JP2006129900A - Method and device for detoxification treatment of pcb-containing oil - Google Patents

Method and device for detoxification treatment of pcb-containing oil Download PDF

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JP2006129900A
JP2006129900A JP2004318865A JP2004318865A JP2006129900A JP 2006129900 A JP2006129900 A JP 2006129900A JP 2004318865 A JP2004318865 A JP 2004318865A JP 2004318865 A JP2004318865 A JP 2004318865A JP 2006129900 A JP2006129900 A JP 2006129900A
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pcb
containing oil
silent discharge
silent
vaporized
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JP4687075B2 (en
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Ryoichi Hanaoka
良一 花岡
Shinzo Takada
新三 高田
Setsu Watanuki
摂 綿貫
Itsuo Jokyo
逸夫 乗京
Shiro Asano
史朗 浅野
Atsushi Obara
敦 小原
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Toshiba Corp
Hokuriku Electric Power Co
Kanazawa Institute of Technology (KIT)
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Toshiba Corp
Hokuriku Electric Power Co
Kanazawa Institute of Technology (KIT)
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<P>PROBLEM TO BE SOLVED: To detoxify PCB-containing oil safely and effectively under the condition of normal temperature and normal pressure with a small environmental load for facilitating the detoxification treatment of the PCB-containing oil with a simple process and a simple device for the detoxification treatment, without much cost for construction or operation of treatment equipment, without using a catalyst or a chemical whose handling is difficult, and without requiring high-temperature treatment. <P>SOLUTION: In the detoxification treatment method, PCB contained in the PCB (perchlorobiphenyls)-containing oil is converted to a harmless substance by atomizing, liquidizing or vaporizing the PCB-containing oil in a detoxification treatment reaction part A1, and letting the atomized, liquidized or vaporized PCB-containing oil flow into a silent discharge space in which a silent discharge system 3 is operated. In other words, PCB is converted to the harmless substance utilizing the oxidation/reduction power generated by the application and desorption of electrons in the silent discharge space. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

この発明は、周知の化学物質PCB(polychlorinated biphenyls=ポリ塩化ビフェニル)を含有する油の無害化処理方法と、その無害化処理方法を実施するPCB含有油の無害化処理装置に関するもので、PCB含有油の噴霧技術と、無声放電(誘電体バリア放電)技術を重畳してPCBを含む油を無害化処理する方法と、その方法でPCB含有油を無害化処理する装置に関するものである。 The present invention relates to a detoxification treatment method for oil containing the well-known chemical substance PCB (polychlorinated biphenyls = polychlorinated biphenyls), and a PCB-containing oil detoxification treatment device for carrying out the detoxification treatment method. The present invention relates to a method for detoxifying oil containing PCB by superimposing oil spraying technology and silent discharge (dielectric barrier discharge) technology, and an apparatus for detoxifying PCB-containing oil by the method.

PCBは、2個のベンゼン環が繋がったビフェニル骨格構造を有してその骨格周囲に配置される水素原子10個のうちの何れかが塩素(Cl)で置換された異性体物質の総称であって、その特性として、高沸点で熱分解し難く化学的に安定である上に高絶縁性、高親油性であることから、過去わが国においても、トランスやコンデンサー等の電気機器の電気絶縁油として、あるいは複写紙の添加物として、あるいは熱媒体や潤滑油として、広範な用途に利用された時期があった。しかし、PCBの人体への有害性が明らかになったことから、1972年にPCBは全面製造中止となり、残存するPCB含有油を高温焼却処理する経緯が一時あったものの、爾来現在まで30余年に亘り残存するPCB含有油は密封状態で継続保管されてきている。しかし、経年に伴う保管施設の老朽化によって、継続保管されているPCB含有油の漏洩が危惧されることから、2001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、以後15年以内にPCBの無害化処理が義務付けられたことから、現在保管されているPCB含有油の無害化処理への対応が急務になってきている。 PCB is a generic name for isomeric substances having a biphenyl skeleton structure in which two benzene rings are connected, and any one of ten hydrogen atoms arranged around the skeleton is substituted with chlorine (Cl). Because of its high boiling point, it is difficult to thermally decompose, is chemically stable, and has high insulation and high lipophilicity, it has been used as an electrical insulation oil for electrical equipment such as transformers and capacitors in Japan. There were times when it was used in a wide range of applications, as an additive for copying paper, or as a heat medium or lubricating oil. However, because the harmful effects of PCBs on the human body became clear, the production of PCBs was completely discontinued in 1972, and there was a history of high-temperature incineration of the remaining PCB-containing oil. The remaining PCB-containing oil has been continuously stored in a sealed state. However, due to concerns over the leakage of PCB-containing oil that has been continuously stored due to aging of storage facilities over time, the “Special Measures Law on Promotion of Proper Treatment of Polychlorinated Biphenyl Waste” was enforced in 2001. Since then, the PCB detoxification process has become obligatory within 15 years, and it has become an urgent need to deal with the detoxification process for PCB-containing oil currently stored.

