JP4889557B2 - Method and apparatus for cleaning PCB contaminated transformer - Google Patents
Method and apparatus for cleaning PCB contaminated transformer Download PDFInfo
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- JP4889557B2 JP4889557B2 JP2007114188A JP2007114188A JP4889557B2 JP 4889557 B2 JP4889557 B2 JP 4889557B2 JP 2007114188 A JP2007114188 A JP 2007114188A JP 2007114188 A JP2007114188 A JP 2007114188A JP 4889557 B2 JP4889557 B2 JP 4889557B2
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Description
本発明は、ポリ塩化ビフェニル(PCB)を含有する油を使用した変圧器を洗浄するPCB汚染変圧器の洗浄方法及び洗浄装置に関し、特に、PCBを含有する油が封入された変圧器からPCB汚染油を抜油し、PCBを含有していない、あるいはポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油を注入して循環あるいは放置させることで、変圧器の内壁及び内部部材に付着あるいは浸透したPCBを洗浄するPCB汚染変圧器の洗浄方法及び洗浄装置に関する。 The present invention relates to a cleaning method and a cleaning device for a PCB-contaminated transformer that cleans a transformer using oil containing polychlorinated biphenyl (PCB), and more particularly, from a transformer in which oil containing PCB is enclosed to PCB contamination. By removing the oil and injecting oil that does not contain PCB or whose polychlorinated biphenyl content is within the regulation (standard) range and circulate or leave it, it will adhere to the inner wall and internal members of the transformer. The present invention relates to a cleaning method and a cleaning apparatus for a PCB-contaminated transformer that cleans a permeated PCB.
変圧器などの重電機器中の絶縁油(PCBを使用していないもの)から微量のPCBが検出されて以降、平成15年に国は「低濃度PCB汚染物対策検討委員会」を設置し、微量PCB混入問題の解決に向けた本格的な検討を行っている。微量PCB混入機器は、濃度がppmオーダーと低く、対象機器は多種多量で、ユーザーは中小企業も含め多業種に亘っているという特徴があげられることから、同機器の処理には、国民経済的にも合理的な処理方法が求められる。 After a small amount of PCB was detected from insulating oil (which does not use PCB) in heavy electrical equipment such as transformers, the country established the “Low Concentration PCB Contamination Countermeasures Review Committee” in 2003. We are conducting a full-scale study to solve the problem of PCB contamination. The amount of PCB-mixed devices is as low as ppm order, the target devices are many, and the users are in many industries including SMEs. In addition, a rational processing method is required.
既に、PCBで汚染された変圧器等を無害化する方法として、PCBを含有する絶縁油が封入された変圧器にPCBを含有していない絶縁油(新油)を注入して循環させることで、洗浄することが開示され(例えば、特許文献1〜13)、さらに、新油を100℃以上にして洗浄することが開示されている(特許文献14参照)。 As a method of detoxifying transformers already contaminated with PCB, by injecting and circulating insulating oil (new oil) that does not contain PCB into a transformer in which insulating oil containing PCB is sealed In addition, it is disclosed that cleaning is performed (for example, Patent Documents 1 to 13), and further, cleaning is performed by setting new oil to 100 ° C. or higher (see Patent Document 14).
しかしながら、特許文献1〜13に記載された方法では、PCBで汚染された変圧器等を効率的に無害化することができず、また、特許文献14に記載された方法では、洗浄作用は高いものの、変圧器内の摩擦等により生じた火花等によって発火する恐れがある。 However, the methods described in Patent Documents 1 to 13 cannot efficiently detoxify transformers contaminated with PCB, and the method described in Patent Document 14 has a high cleaning action. However, there is a risk of ignition due to sparks caused by friction in the transformer.
本発明は、かかる現状に鑑みてなされたものであり、従来における前記諸問題を解決し、以下の目的を達成することを課題とする。即ち、本発明は、PCBで汚染された変圧器を効率的に洗浄することができると共に、洗浄の際の発火を抑制することができるPCB汚染変圧器の洗浄方法及び洗浄装置を提供することを目的とする。 This invention is made | formed in view of this present condition, and makes it a subject to solve the said various problems in the past and to achieve the following objectives. That is, the present invention provides a cleaning method and a cleaning apparatus for a PCB-contaminated transformer that can efficiently clean a transformer contaminated with PCB and can suppress ignition during the cleaning. Objective.
前記課題を解決するため、本発明者らが鋭意検討を重ねた結果、油の温度を30〜40℃としてPCB汚染変圧器の循環洗浄を行った場合、約60時間後に、PCB汚染変圧器から循環している油へのPCBの浸出が停止すること、及び、油の温度を発火の恐れの少ない90℃まで昇温することにより、PCBの浸出が促進されることを見出し、本発明を完成するに至った。 In order to solve the above-mentioned problems, the present inventors have conducted intensive studies. As a result, when the temperature of the oil is 30 to 40 ° C. and the PCB-contaminated transformer is circulated and washed, the PCB-contaminated transformer is removed after about 60 hours. Discovered that PCB leaching into circulating oil stops and that the temperature of oil is raised to 90 ° C where there is little risk of ignition, and PCB leaching is promoted to complete the present invention. It came to do.
本発明は、本発明者による前記知見に基づくものであり、前記課題を解決するための手段としては、以下の通りである。即ち、
<1> ポリ塩化ビフェニルで汚染されたPCB汚染変圧器にポリ塩化ビフェニルを含有していない、あるいはポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油を注入して循環洗浄するPCB汚染変圧器の洗浄方法において、前記注入された油の温度が40〜90℃となるように該油を加熱する加熱工程を含むことを特徴とするPCB汚染変圧器の洗浄方法である。
該<1>においては、注入された油の温度が40〜90℃となるように該油が加熱されるので、PCBで汚染された変圧器を効率的に洗浄することができると共に、洗浄の際の発火を抑制することができる。
<2> 油の循環流速は、2.0〜3.0(mL/min)である前記<1>に記載のPCB汚染変圧器の洗浄方法である。
<3> ポリ塩化ビフェニルで汚染されたPCB汚染変圧器にポリ塩化ビフェニルを含有していない、あるいはポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油を注入し、放置するPCB汚染変圧器の洗浄方法において、前記注入された油の温度が40〜90℃となるように該油を加熱する加熱工程を含むことを特徴とするPCB汚染変圧器の洗浄方法である。
該<3>においては、注入された油の温度が40〜90℃となるように該油が加熱されるので、PCBで汚染された変圧器を効率的に洗浄することができると共に、洗浄の際の発火を抑制することができる。
<4> 加熱によって注入された油の粘度を低下させ、変圧器を構成する変圧器容器内壁及び内部部材に付着あるいは浸透したPCB自身、またはPCBを含む汚染油と、注入された油との交換を促す前記<1>から<3>のいずれかに記載のPCB汚染変圧器の洗浄方法である。
<5> 加熱工程における油の昇温速度は、6〜8(℃/h)である前記<1>から<4>のいずれかに記載のPCB汚染変圧器の洗浄方法である。
<6> さらに、注入された油の温度が30〜40℃となるように温調する温調工程を含む前記<1>から<5>のいずれかに記載のPCB汚染変圧器の洗浄方法である。
<7> 注入される油として、燃料油、潤滑油、食用油などに用いられる天然油、鉱油、又は合成油を使用する前記<1>から<6>のいずれかに記載のPCB汚染変圧器の洗浄方法である。
<8> 変圧器は、リアクトル、コンデンサを含む前記<1>から<7>のいずれかに記載のPCB汚染変圧器の洗浄方法である。
<9> ポリ塩化ビフェニルを含有していない、あるいはポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油を、ポリ塩化ビフェニルで汚染されたPCB汚染変圧器内で循環させて、該PCB汚染変圧器を洗浄するPCB汚染変圧器の洗浄装置において、前記油の温度が40〜90℃となるように該油を加熱する加熱手段を備えることを特徴とするPCB汚染変圧器の洗浄装置である。
<10> 油の循環流速は、2.0〜3.0(mL/min)である前記<9>に記載のPCB汚染変圧器の洗浄装置である。
<11> ポリ塩化ビフェニルを含有していない、あるいはポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油を、ポリ塩化ビフェニルで汚染されたPCB汚染変圧器内に放置して、該PCB汚染変圧器を洗浄するPCB汚染変圧器の洗浄装置において、前記油の温度が40〜90℃となるように該油を加熱する加熱手段を備えることを特徴とするPCB汚染変圧器の洗浄装置である。
<12> 加熱によって油の粘度を低下させ、変圧器を構成する変圧器容器内壁及び内部部材に付着あるいは浸透したPCB自身、またはPCBを含む汚染油と、循環乃至放置された油との交換を促す前記<9>から<11>のいずれかに記載のPCB汚染変圧器の洗浄装置である。
<13> 加熱手段により加熱された油の昇温速度は、6〜8(℃/h)である前記<9>から<12>のいずれかに記載のPCB汚染変圧器の洗浄装置である。
<14> さらに、油の温度が30〜40℃となるように温調する温調手段を含む前記<9>から<13>のいずれかに記載のPCB汚染変圧器の洗浄装置である。
<15> 循環乃至放置された油が、燃料油、潤滑油、食用油などに用いられる天然油、鉱油、又は合成油である前記<9>から<14>のいずれかに記載のPCB汚染変圧器の洗浄装置である。
<16> 変圧器は、リアクトル、コンデンサを含む前記<9>から<15>のいずれかに記載のPCB汚染変圧器の洗浄装置である。
This invention is based on the said knowledge by this inventor, and as a means for solving the said subject, it is as follows. That is,
<1> PCB contamination in which PCB contaminated transformer contaminated with polychlorinated biphenyl is injected with oil that does not contain polychlorinated biphenyl or the concentration of polychlorinated biphenyl is within the regulation (standard) range. In the method for cleaning a transformer, the method for cleaning a PCB-contaminated transformer is characterized by including a heating step of heating the injected oil so that the temperature of the injected oil is 40 to 90 ° C.
In <1>, since the oil is heated so that the temperature of the injected oil is 40 to 90 ° C., it is possible to efficiently clean the transformer contaminated with PCB and The ignition at the time can be suppressed.
<2> The method for cleaning a PCB-contaminated transformer according to <1>, wherein the oil circulation flow rate is 2.0 to 3.0 (mL / min).
<3> PCB pollution transformers that are contaminated with polychlorinated biphenyls are injected with oil that does not contain polychlorinated biphenyls or whose polychlorinated biphenyl content is within the regulation (standard) range. A method for cleaning a PCB contaminated transformer, comprising a heating step of heating the injected oil so that the temperature of the injected oil is 40 to 90 ° C.
In <3>, since the oil is heated so that the temperature of the injected oil becomes 40 to 90 ° C., the transformer contaminated with PCB can be efficiently cleaned, The ignition at the time can be suppressed.
