JP2005204907A - Treatment system and method for rendering electric apparatus using electricity insulating oil containing polychlorinated biphenyl harmless - Google Patents

Treatment system and method for rendering electric apparatus using electricity insulating oil containing polychlorinated biphenyl harmless Download PDF

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JP2005204907A
JP2005204907A JP2004014433A JP2004014433A JP2005204907A JP 2005204907 A JP2005204907 A JP 2005204907A JP 2004014433 A JP2004014433 A JP 2004014433A JP 2004014433 A JP2004014433 A JP 2004014433A JP 2005204907 A JP2005204907 A JP 2005204907A
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electrical
oil
insulating oil
pcb
equipment
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Tadayoshi Iida
飯田忠義
Yoshihiko Suzuki
鈴木義彦
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Takaoka Toko Co Ltd
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Takaoka Electric Mfg Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To continuously use an electric apparatus using electricity insulating oil containing organic chlorine-based compound or to safely scrap the electric apparatus by eliminating the organic chlorine-based compound thereby cleaning the electricity insulating oil to be harmless state without disassembling the electric apparatus at a site where the electric apparatus is installed. <P>SOLUTION: A lead-out port of the electricity insulating oil nearly at the lower end of the electric apparatus is connected through an detachable pipe 4 to an apparatus for rendering the electricity insulating oil harmless with which dechlorination and hydrogenation is applied to the electricity insulating oil in the presence of a nickel-based catalyst in hydrogen gas atmosphere. The electricity insulating oil is poured from the electric apparatus to the pouring port of the apparatus for rendering the electricity insulating oil harmless to render the organic chlorine-base compound harmless and to be cleaned by using the catalyst reaction of the apparatus for rendering the electricity insulating oil harmless. Through a pipe 22 connecting the drain port of the apparatus for rendering the electricity insulating oil harmless detachably with an oil reservation tub 23 capable of housing nearly the whole amount of the cleaned electricity insulating oil, the cleaned electricity insulating oil is transferred to the oil reservation tub. Through a pipe 26 connecting the oil reservation tub and the lead-in port of the electric apparatus detachably, the cleaned electricity insulating oil is circulated back to the electric apparatus to make the electric apparatus itself harmless. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、変圧器や遮断器等の電気機器において、該電気機器が組み立てられ、かつ現地に据え付けられた状態のまま、電気機器の絶縁媒体として使用されている電気絶縁油中に含まれるポリ塩化ビフェニルを脱塩素化、水素化して消滅させるポリ塩化ビフェニルを含有する電気絶縁油の無害化処理装置を用い、ポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器を無害化処理するシステムと無害化方法に関する。
なお、本発明を便宜上、ポリ塩化ビフェニル(以下、PCBという)を含む電気絶縁油の無害化について記述するが、例えばダイオキシン等、有機塩素系化合物であれば、PCBと同様に塩素を分離、水素化して無害化することが出来る。
The present invention relates to an electrical device such as a transformer or a circuit breaker, which is contained in an electrical insulating oil used as an insulating medium of an electrical device while the electrical device is assembled and installed in the field. A system for detoxifying electrical equipment using electrical insulation oil containing polychlorinated biphenyl using a dechlorination treatment equipment for electrical insulation oil containing polychlorinated biphenyl, which dechlorinates and hydrogenates chlorinated biphenyl. It relates to detoxification methods.
For the sake of convenience, the present invention will be described for the detoxification of an electrical insulating oil containing polychlorinated biphenyl (hereinafter referred to as PCB). Can be rendered harmless.

有機塩素化合物であるPCBの有害性が指摘され、生産が中止されてから久しい。
しかし、長期間にわたってPCBの処理が進まず、PCBを使用、あるいはPCBが混入した電気絶縁油を使用した電気機器は、今なお実系統でたくさん使用されている。また、大量の使用をやめた、PCBを使用、あるいはPCBが混入した電気絶縁油を使用した電気機器、及び単独の状態のPCBが混入した電気絶縁油が、その保有者によって保管され続けている。
近年にいたり、化学的にPCBを無害化する技術が開発され、「廃棄物の処理及び清掃に関する法律(昭和四十五年法律第百三十七号)」(以下、廃掃法という)にもとづくPCBの無害化処理に関する公的認証(以下、公的認証という)も制度化されて、一部の保有者においてPCBを使用、あるいはPCBが混入した電気機器や、PCBが混入した電気絶縁油の処理が始まっている。
It has been a long time since the harmfulness of PCB, an organochlorine compound, was pointed out and production was discontinued.
However, PCB processing does not progress over a long period of time, and many electrical devices that use PCB or use electrical insulating oil mixed with PCB are still used in actual systems. In addition, electric appliances that have stopped using a large amount, use PCBs, or use electric insulating oil mixed with PCBs, and electric insulating oils mixed with PCB in a single state continue to be stored by their owners.
In recent years, technology for chemically detoxifying PCBs has been developed, and is based on the “Act on Waste Disposal and Cleaning (Act No. 137 of 1945)” (hereinafter referred to as the Waste Disposal Law). Public certification on PCB detoxification (hereinafter referred to as public certification) has also been institutionalized, and some holders use PCBs or use PCBs mixed with electrical equipment or PCBs containing electrical insulation oil. Processing has begun.

ところで処理を要するPCBの大部分は、変圧器や遮断器等の受変電機器に絶縁媒体として使用されているものである。絶縁媒体には、「PCBそのもの、もしくは主要成分としてPCBを使用している場合」(以下、高濃度PCBという)と、「何らかの原因でごく微量のPCBが混入した電気絶縁油」(以下、低濃度PCBという)がある。低濃度PCBのPCB濃度は(以降、PCB濃度を便宜上ppm表記する場合がある)、ほとんどが10ppm以下で、高くても100ppm程度であることが社団法人日本電機工業会の調査で判明している。この調査においてサンプリングされた報告事例の最も高い濃度が2,110ppmであったことから、最高濃度は10,000ppm(=10,000mg/kg=(1%))程度と想定する事が適当であろう。本発明は、0.5mg/kg超〜10,000mg/kg以下の低濃度PCBの無害化に関するものである。   By the way, most PCBs that require processing are used as insulating media in power receiving and transforming devices such as transformers and circuit breakers. Insulating media include “when PCB itself or PCB is used as a main component” (hereinafter referred to as high-concentration PCB) and “electric insulating oil mixed with a very small amount of PCB for some reason” (hereinafter referred to as low-density PCB). Density PCB). According to a survey by the Japan Electrical Manufacturers' Association, the PCB concentration of low-concentration PCB (hereinafter, the PCB concentration may be expressed in ppm for convenience) is almost 10 ppm or less and at most about 100 ppm. . Since the highest concentration of reported cases sampled in this survey was 2,110 ppm, it is appropriate to assume that the maximum concentration is about 10,000 ppm (= 10,000 mg / kg = (1%)). Let's go. The present invention relates to detoxification of low-concentration PCBs of more than 0.5 mg / kg to 10,000 mg / kg or less.

低濃度PCBは、これまで、電気絶縁油を再生する際にPCBが混入したものと考えられてきており、再生電気絶縁油は、主に柱上変圧器に使用されていることが判明している。しかし、至近にいたり、PCBが入っていないと思われてきた新油を使用した電気機器からPCBが検出される事例が多数報告され、PCB汚染が電気絶縁油を使用するあらゆる電気機器に広がっていることが判明した。電気絶縁油の生産工程や、輸送、貯蔵、各種の作業工程、及び取り扱い器具、メンテナンス等、PCBが混入し得る機会は多々あり、これらの何れか、あるいは複合的に要因が重なって混入が広まったものと考えられる。   So far, low-concentration PCBs have been considered to have been mixed with PCB when regenerating electrical insulation oil, and it has been found that regenerated electrical insulation oil is mainly used in pole transformers. Yes. However, many cases have been reported where PCBs are detected from electrical equipment using new oil that has been considered to be near or not containing PCB, and PCB contamination has spread to all electrical equipment that uses electrical insulating oil. Turned out to be. There are many occasions where PCBs can be mixed, such as the production process of electrical insulating oil, transportation, storage, various work processes, handling equipment, maintenance, etc., and any of these or a combination of factors may cause mixed contamination. It is thought that.

さて、これまでに発表されている低濃度PCBの無害化処理技術は、何れもPCBを含
む絶縁油を無害化するだけで、電気絶縁油、及び電気絶縁油を使用している電気機器本体
の再使用を意図してはいない。つまり、積極的に廃棄することを前提としてはいないまで
も、リサイクルを含む廃棄、又は結果としてリサイクルを含む廃棄を前提としている。こ
こで云うリサイクルとは、無害化した電気絶縁油を燃料に転用したり、電気機器の金属製
部材をもとの金属に戻したりすることを指す。
Now, all of the low-concentration PCB detoxification technologies that have been published so far only render the insulating oil containing PCB harmless, and the electrical insulation oil and the main body of the electrical equipment that uses the electrical insulating oil. Not intended for reuse. In other words, even if it is not premised on aggressive disposal, it is premised on disposal including recycling or disposal including recycling as a result. Recycling here refers to diverting the harmless electrical insulating oil to fuel or returning the metal member of the electrical equipment to the original metal.

前記のように、低濃度PCBは、極めて少量のPCBが電気絶縁油に含まれているだけなのに無害化して廃棄するものと考えられてきたため、大量に存在する電気機器そのものも廃棄するものとして扱われてきたと云える。PCBの適正な処理を進めるための法律である「ポリ塩化ビフェニル廃棄物の適正な処理の推進に関する特別措置法(平成十三年法律第六十五号)」や、この法律の原点といえる前記の「廃掃法」などが、何れも「廃棄」の文言を冠した法律名となっていることが、この間の事情を端的に物語っている。   As described above, low-concentration PCBs have been considered to be detoxified and discarded even though a very small amount of PCB is contained in the electrical insulating oil. It can be said that it has been. “Special Measures Act on Promotion of Proper Treatment of Polychlorinated Biphenyl Waste (Act No. 65 of 2001)”, which is a law for the proper disposal of PCBs, and the above-mentioned origin of this law The “Waste Disposal” and the like are all named after the word “Disposal”.

低濃度PCBが混入した電気機器、なかんずく大形電気機器は、電気機器を更新する場合、電気機器そのものが高価であることはもちろん、無害化処理には多額の費用が必要で、かつ電気系統から分離して据付場所から移動するにも多くの費用を要する。また、費用の問題だけに留まらず、電力需要量の稠密な、特に都心部や都心の地下に設置されている電気機器は、運び出したり運搬することが難しい場合もある。つまり、電気機器にはPCBが含まれているため、分割や分解することが出来ない部位がある。一方、運び出すためには電気機器を分割、あるいは分解しなければならない。という背反する条件によって自己撞着に陥る可能性がある。   Electrical equipment mixed with low-concentration PCBs, especially large electrical equipment, is not only expensive when renewing electrical equipment, but also requires a large amount of cost for detoxification treatment, and from the electrical system. It also takes a lot of money to separate and move from the installation site. Moreover, it is not only a problem of cost, but it is sometimes difficult to carry out or carry an electric device having a dense electric power demand, particularly installed in the city center or underground in the city center. In other words, since the electrical equipment contains PCB, there are parts that cannot be divided or disassembled. On the other hand, in order to carry it out, it is necessary to divide or disassemble the electric equipment. There is a possibility of falling into self-confidence due to the contradicting conditions.