PCBの無害化処理手法は従来から種々提案されており、それらの手法は次の5種類に大別することもできる。
すなわち、
[A]高温焼却による熱分解法
1200〜1400℃の高温炉内にPCBを噴霧して分解処理することにより、PCBを二酸化炭素、水、無機塩、焼却灰に分解するもので、例えば特開2004−132558号公開特許公報(特許文献1)に示されるように、溶剤にPCBを溶解させたPCB溶液と水を混合してエマルジョンを生成し、水素・酸素ガス発生手段で水の電気分解により発生する水素ガスと酸素ガスとを分離した状態で供給してその水素ガスを酸素ガスで燃焼させる燃焼室内に上記エマルジョンを噴霧することによって、PCBを水素ガスバーナーにより1400℃以上で燃焼させるものが提案されている。
[B]化学的脱塩素化分解法
PCBにアルカリ剤や炭素系触媒を混合させ、常圧下窒素雰囲気中で300〜350℃に加熱し化学反応させることにより、PCB中の塩素を水素などに置換してPCB以外の物質に転換するもので、その処理後に無害なビフェニル化合物と無機塩と水が生成される。そして、例えば特開2003−135621号公開特許公報(特許文献2)に示されるように、PCB、塩素化合物にシリコーンとトルエンを混合撹拌させると共にアルカリ剤の触媒を混合し撹拌することでゲル化が始まることにより、40〜120℃の発熱反応を起こさせて、PCBの脱塩素化を図るものが提案されている。
[C]水熱酸化分解法
水熱酸化分解法には、374℃、218気圧を超えた状態の、いわゆる超臨界水(通常、650℃以上、250気圧以上の超臨界水が用いられる)の持つ強い酸化力を利用してPCBを炭酸ガスと水と塩酸にまで分解する超臨界水酸化法や、超臨界直前の状態の水に酸素と炭酸ナトリウムを加えた熱水を用いて380℃、270気圧下でPCBを酸化分解させる熱水分解法がある。そして、例えば特開2003−175327号公開特許公報(特許文献3)に示されるように、供給される処理液中のハロゲン化有機化合物を高温高圧環境下で分解する前段反応器と後段反応器を備えて前段反応器内の処理液を後段反応器の内部に供給する水熱酸化分解装置も提案されている。
[D]光分解法
PCBに波長250〜300nmの紫外線を照射することにより、PCBを脱塩素化し、微量の残留PCBを貴金属触媒や微生物により分解するもので、例えば特開平11−319816号公開特許公報(特許文献4)に示されるように、内部電極を有するエキシマ発光部と、そのエキシマ発光部の外側に配置されて有機化合物を含む液体を満たす金属容器と、それら内部電極と金属容器の間に電圧を印加して誘電体バリア放電を生じさせる電源を備えた有機物分解装置を用い、そのエキシマ発光部と金属容器との間に満たされた有機化合物含有液体をエキシマ発光部から発生するエキシマ光によって二酸化炭素や水などに分解するものが提案されている。
[E]還元熱化学分解法
還元熱化学分解法としては、PCBを純水素雰囲気中の常圧下で加熱し、触媒を用いることなく脱塩素・分解する還元反応によってPCBを最終的に塩酸、メタン、一酸化炭素、二酸化炭素、水素および僅かな低級炭化水素に分解し塩酸は中和して系外に排出して無害化する気相水素還元法や、鉄溶融バスにPCB廃棄物を吹き込むことによりPCBを一旦原子レベルまで分解しその後に圧力、温度、酸素供給量を調節することにより生成物の化学組成を制御する溶融触媒抽出法や、酸素プラズマもしくは空気プラズマによる熱エネルギーを用いて酸化雰囲気中でPCBを分解して無害化する(直流プラズマジェットを用いてPCB含有油と酸素を反応させてPCBを分解して無害化する)プラズマ高温分解法や、高温焼却によって残った焼却灰もしくは焼却飛灰をプラズマによる熱エネルギーを使って溶融固化することによりスラグ化して無害化するプラズマ溶融法などが知られている。そして、例えば特開2003−19434号公開特許公報(特許文献5)に示されるように、PCBで汚染された土壌をサイクロンにより螺旋状に運動させてプラズマ処理容器に供給しそのサイクロンあるいはプラズマ処理容器のガス導入口より導入された処理ガスの活性化プラズマと化学反応させてPCBを無害化処理するものが提案されている。
特開2004−132558号公開特許公報 特開2003−135621号公開特許公報 特開2003−175327号公開特許公報 特開平11−319816号公開特許公報 特開2003−19434号公開特許公報
Various PCB detoxification methods have been proposed in the past, and these methods can be broadly classified into the following five types.
That is,
[A] Thermal decomposition method by high-temperature incineration The PCB is decomposed into carbon dioxide, water, inorganic salts and incineration ash by spraying PCB in a high-temperature furnace at 1200 to 1400 ° C. As shown in Japanese Patent Application Publication No. 2004-132558 (Patent Document 1), a PCB solution in which PCB is dissolved in a solvent and water are mixed to produce an emulsion, which is electrolyzed with water using a hydrogen / oxygen gas generating means. A type in which PCB is burned at 1400 ° C. or higher by a hydrogen gas burner by supplying the generated hydrogen gas and oxygen gas in a separated state and spraying the emulsion into a combustion chamber in which the hydrogen gas is burned with oxygen gas. Proposed.
[B] Chemical dechlorination and decomposition method Alkaline agents and carbon-based catalysts are mixed with PCB and heated to 300 to 350 ° C in a nitrogen atmosphere under normal pressure to cause chemical reaction, thereby replacing chlorine in PCB with hydrogen. Thus, a substance other than PCB is converted into a harmless biphenyl compound, inorganic salt and water after the treatment. For example, as disclosed in Japanese Patent Application Laid-Open No. 2003-135621 (Patent Document 2), gelation is achieved by mixing and stirring PCB and chlorine compound with silicone and toluene, and mixing and stirring an alkali agent catalyst. It has been proposed to initiate an exothermic reaction at 40 to 120 ° C. to dechlorinate PCB.
[C] Hydrothermal oxidative decomposition method In the hydrothermal oxidative decomposition method, so-called supercritical water (usually supercritical water at 650 ° C. or higher and 250 atmospheric pressure or higher) in a state exceeding 374 ° C. and 218 atm. 380 ° C using supercritical water oxidation method that decomposes PCB into carbon dioxide gas, water and hydrochloric acid by using strong oxidizing power, and hot water in which oxygen and sodium carbonate are added to water just before supercritical There is a hydrothermal decomposition method in which PCB is oxidized and decomposed at 270 atm. For example, as disclosed in Japanese Patent Application Laid-Open No. 2003-175327 (Patent Document 3), a pre-reactor and a post-reactor for decomposing a halogenated organic compound in a supplied processing solution under a high temperature and high pressure environment are provided. A hydrothermal oxidative decomposition apparatus is also proposed which supplies the processing liquid in the former stage reactor to the inside of the latter stage reactor.
[D] Photolysis method A PCB is dechlorinated by irradiating the PCB with ultraviolet rays having a wavelength of 250 to 300 nm, and a trace amount of residual PCB is decomposed by a noble metal catalyst or a microorganism. As shown in the publication (Patent Document 4), an excimer light emitting part having an internal electrode, a metal container that is disposed outside the excimer light emitting part and fills a liquid containing an organic compound, and between the internal electrode and the metal container Excimer light that generates an organic compound-containing liquid filled between the excimer light emitting part and the metal container from the excimer light emitting part using an organic substance decomposing apparatus equipped with a power source that generates a dielectric barrier discharge by applying a voltage to Have been proposed to decompose into carbon dioxide or water.
[E] Reductive thermochemical decomposition method As a reductive thermochemical decomposition method, PCB is finally converted into hydrochloric acid and methane by a reduction reaction in which PCB is heated under normal pressure in a pure hydrogen atmosphere and dechlorinated and decomposed without using a catalyst. Gas phase hydrogen reduction method that decomposes into carbon monoxide, carbon dioxide, hydrogen and a few lower hydrocarbons, neutralizes hydrochloric acid and discharges it outside the system to make it harmless, or blowing PCB waste into an iron melting bath The PCB is decomposed once to the atomic level, and then the pressure, temperature, and oxygen supply rate are adjusted to control the chemical composition of the product. PCB is decomposed and rendered harmless in the plasma (decomposed and detoxified by reacting PCB containing oil and oxygen using a direct current plasma jet) A plasma melting method or the like is known in which incineration ash or incineration fly ash left by thermal incineration is melted and solidified using thermal energy of plasma to make it slag and detoxify. For example, as disclosed in Japanese Patent Application Laid-Open No. 2003-19434 (Patent Document 5), soil contaminated with PCB is spirally moved by a cyclone and supplied to the plasma processing vessel, and the cyclone or the plasma processing vessel is supplied. There has been proposed a method for detoxifying a PCB by chemically reacting with an activated plasma of a processing gas introduced from the gas inlet.
Japanese Patent Laid-Open No. 2004-132558 Japanese Patent Laid-Open No. 2003-135621 Japanese Patent Laid-Open No. 2003-175327 Japanese Patent Laid-Open No. 11-319816 Japanese Patent Laid-Open No. 2003-19434