<4> Replacing the injected oil with the PCB itself, or contaminated oil containing PCB, adhering to or penetrating the inner wall and internal member of the transformer container constituting the transformer by reducing the viscosity of the oil injected by heating The method for cleaning a PCB-contaminated transformer according to any one of <1> to <3>.
<5> The method for cleaning a PCB-contaminated transformer according to any one of <1> to <4>, wherein the temperature rising rate of the oil in the heating step is 6 to 8 (° C./h).
<6> The method for cleaning a PCB-contaminated transformer according to any one of <1> to <5>, further including a temperature adjustment step of adjusting the temperature of the injected oil to 30 to 40 ° C. is there.
<7> The PCB-contaminated transformer according to any one of <1> to <6>, wherein a natural oil, a mineral oil, or a synthetic oil used for fuel oil, lubricating oil, edible oil, or the like is used as the injected oil. This is a cleaning method.
<8> The transformer is a method for cleaning a PCB-contaminated transformer according to any one of <1> to <7>, including a reactor and a capacitor.
<9> An oil containing no polychlorinated biphenyl or having a polychlorinated biphenyl content within the regulation (standard) range is circulated in a PCB-contaminated transformer contaminated with polychlorinated biphenyl, A cleaning apparatus for a PCB contaminated transformer for cleaning a contaminated transformer, comprising: heating means for heating the oil so that the temperature of the oil is 40 to 90 ° C. is there.
<10> The cleaning device for a PCB-contaminated transformer according to <9>, wherein the oil circulation flow rate is 2.0 to 3.0 (mL / min).
<11> An oil containing no polychlorinated biphenyl or having a polychlorinated biphenyl content within a regulation (standard) range is left in a PCB-contaminated transformer contaminated with polychlorinated biphenyl, A cleaning apparatus for a PCB contaminated transformer for cleaning a contaminated transformer, comprising: heating means for heating the oil so that the temperature of the oil is 40 to 90 ° C. is there.
<12> Reduce the viscosity of the oil by heating, and replace the PCB itself that has adhered to or penetrated into the inner wall and internal members of the transformer or the contaminated oil containing the PCB with the oil that has been circulated or left unattended. The apparatus for cleaning a PCB-contaminated transformer according to any one of <9> to <11>.
<13> The apparatus for cleaning a PCB-contaminated transformer according to any one of <9> to <12>, wherein the heating rate of the oil heated by the heating unit is 6 to 8 (° C./h).
<14> The PCB contamination transformer cleaning device according to any one of <9> to <13>, further including a temperature adjusting unit that adjusts the temperature of the oil to be 30 to 40 ° C.
<15> The PCB-contaminated transformer according to any one of <9> to <14>, wherein the circulated or left oil is natural oil, mineral oil, or synthetic oil used for fuel oil, lubricating oil, edible oil, and the like. It is a cleaning device for the vessel.
<16> The transformer is a cleaning device for a PCB-contaminated transformer according to any one of <9> to <15>, including a reactor and a capacitor.
本発明によると、PCBで汚染された変圧器を効率的に洗浄することができると共に、洗浄の際の発火を抑制することができるPCB汚染変圧器の洗浄方法及び洗浄装置を提供することができる。
According to the present invention, it is possible to provide a cleaning method and a cleaning apparatus for a PCB-contaminated transformer that can efficiently clean a transformer contaminated with PCB and can suppress ignition during cleaning. .
(PCB汚染変圧器の洗浄方法)
本発明のPCB汚染変圧器の洗浄方法は、ポリ塩化ビフェニルで汚染されたPCB汚染変圧器にポリ塩化ビフェニルを含有していない、あるいはポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油を注入して循環あるいは放置させることで、洗浄するPCB汚染変圧器の洗浄方法において、前記注入された油の温度が40〜90℃となるように該油を加熱する加熱工程を含む。例えば、PCB汚染変圧器の洗浄方法は、PCBで汚染された変圧器からPCB汚染油を抜油する抜油工程と、PCBを含有していない、あるいはポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油をPCB汚染変圧器に注入する注入工程と、PCB汚染変圧器に注入された油の温度が40〜90℃となるように該油を加熱する加熱工程と、その他の工程とを含む。ここで、注入される油として、例えば、燃料油、潤滑油、食用油などに用いられる天然油、鉱油、又は合成油を使用する。なお、ポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油とは、現在のところ、ポリ塩化ビフェニルの含有濃度が0.5ppm(mg/kg)以下(後述する図17)の油を示す。
また、PCB汚染変圧器の洗浄方法には、PCB汚染変圧器を循環洗浄する洗浄装置と、その他の装置とが用いられる。
(Cleaning method for PCB contaminated transformer)
According to the method for cleaning a PCB-contaminated transformer of the present invention, a PCB-contaminated transformer contaminated with polychlorinated biphenyl does not contain polychlorinated biphenyl, or the concentration of polychlorinated biphenyl is within the regulation (standard) range. In a method for cleaning a PCB-contaminated transformer to be cleaned by injecting and circulating or leaving, a heating step of heating the injected oil to a temperature of 40 to 90 ° C. is included. For example, the cleaning method for PCB-contaminated transformers includes a process of removing PCB-contaminated oil from a transformer contaminated with PCB, and the concentration of polychlorinated biphenyl that does not contain PCB or is within the regulation (standard) range. An injection step of injecting the oil into the PCB-contaminated transformer, a heating step of heating the oil so that the temperature of the oil injected into the PCB-contaminated transformer is 40 to 90 ° C., and other steps. . Here, as oil to be injected, for example, natural oil, mineral oil, or synthetic oil used for fuel oil, lubricating oil, edible oil, or the like is used. In addition, the oil whose polychlorinated biphenyl content concentration is within the regulation (standard) range is currently an oil whose polychlorinated biphenyl content concentration is 0.5 ppm (mg / kg) or less (FIG. 17 described later). Show.
In addition, a cleaning device for circulating and cleaning a PCB contaminated transformer and other devices are used as a method for cleaning the PCB contaminated transformer.
<変圧器>
図1及び図2に示すように、変圧器100は、主として、蓋部1と、蓋部1に溶接された外缶容器2と、蓋部1及び外缶容器2に内装された内部部材(コア)3とを備える。
前記コア3は、図3及び図4に示すように、主として、積層された鉄板からなる鉄芯4と、鉄芯4の周囲に配置されたコイル5と、鉄芯4上に載置されたベークライト6と、コイル5を挟むように配置された鉄枠7とを備える。前記コイル5は、主として、鉄芯4に巻きつけられた銅線8(図5)によって構成されるが、この銅線8に巻きつけられた薄紙9(絶縁用紙)(図5)と、銅線8間のスペーサーとして設けられた厚紙10(図6)とを備える。また、結線には布11(図7)が巻きつけられている。
<Transformer>
As shown in FIGS. 1 and 2, the transformer 100 mainly includes a lid portion 1, an outer can container 2 welded to the lid portion 1, and an internal member (inside the lid portion 1 and the outer can container 2). Core) 3.
As shown in FIGS. 3 and 4, the core 3 is mainly placed on the iron core 4, an iron core 4 made of laminated iron plates, a coil 5 arranged around the iron core 4, and the iron core 4. A bakelite 6 and an iron frame 7 arranged so as to sandwich the coil 5 are provided. The coil 5 is mainly composed of a copper wire 8 (FIG. 5) wound around the iron core 4. The thin paper 9 (insulating paper) (FIG. 5) wound around the copper wire 8 and copper And cardboard 10 (FIG. 6) provided as a spacer between the lines 8. Moreover, the cloth 11 (FIG. 7) is wound around the connection.
<洗浄装置>
図8に示すように、変圧器100を洗浄するための洗浄装置80は、主として、内部に変圧器100が設置される油飛散防止容器81と、油飛散防止容器81に接続され、油飛散防止容器81に設置された変圧器100に油を送液する送液ポンプ82と、油飛散防止81に接続され、循環する油を所定温度に温調する温調器(冷却器83、本加熱槽84、及び予熱加熱槽85)とを備える。
洗浄装置80は、さらに、循環する油の温度を測定する温度計86と、循環する油の流量を測定する積算流量計87と、油飛散防止容器81に接続され、発火防止等の安全のために油飛散防止容器81内に窒素を封入する窒素ガスライン88と、予熱加熱槽85と送液ポンプ82との間に配設され、循環する油の送圧を測定する圧力計89と、予熱加熱槽85と圧力計89との間の油をサンプリングするためのサンプリングライン90とを備える。なお、変圧器は、リアクトル、コンデンサ等を含むものである。
<Washing device>
As shown in FIG. 8, a cleaning device 80 for cleaning the transformer 100 is mainly connected to an oil scattering prevention container 81 in which the transformer 100 is installed and an oil scattering prevention container 81 to prevent oil scattering. A liquid feed pump 82 that feeds oil to the transformer 100 installed in the container 81, and a temperature controller (cooler 83, main heating tank) that is connected to the oil splash prevention 81 and regulates the temperature of the circulating oil to a predetermined temperature. 84, and a preheating heating tank 85).
The cleaning device 80 is further connected to a thermometer 86 that measures the temperature of the circulating oil, an integrated flow meter 87 that measures the flow rate of the circulating oil, and an oil scattering prevention container 81 for safety such as prevention of ignition. A nitrogen gas line 88 that encloses nitrogen in the oil scattering prevention container 81, a pressure gauge 89 that is disposed between the preheating heating tank 85 and the liquid feeding pump 82 and measures the pressure of circulating oil, and a preheating. A sampling line 90 for sampling oil between the heating tank 85 and the pressure gauge 89 is provided. The transformer includes a reactor, a capacitor, and the like.
<その他の装置>
PCB汚染変圧器の洗浄方法に用いられる装置は、基本的に油注入あるいは入れ替え、さらに油循環と加温の機能を有していれば、必要に応じて、洗浄装置80以外の装置を備えていてもよい。例えば、変圧器100に油を注入する際に油中の塵あい、水分、溶解ガス等をろ過と真空脱気によって充分に除去する浄油機(例えば、株式会社三美テックス製 VSD−6000ES−N形 屋外可搬式)等が挙げられる。
<Other devices>
The device used for the method of cleaning the PCB contaminated transformer is basically equipped with a device other than the cleaning device 80 if necessary, as long as it has functions of oil injection or replacement, and oil circulation and heating. May be. For example, when injecting oil into the transformer 100, an oil purifier that sufficiently removes dust, moisture, dissolved gas, etc. in the oil by filtration and vacuum degassing (for example, VSD-6000ES- manufactured by Sanmi Tex Co., Ltd.) N type outdoor portable type).
<PCB汚染油の抜油工程>
蓋部1と外缶容器2との溶接部を切断して蓋部1を開け、蓋部1と一体となったコア3を外缶容器2から取り外す。次いで、外缶容器2内のPCB汚染油(元油)を、ポンプを用いて金属製タンクに移す。
なお、上述したように、外缶容器2内のPCB汚染油をポンプを用いて抜油することに限定されるものではなく、例えば、変圧器100の下部に設けられた抜油口からPCB汚染油を抜油してもよい。
<Oil removal process for PCB contaminated oil>
The welded portion between the lid 1 and the outer can container 2 is cut to open the lid 1, and the core 3 integrated with the lid 1 is removed from the outer can container 2. Next, the PCB-contaminated oil (base oil) in the outer can container 2 is transferred to a metal tank using a pump.