さらには、電気機器を運び出すことが出来る場合であっても、電気機器そのものを無害化することが難しいという、もっと本質的な問題がある。すなわち、低濃度PCBの無害化に関しては、たくさんの化学的処理法が、前記の廃掃法にもとづく公的審査に合格、認証されているが、変圧器には絶縁紙を被覆した電線で構成されたコイルがあり、コイルの内部深くにも低濃度PCBが染み込み、浸透している。また、プレスボードのような紙質の集成材や木質材も大量に使用され、当該材にも低濃度PCBが染み込んでいる。しかも、大形電気機器の部材は、長大、高重量品も含め、さまざまな形状や大きさをしている。すなわち、有害物であるPCBが含まれ、かつ大きく、重く、形状がさまざまであることから、無害化処理のために取り扱うこと自体が容易ではない。   Furthermore, even when the electric device can be carried out, there is a more essential problem that it is difficult to make the electric device harmless. In other words, regarding the detoxification of low-concentration PCBs, many chemical treatment methods have passed and been certified by the public examination based on the above-mentioned waste cleaning method, but the transformer is composed of wires coated with insulating paper. A low-concentration PCB penetrates and penetrates deep inside the coil. In addition, a large amount of paper-like laminated materials and wood materials such as press boards are used, and the low-concentration PCB is also infiltrated into the materials. In addition, the members of large electric devices have various shapes and sizes, including long and heavy products. That is, since PCB which is a harmful substance is contained, it is large, heavy, and has various shapes, it is not easy to handle for detoxification.

少なくとも、本発明の特許出願時点においては、このような大形電気機器そのものを無害化処理することは行われておらず、そのようなことを実現する何らの情報もない。
つまり、低濃度PCBを使用した大形の電気機器は、従来の技術では無害化処理することが出来ない。その結果、電気機器の更新が出来ないので、信頼性の低下に対応した電気機器の更新や増容量などの措置が行えず、社会インフラの重要な電力の正常な運用に、特に今後大きな障害要因になってくる懸念は極めて大きい。
At least at the time of patent application of the present invention, such a large electric device itself has not been detoxified, and there is no information to realize such a process.
That is, a large electric device using a low-concentration PCB cannot be rendered harmless by the conventional technology. As a result, it is impossible to renew the electrical equipment, so it is not possible to take measures such as renewing or increasing the capacity of the electrical equipment in response to the decline in reliability. There is a great deal of concern.

本発明は、このような状況に対して、電気絶縁油に含まれる低濃度PCBを無害化するとともに、電気絶縁油としてそのまま使用できるようにして、電気機器そのものを無害化してしまうものである。
なお、本発明は、大形の電気機器に適用した場合に特に大きな効果を発揮するが、以下に説明するように、電気機器を組み立てたまま、かつ電気機器を継続的に使用可能なようにPCBを無害化処理することは、小形の電気機器に適用しても十分効果が期待できるものである。
The present invention renders the low-concentration PCB contained in the electrical insulating oil harmless against such a situation and renders the electrical equipment itself harmless by allowing it to be used as it is.
Although the present invention is particularly effective when applied to a large electric device, as described below, the electric device can be used continuously with the electric device assembled. The effect of detoxifying the PCB can be expected to be sufficiently effective even when applied to a small electric device.

請求項1のポリ塩化ビフェニルに汚染された電気機器そのものを無害化するシステムは、0.5mg/kg超〜10000mg/kg以下のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器と、水素ガス雰囲気中において、ゼオライト・ニッケル、又はニッケル・モリブデン、ニッケル・白金等を骨格とするニッケル系の触媒下でポリ塩化ビフェニルを脱塩素化、水素化し無害化する電気絶縁油の無害化処理装置と、電気機器の略上端、又は下端の導出口から前記電気絶縁油の無害化処理装置の注入口を着脱可能に連接する第1の配管と、水素ガス雰囲気中の前記触媒の間を通過する過程で発生する、触媒の脱塩素化、水素化反応を利用してポリ塩化ビフェニルを無害化処理し、精製した電気絶縁油を収容する貯油槽と、前記電気絶縁油の無害化処理装置の排出口から精製した電気絶縁油を収容する貯油槽を着脱可能に連接する第2の配管と、前記精製した電気絶縁油を収納する貯油槽から前記電気機器の前記導出口と略反対端の導入口を着脱可能に連接する第3の配管によって構成されるポリ塩化ビフェニルを含む電気絶縁油の無害化処理システムであって、前記電気機器から前記無害化処理装置の注入口へ前記ポリ塩化ビフェニルを含有する電気絶縁油を注入し、水素ガス雰囲気中の前記触媒の間を通過する過程で発生する脱塩素化、水素化反応を利用してポリ塩化ビフェニルを無害化処理し、無害化処理装置の注入口とは反対端の排出口から、精製電気絶縁油を貯油槽へ移送し、貯油槽と電気機器の前記導出口とは略反対端の導入口を着脱可能に連接する第3の配管によって、精製電気絶縁油を[電気機器→電気機器の導出口→第1の配管→無害化処理装置の注入口→水素ガス雰囲気下の触媒→無害化処理装置の排出口→第2の配管→貯油槽→第3の配管→電気機器の導入口→電気機器]と循環させ、ポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化するシステム。
請求項2のポリ塩化ビフェニルに汚染された電気機器そのものを無害化するシステムは、請求項1の発明において、無害化処理装置の排出口から貯油槽へ精製電気絶縁油を移送する第2の配管から、再び無害化処理装置の注入口へ循環させる第3の配管を分岐し、第2の配管、及び第3の配管にそれぞれストップバルブを配設し、ストップバルブの開閉操作によって、前記排出口から第3の配管によって、無害化処理装置へ精製途次の電気絶縁油を、又は第2の配管によって、貯油槽へ精製を終了した電気絶縁油を、選択して流通せしめるように構成したことを特徴とする、請求項1記載のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化するシステム。
請求項3のポリ塩化ビフェニルに汚染された電気機器そのものを無害化するシステムは、電気絶縁油の無害化処理装置を車載形で構成し、電気機器の据付場所に移動してポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器、及び貯油槽と現地で連接して電気絶縁油を無害化処理し、無害化処理後は、無害化処理装置を貯油槽、及び電気機器から分離し、該電気機器とは別の場所に移動できるように構成したことを特徴とする、請求項1、及び請求項2記載ののポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化するシステム。
請求項4のポリ塩化ビフェニルに汚染された電気機器そのものを無害化するシステムは、貯油槽にタンクローリー車を適用したことを特徴とする、請求項1、請求項2、及び請求項3記載のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化するシステム。
請求項5のポリ塩化ビフェニルに汚染された電気機器そのものを無害化する方法は、0.5mg/kg超〜10000mg/kg以下のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器と、ポリ塩化ビフェニルを脱塩素化、水素化し無害化する電気絶縁油の無害化処理装置を連接し、前記の電気機器から無害化処理装置の注入口へ前記の電気絶縁油を注入し、前記の無害化処理装置内を流通する過程で無害化が進展した精製電気絶縁油を無害化処理装置の排出口から貯油槽へ蓄え、前記の電気機器内に滴下する電気絶縁油の残留分をさらに回収し、無害化処理装置の注入口へ注入し、貯油槽に蓄えた精製電気絶縁油を前記電気機器に還流し、前記電気機器そのものを無害化する方法。
The system for detoxifying an electrical device itself contaminated with polychlorinated biphenyl according to claim 1 comprises an electrical device using an electrical insulating oil containing polychlorinated biphenyl of more than 0.5 mg / kg to 10000 mg / kg, hydrogen A detoxifying device for electrical insulating oil that dechlorinates, hydrogenates and detoxifies polychlorinated biphenyl under a nickel-based catalyst with a framework of zeolite / nickel or nickel / molybdenum, nickel / platinum, etc. in a gas atmosphere The process of passing between the first pipe detachably connecting the inlet of the detoxifying treatment apparatus for the electrical insulating oil from the substantially upper or lower outlet of the electrical equipment and the catalyst in the hydrogen gas atmosphere Dechlorination of the catalyst generated in the process, detoxification treatment of polychlorinated biphenyl using a hydrogenation reaction, and an oil storage tank for storing the refined electrical insulating oil, A second pipe that detachably connects an oil storage tank that stores the refined electrical insulating oil from the discharge port of the detoxification treatment device, and the outlet port of the electrical device from the oil storage tank that houses the refined electrical insulation oil; A detoxification treatment system for electrical insulating oil containing polychlorinated biphenyl constituted by a third pipe that removably connects an introduction port at a substantially opposite end, from the electrical device to the injection port of the detoxification treatment apparatus Injecting electrical insulating oil containing the polychlorinated biphenyl, dechlorination generated in the process of passing between the catalyst in a hydrogen gas atmosphere, detoxifying the polychlorinated biphenyl using a hydrogenation reaction, The refined electrical insulating oil is transferred to the oil storage tank from the discharge port opposite to the injection port of the detoxification treatment device, and the introduction port at the opposite end to the oil storage tank and the outlet port of the electrical equipment is detachably connected. By the third pipe , Refined electrical insulation oil [electric equipment → outlet of electrical equipment → first piping → inlet of detoxification treatment equipment → catalyst under hydrogen gas atmosphere → discharge port of detoxification treatment equipment → second piping → oil storage A system that detoxifies the electrical equipment itself using electrical insulating oil containing polychlorinated biphenyl by circulating through the tank → third piping → electrical equipment inlet → electrical equipment].
The system for detoxifying electrical equipment itself contaminated with polychlorinated biphenyl according to claim 2 is the second pipe for transferring purified electrical insulating oil from the discharge port of the detoxification processing device to the oil storage tank in the invention of claim 1 Then, a third pipe to be circulated again to the inlet of the detoxification treatment apparatus is branched, a stop valve is provided in each of the second pipe and the third pipe, and the discharge port is opened and closed by opening and closing the stop valve. It was configured so that the electrical insulation oil in the process of refining can be selected and distributed to the detoxification processing device from the third pipe to the detoxification processing apparatus, or the electrical insulation oil that has been refined to the oil storage tank by the second pipe. A system for detoxifying electrical equipment itself using electrical insulating oil containing polychlorinated biphenyl according to claim 1.
The system for detoxifying the electrical equipment itself contaminated with polychlorinated biphenyl according to claim 3 comprises an insulative treatment device for electrical insulating oil, which is moved to the installation location of the electrical equipment and contains polychlorinated biphenyl. The electrical insulation oil is used to detoxify the electrical insulation oil by connecting to the oil storage tank and the oil storage tank at the site, and after the detoxification process, the detoxification treatment device is separated from the oil storage tank and the electrical equipment, It is configured to be able to move to a place different from the electrical equipment, and the electrical equipment itself using the electrical insulating oil containing polychlorinated biphenyl according to claim 1 and claim 2 is rendered harmless. system.
The system for detoxifying an electrical device itself contaminated with polychlorinated biphenyl according to claim 4 uses a tank lorry vehicle as an oil storage tank. A system that renders electrical equipment harmless using electrical insulating oil containing biphenyl chloride.
The method of detoxifying an electrical device itself contaminated with polychlorinated biphenyl according to claim 5 is an electrical device using an electrical insulating oil containing polychlorinated biphenyl of more than 0.5 mg / kg to 10000 mg / kg, The electrical insulation oil detoxification treatment equipment that dechlorinates, hydrogenates and detoxifies biphenyl chloride is connected, and the electrical insulation oil is injected from the electrical equipment into the detoxification treatment equipment inlet. Store the refined electrical insulating oil, which has been made harmless in the process of circulating in the treatment equipment, from the discharge port of the detoxification treatment equipment to the oil storage tank, and further collect the residual amount of electrical insulation oil dripped into the electrical equipment, A method of detoxifying the electrical device itself by recirculating the refined electrical insulating oil injected into the inlet of the detoxification processing apparatus and stored in the oil storage tank to the electrical device.