しかし上記のような従来のPCB無害化処理手法は、何れも実用化する上で大きな難点がある。すなわち、高温焼却による熱分解法では、高温で焼却させるための処理炉の管理が難しい上に、未分解のPCBが焼却灰中に残存する問題や、処理温度が低いとPCBより毒性の強いダイオキシンを発生する危険性があり、化学的脱塩素化分解法では、効果的に脱塩素化を図るために強アルカリ剤を必要とし、その強アルカリ剤は一般に扱い難いもので、NaOH、KOH、Na、Kの順に順次扱い難くなるという難点がある。また、化学的脱塩素化分解法、水熱酸化分解法、光分解法、還元熱化学分解法は、共に大規模の設備を要することから、プラントの建設費や設備の運転コストが嵩むことが実用化上の大きな難点であり、さらに、PCBを含む多量の油を無害処理する際の処理コスト面でも問題視される。 However, any of the conventional PCB detoxification processing methods as described above has a great difficulty in practical use. That is, in the pyrolysis method by high temperature incineration, it is difficult to manage the processing furnace for incineration at high temperature, and there are problems that undecomposed PCB remains in the incineration ash, and dioxins that are more toxic than PCB at low processing temperature. The chemical dechlorination and decomposition method requires a strong alkali agent for effective dechlorination, and the strong alkali agent is generally difficult to handle. NaOH, KOH, Na , K is difficult to handle in order. In addition, chemical dechlorination decomposition method, hydrothermal oxidative decomposition method, photodecomposition method and reductive thermal chemical decomposition method all require large-scale equipment, which may increase plant construction costs and equipment operation costs. This is a major difficulty in practical use, and is also regarded as a problem in terms of processing costs when a large amount of oil containing PCB is harmlessly processed.

この発明は、従来の各種のPCB無害化処理手法が抱える上記のような実用上の難点に鑑み、PCB含有油の無害化処理を促進するために、無害化の処理工程ならびにその処理装置が単純で、処理設備の建設コストや運転コストが嵩張らず、取扱いの難しい強アルカリ剤や特殊の触媒・薬剤を用いることなく、前記のプラズマ溶融法等に見られるような高温処理を必要とせず、常温常圧下で環境負荷も小さく安全且つ効果的にPCB含有油を無害化処理できるような、実用性の高いPCB含有油の無害化処理方法と、その無害化処理方法を実施するための実用性に高いPCB含有油の無害化処理装置を実現しようとするものである。   In view of the above-described practical difficulties of various conventional PCB detoxification treatment techniques, the present invention provides a simple detoxification treatment process and treatment apparatus for promoting detoxification treatment of PCB-containing oil. Therefore, the construction cost and the operation cost of the processing equipment are not bulky, and it does not require a high temperature treatment such as the plasma melting method described above without using a strong alkali agent or a special catalyst / chemical that is difficult to handle. A highly practical PCB-containing oil detoxification method that can safely and effectively detoxify PCB-containing oil under normal pressure, and a practicality for implementing the detoxification treatment method. An object of the present invention is to realize a detoxifying device for high PCB-containing oil.

上記の課題・目的を達するために、この発明は、PCB含有油を霧化または液滴化または蒸気化して、その霧化または液滴化または蒸気化されたPCB含有油を、無声放電作動中の無声放電空間内に流通させることにより、PCB含有油中のPCBを無害物質に転換する。即ちこの発明は、無声放電空間での電子付与と脱離による酸化還元力を利用してPCBを無害物質に転換する原理に基づくものである。   In order to achieve the above-mentioned problems / objects, the present invention is to atomize, drop, or vaporize a PCB-containing oil, and perform the silent discharge operation on the atomized, drop-formed, or vaporized PCB-containing oil. In the silent discharge space, the PCB in the PCB-containing oil is converted into a harmless substance. That is, the present invention is based on the principle of converting PCB into a harmless substance by utilizing the redox power generated by the electron donation and desorption in the silent discharge space.

また、不活性ガスをもってPCB含有油を噴霧ノズルに供給すると共に同不活性ガスを別途上記噴霧ノズルに供給することにより、その噴霧ノズルからPCB含有油を霧化または液滴化または蒸気化して噴出させ、その噴出したPCB含有油を、片面に放電用電極板が装着された複数枚の誘電体の無声放電バリアの間に形成された無声放電空間内を流通させることにより、先に無害化処理された油中になお残存するPCBを無害物質に転換する。   In addition, by supplying PCB-containing oil with an inert gas to the spray nozzle and supplying the inert gas separately to the spray nozzle, the PCB-containing oil is atomized, dropletized or vaporized and ejected from the spray nozzle. The PCB-containing oil that has been ejected is circulated through the silent discharge space formed between the silent discharge barriers of a plurality of dielectrics each having a discharge electrode plate mounted on one side, thereby detoxifying first. PCBs still remaining in the finished oil are converted into harmless substances.

そしてまた、無声放電空間内を流通して無害化処理された後もPCBが残存するPCB含有油を回収し、その回収したPCB含有油を再度霧化または液滴化または蒸気化して、その霧化または液滴化または蒸気化されたPCB含有油を、無声放電作動中の無声放電空間内に流通させることにより、PCB含有油中に残存するPCBを無害物質に転換する。   In addition, the PCB-containing oil in which the PCB remains even after being detoxified through circulation in the silent discharge space is recovered, and the recovered PCB-containing oil is atomized, dropletized, or vaporized again. The PCB-containing oil converted into droplets or vaporized is circulated in the silent discharge space during the silent discharge operation, thereby converting the PCB remaining in the PCB-containing oil into a harmless substance.

一方、PCB含有油の無害化処理装置として、PCB含有油を霧化または液滴化または蒸気化する手段と、その霧化または液滴化または蒸気化されたPCB含有油が流通する無声放電系と、その無声放電系に無声放電エネルギーを供給する電源を主要部とする無害化処理装置を構成する。   On the other hand, as a detoxification treatment device for PCB-containing oil, a means for atomizing, dropletizing or evaporating PCB-containing oil and a silent discharge system through which the atomized, dropletized or vaporized PCB-containing oil circulates And a detoxification processing apparatus having a power supply for supplying silent discharge energy to the silent discharge system as a main part.

