸発濃縮装置において、水系廃液の加熱手段としてのヒーターと、このヒーターを組み込んで水系廃液を蒸発濃縮するための濃縮室と、濃縮室で発生した蒸気を冷却し液化するために冷却水を通水する冷却管と、この冷却管を収納する冷却室と、濃縮室と冷却室を減圧するためのエジェクタと、エジェクタに通水する循環水を送水する循環ポンプと、循環水を貯水する循環タンクと、循環水に含まれる油分を分離・除去・吸着するための油水分離ユニットより構成されることを特徴とする水系廃液の蒸発濃縮装置」というものである。   Although there are many water treatment technologies and related technologies, the invention described in Patent Document 1 (Japanese Patent Application Laid-Open No. 2005-329380) describes “a heater as a heating means for an aqueous waste solution in an evaporation concentration apparatus for an aqueous waste solution” A concentration chamber for evaporating and concentrating the aqueous waste liquid by incorporating this heater, a cooling pipe for passing cooling water to cool and liquefy the steam generated in the concentration chamber, and a cooling chamber for storing the cooling pipe, , Separating, removing, and adsorbing oil contained in the circulating water, an ejector for decompressing the concentrating chamber and the cooling chamber, a circulating pump for supplying circulating water to the ejector, a circulating tank for storing the circulating water, and The water-based waste liquid evaporating and concentrating device is characterized by comprising an oil-water separation unit for the purpose.

また、特許文献2(特許第3358786号公報)に記載される発明は、「界面活性剤と、該界面活性剤の作用によって乳化した油分とを含有する排水の油水分離方法において、多孔性隔膜によって仕切られた陽極室と陰極室にそれぞれ陽極と陰極を設け、該陽極と陰極の間に直流電圧が印可されている隔膜電解工程の陽極室に、前記排水を送液して電解処理し、該陽極処理液の一部は隔膜を通過させて陰極室から排出し、残部の陽極処理液を陽極室から排出して気液分離器の中間部に導入し、気液分離器の上部より該液の一部を抜き出し、付着材が充填された充填層に導入して付着材と接触させた後に、油水分離工程に導き油水分離すると共に、気液分離器の底部より残部を抜き出して、電解工程への送液中に循環することを特徴とする乳化油分含有排水の油水分離方法」というものである。 In addition, the invention described in Patent Document 2 (Japanese Patent No. 3358786) is “in a method for separating oil and water containing a surfactant and an oil emulsified by the action of the surfactant. An anode and a cathode are provided in the partitioned anode chamber and cathode chamber, respectively, and the waste water is sent to the anode chamber of the diaphragm electrolysis process in which a DC voltage is applied between the anode and the cathode, and the electrolytic treatment is performed. Part of the anodizing liquid passes through the diaphragm and is discharged from the cathode chamber, and the remaining anodizing liquid is discharged from the anode chamber and introduced into the middle part of the gas-liquid separator. After extracting a part of the sample and introducing it into the packed bed filled with the adhering material and bringing it into contact with the adhering material, the oil-water separation process is led to the oil-water separation process, and the remaining part is extracted from the bottom of the gas-liquid separator. Milk that circulates during feeding Is that oil-water separation method oil-containing waste water. "

また、特許文献3(特許第5197273号公報)に記載される発明は、「セラミックスの粉末にバインダが添加されたスラリーを噴霧乾燥室内に液滴として噴霧し、該液滴を乾燥させることによって造粒された顆粒を得る噴霧乾燥装置において、前記噴霧乾燥室の内壁の一部に、ガラスファイバー,カーボンファイバー,セラミックファイバーおよびセラミックウィスカーのうち少なくとも1種の繊維状無機物をフッ素樹脂でコーティングした層が形成されていることを特徴とする噴霧乾燥装置」というものである。   In addition, the invention described in Patent Document 3 (Japanese Patent No. 5197273) describes that “a slurry in which a binder is added to ceramic powder is sprayed as droplets in a spray drying chamber and the droplets are dried. In the spray drying apparatus for obtaining granulated granules, a layer obtained by coating at least one fibrous inorganic substance of glass fiber, carbon fiber, ceramic fiber and ceramic whisker with a fluororesin is formed on a part of the inner wall of the spray drying chamber. The spray drying apparatus is characterized in that it is formed.