本発明は、PCBが変質しにくく、通常の使用環境では他の物質と化学的反応が起きないという高い安定性を利用した、いわば逆転の発想にもとづいている。
すなわち、PCBが混入した電気絶縁油を使用した電気機器は、電気絶縁油にPCBが含まれていることだけが問題なのであって、電気機器本体にはPCBが付着したり構成部材に染み込んでいるが、低濃度PCBを除く電気機器本体が有害なものに変質しているわけではない。したがって、低濃度PCBに含まれているPCBを除去、あるいは無害化すれば、電気絶縁油を含む電気機器は無害となる。本発明の重要な着目点である。
The present invention is based on the idea of reversal, which utilizes the high stability that PCBs are not easily altered and do not chemically react with other substances in normal use environments.
That is, the problem with electrical equipment using electrical insulating oil mixed with PCB is that the electrical insulating oil contains PCB, and PCB adheres to the electrical equipment body or soaks into components. However, this does not mean that the main body of electrical equipment except for low-concentration PCB has been changed into harmful ones. Therefore, if the PCB contained in the low-concentration PCB is removed or rendered harmless, the electrical equipment containing the electrical insulating oil becomes harmless. This is an important focus point of the present invention.

つまり、本発明の重要なポイントは、従来の、低濃度PCBと低濃度PCBを使用した電気機器本体を別々の扱いにしたうえ、「PCBは無害化したうえで廃棄するもの」、また、「PCBに汚染された電気機器本体も、付着、及び染み込んだPCBを無害化したうえで廃棄するもの」という考え方から、「電気機器そのものを組み立てた状態のまま無害化してしまう」という、これまでPCBの処理に関する法令においてすら全く想定していなかった方向に、処理の仕組みを変えてしまうことにある。電気機器そのものを無害化した後は、電気機器を継続して使用する、あるいは電気機器を廃棄して新しい電気機器に更新する、の何れとするかは、必要に応じて決めればよい。   That is, the important point of the present invention is that the conventional low-concentration PCB and the main body of the electrical equipment using the low-concentration PCB are handled separately, and “PCB is made harmless and discarded”, “ From the idea that the main body of the electrical equipment contaminated by the PCB is to be disposed of after detoxifying the adhered and soaked PCB, it has been said that the electrical equipment itself is made harmless in the assembled state. This is to change the processing mechanism in a direction that was not even envisaged in the laws on processing. After the electrical device itself has been rendered harmless, whether to continue using the electrical device or to discard the electrical device and replace it with a new electrical device may be determined as necessary.

さて、前記の公的認証を得ているPCBの無害化処理方法には、さまざまな方式がある
が、本発明は、PCBを含む電気絶縁油からPCBを除去した後に電気絶縁油として使用
が可能な無害化処理方法に限り適用できるものである。
There are various methods for detoxifying PCBs that have obtained the above public certification, but the present invention can be used as electrical insulation oil after removing PCB from electrical insulation oil containing PCB. This method can be applied only to a detoxification method.

本発明の特許出願人である一社は、PCBの無害化を推進するべく、経済的で、二次公害のおそれのないゼオライト・ニッケル、又はニッケル・モリブデン、ニッケル・白金等を骨格とするニッケル系の触媒(以下、触媒という)下でPCBを無害化する方法を特許出願し、特許文献1として登録された。また、本発明者の一人は、特許文献1の発明の原理を適用した電気絶縁油の精製装置に関して、平成12年に特許文献2を出願した。特許文献1の原理と、当該原理を適用した特許文献2の無害化処理装置の発明は、[難分解性有機化合物処理技術検討・評価委員会]の審査を経て実用性が認められ、PCBの無害化処理方法である脱塩素化法の中の触媒水素還元法として、平成13年5月に前記の公的認証を得ている。さらに、前記の本発明者の一人は、平成15年に、特許文献2の発明の無害化処理能力を飛躍的に高める発明として、特許文献3を出願した。
特許第1982066号(特公平7−10995号公報) 特開2001−279290号公報 特願2003−351420号
In order to promote the detoxification of PCBs, one company that is a patent applicant of the present invention is an economical, non-polluting zeolite / nickel, nickel / molybdenum, nickel / platinum or other nickel skeleton. A patent application was filed for a method of detoxifying PCB under a system catalyst (hereinafter referred to as catalyst), and it was registered as Patent Document 1. In addition, one of the inventors of the present invention applied for Patent Document 2 in 2000 with respect to a device for purifying electrical insulating oil to which the principle of the invention of Patent Document 1 was applied. The invention of the patent document 1 and the detoxification treatment apparatus of the patent document 2 to which the principle is applied have been found to be practical after examination by the [Refractory Organic Compound Processing Technology Examination / Evaluation Committee]. As the catalytic hydrogen reduction method in the dechlorination method, which is a detoxification treatment method, the above-mentioned public certification was obtained in May 2001. Furthermore, one of the inventors mentioned above filed Patent Document 3 in 2003 as an invention that dramatically increases the detoxification processing ability of the invention of Patent Document 2.
Patent No. 1982066 (Japanese Patent Publication No. 7-10995) JP 2001-279290 A Japanese Patent Application No. 2003-351420

本発明では、特許文献2、及び特許文献3に着目した。
すなわち、特許文献2は特許文献1の発明のPCBの無害化処理原理を適用したPCB
の精製装置の発明で、特許文献3は特許文献2の発明のPCBの精製能力を、さらに改良
した発明であるが、何れもPCBを無害化したときに生成されるビフェニル化合物は、そ
のまま絶縁油の一部として利用できることが特徴の一つである。
In the present invention, attention is focused on Patent Document 2 and Patent Document 3.
That is, Patent Document 2 is a PCB to which the PCB detoxification principle of the invention of Patent Document 1 is applied.
Patent Document 3 is an invention in which the purification ability of PCB of the invention of Patent Document 2 is further improved. In any case, the biphenyl compound produced when detoxifying PCB is used as it is as insulating oil. One of the features is that it can be used as a part of

前記の公的認証を得た触媒水素還元法は、特許文献1の発明のPCBの無害化処理原理と、当該原理を適用したPCBの精製装置である特許文献2の発明を実用的な形で実現したPCBの無害化処理技術である。その無害化の仕組みをごく簡単に云えば、PCBの毒性の由来となっている塩素Clを水素Hに置換し無害なビフェニル化合物に転換するとともに、分離された塩素を食塩水の形にして除去するもので、PCBが水素化されたビフェニル化合物は、電気絶縁油と混じって電気絶縁油の一部となる。   The catalytic hydrogen reduction method which has obtained the above public certification is a practical form of the PCB detoxification treatment principle of the invention of Patent Document 1 and the invention of Patent Document 2 which is a PCB refining device to which the principle is applied. This is a realized PCB detoxification technology. The mechanism of detoxification is very simple. Chlorine Cl, which is the origin of PCB toxicity, is replaced with hydrogen H to convert it into a harmless biphenyl compound, and the separated chlorine is removed in the form of saline. Therefore, the biphenyl compound in which PCB is hydrogenated is mixed with the electrical insulating oil and becomes a part of the electrical insulating oil.

PCBは図1に示す化学構造をしており、6角状の炭素環が2つ繋がったビフェニル核の炭素に1〜10個の塩素が付いたものである。(図1は、塩素が5個の場合を示す)炭素は4価の元素、つまり4本の腕があり、それぞれ他の物質と繋がる性質を持っている。PCBの場合は、6角状に配置されたそれぞれの炭素は、隣接の炭素と一方は2本、他方は1本の腕で繋がり、残った腕の1本が6角状の炭素環の外周で塩素又は水素と繋がっている。前記のとおり、塩素の数が1〜10個の何れであってもPCBと云われる物質であり、塩素の数、及び付いている位置によってさまざまな同位体があり、その種類は209種類に達すると云われている。図1に示すとおり、塩素が付いていない位置には水素が付いている。   PCB has the chemical structure shown in FIG. 1 and has 1 to 10 chlorine atoms attached to carbon of a biphenyl nucleus in which two hexagonal carbon rings are connected. (FIG. 1 shows the case of five chlorines) Carbon has a tetravalent element, that is, four arms, each having a property of being connected to another substance. In the case of PCB, each carbon arranged in a hexagonal shape is connected to adjacent carbon by one arm and the other one by one arm, and one of the remaining arms is the outer periphery of the hexagonal carbon ring. It is connected to chlorine or hydrogen. As mentioned above, even if the number of chlorine is 1 to 10, it is a substance called PCB, and there are various isotopes depending on the number of chlorine and the position where it is attached. It is said that. As shown in FIG. 1, hydrogen is attached to the position where chlorine is not attached.

触媒水素還元法は、塩素を水素に置換する技術であり、PCBの塩素の数、及び塩素が付いている位置に関わりなく塩素を水素に置換する。PCBの塩素を水素に置換した構造には、炭素に水素が1個付いたビフェニル、2個付いたビシクロヘキシル、6角状の炭素環の一方には1個、他方には2個付いたフェニルシクロヘキサンの3種類の形があるが、総称してビフェニル化合物と呼ばれ、それぞれが無害で、熱媒にも使用される安定性の高い物質である。3種類のビフェニル化合物の構造を図2に示す。なお、図1と図2は、炭素環に塩素、又は水素が付着している状態を視覚的にわかりやすく表示した図で、通常の化学式とは若干異なる本発明者のオリジナルな図である。   The catalytic hydrogen reduction method is a technique for replacing chlorine with hydrogen, and replaces chlorine with hydrogen regardless of the number of chlorine in the PCB and the position where the chlorine is attached. The structure in which PCB chlorine is replaced with hydrogen is biphenyl with one hydrogen on carbon, bicyclohexyl with two, phenyl with one on one of the hexagonal carbocycles and two on the other Although there are three forms of cyclohexane, they are collectively called biphenyl compounds, each of which is harmless and is a highly stable substance that is also used for a heating medium. The structures of the three types of biphenyl compounds are shown in FIG. FIG. 1 and FIG. 2 are diagrams showing the state in which chlorine or hydrogen is attached to the carbocyclic ring in an easy-to-understand manner, and are original drawings of the present inventor that are slightly different from ordinary chemical formulas.

図1と図2の化学構造を比較すれば判るように、ビフェニル化合物は、PCBの2つの炭素環の周囲の塩素が水素に置き換わり、全部が水素になっただけの構造であり、化学的性質は類似性が高いことが容易に期待できる。しかも、もともと低濃度PCBのほとんどは、PCB濃度が数ppm、最高でも100ppm程度、つまり、電気絶縁油には0.01%以下程しか含まれていないので、PCBが絶縁性能に悪影響しなかったように、そのまま電気絶縁油中に混じっていても絶縁性能に影響しないと云って差し支えない。表1は、触媒水素還元法をPCBの無害化処理技術として公的認証を受けるに際して実験した結果を示しており、全ての項目が電気絶縁油の特性を定めたJIS C 2320「電気絶縁油」の規定値を満たしている。表1は、前記の[難分解性有機化合物処理技術検討・評価委員会]による審査結果の資料である[<PCB汚染油処理技術> 「触媒水素還元法」実証試験結果報告書]に掲載されている表を転載したものである。   As can be seen from a comparison of the chemical structures in FIGS. 1 and 2, the biphenyl compound has a structure in which the chlorine around the two carbocycles of the PCB is replaced with hydrogen, and the entire structure becomes hydrogen. Can easily be expected to be highly similar. Moreover, most of the low-concentration PCBs originally have a PCB concentration of several ppm, at most about 100 ppm, that is, the electrical insulating oil contains only about 0.01% or less, so the PCB did not adversely affect the insulation performance. Thus, even if it is mixed in the electrical insulating oil as it is, it does not matter that the insulating performance is not affected. Table 1 shows the results of experiments conducted when the catalytic hydrogen reduction method was officially certified as a PCB detoxification treatment technology, and all items defined the characteristics of electrical insulation oil. JIS C 2320 “Electric insulation oil” The specified value is satisfied. Table 1 is published in [<PCB Contaminated Oil Treatment Technology> “Catalyst Hydrogen Reduction Method” Demonstration Test Result Report], which is a document of the results of the examination by the aforementioned [Refractory Organic Compound Treatment Technology Review and Evaluation Committee]. The table is reprinted.

