JP2008229473A - Method of removing pcb in trace pcb contaminated electric equipment - Google Patents
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- JP2008229473A JP2008229473A JP2007071888A JP2007071888A JP2008229473A JP 2008229473 A JP2008229473 A JP 2008229473A JP 2007071888 A JP2007071888 A JP 2007071888A JP 2007071888 A JP2007071888 A JP 2007071888A JP 2008229473 A JP2008229473 A JP 2008229473A
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- 238000000034 method Methods 0.000 title claims abstract description 61
- 239000002904 solvent Substances 0.000 claims abstract description 56
- 238000004140 cleaning Methods 0.000 claims abstract description 42
- 238000011282 treatment Methods 0.000 claims abstract description 30
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 8
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 8
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 8
- 238000012545 processing Methods 0.000 claims description 31
- 150000003071 polychlorinated biphenyls Chemical class 0.000 claims description 14
- 238000011109 contamination Methods 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 8
- 238000005406 washing Methods 0.000 claims description 8
- 238000010828 elution Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 238000012360 testing method Methods 0.000 claims description 4
- 238000004090 dissolution Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 238000009835 boiling Methods 0.000 claims description 2
- 239000012466 permeate Substances 0.000 claims description 2
- 238000000926 separation method Methods 0.000 claims 1
- 239000003921 oil Substances 0.000 description 87
- 238000003860 storage Methods 0.000 description 10
- 238000005516 engineering process Methods 0.000 description 6
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- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
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- 238000005202 decontamination Methods 0.000 description 3
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- 229910052751 metal Inorganic materials 0.000 description 3
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
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- 238000004821 distillation Methods 0.000 description 2
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- 238000011160 research Methods 0.000 description 2
- 229920002545 silicone oil Polymers 0.000 description 2
- 238000012795 verification Methods 0.000 description 2
- FPWNLURCHDRMHC-UHFFFAOYSA-N 4-chlorobiphenyl Chemical compound C1=CC(Cl)=CC=C1C1=CC=CC=C1 FPWNLURCHDRMHC-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000006298 dechlorination reaction Methods 0.000 description 1
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- 239000000295 fuel oil Substances 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
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- 239000002023 wood Substances 0.000 description 1
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/82—Recycling of waste of electrical or electronic equipment [WEEE]
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- Cleaning By Liquid Or Steam (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
本発明は、PCBを含む絶縁油が充填されたPCB汚染電気機器を、解体しないで電気機器内部を洗浄しPCBを除去するPCB除去方法に関する。 The present invention relates to a PCB removal method for removing a PCB by cleaning the inside of the electrical device without disassembling a PCB-contaminated electrical device filled with insulating oil containing PCB.
平成13年に「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」が施行され、PCB及びPCBに汚染された変圧器、コンデンサなどのPCB汚染物は、平成28年までに無害化処理することとなっている。 In 2001, the “Special Measures Law for Promotion of Proper Treatment of Polychlorinated Biphenyl Waste” was enacted, and PCB contaminants such as transformers and capacitors contaminated by PCB and PCB were made harmless by 2016 It is supposed to be processed.
現在、平成28年までの処理完了に向けて、PCB及びPCB汚染物を無害化処理するための広域処理施設が、全国5ケ所に建設あるいは計画され、一部の施設は既に運転している。 At present, wide-area treatment facilities for detoxifying PCBs and PCB contaminants have been constructed or planned in five locations nationwide, and some facilities are already in operation, with the aim of completing the treatment by 2016.
これら広域処理施設で処理されるPCB及びPCB汚染物は、昭和47年までに生産が中止され、昭和49年までに製造・輸入、新規使用が禁じられたもので、それ以降、長期にわたり保管されていた高濃度PCB及び高濃度PCB入り変圧器あるいはコンデンサなどが対象である。 PCBs and PCB contaminants that are processed at these wide-area treatment facilities were discontinued by 1972 and were prohibited from being manufactured, imported, or used by 1979, and have been stored for a long time since then. The high-concentration PCB, the high-concentration PCB-containing transformer or the capacitor, and the like are the objects.
また、その無害化処理技術も、PCBについては金属ナトリウムやアルカリを用いた脱塩素による化学処理などで、PCB汚染物については洗浄法あるいは真空加熱法でのPCBを除去する技術が確立しており、広域処理施設での主たる無害化処理技術として採用されている。 In addition, the detoxification treatment technology has been established for PCBs, such as chemical treatment by dechlorination using metallic sodium or alkali, and for PCB contaminants, technology for removing PCBs by the cleaning method or vacuum heating method has been established. It has been adopted as the main detoxification technology in wide-area treatment facilities.
