JP2006289288A - Method for detoxifying pole-mounted transformer including pcb-mixed insulating oil - Google Patents

Method for detoxifying pole-mounted transformer including pcb-mixed insulating oil Download PDF

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JP2006289288A
JP2006289288A JP2005115145A JP2005115145A JP2006289288A JP 2006289288 A JP2006289288 A JP 2006289288A JP 2005115145 A JP2005115145 A JP 2005115145A JP 2005115145 A JP2005115145 A JP 2005115145A JP 2006289288 A JP2006289288 A JP 2006289288A
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pole
iron core
members
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Takeshi Matsumura
豪 松村
Shizuo Sasaki
静夫 佐々木
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Nichiyo Engineering Corp
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<P>PROBLEM TO BE SOLVED: To provide a method for detoxifying a pole-mounted transformer, in which the pole-mounted transformer including PCB-mixed insulating oil is disassembled safely without compelling a worker to work in a PCB atmosphere, components of the disassembled transformer are sorted by members and each of sorted members is recycled as resources. <P>SOLUTION: The method for detoxifying the pole-mounted transformer, in which the pole-mounted transformer including PCB-mixed insulating oil is disassembled/sorted and each of sorted members is detoxified by multistage cleaning and recycled as resources, comprises a step (a) of withdrawing PCB-mixed insulating oil from the pole-mounted transformer including PCB-mixed insulating oil, a step (b) of disassembling/sorting the oil-withdrawn pole-mounted transformer into a case, metals, a thunder-resistant element, an insulator, electrical wires, a core and other members, a step (c) of disassembling/sorting the core into an iron core and a coil, a step (d) of primarily cleaning, secondarily cleaning and drying each of sorted members, a step (e) of suitably sorting each of sorted members and reducing the volume of each of them and a step (f) of judging the cleanliness of each of the cleaned members and cleaning each of uncleaned members again. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、低濃度PCB混入絶縁油(以下、PCB油という)を使用している機器よりPCB油を抜き出し、PCB油の抜き出された機器を構成部品に解体し、解体された部品を洗浄し、さらに部品を構成する部材をリサイクル資源化するための処理方法に関する。更に詳しくは、PCB混入絶縁油を含有する柱上変圧器(以下、変圧器又はトランスという)からPCB油を抜き出した後、構成部品に解体・切断し、洗浄し、変圧器の部品の構成部材である容器、金属、碍子、鉄芯、銅、紙、PCB油等に分別し、リサイクル資源化するための処理方法に関する。   The present invention extracts PCB oil from equipment using low-concentration PCB-mixed insulating oil (hereinafter referred to as PCB oil), disassembles the equipment from which PCB oil has been extracted, and cleans the disassembled parts. In addition, the present invention relates to a processing method for recycling a member constituting a part as a recycling resource. More specifically, after extracting PCB oil from a pole transformer (hereinafter referred to as transformer or transformer) containing insulating oil mixed with PCB, the component parts of the transformer parts are disassembled, cut, washed, and the like. It is related with the processing method for separating into a container, a metal, an insulator, an iron core, copper, paper, PCB oil, etc., and recycling it.

PCBは、優れた化学的安定性、熱により分解しにくい、酸化されにくい、酸・アルカリに安定、金属をほとんど腐食しない、水にきわめて溶けにくい、電気絶縁性が良好、高沸点、不燃性などの特性を有していることから、高圧トランス用、高圧コンデンサ用、低圧トランス・コンデンサ用(家電製品、蛍光灯、水銀灯用等)、低圧トランス用(6kVA以下)、柱上トランス用絶縁油等に使用されてきた。しかしながら、PCBの人体への有毒性が明らかになり、1974年までに製造、輸入、開放系用途での使用が禁止された。また、1992年には廃PCB、PCBを含む廃油およびPCB汚染物が「廃棄物処理法」に基づく特別管理産業廃棄物に指定され、事業所等での保管が義務づけられ、トランスをはじめPCB含有機器類の相当数が事業所等で保管されている。
さらに、「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」によりPCB、PCBを含む廃油などを15年以内に処理することが義務化された。この結果、保管場所に安全に保管されていたPCBについて、廃棄物処理法に従い無害化処理が始まっている状況にある(例えば、特許文献1〜4等参照)。
PCB has excellent chemical stability, is not easily decomposed by heat, is not easily oxidized, is stable to acids and alkalis, hardly corrodes metals, is extremely insoluble in water, has good electrical insulation, high boiling point, nonflammability, etc. Therefore, for high-voltage transformers, high-voltage capacitors, low-voltage transformers and capacitors (home appliances, fluorescent lamps, mercury lamps, etc.), low-voltage transformers (6 kVA or less), insulating oil for pole transformers, etc. Has been used. However, the toxicity of PCBs to the human body became apparent, and by 1974, the use in manufacturing, importing and open systems was prohibited. In 1992, waste PCBs, waste oil containing PCBs and PCB contaminants were designated as specially controlled industrial wastes based on the “Waste Management Law” and required to be stored at business establishments. A considerable number of devices are stored at offices.
Furthermore, according to the “Special Measures Law for Promotion of Proper Treatment of Polychlorinated Biphenyl Waste”, it became obligatory to treat PCB, waste oil containing PCB, etc. within 15 years. As a result, the PCB that has been safely stored in the storage location is in a state where detoxification processing has begun in accordance with the Waste Disposal Law (see, for example, Patent Documents 1 to 4).

しかし、PCB含有機器の構成部材の無害化処理には、以下に示すような問題点が残されている。
例えば、変圧器は、ケースとコアとから構成されており、コアは鉄芯とコイルとから構成されている。コイルの構成部材のリサイクルに当たって、PCB油の付着したコイルを焼却すると、絶縁油から有毒ガスを発生し大気汚染の原因となるため好ましくない。PCB油の付着したコイルを焼却することなくそのリサイクルを行うためには、コイルからPCB油を除去するため洗浄作業または真空加熱脱気する必要がある。しかし、コイルには、その内部にまでPCB油が浸透した状態にあるため、変圧器をそのまま洗浄または真空加熱脱気してもPCB油を完全に除去することは困難である。また、コアからPCB油を完全に除去するためには、まず鉄芯とコイルとに分離する解体作業を行って鉄芯およびコイルをそれぞれ個別に洗浄または真空加熱脱気の処理を行う必要がある。
However, the following problems remain in the detoxification process for the components of the PCB-containing device.
For example, the transformer is composed of a case and a core, and the core is composed of an iron core and a coil. It is not preferable to incinerate the coil to which the PCB oil adheres when recycling the coil components, because toxic gas is generated from the insulating oil and causes air pollution. In order to recycle the coil to which the PCB oil is adhered without incineration, it is necessary to perform a cleaning operation or vacuum heating and deaeration in order to remove the PCB oil from the coil. However, since the PCB oil is infiltrated into the coil, it is difficult to completely remove the PCB oil even if the transformer is washed or vacuum-heated and degassed as it is. Further, in order to completely remove PCB oil from the core, it is necessary to first perform a disassembly work to separate the iron core and the coil, and individually clean the iron core and the coil or perform a vacuum heating deaeration process. .

一般的な柱上変圧器について図2に示す。図2(a)は柱上変圧器の一部切欠平面図であり、図2(b)は柱上変圧器の一部切欠正面図であり、図2(c)は柱上変圧器の一部切欠側面図である。なお、各図の説明において同一の要素には同一の符号を付す。図2に示すように、変圧器は、容器(ケース)201、蓋(カバー)202、ボルト・ナット203等の金属、耐雷素子204、碍子205、電線206、鉄芯207、コイル208、架台(金属)209、バンド(金属)210、タップ台(碍子)211、絶縁油212等、様々な部品から構成されている。   A typical pole transformer is shown in FIG. 2 (a) is a partially cutaway plan view of a pole transformer, FIG. 2 (b) is a partially cutaway front view of the pole transformer, and FIG. 2 (c) is one of the pole transformers. It is a part notch side view. In the description of each drawing, the same elements are denoted by the same reference numerals. As shown in FIG. 2, the transformer includes a container (case) 201, a lid (cover) 202, a metal such as a bolt and nut 203, a lightning protection element 204, an insulator 205, an electric wire 206, an iron core 207, a coil 208, a gantry ( (Metal) 209, band (metal) 210, tap stand (insulator) 211, insulating oil 212, and the like.

変圧器の構成部品のリサイクルを行うに当たっては、前述の各構成部品それぞれについて洗浄または真空加熱脱気等の処理を行う必要があり、そのために変圧器を前述の各構成部品に解体・分別する必要がある。しかし、PCBは室温でも一定量が気化するため、この気化したPCBを作業環境から完全に排除するには、技術的、経済性の面から困難が大きく、作業員の安全が十分に確保できない恐れがあった。また、変圧器の解体作業の全てを手作業で行うと作業者がPCB油により汚染されるだけでなく、作業時間が膨大になり、作業者への負担やコストが大きい。   When recycling the transformer components, it is necessary to perform a process such as cleaning or vacuum heating and degassing for each of the above-mentioned components. For this purpose, it is necessary to disassemble and separate the transformer into the above-mentioned components. There is. However, since a certain amount of PCB is vaporized even at room temperature, it is difficult to completely remove the vaporized PCB from the work environment from the technical and economic viewpoints, and the safety of workers may not be sufficiently secured. was there. Further, if all the dismantling work of the transformer is performed manually, the worker is not only contaminated with the PCB oil, but the work time becomes enormous, and the burden on the worker and the cost are large.

特許文献1〜4には、さまざまなPCB含有機器の無害化処理方法について開示されている。しかし、特許文献1、3または4に記載された方法はいずれも、変圧器の解体前に変圧器本体内部の洗浄を必要としており、また、特許文献2に記載された方法の好ましい態様では、破砕する前に−70℃以下に冷却することを要件としており、その処理に時間を要し、必要な設備を設けなければならず、コストがかかる。   Patent Documents 1 to 4 disclose various harmless processing methods for PCB-containing devices. However, any of the methods described in Patent Documents 1, 3 and 4 requires cleaning the transformer body before disassembling the transformer, and in a preferred embodiment of the method described in Patent Document 2, It is required to cool to −70 ° C. or lower before crushing, and it takes time for the treatment, and necessary facilities must be provided, which is costly.

特開平9−79531号公報JP-A-9-79531 特開2000−140817号公報JP 2000-140817 A 特開2001−246014号公報JP 2001-246014 A 特開2002−143825号公報JP 2002-143825 A

本発明は、作業員がPCB雰囲気下で作業することなく、PCB混入絶縁油を含有する柱上変圧器を安全に解体し、解体した部品を部材に分別し、各部材をリサイクル資源化できる、柱上変圧器の無害化処理方法を提供することを目的とする。   The present invention allows a worker to safely dismantle a pole transformer containing insulating oil mixed with PCB without separating it from working in a PCB atmosphere, separate the disassembled parts into members, and recycle each member into resources. It aims at providing the detoxification processing method of a pole transformer.

高圧トランス用絶縁油は、PCB濃度が約60%、トリクロロベンゼン約40%であり、PCB濃度が高い。これに対し、柱上トランス用絶縁油のPCB濃度は数十ppm以下である。この事実をもとに、本発明者らは鋭意検討を重ねた結果、低濃度PCB油の処理は、高濃度PCB油の処理とは異なった方法で行うことが可能であり、しかもその方が合理的で低コストで処理できるとの知見を得た。本発明はこのような知見に基づきなされるに至ったものである。   Insulating oil for high-pressure transformers has a PCB concentration of about 60% and trichlorobenzene of about 40%, and the PCB concentration is high. On the other hand, the PCB concentration of the insulating oil for the pole transformer is several tens of ppm or less. Based on this fact, the present inventors have conducted intensive studies, and as a result, the treatment of low-concentration PCB oil can be performed by a method different from the treatment of high-concentration PCB oil. The knowledge that it is reasonable and can be processed at low cost was obtained. The present invention has been made based on such findings.