(表1)低濃度PCBを無害化処理した精製電気絶縁油の特性

Figure 2005204907
(Table 1) Properties of refined electrical insulating oil made by detoxifying low-concentration PCB
Figure 2005204907

すなわち、触媒水素還元法では無害化処理を行った後でも、電気絶縁油としての使用が
可能であり、電気機器への還流が可能である。
That is, the catalytic hydrogen reduction method can be used as an electrical insulating oil even after detoxification treatment, and can be refluxed to an electrical device.

本発明によれば、低濃度PCBを使用している電気機器を、電気機器が据え付けられている現場で、電気機器を組み立てたまま無害化することが出来る。
しかも、電気機器は、無害な電気機器に転換されるので、継続的に使用することが可能である。
該電気機器と無害化処理装置を直結し、低濃度PCBを無害化処理しつつ、該電気機器へ還流し循環する方法も考えられるが、無害化処理装置の排出口の後段に貯油槽を設けると、該電気機器の電気絶縁油を一度抜き取る事が可能となるので、該電気機器の内部に捕捉される電気絶縁油の滴下分を回収し、無害化処理ができ、該電気機器に残留するPCBを少なくできる。すなわち、貯油槽から無害化処理した電気絶縁油を戻し、PCBが溶解平衡に至った際のPCB濃度を低くすることが可能である。
また、無害化処理装置の後段に貯油槽を設けず、該電気機器を無害化処理後も継続的に使用する場合には、電気絶縁油の無害化精製の際に昇温した電気絶縁油の温度を低下させなければ該電気機器に入れ戻すことができないが、貯油槽を設ける場合は、貯油槽で保管していることで温度を低下できるので、前記の冷却器が不要とできる。
さらに、貯油槽を利用し、電気絶縁油の特性を向上させる添加剤を投入し、成分を調整することもできる。
According to the present invention, an electrical device using a low-concentration PCB can be rendered harmless while the electrical device is assembled at a site where the electrical device is installed.
Moreover, since the electrical device is converted into a harmless electrical device, it can be used continuously.
A method of directly connecting the electrical equipment and the detoxification treatment apparatus and decirculating the low-concentration PCB to the electrical equipment to circulate is also conceivable, but an oil storage tank is provided after the discharge port of the detoxification treatment equipment. Then, the electrical insulating oil of the electrical device can be extracted once, so that the dripping portion of the electrical insulating oil trapped inside the electrical device can be collected and detoxified, and remains in the electrical device. PCB can be reduced. That is, it is possible to return the detoxified electrical insulating oil from the oil storage tank and reduce the PCB concentration when the PCB reaches a dissolution equilibrium.
In addition, when an oil storage tank is not provided after the detoxification treatment device and the electrical equipment is continuously used after the detoxification treatment, the electrical insulation oil heated up during the detoxification purification of the electrical insulation oil If the temperature is not lowered, it cannot be put back into the electric device. However, when an oil storage tank is provided, the temperature can be lowered by storing in the oil storage tank, so that the cooler is not necessary.
Furthermore, using an oil storage tank, an additive for improving the characteristics of the electrical insulating oil can be introduced to adjust the components.

以上をまとめると、本発明は次のような効果をもたらすものであると云える。
1.電気機器を継続して使用する場合
1)電気機器をそのまま使い続けることが出来るので、代わりの電気機器を新たに製作する必要がない。
2)電気絶縁油と、電気機器本体を別々に無害化処理する従来の方法に比べ、格段に経済的にPCBを無害化処理できる。
3)電気機器を系統から切り離す必要、及び代わりの電気機器に繋ぎ代える作業が生じないので、作業に要する費用、及び時間が不要。
4)電気機器を現地から運び出す費用と時間、及び代わりの電気機器を搬入して据え付ける費用、及び時間が生じない。
2.電気機器を廃棄する場合
1)電気絶縁油と、電気機器本体を別々に無害化処理する従来の方法に比べ、格段に経済的にPCBを無害化処理できる。
2)無害な電気機器に転換されるので、現地で電気機器から電気絶縁油を抜き取ることが可能になり、現地で電気機器を所要の大きさ、形状などに分割してから撤去できるようになる。
3)無害な電気機器になるから、電気機器の分解や搬出、運搬を安全に行うことが出来る。
等、何れの場合も経済的、及び時間的効果は膨大で、計り知れないほどであることが期待できる。
しかし、何よりも大きな効果は、大形の電気機器を無害化できるようになることにともなう基幹的社会インフラとしての電力の安定供給に貢献できることである。
In summary, it can be said that the present invention provides the following effects.
1. When using an electric device continuously 1) Since an electric device can be used as it is, it is not necessary to manufacture a new electric device.
2) The PCB can be detoxified much more economically than the conventional method of separately detoxifying the electrical insulating oil and the electrical device main body.
3) There is no need to disconnect the electrical equipment from the system, and there is no need to replace it with a replacement electrical equipment, so the cost and time required for the work are not required.
4) Costs and time for carrying out electrical equipment from the site, and costs and time for installing and installing alternative electrical equipment do not occur.
2. Disposal of electrical equipment 1) The PCB can be detoxified much more economically than the conventional method of separately detoxifying the electrical insulating oil and the electrical equipment body.
2) Since it will be converted into harmless electrical equipment, it will be possible to extract the electrical insulating oil from the electrical equipment locally, and it will be possible to remove the electrical equipment locally after dividing it into the required size and shape. .
3) Since it becomes a harmless electrical device, it is possible to safely disassemble, carry out and transport the electrical device.
In any case, the economic and temporal effects are enormous and can be expected to be immeasurable.
However, the greatest effect is that it can contribute to the stable supply of electric power as a basic social infrastructure accompanying the detoxification of large electric devices.

以下に、本発明の具体的内容を、実施例により詳細に説明する。
図3は特許文献3の発明を応用した低濃度PCBの精製装置1と変圧器2、及び貯油槽23を組み合わせて構成した電気絶縁油の精製システムにより、変圧器2そのものを無害化してしまうことを説明するための、本発明の具体的な構成を説明する図である。精製装置1は、変圧器2、及び貯油槽23を除く低濃度PCB6aの精製装置全体を意味している。
なお、変圧器2は、電気機器一般を代表しており、低濃度PCB6aを使用している電気機器であれば、機種を問わず、どういう電気機器であってもよい。
Hereinafter, the specific contents of the present invention will be described in detail with reference to examples.
FIG. 3 shows that the transformer 2 itself is rendered harmless by the refining system of the electrical insulating oil configured by combining the refining device 1 of the low-concentration PCB, the transformer 2 and the oil storage tank 23 to which the invention of Patent Document 3 is applied. It is a figure explaining the specific structure of this invention for demonstrating this. The refinement | purification apparatus 1 means the whole refinement | purification apparatus of the low concentration PCB6a except the transformer 2 and the oil storage tank 23. FIG.
Note that the transformer 2 represents electric equipment in general, and any electric equipment may be used as long as it is an electric equipment using the low-concentration PCB 6a.

変圧器2の略下端の導出口3と連接し、変圧器2とは着脱可能な第1の配管4を介してポンプ5によって低濃度PCB6aを変圧器2から導出する。第1の配管4には苛性ソーダ7の投入口8が配設されており、低濃度PCB6aと苛性ソーダ7は、第1の配管4中を流通する過程やポンプ5で撹拌されて混合される。低濃度PCB6aと苛性ソーダ7の混合は、第1の配管4の途中に図示しない攪拌機を配設して行ってもよい。   The low concentration PCB 6 a is led out from the transformer 2 by a pump 5 through a first pipe 4 that is connected to the lead-out port 3 at the substantially lower end of the transformer 2 and is detachable from the transformer 2. An inlet 8 for caustic soda 7 is disposed in the first pipe 4, and the low-concentration PCB 6 a and the caustic soda 7 are agitated and mixed in the process of flowing through the first pipe 4 or by the pump 5. The mixing of the low-concentration PCB 6a and the caustic soda 7 may be performed by arranging a stirrer (not shown) in the middle of the first pipe 4.

次に、塩素を分離、水素化する化学反応が速やかに進展するように、加熱器9により低濃度PCB6aを150〜250℃に加熱した後、精製装置本体10の容器11の上端に設けた注入口12から低濃度PCB6aを注入する。   Next, the low-concentration PCB 6a is heated to 150 to 250 ° C. by the heater 9 so that the chemical reaction for separating and hydrogenating chlorine progresses quickly, and then provided at the upper end of the container 11 of the purification apparatus main body 10. Low concentration PCB 6a is injected from the inlet 12.

低濃度PCB6aの精製は、圧力が高い方が早く進展するが、大気圧でも精製反応は進展するので、安全性を考えれば大気圧に近い方が望ましい。本発明のもととなった特許文献1の発明では、水素ガス圧力を80kgf/cmとして精製実験を行った結果が説明されているが、特許文献2に示す発明の装置により実験を行った結果、大気圧でも十分な実用性能を発揮することを見いだし、その結果を、特許文献2の発明に適用している。前記の公的認証は、濃度1%(10,000mg/kg)以下の低濃度PCBを、温度=150〜250℃、圧力=大気圧〜0.3MPaで無害化処理を行うことが認証条件となっている。本発明の無害化処理条件は、公的認証の範囲内である。
公的認証を得るに際しての実証試験では、触媒(平均粒径2mm)を35kgf収納した電気絶縁油の精製装置において、温度250℃、PCB含有量100ppmの100リットルの低濃度PCBを3時間で注入処理した結果、大気圧(1kgf/cm)、5kgf/cm、及び50kgf/cm 何れの圧力の場合も脱塩素反応がほぼ完全に行われており、精製処理された電気絶縁油中の残存PCB、及び特に毒性が高いと云われるコプラナPCB量をガスクロマトグラフ質量分析法/選択イオン検出(GC−MS/SIM法)で分析した結果、全て検出下限以下(ND)であった。結果の詳細は、特許文献2で説明してあるので省略する。
The purification of the low-concentration PCB 6a progresses faster when the pressure is higher, but the purification reaction proceeds even at atmospheric pressure. In the invention of Patent Document 1 that is the basis of the present invention, the results of a purification experiment with a hydrogen gas pressure of 80 kgf / cm 2 are explained. However, the experiment was performed using the apparatus of the invention shown in Patent Document 2. As a result, it has been found that sufficient practical performance is exhibited even at atmospheric pressure, and the result is applied to the invention of Patent Document 2. The official certification is that the decontamination treatment is performed on a low-concentration PCB having a concentration of 1% (10,000 mg / kg) or less at a temperature = 150 to 250 ° C. and a pressure = atmospheric pressure to 0.3 MPa. It has become. The detoxification process conditions of the present invention are within the scope of public certification.
In the verification test for obtaining public certification, 100 liters of low-concentration PCB with a temperature of 250 ° C and a PCB content of 100 ppm was injected in 3 hours in a refiner for electrical insulating oil containing 35 kgf of catalyst (average particle size 2 mm). As a result of the treatment, the dechlorination reaction is almost completely performed at any pressure of atmospheric pressure (1 kgf / cm 2 ), 5 kgf / cm 2 , and 50 kgf / cm 2 , As a result of analyzing the residual PCB and the amount of coplanar PCB, which is said to be particularly toxic, by gas chromatography mass spectrometry / selected ion detection (GC-MS / SIM method), all were below the lower limit of detection (ND). Details of the results are described in Patent Document 2 and will be omitted.