一方、平成14年7月に経産省と環境省から(社)日本電機工業会(以下、JEMAという)に対して、「新油を使用した変圧器などへの微量PCBの混入可能性」について原因究明と機器特定について調査を指示した旨のプレス発表があり、変圧器などの油入電気機器の絶縁油中に微量のPCBが何らかの原因で混入している電気機器などがあることが判った。 On the other hand, the Ministry of Economy, Trade and Industry and the Japan Electrical Manufacturers' Association (hereinafter referred to as JEMA) announced in July 2002 that “the possibility of mixing a small amount of PCB into transformers using new oil” There was a press announcement stating that the investigation of the cause and the identification of the equipment were instructed, and it was found that there was an electrical equipment in which a small amount of PCB was mixed for some reason in the insulating oil of oil-filled electrical equipment such as transformer It was.
JEMAなどの調査によると、0.5〜数十ppmレベルの微量PCBが混入しているPCB汚染電気機器は非常に広範囲に及んでおり、一説では、大容量の変圧器も含んで百万台近くあると推定されている。 According to research by JEMA and others, PCB-contaminated electrical equipment mixed with trace amounts of PCBs in the 0.5 to tens of ppm level is extremely widespread, and one theory includes millions of units including large-capacity transformers. Estimated to be close.
この問題に対して、現在、有識者による国レベルでの「低濃度PCB汚染物対策検討委員会」が設置され、この委員会で原因究明、対策などについて議論がなされており、処理の方向性が打ち出される予定である。 In response to this problem, the “Low-Concentration PCB Contamination Countermeasures Review Committee” has been established at the national level by experts, and the investigation of the cause and countermeasures have been discussed in this committee. It will be launched.
しかしながら、このような、絶縁油中に微量のPCBが何らかの原因で混入したPCB汚染電気機器などは、高濃度PCB及び高濃度PCB入りの変圧器あるいはコンデンサなどを対象とした広域処理施設で処理することを想定していない。このため、微量のPCBが混入したPCB汚染電気機器についての広域処理施設での処理は、主に処理能力あるいは経済性の観点から困難で、我が国としての処理技術を確立することが急務となっている。 However, such PCB-contaminated electrical equipment in which a small amount of PCB is mixed in insulating oil for some reason is processed in a wide-area processing facility for high-concentration PCB and transformers or capacitors containing high-concentration PCB. I do not assume that. For this reason, it is difficult to process PCB contaminated electrical equipment mixed with a small amount of PCB in a wide-area processing facility mainly from the viewpoint of processing capacity or economy, and it is an urgent task to establish processing technology in Japan. Yes.
このような、PCBを含む絶縁油が充填されたPCB汚染変圧器の処理についての、カナダ、米国における代表例を以下に述べる。 A typical example in Canada and the United States regarding the treatment of such a PCB contaminated transformer filled with insulating oil containing PCB will be described below.
例えば、非特許文献1は、MOF除染法(Ontario Ministry of Environment)(オンタリオ環境庁の方法)についての記述があり、その概略内容は、PCBを含む絶縁油を抜いた後、「No.2燃料油」あるいは「トリクロロエチレン」などの洗浄溶剤を満たして浸漬放置し、その後に洗浄溶剤を抜取り、きれいな洗浄溶剤を満たして除染する工程を繰返すものである。 For example, Non-Patent Document 1 describes the MOF decontamination method (Ontario Ministry of Environment) (method of the Ontario Environment Agency). The outline of the method is “No. 2” after removing the insulating oil containing PCB. This is a process in which a cleaning solvent such as “fuel oil” or “trichlorethylene” is filled and allowed to stand for immersion, and then the cleaning solvent is removed, followed by a clean cleaning solvent and decontamination.
また、非特許文献2では、PCB汚染変圧器の処理には洗浄溶剤(絶縁油も兼ねる)によるレトロフィル(逆充填)が望ましいとされ、PCB汚染変圧器のフラッシングと洗浄溶剤回収とを組み合わせた自動化システムが適用されている。
Further, in
また、特殊な洗浄溶剤(絶縁油も兼ねる)で変圧器内をフラッシングしつつ、洗浄溶剤を取り換えて変圧器を活かす方法も適用されており、最終的にはシリコーン油で置換する。このレトロフィルによって、PCB代替油(主にシリコーン油が使用されている。)中のPCB濃度は、50ppm以下に再分類される(米国におけるPCB規制値:50ppm以上)。 In addition, there is a method in which the transformer is used by flushing the inside of the transformer with a special cleaning solvent (also serving as insulating oil), and finally the replacement with silicone oil. By this retrofill, the PCB concentration in the PCB alternative oil (mainly silicone oil is used) is reclassified to 50 ppm or less (PCB regulation value in the United States: 50 ppm or more).
このように、処理をして再使用する場合には、変圧器を解体しないため、分析可能なものは液サンプルのみとなる。変圧器は、多種の部材による複雑な組立構成物であるため、全ての部材から一様にPCBを溶出することは難しく、溶出処理を重ねる毎に部材間のバラツキは大きくなってくる。 In this way, when processing and reusing, the transformer is not disassembled, so that only the liquid sample can be analyzed. Since the transformer is a complicated assembly structure composed of various members, it is difficult to elute PCBs uniformly from all the members, and the variation between the members increases with each elution process.