特開2005−329380号公報JP 2005-329380 A 特許第3358786号公報Japanese Patent No. 3358786 特許第5197273号公報Japanese Patent No. 5197273

本出願人は水処理に関する永年の研究や実験から得た知見を元に、特に切削油等(クーラントも含む)に代表される油分を含む廃液、排水や汚水等の無害化処理に当たって、まず、油分と水分とを分離することが肝要であるとの考えに至った。そこでまず、油と金属イオンとがくっつかないことを利用して、油分を含む廃液、排水や汚水等の当初の処理は液電解技術により油と水との分離を達成し、分離された水のさらなる無害化処理には必要に応じて電解分離処理や電解殺菌処理や噴霧乾燥処理を適用して無害化することにより課題の解決を図った。   Based on the knowledge gained from years of research and experiments on water treatment, the present applicant, in particular, in the detoxification treatment of waste liquids including oil, such as cutting oil (including coolant), drainage and sewage, It came to the idea that it is important to separate oil and water. First of all, by utilizing the fact that oil and metal ions do not stick together, the initial treatment of oil-containing waste liquid, waste water, sewage, etc. achieved separation of oil and water by liquid electrolysis technology, and the separated water To further detoxify treatment, the solution was solved by applying electrolytic separation treatment, electrolytic sterilization treatment, and spray drying treatment as necessary.

この地球環境改善機器は、要処理廃液の無害化を行う地球環境改善機器において、要処理廃液を多段階で処理する個別処理装置を備え、前段側に配置される前記個別装置は前記要処理廃液を油水分離する機能を発揮する液電解処理装置であり、その特殊電極が、複数枚の対向配置されたプレート状電極であると共に、上記特殊電極に供給される電源は、交直両用の高速電解電源である、ことを特徴とする地球環境改善機器。   This global environment improvement device is a global environment improvement device that detoxifies the waste liquid to be processed, and includes an individual processing device that processes the waste liquid to be processed in multiple stages, and the individual device disposed on the front side is the waste liquid to be processed Is a liquid electrolytic treatment apparatus that exhibits the function of separating oil and water, and the special electrode is a plurality of plate electrodes arranged opposite to each other, and the power supplied to the special electrode is a high-speed electrolytic power supply for both AC and DC A global environment improvement device characterized by that.

また、この地球環境改善機器は、前記プレート状電極の正面形状は概略方形である、ことを特徴とする。   Moreover, this global environment improvement apparatus is characterized in that the front shape of the plate-like electrode is a substantially rectangular shape.

また、この地球環境改善機器は、前記プレート状電極の正面形状は概略円形である、ことを特徴とする。   Further, in this global environment improving device, the front shape of the plate-like electrode is substantially circular.

また、この地球環境改善機器において、前記油水分離後の油成分は、前記液電解処理装置から回収される、ことを特徴とする。   Moreover, in this global environment improvement apparatus, the oil component after the said oil-water separation is collect | recovered from the said liquid electrolysis processing apparatus.

また、この地球環境改善機器において、前記油水分離後の水成分は、さらに高速電解殺菌装置によって、殺菌処理を受けることを特徴とする。   Moreover, in this global environment improvement apparatus, the water component after the oil-water separation is further subjected to a sterilization treatment by a high-speed electrolytic sterilization apparatus.

また、この地球環境改善機器において、前記油水分離後の水成分は、過給器により空気と熱源とが付与されるスプレー塔に送られて噴霧乾燥処理された後、直流電源が付与されるイオン化電極からなる集塵電極を有する電気集塵器で粒子を吸着した後、大気クリーン排気として放出される、ことを特徴とする。 Further, in this global environment improvement device, the water component after the oil-water separation is ionized by being supplied to a spray tower to which air and a heat source are provided by a supercharger and spray-dried, and then provided with a DC power source. It is characterized in that the particles are adsorbed by an electric dust collector having a dust collecting electrode composed of electrodes and then discharged as an air clean exhaust.

本発明の地球環境改善機器によれば、油成分と化学物質成分や金属成分と水成分とからなる混合物から構成された廃液は油成分と水成分とに分離され、引き続き処理対象や処理目標が明確化された処理が進められるので、無害化処理の効率的進捗がし易くなる。   According to the global environment improvement device of the present invention, the waste liquid composed of the mixture of the oil component and the chemical component, the metal component and the water component is separated into the oil component and the water component. Since the clarified process is advanced, the detoxification process can be progressed efficiently.

また、請求項2の発明によれば、電解用電極の作成が簡素化されると共に、電極の汚れ低減に寄与することができる。   Moreover, according to the invention of claim 2, the production of the electrode for electrolysis is simplified, and it can contribute to the reduction of contamination of the electrode.

また、請求項3の発明によれば、より一層電極の汚れ低減に寄与することができる。   Further, according to the invention of claim 3, it is possible to further contribute to the reduction of contamination of the electrode.

また、請求項4の発明によれば、回収した油成分を有価で取引できるので、省資源に対する効果が大きい。   According to the invention of claim 4, since the recovered oil component can be traded with value, the effect on resource saving is great.