As described above, it is not limited to removing the PCB contaminated oil in the outer can container 2 using a pump. For example, the PCB contaminated oil is removed from the oil vent provided in the lower part of the transformer 100. You may drain oil.
<油の注入工程>
まず、外缶容器2を油飛散防止容器81内に設置し、続いて、蓋部1と一体となったコア3を油飛散防止容器81内に設置された外缶容器2内に設置する。その後、外缶容器2が送液ポンプ82に接続されるように第1の配管(吸入口)91(図9)を設置し、外缶容器が冷却器83に接続されるように第2の配管(吐出口)92(図9)を設置する。さらに、異常時のために第3の配管(排出口)93(図9)を設置する。これらの配管91〜93を設置した後、油飛散防止容器81に蓋をして油飛散防止容器81内に窒素ガスを封入し、PCBに汚染されてない油あるいはポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油45Lを、第1の配管(吸入口)91を通じて変圧器100の下層から注入し(注入工程)、第2の配管(吐出口)92を通じて変圧器100の上層から排出するように循環させて、あるいは放置して変圧器100を洗浄する。
<Oil injection process>
First, the outer can container 2 is installed in the oil scattering prevention container 81, and then the core 3 integrated with the lid portion 1 is installed in the outer can container 2 installed in the oil scattering prevention container 81. After that, the first pipe (suction port) 91 (FIG. 9) is installed so that the outer can container 2 is connected to the liquid feed pump 82, and the second can so that the outer can container is connected to the cooler 83. A pipe (discharge port) 92 (FIG. 9) is installed. Furthermore, a third pipe (discharge port) 93 (FIG. 9) is installed for an abnormal time. After installing these pipes 91-93, the oil spill prevention container 81 is covered and nitrogen gas is sealed in the oil spill prevention container 81, so that the concentration of oil or polychlorinated biphenyl that is not contaminated with PCB is regulated. Oil 45L within the (reference) range is injected from the lower layer of the transformer 100 through the first pipe (suction port) 91 (injection process), and from the upper layer of the transformer 100 through the second pipe (discharge port) 92. The transformer 100 is washed by being circulated or left to be discharged.
<加熱工程>
なお、循環洗浄の全期間において、循環される油の送液速度(循環流速)が0〜10.0mL/min、好ましくは、2.0〜3.0mL/minとなるように設定する。また、循環される油の温度が40〜90℃、好ましくは50〜90℃、さらに好ましくは50〜70℃になるように該油を加熱し(加熱工程)、加熱終了後は自然冷却する。
なお、加熱工程における油の昇温速度は、例えば、6〜8(℃/h)となるように設定する。
<Heating process>
In all periods of the circulation washing, circulation is the feed rate of the oil (circulating flow rate) is 0 to 10.0 m L / min, preferably, such that 2.0 to 3.0 m L / min Set. Further, the oil is heated so that the temperature of the circulated oil is 40 to 90 ° C., preferably 50 to 90 ° C., more preferably 50 to 70 ° C. (heating step), and naturally cooled after the heating.
In addition, the temperature increase rate of the oil in a heating process is set so that it may become 6-8 (degreeC / h), for example.
<その他の工程>
PCB汚染変圧器の洗浄方法として、必要に応じて、抜油工程、注入工程、及び加熱工程以外の工程を含んでいてもよい。例えば、油を30〜40℃に温調する温調工程や、油の温度が40〜90℃になるように該油を加熱して自然冷却した後に、再度、油の温度が40〜90℃になるように該油を加熱する第2の加熱工程や、変圧器100にPCBに汚染されてない油あるいは、ポリ塩化ビフェニルの含有濃度が規制(基準)範囲内である油を注入する際に油中の塵あい、水分、溶解ガス等をろ過と真空脱気によって充分に除去する浄油工程等が挙げられる。
本実施の形態では、変圧器100を一部分解して洗浄装置80内に設置し、油を循環させて、あるいは放置して変圧器100を洗浄したが、これに限定されるものではなく、例えば、変圧器100に浄油機を接続して、変圧器100及び浄油機間を油で循環させて変圧器100を洗浄してもよい。
<Other processes>
As a method for cleaning the PCB-contaminated transformer, steps other than the oil removal step, the injection step, and the heating step may be included as necessary. For example, a temperature adjustment step for adjusting the temperature of the oil to 30 to 40 ° C, or after naturally cooling the oil so that the temperature of the oil becomes 40 to 90 ° C and naturally cooling, the temperature of the oil is again 40 to 90 ° C. In the second heating step for heating the oil so as to become, when the transformer 100 is injected with oil that is not contaminated by PCB, or oil whose polychlorinated biphenyl concentration is within the regulation (standard) range An oil purification process for sufficiently removing dust, moisture, dissolved gas, and the like in oil by filtration and vacuum degassing.
In the present embodiment, the transformer 100 is partially disassembled and installed in the cleaning apparatus 80, and the transformer 100 is cleaned by circulating or leaving the oil. However, the present invention is not limited to this. Alternatively, an oil purifier may be connected to the transformer 100, and the transformer 100 may be cleaned by circulating oil between the transformer 100 and the oil purifier.
以下、本発明の実施例について説明するが、本発明はこの実施例に何ら限定されるものではなく、本技術分野において行われるこれらに対する通常の改変及び修飾を含むものとする。 EXAMPLES Examples of the present invention will be described below, but the present invention is not limited to these examples, and includes ordinary alterations and modifications to these performed in the technical field.
(実施例1)
<変圧器>
PCBで汚染された変圧器としては、財団法人電力中央研究所の横須賀地区(神奈川県横須賀市長坂2−6−1)にて保管されていた小型リアクトル(形式NITX,油入密閉式、油量45L容量、株式会社明電舎製、製造年1964年、製造番号1T85701)を用いた。
Example 1
<Transformer>
Transformers contaminated with PCB are small reactors (type NITX, oil-filled hermetically sealed, oil quantity) stored in Yokosuka area (2-6-1 Nagasaka, Yokosuka City, Kanagawa Prefecture) A 45 L capacity, manufactured by Meidensha Co., Ltd., production year 1964, production number 1T85701) was used.
<洗浄装置>
洗浄装置としては、図8に示した構造の洗浄装置を用いた。
<Washing device>
As the cleaning device, the cleaning device having the structure shown in FIG. 8 was used.
<PCB汚染油の抜油工程>
PCB汚染油が飛散や漏洩した場合に、床面に浸透しないようビニールシートを敷き、ビニールシート上に設置したバットに小型リアクトルを載置し、蓋部と外缶容器との溶接部を切断して蓋部を開け、蓋部と一体となったコアを外缶容器から取り外した。次いで、20Lの金属製タンク(有機溶剤廃液用タンク)を2個用意し、外缶容器内のPCB汚染油を、ポンプを用いて金属製タンクに移した。なお、この抜油したPCB汚染油(元油)の総PCB濃度は20.7mg/kgであった。
<Oil removal process for PCB contaminated oil>
If PCB contaminated oil scatters or leaks, place a vinyl sheet so that it does not penetrate the floor, place a small reactor on the bat installed on the vinyl sheet, and cut the weld between the lid and the outer can container. The lid was opened, and the core integrated with the lid was removed from the outer can container. Next, two 20 L metal tanks (organic solvent waste liquid tanks) were prepared, and the PCB-contaminated oil in the outer can container was transferred to the metal tank using a pump. The total PCB concentration of the extracted PCB-contaminated oil (base oil) was 20.7 mg / kg.
<注入工程及び加熱工程>
まず、小型リアクトルの外缶容器を、洗浄装置の油飛散防止容器内に設置し、続いて、小型リアクトルの蓋部及びコアを油飛散防止容器内に設置された外缶容器内に設置した。その後、外缶容器が送液ポンプに接続されるように第1の配管(吸入口)を設置し、外缶容器が冷却器に接続されるように第2の配管(吐出口)を設置した。さらに、異常時のために第3の配管(排出口)を設置した。これらの配管を設置した後、PCBに汚染されてない油45Lを第1の配管(吸入口)を通じて小型リアクトルに注入し、油飛散防止容器内に窒素ガスを封入した。循環洗浄の全期間において、循環される油の送液速度が2.0mL/minとなるように設定した。また、試験開始から98時間後までは、循環される油の温度が30〜40℃となるように加温及び冷却により温調し、98時間から105時間の間は、循環される油の温度が40〜90℃となるように加温及び冷却により温調した。105時間後は、温調を停止し、自然冷却した。さらに、119時間後から再び循環される油の温度が40〜90℃となるように温調を開始し、127時間後に温調を停止し、142時間後まで自然冷却した。全試験期間に渡り、任意の時間に洗浄装置のサンプリングラインから循環される油を採取し、分析試料とした。また、循環される油の温度は小型リアクトル内に設置した温度計、循環流速は、変圧器への流入口付近に設置された積算流量計で計測した。
<Injection process and heating process>
First, the outer can container of the small reactor was installed in the oil scattering prevention container of the cleaning device, and then the lid and the core of the small reactor were installed in the outer can container installed in the oil scattering prevention container. After that, the first pipe (suction port) was installed so that the outer can container was connected to the liquid feed pump, and the second pipe (discharge port) was installed so that the outer can container was connected to the cooler. . In addition, a third pipe (discharge port) was installed in case of an abnormality. After installing these pipes, 45 L of oil not contaminated with PCB was injected into the small reactor through the first pipe (suction port), and nitrogen gas was sealed in the oil scattering prevention container. In the entire period of the circulating washing were set as feed rate of the oil to be circulated is 2.0 m L / min. Further, the temperature of the circulated oil is adjusted by heating and cooling so that the temperature of the circulated oil becomes 30 to 40 ° C. until 98 hours after the start of the test, and the temperature of the circulated oil is between 98 hours and 105 hours. The temperature was adjusted by heating and cooling so as to be 40-90 ° C. After 105 hours, the temperature control was stopped and natural cooling was performed. Furthermore, temperature control was started so that the temperature of the oil circulated again after 40 hours would be 40 to 90 ° C, temperature control was stopped after 127 hours, and natural cooling was performed until 142 hours later. Over the entire test period, oil circulated from the sampling line of the cleaning device at an arbitrary time was collected and used as an analysis sample. The temperature of the circulated oil was measured with a thermometer installed in a small reactor, and the circulation flow rate was measured with an integrating flow meter installed near the inlet to the transformer.