さて、容器11中には、触媒13があらかじめ封入してあり、精製装置本体10に注入された低濃度PCB6aは、触媒13に接触しつつ容器11内を精製装置本体10の下部に設けた貯留部14に向かって移動する。このとき、容器11の水素ガス供給口15から水素ガス16を送り込み、低濃度PCB6aに含まれているPCBから、触媒13の表面で塩素を脱離させ塩化水素に変化させる。生成した塩化水素は、低濃度PCB6aに混ぜられている苛性ソーダ7によりただちに中和されて食塩(NaCl)+水(HO)=食塩水に変化する。 Now, the catalyst 13 is enclosed in the container 11 in advance, and the low-concentration PCB 6a injected into the purifier main body 10 is stored in the container 11 in the lower part of the purifier main body 10 while being in contact with the catalyst 13. It moves toward the part 14. At this time, hydrogen gas 16 is sent from the hydrogen gas supply port 15 of the container 11, and chlorine is desorbed from the PCB contained in the low-concentration PCB 6 a on the surface of the catalyst 13 and changed to hydrogen chloride. The produced hydrogen chloride is immediately neutralized by the caustic soda 7 mixed in the low-concentration PCB 6a, and changes into salt (NaCl) + water (H 2 O) = saline.

貯留部14にはPCBの測定装置17が設置してあり、PCBの無害化の進展をチェッ
ク出来るようになっている。
A PCB measurement device 17 is installed in the storage unit 14 so that the progress of detoxification of the PCB can be checked.

貯留部14の排出口18は、食塩分離フィルタ19、油水分離器20、ポンプ21が配設された、着脱可能な第2の配管22によって貯油槽23と連接されており、測定装置17によって、低濃度PCB6aの無害化の進展状況を測定し、無害化が達成されている場合は、低濃度PCBが無害化された精製電気絶縁油6bは、第2の配管22から貯油槽23に移送される。
PCBから分離された塩素と余剰の苛性ソーダ7、及び水素ガス16は化学反応して生じた食塩と水は何れも変圧器にとって有害であるので、変圧器2を継続して使用する場合には、精製電気絶縁油6bが変圧器2に還流する前に除去しておかなければならない。
The discharge port 18 of the storage unit 14 is connected to the oil storage tank 23 by a detachable second pipe 22 in which a salt separation filter 19, an oil / water separator 20, and a pump 21 are arranged. When the progress of detoxification of the low-concentration PCB 6a is measured and the detoxification is achieved, the refined electrical insulating oil 6b detoxified from the low-concentration PCB is transferred from the second pipe 22 to the oil storage tank 23. The
Chlorine separated from PCB, excess caustic soda 7, and hydrogen gas 16 are both harmful to the transformer because salt and water produced by chemical reaction are both harmful. The refined electrical insulating oil 6b must be removed before returning to the transformer 2.

精製装置1の低濃度PCB6aの処理能力は、変圧器2に使用されている低濃度PCB6aの全量を一度に無害化処理する能力を有している必要はない。精製装置1の精製能力に見あった分量づつ低濃度PCB6aは無害化され、精製電気絶縁油6bとなって順次、貯油槽23に送られてくる。   The processing capacity of the low-concentration PCB 6a of the refining device 1 does not need to have the capability of detoxifying all the low-concentration PCB 6a used in the transformer 2 at once. The low-concentration PCB 6a is made harmless by an amount suitable for the refining capacity of the refining device 1, and is sequentially sent to the oil storage tank 23 as a refined electrical insulating oil 6b.

貯油槽23は、変圧器2の低濃度PCB6aのほぼ全量を収納する容量を有しており、変圧器2の低濃度PCBの「ほぼ全て」が無害化されるまで貯油される。ただし、この段階でPCBが無害化されるのは、変圧器2に使用されている低濃度PCB6の「ほぼ全て」であって、「全量」ではない。すなわち、前記のごとく、変圧器2に使用されている低濃度PCB6aには、変圧器2の容器に付着したり、絶縁紙等に捕捉されている分があり、ポンプ5によって変圧器2から排出できる低濃度PCB6aには限りがある。   The oil storage tank 23 has a capacity for storing almost the entire amount of the low concentration PCB 6a of the transformer 2, and the oil is stored until "almost all" of the low concentration PCB of the transformer 2 is rendered harmless. However, at this stage, the PCB is rendered harmless by “almost all” of the low-concentration PCB 6 used in the transformer 2 and not by “total amount”. That is, as described above, the low-concentration PCB 6a used in the transformer 2 is attached to the container of the transformer 2 or trapped by insulating paper or the like, and is discharged from the transformer 2 by the pump 5. There is a limit to the low-density PCB 6a that can be produced.

変圧器2から抜き取り無害化した精製電気絶縁油6bは、貯油槽23と着脱可能な第3の配管26を介して、変圧器2の導出口3とは略略反対側にある導入口27から変圧器に還流される。
低濃度PCB6aを無害化するに際して、一旦150〜250℃に加熱したが、変圧器の許容温度は、概ね100℃程度に設計されていることから、この温度のままで精製電気絶縁油6bを戻すわけにはいかない。しかし、貯油槽23に投入、あるいは貯留されている間に冷めてしまうので、変圧器2に還流する前に温度確認が必要ではあるものの、精製電気絶縁油6bを貯油槽23に一旦留置することは好都合である。
The refined electrical insulating oil 6b extracted from the transformer 2 and rendered harmless is transformed from an inlet 27 that is substantially opposite to the outlet 3 of the transformer 2 through a third pipe 26 that is detachable from the oil storage tank 23. To reflux.
When decontaminating the low-concentration PCB 6a, it was once heated to 150 to 250 ° C., but the allowable temperature of the transformer is designed to be about 100 ° C., so the purified electrical insulating oil 6b is returned at this temperature. I can't help. However, since it cools while being put into or stored in the oil storage tank 23, the temperature of the oil needs to be checked before returning to the transformer 2, but the refined electrical insulating oil 6 b is temporarily placed in the oil storage tank 23. Is convenient.

第2の配管22の途中には、加熱器9を介して精製装置本体10の注入口12と連通する着脱可能な第4の配管24が分岐して配設してあり、第4の配管24と第2の配管22には、それぞれストップバルブ25aとストップバルブ25bが装着してある。低濃度PCB6aのPCB濃度が高いなどの理由で、測定装置17によって低濃度PCB6aの無害化が不十分と判定された場合、精製途次にある低濃度PCB6aは、第2の配管22の途中から第4の配管24を通って加熱器9を介して精製装置本体10に環流させ無害化処理を継続できるようになっている。
精製装置1が、この環流系を有すること、すなわち低濃度PCB6aを循環させて所望の無害化水準を達成出来るようにしてあることは、特許文献3に詳しく説明してある。
In the middle of the second pipe 22, a detachable fourth pipe 24 communicating with the inlet 12 of the purification apparatus main body 10 is branched and disposed via the heater 9. The second pipe 22 is provided with a stop valve 25a and a stop valve 25b, respectively. If the measurement device 17 determines that the low-concentration PCB 6a is not detoxified because the PCB concentration of the low-concentration PCB 6a is high, the low-concentration PCB 6a that is in the process of purification is removed from the middle of the second pipe 22. The detoxification process can be continued by circulating through the fourth pipe 24 to the purification apparatus main body 10 via the heater 9.
It is described in detail in Patent Document 3 that the purifying apparatus 1 has this reflux system, that is, the low concentration PCB 6a can be circulated to achieve a desired detoxification level.

第2の配管22から貯油槽23に移送するか、加熱器9を介して精製装置本体10に循環させるかは、ストップバルブ25aとストップバルブ25bの開閉装置操作によって制御される。すなわち、無害化処理を継続している間はストップバルブ25aを開、ストップバルブ25bを閉とし、精製装置本体10から排出された無害化が進行中の低濃度PCB6aを第2の配管22から第4の配管24を介して精製装置本体10に必要回数だけ循環させる。PCBの無害化反応が終了したらストップバルブ25aを閉、ストップバルブ25bを開とし、第2の配管22から精製電気絶縁油6bを貯油槽23に導出する。
なお、第4の配管は、第2の配管から分岐するのではなく、貯留部14に第2の配管と併設してもよい。
Whether the oil is transferred from the second pipe 22 to the oil storage tank 23 or circulated to the purifier main body 10 via the heater 9 is controlled by operating the stop valves 25a and 25b. That is, while the detoxification process is continued, the stop valve 25a is opened, the stop valve 25b is closed, and the low-concentration PCB 6a that is being detoxified and is discharged from the purifier main body 10 is removed from the second pipe 22 through the second pipe 22. 4 is circulated through the purifier main body 10 through the pipe 24 of the required number of times. When the PCB detoxification reaction is completed, the stop valve 25 a is closed, the stop valve 25 b is opened, and the purified electrical insulating oil 6 b is led out from the second pipe 22 to the oil storage tank 23.
Note that the fourth pipe may not be branched from the second pipe, but may be provided in the storage unit 14 together with the second pipe.

また、PCBの測定装置17を貯留部14に設置する場合について説明したが、測定装置17のコストや、分析に要する時間によっては、測定装置17は精製装置本体10に付加しないで、例えば別に用意した分析装置や既存の分析装置を使用してもよい。
また、精製装置本体10の大きさや製作費によっては、貯留部14を精製装置本体10から分離し、第2の配管22の途中に設置してもよい。
Moreover, although the case where the measuring device 17 of PCB was installed in the storage part 14 was demonstrated, depending on the cost of the measuring device 17 and the time which analysis requires, the measuring device 17 is not added to the refiner | purifier main body 10, For example, it prepares separately. Analyzing apparatuses that have been used or existing analyzing apparatuses may be used.
Further, depending on the size and manufacturing cost of the purification apparatus main body 10, the storage unit 14 may be separated from the purification apparatus main body 10 and installed in the middle of the second pipe 22.

窒素ガス28は、精製装置本体10内に空気が侵入して水素ガス16と反応するのを防止するための保安用である。   The nitrogen gas 28 is used for security to prevent air from entering the purifier main body 10 and reacting with the hydrogen gas 16.

なお、この電気絶縁油の精製システムは、有害性がいわれているPCBを扱い、かつ変圧器2の据付場所で化学処理を行うものであることから、変圧器2を含めクローズドシステムとして構成することが必要である。   This electrical insulation oil refining system handles PCBs that are said to be harmful and performs chemical treatment at the place where the transformer 2 is installed, so it should be configured as a closed system including the transformer 2. is required.