すなわち、本発明は、
(1)PCB混入絶縁油を含有する柱上変圧器を分別解体し、各部材を無害化して再資源化する柱上変圧器の無害化処理方法であって、
(a)PCB混入絶縁油を含有する柱上変圧器からPCB混入絶縁油を油抜きする工程、
(b)前記柱上変圧器を、ケース、金属、耐雷素子、碍子、電線、コア、及びその他の部材にそれぞれ分別解体する工程、
(c)前記コアを、さらに鉄芯とコイルに分別解体する工程、
(d)前記の解体した各部材をそれぞれ、一次洗浄し、二次洗浄し、乾燥する工程、
(e)前記の各部材を適宜分別して減容する工程、
(f)前記の洗浄後の各部材を判定洗浄する工程
を含んでなることを特徴とする柱上変圧器の無害化処理方法、
(2)PCB混入絶縁油を含有する柱上変圧器を分別解体し、各部材を無害化して再資源化する柱上変圧器の無害化処理方法であって、
(a)PCB混入絶縁油を含有する柱上変圧器からPCB混入絶縁油を油抜きする工程、
(b)前記柱上変圧器を、ケース、金属、耐雷素子、碍子、電線、コア、並びに木・パッキン・プレスボード及びその他の部材に分別解体する工程、
(c)前記耐雷素子をさらに金属、並びに碍子および素子に分別解体する工程、
(d)前記碍子をさらに碍子部品と電線に分別解体する工程、
(e)前記コアの巻線を切断して、さらに鉄芯とコイルに分別解体する工程、
(f)前記鉄芯を切断し、鉄芯湾曲矯正をしてからV字プレス処理し、得られた鉄芯板を洗浄装置にて洗浄する工程、
(g)前記コイルから木を除去した後に、該コイルを洗浄装置にて洗浄し、破砕して、比重選別機により銅と紙に分別し、銅を洗浄装置にて二次洗浄し、紙を圧縮して減容する工程、
(h)前記のケース、金属、碍子、電線、並びに木・パッキン・プレスボード及びその他の部材をそれぞれ洗浄装置にて洗浄する工程、
(i)前記の洗浄後のケース、金属、碍子、鉄芯板および銅を、部材毎に洗浄装置にて判定洗浄する工程
を含んでなることを特徴とする柱上変圧器の無害化処理方法、
That is, the present invention
(1) It is a detoxification processing method for a pole transformer that separates and dismantles pole transformers containing insulating oil mixed with PCB, detoxifies each member, and recycles them.
(A) A step of draining the PCB mixed insulating oil from the pole transformer containing the PCB mixed insulating oil,
(B) a step of separating and disassembling the pole transformer into a case, a metal, a lightning protection element, an insulator, an electric wire, a core, and other members,
(C) a step of further separating and disassembling the core into an iron core and a coil;
(D) Steps of primary cleaning, secondary cleaning, and drying of each of the disassembled members,
(E) a step of appropriately separating and reducing the volume of each member described above,
(F) A detoxifying treatment method for a pole transformer, comprising a step of determining and washing each member after washing,
(2) A method for detoxifying a pole transformer that separates and dismantles pole transformers containing insulating oil mixed with PCBs, detoxifies each member, and recycles them.
(A) A step of draining the PCB mixed insulating oil from the pole transformer containing the PCB mixed insulating oil,
(B) a step of separating and disassembling the pole transformer into a case, metal, lightning protection element, insulator, electric wire, core, and wood, packing, press board, and other members;
(C) a step of separating and disassembling the lightning-resistant element into metal and insulators and elements;
(D) a step of further separating and separating the insulator into an insulator part and an electric wire;
(E) cutting the winding of the core and further separating and disassembling into an iron core and a coil;
(F) cutting the iron core, correcting the iron core curvature, performing a V-shaped press treatment, and cleaning the obtained iron core plate with a cleaning device;
(G) After removing the wood from the coil, the coil is washed with a washing device, crushed, separated into copper and paper with a specific gravity sorter, and the copper is secondarily washed with the washing device, Compressing and reducing the volume,
(H) a step of cleaning the case, metal, insulator, electric wire, wood, packing, press board and other members with a cleaning device,
(I) A method for detoxifying a pole transformer, comprising a step of determining and cleaning the cleaned case, metal, insulator, iron core plate, and copper with a cleaning device for each member. ,

(3)前記の各部材を、識別子が付与された搬送容器に各部材毎に収納し、搬送容器に付与された識別子の情報と管理システムの処理予約登録とを照合し、前記の各工程間または各処理間を自動搬送機により搬送することを特徴とする(1)又は(2)項に記載の柱上変圧器の無害化処理方法、
(4)前記の各洗浄工程において、第2石油類又は第3石油類の炭化水素系洗浄剤や有機溶剤を使用して洗浄を行い、使用後の洗浄剤を蒸留再生装置により浄化してPCB混入絶縁油を分離回収し、洗浄剤を繰返し使用することを特徴とする(1)〜(3)のいずれか1項に記載の柱上変圧器の無害化処理方法、
(5)前記の各工程に用いられる各処理装置の開口部をフードで囲い、フード内を負圧吸引し、活性炭フィルターを経由して雰囲気循環することを特徴とする(1)〜(4)のいずれか1項に記載の柱上変圧器の無害化処理方法、
(3) Each member is stored in a transport container to which an identifier is assigned for each member, the identifier information given to the transport container is collated with the processing reservation registration of the management system, Alternatively, the process for detoxifying a pole transformer according to the item (1) or (2), wherein each process is carried by an automatic carrier.
(4) In each of the above-described cleaning steps, cleaning is performed using a hydrocarbon-based cleaning agent or an organic solvent of the second petroleum or the third petroleum, and the used cleaning agent is purified by a distillation regenerator and printed on the PCB. (1) to (3), the detoxification method for a pole transformer according to any one of (1) to (3), wherein the mixed insulating oil is separated and recovered, and the cleaning agent is used repeatedly.
(5) The opening of each processing apparatus used in each of the above steps is surrounded by a hood, the inside of the hood is sucked under negative pressure, and the atmosphere is circulated through an activated carbon filter (1) to (4) Detoxification method for pole transformers according to any one of the above,

(6)前記の各工程のうち排気が発生する工程において、凝縮装置、局所排気吸引装置及び活性炭フィルターを用いて、PCB蒸気含有量を環境規制値未満の濃度に低減して排気することを特徴とする(1)〜(5)のいずれか1項に記載の柱上変圧器の無害化処理方法、および
(7)前記の洗浄装置または蒸留再生装置が、PCB漏洩検知装置およびオイルパンを備え、該各装置を減圧下にて運転することを特徴とする(1)〜(6)のいずれか1項に記載の柱上変圧器の無害化処理方法
を提供するものである。
なお、(2)項において、工程(c)と工程(d)とはいずれの工程を先に行ってもよく、また、工程(e)〜(g)は、工程(b)の後であって工程(h)の前に行われればよく工程(c)又は(d)よりも先に行ってもよい。
(6) In the process where exhaust is generated among the above processes, the PCB vapor content is reduced to a concentration lower than the environmental regulation value using a condenser, a local exhaust suction device and an activated carbon filter, and exhausted. (1) The detoxification method for a pole transformer according to any one of (1) to (5), and (7) the cleaning device or the distillation regeneration device includes a PCB leakage detection device and an oil pan. The present invention provides a method for detoxifying a pole transformer according to any one of (1) to (6), wherein each of the devices is operated under reduced pressure.
In step (2), either step (c) or step (d) may be performed first, and steps (e) to (g) are performed after step (b). It may be performed before step (h) and may be performed before step (c) or (d).

本発明は、PCBそのものを除去することを第一義とするが、除去の過程にあって、工程の合理性、作業の容易さ、作業員の安全性の高さ、設備からの有害物蒸散の防止、排気の処理、安全な溶剤の適用、溶剤の回収、低ランニングコスト、臭い等周辺環境への配慮、十分な処理能力、搬送その他処理の自動化、部材の再資源化、再資源化によるコストの回収等あらゆる面に高い配慮がなされており、長年保管を余儀なくされてきたPCB含有絶縁油変圧器を処理し、産業廃棄物として、また有価物である金属、銅、碍子等をリサイクルする有効な方法である。
すなわち、本発明の方法は、低濃度PCB含有絶縁油が使用されていた柱上変圧器を、低コストで安全に無害化することができ、部品を構成する部材をリサイクル資源化することができる。
The primary purpose of the present invention is to remove the PCB itself, but in the process of removal, the rationality of the process, the ease of work, the high safety of the workers, the evaporation of harmful substances from the equipment. Prevention, exhaust treatment, safe solvent application, solvent recovery, low running cost, consideration of the surrounding environment such as odor, sufficient processing capacity, transportation and other processing automation, parts recycling, recycling High consideration is given to all aspects such as cost recovery, and PCB-containing insulating oil transformers that have been stored for many years are processed, and recycled as industrial waste and valuable metals, copper, insulators, etc. It is an effective method.
That is, the method of the present invention can safely detoxify a pole transformer in which low-concentration PCB-containing insulating oil has been used at low cost, and can recycle the members constituting the parts. .

以下、本発明について詳細に説明する。
前述したように、変圧器は、容器、金属(ボルト・ナット等を含める)、耐雷素子、碍子、電線、鉄芯、コイル、紙、木・パッキン・プレスボード等、様々な部品から構成されている(図2参照)。本発明の方法は、これらの部品・部材に分別解体し、それぞれ洗浄して無害化し、各部材をリサイクル資源化するものである。
Hereinafter, the present invention will be described in detail.
As mentioned above, transformers are composed of various parts such as containers, metals (including bolts and nuts), lightning protection elements, insulators, electric wires, iron cores, coils, paper, wood, packing and press boards. (See FIG. 2). In the method of the present invention, these parts / members are separated and disassembled, cleaned and rendered harmless, and each member is recycled.

本発明の好ましい一実施態様のフローチャート図を図1に示す。図1に示すように、本発明は、以下の工程を含むことが好ましい。
(1)受入工程101
(2)乾燥工程102
(3)保管工程103
(4)油抜き・解体工程104
(5)洗浄工程105
(6)コア処理工程106
(7)判定洗浄工程107
(8)判定待ち保管工程108
(9)払出・保管工程109
(10)排気処理工程(図示せず)
これらの工程の他に、洗浄剤の再生工程、紙、木、パッキン等を処理する工程、PCB油の無害化処理工程を含むことが好ましい。
A flow chart of one preferred embodiment of the present invention is shown in FIG. As shown in FIG. 1, the present invention preferably includes the following steps.
(1) Acceptance process 101
(2) Drying step 102
(3) Storage process 103
(4) Oil removal / disassembly step 104
(5) Cleaning step 105
(6) Core processing step 106
(7) Determination washing process 107
(8) Judgment waiting storage process 108
(9) Discharge / storage process 109
(10) Exhaust treatment process (not shown)
In addition to these steps, it is preferable to include a cleaning agent regeneration step, a step of treating paper, wood, packing, etc., and a PCB oil detoxification treatment step.

上記の(4)油抜き・解体工程から(8)判定待ち保管工程までの各工程のそれぞれは、ボックス化され、あるいはフード化され、外気と作業雰囲気とが遮断されており、各工程は、(8)判定待ち保管工程の下流側より空気を供給し、(4)油抜き・解体工程の上流側に設置したブロワ等の吸引装置で、作業雰囲気を清浄化することが好ましい。
また、(4)油抜き・解体工程から(9)払出・保管工程までの搬送容器あるいはバスケット等には識別番号が付与され、管理システムに登録された状態にあり、(4)油抜き・解体工程から(9)払出・保管工程までは、管理システムの制御下で各工程の搬送および作業が行われるのが好ましい。
以下に、図1を参照しながら、各工程の好ましい態様を説明する。
Each of the steps from the above (4) oil draining / disassembling step to (8) determination waiting storage step is boxed or hooded, and the outside air and the working atmosphere are shut off. (8) It is preferable that air is supplied from the downstream side of the determination waiting storage step, and (4) the working atmosphere is cleaned with a suction device such as a blower installed on the upstream side of the oil draining / disassembling step.
In addition, (4) Oil draining / dismantling process and (9) Discharge / storage process from the container or basket to the identification number is assigned and registered in the management system. (4) Oil draining / dismantling From the process to the (9) payout / storage process, it is preferable that the transport and work of each process be performed under the control of the management system.
Below, the preferable aspect of each process is demonstrated, referring FIG.