<PCB濃度分析>
<<サンプリングラインから採取した油のPCB濃度分析>>
油のPCB濃度分析には、バイオセンサー、ゲル浸透クロマトグラフィー/電子捕獲型検出器付きガスクロマトグラフィー(GPC/GC/ECD)、及び高分解能ガスクロマトグラフ−高分解能質量分析計(HRGC/HRMS)を用いた。
<PCB concentration analysis>
<< PCB concentration analysis of oil collected from sampling line >>
For PCB analysis of oil, biosensor, gel permeation chromatography / gas chromatography with electron capture detector (GPC / GC / ECD), and high resolution gas chromatograph-high resolution mass spectrometer (HRGC / HRMS) Using.
<<<バイオセンサーを用いた油のPCB濃度分析>>>
バイオセンサーを用いた油のPCB濃度分析には、以下の抗体及び担体を用い、PCB濃度分析を行う油には以下の前処理を行った。
<<< PCB analysis of oil using biosensor >>>
The following antibody and carrier were used for the PCB concentration analysis of oil using a biosensor, and the following pretreatment was performed on the oil for PCB concentration analysis.
バイオセンサーを用いた油のPCB濃度分析には、モノクローナル マウス抗PCB抗体(株式会社住化分析センター製)を使用した。2次抗体には、CY−5標識モノクローナル ヤギ抗マウス抗体(Jackson lmmunoResearch co.製)を使用した。 Monoclonal mouse anti-PCB antibody (manufactured by Sumika Chemical Analysis Co., Ltd.) was used for PCB concentration analysis of oil using a biosensor. As the secondary antibody, a CY-5-labeled monoclonal goat anti-mouse antibody (Jackson ImmunoResearch co.) Was used.
アガロースビーズ(NHS−activated SepharoseTM 4 fast flow、 Amercham Biosciences社製)を固相担体として使用した。ビーズ担体の活性化は以下の手順に従って行った。ビーズ容量1mLとなるように懸濁液を採取し、1mLの1mMの塩酸(HCl)で10回洗浄する。さらに1mLの生理食塩水(Phosphate Buffered Saline,pH7,5、以下「PBS」とする)にて10回洗浄した後、0.9mLのPBSに懸濁した。次に合成したジクロロフェノール誘導体と牛血清アルブミン(Bovine Serum Albumin、以下「BSA」とする)の複合体を1mg/mLの濃度で含むPBS溶液を懸濁液に0.1mL添加した。室温にて2時間振とうした後、100mg/mLの濃度でBSAを含むPBS溶液を0.1mL添加し、さらに2時間振とうした。振とう後、ビーズを30mLのPBSに懸濁し、後述する検出セルに充填した。 Agarose beads (NHS-activated Sepharose ™ 4 fast flow, manufactured by Amercham Biosciences) were used as a solid support. The bead carrier was activated according to the following procedure. The suspension is taken to a bead volume of 1 mL and washed 10 times with 1 mL of 1 mM hydrochloric acid (HCl). Furthermore, after washing 10 times with 1 mL of physiological saline (phosphate buffered saline, pH 7,5, hereinafter referred to as “PBS”), the suspension was suspended in 0.9 mL of PBS. Next, 0.1 mL of a PBS solution containing a complex of the synthesized dichlorophenol derivative and bovine serum albumin (hereinafter referred to as “BSA”) at a concentration of 1 mg / mL was added to the suspension. After shaking at room temperature for 2 hours, 0.1 mL of a PBS solution containing BSA at a concentration of 100 mg / mL was added, followed by further shaking for 2 hours. After shaking, the beads were suspended in 30 mL of PBS and filled into a detection cell described later.
油の前処理には、シリカゲルの多層カラムを用いた。詳しくは、上層に発煙硫酸を含浸したシリカゲル、下層に発煙硫酸を含浸していないシリカゲルの二層カラムである。このカラムに0.5gの無水硫酸ナトリウムを重層した後、0.25gの油を添加し、さらに油をカラム内に浸透させるため0.2mLのn−ヘキサンを添加した。5分間放置して油成分の分解を促した後、15mLのn−ヘキサンを添加し、その全量をナス型フラスコに回収した。0.25mLのジメチルスルホキシド(DMSO)を加え、40℃の湯浴中でロータリーエバポレータでn−ヘキサンを除去した。この後、残液をマイクロチューブに移して遠心分離(10,000rpm、1分間)し、DMSO層を0.15mL分取して前処理液とした。 A silica gel multilayer column was used for oil pretreatment. Specifically, it is a two-layer column of silica gel impregnated with fuming sulfuric acid in the upper layer and silica gel not impregnated with fuming sulfuric acid in the lower layer. After 0.5 g of anhydrous sodium sulfate was overlaid on this column, 0.25 g of oil was added, and 0.2 mL of n-hexane was further added to allow the oil to penetrate into the column. After being allowed to stand for 5 minutes to promote decomposition of the oil component, 15 mL of n-hexane was added, and the whole amount was recovered in an eggplant type flask. 0.25 mL of dimethyl sulfoxide (DMSO) was added, and n-hexane was removed with a rotary evaporator in a 40 ° C. hot water bath. Thereafter, the remaining solution was transferred to a microtube and centrifuged (10,000 rpm, 1 minute), and 0.15 mL of a DMSO layer was taken as a pretreatment solution.
PCB濃度測定には、Kinexa3000装置(Sapidyne Instruments Inc.製 )を用いた検出セルで行った。この中空状のセル内にはビーズ担体が充填されており、上記の手順で調製した油前処理液に抗体の混合溶液(1次抗体:マウス 抗PCBモノクローナル抗体、2次抗体:Cy−5標識 ヤギ 抗マウス抗体)を加えてセルに送液する。抗体の混合溶液中では、1次抗体は2次抗体が結合した標識体として存在する。油にPCBが含まれる場合、1次抗体は抽出液中のPCBと結合して抗体−PCB結合体を形成するため、検出セルを素通りする。一方、油にPCBが含まれていない場合、1次抗体は検出セル内にあるジクロロフェノール誘導体と結合するので、セル内に抗体が捕捉される。捕捉された抗体の量を調べれば、油中のPCBの有無を知ることができる。セル内に捕捉された抗体量は、2次抗体上の色素からの蛍光(励起波長;620nm、測定波長;670nm)として光学的に計測できる。検出セルに励起光を照射し、得られる蛍光をフォトダイオードによって電気信号として計測する。油中のPCB濃度が高いほど、信号値が小さくなり、その減少から油中のPCB濃度を測定できる。
装置に供する抗体溶液は以下の手順で調製した。1次抗体及び2次抗体は、共に0.1%(w/w)のBSAを含むPBS(以下、「PBS−BSA」とする)で希釈して用いた。1次抗体と2次抗体の濃度は、それぞれ500pMと2nMとした。一方、各種油(新油、カネクロールを添加した新油及び洗浄に使用した新油)は前述の操作に従って前処理液を調製し、50倍にPBS−BSAにて希釈した。等量の抗体溶液と前処理液の希釈液を混合して測定液を調製した。この時、測定液中のDMSO濃度は2%(v/v)となるようにした。調製した測定液は自動装置に供した。測定した信号値からのPCB濃度への換算は、カネクロール300、400及び500の等質量混合液を添加した新油を前処理して測定した校正曲線を用いて行った。
The PCB concentration was measured with a detection cell using a Kinexa 3000 apparatus (manufactured by Sapidyne Instruments Inc.). The hollow cell is filled with a bead carrier. The oil pretreatment liquid prepared by the above procedure is mixed with an antibody (primary antibody: mouse anti-PCB monoclonal antibody, secondary antibody: Cy-5 labeling). Goat anti-mouse antibody) is added to the cell. In the antibody mixed solution, the primary antibody is present as a label to which the secondary antibody is bound. When the oil contains PCB, the primary antibody binds to the PCB in the extract to form an antibody-PCB conjugate and therefore passes through the detection cell. On the other hand, when PCB does not contain in oil, since a primary antibody couple | bonds with the dichlorophenol derivative in a detection cell, an antibody is capture | acquired in a cell. By examining the amount of captured antibody, it is possible to know the presence or absence of PCB in the oil. The amount of antibody captured in the cell can be optically measured as fluorescence (excitation wavelength: 620 nm, measurement wavelength: 670 nm) from the dye on the secondary antibody. The detection cell is irradiated with excitation light, and the resulting fluorescence is measured as an electrical signal by a photodiode. The higher the PCB concentration in oil, the smaller the signal value, and the PCB concentration in oil can be measured from the decrease.
The antibody solution to be used in the apparatus was prepared by the following procedure. The primary antibody and the secondary antibody were both diluted with PBS containing 0.1% (w / w) BSA (hereinafter referred to as “PBS-BSA”). The concentrations of the primary antibody and the secondary antibody were 500 pM and 2 nM, respectively. On the other hand, various oils (new oil, new oil to which Kanechlor was added and new oil used for washing) were prepared in accordance with the above-mentioned operation, and pretreatment liquids were prepared and diluted 50 times with PBS-BSA. An assay solution was prepared by mixing an equal amount of the antibody solution and a diluted solution of the pretreatment solution. At this time, the DMSO concentration in the measurement solution was set to 2% (v / v). The prepared measurement solution was subjected to an automatic apparatus. Conversion from the measured signal value to the PCB concentration was performed using a calibration curve measured by pretreatment of fresh oil to which an equal mass mixture of Kanechlor 300, 400 and 500 was added.
<<<GPC/GC/ECDを用いた油のPCB濃度分析>>>
GPC/GC/ECDを用いた油のPCB濃度分析を行う油には以下の前処理を行った。
<<< PCB concentration analysis of oil using GPC / GC / ECD >>>
The oil to be subjected to PCB concentration analysis of oil using GPC / GC / ECD was subjected to the following pretreatment.
容量50mLのフラスコにn−ヘキサン20mLと濃硫酸10mLを注入した後、試料1gを加えた。2時間ゆっくり撹拌して有機物を分解した後、ヘキサン層を分離後10mLの精製水で3回洗浄して、硫酸ナトリウム(無水物)で脱水した。次に、ヘキサン層を0.5mL以下まで濃縮し、GPC溶離液(酢酸エチル:シクロヘキサン=3:7)で10mLにメスアップし前処理液を調製した。 After injecting 20 mL of n-hexane and 10 mL of concentrated sulfuric acid into a 50 mL flask, 1 g of a sample was added. After slowly stirring for 2 hours to decompose organic matter, the hexane layer was separated, washed 3 times with 10 mL of purified water, and dehydrated with sodium sulfate (anhydrous). Next, the hexane layer was concentrated to 0.5 mL or less, and made up to 10 mL with a GPC eluent (ethyl acetate: cyclohexane = 3: 7) to prepare a pretreatment solution.