本発明は、前記のとおり、主に大形の変圧器等の電気機器そのものを無害化することをねらいとしているが、一口に大形変圧器といっても、その容量には、比較的小形の10MVA級品から300MVAを超えるような大きな電気機器があり、電気絶縁油の使用量には数十倍の差がある製品群がある。無害化する対象変圧器2の大きさに見あって精製装置1を適宜の精製能力を付与することが適当な場合もあろうが、精製能力の比較的小さい精製装置1によって、いろいろな容量の変圧器2に適用することは、経済性の観点から重要で、本発明を適用する変圧器2の容量や、無害化処理をする数量、処理期間等を考慮して精製装置1の精製能力を決めることが必要がある。   As described above, the present invention is mainly aimed at detoxifying the electrical equipment itself such as a large transformer, but even if it is a large transformer, the capacity is relatively small. There are large electrical devices that exceed 300 MVA from 10 MVA class products, and there is a product group that has a difference of several tens of times in the amount of electrical insulating oil used. Depending on the size of the target transformer 2 to be detoxified, it may be appropriate to give the refining apparatus 1 an appropriate refining capacity, but depending on the refining apparatus 1 having a relatively small refining capacity, various capacities can be obtained. Application to the transformer 2 is important from the viewpoint of economic efficiency, and the refining capacity of the refining apparatus 1 is considered in consideration of the capacity of the transformer 2 to which the present invention is applied, the quantity to be detoxified, the processing period, and the like. It is necessary to decide.

本発明の重要な点は、単独の液状で存在する低濃度PCB6aを変圧器2から抜き取った後、変圧器2内に自然滴下して溜まる低濃度PCB6aを更に変圧器2から抜き取るとともに、絶縁紙等に捕捉され変圧器2内に留まった低濃度PCB6aに含まれているPCBを、低濃度PCBの無害化が進展した精製電気絶縁油6b中に滲出、溶解させ、十分低濃度化した電気絶縁油6b中のPCB濃度と平衡させて、無害化に関するいわゆる卒業基準を達成させる手法をとっていることである。自然滴下と溶解平衡をもたらす分配の法則の最適な活用について説明する。   The important point of the present invention is that after the low-concentration PCB 6a existing in the form of a single liquid is extracted from the transformer 2, the low-concentration PCB 6a that is naturally dropped and collected in the transformer 2 is further extracted from the transformer 2, and insulating paper is used. PCBs contained in the low-concentration PCB 6a captured in the transformer 2 and remaining in the transformer 2 are exuded and dissolved in the refined electrical insulating oil 6b in which the decontamination of the low-concentration PCB has been made harmless, and the electric insulation is sufficiently reduced In other words, a technique is adopted in which the so-called graduation standard regarding detoxification is achieved by balancing with the PCB concentration in the oil 6b. Explain the optimal use of the law of partitioning that causes spontaneous dripping and dissolution equilibrium.

まず、分配の法則とPCB濃度の平衡について説明する。
濃度の高いPCBを含む電気絶縁油が染み込んだ絶縁紙等を、PCBを含まないか、濃度の低いPCBを含む電気絶縁油に浸漬すると、絶縁紙等に捕捉されているPCB濃度の高い電気絶縁油からPCBが、PCBを含まないか濃度の低いPCBを含む電気絶縁油中に滲み出してくる。これを分配の法則といい、PCB以外でも起こる普遍的な物理現象である。絶縁紙等に捕捉されている電気絶縁油中のPCB濃度と、単独の液状で存在する電気絶縁油中のPCB濃度が平衡(等しくなる)に達すれば、PCBの滲み出しは停止する。
図4に約20ppmの低濃度PCBが混入した小形変圧器から電気絶縁油を抜き取り、PCBを含まない新油である電気絶縁油に入れ換えた場合の、変圧器本体から新油中へのPCBの滲出、溶解状況を測定した実験結果を示す。絶縁紙等に捕捉されたPCBは、電気絶縁油を交換した直後から新油中へ溶解を始め、新油中のPCB濃度が上昇するにしたがい滲出速度が低下する。この実験では、約25日で新油中のPCB濃度が飽和に達した。このときの新油中のPCB濃度は、絶縁紙等に捕捉され変圧器中に残留したPCBの総量から計算した平衡時の濃度に合致することが確認された。絶縁紙等から電気絶縁油中へのPCBの滲出、溶解速度、すなわち電気絶縁油中と絶縁紙等に捕捉されている電気絶縁油中のPCB濃度が平衡するまでの時間は、PCB濃度や絶縁紙などの絶縁油浸透性材料の種類、量等によって異なるが、前記のとおり、小形の変圧器でも1ヶ月程度を要する。構造が複雑で、使用されている絶縁紙等の量の多い大形電気機器ではさらに長期間を要すると考えられる。実際の低濃度PCB6aの処理に際しては実態に即して日程計画を立てなければならない。
First, the distribution law and the PCB concentration balance will be described.
When insulating paper or the like soaked in electrical insulating oil containing PCB with high concentration is immersed in electrical insulating oil containing PCB with low concentration or PCB with low concentration, electrical insulation with high PCB concentration captured by insulating paper etc. PCBs ooze out of the oil into electrical insulating oil that contains no PCBs or low concentrations of PCBs. This is called the law of distribution, and is a universal physical phenomenon that occurs outside of PCB. When the PCB concentration in the electrical insulating oil captured by the insulating paper or the like and the PCB concentration in the electrical insulating oil existing in a single liquid state reach an equilibrium (equal), the bleeding of the PCB stops.
Fig. 4 shows that the electrical insulation oil is extracted from a small transformer mixed with low-concentration PCB of about 20 ppm and replaced with electrical insulation oil that is a new oil that does not contain PCB. The experimental result which measured the exudation and the dissolution condition is shown. The PCB captured by the insulating paper or the like starts to dissolve in the new oil immediately after the electric insulating oil is replaced, and the leaching rate decreases as the PCB concentration in the new oil increases. In this experiment, the PCB concentration in the fresh oil reached saturation in about 25 days. It was confirmed that the PCB concentration in the new oil at this time matched the concentration at equilibrium calculated from the total amount of PCB captured in the insulating paper or the like and remaining in the transformer. PCB leaching / dissolution rate from insulating paper or the like into the electrical insulating oil, that is, the time until the PCB concentration in the electrical insulating oil and the electrical insulating oil captured by the insulating paper equilibrates is the PCB concentration or insulation Although it depends on the type and amount of insulating oil-permeable material such as paper, as described above, even a small transformer requires about one month. Large electric devices with a complicated structure and a large amount of insulating paper or the like used are considered to require a longer period of time. When actually processing the low-concentration PCB 6a, it is necessary to make a schedule according to the actual situation.

次に、自然滴下について説明する。
変圧器の容器壁面等に付着した電気絶縁油、及び絶縁紙等の絶縁油浸透性材に捕捉された電気絶縁油に対し、重力による自然滴下による付着量、及び捕捉量の減少について実験した結果を図5、及び図6に示す。
Next, natural dripping will be described.
Results of experiments on the amount of adhesion due to gravity dripping and the reduction of the amount of trapped electrical insulating oil attached to the container wall of the transformer and the insulating oil permeable material such as insulating paper Are shown in FIG. 5 and FIG.

図5は、電気絶縁油の入った小形変圧器の容器から電気絶縁油を抜き取ったあと、該容器を逆さにした場合の、容器の壁面に付着した電気絶縁油の減少状況を実験した結果である。付着電気絶縁油の減少量は、容器の重量変化から換算した。図5によれば約1分で使用電気絶縁油の0.1%が容器壁面等に留まっているだけになる。つまり、短時間でほとんどの電気絶縁油は滴下してしまう。したがって、実際にPCBの無害化処理を行う場合は、低濃度PCB6aを変圧器2から精製装置1に移送する間に、変圧器2の容器の壁面等に付着しているだけの低濃度PCB6aは、変圧器2の底部に滴下してしまい回収できるので、特に気を配る必要はない。   Fig. 5 shows the results of an experiment on the reduction of the electrical insulating oil adhering to the wall of the container when the container was turned upside down after the electrical insulating oil was extracted from the container of the small transformer containing the electrical insulating oil. is there. The amount of decrease in the adhered electrical insulating oil was converted from the change in the weight of the container. According to FIG. 5, only 0.1% of the used electric insulating oil remains on the container wall surface in about 1 minute. That is, most of the electrical insulating oil is dripped in a short time. Therefore, when actually detoxifying the PCB, the low-concentration PCB 6a only attached to the wall surface of the container of the transformer 2 while the low-concentration PCB 6a is transferred from the transformer 2 to the refining device 1 Since it drops to the bottom of the transformer 2 and can be recovered, there is no need to pay particular attention.

図6は、変圧器の中身をつり上げた状態で、絶縁紙等に捕捉された電気絶縁油を自然滴下させた場合の、捕捉されている電気絶縁油の減少状況を実験した結果である。この場合も、変圧器の中身の重量変化から電気絶縁油の捕捉量を換算して求めた。変圧器の中身の場合は、中身をつり上げた直後から、中身に付着したり捕捉された電気絶縁油は、重力による自然滴下によって急速に減少し始める。30分以内に変圧器に使用されている電気絶縁油の1%程が変圧器の中身より滴り落ちるが、自然滴下量は二次曲線的に減少し、次の1%減少には、約10時間を要する。このように自然滴下によって低濃度PCBを回収できる量には限りがあるが、自然滴下によって出来るだけ多くの低濃度PCBを回収しようとすれば、相当時間を要すると考えなければならない。
しかし、このことは、本発明に適用する精製装置1の処理能力とマッチングさせやすく、好都合な面でもある。すなわち、前記のとおり、精製装置1は、変圧器2に使用されている低濃度PCB6aの全量を一度に精製する処理能力を有する必要はなく、低濃度PCB6aを何度かに分けて無害化処理を行う。また、PCBの濃度によっては、精製装置1を繰り返し循環させて無害化処理を行うので、相当長時間の作業となる。結果的には、自然滴下の過程を踏みつつ、並行作業的に無害化処理を進行させるということになって、自然滴下を促すための作業時間をほとんど設定する必要がないということになる。
FIG. 6 is a result of an experiment on a decrease state of the captured electric insulating oil when the electric insulating oil captured by the insulating paper or the like is naturally dropped while the content of the transformer is lifted. Also in this case, the amount of electrical insulating oil captured was converted from the change in weight of the transformer contents. In the case of the contents of the transformer, immediately after the contents are lifted, the electrical insulating oil adhering to or captured by the contents starts to decrease rapidly due to natural dripping due to gravity. Within 30 minutes, about 1% of the electrical insulating oil used in the transformer drops from the transformer, but the amount of natural dripping decreases in a quadratic curve. It takes time. As described above, the amount of low-concentration PCB that can be recovered by natural dripping is limited, but if it is attempted to recover as much low-concentration PCB as possible by natural dripping, it must be considered that a considerable amount of time is required.
However, this is easy to match with the processing capacity of the refining apparatus 1 applied to the present invention, which is also an advantageous aspect. That is, as described above, the refining device 1 does not need to have a processing capacity for refining the entire amount of the low-concentration PCB 6a used in the transformer 2 at once, and the decontamination treatment is performed by dividing the low-concentration PCB 6a several times. I do. In addition, depending on the PCB concentration, the purification device 1 is repeatedly circulated to perform the detoxification process, which requires a considerable amount of work. As a result, the detoxification process is advanced in parallel work while stepping on the natural dripping process, so that it is not necessary to set a work time for promoting the natural dripping.