また、PCB含有油と不活性ガスが供給されてPCB含有油を霧化または液滴化または蒸気化する噴霧ノズル、並びに、片面に放電用電極板が装着された複数枚の誘電体の無声放電バリアを間隔を保って並設させその互に向かい合う無声放電バリアの間に無声放電空間を形成しその無声放電空間内に霧化または液滴化または蒸気化されたPCB含有油が流通する無声放電系を有するリアクタと、その無声放電系に無声放電エネルギーを供給する電源を主要部としたPCB含有油の無害化処理装置を構成する。   Also, a spray nozzle that atomizes, drops or vaporizes PCB-containing oil by supplying PCB-containing oil and inert gas, and silent discharge of a plurality of dielectrics each having a discharge electrode plate mounted on one side Silent discharge where PCBs containing oil that is atomized, dropletized, or vaporized circulates in the silent discharge space formed between the silent discharge barriers facing each other by arranging the barriers in parallel with each other A PCB-containing oil detoxification treatment apparatus comprising a reactor having a system and a power supply for supplying silent discharge energy to the silent discharge system is constituted.

更にまた、リアクタに収まる無声放電系としては、片面に放電用電極板が装着された複数枚の誘電体の無声放電バリアをスペーサを介して間隔を保って並設させ、互に向かい合う無声放電バリアの間に無声放電空間を形成し、無声放電バリアと共に並設状態にある放電用電極板を順次交互に選択した二つの電極グループを形成し、その一方の電極グループを接地電極とし、他方の電極グループを電源出力端子に接続するものとする。   Furthermore, as a silent discharge system that can be accommodated in the reactor, a plurality of dielectric silent discharge barriers each having a discharge electrode plate mounted on one side thereof are arranged in parallel with a space therebetween, and the silent discharge barriers facing each other are arranged. A silent discharge space is formed between them, and two electrode groups are formed by alternately selecting discharge electrode plates in parallel with the silent discharge barrier, one of which is the ground electrode, and the other electrode The group shall be connected to the power output terminal.

そして、この発明に係るPCB含有油の無害化処理方法とその無害化処理装置によれば、PCB含有油を霧化または液滴化または蒸気化する噴霧ノズルと、誘電体バリアを備えた無声放電系を組み合わせて無害化処理を実行するものであり、その無害化処理方法の工程は極めて単純で、無害化処理装置の建設コストや使用コストを低く抑えることができ、環境コストも小さく、安全且つ効果的に実施できる無害化処理技術である。またこの発明に係る無害化処理における反応は、前記したプラズマ溶融法等に見られるような高温処理を必要とせず、常温常圧下で極めて取り扱い易いものであり、特殊な触媒や薬剤を必要とせず、残渣の発生もない。また、処理油は燃料として利用できる。更にこの発明に係る無害化処理は、気体液体混合処理であることから、従来技術のような高温焼却時に発生する飛灰や、固形化した焼却灰の埋め立て問題などが生じないという効果もある。したがって、環境に考慮しながら、限られた時間内で迅速に残存PCBを廃棄処理する方法として実用効果の大きいものである。   According to the PCB-containing oil detoxification treatment method and the detoxification treatment apparatus according to the present invention, a silent discharge comprising a spray nozzle for atomizing, dropletizing, or vaporizing PCB-containing oil, and a dielectric barrier is provided. The detoxification process is performed by combining the systems, the process of the detoxification process is very simple, the construction cost and the use cost of the detoxification treatment apparatus can be kept low, the environmental cost is small, safe and It is a detoxification treatment technology that can be implemented effectively. Further, the reaction in the detoxification treatment according to the present invention does not require a high-temperature treatment as seen in the plasma melting method described above, and is extremely easy to handle at room temperature and normal pressure, and does not require a special catalyst or chemical. There is no generation of residue. Further, the treated oil can be used as a fuel. Further, since the detoxification process according to the present invention is a gas-liquid mixing process, there is an effect that the fly ash generated during high-temperature incineration as in the prior art and the landfill problem of solidified incineration ash do not occur. Therefore, it is a practical effect as a method for quickly discarding the remaining PCB within a limited time while considering the environment.

この発明に係るPCB含有油の無害化処理方法の極めて優れた実施形態は、窒素ガスでもってPCB含有油を噴霧ノズルに供給すると共に同時に同窒素ガスを別途前記噴霧ノズルに供給することにより、前記噴霧ノズルから前記PCB含有油を霧化または液滴化または蒸気化して噴出させ、その噴出したPCB含有油を、片面に放電用電極板が装着された複数枚の誘電体の無声放電バリアが間隔を保って並設されてその向かい合う無声放電バリアの間に無声放電空間が形成され且つ前記各無声放電バリアの放電用電極板が順次交互に選択されて成る二つの電極グループ間に高電圧が印加されて無声放電が生成される無声放電系の前記無声放電空間内を流通させることにより、前記PCB含有油中のPCBを無害物質に転換し、更に、前記無声放電空間内を流通して無害化処理された処理済油を回収して再度霧化または液滴化または蒸気化し、その霧化または液滴化または蒸気化されたPCB含有油を、再度前記無声放電作動中の無声放電空間内を流通させて、前記処理済油中になお残存するPCBを無害物質に転換するPCB含有油の無害化処理方法である。 An extremely excellent embodiment of the PCB-containing oil detoxification method according to the present invention is the above-described method, wherein the PCB-containing oil is supplied to the spray nozzle with nitrogen gas and simultaneously the nitrogen gas is supplied to the spray nozzle separately. The PCB-containing oil is atomized, dropletized or vaporized and ejected from the spray nozzle, and the ejected PCB-containing oil is spaced by a plurality of dielectric silent discharge barriers each having a discharge electrode plate mounted thereon. A high voltage is applied between two electrode groups in which a silent discharge space is formed between the silent discharge barriers facing each other and the discharge electrode plates of the silent discharge barriers are alternately selected. The PCB in the PCB-containing oil is converted into a harmless substance by circulating in the silent discharge space of the silent discharge system where the silent discharge is generated, and further, the silent The treated oil that has been detoxified through circulation in the electric space is recovered and atomized, dropletized, or vaporized again, and the atomized, dropletized, or vaporized PCB-containing oil is again silenced. It is a detoxification treatment method for PCB-containing oil, which circulates in a silent discharge space during discharge operation and converts PCB still remaining in the treated oil into harmless substances.