また、請求項5の発明によれば、油水分離後の水成分は、さらに高速電解殺菌装置によって殺菌処理を受けることとなるので、廃液、排水や汚水等と呼ばれる成分の油液分離度はさらに高まり、水成分の殺菌効果も大いに高まる。   According to the invention of claim 5, since the water component after the oil-water separation is further subjected to a sterilization treatment by the high-speed electrolytic sterilization device, the oil-liquid separation degree of the components called waste liquid, drainage, sewage and the like is further increased. The sterilizing effect of the water component is greatly enhanced.

また、請求項6の発明によれば、噴霧乾燥と電気集塵により微粒子さえも含まれない大気クリーン排気が達成されるので環境に好適な無害化処理が達成される。そして、集塵電極に回収された有用物の資源化も可能であるし、集塵電極によるゴミの粉体減容化も可能となるので、産業廃棄物管理表(マニフェスト)は不要となり、廃液が製造工程や工場内で処理可能となって、運搬燃料費や管理工数の削減によるCo削減に寄与するところが大きい。 Further, according to the invention of claim 6, the atmosphere-cleaning exhaust that does not contain even fine particles is achieved by spray drying and electrostatic dust collection, so that a detoxification process suitable for the environment is achieved. In addition, it is possible to recycle useful materials collected in the dust collection electrode, and it is also possible to reduce the volume of dust by using the dust collection electrode, so an industrial waste management table (manifest) is not required, and waste liquid Can be processed in the manufacturing process and in the factory, and greatly contributes to CO 2 reduction by reducing transportation fuel cost and management man-hours.

主として電解油水分離装置や電解分離装置や高速電解殺菌装置や電気集塵塔とからなる地球環境改善機器の一例の説明図である。It is explanatory drawing of an example of the global environment improvement apparatus which mainly consists of an electrolytic oil water separator, an electrolytic separator, a high-speed electrolytic sterilizer, and an electrostatic precipitator. 主として電解油水分離装置や電解分離装置や高速電解殺菌装置や電気集塵塔とからなる地球環境改善機器の他の例の説明図である。It is explanatory drawing of the other example of the global environment improvement apparatus mainly consisting of an electrolytic oil water separator, an electrolytic separator, a high-speed electrolytic sterilizer, and an electrostatic precipitator. 円形電極の正面の説明図である。It is explanatory drawing of the front of a circular electrode. 円形電極の側面の説明図である。It is explanatory drawing of the side surface of a circular electrode. 円形電極を説明する斜視図である。It is a perspective view explaining a circular electrode.

本願発明を実施する形態として、要処理廃液の無害化を行う地球環境改善機器において、要処理廃液を多段階で処理する個別処理装置を備え、前段側に配置される前記個別装置は前記要処理廃液を油水分離する機能を発揮する液電解処理装置であり、その特殊電極が、複数枚の対向配置されたプレート状電極であると共に、上記特殊電極に供給される電源は、交直両用の高速電解電源である、ことを特徴とする地球環境改善機器、とすることができる。   As an embodiment for carrying out the invention of the present application, in a global environment improvement device for detoxifying treatment waste liquid, the individual device disposed in the previous stage is provided with an individual treatment device for treating the treatment waste liquid in multiple stages. This is a liquid electrolysis processing device that exhibits the function of separating waste water from oil and water. The special electrode is a plurality of plate electrodes arranged opposite to each other, and the power supplied to the special electrode is AC / DC high-speed electrolysis. It can be set as the global environment improvement apparatus characterized by being a power supply.

また、前記プレート状電極の正面形状は概略方形である、ことを特徴とする請求項1に記載される地球環境改善機器、とすることができる。 The global environment improving device according to claim 1, wherein a front shape of the plate-like electrode is a substantially square shape.

また、前記プレート状電極の正面形状は概略円形である、ことを特徴とする請求項1に記載される地球環境改善機器、とすることができる。 The global environment improving device according to claim 1, wherein a front shape of the plate-like electrode is substantially circular.

また、前記油水分離後の油成分は、前記液電解処理装置から回収される、ことを特徴とする請求項1〜3に記載される地球環境改善機器、とすることができる。   Moreover, it can be set as the global environment improvement apparatus described in Claims 1-3 by which the oil component after the said oil-water separation is collect | recovered from the said liquid electrolysis processing apparatus.

また、前記油水分離後の水成分は、さらに高速電解殺菌装置によって、殺菌処理を受けることを特徴とする請求項1〜4に記載される地球環境改善機器、とすることができる。 Moreover, the water component after the oil-water separation is further subjected to a sterilization treatment by a high-speed electrolytic sterilization apparatus, and the global environment improving device according to any one of claims 1 to 4 can be obtained.