処理直後には、この部材間のバラツキが顕著であるため、液を分析してもPCBが検出されず、部材の中に残っているという状態が起こる。このため、アメリカでは、処理後3ヶ月経過してから測定した値についての基準を設けている。
我が国において広域処理施設での処理が困難である事情を勘案すると、上記した海外の「現地において解体しないで洗浄する」技術は、基本的にわが国における処理技術の指針となるものである。 Considering the fact that processing in a wide-area processing facility is difficult in Japan, the above-mentioned overseas “cleaning without dismantling on site” basically serves as a guideline for processing technology in Japan.
本発明は上述の点を考慮してなされたものであり、電気機器中のPCBを溶剤に抽出して除去するにつき、機器の内部状態を把握しながら安全かつ経済的に除去処理を進めることができる微量PCB汚染電気機器のPCB除去方法を提供することを目的とする。 The present invention has been made in consideration of the above-mentioned points, and when extracting and removing PCBs in electrical equipment as a solvent, it is possible to proceed with the removal process safely and economically while grasping the internal state of the equipment. An object of the present invention is to provide a PCB removal method for a small amount of PCB-contaminated electrical equipment.
上記目的達成のため、本発明では、
PCBを含む絶縁油が充填された電気機器から前記絶縁油を抜取った後、炭化水素系溶剤を注入して、この炭化水素系溶剤に前記電気機器の内部に残留するPCBを溶解させて排出させるPCB汚染電気機器のPCB除去方法において、
下記計算式、
初期油中PCB濃度×重量×残油率(油付着率)×洗浄効率
ここで、初期油中PCB濃度:未処理油中のPCB濃度
重量:変圧器全体または構成部材の重量
油付着率:部材毎および状況により定まる油の付着率(含浸物
1gに滲み込む油量)
洗浄効率:単位洗浄当りのPCBの溶出率
により、前記電気機器内の除去処理の状況を算出し、
この算出結果を確認しながら除去処理を進める
ことを特徴とするPCB汚染電気機器のPCB除去方法、
を提供するものである。
In order to achieve the above object, in the present invention,
After the insulating oil is extracted from the electrical equipment filled with insulating oil containing PCB, a hydrocarbon solvent is injected, and the PCB remaining in the electrical equipment is dissolved and discharged in the hydrocarbon solvent. In the PCB removal method of PCB-contaminated electrical equipment to be performed,
The following calculation formula,
PCB concentration in initial oil × weight × residual oil rate (oil adhesion rate) × cleaning efficiency Here, PCB concentration in initial oil: PCB concentration in untreated oil
Weight: Weight of the entire transformer or components
Oil adhesion rate: Oil adhesion rate determined by each component and situation (impregnated material)
(Amount of oil that permeates into 1 g)
Cleaning efficiency: Calculate the status of the removal process in the electrical equipment based on the dissolution rate of PCB per unit cleaning.
PCB removal method for PCB-contaminated electrical equipment, characterized in that the removal process proceeds while confirming the calculation result,
Is to provide.
本発明は上述のように、微量のPCBが何らかの原因で混入した電気機器を、基本プロセスにより内部状態を把握しながら洗浄することにより、効率的にPCBを除去することができる。そして、現地において電気機器を解体することがないため、経済性に優れ、洗浄時の温度及び圧力を特別なものとすることなく安全に洗浄することができる。 As described above, according to the present invention, PCBs can be efficiently removed by cleaning an electrical device mixed with a trace amount of PCB for some reason while grasping the internal state by a basic process. And since the electric equipment is not disassembled locally, it is excellent in economic efficiency and can be safely washed without special temperature and pressure at the time of washing.
本発明の処理対象となる、何らかの原因で微量のPCBが混入したPCB汚染電気機器を変圧器について整理すると、(a)変圧器に注入された絶縁油中のPCB濃度は0.5〜数十ppmレベルである、(b)変圧器の大きさは、解体しないと輸送できないものが多い、(c)変圧器の台数は、百万台近くあると推定される、という特徴がある。 When the PCB-contaminated electrical equipment mixed with a trace amount of PCB for some reason, which is a processing target of the present invention, is arranged with respect to the transformer, (a) the PCB concentration in the insulating oil injected into the transformer is 0.5 to several tens. It is in ppm level. (b) Many transformers cannot be transported without being dismantled. (c) The number of transformers is estimated to be close to 1 million.
本発明では、これらの特徴、および上述の広域処理施設での処理が困難であることを勘案して、現地据付場所あるいは現地保管場所で移動可能な処理装置を用いることにより、変圧器からPCBを含む絶縁油を抜取った後、変圧器の内部を洗浄してPCBを除去する処理を行う。 In the present invention, in consideration of these characteristics and the processing at the above-mentioned wide-area processing facility, it is possible to remove the PCB from the transformer by using a processing device that can be moved at the local installation location or the local storage location. After the insulating oil is removed, the inside of the transformer is washed to remove PCB.