この発明に係るPCB含有油の無害化処理装置の極めて優れた実施形態は、無害化処理を要するPCB含有油を貯留する圧力容器と、前記PCB含有油を供給し霧化または液滴化または蒸気化するための窒素ガスを封入した窒素ガスボンベと、前記PCB含有油を霧化または液滴化または蒸気化する噴霧ノズル、並びにその霧化または液滴化または蒸気化されたPCB含有油が流入し流通する無声放電系を内蔵したリアクタと、前記無声放電系に無声放電エネルギーを供給する電源と、前記リアクタで無害化処理された処理済油を回収する回収容器と、前記回収容器で回収した処理済油をPCB含有油を貯留する圧力容器に戻す手段とを備え、前記無声放電系は、片面に放電用電極板が装着された複数枚の誘電体の無声放電バリアがスペーサを介して間隔を保って並設されてその向かい合う無声放電バリアの間に前記霧化または液滴化または蒸気化されたPCB含有油が流通する無声放電空間が形成され且つ前記各無声放電バリアの放電用電極板が順次交互に選択されて二つの電極グループに形成されその一方の電極グループを接地電極とし他方の電極グループを前記電源の出力端子に接続する電極としたものとし、前記圧力容器と前記窒素ガスボンベの間を液体側減圧弁を介して配管で連通させると共に、前記圧力容器のPCB含有油中と前記リアクタの前記噴霧ノズルの間を液体流量調節バルブを介して配管で連通させ、更に前記窒素ガスボンベと前記噴霧ノズルの間を気体側減圧弁を介して連通させたPCB含有油の無害化処理装置である。   An extremely excellent embodiment of the PCB-containing oil detoxification processing apparatus according to the present invention includes a pressure vessel that stores a PCB-containing oil that requires detoxification processing, and supplies the PCB-containing oil to atomize, dropletize, or steam. A nitrogen gas cylinder filled with nitrogen gas for atomization, a spray nozzle for atomizing, dropletizing, or vaporizing the PCB-containing oil, and an atomized, dropletized, or vaporized PCB-containing oil Reactor incorporating a silent discharge system that circulates, a power source that supplies silent discharge energy to the silent discharge system, a recovery container that recovers treated oil detoxified in the reactor, and a process recovered in the recovery container Means for returning the finished oil to a pressure vessel for storing the PCB-containing oil, and the silent discharge system includes a plurality of dielectric silent discharge barriers each having a discharge electrode plate mounted on one side as spacers. A silent discharge space is formed in which the atomized, dropletized, or vaporized PCB-containing oil flows between the silent discharge barriers that are arranged side by side with a space therebetween and discharge of each silent discharge barrier. The electrode plates are alternately selected and formed into two electrode groups, one electrode group of which is a ground electrode and the other electrode group is an electrode connected to the output terminal of the power source, the pressure vessel and the The nitrogen gas cylinder is communicated with a pipe via a liquid-side pressure reducing valve, the PCB-containing oil in the pressure vessel and the spray nozzle of the reactor are communicated with a pipe via a liquid flow rate adjustment valve, and This is a PCB-containing oil detoxifying device in which a nitrogen gas cylinder and the spray nozzle are communicated with each other via a gas side pressure reducing valve.

以下、この発明に係るPCB含有油の無害化処理方法ならびにPCB含有油の無害化処理装置の実施例を、図面を参考に説明する。図1はこの発明に係るPCB含有油の無害化処理装置の構成図、図2は同無害化処理装置の無声放電系の斜視図、図3は図2におけるS−S’線で切断した同無声放電系の断面図である。また図4は、この発明に係るPCB含有油の無害化処理方法の実施結果であるところの、放電処理回数に対するPCBの残存濃度変化図である。   Embodiments of a PCB-containing oil detoxification treatment method and a PCB-containing oil detoxification treatment apparatus according to the present invention will be described below with reference to the drawings. FIG. 1 is a configuration diagram of a PCB-containing oil detoxification treatment apparatus according to the present invention, FIG. 2 is a perspective view of a silent discharge system of the detoxification treatment apparatus, and FIG. 3 is a cross-sectional view taken along line SS ′ in FIG. It is sectional drawing of a silent discharge system. FIG. 4 is a graph showing a change in the residual concentration of PCB with respect to the number of discharge treatments, which is the result of the detoxification treatment method for PCB-containing oil according to the present invention.

この発明の一実施例として示すPCB含有油の無害化処理装置は、図1に示すように、装置の心臓部となる無害化処理反応部A1と、その無害化処理反応部A1にPCB含有油を供給するPCB含有油供給部A2と、無害化処理反応部A1に無声放電エネルギーを供給する高電圧電源部A3と、無害化処理反応部A1で無害化処理された油を回収する処理済油回収部A4とで構成されている。   As shown in FIG. 1, a PCB-containing oil detoxification treatment apparatus shown as an embodiment of the present invention includes a detoxification treatment reaction part A1 which is the heart of the apparatus, and a PCB-containing oil in the detoxification treatment reaction part A1. PCB-containing oil supply unit A2 for supplying detoxification, high-voltage power supply unit A3 for supplying silent discharge energy to the detoxification treatment reaction unit A1, and treated oil for recovering the detoxified oil in the detoxification treatment reaction unit A1 It consists of a collection unit A4.

無害化処理反応部A1は容器状のリアクタ1から成り、リアクタ1内には、供給されるPCB含有油を霧化あるいは液滴化あるいは蒸気化してリアクタ1内に噴出させる噴霧ノズル2と、無声放電(誘電バリア放電)を発生させる無声放電系3が配設されている。なお、4はリアクタ1内で無害化処理された処理済油を受ける下部ロート、5は下部ロート4で受けた処理済油を処理済油回収部A4へ導く導出管である。無声放電系3の構造は、図2,3に示すように、片面に厚さ0,1mmのステンレス薄板の放電用電極板31を貼り付けた長さ200mm×幅100mm×厚さ3mmの8枚のガラス板(例えば、商品名:テンパックス)32を、ギャップ長2mmの無声放電空間33を保って、並行状態に配して一体化したものである。ガラス板32は無声放電系3の無声放電バリアとなるもので、互に対向するガラス板32の間にギャップ長2mmの無声放電空間33を形成するために、ガラス板32の向かい合う長辺に沿う厚さ2mmのガラスエポキシ製のスペーサ34を、互に対向するガラス板32の間に介在させて7室の無声放電空間33が形成されている。また、ガラス板(無声放電バリア)32と共に並行状態に配設されている放電用電極板31を順次交互に選択して二つの電極グループ31a,31bを形成し、その一方の電極グループ31aに属する放電用電極板31を接地電極とし、他方の電極グループ31bに属する放電用電極板31を、高電圧電源トランス16の高電圧出力端子16aに接続するものとする。そして、電極グループ31aに属する放電用電極板31と、他方の電極グループ31bに属する放電用電極板31の間に、高電圧電源部A3の高電圧電源トランスから商用周波交流10kVの高電圧が印加されることにより、無声放電系3の無声放電空間33に常温常圧下で無声放電(誘電体バリア放電)が生じ持続されるものである。 The detoxification treatment reaction part A1 comprises a container-like reactor 1, and in the reactor 1, a spray nozzle 2 for atomizing, dropping or vaporizing the supplied PCB-containing oil into the reactor 1 and silent. A silent discharge system 3 for generating a discharge (dielectric barrier discharge) is provided. Reference numeral 4 denotes a lower funnel that receives the treated oil detoxified in the reactor 1, and 5 denotes a lead-out pipe that guides the treated oil received by the lower funnel 4 to the treated oil recovery section A4. The structure of the silent discharge system 3, as shown in FIGS. 2 and 3, is 8 sheets of length 200 mm × width 100 mm × thickness 3 mm in which a discharge electrode plate 31 of a stainless steel plate having a thickness of 0.1 mm is attached on one side. Glass plates (for example, trade name: TEMPAX) 32 are integrated in a parallel state while maintaining a silent discharge space 33 with a gap length of 2 mm. The glass plate 32 serves as a silent discharge barrier of the silent discharge system 3, and in order to form a silent discharge space 33 with a gap length of 2 mm between the glass plates 32 facing each other, the glass plate 32 extends along the long sides facing each other. Seven chamber silent discharge spaces 33 are formed by interposing glass epoxy spacers 2 having a thickness of 2 mm between glass plates 32 facing each other. Further, the discharge electrode plates 31 arranged in parallel with the glass plate (silent discharge barrier) 32 are alternately and sequentially selected to form two electrode groups 31a and 31b, which belong to one of the electrode groups 31a. The discharge electrode plate 31 is a ground electrode, and the discharge electrode plate 31 belonging to the other electrode group 31 b is connected to the high voltage output terminal 16 a of the high voltage power transformer 16. A high voltage of commercial frequency AC 10 kV is applied between the discharge electrode plate 31 belonging to the electrode group 31a and the discharge electrode plate 31 belonging to the other electrode group 31b from the high voltage power transformer of the high voltage power supply unit A3. As a result, silent discharge (dielectric barrier discharge) is generated and maintained in the silent discharge space 33 of the silent discharge system 3 at room temperature and normal pressure.