前処理液2mLを注射筒でGPC装置に注入して分画を行なった。約30mLの溶出液(18〜25分間)をPCB画分として分取し、濃縮後にGPC溶離液で1mLに定容してGC/ECD分析に供した。GPC分画条件を以下に示す。また、GC/ECD分析には、InnertCap−1カラム(長さ30m、膜圧1.5μm、内径0.53mm)を使用した。 Fractionation was performed by injecting 2 mL of the pretreatment liquid into the GPC apparatus with a syringe. About 30 mL of the eluate (18 to 25 minutes) was collected as a PCB fraction, concentrated and then made up to 1 mL with the GPC eluent and subjected to GC / ECD analysis. The GPC fractionation conditions are shown below. For GC / ECD analysis, an InnerCap-1 column (length 30 m, membrane pressure 1.5 μm, inner diameter 0.53 mm) was used.
−GPC分画条件−
プレカラム:CLNpak EV−G, 20φ×100mm
分取カラム:CLNpak EV−2000, 20φ×300mm
溶離液:酢酸エチル:シクロヘキサン=3:7
溶離速度:4.2mL/min
-GPC fractionation conditions-
Precolumn: CLNpak EV-G, 20φ × 100mm
Preparative column: CLNpak EV-2000, 20φ × 300mm
Eluent: Ethyl acetate: Cyclohexane = 3: 7
Elution rate: 4.2 mL / min
図14は、循環洗浄時における油中のPCB濃度変化を示すグラフである。なお、図14中における点線枠内は、油を加熱した期間を示す。
油の循環洗浄を開始した時点から経時的に油を採取し、採取した試料について油中総PCB濃度をバイオセンサーとGPC/GC/ECDにより決定した。バイオセンサーの測定結果から、循環洗浄を開始して20時間後に油中総PCB濃度は、約0.2mg−PCB/kg−Oilとなった。その後、油中総PCB濃度は、60時間後にほぼ一定となった。そこで、98時間後から105時間後までの期間に加温して循環洗浄を行った結果、加温期間中に急激な油中総PCB濃度の増加が観察された。しかし、119時間後から127時間後までの期間に再び加温して循環洗浄を行ったところ、油中総PCB濃度の増加は見られなかった。油中総PCB濃度の確認として行ったGPC/GC/ECDの測定結果も、上記のバイオセンサーの測定結果と同様な傾向が見られた。
図15は、循環洗浄時における油の温度の経時変化を示すグラフであり、図16は、循環洗浄時における油の流速の経時変化を示すグラフである。なお、図15及び図16中における点線枠内は、油を加熱した期間を示す。
図15及び図16に示すように、循環洗浄を行った全期間において、油の流速は2.0mL/min前後の範囲で一定であり、循環条件としては温度だけが変化したことを確認した。
以上の結果から、本実験の条件下(循環流速2.0mL/min)では、油温30〜40℃で循環洗浄を行った場合には、約60時間後にリアクトルから循環油へのPCBの浸出が停止すること。また、油温を90℃まで昇温することにより、PCBの浸出が促進されることが分かった。さらに、この促進効果は、約7時間の昇温時間内に得られ、それ以上加温時間を延長してもPCBの浸出には寄与しないことが示唆された。
なお、油温の上昇によるPCB浸出の促進は、油粘度の低下に基づく被洗浄部材の表面における油交換率の上昇によるものと考えられる。すなわち、加熱によって循環油の粘度を低下させ、変圧器を構成する変圧器容器内壁及び内部部材に付着あるいは浸透したPCB自身、またはPCBを含む汚染油の注入油との交換を促す原理によって効果を得る洗浄方法である。
FIG. 14 is a graph showing changes in PCB concentration in oil during circulation cleaning. In addition, the inside of the dotted line frame in FIG. 14 shows the period which heated oil.
The oil was collected over time from the start of oil circulation cleaning, and the total PCB concentration in the oil was determined by a biosensor and GPC / GC / ECD for the collected sample. From the measurement results of the biosensor, the total PCB concentration in oil was about 0.2 mg-PCB / kg-Oil 20 hours after the start of the circulation cleaning. Thereafter, the total PCB concentration in the oil became almost constant after 60 hours. Therefore, as a result of heating and circulating cleaning in the period from 98 hours to 105 hours, a sudden increase in total PCB concentration in oil was observed during the heating period. However, when the circulation cleaning was performed by heating again during the period from 119 hours to 127 hours, no increase in the total PCB concentration in the oil was observed. The GPC / GC / ECD measurement results performed as confirmation of the total PCB concentration in the oil also showed the same tendency as the biosensor measurement results.
FIG. 15 is a graph showing the change with time of the oil temperature during the circulation cleaning, and FIG. 16 is a graph showing the change with time of the oil flow rate during the circulation cleaning. In addition, the inside of the dotted line frame in FIG.15 and FIG.16 shows the period which heated oil.
As shown in FIG. 15 and FIG. 16, it was confirmed that the oil flow rate was constant in the range of around 2.0 mL / min throughout the period of the circulation cleaning, and only the temperature was changed as the circulation condition.
From the above results, under the conditions of this experiment (circulation flow rate of 2.0 mL / min), when circulating cleaning was performed at an oil temperature of 30 to 40 ° C., PCB leaching from the reactor to the circulating oil after about 60 hours To stop. Moreover, it turned out that the leaching of PCB is accelerated | stimulated by heating up oil temperature to 90 degreeC. Furthermore, this promoting effect was obtained within a heating time of about 7 hours, and it was suggested that extending the heating time further does not contribute to PCB leaching.
The promotion of PCB leaching due to an increase in oil temperature is considered to be due to an increase in the oil exchange rate on the surface of the member to be cleaned due to a decrease in oil viscosity. That is, the effect is achieved by the principle of encouraging replacement of the circulating oil with heating by reducing the viscosity of the circulating oil and the PCB itself adhering to or penetrating the inner wall and internal members of the transformer, or contaminated oil containing PCB. It is a cleaning method to obtain.
<<<高分解能ガスクロマトグラフ−高分解能質量分析計を用いた油のPCB濃度分析>>>
後述する表1における油(元油)中のPCB濃度分析は、「特別管理一般廃棄物及び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)別表第二(廃油中PCB分析方法)(図10)に準じて行った。なお、測定に使用した装置は、高分解能ガスクロマトグラフ−高分解能質量分析計(HRGC:HP6890N、Agilent社製、HRMS:AutoSpec NTS、Micromass社製)である。
<<< High-resolution gas chromatograph-PCB concentration analysis of oil using high-resolution mass spectrometer >>>
The PCB concentration analysis in oil (base oil) in Table 1 described later is the “Test method for standards pertaining to specially managed general waste and specially controlled industrial waste” (Ministry of Health, Welfare Notification No. 192), Schedule 2 ( This was performed according to the method for analyzing PCBs in waste oil) (FIG. 10). In addition, the apparatus used for the measurement is a high resolution gas chromatograph-high resolution mass spectrometer (HRGC: HP6890N, manufactured by Agilent, HRMS: AutoSpec NTS, manufactured by Micromass).
<<洗浄前の変圧器部材採取>>
小型リアクトルの蓋部及びコアを吊り上げて外缶容器から取り出し、そのまま数時間放置した。放置後に電動鋸にてコアを一部切断した。切断した部材は、材料別に分けてPCB濃度分析用試料とした。具体的には、コアの銅線コイルからは薄紙(銅線に巻きついていた絶縁用紙)と銅線(薄紙を取り除いた金属銅)を分別して採取した。また、コイル間のスペーサーとして使用されていた厚紙も採取した。なお、この時、外缶容器の内壁についても別表第三の第二(拭き取り試験法)(図11)に従ってPCB濃度分析用試料を採取した。
<< Collecting transformer parts before cleaning >>
The lid and core of the small reactor were lifted and removed from the outer can container, and left as it was for several hours. After leaving, a part of the core was cut with an electric saw. The cut members were divided into materials and used as PCB concentration analysis samples. Specifically, thin paper (insulating paper wound around the copper wire) and copper wire (metal copper with the thin paper removed) were collected from the core copper wire coil. Cardboard used as a spacer between the coils was also collected. At this time, a sample for PCB concentration analysis was also collected from the inner wall of the outer can container in accordance with the second (wiping test method) (Table 11) of the third table.
<<洗浄後の変圧器部材採取>>
小型リアクトルと洗浄装置との接続配管を撤去した後、蓋部、コア、及び外缶容器を洗浄装置の油飛散防止容器から取り外した。その後、数時間放置した。放置後に、コアを取り出し、電動鋸にて一部切断した。切断した部材は、前記と同様に材料別に分けてPCB濃度分析用試料とした。また、外缶容器の内壁についても別表第三の第二(拭き取り試験法)(図11)に従ってPCB濃度分析用試料を採取した。
さらに、コアを完全に分解し、中心部の鉄芯として積層された鉄板を採取して、別表第三の第二(拭き取り試験法)(図11)を実施した。同様に、鉄枠として積層された鉄板も、取り分け、別表第三の第二(拭き取り試験法)(図11)に従ってPCB濃度分析用試料を採取した。また、ベークライトからも別表第三の第二(拭き取り試験法)(図11)に従ってPCB濃度分析用試料を採取した。
<<変圧器部材のPCB濃度分析>>
変圧器部材のPCB濃度分析は、特別管理一般廃棄物及び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)に記載された方法に従って前処理を行い、以下に記載の測定装置により分析を行った。
外缶容器に付着したPCBは、別表第三の第二(拭き取り試験法)(図11)に従い前処理を行い、低分解能質量分析(LRGC/LRMS)にてPCBの定量を行った。コイルから採取した銅線及び紙類(厚紙及び薄紙)は、それぞれ別表第三の第三(図13)及び別表第四(図12)に従い前処理を行い、低分解能質量計にてPCBの定量を行った。
一方、鉄芯、鉄枠及びベークライトは、別表第三の第二(拭き取り試験法)(図11)に従い前処理を行った。
<< Collecting transformer parts after cleaning >>
After removing the connecting piping between the small reactor and the cleaning device, the lid, the core, and the outer can container were removed from the oil scattering prevention container of the cleaning device. Then, it was left for several hours. After leaving, the core was taken out and partly cut with an electric saw. The cut members were divided into materials as described above and used as PCB concentration analysis samples. In addition, a sample for PCB concentration analysis was also collected from the inner wall of the outer can container in accordance with the second (wiping test method) (Table 11) of Appendix 3.
Further, the core was completely disassembled, and the iron plates laminated as the iron core in the center were collected, and the second (wiping test method) of Appendix Table 3 was performed (FIG. 11). Similarly, the iron plate laminated | stacked as an iron frame was separated, and the sample for PCB density | concentration analysis was extract | collected according to the 2nd (wiping test method) of the attached table 3 (FIG. 11). Further, a sample for PCB concentration analysis was also collected from bakelite according to the second (wiping test method) of Appendix Table 3 (FIG. 11).
<< PCB concentration analysis of transformer members >>
PCB concentration analysis of transformer members is pre-processed according to the method described in the standard verification method for specially managed general waste and specially controlled industrial waste (Ministry of Health and Welfare Notification No. 192). The analysis was performed using a measuring apparatus.