さて、ここまでの結果を実器に適用した場合について考察する。
PCBの無害化処理に関するいわゆる卒業基準は、0.5mg/kg(≒0.5ppm)である。
1)考察のための設定条件
・変圧器に使用されている電気絶縁油の総量を20kg。
・12時間の自然滴下処理後に、変圧器中身に捕捉されたままの電気絶縁油量は、図6のとおり6%。
・無害化処理によって電気絶縁油単独のPCB濃度を0.1ppmまで精製する。
2)溶解、平衡に達したときに卒業基準を満たすことが出来る変圧器のPCB濃度
無害化処理前のPCB濃度をχppm(χmg/kg)とすれば、
・変圧器中身に捕捉されたPCB量
20×0.06×χ (mg)
・無害化処理した電気絶縁油中に含まれるPCB量
20×(1−0.06)×0.1 (mg)
・無害化処理した電気絶縁油を変圧器に戻した場合のPCB量はこの和となる。
20×0.06×χ+20×(1−0.06)×0.1 (mg)
・いっぽう無害化処理した電気絶縁油を変圧器に戻し、平衡後のPCB濃度が卒業基準の濃度(0.5ppm)となるPCB量
20×0.5=10 (mg)
したがって、平衡後に卒業基準を満たすことが出来る変圧器の電気絶縁油の初期PCB濃度は
20×0.06×χ+20×(1−0.06)×0.1=20×0.5
χ={0.5−(1−0.06)×0.1}/0.06≒6.8 (mg/kg)
つまり、電気絶縁油の初期PCB濃度が、約6.8ppm以下であれば1回の処理で卒業基準を満たすことが可能である。
大形変圧器のPCB濃度は、ほとんどが5ppm以下と考えられることから、上記の条件で無害化の目的を達することが出来る。
Now, let us consider the case where the results up to here are applied to a real device.
The so-called graduation standard for PCB detoxification is 0.5 mg / kg (≈0.5 ppm).
1) Setting conditions for consideration ・ The total amount of electrical insulating oil used in the transformer is 20 kg.
・ After 12 hours of natural dripping treatment, the amount of electrical insulating oil still trapped in the transformer is 6% as shown in FIG.
-Refine the PCB concentration of the electrical insulating oil alone to 0.1 ppm by detoxification treatment.
2) PCB concentration of transformer that can satisfy graduation criteria when it reaches dissolution and equilibrium If PCB concentration before detoxification treatment is χppm (χmg / kg),
・ The amount of PCB trapped in the transformer 20 × 0.06 × χ (mg)
-PCB content in detoxified electrical insulation oil 20 x (1-0.06) x 0.1 (mg)
・ The amount of PCB when detoxified electrical insulating oil is returned to the transformer is this sum.
20 × 0.06 × χ + 20 × (1−0.06) × 0.1 (mg)
・ On the other hand, detoxified electrical insulating oil is returned to the transformer, and the PCB concentration after equilibrium is the graduation standard concentration (0.5 ppm) 20 × 0.5 = 10 (mg)
Therefore, the initial PCB concentration of the electrical insulating oil of the transformer that can meet the graduation criteria after equilibrium is 20 × 0.06 × χ + 20 × (1−0.06) × 0.1 = 20 × 0.5
χ = {0.5− (1−0.06) × 0.1} /0.06≈6.8 (mg / kg)
That is, if the initial PCB concentration of the electrical insulating oil is about 6.8 ppm or less, it is possible to satisfy the graduation criteria in one process.
Since the PCB concentration of large transformers is considered to be almost 5 ppm or less, the purpose of detoxification can be achieved under the above conditions.

しかし、余裕を持って処理をする、あるいはもっと高濃度のPCB混入油を無害化処理するには十分ではない。
したがって、このような条件の変圧器を無害化するには、
1)上記と同じ工程を繰り返す。
2)無害化する電気絶縁油の精製度を0.1ppmより低濃度化する。
3)低濃度PCBの回収率を上げる。
その方法としては、
a)自然滴下時間をもっと長くする。
b)変圧器2の内部圧力を、いわゆる真空引きの操作によって低圧化し、低濃度PCBの流動性を高めて滴下量を増やす。
大形変圧器は、もともと真空引き後に空気に触れないようにして注油する電気機器であり、真空引きに耐える強度を有する電気機器である。
等の方法がある。
また、図4に見るとおり、PCBの濃度差が大きいほど電気絶縁油中へのPCBの滲出が早い。そこで、無害化処理によってPCB濃度が低下した精製電気絶縁油6bを変圧器2の上部から降り注ぐように変圧器中身に掛けてやれば、絶縁紙等に再び染み込み、PCBが濃くなった状態で自然滴下してくる。これを回収し無害化すれば、絶縁紙等に捕捉されているPCBの総量を素早く低減することが可能である。ただし、降り注ぐ精製電気絶縁油6bは、PCBに汚染されて低濃度PCB6aになってしまうので、再び回収してPCBの無害化処理を行うことが必要になる。精製電気絶縁油6bの散布に際しては、変圧器2の構造やPCB濃度等を考慮し、実態にあった所要量を見定めて行うようにすることが肝要である。
以上のような方法を適用することによって、さらに高濃度のPCBが入った電気機器についても容易に無害化処理が可能であるが、何れの方法とするかとか、いくつかの方法を組み合わせて適用するかなどについては、実態に合わせて選択するのがよい。
However, it is not sufficient for processing with a margin, or for detoxifying the higher concentration PCB mixed oil.
Therefore, to detoxify a transformer with such conditions,
1) Repeat the same steps as above.
2) Reduce the purity of the electrical insulating oil to be detoxified below 0.1 ppm.
3) Increase the recovery rate of low-concentration PCB.
As the method,
a) Make the natural dripping time longer.
b) The internal pressure of the transformer 2 is reduced by a so-called evacuation operation to increase the fluidity of the low-concentration PCB and increase the dripping amount.
A large transformer is an electrical device that is originally lubricated so that it does not come into contact with air after evacuation, and is strong enough to withstand evacuation.
There are methods.
Further, as seen in FIG. 4, the larger the PCB concentration difference, the faster PCB bleeds into the electrical insulating oil. Therefore, if the refined electrical insulating oil 6b, whose PCB concentration has been reduced by detoxification treatment, is applied to the transformer contents so as to pour down from the upper part of the transformer 2, it will soak into the insulating paper and the like again, and the PCB will naturally become darker. Dripping. If this is recovered and rendered harmless, the total amount of PCB captured by insulating paper or the like can be quickly reduced. However, since the refined electrical insulating oil 6b poured down is contaminated by the PCB and becomes a low-concentration PCB 6a, it is necessary to collect it again and perform a PCB detoxification process. When spraying the refined electrical insulating oil 6b, it is important to determine the required amount in accordance with the actual situation in consideration of the structure of the transformer 2, the PCB concentration, and the like.
By applying the method described above, it is possible to easily detoxify electrical equipment that contains even higher concentrations of PCB. However, which method is used, and some methods can be used in combination. It is better to choose according to the actual situation.

PCBの無害化処理は、電気絶縁油中のPCBの濃度が0.5mg/kg(≒0.5ppm)以下になれば、いわゆる卒業基準に達し、特定有害産業廃棄物とする必要がなくなることが廃掃法で定められている。上記で説明した方法によって、変圧器2内の絶縁紙等に残存しているPCBが、無害化が進展した精製電気絶縁油6b中に抽出され、絶縁紙等に捕捉されているPCBと精製電気絶縁油6b中のPCBの両者のPCB濃度が平衡状態に達したときに卒業基準を満たすようにすれば、低濃度PCB6aは無害な精製電気絶縁油6bになって変圧器2そのものが無害な電気機器となる。
絶縁紙等に染み込んだ低濃度PCB6aからPCBが抽出され、精製電気絶縁油6bのPCB濃度と平衡に達するには、前記のとおり長い時間が必要であるが、変圧器2を継続して使用する場合は、PCB無害化の達成を急ぐ必要は全くない。
The PCB detoxification treatment can reach the so-called graduation standard and eliminate the need for specific hazardous industrial waste if the PCB concentration in the electrical insulating oil is 0.5 mg / kg (≈0.5 ppm) or less. It is defined by the Waste Disposal Law. By the method described above, the PCB remaining on the insulating paper or the like in the transformer 2 is extracted into the refined electrical insulating oil 6b that has been made harmless, and the PCB and the refined electricity captured by the insulating paper or the like. If the PCB concentration of both PCBs in the insulating oil 6b reaches the equilibrium state, the low concentration PCB 6a becomes harmless purified electrical insulating oil 6b and the transformer 2 itself is harmless. It becomes equipment.
It takes a long time for the PCB to be extracted from the low-concentration PCB 6a soaked in insulating paper, etc., and to reach equilibrium with the PCB concentration of the refined electrical insulating oil 6b, but the transformer 2 is used continuously. In that case, there is no need to rush to achieve PCB detoxification.

なお、精製装置1は、低濃度PCB6aの無害化処理が済んだら、変圧器2から分離し、次の変圧器2の無害化処理を行えるようにすることが経済的で望ましい。そのためには、精製装置1は、車載形や可搬形で構成するのがよい。特に車載形とすれば迅速な移動が可能で、速やかにPCBを無害化処理するという社会的要請に沿うものとなる。
他の実施例として、車29に車載型の精製装置1を適用した変圧器2の無害化処理システムを図7に示す。
In addition, it is economically desirable that the refining apparatus 1 is separated from the transformer 2 after the decontamination process of the low-concentration PCB 6a is completed so that the next transformer 2 can be detoxified. For that purpose, the refiner | purifier 1 is good to comprise with a vehicle-mounted type or a portable type. In particular, if it is an on-vehicle type, it can be moved quickly, and it meets the social demand for promptly detoxifying the PCB.
As another embodiment, FIG. 7 shows a harmless treatment system for the transformer 2 in which the in-vehicle refining device 1 is applied to a car 29.

また、上記では貯油槽23を独立した容器のように説明したが、貯油槽23は、可搬形てあることが望ましく、タンクローリー車のような市販車をそのまま利用してもよい。低濃度PCB6aの収容量に制約があるが複数の車輌を連接すれば対処でき、再利用に向いている。また、精製装置1を車載型に構成した場合は、貯油槽23となるタンクローリー車30と同期して運用することが容易となって、一層利用効率が高まり、迅速で、かつ経済的に低濃度PCB6aを無害化処理することが可能である。他の実施例として、貯油槽23にタンクローリー車30を適用した場合を図8に示す。   In the above description, the oil storage tank 23 is described as an independent container. However, the oil storage tank 23 is preferably portable, and a commercial vehicle such as a tank truck may be used as it is. Although there is a restriction on the amount of low-concentration PCB 6a, it can be dealt with by connecting a plurality of vehicles and is suitable for reuse. Further, when the refining device 1 is configured as an on-vehicle type, it becomes easy to operate in synchronization with the tank truck 30 serving as the oil storage tank 23, and the utilization efficiency is further increased, and the concentration is reduced quickly and economically. It is possible to detoxify the PCB 6a. As another embodiment, FIG. 8 shows a case where a tank truck 30 is applied to the oil storage tank 23.