PCB含有油供給部A2は、無害化処理を要するPCB含有油6を蓄えたステンレス製の圧力容器7と、安価な不活性ガスである窒素ガスを封入した窒素ガスボンベ8を備えて成る。窒素ガスボンベ8とリアクタ1の噴霧ノズル2の間は、気体側減圧弁9を介して配管10を通じて連通するものであり、窒素ガスボンベ8と圧力容器7の間は、液体側減圧弁11を介して配管12を通じて連通するものであり、更に圧力容器7内のPCB含有油6とリアクタ1の噴霧ノズル2の間は、圧力調整弁13および液体流量調節バルブ14を介して配管15を通じて連通するものである。なお、配管10,12,15は化学的に安定なテフロン(登録商標)管が用いられている。窒素ガスボンベ8に貯留された高圧窒素ガスは、圧力容器7内のPCB含有油6をリアクタ1の噴霧ノズル2へ圧送して供給し噴霧ノズル2で霧化あるいは液滴化あるいは蒸気化してリアクタ1内の無声放電系3に向けて噴霧する働きをする。すなわち、窒素ガスボンベ8から供給される窒素ガスは、気体側減圧弁9と配管10を経て、リアクタ1の上部に取り付けられた噴霧ノズル2へ送られると同時に、液体側減圧弁11を経て、PCB含有油6を充填した圧力容器7にも送られる。そして圧力容器7において窒素ガスによって加圧されたPCB含有油6は、液体流量調整バルブ14、配管15を経て噴霧ノズル2へ送られる。配管10を流れる気体(窒素ガス)と、配管15を流れる液体(PCB含有油6)の圧力や流量比率は、気体側減圧弁9、液体側減圧弁11、圧力調整弁13、液体流量調節バルブ14などによって予め調整設定されており、PCB含有油6は、噴霧ノズル2で窒素ガスと混合された後にリアクタ1内に設置されている無声放電系3の無声放電空間33に向けて噴霧される。そして、噴霧ノズル2から噴霧されたPCB含有油6が、無声放電が持続している無声放電系3の無声放電空間33に、図2の矢印Mに示すように、流入し流通して無声放電空間33を通過する過程で、油中のPCB成分の塩素が取り除かれて無害化処理されるものである。 The PCB-containing oil supply unit A2 includes a stainless steel pressure vessel 7 that stores PCB-containing oil 6 that requires detoxification, and a nitrogen gas cylinder 8 that contains nitrogen gas that is an inexpensive inert gas. The nitrogen gas cylinder 8 and the spray nozzle 2 of the reactor 1 communicate with each other through a pipe 10 via a gas side pressure reducing valve 9, and the nitrogen gas cylinder 8 and the pressure vessel 7 are connected via a liquid side pressure reducing valve 11. The pipe 12 communicates with the PCB-containing oil 6 in the pressure vessel 7 and the spray nozzle 2 of the reactor 1 through the pressure regulation valve 13 and the liquid flow rate regulation valve 14 through the pipe 15. is there. The pipes 10, 12, and 15 are chemically stable Teflon (registered trademark) pipes. The high-pressure nitrogen gas stored in the nitrogen gas cylinder 8 is supplied by pumping the PCB-containing oil 6 in the pressure vessel 7 to the spray nozzle 2 of the reactor 1 and atomizing, dropletizing, or vaporizing with the spray nozzle 2. It functions to spray toward the silent discharge system 3 inside. That is, the nitrogen gas supplied from the nitrogen gas cylinder 8 is sent to the spray nozzle 2 attached to the upper part of the reactor 1 through the gas side pressure reducing valve 9 and the pipe 10 and simultaneously through the liquid side pressure reducing valve 11 to the PCB. It is also sent to the pressure vessel 7 filled with the containing oil 6. Then, the PCB-containing oil 6 pressurized with nitrogen gas in the pressure vessel 7 is sent to the spray nozzle 2 through the liquid flow rate adjusting valve 14 and the pipe 15. The pressure and flow ratio of the gas (nitrogen gas) flowing through the pipe 10 and the liquid (PCB-containing oil 6) flowing through the pipe 15 are the gas side pressure reducing valve 9, the liquid side pressure reducing valve 11, the pressure adjusting valve 13, and the liquid flow rate adjusting valve. The PCB-containing oil 6 is sprayed toward the silent discharge space 33 of the silent discharge system 3 installed in the reactor 1 after being mixed with nitrogen gas by the spray nozzle 2. . Then, the PCB-containing oil 6 sprayed from the spray nozzle 2 flows into the silent discharge space 33 of the silent discharge system 3 where the silent discharge continues as shown by the arrow M in FIG. In the process of passing through the space 33, chlorine of the PCB component in the oil is removed and detoxified.