(1)受入工程101
保管場所より、トラック等で処理工場に搬入された変圧器は、受入工程101で受入処理が行われる。
トラックが荷受室に進入し、指定場所に停車すると専用移載ハンドが取り付けられた天井クレーン等で、荷降しをし、受入装置指定位置に載置された空パレットに積載する。変圧器には、搬入された変圧器を識別できるバーコード等の識別子が付与されており、バーコード等を専用端末で読取り、管理システムに受入情報を入力する。
変圧器の識別は特に限定されず、バーコードにこだわることはなく、変圧器が識別できるのに必要桁数を備えた、穿孔コード、2進コード、数値コード、記号コード等のものであればよい。
また、識別番号の付与は、受入時にこだわるものではなく、適宜必要な時期に付与すればよい。
(1) Acceptance process 101
The transformer carried into the processing factory from the storage location by truck or the like is subjected to an acceptance process in the acceptance process 101.
When the truck enters the cargo receiving room and stops at the designated location, it is unloaded with an overhead crane or the like with a dedicated transfer hand attached and loaded onto an empty pallet placed at the designated location of the receiving device. The transformer is given an identifier such as a barcode that can identify the transformer that has been carried in. The barcode is read by a dedicated terminal, and acceptance information is input to the management system.
Transformer identification is not particularly limited, as long as it is a perforated code, binary code, numeric code, symbol code, etc. that does not stick to barcodes and has the necessary number of digits to enable the transformer to be identified Good.
Further, the identification number is not given at the time of acceptance, but may be given at a necessary time.

(2)乾燥工程102
受け入られた変圧器は、雨天時の雨濡れ等による工程内への水の浸入を避けるべく、外面に付着した雨滴等を乾燥機で乾燥させる乾燥工程102へ送られる。
乾燥工程102では、処理工程内への水の浸入を阻止することが目的であり、工程内への水の浸入を避けることができれば、乾燥工程102での作業は省略することも可能である。ここで使われる乾燥機は、特殊なものではなく、変圧器の表面の水分を乾燥できるものであればよい。
変圧器外表面水分等の乾燥の終わった変圧器は、生産負荷の均一化等を測る目的のため、管理システムの制御下で保管工程103へ自動搬送される。
(2) Drying step 102
The accepted transformer is sent to a drying process 102 where raindrops and the like adhering to the outer surface are dried by a dryer in order to avoid intrusion of water into the process due to rain or the like during rainy weather.
The purpose of the drying process 102 is to prevent water from entering the treatment process. If the water can be prevented from entering the process, the operation in the drying process 102 can be omitted. The dryer used here is not a special one as long as it can dry the moisture on the surface of the transformer.
The transformer after drying of moisture on the outer surface of the transformer is automatically transferred to the storage process 103 under the control of the management system for the purpose of measuring the uniformity of the production load.

(3)保管工程103
保管工程103へ搬送された変圧器は、管理システムの制御下で、指定された番地の受入保管庫に保管される。
受入保管庫は先入れ・先出し方式の保管庫が好ましく、移載にあたってはスタッカークレーン等を使用する。
工程全体は、管理システムで制御されている。管理システムは、特別なシステムである必要はなく、通常の管理システムが使われる。変圧器は、管理システムでスケジューリングされた処理予約に基づき保管工程103からコンベア等の自動搬送装置により管理システムの制御下で油抜き・解体工程104へ搬出される。
自動搬送装置は特に限定されず、ベルトコンベア、ローラコンベヤ、自走台車、リフター、エレベーター、移載装置等であり、管理システムで制御のできるものであれば良く、特別な自動搬送装置は必要としない。
(3) Storage process 103
The transformer transported to the storage process 103 is stored in the receiving storage at the designated address under the control of the management system.
The receiving storage is preferably a first-in / first-out storage, and a stacker crane or the like is used for transfer.
The entire process is controlled by a management system. The management system does not need to be a special system, and a normal management system is used. The transformer is carried out from the storage process 103 to the oil draining / dismantling process 104 under the control of the management system by an automatic transfer device such as a conveyor based on the processing reservation scheduled by the management system.
The automatic transfer device is not particularly limited, and may be a belt conveyor, a roller conveyor, a self-propelled carriage, a lifter, an elevator, a transfer device, etc., as long as it can be controlled by a management system, and a special automatic transfer device is necessary. do not do.

(4)油抜き・解体工程104
油抜き・解体工程104は、気流制御され、雰囲気が清浄化されている解体場所で行われる。柱上変圧器に用いられているPCB混入絶縁油はPCB濃度が低いため、油抜き後に変圧器本体内部の洗浄をする必要はなく、油抜き後すぐに解体することができる。変圧器の解体は、PCB濃度が低いことから手作業で行うこともできるが、作業員の安全性、作業効率、コスト等を考慮してオートメーション化することが好ましい。
まず、PCB混入絶縁油を含有する柱上変圧器からPCB混入絶縁油10を油抜きする。油抜きされたPCB油10は蒸留再生装置によって分離された絶縁油とともに、工程内のタンクで一時保管し、PCB油処理工程の要求によりポンプ等で移送し、移送先の処理工程129で分解処理し、無害化される。
(4) Oil removal / disassembly step 104
The oil draining / disassembling step 104 is performed at a dismantling place where the airflow is controlled and the atmosphere is cleaned. Since the PCB mixed insulating oil used in the pole transformer has a low PCB concentration, it is not necessary to clean the inside of the transformer body after oil draining, and can be disassembled immediately after oil draining. The transformer can be dismantled manually because the PCB concentration is low, but it is preferable to automate in consideration of worker safety, work efficiency, cost, and the like.
First, the PCB mixed insulating oil 10 is drained from the pole transformer containing the PCB mixed insulating oil. The deoiled PCB oil 10 is temporarily stored in the tank in the process together with the insulating oil separated by the distillation regenerator, transferred by a pump or the like at the request of the PCB oil processing process, and decomposed in the processing process 129 of the transfer destination. And detoxified.

次いで前記柱上変圧器を、ケース(容器)1、金属2、耐雷素子3、碍子4、電線5、コア、並びに木・パッキン・プレスボード及びその他の部材9に、それぞれ分別解体する。
更に、耐雷素子3について解体し、セラミック製素子を収納している金属製保持器を効率的に除去し、金属2と、碍子および素子4(以下、単に碍子という)とに分別する(工程111)。耐雷素子3の解体は任意の方法により行うことができる。
Subsequently, the pole transformer is separated and disassembled into a case (container) 1, a metal 2, a lightning protection element 3, an insulator 4, an electric wire 5, a core, and wood / packing / press board and other members 9.
Further, the lightning protection element 3 is disassembled, the metal cage containing the ceramic element is efficiently removed, and is separated into the metal 2, the insulator and the element 4 (hereinafter simply referred to as insulator) (step 111). ). The lightning protection element 3 can be disassembled by any method.

また、碍子4については碍子の中心を貫通するケーブルがエポキシ樹脂で固定されているので、これを効率的に除去し、碍子部品4(以下、単に碍子という)と電線5とに分別解体する(工程112)。碍子4の解体は任意の方法により行うことができる。   Moreover, since the cable which penetrates the center of an insulator is fixed with the epoxy resin about the insulator 4, this is removed efficiently, and it separates and disassembles into the insulator component 4 (henceforth only insulator) and the electric wire 5 ( Step 112). The insulator 4 can be disassembled by any method.

上記で分別解体された容器1、金属2、碍子・素子4、電線5、並びに木・パッキン・プレスボード及びその他の部材9は、それぞれ専用の搬送容器(例えばバスケット等)に分別して収納される。
これらの分別された部材の入った搬送容器には、分別された部材ごとに適宜バーコード等により識別子が付与され、管理システムに入力される。管理システムの制御下、搬送容器に付与された識別子の情報と管理システムの処理予約登録とを照合し、各工程間または各処理間を自動搬送機により搬送することが好ましい。なお、識別子は、搬送容器が使われる前や部材が投入された時点等で、必要に応じ付与すればよい。
The container 1, metal 2, insulator / element 4, electric wire 5, and wood / packing / press board and other members 9 separated and disassembled as described above are separately stored in dedicated transport containers (for example, baskets). .
An identifier is appropriately given to each of the sorted members by a bar code or the like, and is input to the management system. Under the control of the management system, it is preferable to collate the information of the identifier given to the transport container with the processing reservation registration of the management system and transport each process or each process by an automatic transport machine. The identifier may be given as needed before the transport container is used or when a member is inserted.

(5)洗浄工程105
各搬送用容器に分別収納された容器、金属、碍子、電線、並びに木・パッキン・プレスボード及びその他の部材は、管理システムの制御下で、ベルトコンベア等の自動搬送機でそれぞれ洗浄工程105に自動的に搬送され、洗浄される。
洗浄は、減圧下で浸漬、超音波洗浄、蒸気洗浄、真空乾燥の単位工程を管理システムの制御下で任意の順序・時間を組み合わせることで、部材の特性に合った効率的な洗浄を行う。例えば、特願2004−73936号明細書に記載された多段洗浄方法により行うことができる。
(5) Cleaning step 105
Containers, metal, insulators, electric wires, wood, packing, pressboards and other members separated and stored in each transport container are respectively transferred to the cleaning process 105 by an automatic transport machine such as a belt conveyor under the control of the management system. Automatically transported and cleaned.
Cleaning is performed efficiently in accordance with the characteristics of the member by combining unit steps of immersion, ultrasonic cleaning, steam cleaning, and vacuum drying under reduced pressure in any order and time under the control of the management system. For example, it can be performed by a multi-stage cleaning method described in Japanese Patent Application No. 2004-73936.

具体的には、浸漬洗浄とは、洗浄槽中に溜められた洗浄液中に対象物を所定時間浸漬させることにより、PCB等の汚染物を溶解除去する方法である。浸漬洗浄では、洗浄槽に供給された洗浄液(溶剤)が用いられる。洗浄液(溶剤)については、炭化水素系の洗浄液(例えばノルマルパラフィン系洗浄液など)の中から洗浄対象物の汚染度や除去するPCBの種類等にあった洗浄液を選択することができる。浸漬洗浄手段には、洗浄槽および回収したPCBを含む溶剤を再生する装置(例えば蒸留装置)を備えていることが好ましい。溶剤再生装置を備えることで、新たな溶剤の使用量(補給する溶剤量)を減らすことができる。また、溶剤洗浄手段は洗浄槽よりも低い位置に設置することが好ましい。このような配置とすることにより洗浄槽への液を抜く際に重力によって溶剤を溶剤洗浄手段に流下させることができ、ポンプなどの機器を省略することができる。除染効率の点からは、この浸漬洗浄中にバスケット中の洗浄対象物に対して超音波を照射して洗浄効果を高めることが好ましい。   Specifically, the immersion cleaning is a method of dissolving and removing contaminants such as PCBs by immersing an object in a cleaning solution stored in a cleaning tank for a predetermined time. In the immersion cleaning, a cleaning liquid (solvent) supplied to the cleaning tank is used. As the cleaning liquid (solvent), a cleaning liquid suitable for the degree of contamination of the object to be cleaned and the type of PCB to be removed can be selected from hydrocarbon-based cleaning liquids (for example, normal paraffin-based cleaning liquids). The immersion cleaning means is preferably provided with a cleaning tank and a device (for example, a distillation device) for regenerating the solvent containing the collected PCB. By providing the solvent regeneration device, the amount of new solvent used (the amount of solvent to be replenished) can be reduced. The solvent cleaning means is preferably installed at a position lower than the cleaning tank. With this arrangement, the solvent can be caused to flow down to the solvent cleaning means by gravity when draining the liquid into the cleaning tank, and equipment such as a pump can be omitted. From the viewpoint of decontamination efficiency, it is preferable to increase the cleaning effect by irradiating an object to be cleaned in the basket with ultrasonic waves during the immersion cleaning.