ここにおいて、変圧器内部の構成と処理条件(溶剤温度や処理時間など)による溶出率を考慮して、所定計算式を用いた計算により処理後の状態を求めるものである。基本的には、初期のPCB量から処理により溶出したPCB量を差し引いて処理後のPCB量を求める。 Here, the state after processing is obtained by calculation using a predetermined calculation formula in consideration of the elution rate depending on the internal configuration of the transformer and processing conditions (solvent temperature, processing time, etc.). Basically, the amount of PCB after processing is obtained by subtracting the amount of PCB eluted by processing from the initial amount of PCB.
求め方の詳細を、引き続き変圧器を例として以下に説明する。 Details of how to find it will be described below, taking a transformer as an example.
まず、初期つまり除去処理前のPCB量は、油量と液中PCB濃度とから求めることができる。このPCBの分布状態は、変圧器を構成する各部材の重量や含浸率から求めることができる。 First, the initial amount of PCB before being removed, that is, the amount of PCB can be determined from the amount of oil and the PCB concentration in the liquid. This PCB distribution state can be determined from the weight and impregnation rate of each member constituting the transformer.
微量PCBが混入した絶縁油を抜油すると、変圧器内に残る油は、
(1)金属などの非含浸物の表面に付着しているもの、
(2)紙などの含浸物にしみ込んでいるもの、
(3)容器の底部や構造上の隙間などに残っているもの、
の3種類に分けられる。
When the insulating oil mixed with a small amount of PCB is extracted, the oil remaining in the transformer is
(1) Attached to the surface of a non-impregnated material such as metal,
(2) What is impregnated in an impregnated material such as paper,
(3) What remains in the bottom of the container or structural gaps,
It is divided into three types.
抜油後に溶剤を注入したとき、残油の溶出度合いは、含浸(あるいは付着)している材質の種類や構成により異なる。この溶出度合いは、溶出処理の条件にも関わっており、これらを併せ考えれば処理による最終状態を既知の値または必要に応じて測定により得た測定値を得、その値を用いた計算により求めることができる。 When the solvent is injected after oil removal, the degree of elution of the residual oil varies depending on the type and configuration of the impregnated (or adhered) material. This elution degree is also related to the conditions of elution treatment, and taking these together, obtain the final value of the treatment by a known value or a measurement value obtained by measurement as necessary, and obtain by calculation using that value. be able to.
このように除去処理と所定の式による計算とを組み合わせれば、変圧器を解体・分別することなく変圧器の除去処理後の内部状態を把握できる。解体・分別をしないことにより、それらに関わる設備や作業が不要となって経済的である上に、変圧器を送配電線に接続した状態で除去処理をメンテナンスと同様に行えば、変圧器の継続使用も可能となる。 In this way, by combining the removal process and the calculation by a predetermined formula, it is possible to grasp the internal state after the removal process of the transformer without disassembling and separating the transformer. By not disassembling and separating, it is economical because the equipment and work related to them are unnecessary, and if the removal process is performed in the same way as maintenance with the transformer connected to the power transmission and distribution line, Continuous use is also possible.
変圧器を再使用する場合は、溶剤による変圧器への影響を変圧器絶縁油に対して行う規格試験により予め調べ、問題とならない混入濃度以下になるように絶縁油を注入する必要があり、この混入量も上記計算の中で求めることができる。 When reusing a transformer, it is necessary to inspect the influence of the solvent on the transformer in advance by a standard test performed on the transformer insulating oil, and to inject the insulating oil so that the concentration does not become a problem. This mixing amount can also be obtained in the above calculation.
処理により生ずる部材その他によるPCB濃度の不均衡は、液に浸した状態で放置した場合には、時間の経過とともに緩和され、充分な時間の経過後には平衡した状態になる。 The PCB concentration imbalance due to the components and the like caused by the treatment is alleviated with the passage of time when left in a state immersed in the liquid, and is brought into an equilibrium state after a sufficient amount of time has passed.
この計算に必要なパラメータは、変圧器の種類によっていくつかに分かれる。これは、変圧器の種類により、部材構成比が大きく違うものがあるからである。 The parameters required for this calculation are divided into several types depending on the type of transformer. This is because there is a material composition ratio that varies greatly depending on the type of transformer.
また、計算に使用するパラメータのうちのいくつかは、対象となる変圧器の容量により変動する。例えば、容量が大きくなるに連れて重量比率が増す変圧器容器などがそれに当たる。 In addition, some of the parameters used for the calculation vary depending on the capacity of the target transformer. For example, a transformer container whose weight ratio increases as the capacity increases corresponds to this.