PCBの化学構造の一例を示す図である。It is a figure which shows an example of the chemical structure of PCB. PCBを水素化し、無害化したビフェニル化合物の化学構造を示す図である。It is a figure which shows the chemical structure of the biphenyl compound which hydrogenated and detoxified PCB. 本発明のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器の無害化処理システムの一実施例を示す図である。It is a figure which shows one Example of the detoxification processing system of the electric equipment using the electric insulation oil containing the polychlorinated biphenyl of this invention. PCBの電気絶縁油中への滲出、溶解状況を測定した実験結果を示す図である。It is a figure which shows the experimental result which measured the exudation in the electric insulation oil of PCB, and the dissolution condition. 変圧器の容器に付着した電気絶縁油が、重力による自然滴下によって減少していく実験結果をす示す図である。It is a figure which shows the experimental result in which the electric insulation oil adhering to the container of a transformer reduces by the natural dripping by gravity. 変圧器2の中身の絶縁紙等に捕捉された電気絶縁油が、重力による自然滴下によって減少していく実験結果を示す図である。It is a figure which shows the experimental result in which the electric insulation oil capture | acquired by the insulating paper etc. of the content of the transformer 2 reduces by the natural dripping by gravity. 本発明のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器の無害化処理システムの、他の実施例を示す図である。It is a figure which shows the other Example of the detoxification processing system of the electric equipment using the electric insulation oil containing the polychlorinated biphenyl of this invention. 本発明のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器の無害化処理システムの、他の実施例を示す図である。It is a figure which shows the other Example of the detoxification processing system of the electric equipment using the electric insulation oil containing the polychlorinated biphenyl of this invention.

符号の説明Explanation of symbols

1 精製装置
2 変圧器
3 導出口
4 第1の配管
5 ポンプ
6a 低濃度PCB
6b 精製電気絶縁油
7 苛性ソーダ
8 投入口
9 加熱器
10 精製装置本体
11 容器
12 注入口
13 触媒
14 貯留部
15 水素ガス供給口
16 水素ガス
17 測定装置
18 排出口
19 食塩分離フィルタ
20 油水分離器
21 ポンプ
22 第2の配管
23 貯油槽
24 第4の配管
25a ストップバルブ
25b ストップバルブ
26 第3の配管
27 導入口
28 窒素ガス
29 車
30 タンクローリー車
DESCRIPTION OF SYMBOLS 1 Refiner 2 Transformer 3 Outlet 4 1st piping 5 Pump 6a Low concentration PCB
6b Refined electrical insulating oil 7 Caustic soda 8 Input port 9 Heater 10 Purifier main body 11 Container 12 Inlet 13 Catalyst 14 Reservoir 15 Hydrogen gas supply port 16 Hydrogen gas 17 Measuring device 18 Discharge port 19 Salt separation filter 20 Oil / water separator 21 Pump 22 Second piping 23 Oil storage tank 24 Fourth piping 25a Stop valve 25b Stop valve 26 Third piping 27 Inlet port 28 Nitrogen gas 29 Car 30 Tank truck

Claims (5)

0.5mg/kg超〜10000mg/kg以下のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器と、水素ガス雰囲気中において、ゼオライト・ニッケル、又はニッケル・モリブデン、ニッケル・白金等を骨格とするニッケル系の触媒下でポリ塩化ビフェニルを脱塩素化、水素化し無害化する電気絶縁油の無害化処理装置と、電気機器の略上端、又は下端の導出口から前記電気絶縁油の無害化処理装置の注入口を着脱可能に連接する第1の配管と、水素ガス雰囲気中の前記触媒の間を通過する過程で発生する、触媒の脱塩素化、水素化反応を利用してポリ塩化ビフェニルを無害化処理し、精製した電気絶縁油を収容する貯油槽と、前記電気絶縁油の無害化処理装置の排出口から精製した電気絶縁油を収容する貯油槽を着脱可能に連接する第2の配管と、前記精製した電気絶縁油を収納する貯油槽から前記電気機器の前記導出口と略反対端の導入口を着脱可能に連接する第3の配管によって構成されるポリ塩化ビフェニルを含む電気絶縁油の無害化処理システムであって、前記電気機器から前記無害化処理装置の注入口へ前記ポリ塩化ビフェニルを含有する電気絶縁油を注入し、水素ガス雰囲気中の前記触媒の間を通過する過程で発生する脱塩素化、水素化反応を利用してポリ塩化ビフェニルを無害化処理し、無害化処理装置の注入口とは反対端の排出口から、精製電気絶縁油を貯油槽へ移送し、貯油槽と電気機器の前記導出口とは略反対端の導入口を着脱可能に連接する第3の配管によって、精製電気絶縁油を[電気機器→電気機器の導出口→第1の配管→無害化処理装置の注入口→水素ガス雰囲気下の触媒→無害化処理装置の排出口→第2の配管→貯油槽→第3の配管→電気機器の導入口→電気機器]と循環させ、ポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化するシステム。   Electric equipment using electrical insulating oil containing polychlorinated biphenyl of more than 0.5mg / kg to 10000mg / kg or less, and in a hydrogen gas atmosphere, zeolite / nickel, nickel / molybdenum, nickel / platinum, etc. Detoxification treatment equipment for electrical insulation oil that dechlorinates, hydrogenates and renders polychlorinated biphenyl detoxified under a nickel-based catalyst, and detoxification treatment of the electrical insulation oil from the outlet at the substantially upper or lower end of the electrical equipment Polychlorinated biphenyls are produced by utilizing the dechlorination and hydrogenation reaction of the catalyst that occurs in the process of passing between the first pipe that removably connects the inlet of the apparatus and the catalyst in the hydrogen gas atmosphere. An oil storage tank for storing detoxified and refined electrical insulating oil and an oil storage tank for storing purified electrical insulating oil from the discharge port of the detoxifying treatment apparatus for the electrical insulating oil are detachably connected. And polychlorinated biphenyl constituted by a third pipe that detachably connects an inlet port substantially opposite to the outlet port of the electrical device from an oil storage tank that stores the refined electrical insulating oil. An electrical insulating oil detoxification treatment system, wherein the electrical insulation oil containing the polychlorinated biphenyl is injected from the electrical equipment into an inlet of the detoxification processing apparatus and passes between the catalysts in a hydrogen gas atmosphere. Polychlorinated biphenyl is detoxified using the dechlorination and hydrogenation reactions that occur during the process, and the refined electrical insulating oil is transferred to the oil storage tank from the discharge port opposite to the inlet of the detoxification device. Then, the refined electrical insulating oil [electric equipment → electric equipment outlet → first pipe] is connected by a third pipe that removably connects the inlet of the oil storage tank and the outlet of the electric equipment. → Injection of detoxification equipment → Catalyst under hydrogen gas atmosphere → Deleting port of detoxification treatment device → Second piping → Oil storage tank → Third piping → Electrical equipment inlet → Electric equipment] A system that renders electrical equipment that uses oil harmless. 請求項1の発明において、無害化処理装置の排出口から貯油槽へ精製電気絶縁油を移送する第2の配管から、再び無害化処理装置の注入口へ循環させる第3の配管を分岐し、第2の配管、及び第3の配管にそれぞれストップバルブを配設し、ストップバルブの開閉操作によって、前記排出口から第3の配管によって、無害化処理装置へ精製途次の電気絶縁油を、又は第2の配管によって、貯油槽へ精製を終了した電気絶縁油を、選択して流通せしめるように構成したことを特徴とする、請求項1記載のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化するシステム。   In the invention of claim 1, a second pipe that circulates the purified electrical insulating oil from the discharge port of the detoxification treatment device to the oil storage tank to the injection port of the detoxification treatment device is branched from the second pipe that transfers the purified electrical insulating oil, A stop valve is disposed in each of the second pipe and the third pipe, and by opening and closing the stop valve, the electrical insulation oil in the course of purification is supplied from the discharge port to the detoxification treatment apparatus through the third pipe. Alternatively, the electrical insulating oil containing polychlorinated biphenyl according to claim 1, wherein the electrical insulating oil that has been refined to the oil storage tank is selected and circulated by the second pipe. System that renders the electrical equipment itself harmless. 電気絶縁油の無害化処理装置を車載形で構成し、電気機器の据付場所に移動してポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器、及び貯油槽と現地で連接して電気絶縁油を無害化処理し、無害化処理後は、無害化処理装置を貯油槽、及び電気機器から分離し、該電気機器とは別の場所に移動できるように構成したことを特徴とする、請求項1、及び請求項2記載のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化するシステム。   The electric insulation oil detoxification treatment equipment is configured on-board, moved to the installation location of the electric equipment, and the electric equipment using the electric insulation oil containing polychlorinated biphenyl and the oil storage tank are connected on-site for electric insulation. The oil is detoxified, and after the detoxification treatment, the detoxification processing device is separated from the oil storage tank and the electrical equipment, and can be moved to a place different from the electrical equipment. A system for detoxifying electrical equipment itself using electrical insulating oil containing polychlorinated biphenyl according to claim 1 and claim 2. 貯油槽にタンクローリー車を適用したことを特徴とする、請求項1、請求項2、及び請求項3記載のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化するシステム。   4. A system for detoxifying electrical equipment itself using electrical insulating oil containing polychlorinated biphenyl according to claim 1, wherein a tank truck is applied to an oil storage tank. 0.5mg/kg超〜10000mg/kg以下のポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器と、ポリ塩化ビフェニルを脱塩素化、水素化し無害化する電気絶縁油の無害化処理装置を連接し、前記の電気機器から無害化処理装置の注入口へ前記の電気絶縁油を注入し、前記の無害化処理装置内を流通する過程で無害化が進展した精製電気絶縁油を無害化処理装置の排出口から貯油槽へ蓄え、前記の電気機器内に滴下する電気絶縁油の残留分をさらに回収し、無害化処理装置の注入口へ注入し、貯油槽に蓄えた精製電気絶縁油を前記電気機器に還流し、ポリ塩化ビフェニルを含有する電気絶縁油を使用した電気機器そのものを無害化する方法。   Electric equipment using electrical insulation oil containing polychlorinated biphenyl of 0.5 mg / kg or more and 10000 mg / kg or less, and electrical insulation oil detoxification treatment equipment that dechlorinates, hydrogenates and detoxifies polychlorinated biphenyl Decontamination treatment of purified electrical insulation oil that has been detoxified in the process of being connected, injecting the electrical insulating oil from the electrical equipment to the inlet of the detoxification treatment device, and circulating in the detoxification treatment device The electrical insulation oil that is stored in the oil storage tank from the discharge port of the device and dripped into the electrical equipment is further recovered, injected into the injection port of the detoxification treatment device, and the refined electrical insulation oil stored in the oil storage tank is stored. A method for detoxifying an electrical device itself using an electrical insulating oil containing polychlorinated biphenyl by being refluxed to the electrical device.
JP2004014433A 2004-01-22 2004-01-22 Treatment system and method for rendering electric apparatus using electricity insulating oil containing polychlorinated biphenyl harmless Pending JP2005204907A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008271999A (en) * 2006-12-04 2008-11-13 Meidensha Corp Method of making pcb in electric equipment insulating oil harmless and method of cleaning electric equipment insulating oil
JP2009260283A (en) * 2008-03-17 2009-11-05 Central Res Inst Of Electric Power Ind Method of cleaning pcb contaminated transformer and cleaning apparatus
JP2014067957A (en) * 2012-09-27 2014-04-17 Nippon Shiigatekku Kk Purification method of transformer with oil contaminated by polychlorinated biphenyl stored therein and purification system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008271999A (en) * 2006-12-04 2008-11-13 Meidensha Corp Method of making pcb in electric equipment insulating oil harmless and method of cleaning electric equipment insulating oil
JP2009260283A (en) * 2008-03-17 2009-11-05 Central Res Inst Of Electric Power Ind Method of cleaning pcb contaminated transformer and cleaning apparatus
JP2014067957A (en) * 2012-09-27 2014-04-17 Nippon Shiigatekku Kk Purification method of transformer with oil contaminated by polychlorinated biphenyl stored therein and purification system

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