The PCB adhering to the outer can container was pretreated according to the second (wiping test method) (Fig. 11) of Appendix 3, and the PCB was quantified by low resolution mass spectrometry (LRGC / LRMS). Copper wires and papers (thick paper and thin paper) collected from the coil are pretreated according to the third (Fig. 13) and fourth (Fig. 12) of Appendix Table 3, respectively, and the PCB is quantified with a low-resolution mass meter. Went.
On the other hand, the iron core, the iron frame, and the bakelite were pretreated in accordance with the second (wiping test method) of Appendix Table 3 (FIG. 11).
循環洗浄前後の外缶容器の内壁及び内部部材に残留するPCB濃度を測定した。その結果を表1に示す。なお、分析は、記載した前処理法にて行い、測定には全て低分解能質量分析計を使用した。 The PCB concentration remaining on the inner wall and inner member of the outer can container before and after circulation cleaning was measured. The results are shown in Table 1. The analysis was performed by the pretreatment method described, and a low-resolution mass spectrometer was used for all measurements.
外缶容器の内壁に付着したPCBは、別表第三の第二(拭き取り試験)(図11)に従い前処理を行い分析した。拭き取り試験では、有機溶媒を含む脱脂綿で金属表面を拭き取るため、外缶容器の内壁面に表面に付着したPCBを油成分とともに回収できる。循環洗浄前では、PCBの付着量は0.34μg−PCB/100cm2−表面積であったが、循環洗浄後には、0.007μg−PCB/100cm2−表面積となり、顕著な洗浄効果が認められた。PCB無害化処理における拭き取り試験の判定基準(図17)は0.1μg−PCB/100cm2−表面積以下であることから、容器に関しては、油の循環により、少なくとも拭き取り試験の判定基準(図17)を満足する濃度までPCBを洗浄除去できると考えられた。また、洗浄による二次汚染も見られなかった。 The PCB adhering to the inner wall of the outer can container was subjected to pretreatment according to the second (wiping test) (Fig. 11) of Appendix Table 3 and analyzed. In the wiping test, the metal surface is wiped off with absorbent cotton containing an organic solvent, so that the PCB attached to the inner wall surface of the outer can container can be recovered together with the oil component. Before the circulation cleaning, the amount of PCB adhered was 0.34 μg-PCB / 100 cm 2 -surface area, but after the circulation cleaning, it became 0.007 μg-PCB / 100 cm 2 -surface area, and a remarkable cleaning effect was recognized. . Since the judgment standard (FIG. 17) of the wiping test in the PCB detoxification treatment is 0.1 μg-PCB / 100 cm 2 -the surface area or less, the judgment criterion of the wiping test is at least due to the circulation of the oil (FIG. 17). It was thought that PCB could be removed by washing to a concentration satisfying the above. In addition, secondary contamination due to washing was not observed.
コイルから採取した銅線に付着したPCBは、別表第三の第三(部材採取試験)(図13)に従い前処理を行い分析した。部材採取試験では、PCBが溶解しやすい有機溶媒で部材を洗浄するため、部材表面あるいは内部に付着したPCBも回収できる。しかし、循環洗浄前後においてPCBの付着量は、0.01mg−PCB/kg−部材未満であった。PCB無害化処理における部材採取試験の判定基準(図17)は、0.01mg−PCB/kg−部材以下である。従って、コイルから採取した銅線に関しては、循環洗浄前後において、少なくとも部材採取試験の判定基準(図17)を超えるPCBの付着は認められなかった。また、洗浄による二次汚染も見られなかった。 PCB attached to the copper wire sampled from the coil was analyzed by pretreatment according to the third (member sampling test) of the third table (FIG. 13). In the member sampling test, since the member is washed with an organic solvent in which PCB easily dissolves, PCB attached to the surface or inside of the member can also be recovered. However, the amount of PCB adhered before and after the circulation cleaning was less than 0.01 mg-PCB / kg-member. The criterion (FIG. 17) of the member sampling test in the PCB detoxification process is 0.01 mg-PCB / kg-member or less. Therefore, with respect to the copper wire collected from the coil, no PCB adhesion exceeding at least the judgment standard of the member sampling test (FIG. 17) was observed before and after the circulation cleaning. In addition, secondary contamination due to washing was not observed.
銅線コイルに巻きつけられていた薄紙及び銅線コイルの隙間材として使用されていた厚紙に含有されていたPCBは、別表第四(図12)に従い前処理を行い分析した。別表第四(図12)は、部材から水へのPCBの溶出を見積もることを目的とした前処理法である。その結果、循環洗浄前後のコイルから採取した薄紙及び厚紙から水へのPCBの溶出は認められず、PCB濃度は0.003mg−PCB/L−検液未満であった。PCB無害化処理における紙くずの判定基準(図17)は、0.003mg−PCB/L−検液以下である。このことから、紙類に関しては、循環洗浄前後において、少なくとも別表第四の判定基準(図17)を超えるPCBの検液への溶出は認められなかった。また、洗浄による二次汚染も見られなかった。 The PCB contained in the thin paper wound around the copper wire coil and the cardboard used as the gap material of the copper wire coil was subjected to pretreatment according to Attached Table 4 (FIG. 12) and analyzed. Attached Table No. 4 (FIG. 12) is a pretreatment method for the purpose of estimating the dissolution of PCB from a member into water. As a result, no elution of PCB from the thin paper and the thick paper collected from the coil before and after the circulation cleaning to the water was observed, and the PCB concentration was less than 0.003 mg-PCB / L-test solution. The criterion for waste paper in the PCB detoxification process (FIG. 17) is 0.003 mg-PCB / L-test solution or less. From this, with respect to paper, before and after the circulation cleaning, at least elution of PCB in the test solution exceeding the fourth criterion (FIG. 17) was not recognized. In addition, secondary contamination due to washing was not observed.
以上、外缶容器、コイルから採取した銅線及び紙(厚紙及び薄紙)については、循環洗浄によるPCBの除去効果が明らかとなった。そこで、洗浄効果を確かめる目的で、循環洗浄後の鉄芯、鉄枠、及びベークライトについてもPCB濃度を測定した。試料としては、小型リアクトルのコアを解体し、コア中心部の鉄芯として積層された鉄板を採取した。同様に、鉄枠として積層された鉄板も、取り分けた。さらに、鉄芯の構成物であったベークライトもPCB濃度分析用試料として採取した。以上、採取した分析試料は、記載した前処理法にて行い、電子捕獲検出付きガスクロマトグラフィーで分析を行った。その結果を表1に示す。 As mentioned above, the removal effect of PCB by circulation washing became clear about copper wire and paper (thick paper and thin paper) collected from an outer can container and a coil. Therefore, for the purpose of confirming the cleaning effect, the PCB concentration was also measured for the iron core, iron frame, and bakelite after circulation cleaning. As a sample, a core of a small reactor was disassembled, and an iron plate stacked as an iron core at the center of the core was collected. Similarly, iron plates stacked as iron frames were also arranged. Furthermore, bakelite, which was a component of an iron core, was also collected as a sample for PCB concentration analysis. As described above, the collected analysis samples were analyzed by the described pretreatment method and analyzed by gas chromatography with electron capture detection. The results are shown in Table 1.
鉄芯及び鉄枠に付着したPCBは、別表第三の第二(拭き取り試験)(図11)に従い前処理を行い分析した。その結果、循環洗浄後の鉄芯及び鉄枠については、0.1μg−PCB/100cm2−表面積未満であった。PCB無害化処理における拭き取り試験の判定基準(図17)は、0.1μg−PCB/100cm2−表面積以下である。このことから、鉄芯及び鉄枠に関しては、油の循環により、少なくとも拭き取り試験の判定基準(図17)を満足する濃度までPCBを洗浄除去できた。 The PCB attached to the iron core and the iron frame was analyzed by pretreatment according to the second (wiping test) of the third table (FIG. 11). As a result, the iron core and the iron frame after the circulation cleaning were less than 0.1 μg-PCB / 100 cm 2 -surface area. The criterion for the wiping test in the PCB detoxification treatment (FIG. 17) is 0.1 μg-PCB / 100 cm 2 -surface area or less. From this, with respect to the iron core and the iron frame, the PCB could be washed and removed to a concentration satisfying at least the criteria for the wiping test (FIG. 17) by circulating the oil.
ベークライトに付着したPCBは、別表第三の第二(拭き取り試験)(図11)に従い前処理を行い分析した。その結果、PCB付着量は0.1μg−PCB/100cm2−表面積未満であった。従って、循環洗浄後にベークライトに付着しているPCB量は、PCB無害化処理における拭き取り試験の判定基準(図17)である0.1μg−PCB/100cm2−表面積以下を満足した。 The PCB adhering to the bakelite was subjected to pretreatment according to the second (wiping test) of the third table (FIG. 11) and analyzed. As a result, the PCB adhesion amount was less than 0.1 μg-PCB / 100 cm 2 -surface area. Therefore, the amount of PCB adhering to the bakelite after the circulation cleaning satisfied 0.1 μg-PCB / 100 cm 2 -surface area or less, which is a judgment standard (FIG. 17) of the wiping test in the PCB detoxification process.
上述の結果から、PCB汚染油(総PCB濃度20.7mg/kg)を小型リアクトルから抜油し、小型リアクトル内にPCBを含まない油を注入して循環洗浄した結果、油温30〜40℃で循環洗浄を行った場合には、約60時間後に小型リアクトルから循環油へのPCBの浸出が停止すること。また、油温を90℃まで昇温することにより、PCBの浸出が促進されることが分かった。 From the above results, the PCB contaminated oil (total PCB concentration 20.7 mg / kg) was extracted from the small reactor, and the oil not containing PCB was injected into the small reactor and circulated and washed. When circulating cleaning is performed, the leaching of PCB from the small reactor to the circulating oil should stop after about 60 hours. Moreover, it turned out that the leaching of PCB is accelerated | stimulated by heating up oil temperature to 90 degreeC.
また、上記の循環洗浄により、小型リアクトルの外缶容器については、PCB無害化処理における別表第三の第二(拭き取り試験)の判定基準(図17)を満足する濃度までPCBを洗浄除去できると考えられた。また、小型リアクトルのコアを構成する部材であるコイルから採取した銅線については、循環洗浄前後において、PCB無害化処理における別表第三の第三(部材採取試験)の判定基準(図17)を超えるPCBの付着は認められなかった。コイルから採取した紙類についても、循環洗浄前後において、PCB無害化処理における別表第四の判定基準(図17)を超えるPCBの検液への溶出は認められなかった。 In addition, with the above-described circulation cleaning, for the outer can container of the small reactor, the PCB can be cleaned and removed to a concentration that satisfies the second criterion (wiping test) of the third table (wiping test) in the PCB detoxification process (FIG. 17). it was thought. In addition, for copper wire sampled from a coil that is a member constituting a core of a small reactor, the third (member sampling test) judgment standard (FIG. 17) in the third table of the PCB detoxification process is performed before and after circulation cleaning. Excess PCB adhesion was not observed. Regarding the papers collected from the coil, the PCB elution into the test solution exceeding the fourth criterion (Figure 17) in the PCB detoxification treatment was not observed before and after the circulation cleaning.