次に、本発明の実施形態について図面を参照して説明する。 Next, embodiments of the present invention will be described with reference to the drawings.
図1は、本発明に係る処理プロセスを示す工程図であり、図2は、本発明に用いる装置構成を示した説明図である。以下、処理プロセスの各ステップを図1に基き説明することとし、その各工程に使用する機器につき図2により説明する。 FIG. 1 is a process diagram showing a processing process according to the present invention, and FIG. 2 is an explanatory diagram showing an apparatus configuration used in the present invention. Hereinafter, each step of the processing process will be described with reference to FIG. 1, and devices used for each process will be described with reference to FIG. 2.
処理プロセスとしては、PCB汚染変圧器1の排油弁4に、抜取り配管14、抜取りポンプ6及び排油貯槽7を接続し、抜取りポンプ6を起動してPCB汚染変圧器1からPCBを含む絶縁油2を抜油する(図1、ステップS1)。抜油したPCBを含む絶縁油2は、排油貯槽7に貯める。
As a treatment process, an
このとき、PCBの除去効率を向上するには、PCB汚染変圧器1からの抜油率を高めることが有効で、その方法として、抜油後にPCB汚染変圧器1のハンドホール5などから抜油ノズル9を挿入し、残油を上述と同様に排油貯槽11に回収する(図1、ステップS2)。抜油により回収したPCBを含む絶縁油2は、別途、排油処理施設に搬入され無害化処理される。
At this time, in order to improve the removal efficiency of the PCB, it is effective to increase the oil removal rate from the PCB contamination transformer 1. As the method, the
次に、PCB汚染変圧器1に、洗浄溶剤注入配管15、洗浄溶剤貯槽12、加温循環装置11、循環ポンプ10を接続し、排気配管17及び排気処理装置18を接続した上で、循環ポンプ10を起動して溶剤貯槽12の洗浄溶剤13をPCBで汚染した変圧器1内に注入し(図1、ステップS3)、溶剤を循環またはポンプを止めて浸漬する(図1、ステップS4)。排油貯槽7、洗浄溶剤貯槽12は蒸留装置19に接続するように構成してもよい。
Next, the cleaning
このとき放出される排気ガスは、排気処理装置18内の活性炭あるいは光触媒などで構成された排気処理装置18を通すことで、排気ガス中のPCBを分解、除去して環境への放出を防止する。ただし、排気配管17および排気処理装置18は省略することもある。
The exhaust gas released at this time passes through the
ここで、洗浄に使用する溶剤13は、石油系溶剤を採用する。これらの洗浄溶剤10は、危険物に分類されるものの、低毒性で溶解力および安定性に優れ、取扱いが容易であり、実証データから洗浄効果に優れることが分っており、且つ経済性が良い。しかも、引火点以下の温度および大気圧状態で洗浄できるため、安全性にも優れている。
Here, the solvent 13 used for cleaning employs a petroleum solvent. Although these cleaning
次に、上述の循環洗浄終了後に抜取りポンプ6を起動してPCB汚染変圧器1から洗浄溶剤13を排油貯槽7に回収し、貯める(図1、ステップS5)。
Next, after completion of the above-described circulation cleaning, the
上述の溶剤注入、洗浄から抜油までの工程を数回繰返し(図1、ステップS3−S5)、PCB汚染変圧器1内の部材3の洗浄効果をさらに高めることができる。
The above-described steps from solvent injection and cleaning to oil removal are repeated several times (FIG. 1, steps S3 to S5), and the cleaning effect of the
そして、変圧器1を継続使用する場合は、図1におけるステップS6ないしS9に示す、加湿循環/乾燥、脱気注油(ステップS6)、絶縁油適合性検証(ステップS7)、変圧器改造時の性能検証(ステップS8)、そして、運転(ステップS9)へと移行していく。 When the transformer 1 is continuously used, humidification circulation / drying, degassing oiling (step S6), insulation oil compatibility verification (step S7), and transformer modification shown in steps S6 to S9 in FIG. The process proceeds to performance verification (step S8) and operation (step S9).
以上のPCBを除去するための基本プロセス、及びシステム構成により洗浄効果を高めて、部材3中のPCBを洗浄溶剤13中に効率的に回収し除去することができる。
The basic process for removing PCB and the system configuration can enhance the cleaning effect, and the PCB in the
このようにPCBが除去された状態というのは、通常は解体して分析することにより把握するが、本発明では、これを計算により把握する。この計算について、以下に説明する。 The state in which the PCB is removed as described above is normally grasped by disassembling and analyzing, but in the present invention, this is grasped by calculation. This calculation will be described below.