蒸気洗浄について説明する。まず洗浄槽中に洗浄液を蒸発させた蒸気を導入する。この際、洗浄対象物の温度を蒸気の凝縮温度以下とすることにより、洗浄対象物上で洗浄液の蒸気が凝縮する。この凝縮液により対象物表面に付着したPCB等の汚染物を溶解除去する方法を蒸気洗浄という。凝縮時には、蒸気が保有している凝縮潜熱を対象物に移動させる効果があるため、対象物を加熱する効果をもあわせ持つ。
蒸気洗浄手段は、浸漬洗浄から直接洗浄槽へ洗浄液を流入させる手段に加えて、蒸発気化させた洗浄液を洗浄槽へ流入させる手段を有する。洗浄液を蒸発させ、気化させるのに必要な熱量を供給するための蒸気洗浄手段(蒸気発生器等)が浸漬洗浄から洗浄槽への配管の途中に設置されている。蒸気発生器に供給される熱源は、水蒸気や加熱油などの熱媒体を適宜使用することができる。
The steam cleaning will be described. First, steam obtained by evaporating the cleaning liquid is introduced into the cleaning tank. At this time, by setting the temperature of the cleaning object to be equal to or lower than the vapor condensation temperature, the steam of the cleaning liquid is condensed on the cleaning object. A method of dissolving and removing contaminants such as PCB attached to the surface of the object with this condensate is called steam cleaning. At the time of condensation, it has the effect of moving the latent heat of condensation possessed by the steam to the object, so it also has the effect of heating the object.
The vapor cleaning means has means for flowing the evaporated and evaporated cleaning liquid into the cleaning tank in addition to the means for flowing the cleaning liquid directly from the immersion cleaning into the cleaning tank. A steam cleaning means (steam generator or the like) for supplying heat necessary for evaporating and evaporating the cleaning liquid is installed in the middle of the pipe from the immersion cleaning to the cleaning tank. As a heat source supplied to the steam generator, a heat medium such as water vapor or heating oil can be appropriately used.

真空乾燥は、洗浄槽内部を減圧するために用いられる。真空ポンプは使用する条件(洗浄液に対するポンプの耐性、必要とする真空度等)を満足するポンプを適宜選択することができる。また、より効率的に必要とする真空度に達するように、複数台の真空ポンプを利用することが好ましい。真空乾燥の前後には、気体の洗浄溶剤(洗浄液)を冷却するための冷却器が設置されていることが好ましい。冷却器により液化した溶剤やPCBを溶剤洗浄手段に送り、溶剤を再生利用することができ、また、気体状のPCB量を減少させることにより、後段の排気処理への負荷を低減することができる。   Vacuum drying is used to depressurize the inside of the cleaning tank. As the vacuum pump, a pump satisfying the conditions to be used (the resistance of the pump to the cleaning liquid, the required degree of vacuum, etc.) can be appropriately selected. Further, it is preferable to use a plurality of vacuum pumps so as to reach the required degree of vacuum more efficiently. Before and after the vacuum drying, it is preferable to install a cooler for cooling the gaseous cleaning solvent (cleaning liquid). The solvent or PCB liquefied by the cooler can be sent to the solvent cleaning means to recycle the solvent, and by reducing the amount of gaseous PCB, it is possible to reduce the load on the exhaust processing at the subsequent stage. .

洗浄工程で使用される洗浄剤は、第2石油類又は第3石油類から選ばれる炭化水素系洗浄剤や有機溶剤から選ばれる1種類あるいは複数の混合液を使用することができ、適宜再生利用性および経済性を考慮して選ばれる。なお、使用後の洗浄剤は、大気圧又は減圧蒸留再生装置などの再生装置により浄化してPCB混入絶縁油を分離回収し、洗浄剤を繰返し使用・再生利用することができる。   As the cleaning agent used in the cleaning process, one or a plurality of mixed liquids selected from hydrocarbon-based cleaning agents selected from the second petroleums or the third petroleums and organic solvents can be used. Selected in consideration of sex and economy. The cleaning agent after use can be purified by a regenerator such as an atmospheric pressure or vacuum distillation regenerator to separate and recover the PCB mixed insulating oil, and the cleaning agent can be repeatedly used and recycled.

木・パッキン・プレスボード及びその他の部材9については、さらにPCBを低減化する必要がある場合は、洗浄工程105の後、破砕処理し、再洗浄する(工程124、125)。この際の破砕粒度を2mm程度とすることが好ましく、これにより洗浄後の部材中のPCB濃度をムラなく均一化できる。破砕した部材の洗浄は、例えば、特願2004−77219号明細書に記載された洗浄乾燥方法により行うことができる。具体的には、洗浄液を用いて上記破砕部材を洗浄し乾燥するカゴであって洗浄液の総蒸発熱以上の熱量を蓄熱しうる蓄熱材を設けた洗浄乾燥用カゴで洗浄することが好ましい。   If it is necessary to further reduce PCB, wood, packing, press board and other members 9 are crushed and washed again after the cleaning step 105 (steps 124 and 125). The crushing particle size at this time is preferably about 2 mm, whereby the PCB concentration in the cleaned member can be made uniform without unevenness. The crushed member can be cleaned by, for example, a cleaning and drying method described in Japanese Patent Application No. 2004-77219. Specifically, it is preferable to wash with a basket for washing and drying, which is provided with a basket for washing and drying the crushing member using a washing liquid and having a heat storage material capable of storing a heat quantity equal to or greater than the total evaporation heat of the washing liquid.

洗浄工程の終了した木・パッキン・プレスボード及びその他の部材9は、後述するコイルに含まれる紙8と同様に、ドラム充填され、倉庫保管される(工程126、127)。一方、洗浄工程の終了した容器1、金属2、碍子4の入った搬送容器は、管理システムの制御下、自動的に判定洗浄工程107に搬送される。洗浄後の電線は、後述する洗浄後のコイルと共に破砕するために、コイル破砕工程119に搬送される。   The wood, packing, press board, and other members 9 that have completed the cleaning process are filled with drums and stored in a warehouse (processes 126 and 127) in the same manner as paper 8 included in the coil described later. On the other hand, the transport container containing the container 1, the metal 2 and the insulator 4 after the cleaning process is automatically transported to the determination cleaning process 107 under the control of the management system. The washed electric wire is conveyed to the coil crushing step 119 in order to crush it together with the washed coil described later.

(6)コア処理工程106
コアは、コア処理工程106に搬送され、更に解体が行われる。コアは、薄板珪素鋼板が多数枚積層された鉄芯6と、絶縁紙やオイルダクト(割り箸様の木、波板等)を挟んで巻回された、一次・二次の巻線7(銅線:絶縁紙、オイルダクト、巻線から構成されるものをコイルと呼称する。)とが相互に鎖状に組み合わされて構成されている。
解体するためには、鉄芯6かコイル7のいずれか一方を切断するが、鉄芯は積層方法が複数種類に渡り、切断個所によっては切断すると後工程に不都合を生じる可能性があるため、本発明ではコイルを切断する方法が好ましい。
コアには内鉄型、外鉄型等があり、いずれも切断歯に対しては鉄芯の積層面が前後に対面し、コイルの上下端が上下となるような位置関係にセットし、切断歯によって切断・解体する。解体されたコイル7は、作業場で手作業によって、オイルダクトが分別される(工程117)。しかし、紙・木の最終処理形態によっては、特に分別しなくても後工程への影響は無い。
(6) Core processing step 106
The core is conveyed to the core processing step 106 and further disassembled. The core is composed of an iron core 6 in which a large number of thin silicon steel plates are laminated, and primary and secondary windings 7 (copper) wound around insulating paper and oil ducts (wooden chopstick-like wood, corrugated sheets, etc.) Wires: those composed of insulating paper, oil ducts and windings are called coils.) Are combined in a chain.
In order to dismantle, either one of the iron core 6 or the coil 7 is cut, but the iron core has a plurality of lamination methods, and depending on the cutting location, there is a possibility of causing inconvenience in the subsequent process. In the present invention, a method of cutting a coil is preferable.
The core has an inner iron type, an outer iron type, etc., both of which are set in such a positional relationship that the laminated surface of the iron core faces front and back and the upper and lower ends of the coil are up and down with respect to the cutting teeth, and cut Cut and dismantle with teeth. In the disassembled coil 7, the oil duct is separated by manual work at the work place (step 117). However, depending on the final processing form of paper / wood, there is no influence on the subsequent process even if the separation is not performed.

コアの解体は任意の方法により行うことができるが、例えば、特開2003−217956号公報に記載された変圧器の解体方法により行うことができる。具体的には、変圧器の鉄心からコイルを分離する方法として、電動鋸などで鉄心を側面部に当てて位置決めし、鉄心に巻回しされているコイルを切断して分離する方法が好ましい。   The disassembly of the core can be performed by any method, and for example, can be performed by the disassembly method of the transformer described in Japanese Patent Application Laid-Open No. 2003-217756. Specifically, as a method for separating the coil from the iron core of the transformer, a method is preferable in which the iron core is placed on the side surface with an electric saw or the like, and the coil wound around the iron core is cut and separated.

解体分別された鉄芯6はさらに切断される。鉄芯切断(工程113)では鉄芯のタイプ(ラップ巻、C型、巻鉄芯等)によって最適切断場所を油圧切断歯で切断し、一鉄芯を半割2個とする。半割鉄芯は一個ずつ、湾曲矯正装置でほぼ直線状に矯正する(工程114)。この工程では鉄芯を一枚ずつ高速で捌く動作を加えるため、隙間に付着PCB油の多くを洗浄等により、より多く除去できる特徴を有する。鉄芯の切断は任意の方法により行うことができるが、例えば、特開2003−285224号公報に記載された鉄芯切断方法により行うこともできる。具体的には、鉄心をターンテーブル等に載置し、鉄心の内部中空部に設置される中子(上下から押さえる)に対して切断刃をあてがい切断する方法が好ましい。   The iron core 6 separated and separated is further cut. In the iron core cutting (step 113), the optimum cutting location is cut with hydraulic cutting teeth according to the type of iron core (wrap winding, C type, wound iron core, etc.), and one iron core is divided in half. One half of the iron core is straightened by the straightening device almost straightly (step 114). In this process, since an operation of spreading iron cores one by one at a high speed is added, a large amount of PCB oil adhering to the gap can be removed by washing or the like. The iron core can be cut by any method, but for example, the iron core cutting method described in JP-A-2003-285224 can also be used. Specifically, a method in which an iron core is placed on a turntable or the like, and is cut by applying a cutting blade to a core (pressed from above and below) installed in an internal hollow portion of the iron core.

切断された鉄芯の湾曲を矯正してから、V字プレス処理(工程115)をし、得られた鉄芯板を洗浄バスケットに投入する。
V字プレスでは、矯正後の鉄芯を一度に50〜60枚(厚さ:20mm程度)程度ずつプレス台にセットし、油圧によりプレス型を押し下げ、鉄芯板を長手方向に並行にV字プレスする(工程115)。これを行うことで、湾曲矯正された鉄芯はさらに直線状に矯正されるため、ロボットハンドで把持し、鉄板分離機に自動吸引させることが可能となり、洗浄前の鉄芯板への要求処理を適正に終えることができる。
鉄芯板の分離は任意の方法により行うことができるが、例えば、特開2002−124426号公報に記載された鉄板分離機により行うことができる。具体的には、板状体に磁性体を設置することにより、板状体の端面から主面に沿って磁界を誘起して板状体の間に反発力を与え、反発力によって生じた板状体に空隙を与える方法が好ましい。
After correcting the curvature of the cut iron core, a V-shaped press process (step 115) is performed, and the obtained iron core plate is put into a cleaning basket.
In the V-shaped press, 50 to 60 sheets of iron core after correction (thickness: about 20 mm) are set on the press stand at a time, the press die is pushed down by hydraulic pressure, and the iron core plate is V-shaped in parallel with the longitudinal direction. Press (step 115). By doing this, the iron core that has been curved is further straightened, so it can be gripped by a robot hand and automatically sucked by an iron plate separator. Can be finished properly.
Separation of the iron core plate can be performed by any method, and for example, it can be performed by an iron plate separator described in JP-A No. 2002-124426. Specifically, by installing a magnetic body on the plate-like body, a magnetic field is induced along the main surface from the end face of the plate-like body to give a repulsive force between the plate-like bodies, and the plate generated by the repulsive force A method of providing voids in the shape is preferred.