また、前記油水分離後の水成分は、過給器により空気と熱源とが付与されるスプレー塔に送られて噴霧乾燥処理された後、直流電源が付与されるイオン化電極からなる集塵電極を有する電気集塵器で粒子を吸着した後、大気クリーン排気として放出される、ことを特徴とする請求項1〜5に記載される地球環境改善機器、とすることができる。 Further, the water component after the oil-water separation is sent to a spray tower to which air and a heat source are applied by a supercharger and spray-dried, and then a dust collecting electrode including an ionization electrode to which a DC power source is applied. It can be set as the global environment improvement apparatus as described in any one of Claims 1-5 characterized by discharging | emitting as air | atmosphere clean exhaust, after adsorb | sucking particle | grains with the electric dust collector which has.

以下、本発明の実施例を図面を参照しながら説明する。 Embodiments of the present invention will be described below with reference to the drawings.

図1は本願発明に係る主として電解油水分離装置や電解分離装置や高速電解殺菌装置や電気集塵塔とからなる地球環境改善機器の一例の説明図である。
一旦廃液槽4に貯留された廃液は送液ポンプ5により電解分離電極槽2に送られた後、電解分離電極3により電解分離処理を受ける。電解分離電極3により油水の分離が行われて一般的に油液層と夾雑物層と水成分層の三層に綺麗に分離される。廃液は、水成分の上方に油成分が浮く形で貯留されることとなる。廃液中の金属イオンと油成分はくっつき合うことがないので上方に浮かんだ油成分に金属イオンがくっつかないことは処理上好都合である。
電解分離電極2で三層に分離された廃液から少なくとも最上層の油成分は送油管6を介して油液回収層7に回収され、所望により再処理を経て有価で取引することができるので、省資源に大いに寄与することができる。その際に、夾雑物を並行して回収することを妨げるものでは決してない。
FIG. 1 is an explanatory diagram of an example of a global environment improvement device mainly composed of an electrolytic oil / water separator, an electrolytic separator, a high-speed electrolytic sterilizer, and an electrostatic precipitator according to the present invention.
The waste liquid once stored in the waste liquid tank 4 is sent to the electrolytic separation electrode tank 2 by the liquid feed pump 5 and then subjected to electrolytic separation treatment by the electrolytic separation electrode 3. Oil / water is separated by the electrolytic separation electrode 3 and is generally cleanly separated into three layers of an oil liquid layer, a contaminant layer and a water component layer. The waste liquid is stored in a form in which the oil component floats above the water component. Since the metal ions and the oil component in the waste liquid do not stick to each other, it is advantageous in terms of treatment that the metal ions do not stick to the oil component floating upward.
Since at least the uppermost oil component is recovered from the waste liquid separated into three layers by the electrolytic separation electrode 2 to the oil liquid recovery layer 7 through the oil feed pipe 6, and can be traded valuable by reprocessing as desired. It can greatly contribute to resource saving. At that time, it does not prevent the collection of foreign matters in parallel.

電解分離電極槽2で油成分を回収された廃液は電解油水分離槽1に送られて、必要に応じてさらなる電解油水分離や電解分離や高速電解殺菌を受けることができる。図1の例では、次段に高速電解殺菌装置9が備わっていて電解油水分離槽1から第1送液管15を介して高速電解殺菌装置9に送られた廃液は、さらなる電解処理を受けることができる。キャスター21が下部に設置されてユニット化が可能な高速電解殺菌装置9で、電解分離電極3により高速電解殺菌を行うことができる。高速電解殺菌装置9で殺菌と電解分離がなされた処理液は、さらに油液と夾雑物を分離して、分離された油液や夾雑物を油液、夾雑物回収管12から回収して、水成分や夾雑物は電解殺菌された清潔な状態で第2送液管15−1を介して貯留槽11にほぼ水成分と夾雑物とからなる処理液として貯留される。 The waste liquid from which the oil component has been recovered in the electrolytic separation electrode tank 2 is sent to the electrolytic oil / water separation tank 1 and can be subjected to further electrolytic oil / water separation, electrolytic separation, and high-speed electrolytic sterilization as necessary. In the example of FIG. 1, the high-speed electrolytic sterilization device 9 is provided in the next stage, and the waste liquid sent from the electrolytic oil / water separation tank 1 to the high-speed electrolytic sterilization device 9 via the first liquid feeding pipe 15 is subjected to further electrolytic treatment. be able to. The high-speed electrolytic sterilization apparatus 9 in which the caster 21 is installed in the lower part and can be unitized can perform high-speed electrolytic sterilization by the electrolytic separation electrode 3. The treatment liquid that has been sterilized and electrolytically separated by the high-speed electrolytic sterilization apparatus 9 further separates the oil liquid and the foreign substances, and collects the separated oil liquid and foreign substances from the oil liquid and the foreign substance collection pipe 12, The water component and impurities are stored in the storage tank 11 as a treatment liquid substantially composed of water components and impurities via the second liquid feeding pipe 15-1 in a clean state that has been subjected to electrolytic sterilization.