図3は、本発明による処理に伴う変圧器の内部状態の変化を表した説明図である。対象となる微量のPCBが混入した変圧器1において、除去処理前の状態では、変圧器1内にある油中のPCB濃度は均一である(状態101)。抜油して状態102のようになると、微量PCB混入油は各構成部材中に残される。
FIG. 3 is an explanatory diagram showing changes in the internal state of the transformer accompanying the processing according to the present invention. In the transformer 1 in which a small amount of PCB to be mixed is mixed, the PCB concentration in the oil in the transformer 1 is uniform (state 101) before the removal process. When the oil is extracted and the
ここで、状態103に示すように溶剤Sを注入すると、徐々にPCBが溶け出して状態104になる。溶け出したPCBを含む溶剤Sを抜油すると、状態105となり、注油−溶出−抜油を繰り返すことによって変圧器1内部のPCB量を減らすことができる。
Here, when the solvent S is injected as shown in the
除去処理後に変圧器を継続して使用する場合には、除去処理に使用する溶剤について変圧器の絶縁油として必要な規定値を満たすことが可能な混入濃度の上限値を予め試験によって求めておき、この上限値以下になるまで溶剤Sを除去する。この後、変圧器1内に絶縁油を注入する。この状態のまま充分に長い時間が経てば、変圧器1内の油のPCB濃度は再び平衡に達して均一にPCBが除去された状態となる(状態106)。 If the transformer is to be used continuously after the removal process, the upper limit of the concentration of contamination that can satisfy the specified value required for the insulating oil of the transformer for the solvent used in the removal process must be determined in advance by testing. The solvent S is removed until the upper limit is reached. Thereafter, insulating oil is injected into the transformer 1. If a sufficiently long time has passed in this state, the PCB concentration of the oil in the transformer 1 reaches equilibrium again and the PCB is uniformly removed (state 106).
一方、変圧器を除却する場合は、抜油した状態で処理を終了する。 On the other hand, when removing a transformer, a process is complete | finished in the state which drained.
図4は、図3の状態105における変圧器1内部の詳細図である。変圧器1の内部には、紙などの絶縁物と銅などの金属とを積層した部材3(例えば、コイル3aや鉄心3bなどの金属を積層した芯、その他に木やプレスボードなどの多くの部材)が含まれており、それぞれが種類毎に異なる割合で油を含んでいる。
FIG. 4 is a detailed view of the inside of the transformer 1 in the
このため、処理により溶出するPCBの割合も部材の種類や構造によって異なり、処理を繰り返した後に排油弁4から抜油すると濃度に分布ができる。そこで、容器底部に残る油2aに関する残油率とか容器内面に付着する油2bに関する油付着率や、部材による洗浄効率などを導入して計算すると、処理に伴う変圧器内部の状態を求めることができる。
For this reason, the proportion of PCBs eluted by processing varies depending on the type and structure of the member, and when oil is removed from the
すなわち、下記残留濃度計算式、
初期油中PCB濃度×重量×残油率(油付着率)×洗浄効率
ここで、初期油中PCB濃度:未処理油中のPCB濃度
重量:変圧器全体または構成部材の重量
油付着率:部材毎および状況により定まる油の付着率(含浸物1
gに滲み込む油量)
洗浄効率:単純洗浄当りのPCBの溶出率
による計算を行う。
That is, the following residual concentration formula:
PCB concentration in initial oil × weight × residual oil rate (oil adhesion rate) × cleaning efficiency Here, PCB concentration in initial oil: PCB concentration in untreated oil
Weight: Weight of the entire transformer or components
Oil adhesion rate: Oil adhesion rate determined by each member and situation (impregnated material 1
amount of oil soaking into g)
Washing efficiency: Calculation is based on the dissolution rate of PCB per simple wash.
この残留濃度計算式による計算により、最終的に残留しているPCBの濃度も求めることができる。処理の途中経過を求めることも可能であるため、処理の指針として使用することができる。 By the calculation based on the residual concentration calculation formula, the concentration of the PCB that finally remains can be obtained. Since it is possible to determine the progress of the process, it can be used as a guide for the process.
これらの処理は、変圧器などの通常の油入換えメンテナンスとほぼ同様の処理であり、これをメンテナンスと同時に行うことで稼働中の変圧器への負担を軽減することができる。 These processes are almost the same as normal oil replacement maintenance for transformers and the like, and by performing this simultaneously with the maintenance, it is possible to reduce the burden on the operating transformer.
(計算例)
次に具体的機器について変圧器を例にとり、上記残留濃度計算式を用いてPCB濃度を算出してみる。
(Calculation example)
Next, taking a transformer as an example of specific equipment, the PCB concentration is calculated using the above-described residual concentration calculation formula.