高電圧電源部A3は高電圧電源トランス16を備え、高電圧電源トランス16の高電圧側出力端子16aは、無声放電系3のガラス板(無声放電バリア)32上に配設された電極グループ31bに属する放電用電極31に接続される。そして、電極グループ31aに属する放電用電極板31と、他方の電極グループ31bに属する放電用電極板31の間に商用周波交流10kVの高電圧が印加される。なお、17は高電圧電源トランス16に付設した電圧計、18は高電圧電源トランス16に付設した電流計である。   The high-voltage power supply unit A3 includes a high-voltage power supply transformer 16, and a high-voltage side output terminal 16a of the high-voltage power supply transformer 16 has an electrode group 31b disposed on the glass plate (silent discharge barrier) 32 of the silent discharge system 3. Is connected to the discharge electrode 31 belonging to. A high voltage of commercial frequency AC of 10 kV is applied between the discharge electrode plate 31 belonging to the electrode group 31a and the discharge electrode plate 31 belonging to the other electrode group 31b. Reference numeral 17 denotes a voltmeter attached to the high voltage power transformer 16, and 18 denotes an ammeter attached to the high voltage power transformer 16.

処理済油回収部A4は、回収容器20、ミストトラップ21、へキサントラップ22、活性炭トラップ23が順に縦列接続されて成り、リアクタ1で無害化処理された処理済油は、前記下部ロート4で受けられ凝縮液化して回収容器20に導かれ蓄積される。また、回収容器20から排出した油ミスト分を含む窒素ガスは、ミストトラップ21、へキサントラップ22、活性炭トラップ23を経て油ミストが除去され浄化された後、大気中に放出される。そしてまた、回収容器20で回収した処理済油をPCB含有油供給部A2の圧力容器7へ戻して、上述の無害化処理工程サイクルを繰り返し実行することにより、PCB含有油の無害化処理の実効を高めることができる。 The treated oil recovery section A4 is composed of a collection container 20, a mist trap 21, a hexane trap 22, and an activated carbon trap 23 connected in series, and the treated oil detoxified in the reactor 1 is in the lower funnel 4. It is received, condensed and liquefied, guided to the collection container 20 and accumulated. Further, the nitrogen gas containing the oil mist discharged from the collection container 20 is released into the atmosphere after the oil mist is removed and purified through the mist trap 21, the hexane trap 22, and the activated carbon trap 23. Further, the treated oil recovered in the recovery container 20 is returned to the pressure container 7 of the PCB-containing oil supply unit A2, and the detoxification process cycle described above is repeatedly executed, whereby the detoxification process of the PCB-containing oil is effectively performed. Can be increased.

なお、上記実施例の外、リアクタ、無声放電系を構成するガラスや電極のサイズ、供給ガス流量、ガス圧力等の条件を種々変えても問題なくPCB含有油の無害化処理が可能であった。更に上記実施例では、PCB含有油6をリアクタ1に供給してリアクタ1内に噴霧させるために窒素ガスを用いたが、窒素ガスに替えてアルゴンガスや、アルゴン・窒素混合ガスを用いても同様の結果が得られた。また、上記実施例では、無声放電空間33を形成する誘電体バリアとしてガラス板を採用したが、そのガラス板を絶縁性セラミック板に置き換えてもほぼ同様の結果を得た。したがって誘電体の無声放電バリアは、緻密質で電気絶縁性の高い材料であれば良いと考えられる。また、無声放電空間33に印加する高電圧がパルス波電圧であっても、全く問題なくPCB含有油の無害化処理が可能であった。   In addition to the above examples, the PCB-containing oil could be rendered harmless without any problems even if various conditions such as the size of the glass and electrodes constituting the reactor and the silent discharge system, the supply gas flow rate, and the gas pressure were changed. . Further, in the above embodiment, nitrogen gas is used to supply the PCB-containing oil 6 to the reactor 1 and spray it into the reactor 1, but argon gas or argon / nitrogen mixed gas may be used instead of nitrogen gas. Similar results were obtained. Moreover, in the said Example, although the glass plate was employ | adopted as a dielectric barrier which forms the silent discharge space 33, even if it replaced the glass plate with the insulating ceramic plate, the substantially same result was obtained. Therefore, it is considered that the silent silent discharge barrier may be a dense material having high electrical insulation. Moreover, even if the high voltage applied to the silent discharge space 33 is a pulse wave voltage, the PCB-containing oil can be rendered harmless without any problem.

また、図1に示した本発明に係るPCB含有油の無害化処理装置を用い、次の表1に示す処理条件下で、リアクタ1に供給されるPCB含有油と窒素ガスとの流量比を調整して噴霧ノズルのパターンと無声放電空間の入口形状を一致させるようにし且つPCB含有油を視認できない程に微細な油ミストもしくは液滴として無声放電処理を行い、その放電処理工程は1段とし、処理済油回収部A4で回収された処理済油を再び圧力容器7へ戻して再処理し、その再処理手順を6回繰り返し、無害化処理前の初期のPCB含有油の状態を放電処理回数0回目の状態とし、放電処理回数1回目、3回目および6回目の放電処理終了後に、処理済油回収部A4で回収された処理済油における残存PCB濃度を測定したところ、放電処理回数に対する残存PCB濃度変化は図4に示す通りであった。即ち図4は、放電処理回数に対するPCB残存濃度の変化を示すもので、初期のPCB残存濃度26ppm に対して、6回目の放電処理後のPCB残存濃度は略半減した効果が示されている。なお上記実施例では、放電処理工程は1段で繰り返し処理を6回処理としたものであるが、放電処理工程を多段処理とし繰り返し処理回数を更に増やすことは更に効果的であった。   Further, using the PCB-containing oil detoxifying apparatus according to the present invention shown in FIG. 1, the flow rate ratio between the PCB-containing oil supplied to the reactor 1 and the nitrogen gas is adjusted under the processing conditions shown in Table 1 below. Adjust the spray nozzle pattern to match the inlet shape of the silent discharge space, and perform silent discharge processing as fine oil mist or droplets so that the PCB-containing oil cannot be visually recognized. The treated oil recovered in the treated oil recovery unit A4 is returned to the pressure vessel 7 and reprocessed, and the reprocessing procedure is repeated 6 times to discharge the initial PCB-containing oil state before detoxification. When the number of times of discharge processing was set to 0, and the discharge processing times of the first time, the third time, and the sixth time were completed, the residual PCB concentration in the processed oil recovered by the processed oil recovery unit A4 was measured. Remaining PC The change in B concentration was as shown in FIG. That is, FIG. 4 shows the change in the PCB residual concentration with respect to the number of discharge treatments, and shows the effect that the PCB residual concentration after the sixth discharge treatment is substantially halved with respect to the initial PCB residual concentration of 26 ppm. In the above embodiment, the discharge treatment process is performed in one step and the repetition treatment is performed six times. However, it is more effective to further increase the number of repetition treatments by making the discharge treatment step a multi-stage treatment.