前処理で予め鉄板分離機に懸垂され搬送容器に投入されて搬送された鉄芯板は、移載機で搬送装置から洗浄機に移載され投入される。洗浄バスケットに投入された鉄芯板は、板状体のままで洗浄が行われる(工程116)。
なお、洗浄処理の基準値は、「特別管理産業廃棄物に係る基準の検定方法」(平成4年厚生省告示第192号、改正 平成10年8月第222号)に従うことが好ましく、これによれば、洗浄液試験法:洗浄液PCB濃度0.5mg/kg以下(別表第2の第1)、拭き取り試験法:PCB付着量0.1μg/100cm2以下(別表第2の第2)、部材採取試験法:PCB付着量0.01mg/kg以下(別表第2の第3)である。
The iron core plate that is suspended in the iron plate separator in the pre-treatment and loaded into the transport container and transported is transferred from the transport device to the washing machine by the transfer device and loaded. The iron core plate put in the cleaning basket is cleaned with the plate-like body (step 116).
In addition, it is preferable that the standard value for the cleaning treatment conforms to the “Certification Method for Standards Concerning Specially Managed Industrial Waste” (Ministry of Health and Welfare Notification No. 192, revised August 1998, No. 222). For example, cleaning solution test method: cleaning solution PCB concentration 0.5 mg / kg or less (first of the second table), wiping test method: PCB adhesion amount 0.1 μg / 100 cm 2 or less (second table, second table), member sampling test Method: PCB adhesion amount of 0.01 mg / kg or less (Attached Table 2nd 3rd).

洗浄には、第2石油類又は第3石油類から選ばれる炭化水素系洗浄剤や有機溶剤の1種あるいは複数の混合液を洗浄原液として用いる。洗浄機では、先ず第1原液を蒸発器に導入し、減圧下で溶剤(第1原液)を、熱交換器によってスチームで加熱することによって、溶剤を低温で沸騰させ、溶剤蒸気を継続的に発生させ、これを配管によって、洗浄槽に導入し鉄芯板を洗浄・加熱(以下、減圧蒸気洗浄と呼称する)する。
減圧蒸気洗浄によって付着PCB油を流下除去しつつ、鉄芯板並びに残存PCB油を加温・流動化せしめ、続く減圧浸漬洗浄の効果を高める。減圧浸漬洗浄では超音波洗浄を併用し、減圧装置との相乗によって、脱気超音波洗浄を行う。鉄芯板を高速で振動させることで表面からの絶縁油の脱着を促進し、かつ振動による流れによって脱着したPCB油を速やかに溶剤中へと拡散させる効果により、洗浄力を高め、絶縁油除去を促進している。
第1原液による浸漬洗浄の次には、より清浄な第2原液によりリンス洗浄を行う。この洗浄も前記と同様に行われる。
For cleaning, one or a mixture of a hydrocarbon-based cleaning agent selected from the second petroleum or the third petroleum and an organic solvent is used as a cleaning stock solution. In the washing machine, first, the first stock solution is introduced into the evaporator, and the solvent (first stock solution) is heated by steam with a heat exchanger under reduced pressure, whereby the solvent is boiled at a low temperature and the solvent vapor is continuously supplied. It is generated and introduced into a cleaning tank by piping, and the iron core plate is cleaned and heated (hereinafter referred to as reduced-pressure steam cleaning).
While the attached PCB oil is removed by flowing under reduced pressure steam cleaning, the iron core plate and the remaining PCB oil are heated and fluidized to enhance the effect of subsequent reduced pressure immersion cleaning. In vacuum immersion cleaning, ultrasonic cleaning is used in combination, and degassing ultrasonic cleaning is performed by synergy with the vacuum device. By oscillating the iron core plate at high speed, the desorption of the insulating oil from the surface is promoted, and the PCB oil that has been desorbed by the flow caused by the vibration is quickly diffused into the solvent, increasing the cleaning power and removing the insulating oil. Promotes.
Following immersion cleaning with the first stock solution, rinse cleaning is performed with a cleaner second stock solution. This cleaning is also performed in the same manner as described above.

第2原液の浸漬洗浄後は、第1原液洗浄液を原液タンクに戻し、洗浄槽を空状態にした後、第2原液を蒸発器に導入し、蒸気洗浄を行い鉄芯板、洗浄槽壁、付着液体を約120℃まで加熱する。この時、洗浄槽内は60〜100Torr(7999〜13332Pa)程度となるように諸条件を設定しておく。
時間制御によって蒸気洗浄が終了した後は、真空ポンプの入口弁を開放し、真空吸引することによって槽内真空度を高め、表面付着液体を過飽和状態にして再蒸発させ、鉄芯板、バスケット、槽内壁等を乾燥させ、板状体洗浄を完成させる。
鉄芯板の洗浄は、上述した方法に限定されず、例えば、特開2002−124426号公報に記載された板状体洗浄方法により行うこともできる。具体的には、板状体に磁性体を設置することにより、板状体の端面から主面に沿って磁界を誘起して板状体の間に反発力を与え、反発力によって生じた板状体の空隙に洗浄用流体を導入して板状体の主面を洗浄するので、積層された板状体の主面を積層された状態のまま効率よく洗浄できる方法が好ましい。
洗浄後の鉄芯板は、搬送容器に収容され、管理システムの制御下、自動的に判定洗浄工程107に搬送される。
After immersion cleaning of the second stock solution, return the first stock solution to the stock solution tank, empty the cleaning tank, introduce the second stock solution into the evaporator, perform steam cleaning, iron core plate, cleaning tank wall, Heat the deposited liquid to about 120 ° C. At this time, various conditions are set so that the inside of the cleaning tank is about 60 to 100 Torr (7999 to 13332 Pa).
After steam cleaning is completed by time control, the inlet valve of the vacuum pump is opened, the vacuum in the tank is increased by vacuum suction, the surface adhering liquid is supersaturated and re-evaporated, iron core plate, basket, The inner wall of the tank is dried to complete the plate cleaning.
The cleaning of the iron core plate is not limited to the above-described method, and can be performed by, for example, a plate-like body cleaning method described in JP-A-2002-124426. Specifically, by installing a magnetic body on the plate-like body, a magnetic field is induced along the main surface from the end face of the plate-like body to give a repulsive force between the plate-like bodies, and the plate generated by the repulsive force Since the cleaning fluid is introduced into the gap of the plate-like body to wash the main surface of the plate-like body, a method that can efficiently wash the main surface of the laminated plate-like body while being laminated is preferable.
The cleaned iron core plate is accommodated in a transfer container and automatically transferred to the determination cleaning step 107 under the control of the management system.

解体分別されたコイル7は、木(オイルダクト)を除去した後、洗浄され、破砕され、比重選別機により銅と紙に分別される(工程117〜120)。銅については更に2回目の洗浄を行い(工程121)、紙については破砕して洗浄を行う(工程122、123)。
コイルは前述したように、銅線・銅帯・銅板の他絶縁紙(クラフト紙)や絶縁布、オイルダクト、固定用糸など絶縁材や冷却用構造材等のPCB含浸性材料から構成されている。ここで、PCB含浸性材料とは、PCBが染み込んだ紙くず、木くず及び繊維くずをいう(なお、PCBが付着し又は封入された金属くずをPCB非含浸性材料という)。
まず、コイルからオイルダクト(木)を除去し、該コイルを洗浄装置にて洗浄・乾燥する(工程117、118)。洗浄方法は特に限定されず、例えば、特開2003−257759号公報に記載された変圧器の巻線処理方法により行うこともできる。具体的には、コイルを二軸破砕機、低速破砕機、高速破砕機より構成される破砕機で破砕処理し、比重選別機で銅線と絶縁紙に選別する方法が好ましい。
The disassembled and separated coil 7 is washed, crushed, and separated into copper and paper by a specific gravity sorter after removing the tree (oil duct) (steps 117 to 120). The copper is further washed for the second time (step 121), and the paper is crushed and washed (steps 122 and 123).
As described above, the coil is composed of a PCB-impregnated material such as a copper wire, a copper strip, a copper plate, an insulating paper (craft paper), an insulating cloth, an oil duct, a fixing thread, or a structural material for cooling. Yes. Here, the PCB-impregnated material refers to paper waste, wood waste and fiber waste infiltrated with PCB (note that the metal waste to which PCB is attached or enclosed is referred to as PCB non-impregnated material).
First, the oil duct (wood) is removed from the coil, and the coil is cleaned and dried with a cleaning device (steps 117 and 118). The cleaning method is not particularly limited, and for example, it may be performed by a transformer winding method described in Japanese Patent Application Laid-Open No. 2003-257759. Specifically, a method is preferred in which the coil is crushed by a crusher composed of a biaxial crusher, a low-speed crusher, and a high-speed crusher, and sorted into copper wire and insulating paper by a specific gravity sorter.

乾燥後のコイル等は含浸性材料の影響のため、基準値まで洗浄されていない可能性が考えられるため、銅を回収して2回目の洗浄を行う。銅を回収するために次の破砕及び比重選別を行う。
コイルを破砕機で破砕し、砕片化すると同時に、一次・二次側導体を覆っている絶縁被覆、紙テープ等を効果的に剥離する(工程119)。二次側導体被覆は剥離しにくい性質があるため、段階的に複数の破砕機を組み合わせる(二軸破砕機、一軸破砕機、高速破砕機の三段の組合せが好ましい)場合は最終段の高速破砕機ではスクリーン径を7〜8mmとするのが好ましい。
Since the coil after drying may be not cleaned to the reference value due to the influence of the impregnating material, copper is collected and the second cleaning is performed. The following crushing and specific gravity sorting are performed to recover copper.
The coil is crushed with a crusher and broken into pieces, and at the same time, the insulation coating, paper tape, etc. covering the primary and secondary conductors are effectively peeled off (step 119). Since the secondary conductor coating is difficult to peel off, when combining multiple crushers in stages (a combination of three stages: a twin-screw crusher, a single-screw crusher, and a high-speed crusher is preferred), the final stage high speed In the crusher, the screen diameter is preferably 7 to 8 mm.

破砕後のコイル砕片は定量フィーダーを経由して、比重選別機に投入し、紙・布・糸等を分離し、純度の高い銅を回収する(工程120)。比重選別機は細径穴パンチングメタルを使用したスクリーンを階段状に加工し、このスクリーンを楕円運動させることによって、昇段力を付与しながらスクリーン下側から送風し、軽比重の紙を分離するタイプのものが高い銅純度を与えるため好ましい。
パンチングメタル穴径は詰り防止、銅の高純度化に多大な影響が考えられるため、選定には十分な検討が必要であるが、直径0.8mmとすると詰りが少なく、銅純度も99.9重量%以上の良い結果が得られているので特に好ましい。
The crushed coil fragments are put into a specific gravity sorter via a quantitative feeder, paper, cloth, yarn, etc. are separated, and high purity copper is recovered (step 120). The specific gravity sorter processes a screen using a small-diameter hole punching metal into a staircase shape, and by moving the screen elliptically, it blows air from the bottom of the screen while applying a step-up force to separate light specific gravity paper. Are preferred because they give high copper purity.
The punching metal hole diameter has a great influence on preventing clogging and increasing the purity of copper. Therefore, a sufficient examination is necessary for selection. However, when the diameter is 0.8 mm, clogging is small and the copper purity is 99.9. It is particularly preferable because good results of weight percent or more are obtained.

比重選別機を経由し高純度で回収された銅は、含浸性材料から再付着すると思われるPCB油を基準値以下(「特別管理産業廃棄物に係る基準の検定方法」に示される基準値)まで除去する目的で、2回目の洗浄を行う(工程121)。
2回目の洗浄は、上記(5)の洗浄工程で用いられたものと同様の洗浄方法を用いることによって、搬送容器等に投入された部材は蒸気洗浄、浸漬洗浄、超音波洗浄、真空乾燥が部材毎の適切に設定された時間、自動的かつ効果的に洗浄を行う。また、使用する洗浄剤についても前記と同様のものを使用することができる。
洗浄後の銅は、搬送容器に収容され、管理システムの制御下、自動的に判定洗浄工程107に搬送される。
Copper recovered with high purity via a specific gravity sorter is less than the standard value for PCB oil that is supposed to re-adhere from the impregnating material (standard value indicated in “Standard Test Method for Specially Controlled Industrial Waste”) The second cleaning is performed for the purpose of removing (step 121).
In the second cleaning, the same cleaning method as that used in the cleaning step (5) above is used, so that the members put into the transport container etc. can be subjected to steam cleaning, immersion cleaning, ultrasonic cleaning, and vacuum drying. Cleaning is performed automatically and effectively for an appropriately set time for each member. Moreover, the same thing as the above-mentioned can be used also about the cleaning agent to be used.
The cleaned copper is accommodated in a transfer container and automatically transferred to the determination cleaning step 107 under the control of the management system.