各種の電解分離や高速電解殺菌を受けた後の廃液は細菌類の含有が少なく、油成分も取り除かれているから、基本的に水成分と夾雑物とからなっている。このような水成分主体の処理液は、送水管16内を送水される間に、加熱器13により好ましくは直接加熱を受けて処理水は110℃〜160℃に昇温されて噴霧ユニット22に送られる。一方、過給機23からも熱と空気が空気、熱伝達管14を通って噴霧ユニット22に送られる。噴霧ユニット22から第1送気管17に吹き出された熱の力により、処理水は上昇過程で気化され、夾雑物は乾燥される。横行する第2送気管18と下降する第3送気管19で更に気化と乾燥作用を受けた処理水は最終送気管20に至る。更にキャスター21を有してユニット化されている電気集塵塔27で電気集塵により気体中の夾雑物を分離回収して、空気や水蒸気はクリーン排気として排気排出管31より大気中に排出される。 The waste liquid after various types of electrolytic separation and high-speed electrolytic sterilization is basically composed of water components and contaminants because it contains little bacteria and oil components are removed. Such a water component-based treatment liquid is preferably heated directly by the heater 13 while being fed through the water feed pipe 16, and the treated water is heated to 110 ° C. to 160 ° C. to reach the spray unit 22. Sent. On the other hand, heat and air are also sent from the supercharger 23 to the spray unit 22 through the air and the heat transfer pipe 14. Due to the heat force blown from the spray unit 22 to the first air supply pipe 17, the treated water is vaporized in the ascending process, and impurities are dried. The treated water that has been further vaporized and dried by the traversing second air pipe 18 and the descending third air pipe 19 reaches the final air pipe 20. Further, the dust collector 27 having a caster 21 separates and collects impurities in the gas by electrostatic dust collection, and the air and water vapor are discharged into the atmosphere from the exhaust discharge pipe 31 as clean exhaust. The

図2は本願発明に係る主として電解油水分離装置や電解分離装置や高速電解殺菌装置で電解分離電極3により電解分離処理を受ける。
電解分離電極3により油水の分離が行われて一般的に油液層と夾雑物層と水成分層の三層に綺麗に分離される。廃液は、水成分の上方に油成分が浮く形で貯留されることとなる。廃液中の金属イオンと油成分はくっつき合うことがないので上方に浮かんだ油成分に金属イオンがくっつかないことは処理上好都合である。
電解分離電極2で三層に分離された廃液から少なくとも最上層の油成分は送油管6を介して油液回収層7に回収され、所望により再処理を経て有価で取引することができるので、省資源に大いに寄与することができる。その際に、夾雑物を並行して回収することを妨げるものでは決してない。夾雑物も油成分と並行して回収してしまうのも有力な手法であることに変わりはない。処理水を電解分離したり高速電解殺菌した後の分離槽に発生する油液層や夾雑物層を回収する手法を採れば、水成分の再利用も法に叶う範囲で可能である。
FIG. 2 is subjected to electrolytic separation treatment by the electrolytic separation electrode 3 mainly in an electrolytic oil / water separator, electrolytic separator, or high-speed electrolytic sterilizer according to the present invention.
Oil / water is separated by the electrolytic separation electrode 3 and is generally cleanly separated into three layers of an oil liquid layer, a contaminant layer and a water component layer. The waste liquid is stored in a form in which the oil component floats above the water component. Since the metal ions and the oil component in the waste liquid do not stick to each other, it is advantageous in terms of treatment that the metal ions do not stick to the oil component floating upward.
Since at least the uppermost oil component is recovered from the waste liquid separated into three layers by the electrolytic separation electrode 2 to the oil liquid recovery layer 7 through the oil feed pipe 6, and can be traded valuable by reprocessing as desired. It can greatly contribute to resource saving. At that time, it does not prevent the collection of foreign matters in parallel. It is still a powerful technique to collect impurities in parallel with oil components. If a method of recovering the oil liquid layer and the contaminant layer generated in the separation tank after electrolytic separation of the treated water or high-speed electrolytic sterilization is adopted, the water component can be reused as long as the method is applicable.