1.処理対象変圧器
総重量;21500kg
油量;6600L
中身重量;10500kg
初期油中PCB濃度;35mg/kg
1. Transformer target total weight: 21500kg
Oil amount: 6600L
Contents weight: 10500kg
Initial PCB concentration in oil; 35 mg / kg
2.処理条件
洗浄溶剤;HC370(東ソー社製)
洗浄時間;24時間(1回当たり)
洗浄温度;60度(洗浄液循環中)
2. Processing conditions Cleaning solvent: HC370 (manufactured by Tosoh Corporation)
Washing time: 24 hours (per time)
Cleaning temperature: 60 degrees (during cleaning liquid circulation)
3.部材構成比の計算
部材構成比は、これまでの測定結果より表1のように求められる。
4.処理後の残留PCB量の計算
処理毎のPCB残留量は、上記2.の処理条件の場合に表2のように求められる。
5.処理回数の決定
上記表3より3回で、目標の0.5以下となることが分かる。
5. Determination of the number of treatments From Table 3, it can be seen that the number of treatments is less than or equal to the target of 0.5.
(その他の処理)
前述したように、機器内の残留PCBの一つとして、抜油した後に容器底に残る油があり、これを減らすことでPCBの残量を減らすことができる。抜油用のバルブは機器の下部に設けられていることが多いが、底面には設けられていないため、多少の残量が出る。ノズルを挿入してこれを回収することで、残量を減らすことができる。
(Other processing)
As described above, as one of the residual PCBs in the equipment, there is oil remaining on the bottom of the container after the oil is removed, and by reducing this, the remaining amount of PCB can be reduced. The valve for oil removal is often provided at the lower part of the device, but since it is not provided on the bottom surface, there is a little remaining amount. The remaining amount can be reduced by inserting the nozzle and collecting it.
以上の処理により、PCBを含んだ絶縁油と溶剤との混合物が回収される。この混合物を蒸留分離すると、溶剤のみと絶縁油にPCBを含んだものとに分離できる。絶縁油およびPCBは、両者を分離せずに無害化処理施設へ運ぶ。このため、PCBは初期の濃度より濃くなることがなく、濃縮したPCBを扱わないので安全性が高くなる。 Through the above treatment, a mixture of insulating oil containing PCB and solvent is recovered. When this mixture is separated by distillation, it can be separated into only a solvent and an insulating oil containing PCB. Insulating oil and PCB are transported to the detoxification facility without separating them. For this reason, the PCB does not become darker than the initial concentration, and since the concentrated PCB is not handled, the safety is increased.
処理後に変圧器を再使用するためには、溶剤を抜いた後に変圧器に本来使われている絶縁油を注入する。溶剤の変圧器への影響は予め定められた試験により調べ、問題の無いレベルになるまで洗浄溶剤を取り除く。取り除く方法としては、抜油または共洗いがある。 In order to reuse the transformer after the treatment, the insulating oil used for the transformer is injected after removing the solvent. The effect of the solvent on the transformer is examined by a predetermined test, and the cleaning solvent is removed until a problem-free level is reached. As a method of removing, there is oil removal or co-washing.
処理に使用する溶剤は、PCBと分離して再使用するため、沸点範囲がPCBに重ならないことが必要である。 Since the solvent used for the treatment is separated from the PCB and reused, it is necessary that the boiling range does not overlap with the PCB.
変圧器を再使用するためには、変圧器内部の温度上昇を規定値以内に保つ必要がある。また、溶剤の引火点を超えない温度で洗浄することにより、安全性が高まる。このため、洗浄中の温度は80度以下とする。 In order to reuse the transformer, it is necessary to keep the temperature rise inside the transformer within the specified value. Further, safety is enhanced by washing at a temperature not exceeding the flash point of the solvent. For this reason, the temperature during cleaning is set to 80 degrees or less.
1・・・・PCB汚染変圧器
2・・・・PCBを含む絶縁油
3・・・・変圧器内部構成物
4・・・・排油バルブ
5・・・・ハンドホール
6・・・・抜取りポンプ
7・・・・排油貯槽
8・・・・排油または廃溶剤
9・・・・抜油ノズル
10・・・循環ポンプ
11・・・加温循環装置
12・・・溶剤貯槽
13・・・溶剤
14・・・抜取り配管
15・・・洗浄溶剤注入配管
16・・・洗浄溶剤循環配管
17・・・真空排気配管
18・・・排気処理装置
19・・・変圧器の初期状態
20・・・初期の油を抜油した状態
21・・・石油系溶剤
22・・・溶剤を注入した状態
23・・・PCBが溶出した溶剤
24・・・溶剤にPCBが溶出した状態
25・・・PCBが溶出した溶剤を抜油した状態
26・・・各部材に溶け込んだPCBが溶出して均質化した状態
27・・・排油弁
28・・・コイル
29・・・芯
30・・・容器内残油
31・・・容器壁面に付着した油
1 ... PCB contaminated
Claims (7)
下記計算式、
初期油中PCB濃度×重量×残油率(油付着率)×洗浄効率
ここで、初期油中PCB濃度:未処理油中のPCB濃度
重量:変圧器全体または構成部材の重量
油付着率:部材毎および状況により定まる油の付着率(含浸物
1gに滲み込む油量)
洗浄効率:単位洗浄当りのPCBの溶出率
により、前記電気機器内の除去処理の状況を算出し、
この算出結果を確認しながら除去処理を進める
ことを特徴とするPCB汚染電気機器のPCB除去方法。 After the insulating oil is extracted from the electrical equipment filled with insulating oil containing PCB, a hydrocarbon solvent is injected, and the PCB remaining in the electrical equipment is dissolved in the hydrocarbon solvent and discharged. In the PCB removal method of PCB-contaminated electrical equipment to be performed,
The following calculation formula,
PCB concentration in initial oil × weight × residual oil rate (oil adhesion rate) × cleaning efficiency Here, PCB concentration in initial oil: PCB concentration in untreated oil
Weight: Weight of the entire transformer or components
Oil adhesion rate: Oil adhesion rate determined by each member and situation (impregnated material)
(Amount of oil that permeates into 1 g)
Cleaning efficiency: Calculate the status of the removal process in the electrical equipment by the PCB elution rate per unit cleaning.