加えて、小型リアクトルのコアを構成する鉄芯及び鉄枠については、循環洗浄後には、PCB無害化処理における別表第三の第二(拭き取り試験)の判定基準(図17)を超えるPCBの付着は認められなかった。同様に、ベークライトについても、循環洗浄後には、別表第三の第二(拭き取り試験)の判定基準(図17)を超えるPCBの付着は認められなかった。 In addition, with regard to the iron core and iron frame constituting the core of the small reactor, after circulation cleaning, PCB adhesion exceeding the second (wiping test) judgment standard (Fig. 17) in the third table of PCB detoxification treatment Was not recognized. Similarly, with regard to bakelite, no adhesion of PCB exceeding the second (wiping test) judgment standard (FIG. 17) in the third table was observed after circulation cleaning.
(原理確認試験)
本研究により、PCBに汚染された絶縁油を絶縁油が封入された変圧器から抜油し、PCBに汚染されてない新油を注入・循環させることにより変圧器内壁及び内部部材に付着・浸透したPCBを洗浄できることが明らかとなった。この際、循環させる新油を加温することで、高いPCBの洗浄効果が得られることも確かめられた、しかしながら、その科学的根拠については不明である。そこで、本項では、油温の上昇に伴う循環油粘度の減少に着目し、循環油粘度の減少と洗浄効果との関係について検討することとした。
(Principle confirmation test)
In this research, insulating oil contaminated with PCB was removed from the transformer filled with insulating oil, and new oil not contaminated with PCB was injected and circulated to adhere to and penetrate the inner wall and internal members of the transformer. It became clear that the PCB could be washed. At this time, it was confirmed that a high PCB cleaning effect can be obtained by heating the new oil to be circulated. However, the scientific basis is unknown. Therefore, in this section, we focused on the decrease in the circulating oil viscosity accompanying the increase in the oil temperature, and examined the relationship between the decrease in the circulating oil viscosity and the cleaning effect.
<部材>
原理確認試験には、変圧器(100kVA)から採取した紙類を用いた。採取した紙試料は、約5mm四方に切断して実験に供した。
<Member>
For the principle confirmation test, papers collected from a transformer (100 kVA) were used. The collected paper sample was cut into a square of about 5 mm and used for the experiment.
<油中PCB分析>
油中の総PCB濃度は、上述したバイオセンサーを用いた油のPCB濃度分析により測定した。
<Analysis of PCB in oil>
The total PCB concentration in the oil was measured by PCB concentration analysis of the oil using the biosensor described above.
<粘度測定>
粘度測定には、AND社 SV-10型粘度計を使用した。まず、30℃〜90℃までの温度制御が可能な湯浴インキュベータを用意した。30℃に設定したインキュベータ中に粘度測定容器を浸し、油試料の40mLを入れた。さらに、測定部を試料に浸して試料の温度が30℃になった後、測定を開始した。経時的に温度を90℃まで上昇させ、その間粘度測定を継続して行った。試料として使用した油試料は、シリコーンオイル(KF−96L−2C、KF−96−10CS、及びKF-96−100CS、全て信越化学工業株式会社製)、絶縁油(電気絶縁油1種2号、松村石油株式会社製)、植物油(サラダ油)(市販品、味の素株式会社製)、及び灯油である。
<Viscosity measurement>
For the viscosity measurement, an SV-10 viscometer manufactured by AND was used. First, a hot water bath incubator capable of temperature control from 30 ° C. to 90 ° C. was prepared. The viscosity measurement container was immersed in an incubator set at 30 ° C., and 40 mL of an oil sample was placed therein. Furthermore, the measurement was started after the measurement part was immersed in the sample and the temperature of the sample reached 30 ° C. The temperature was raised to 90 ° C. over time, and the viscosity measurement was continued during that time. The oil samples used as samples were silicone oil (KF-96L-2C, KF-96-10CS, and KF-96-100CS, all manufactured by Shin-Etsu Chemical Co., Ltd.), insulating oil (electric insulating oil type 1 No. 2, Matsumura Oil Co., Ltd.), vegetable oil (salad oil) (commercial product, Ajinomoto Co., Inc.), and kerosene.
<溶出試験>
上記の各種油50mLを100mL容量の三角フラスコに入れ、30℃〜70℃までの温度制御が可能なインキュベータに格納した。設定したインキュベータ内温度と油温が一定になった段階で、上記の紙試料10gを投入して試験を開始した。試験時間内はフラスコを随時攪拌しながら経時的に油試料の1mLを採取した。これらの採取試料をバイオセンサーに供して油中総PCB濃度を決定した。
<Dissolution test>
50 mL of each of the above oils was placed in a 100 mL Erlenmeyer flask and stored in an incubator capable of temperature control from 30 ° C to 70 ° C. When the set incubator temperature and oil temperature became constant, 10 g of the paper sample was added and the test was started. During the test time, 1 mL of an oil sample was collected over time while stirring the flask as needed. These collected samples were subjected to a biosensor to determine the total PCB concentration in oil.
<試験結果>
−加温による溶出促進効果−
変圧器では、循環油を70℃あるいは90℃まで加温することで部材からのPCBの溶出が促進し、循環油中のPCB濃度の増加が観察された。同様の現象が、本実験からも確かめられた。すなわち、PCB汚染紙を絶縁油に浸漬してPCBの溶出を油中のPCB濃度を測定することで観察したところ、油温度30℃で溶出(浸漬)を開始した場合には、ほぼ7時間程度で溶出速度は減少した(油中総PCB濃度がほぼ一定となる)。しかし、9時間以降に90℃までの加温を開始したところ、PCB溶出の促進を示す油中PCB濃度の増加が見られた(図18A)。そこで、油温度70℃にて溶出試験を行ったところ、高いPCB溶出促進が油中PCB濃度の増加から示された(図18B)。以上の結果から、加温によるPCB促進効果は粘度低下による油相交換に起因すると予想した。実際、絶縁油の粘度を油温毎に測定したところ、30℃から70℃の昇温により8.8mPa・sから2.9mPa・sまで低下することがわかった(図19A及びB)。
次に、PCB溶出促進効果が絶縁油中の特殊な成分などに起因するどうかを確かめるため、油成分の化合構造が大きく異なる植物(サラダ)油を用いて加温による粘度変化によってPCB促進効果が見られるか否かを確認した。30℃、45℃及び70℃に加温し、それぞれ経時的にPCB溶出濃度を測定したところ、溶出量は温度が高い順に多くなった(図20)。なお、植物油の粘度は、30℃で40.3mPa・s、45℃で23.3mPa・s、70℃で11.4mPa・sである(図19A及びB)。従って、PCB溶出促進効果は、絶縁油中の特殊な化学成分よりも洗浄する油の粘度の低下によって得られると考えられた。
もし、粘度の低下によりPCBの促進効果が得られるならば、同温度条件で元々粘度の異なる油であれば、加温することなく同様な効果が見られるはずである。そこで、合成油であるシリコーンオイルを使って油温70℃にてPCB汚染紙からのPCB溶出試験を行った(図21)。シリコーンオイルを選択した理由は、第一に異なる粘度の油が入手できること、第二に絶縁油とは組成が異なる合成油でも同様な促進効果を確かめるためである。その結果、PCBの溶出効果は、粘度の低い順に高くなることがわかった。70℃におけるシリコーンオイルの粘度は図19A及びBに示した。70℃における各シリコーンオイルの粘度は、Aが0.9mPa・s、Bが3.8mPa・s、Cが39.3mPa・sである。以上、PCB溶出は、同温度条件下で油の粘度の違いにより差が見られた。このことから、加温によって得られる変圧器のPCB汚染部材からの絶縁油への溶出促進効果は、少なくとも油の粘度低下により部材中の汚染油と洗浄油の交換が活性化する作用が関与することが明らかとなった。この作用は、絶縁油や植物油において同じ油を加温によって粘度を変化させた場合に絶縁油粘度とPCB溶出濃度の間に直線関係が成立することからも裏付けられた。さらに、同じ温度で粘度の異なるシリコーンオイルを洗浄油に用いた場合にも、油粘度とPCB溶出濃度の間に直線関係が見られ、先の作用を確認する結果となった。
一方、PCB溶出量が浸漬油粘度にのみ支配されるのであれば、同じ粘度の洗浄油であれば油種に関わらずPCB溶出効果は同程度である。しかし、絶縁油、植物油及びシリコーンオイルでは、粘度とPCB溶出濃度の間に成立する直線関係の傾きや位置に差があった(図22)。これらの結果は、PCB溶出効果は粘度低下による油相交換の活性化によって起こるが、活性化の度合いは部材中の汚染油と洗浄油との混和のし易さにも影響されると考えられた。
そこで、絶縁油と混和しやすい灯油を用いて30℃にて溶出試験を行った。灯油は、絶縁油に比し粘度が低く、30℃では0.83mPa・s (図19A及びB)である。従って、粘度が低くかつ絶縁油と混和しやすい灯油では高い溶出効果が期待でき、実際30℃における同じ浸漬時間では、絶縁油の約2倍の油中総PCB濃度が観測された(図23)。
<Test results>
-Elution promotion effect by heating-
In the transformer, elution of PCB from the member was promoted by heating the circulating oil to 70 ° C. or 90 ° C., and an increase in PCB concentration in the circulating oil was observed. A similar phenomenon was confirmed from this experiment. That is, when PCB-contaminated paper was immersed in insulating oil and PCB elution was observed by measuring the PCB concentration in the oil, when elution (immersion) was started at an oil temperature of 30 ° C., about 7 hours. The elution rate decreased (total PCB concentration in oil became almost constant). However, when heating up to 90 ° C. was started after 9 hours, an increase in PCB concentration in oil showing promotion of PCB elution was observed (FIG. 18A). Therefore, when an elution test was performed at an oil temperature of 70 ° C., high PCB elution acceleration was shown from an increase in the PCB concentration in the oil (FIG. 18B). From the above results, it was predicted that the PCB acceleration effect by heating was caused by the oil phase exchange due to the decrease in viscosity. In fact, when the viscosity of the insulating oil was measured at each oil temperature, it was found that the temperature decreased from 8.8 mPa · s to 2.9 mPa · s with a temperature increase from 30 ° C. to 70 ° C. (FIGS. 19A and B).
Next, in order to ascertain whether the PCB elution promoting effect is caused by special components in the insulating oil, the PCB promoting effect is obtained by the viscosity change due to heating using a vegetable (salad) oil having a significantly different compound structure of the oil component. It was confirmed whether it was seen or not. When the PCB elution concentration was measured over time after heating to 30 ° C., 45 ° C. and 70 ° C., the elution amount increased in descending order of temperature (FIG. 20). The viscosity of the vegetable oil is 40.3 mPa · s at 30 ° C., 23.3 mPa · s at 45 ° C., and 11.4 mPa · s at 70 ° C. (FIGS. 19A and B). Therefore, it was considered that the PCB elution promoting effect was obtained by lowering the viscosity of the washing oil rather than the special chemical component in the insulating oil.