電解油水分離槽1で油成分を回収された処理液は次段の電解油水分離槽1に送られて、必要に応じてさらなる電解油水分離や電解分離や高速電解殺菌を受けることができる。図2の例では、次段に高速電解殺菌装置9が備わっていて電解油水分離槽1から高速電解殺菌装置9に送られた処理液は、さらなる電解処理を受けることができる。キャスター21が下部に設置されてユニット化が可能な高速電解殺菌装置9で、電解分離電極3により高速電解殺菌を行うことができる。高速電解殺菌装置9で殺菌と電解分離がなされた処理液は、さらに油液と夾雑物を分離して、分離された油液や夾雑物を油液、夾雑物回収管12から油液、夾雑物回収槽10に回収して、水成分や含まれている夾雑物は電解殺菌された清潔な状態で加熱送水管24を経て加温されて噴霧ユニット22に送られる。 The treatment liquid from which the oil component has been recovered in the electrolytic oil / water separation tank 1 is sent to the subsequent electrolytic oil / water separation tank 1 and can undergo further electrolytic oil / water separation, electrolytic separation, and high-speed electrolytic sterilization as necessary. In the example of FIG. 2, the high-speed electrolytic sterilization device 9 is provided in the next stage, and the treatment liquid sent from the electrolytic oil / water separation tank 1 to the high-speed electrolytic sterilization device 9 can be subjected to further electrolytic treatment. The high-speed electrolytic sterilization apparatus 9 in which the caster 21 is installed in the lower part and can be unitized can perform high-speed electrolytic sterilization by the electrolytic separation electrode 3. The treatment liquid that has been sterilized and electrolytically separated by the high-speed electrolysis sterilizer 9 further separates the oil liquid and impurities, and then separates the separated oil liquid and impurities from the oil liquid and the impurities collection tube 12 into the oil liquid and impurities. The water components and impurities contained in the material recovery tank 10 are heated in a clean state that has been subjected to electrolytic sterilization through the heated water supply pipe 24 and sent to the spray unit 22.

各種の電解分離や高速電解殺菌を受けた後の廃液は細菌類の含有が少なく、油成分も取り除かれているから、基本的には水成分と夾雑物とからなっている。このような水成分主体の処理液は、加熱送水管24内を送水される間に加熱されて、噴霧ユニット22に送られる。一方、過給機23からも熱と空気が噴霧ユニット22に送られる。噴霧ユニット22からスプレー塔25内に噴霧された処理水は、下降過程で気化され、夾雑物は乾燥される。乾燥した微粒子を含んだ気体状態の処理液は電気集塵塔27に送られる。電気集塵塔27には少なくとも一対の直流電極28がアースされており、直流電極28間に設けられた集塵電極29には直流電源30から直流電源が印加されているので、混合気中の粉体は集塵電極29に吸着されて回収される。集塵電極29により粉体が吸着された気体は、クリーン排気として排気排出管31から大気中に放出される。集塵電極29に吸着されて回収された粉体は有用物として再利用されたり、産業廃棄物として減容化されて廃棄に向けられる。 The waste liquid after various types of electrolytic separation and high-speed electrolytic sterilization is low in bacteria content and oil components are removed, so it basically consists of water and impurities. Such a treatment liquid mainly composed of a water component is heated while being fed through the heated water feed pipe 24 and sent to the spray unit 22. On the other hand, heat and air are also sent from the supercharger 23 to the spray unit 22. The treated water sprayed from the spray unit 22 into the spray tower 25 is vaporized in the descending process, and impurities are dried. The treatment liquid in a gaseous state containing the dried fine particles is sent to the electrostatic precipitator 27. At least a pair of DC electrodes 28 are grounded in the electric dust collection tower 27, and a DC power supply is applied from a DC power supply 30 to a dust collection electrode 29 provided between the DC electrodes 28. The powder is adsorbed by the dust collecting electrode 29 and collected. The gas having the powder adsorbed by the dust collecting electrode 29 is released into the atmosphere from the exhaust discharge pipe 31 as clean exhaust. The powder adsorbed and collected by the dust collecting electrode 29 is reused as a useful material, or reduced in volume as an industrial waste and directed to disposal.

図3には本願の電解分離に用いられる円形電極の正面の説明図が示されている。電解分離に用いられる円形電極40には夫々正端子41または負端子42が取り付けられていて、正端子41同士と負端子42同士は互いに配線で導電関係を担保されている。電解分離に用いられる円形電極40には図2にも示されるように交直両用の高速電解電源8から給電される。用いられるものが円形電極であれ、方形電極であれ、プレート電極の面が荒れていたり滑らかさを欠くと電解効率を大きく損ねるので端面にはアール加工を施すのがよい。 FIG. 3 shows a front view of a circular electrode used for electrolytic separation of the present application. A positive terminal 41 or a negative terminal 42 is attached to each of the circular electrodes 40 used for electrolytic separation, and the positive terminals 41 and the negative terminals 42 are secured to each other by wiring. As shown in FIG. 2, the circular electrode 40 used for electrolytic separation is supplied with power from an AC / DC high-speed electrolytic power source 8. Regardless of whether the electrode used is a circular electrode or a square electrode, the surface of the plate electrode is rough or lacks smoothness, so that the electrolysis efficiency is greatly impaired.