前述の分離された紙8は、紙圧縮機で減容・ブロック化した後、ホッパへ自動搬送機にて搬送・投入し、ドラム充填装置でドラム缶に計量充填を行う(工程126)。   The separated paper 8 is reduced in volume and blocked by a paper compressor, and is then transported and put into a hopper by an automatic transporter, and the drum can is metered and filled by a drum filling device (step 126).

(7)判定洗浄工程107
洗浄後の各部材のうち、容器1、金属2、碍子4、鉄芯板6および銅は、部材毎に判定洗浄工程へ搬送されて判定洗浄され、判定洗浄後、判定待ち保管工程108へ送られる。
判定洗浄工程107では、原液槽が1槽のみから構成される洗浄方法及び装置により、洗浄を行う。判定洗浄で使われる洗浄剤は、上記(5)の洗浄工程や(6)のコア処理工程における銅の二次洗浄に用いられた洗浄剤と同様な洗浄剤を使用することができ、洗浄方法も上記と同様である。
判定洗浄後は洗浄液を分析し(FID(水素炎イオン化検出器)による油分分析またはECD(電子捕獲型検出器)によるPCB分析)、法律基準値以内(「特別管理産業廃棄物に係る基準の検定方法」に示される基準値)であるかどうかを判定する。この判定には、オンライン分析装置(FID式ガスクロマトグラフ、ECD式ガスクロマトグラフ等)を使用することができる。
(7) Determination washing process 107
Of each member after cleaning, the container 1, the metal 2, the insulator 4, the iron core plate 6 and the copper are transported to the determination cleaning step for each member and subjected to determination cleaning, and after the determination cleaning, are sent to the determination waiting storage step 108. It is done.
In the determination cleaning step 107, cleaning is performed by a cleaning method and apparatus in which the stock solution tank is composed of only one tank. The cleaning agent used in the determination cleaning can use the same cleaning agent as the cleaning agent used for the secondary cleaning of copper in the cleaning step (5) and the core processing step (6). Is the same as above.
After the cleaning, the cleaning solution is analyzed (oil analysis by FID (hydrogen flame ionization detector) or PCB analysis by ECD (electron capture detector)) and within legal standard values (“standard test for specially controlled industrial waste” It is determined whether it is the reference value indicated in “Method”. An online analyzer (FID type gas chromatograph, ECD type gas chromatograph, etc.) can be used for this determination.

(8)判定待ち保管工程108
判定洗浄後、判定液はガスクロマトグラフィーなどの分析計で分析するが、分析時間が長いため、結果が出るまでの間搬送の渋滞を防ぐ目的で、判定待ち保管を行う。
洗浄判定の合格・不合格は、「特別管理産業廃棄物に係る基準の検定方法」による判定液法で判定する。
判定待ち保管工程で保管されている各部材は、判定洗浄液の分析結果が合格(0.5mg−PCB/kg−判定液 未満)であれば払出保管工程へ搬送され、保管庫で保管し、傾転装置、パレタイザなどの出荷関連装置でコンテナ・パレット等に収納し随時出荷する。不合格であれば各洗浄装置工程に戻し、洗浄工程以降を繰返し実施する。
なお、判定待ち保管工程の下流側には空気吸い込み口が設けられており、連続的に空気が吸い込まれている。空気の吸い込み量は、各工程の空気清浄度を監視しながら、管理システムの制御下に決定される。吸い込まれた空気は、密閉されたフードを通って、活性炭フィルターを経由し雰囲気循環される。
(8) Judgment waiting storage process 108
After the determination cleaning, the determination liquid is analyzed with an analyzer such as gas chromatography. However, because the analysis time is long, the determination liquid is stored for the purpose of preventing the traffic jam until the result is obtained.
The pass / fail status of the cleaning determination is determined by the determination liquid method according to the “standard verification method for specially controlled industrial waste”.
Each member stored in the judgment waiting storage process is transported to the dispensing storage process if the analysis result of the judgment cleaning liquid is acceptable (less than 0.5 mg-PCB / kg-determination liquid), stored in the storage, and tilted. Stored in containers, pallets, etc. with shipping-related equipment such as rolling equipment and palletizers, and shipped from time to time. If it fails, it returns to each washing | cleaning apparatus process, and repeats after a washing | cleaning process.
Note that an air suction port is provided on the downstream side of the determination waiting storage step, and air is continuously sucked in. The amount of air sucked is determined under the control of the management system while monitoring the air cleanliness of each process. The sucked air passes through the sealed hood and is circulated through the activated carbon filter.

(9)払出・保管工程109
払出・保管工程109では、容器はパレタイザにてパレットに載荷し、払出保管庫へ収納する。
金属2、碍子4、鉄芯板6、銅はバスケット反転装置にて専用コンテナへ部材を入替え、払出保管庫へ収納する。出荷は予約管理システムからの払出指令に基づき、順次払出保管庫から部材・数量等要求に応じて払出し、トラックへ荷積みを行う(工程128)。
紙8、並びに洗浄後の木・パッキン・プレスボード及びその他の部材9は、ホッパへ自動搬送機にて搬送・投入し、ドラム充填装置でドラム缶に計量充填を行う(工程126)。充填後のドラム缶はドラム充填室に設置するドラム缶保管庫に一時保管し、払出予約に従い倉庫へ払出・保管する(工程127)。
(9) Discharge / storage process 109
In the payout / storage process 109, the container is loaded on the pallet by the palletizer and stored in the payout storage.
The metal 2, the insulator 4, the iron core plate 6, and the copper are replaced in a dedicated container by a basket reversing device and stored in a payout storage. In the shipment, based on a delivery command from the reservation management system, the delivery is sequentially delivered from the delivery storage in response to a request for parts, quantities, etc., and loaded onto the truck (step 128).
The paper 8 and the cleaned wood, packing, press board, and other members 9 are transported and loaded into the hopper by an automatic transport machine, and the drum can is metered and filled by the drum filling device (step 126). The filled drum cans are temporarily stored in a drum can storage installed in the drum filling chamber, and are discharged and stored in the warehouse according to a payout reservation (step 127).

(10)排気処理工程
排気処理工程は、前記の解体、コア切断/解体、破砕などの各工程における排気を処理する工程である(図示せず)。排気処理工程としては、前記の解体等の各工程における処理対象物をフード等に収納して、発生する排気をファンで吸引し活性炭処理して施設外へ排気する工程、または洗浄装置のような装置から圧送された排気を活性炭処理する工程などが挙げられる。前者は、排気をファンで吸引することでフード内が負圧に維持され、排気がフード外に漏洩することなく処理することができる。後者は、真空ポンプ等により排気が圧送されるが、気密性の高いダクトに排気を導入することで系外へ排気を漏洩させることなく排気処理することができる。
(10) Exhaust treatment step The exhaust treatment step is a step of treating exhaust in each step such as disassembly, core cutting / disassembly, and crushing (not shown). As the exhaust treatment process, the object to be processed in each process such as the above dismantling is stored in a hood, etc., the generated exhaust is sucked with a fan, activated carbon treatment and exhausted outside the facility, or a cleaning device Examples include a step of treating the exhaust gas pumped from the apparatus with activated carbon. In the former, the inside of the hood is maintained at a negative pressure by sucking the exhaust with a fan, and the exhaust can be processed without leaking outside the hood. In the latter case, the exhaust is pumped by a vacuum pump or the like, but by introducing the exhaust into a highly airtight duct, the exhaust can be processed without leaking out of the system.

上記の工程により、作業員がPCB雰囲気下で作業することなく、PCB混入絶縁油を含有する柱上変圧器を安全に解体し、解体した部品を部材に分別し、各部材をリサイクル資源化することができる。   By the above process, without the operator working in the PCB atmosphere, the pole transformer containing the PCB mixed insulating oil can be safely disassembled, the disassembled parts are separated into members, and each member is recycled. be able to.

以下に、本発明を実施例に基づきさらに詳細に説明するが、本発明はそれらに限定されるものではない。   Hereinafter, the present invention will be described in more detail based on examples, but the present invention is not limited thereto.

PCB含有変圧器をトラックで搬入し、受入装置定位置に載置された空パレットに積載した。この時、変圧器に貼付されたバーコードを専用端末で読取り、管理システムに情報を入力し、与えられた番地の受入保管庫へ移載した。変圧器の移載にあたってはスタッカークレーンを使用した。   The PCB-containing transformer was carried in a truck and loaded on an empty pallet placed at a fixed position of the receiving device. At this time, the bar code affixed to the transformer was read with a dedicated terminal, the information was entered into the management system, and transferred to the receiving storage at the given address. A stacker crane was used to transfer the transformer.

変圧器を受入保管庫から油抜き・解体工程にパレット単位で自動搬送した。パレットからジブクレーンを使用して、変圧器一台を解体コンベヤに移載した。コンベヤは各作業ステーションのフットスイッチ等によって一ポジション移動し、持ち場の作業員によって、以下の作業が順次行われた。なお、以下の解体作業は、柱上変圧器に使用された絶縁油のPCB濃度が低く人体に影響がないため、作業員の手作業により行った。   The transformer was automatically transported from the receiving storage to the oil draining and dismantling process in units of pallets. One transformer was transferred from the pallet to the dismantling conveyor using a jib crane. The conveyor was moved to one position by a foot switch at each work station, and the following operations were sequentially performed by workers in the workplace. The following dismantling work was performed manually by workers because the PCB concentration of the insulating oil used in the pole transformer is low and does not affect the human body.

まず、変圧器蓋固定ねじを緩め、蓋を取り除いた。蓋は、取り付けられたパッキンを取り外し、部材毎にバスケットに分別投入した。次に、ヒール油抜出ポンプノズルを挿入し、油抜き作業を行った。油抜きされたPCB油は蒸留再生装置によって分離された絶縁油とともに、工程内のタンクで一時保管し、PCB油処理工程の要求によりポンプ等で移送し、移送先の処理工程で分解処理し、無害化した。
油抜きが終了した時点で、ケースを貫通する一次、二次それぞれの電線を切断した。電線用一次、二次の碍子を固定しているビスやスプリング等を取り外し、碍子をケースから取り外し、部材毎に識別番号の付与されたバスケットへ投入した。
First, the transformer lid fixing screw was loosened and the lid was removed. The lid was removed from the attached packing, and each member was put into the basket separately. Next, the heel oil extraction pump nozzle was inserted to perform the oil removal operation. The drained PCB oil is temporarily stored in the tank in the process together with the insulating oil separated by the distillation regenerator, transferred by a pump or the like according to the demand of the PCB oil processing process, and decomposed in the processing process of the transfer destination. Made harmless.
When oil draining was completed, the primary and secondary electric wires penetrating the case were cut. The screws and springs fixing the primary and secondary insulators for electric wires were removed, the insulators were removed from the case, and the members were put into baskets assigned identification numbers.

内容物をケースに固定しているボルトを緩め取り外し、ボルトを金属バスケットへ投入した。内容物の固定バンド、ビス、電線等を切断又は取り外し、コアから部材取付架台を取り外した。この架台にはタップ台や耐電素子その他の部品も取り付いているため、金属、耐雷素子、碍子、電線、コア、木・プレスボードその他の部材単位まで分解し、それぞれをバスケットに投入した。   The bolts fixing the contents to the case were loosened and removed, and the bolts were put into a metal basket. The fixing band, screws, electric wires, etc. of the contents were cut or removed, and the member mounting base was removed from the core. Since this base also has tapping bases, electric resistance elements, and other parts, they were disassembled into metal, lightning resistance elements, insulators, electric wires, cores, wood, press boards, and other parts, and each was put into a basket.