If a PCB promoting effect can be obtained by lowering the viscosity, an oil having an originally different viscosity under the same temperature condition should have the same effect without heating. Therefore, a PCB elution test from PCB-contaminated paper was performed using silicone oil, which is a synthetic oil, at an oil temperature of 70 ° C. (FIG. 21). The reason why the silicone oil was selected is that oils having different viscosities can be obtained first, and secondly, the same accelerating effect can be confirmed even with synthetic oils having a composition different from that of the insulating oil. As a result, it was found that the PCB elution effect increased in order of increasing viscosity. The viscosity of the silicone oil at 70 ° C. is shown in FIGS. The viscosity of each silicone oil at 70 ° C. is 0.9 mPa · s for A, 3.8 mPa · s for B, and 39.3 mPa · s for C. As described above, the PCB elution was different due to the difference in the viscosity of the oil under the same temperature condition. From this, the effect of promoting the elution from the PCB contaminated member of the transformer to the insulating oil obtained by heating involves the activation of at least the exchange of the contaminated oil and the cleaning oil in the member due to the decrease in the viscosity of the oil. It became clear. This effect was supported by the fact that a linear relationship was established between the insulating oil viscosity and the PCB elution concentration when the viscosity of the insulating oil or vegetable oil was changed by heating. Furthermore, when silicone oils having different viscosities at the same temperature were used as the cleaning oil, a linear relationship was observed between the oil viscosity and the PCB elution concentration, confirming the previous action.
On the other hand, if the PCB elution amount is governed only by the immersion oil viscosity, the PCB elution effect is the same regardless of the oil type if the cleaning oil has the same viscosity. However, in the insulating oil, vegetable oil, and silicone oil, there was a difference in the slope and position of the linear relationship established between the viscosity and the PCB elution concentration (FIG. 22). These results indicate that the PCB elution effect is caused by the activation of oil phase exchange due to a decrease in viscosity, but the degree of activation is considered to be affected by the ease of mixing the contaminated oil in the member with the cleaning oil. It was.
Then, the elution test was done at 30 degreeC using the kerosene which is easy to mix with insulating oil. Kerosene has a lower viscosity than insulating oil and is 0.83 mPa · s at 30 ° C. (FIGS. 19A and B). Therefore, a high elution effect can be expected with kerosene having a low viscosity and easy to mix with insulating oil. In fact, a total PCB concentration in oil approximately twice that of insulating oil was observed at the same immersion time at 30 ° C. (FIG. 23). .
本発明のPCB汚染変圧器の洗浄方法は、0.5t未満の小型変圧器(例えば、電柱に設置された変圧器)や、0.5t以上30t未満の中型変圧器(例えば、変電所に設置された変圧器)や、30t以上の大型変圧器(例えば、発電所に設置された変圧器)のPCB洗浄に好適に使用することができる。 The method for cleaning a PCB-contaminated transformer of the present invention is a small transformer of less than 0.5t (for example, a transformer installed on a power pole) or a medium-sized transformer of 0.5t or more but less than 30t (for example, installed in a substation) Can be suitably used for PCB cleaning of large transformers (for example, transformers installed in power plants) of 30 tons or more.
1 蓋部
2 外缶容器
3 内部部材(コア)
4 鉄芯
5 コイル
6 ベークライト
7 鉄枠
8 銅線
9 薄紙
10 厚紙
11 布
80 洗浄装置
81 油飛散防止容器
82 送液ポンプ
83 冷却器
84 本加熱槽
85 予熱加熱槽
86 温度計
87 積算流量計
88 窒素ガスライン
89 圧力計
90 サンプリングライン
91 第1の配管(吸入口)
92 第2の配管(吐出口)
93 第3の配管(排出口)
100 変圧器
1 Lid 2 Outer can 3 Internal member (core)
4 Iron core 5 Coil 6 Bakelite 7 Iron frame 8 Copper wire 9 Thin paper 10 Thick paper 11 Cloth 80 Cleaning device 81 Oil scattering prevention container 82 Liquid feed pump 83 Cooler 84 Main heating tank 85 Preheating heating tank 86 Thermometer 87 Integrated flow meter 88 Nitrogen gas line 89 Pressure gauge 90 Sampling line 91 First pipe (suction port)
92 Second piping (discharge port)
93 3rd piping (discharge port)
100 transformer
Claims (18)
前記注入された油の温度が40〜90℃となるように該油を加熱する加熱工程を含み、
洗浄後の変圧器部材が、「特別管理一般廃棄物及び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)別表第三の第二(拭き取り試験)の判定基準、同別表第三の第三(部材採取試験)の判定基準、及び同別表第四の判定基準をいずれも満たすことを特徴とするPCB汚染変圧器の洗浄方法。 PCB contaminated transformer that does not contain polychlorinated biphenyl in the PCB contaminated transformer contaminated with polychlorinated biphenyl or circulates and cleans by injecting oil whose polychlorinated biphenyl content is within the regulation (standard) range In the cleaning method,
Look including a heating step where the temperature of the injected oil heats the oil so that the 40 to 90 ° C.,
Transformer members after cleaning are judged according to the second (wiping test) in Appendix 3 of the “Examination Method for Standards Related to Specially Managed General Waste and Specially Controlled Industrial Waste” (Ministry of Health and Welfare Notification No. 192) A method for cleaning a PCB-contaminated transformer, characterized by satisfying both the third (member sampling test) judgment standard of the Attached Table 3 and the fourth judgment standard of the Attached Table 4 .
温調された油の温度が、50〜90℃となるように該油を加熱する加熱工程と、を含む請求項1に記載のPCB汚染変圧器の洗浄方法。The method for cleaning a PCB-contaminated transformer according to claim 1, further comprising a heating step of heating the oil so that a temperature of the temperature-controlled oil becomes 50 to 90 ° C.
前記注入された油の温度が40〜90℃となるように該油を加熱する加熱工程を含み、A heating step of heating the oil so that the temperature of the injected oil is 40 to 90 ° C.,
洗浄後の変圧器部材が、「特別管理一般廃棄物及び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)別表第三の第二(拭き取り試験)の判定基準、同別表第三の第三(部材採取試験)の判定基準、及び同別表第四の判定基準をいずれも満たすことを特徴とするPCB汚染変圧器の洗浄方法。Transformer members after cleaning are judged according to the second (wiping test) in Appendix 3 of the “Examination Method for Standards Related to Specially Managed General Waste and Specially Controlled Industrial Waste” (Ministry of Health and Welfare Notification No. 192) A method for cleaning a PCB-contaminated transformer, characterized by satisfying both the third (member sampling test) judgment standard of the Attached Table 3 and the fourth judgment standard of the Attached Table 4.
温調された油の温度が、50〜90℃となるように該油を加熱する加熱工程と、を含む請求項4に記載のPCB汚染変圧器の洗浄方法。The method for cleaning a PCB-contaminated transformer according to claim 4, further comprising: a heating step of heating the oil so that a temperature of the temperature-controlled oil becomes 50 to 90 ° C.
前記油の温度が40〜90℃となるように該油を加熱する加熱手段を備え、A heating means for heating the oil so that the temperature of the oil is 40 to 90 ° C;
洗浄後の変圧器部材が、「特別管理一般廃棄物及び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)別表第三の第二(拭き取り試験)の判定基準、同別表第三の第三(部材採取試験)の判定基準、及び同別表第四の判定基準をいずれも満たすことを特徴とするPCB汚染変圧器の洗浄装置。Transformer members after cleaning are judged according to the second (wiping test) in Appendix 3 of the “Examination Method for Standards Related to Specially Managed General Waste and Specially Controlled Industrial Waste” (Ministry of Health and Welfare Notification No. 192) A cleaning device for a PCB-contaminated transformer, characterized by satisfying both the third (member sampling test) judgment standard of the third table and the fourth judgment standard of the second table.
温調された油の温度が、50〜90℃となるように該油を加熱する加熱手段と、を有する請求項10に記載のPCB汚染変圧器の洗浄装置。The cleaning device for a PCB-contaminated transformer according to claim 10, further comprising a heating unit that heats the temperature-controlled oil so that the temperature of the oil becomes 50 to 90 ° C.
前記油の温度が40〜90℃となるように該油を加熱する加熱手段を備え、A heating means for heating the oil so that the temperature of the oil is 40 to 90 ° C;
洗浄後の変圧器部材が、「特別管理一般廃棄物及び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)別表第三の第二(拭き取り試験)の判定基準、同別表第三の第三(部材採取試験)の判定基準、及び同別表第四の判定基準をいずれも満たすことを特徴とするPCB汚染変圧器の洗浄装置。Transformer members after cleaning are judged according to the second (wiping test) in Appendix 3 of the “Examination Method for Standards Related to Specially Managed General Waste and Specially Controlled Industrial Waste” (Ministry of Health and Welfare Notification No. 192) A cleaning device for a PCB-contaminated transformer, characterized by satisfying both the third (member sampling test) judgment standard of the third table and the fourth judgment standard of the second table.
温調された油の温度が、50〜90℃となるように該油を加熱する加熱手段と、を有する請求項13に記載のPCB汚染変圧器の洗浄装置。The cleaning device for a PCB-contaminated transformer according to claim 13, further comprising a heating unit that heats the temperature-controlled oil so that the temperature of the oil becomes 50 to 90 ° C.
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| JP5163592B2 (en) * | 2009-05-25 | 2013-03-13 | 東京電力株式会社 | Detoxification processing method and detoxification processing system for PCB equipment |
| JP5287505B2 (en) * | 2009-05-27 | 2013-09-11 | 東京電力株式会社 | Detoxification treatment method and detoxification treatment apparatus for organohalogen compound residual equipment |
| JP5654907B2 (en) * | 2011-03-09 | 2015-01-14 | 株式会社神鋼環境ソリューション | Electric equipment regeneration method and electric equipment regeneration apparatus |
| JP5980192B2 (en) * | 2013-11-25 | 2016-08-31 | プリンス海運株式会社 | PCB purification treatment equipment |
| JP6435364B2 (en) * | 2017-03-30 | 2018-12-05 | 株式会社神鋼環境ソリューション | Method of cleaning and detoxifying PCB-contaminated electrical equipment |
| JP6373438B1 (en) * | 2017-03-30 | 2018-08-15 | 株式会社神鋼環境ソリューション | Method of cleaning and detoxifying PCB-contaminated electrical equipment |
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| JP3619198B2 (en) * | 2002-02-05 | 2005-02-09 | 北陸電機製造株式会社 | Method for recovering insulating oil from PCB contaminants |
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| JP3919633B2 (en) * | 2002-08-29 | 2007-05-30 | 株式会社神鋼環境ソリューション | Treatment method and equipment for ballasts, low voltage transformers and capacitors contaminated with polychlorinated biphenyls |
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