図4には本願の電解分離に用いられる円形電極の側面の説明図が示されている。正電極41a〜41n間には負電極42a〜42nが互いに対向するように設けられている。電解電極は41a〜41nと42a〜42nとからなってユニット化されているので、電解電極のユニット数を調整することにより、電解処理装置の容量や処理液の種類等に適切に対応できる。 FIG. 4 shows a side view of a circular electrode used for electrolytic separation of the present application. Negative electrodes 42a to 42n are provided between the positive electrodes 41a to 41n so as to face each other. Since the electrolytic electrode is composed of 41a to 41n and 42a to 42n, it is possible to appropriately cope with the capacity of the electrolytic processing apparatus, the type of the processing solution, and the like by adjusting the number of units of the electrolytic electrode.

図5には本願の電解分離に用いられる円形電極を説明する斜視図が示されている。このようにユニット化された電解電極が用意されており、図1、図2にも示されるように、本発明の電解装置が要処理廃液を多段階で処理する個別処理装置を備えるという、ユニット化の精神が行き届いているので、各種処理或いは処理装置の規模や容量に合わせて処理装置の選択が自由で、処理液の浄化の幅を広げることができる。 FIG. 5 is a perspective view for explaining a circular electrode used for electrolytic separation of the present application. A unitized electrolytic electrode is prepared in this way, and as shown in FIGS. 1 and 2, the electrolysis apparatus of the present invention is provided with an individual processing apparatus for processing waste liquids to be processed in multiple stages. Therefore, the processing apparatus can be freely selected in accordance with the scale and capacity of each processing or processing apparatus, and the range of purification of the processing liquid can be widened.

以上、本発明の実施例について説明してきたが、この発明の地球環境改善機器は廃液の油水分離を電解油水分離でまず行った後、水処理をするものであるから、産業用工場などからの切削、研磨などの廃液やメッキ工場、食品工場などの廃液処理に適用して大幅なコスト削減に寄与できるので、産業界に広く受け入れられることが期待できる。
本発明はその精神や主要な特徴から逸脱することなく、他の種々な形で実施することができる。そのため、前述の実施例は単なる例示に過ぎず、本発明を限定的に解釈してはならない。
As mentioned above, although the Example of this invention has been described, since the earth environment improvement apparatus of this invention performs the water treatment after performing the oil-water separation of the waste liquid first by the electrolytic oil-water separation, from the industrial factory etc. It can be applied to waste liquids such as cutting and polishing, and waste liquid treatment at plating factories, food factories, etc., and can be expected to be widely accepted by industry.
The present invention can be implemented in various other forms without departing from the spirit and main features thereof. For this reason, the above-described embodiments are merely examples, and the present invention should not be construed in a limited manner.

1 電解油水分離槽
2 電解分離電極槽
3 電解分離電極
4 廃液槽
5 送液ポンプ
6 送油管
7 油液回収槽
8 交直両用の高速電解電源
9 高速電解殺菌装置
10 油液、夾雑物回収槽
11 貯留槽
12 油液、夾雑物回収管
13 加熱器
14 空気、熱源伝達管
15 第1送液管
15−1 第2送液管
16 送水管
17 第1送気管
18 第2送気管
19 第3送気管
20 最終送気管
21 キャスター
22 噴霧ユニット
23 過給器
24 加熱送水管
25 スプレー塔
27 電気集塵塔
28 直流電極
29 集塵電極
30 直流電極電源
31 排気排出管
40 円形電極
40a〜n 個々の円形電極群
41 正端子
41a〜n 個々の正端子
42 負端子
42a〜n 個々の負端子
DESCRIPTION OF SYMBOLS 1 Electrolytic oil water separation tank 2 Electrolytic separation electrode tank 3 Electrolytic separation electrode 4 Waste liquid tank 5 Liquid feed pump 6 Oil feed pipe
7 Oil / Liquid Recovery Tank 8 AC / DC High-Speed Electrolytic Power Supply 9 High-Speed Electrolysis Sterilizer 10 Oil / Solids Recovery Tank 11 Storage Tank
12 Oil / Contaminant Recovery Pipe 13 Heater 14 Air / Heat Source Transfer Pipe 15 First Liquid Supply Pipe 15-1 Second Liquid Supply Pipe 16 Water Supply Pipe 17 First Air Supply Pipe 18 Second Air Supply Pipe 19 Third Air Supply Pipe 20 Final air supply pipe 21 Caster 22 Spray unit 23 Supercharger 24 Heating water supply pipe 25 Spray tower 27 Electric dust collection tower 28 DC electrode 29 Dust collection electrode 30 DC electrode power supply 31 Exhaust discharge pipe 40 Circular electrodes 40a-n Individual circular electrode group 41 Positive terminals 41a-n Individual positive terminals 42 Negative terminals 42a-n Individual negative terminals