耐雷素子は耐雷素子を構成する碍子等を取り外した後、素子を内包する金属容器を解体し、さらにセラミックの素子と金属部品までに分解し、それぞれのバスケットへ投入した。また、エポキシ樹脂等で碍子に固定されている電線を碍子から分別し、それぞれのバスケットへ投入した。
ここで残った部材は容器及びコアとなり、容器を容器用バスケットに移載し、コアを鉄芯/コイル分離装置へ搬送した。
容器、金属、碍子、電線、並びに木・パッキン・プレスボード及びその他の部材を投入したバスケットをベルトコンベアで洗浄装置へ搬送した。
解体分別された各部材の搬送・移載は、識別番号を付与したバスケット単位で行われ、PCB蒸気の外部への発散や雰囲気汚染を防止するため、開口部は全てフードで囲っておいた。
For the lightning protection element, the insulator constituting the lightning protection element was removed, the metal container containing the element was disassembled, further disassembled into ceramic elements and metal parts, and put into each basket. In addition, the electric wires fixed to the insulators with epoxy resin or the like were separated from the insulators and put into the respective baskets.
The remaining members here became a container and a core, the container was transferred to a container basket, and the core was transported to an iron core / coil separation device.
Containers, metal, insulators, electric wires, and baskets filled with wood, packing, press board, and other members were conveyed to a cleaning device by a belt conveyor.
Each member separated and disassembled is transported and transferred in a basket unit with an identification number, and all openings are surrounded by a hood to prevent the release of PCB vapor to the outside and atmospheric contamination.

バスケットに投入された容器、金属、碍子、電線、並びに木・パッキン・プレスボード及びその他の部材について洗浄を行った。容器については、浸漬洗浄1を3分、浸漬洗浄2を3分、蒸気洗浄を10分、真空乾燥を6分行った。金属については、浸漬洗浄1を8分、浸漬洗浄2を8分、蒸気洗浄を16分、真空乾燥を9分行った。碍子については、浸漬洗浄1を8分、浸漬洗浄2を8分、蒸気洗浄を16分、真空乾燥を9分行った。電線については、浸漬洗浄1を8分、浸漬洗浄2を8分、蒸気洗浄を16分、真空乾燥を9分行った。木・パッキン・プレスボード及びその他の部材については浸漬洗浄1を3分、浸漬洗浄2を3分、蒸気洗浄を10分、真空乾燥を6分行った。各洗浄において洗浄剤はNS200P(商品名、日鉱石油化学株式会社製)を用いた。洗浄後の容器、金属、碍子は、判定洗浄工程へ搬送した。洗浄後の電線は、後述する洗浄後のコイルと共に破砕するために、コイル破砕工程に搬送した。   The container, metal, insulator, electric wire, and wood / packing / press board and other members placed in the basket were cleaned. The container was subjected to immersion cleaning 1 for 3 minutes, immersion cleaning 2 for 3 minutes, steam cleaning for 10 minutes, and vacuum drying for 6 minutes. For the metal, immersion cleaning 1 was performed for 8 minutes, immersion cleaning 2 was performed for 8 minutes, steam cleaning was performed for 16 minutes, and vacuum drying was performed for 9 minutes. For the insulator, immersion cleaning 1 was performed for 8 minutes, immersion cleaning 2 was performed for 8 minutes, steam cleaning was performed for 16 minutes, and vacuum drying was performed for 9 minutes. The electric wire was subjected to immersion cleaning 1 for 8 minutes, immersion cleaning 2 for 8 minutes, steam cleaning for 16 minutes, and vacuum drying for 9 minutes. For wood, packing, press board and other members, immersion cleaning 1 was performed for 3 minutes, immersion cleaning 2 was performed for 3 minutes, steam cleaning was performed for 10 minutes, and vacuum drying was performed for 6 minutes. In each cleaning, NS200P (trade name, manufactured by Nikko Petrochemical Co., Ltd.) was used as the cleaning agent. The container, metal, and insulator after cleaning were transported to the determination cleaning process. The washed electric wire was conveyed to a coil crushing step in order to crush it together with the washed coil described later.

コアは0.3mm程度の薄板珪素鋼板が多数枚積層された鉄芯と、絶縁紙やオイルダクト(割り箸様の木、波板等)を挟んで巻回された、一次・二次の巻線(銅線:絶縁紙、オイルダクト、巻線から構成されるものをコイルと呼称する)とが相互に鎖状に組み合わされて構成されている。コアを解体するために、コイルを切断した。   The core is a primary / secondary winding wound around an iron core in which a large number of thin silicon steel sheets with a thickness of about 0.3 mm are laminated and insulating paper or oil ducts (wooden chopstick-like wood, corrugated sheet, etc.) (Copper wire: what consists of insulating paper, an oil duct, and a coil | winding is called a coil) and it is comprised by combining in a chain form mutually. In order to disassemble the core, the coil was cut.

解体分別された鉄芯を油圧切断歯で切断し、一鉄芯を半割2個とした。半割鉄芯は一個ずつ、湾曲矯正装置でほぼ直線状に矯正した。矯正後の鉄芯を一度に50〜60枚(厚さ:20mm)程度ずつ作業員がプレス台にセットし、押し釦を押してプレス型を油圧で押し下げ、鉄芯を長手方向に並行にV字プレスした。得られた鉄芯板を鉄板分離機により洗浄バスケットに投入し、ベルトコンベアで洗浄装置へ搬送した。   The disassembled and separated iron core was cut with hydraulic cutting teeth, and one iron core was divided into two halves. One half of each iron core was straightened with a straightening device. About 50 to 60 sheets of iron core after correction (thickness: 20 mm) are set on the press stand by an operator, the press button is pressed to press the press die down hydraulically, and the iron core is V-shaped in parallel with the longitudinal direction. Pressed. The obtained iron core plate was put into a washing basket by an iron plate separator and conveyed to a washing device by a belt conveyor.

鉄芯板について、「特別管理産業廃棄物に係る基準の検定方法」の基準値(洗浄液試験法:洗浄液PCB濃度0.5mg/kg以下、拭き取り試験法:PCB付着量0.1μg/100cm2以下、部材採取試験法:PCB付着量0.01mg/kg以下)を満足するように洗浄を行った。 For iron core plates, the standard values of “Standard Test Methods for Specially Controlled Industrial Waste” (cleaning solution test method: cleaning solution PCB concentration 0.5 mg / kg or less, wiping test method: PCB adhesion amount 0.1 μg / 100 cm 2 or less In addition, cleaning was performed so as to satisfy the member sampling test method: PCB adhesion amount of 0.01 mg / kg or less.

洗浄機では、先ず第1原液(NS200P)を蒸発器に導入し、10kPaの減圧下で溶剤(NS200P)を、熱交換器によってスチームで130℃に加熱することによって、溶剤を低温で沸騰させ、溶剤蒸気を継続的に発生させ、これを配管によって洗浄槽に導入し、鉄芯板を減圧蒸気洗浄した。引き続き、超音波洗浄を併用した減圧浸漬洗浄を行った。10kPaに減圧した状態で脱気超音波洗浄を行い、鉄芯板を高速で10分間振動させた。   In the washing machine, first, the first stock solution (NS200P) is introduced into the evaporator, and the solvent (NS200P) is heated to 130 ° C. by steam with a heat exchanger under a reduced pressure of 10 kPa. Solvent vapor was continuously generated and introduced into a washing tank by piping, and the iron core plate was subjected to vacuum steam washing. Subsequently, vacuum immersion cleaning combined with ultrasonic cleaning was performed. Deaeration ultrasonic cleaning was performed in a state where the pressure was reduced to 10 kPa, and the iron core plate was vibrated at high speed for 10 minutes.

第1原液による浸漬洗浄の後、より清浄な第2原液(NS200P)により、リンス洗浄を行った。この洗浄の条件は上記の減圧浸漬洗浄と同様である。第2原液による浸漬洗浄後、洗浄液を原液タンクに戻し、洗浄槽を空状態にした後、第2原液を蒸発器に導入し、蒸気洗浄を行い鉄芯板、洗浄槽壁、付着液体を約120℃まで加熱し、10分間保持した。この時、洗浄槽内は60〜100Torr(7999〜13332Pa)程度とした。
蒸気洗浄が終了した後は、真空ポンプの入口弁を開放し、真空吸引することによって槽内真空度を高め、表面付着液体を過飽和状態にして再蒸発させ、鉄芯板、バスケット、槽内壁等を乾燥させ、板状体洗浄を終了した。洗浄後の鉄芯板は、判定洗浄工程へ搬送した。
After immersion cleaning with the first stock solution, rinse cleaning was performed with a cleaner second stock solution (NS200P). The conditions for this cleaning are the same as in the above-described vacuum immersion cleaning. After immersion cleaning with the second stock solution, return the cleaning solution to the stock solution tank, empty the cleaning tank, introduce the second stock solution into the evaporator, perform steam cleaning, and remove the iron core plate, cleaning tank wall, and attached liquid. Heat to 120 ° C. and hold for 10 minutes. At this time, the inside of the cleaning tank was set to about 60 to 100 Torr (7999 to 13332 Pa).
After completion of steam cleaning, open the inlet valve of the vacuum pump and increase the vacuum in the tank by vacuuming, re-evaporate the surface adhering liquid by supersaturation, iron core plate, basket, tank inner wall, etc. Was dried to finish washing the plate-like body. The iron core plate after washing was conveyed to the judgment washing process.

解体分別されたコイルは、作業場で手作業によって、オイルダクトを分別した。コイルについて、浸漬洗浄1を12分、浸漬洗浄2を12分、蒸気洗浄を12分、真空乾燥を10分行った。洗浄剤にはNS200P(商品名、日鉱石油化学株式会社製)を用いた。   The disassembled and separated coils were manually separated from the oil duct at the work site. The coil was subjected to immersion cleaning 1 for 12 minutes, immersion cleaning 2 for 12 minutes, steam cleaning for 12 minutes, and vacuum drying for 10 minutes. NS200P (trade name, manufactured by Nikko Petrochemical Co., Ltd.) was used as the cleaning agent.

洗浄・乾燥後のコイルを破砕機で破砕し、同時に、一次・二次側導体を覆っている絶縁被覆、紙テープ等を剥離した。破砕機は、二軸破砕機、一軸破砕機、高速破砕機の三段を組み合せた。一軸破砕機でのスクリーン径は20〜50mmとし、最終段の高速破砕機ではスクリーン径を7〜8mmとした。
破砕後のコイル砕片を、定量フィーダーを経由して、比重選別機に投入した。比重選別機は細径穴パンチングメタルを使用したスクリーンを階段状に加工し、このスクリーンを楕円運動させることによって、昇段力を付与しながらスクリーン下側から送風し、軽比重の紙・布・糸類を銅から分離した。パンチングメタル穴径は直径0.8mmとした。
The coil after washing and drying was crushed with a crusher, and at the same time, the insulation coating and paper tape covering the primary and secondary conductors were peeled off. The crusher was a combination of three stages: a twin-screw crusher, a single-screw crusher, and a high-speed crusher. The screen diameter in the uniaxial crusher was 20 to 50 mm, and the screen diameter was 7 to 8 mm in the final stage high-speed crusher.
The crushed coil fragments were put into a specific gravity sorter via a quantitative feeder. The specific gravity sorter processes a screen using small-diameter punched metal into a staircase shape, and this screen is elliptically moved to blow air from the bottom of the screen while applying a step-up force. Were separated from copper. The punching metal hole diameter was 0.8 mm.

比重選別機により分離回収された銅について二次洗浄を行った。二次洗浄は、浸漬洗浄1を10分、蒸気洗浄を11分、真空乾燥を10分行った。洗浄剤にはNS200P(商品名、日鉱石油化学株式会社製)を用いた。洗浄後の銅は、判定洗浄工程へ搬送した。   The copper separated and collected by the specific gravity sorter was subjected to secondary washing. In the secondary cleaning, immersion cleaning 1 was performed for 10 minutes, steam cleaning was performed for 11 minutes, and vacuum drying was performed for 10 minutes. NS200P (trade name, manufactured by Nikko Petrochemical Co., Ltd.) was used as the cleaning agent. The copper after washing was transported to the judgment washing process.