A PCB removal method for PCB-contaminated electrical equipment, wherein the removal process is performed while checking the calculation result.
前記計算式には、前記電気機器の構成と、処理条件に伴う溶出率を使用し、
前記電気機器の種類および容量による微小な変更を加えて洗浄回数を変更する
ことを特徴とするPCB汚染電気機器のPCB除去方法。 In the PCB removal method of the PCB contaminated electrical equipment according to claim 1,
In the calculation formula, use the configuration of the electrical equipment and the dissolution rate associated with the processing conditions,
A PCB removal method for PCB-contaminated electrical equipment, wherein the number of cleanings is changed by making a minute change depending on the type and capacity of the electrical equipment.
除去処理中に、予め定められた洗浄回数毎に洗浄後の洗浄液中のPCB濃度を測定し、前記算出結果と比較して、除去処理にフィードバックすることを特徴とするPCB汚染電気機器のPCB除去方法。 In the PCB removal method of the PCB contaminated electrical equipment according to claim 1,
PCB removal of PCB-contaminated electrical equipment characterized in that, during the removal process, the PCB concentration in the washing liquid after washing is measured every predetermined number of washing times, and compared with the calculation result and fed back to the removal process Method.
除去処理に使用した洗浄溶剤は、絶縁油およびPCBの混在した液と分離して再使用し、この分離の際に絶縁油とPCBとは分離しないことを特徴とするPCB汚染電気機器のPCB除去方法。 In the PCB removal method of the PCB contaminated electrical equipment according to claim 1,
The cleaning solvent used in the removal process is separated from the mixture of insulating oil and PCB and reused, and the insulating oil and PCB are not separated during this separation. PCB removal for PCB-contaminated electrical equipment Method.
除去処理後に前記電気機器を継続して使用する場合には、除去処理に使用する溶剤について前記電気機器の絶縁油として必要な規定値を満たすことが可能な混入濃度の上限値を予め試験によって求め、
前記上限値以下になるまで洗浄溶剤を除去する
ことを特徴とするPCB汚染電気機器のPCB除去方法。 In the PCB removal method of the PCB contamination electric equipment according to claim 1,
When the electrical equipment is to be used continuously after removal treatment, the upper limit value of the mixing concentration that can satisfy the specified value required for the insulating oil of the electrical equipment for the solvent used in the removal treatment is obtained in advance by a test. ,
The cleaning solvent is removed until the upper limit value is reached or less. A PCB removal method for PCB-contaminated electrical equipment.
前記炭化水素系溶剤は、沸点が250度以下であることを特徴とするPCB汚染電気機器のPCB除去方法。 In the PCB removal method of the PCB contaminated electrical equipment according to claim 1,
The method for removing PCBs from PCB-contaminated electrical equipment, wherein the hydrocarbon solvent has a boiling point of 250 degrees or less.
前記溶剤を80℃以下に加温して循環することを特徴とするPCB汚染電気機器のPCB除去方法。 In the PCB removal method of the PCB contamination electric equipment according to claim 1,
A PCB removal method for PCB-contaminated electrical equipment, wherein the solvent is heated to 80 ° C. or less and circulated.
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JP2011011184A (en) * | 2009-07-06 | 2011-01-20 | Mitsui Eng & Shipbuild Co Ltd | Method for dismounting contaminated equipment |
JP2012187441A (en) * | 2011-03-08 | 2012-10-04 | Kobelco Eco-Solutions Co Ltd | Method for rendering distillation column harmless |
JP2012187442A (en) * | 2011-03-08 | 2012-10-04 | Kobelco Eco-Solutions Co Ltd | Method for demolishing facility for rendering pcb-contaminated equipment harmless |
JP2015202455A (en) * | 2014-04-14 | 2015-11-16 | 一般財団法人電力中央研究所 | Ending determination method of washing processing of pcb contaminated equipment, completion determination method of pcb detoxification processing by washing and estimation method of pcb concentration of washing liquid after washing |
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