Claims (6)

要処理廃液の無害化を行う地球環境改善機器において、要処理廃液を多段階で処理する個別処理装置を備え、前段側に配置される前記個別装置は前記要処理廃液を油水分離する機能を発揮する液電解処理装置であり、その特殊電極が、複数枚の対向配置されたプレート状電極であると共に、上記特殊電極に供給される電源は、交直両用の高速電解電源である、ことを特徴とする地球環境改善機器。   In a global environment improvement device that detoxifies waste liquid requiring treatment, it is equipped with an individual treatment device that treats waste liquid to be treated in multiple stages, and the individual device arranged on the front side demonstrates the function of separating the waste liquid requiring treatment into oil and water. And a special electrode is a plurality of plate electrodes arranged opposite to each other, and the power supplied to the special electrode is a high-speed electrolytic power supply for both AC and DC. To improve the global environment. 前記プレート状電極の正面形状は概略方形である、ことを特徴とする請求項1に記載される地球環境改善機器。   The global environment improving apparatus according to claim 1, wherein a front shape of the plate-like electrode is a substantially square shape. 前記プレート状電極の正面形状は概略円形である、ことを特徴とする請求項1に記載される地球環境改善機器。   2. The global environment improving apparatus according to claim 1, wherein a front shape of the plate-like electrode is substantially circular. 前記油水分離後の油成分は、前記液電解処理装置から回収される、ことを特徴とする請求項1〜3に記載される地球環境改善機器。   The oil component after the said oil-water separation is collect | recovered from the said liquid electrolysis processing apparatus, The global environment improvement apparatus described in Claims 1-3 characterized by the above-mentioned. 前記油水分離後の水成分は、さらに高速電解殺菌装置によって、殺菌処理を受けることを特徴とする請求項1〜4に記載される地球環境改善機器。   5. The global environment improving apparatus according to claim 1, wherein the water component after the oil / water separation is further subjected to a sterilization treatment by a high-speed electrolytic sterilization apparatus. 前記油水分離後の水成分は、過給器により空気と熱源とが付与されるスプレー塔に送られて噴霧乾燥処理された後、直流電源が付与されるイオン化電極からなる集塵電極を有する電気集塵器で粒子を吸着した後、大気クリーン排気として放出される、ことを特徴とする請求項1〜5に記載される地球環境改善機器。 The water component after the oil-water separation is sent to a spray tower to which air and a heat source are applied by a supercharger and spray-dried, and then the electric component having a dust collection electrode including an ionization electrode to which a DC power source is applied. 6. The global environment improving apparatus according to claim 1, wherein particles are adsorbed by a dust collector and then released as air clean exhaust.
JP2015017353A 2015-01-30 2015-01-30 Global environment improvement apparatus Pending JP2016140808A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109248785A (en) * 2018-08-16 2019-01-22 内蒙古万众炜业科技环保股份公司 Electrical tar precipitator is used in a kind of production and processing of semi-coke
DE112017003574T5 (en) 2016-07-15 2019-04-25 Denso Corporation STATOR OF AN ELECTRIC LATHE
CN114647953A (en) * 2022-04-06 2022-06-21 中科三清科技有限公司 Method and device for measuring and calculating atmospheric environment capacity and electronic equipment

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE112017003574T5 (en) 2016-07-15 2019-04-25 Denso Corporation STATOR OF AN ELECTRIC LATHE
CN109248785A (en) * 2018-08-16 2019-01-22 内蒙古万众炜业科技环保股份公司 Electrical tar precipitator is used in a kind of production and processing of semi-coke
CN109248785B (en) * 2018-08-16 2020-03-20 内蒙古万众炜业科技环保股份公司 Electrical tar precipitator for semi-coke production and processing
CN114647953A (en) * 2022-04-06 2022-06-21 中科三清科技有限公司 Method and device for measuring and calculating atmospheric environment capacity and electronic equipment
CN114647953B (en) * 2022-04-06 2022-10-11 中科三清科技有限公司 Method and device for measuring and calculating atmospheric environment capacity and electronic equipment

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