破砕され比重選別機で分離された紙・布・糸類、並びに洗浄工程の終了した木・パッキン・プレスボード及びその他の部材については、ドラム缶に充填し易いように圧縮装置でブロック状に圧縮減容し、ベルトコンベアにてホッパへ搬送・投入し、ドラム充填装置でドラム缶に計量充填した。   Paper, cloth, and threads that have been crushed and separated by a specific gravity sorter, as well as wood, packing, pressboard, and other components that have been cleaned are compressed into blocks using a compression device so that drums can be filled easily. Then, it was transferred to the hopper by a belt conveyor and charged into a drum can with a drum filling device.

洗浄後の容器、金属、碍子、鉄芯板および銅について判定洗浄を行った。判定洗浄は、原液槽が1槽のみから構成される。洗浄は浸漬洗浄を10分、蒸気洗浄を10分、真空乾燥を10分行った。   The container, metal, insulator, iron core plate and copper after washing were subjected to judgment washing. In the determination cleaning, the stock solution tank is composed of only one tank. Cleaning was performed by immersion cleaning for 10 minutes, steam cleaning for 10 minutes, and vacuum drying for 10 minutes.

判定洗浄後、判定液を採取し、電子捕獲型ガスクロマトグラフ分析装置(GC17A、商品名、島津製作所製)により分析を行った。0.5mg−PCB/kg−判定液 未満であれば合格とした。結果が出るまでの間、各部材は判定待ち保管工程へ搬送した。分析の結果、判定洗浄液のPCB濃度は、0.1mg−PCB/kg−判定液 未満であり合格であった。部材毎に判定待ち保管工程から払出保管工程へ搬送した。この工程では、変圧器容器はパレタイザにてパレットに載荷し、払出保管庫へ収納した。金属、碍子、鉄芯板、銅はバスケット反転装置にて専用コンテナへ部材を入替え、払出保管庫へ収納した。出荷は予約管理システムからの払出指令に基づき、順次払出保管庫から部材・数量等要求に応じて払出し、トラックへ荷積みを行った。   After the determination cleaning, the determination liquid was collected and analyzed with an electron capture gas chromatograph analyzer (GC17A, trade name, manufactured by Shimadzu Corporation). If it was less than 0.5 mg-PCB / kg-determination solution, it was judged as acceptable. Until the result was obtained, each member was transported to the determination waiting storage process. As a result of the analysis, the PCB concentration of the judgment washing liquid was less than 0.1 mg-PCB / kg-judgment liquid and passed. Each member was transferred from the waiting-for-determination storage process to the payout storage process. In this process, the transformer container was loaded on a pallet with a palletizer and stored in a dispensing storage. Metals, insulators, iron core plates, and copper were replaced by a basket reversing device with special members and stored in a payout storage. Shipments were sequentially paid out from the payout storage in response to requests for parts, quantities, etc., and loaded onto trucks based on the payout command from the reservation management system.

図1は、本発明の好ましい一実施態様のフローチャート図である。FIG. 1 is a flow chart diagram of a preferred embodiment of the present invention. 図2(a)は柱上変圧器の一部切欠平面図であり、図2(b)は柱上変圧器の一部切欠正面図であり、図2(c)は柱上変圧器の一部切欠側面図である。2 (a) is a partially cutaway plan view of a pole transformer, FIG. 2 (b) is a partially cutaway front view of the pole transformer, and FIG. 2 (c) is one of the pole transformers. It is a part notch side view.

符号の説明Explanation of symbols

1 ケース
2 金属
3 耐雷素子
4 碍子
5 電線
6 鉄芯
7 コイル
8 紙
9 木・パッキン・プレスボード及びその他の部材
10 PCB混入絶縁油
104 油抜き・解体工程
105 洗浄工程
106 コア処理工程
107 判定洗浄工程
111 耐雷素子解体工程
112 碍子解体工程
113 鉄芯切断工程
114 鉄芯湾曲矯正工程
115 V字プレス工程
116 鉄芯板洗浄工程
117 木除去工程
118 一次洗浄工程
119 破砕工程
120 比重選別工程
121 二次洗浄工程
122 破砕工程
123 洗浄工程
124 破砕工程
125 洗浄工程
DESCRIPTION OF SYMBOLS 1 Case 2 Metal 3 Lightning protection element 4 Insulator 5 Electric wire 6 Iron core 7 Coil 8 Paper 9 Wood, packing, press board, and other members 10 Insulating oil mixed with PCB 104 Oil removal / disassembly process 105 Cleaning process 106 Core processing process 107 Determination cleaning Process 111 Lightning protection element disassembly process 112 Insulator disassembly process 113 Iron core cutting process 114 Iron core curving correction process 115 V-shaped press process 116 Iron core plate cleaning process 117 Wood removal process 118 Primary cleaning process 119 Crushing process 120 Specific gravity sorting process 121 Secondary Cleaning process 122 Crushing process 123 Cleaning process 124 Crushing process 125 Cleaning process

Claims (7)

PCB混入絶縁油を含有する柱上変圧器を分別解体し、多段洗浄により各部材を無害化して再資源化する柱上変圧器の無害化処理方法であって、
(a)PCB混入絶縁油を含有する柱上変圧器からPCB混入絶縁油を油抜きする工程、
(b)前記柱上変圧器を、ケース、金属、耐雷素子、碍子、電線、コア、及びその他の部材にそれぞれ分別解体する工程、
(c)前記コアを、さらに鉄芯とコイルに分別解体する工程、
(d)前記の解体した各部材をそれぞれ、一次洗浄し、二次洗浄し、乾燥する工程、
(e)前記の各部材を適宜分別して減容する工程、
(f)前記の洗浄後の各部材を判定洗浄する工程
を含んでなることを特徴とする柱上変圧器の無害化処理方法。
It is a detoxification method for a pole transformer that separates and dismantles pole transformers containing PCB-mixed insulating oil, detoxifies each member by multi-stage cleaning, and recycles them.
(A) A step of draining the PCB mixed insulating oil from the pole transformer containing the PCB mixed insulating oil,
(B) a step of separating and disassembling the pole transformer into a case, a metal, a lightning protection element, an insulator, an electric wire, a core, and other members,
(C) a step of further separating and disassembling the core into an iron core and a coil;
(D) Steps of primary cleaning, secondary cleaning, and drying of each of the disassembled members,
(E) a step of appropriately separating and reducing the volume of each member described above,
(F) A method for detoxifying a pole transformer, comprising a step of determining and cleaning each member after the cleaning.
PCB混入絶縁油を含有する柱上変圧器を分別解体し、各部材を無害化して再資源化する柱上変圧器の無害化処理方法であって、
(a)PCB混入絶縁油を含有する柱上変圧器からPCB混入絶縁油を油抜きする工程、
(b)前記柱上変圧器を、ケース、金属、耐雷素子、碍子、電線、コア、並びに木・パッキン・プレスボード及びその他の部材に分別解体する工程、
(c)前記耐雷素子をさらに金属、並びに碍子および素子に分別解体する工程、
(d)前記碍子をさらに碍子部品と電線に分別解体する工程、
(e)前記コアの巻線を切断して、さらに鉄芯とコイルに分別解体する工程、
(f)前記鉄芯を切断し、鉄芯湾曲矯正をしてからV字プレス処理し、得られた鉄芯板を洗浄装置にて洗浄する工程、
(g)前記コイルから木を除去した後に、該コイルを洗浄装置にて洗浄し、破砕して、比重選別機により銅と紙に分別し、銅を洗浄装置にて二次洗浄し、紙を圧縮して減容する工程、
(h)前記のケース、金属、碍子、電線、並びに木・パッキン・プレスボード及びその他の部材をそれぞれ洗浄装置にて洗浄する工程、
(i)前記の洗浄後のケース、金属、碍子、鉄芯板および銅を、部材毎に洗浄装置にて判定洗浄する工程
を含んでなることを特徴とする柱上変圧器の無害化処理方法。
It is a detoxification processing method for a pole transformer that separates and dismantles pole transformers containing insulating oil mixed with PCB, renders each member harmless and recycles,
(A) A step of draining the PCB mixed insulating oil from the pole transformer containing the PCB mixed insulating oil,
(B) a step of separating and disassembling the pole transformer into a case, metal, lightning protection element, insulator, electric wire, core, and wood, packing, press board, and other members;
(C) a step of separating and disassembling the lightning-resistant element into metal and insulators and elements;
(D) a step of further separating and separating the insulator into an insulator part and an electric wire;
(E) cutting the winding of the core and further separating and disassembling into an iron core and a coil;
(F) cutting the iron core, correcting the iron core curvature, performing a V-shaped press treatment, and cleaning the obtained iron core plate with a cleaning device;
(G) After removing the wood from the coil, the coil is washed with a washing device, crushed, separated into copper and paper with a specific gravity sorter, and the copper is secondarily washed with the washing device, Compressing and reducing the volume,
(H) a step of cleaning the case, metal, insulator, electric wire, wood, packing, press board and other members with a cleaning device,
(I) A method for detoxifying a pole transformer, comprising a step of determining and cleaning the cleaned case, metal, insulator, iron core plate, and copper with a cleaning device for each member. .
前記の各部材を、識別子が付与された搬送容器に各部材毎に収納し、搬送容器に付与された識別子の情報と管理システムの処理予約登録とを照合し、前記の各工程間または各処理間を自動搬送機により搬送することを特徴とする請求項1又は2に記載の柱上変圧器の無害化処理方法。   Each of the above members is stored for each member in a transport container to which an identifier has been assigned, and the identifier information given to the transport container is checked against the processing reservation registration of the management system. 3. The method for detoxifying a pole transformer according to claim 1 or 2, wherein the gap is conveyed by an automatic conveyor. 前記の各洗浄工程において、第2石油類又は第3石油類の炭化水素系洗浄剤や有機溶剤を使用して洗浄を行い、使用後の洗浄剤を蒸留再生装置により浄化してPCB混入絶縁油を分離回収し、洗浄剤を繰返し使用することを特徴とする請求項1〜3のいずれか1項に記載の柱上変圧器の無害化処理方法。   In each of the above-described cleaning steps, cleaning is performed using a hydrocarbon-based cleaning agent or an organic solvent of the second petroleum or the third petroleum, and the used cleaning agent is purified by a distillation regenerator, and the PCB mixed insulating oil The method for detoxifying a pole transformer according to any one of claims 1 to 3, wherein the cleaning agent is repeatedly used. 前記の各工程に用いられる各処理装置の開口部をフードで囲い、フード内を負圧吸引し、活性炭フィルターを経由して雰囲気循環することを特徴とする請求項1〜4のいずれか1項に記載の柱上変圧器の無害化処理方法。   The opening part of each processing apparatus used for each said process is enclosed with a hood, the inside of the hood is sucked under negative pressure, and the atmosphere is circulated through an activated carbon filter. Detoxification method for pole transformers described in 1. 前記の各工程のうち排気が発生する工程において、凝縮装置、局所排気吸引装置及び活性炭フィルターを用いて、PCB蒸気含有量を環境規制値未満の濃度に低減して排気することを特徴とする請求項1〜5のいずれか1項に記載の柱上変圧器の無害化処理方法。   The step of generating exhaust gas among the above steps is characterized in that the PCB vapor content is reduced to a concentration lower than the environmental regulation value by using a condenser, a local exhaust suction device and an activated carbon filter, and exhausted. Item 6. The method for detoxifying a pole transformer according to any one of Items 1 to 5. 前記の洗浄装置または蒸留再生装置が、PCB漏洩検知装置およびオイルパンを備え、該各装置を減圧下にて運転することを特徴とする請求項1〜6のいずれか1項に記載の柱上変圧器の無害化処理方法。
The above-mentioned washing device or distillation reproduction device is provided with a PCB leak detection device and an oil pan, and each of these devices is operated under reduced pressure, The column top according to any one of claims 1 to 6 Transformer detoxification method.
JP2005115145A 2005-04-12 2005-04-12 Method for detoxifying pole-mounted transformer including pcb-mixed insulating oil Pending JP2006289288A (en)

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KR101020165B1 (en) 2008-07-08 2011-03-07 학산금속공업 주식회사 disjointing method and the apparatus of wastetransformer
JP2013220415A (en) * 2012-04-19 2013-10-28 Dowa Eco-System Co Ltd Device and method for disassembling transformer core
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