表1

Figure 2006129900
Table 1
Figure 2006129900

PCBは、塩素の置換数と位置によって多くの異性体が存在し、その毒性も大きく異なるので、脱塩素化処理を効率良く行って無害化することが重要である。この発明は、PCBを含有する油を霧化または液滴化あるいは蒸気化して噴霧し、その噴霧されたPCB含有油から、無声放電エネルギーによって塩素の結合を解いて、PCB含有油を無害化するもので、無声放電時の電流は、ガラス板などの誘電体バリアの存在によって非常に小さいことから、装置の運転コストは安く、長時間運転の信頼性も高い。また、無声放電系に印加する電圧は10kV程度で良いため、通常のネオントランスでも十分に用をなすことから、装置価格の面でも極めて経済的である。更にまた、無害化処理反応は常温常圧下で可能であり、特殊の触媒・薬剤も必要としないことから、無害化方法・装置の取り扱いは極めて容易で、無害化処理に伴う残渣の発生もない。したがって、この発明の実用上の効果は極めて大である。 PCBs have many isomers depending on the number and position of chlorine substitution, and their toxicity varies greatly. Therefore, it is important to efficiently dechlorinate and detoxify. In this invention, oil containing PCB is atomized, dropletized or vaporized and sprayed, and the chlorine-containing oil is released from the sprayed PCB-containing oil by silent discharge energy, thereby detoxifying the PCB-containing oil. However, since the current during silent discharge is very small due to the presence of a dielectric barrier such as a glass plate, the operating cost of the apparatus is low and the reliability of long-time operation is high. In addition, since the voltage applied to the silent discharge system may be about 10 kV, it can be used even with a normal neon transformer, so that it is extremely economical in terms of the device price. Furthermore, the detoxification reaction can be performed at normal temperature and pressure, and no special catalyst or chemical is required. Therefore, the detoxification method and equipment are extremely easy to handle, and no residue is generated by the detoxification process. . Therefore, the practical effect of the present invention is extremely great.

現在継続保管されているPCB含有油の無害化処理は産業上の大きな且つ火急の課題であるが、この発明に係るPCB含有油の無害化処理方法、ならびにその無害化処理装置は、産業上の負の遺産を取り除く上で大いに活用できるものと考えられる。   The detoxification treatment of PCB-containing oil that is currently stored continuously is a major and urgent issue in the industry. The detoxification treatment method for PCB-containing oil and the detoxification treatment apparatus according to the present invention are It is thought that it can be used greatly to remove negative heritage.

この発明に係るPCB含有油の無害化処理装置の構成図。The block diagram of the detoxification processing apparatus of PCB containing oil which concerns on this invention. 同無害化処理装置の無声放電系の斜視図。The perspective view of the silent discharge system of the same detoxification processing apparatus. 図2のS−S’線で切断した同無声放電系の断面図。Sectional drawing of the silent discharge system cut | disconnected by the S-S 'line | wire of FIG. この発明に係るPCB含有油の無害化処理方法における放電処理回数に対するPCB残存濃度変化図。The PCB residual density change figure with respect to the frequency | count of the discharge process in the detoxification processing method of the PCB containing oil which concerns on this invention.

符号の説明Explanation of symbols

A1 : 無害化処理反応部
A2 : PCB含有油供給部
A3 : 高電圧電源部(電源部)
A4 : 処理済油回収部
1 : リアクタ
2 : 噴霧ノズル
3 : 無声放電系
4 : 下部ロード
5 : 導出管
6 : PCB含有油
7 : 圧力容器
8 : 窒素ガスボンベ
9 : 気体側減圧弁
10,12,15: 配管
11: 液体側減圧弁
13: 圧力調整弁
14: 液体流量調節バルブ
16: 高電圧電源トランス(電源)
16a:高電圧出力端子(電源出力端子)
17: 電圧計
18: 電流計
20: 回収容器
21: ミストトラップ
22: ヘキサントラップ
23: 活性炭トラップ
31: 放電用電極板
31a,31b:電極グループ
32: ガラス板(誘電体の無声放電バリア)
33: 無声放電空間
34: スペーサ
A1: Detoxification treatment reaction part
A2: PCB-containing oil supply section
A3: High voltage power supply (power supply)
A4: Treated oil recovery part 1: Reactor 2: Spray nozzle 3: Silent discharge system 4: Lower load 5: Outlet pipe 6: PCB containing oil 7: Pressure vessel 8: Nitrogen gas cylinder 9: Gas side pressure reducing valves 10, 12, 15: Pipe 11: Liquid side pressure reducing valve 13: Pressure adjusting valve 14: Liquid flow rate adjusting valve 16: High voltage power transformer (power source)
16a: High voltage output terminal (power output terminal)
17: Voltmeter 18: Ammeter 20: Collection vessel 21: Mist trap 22: Hexane trap 23: Activated carbon trap 31: Electrode plate 31a, 31b for discharge: Electrode group 32: Glass plate (dielectric silent discharge barrier)
33: Silent discharge space 34: Spacer

Claims (6)

PCB含有油を霧化または液滴化または蒸気化し、その霧化または液滴化または蒸気化されたPCB含有油を、無声放電作動中の無声放電空間内を流通させることにより、前記PCB含有油中のPCBを無害物質に転換することを特徴とするPCB含有油の無害化処理方法。   The PCB-containing oil is atomized, dropletized, or vaporized, and the atomized, dropletized, or vaporized PCB-containing oil is circulated in the silent discharge space during the silent discharge operation. A method for detoxifying PCB-containing oil, characterized in that the PCB contained therein is converted into a harmless substance. 不活性ガスをもってPCB含有油を噴霧ノズルに供給すると共に同不活性ガスを別途前記噴霧ノズルに供給することにより、その噴霧ノズルから前記PCB含有油を霧化または液滴化または蒸気化して噴出させ、その噴出したPCB含有油を、片面に放電用電極板が装着され互に対向して並設された誘電体の無声放電バリアの間に形成された無声放電空間内を流通させることにより、前記PCB含有油中のPCBを無害物質に転換することを特徴とするPCB含有油の無害化処理方法。   By supplying the PCB-containing oil with the inert gas to the spray nozzle and supplying the inert gas to the spray nozzle separately, the PCB-containing oil is atomized, dropletized or vaporized and ejected from the spray nozzle. The squirted PCB-containing oil is circulated in the silent discharge space formed between the dielectric silent discharge barriers that are mounted on one side and the discharge electrode plates are arranged opposite to each other. A method for detoxifying a PCB-containing oil, which comprises converting PCB in the PCB-containing oil into a harmless substance. 無声放電空間内を流通して無害化処理された後、なおPCBが残存するPCB含有油を回収し、その回収したPCB含有油を再度、霧化または液滴化または蒸気化し、その霧化または液滴化または蒸気化されたPCB含有油を、無声放電作動中の無声放電空間内を流通させることにより、前記PCB含有油中のPCBを無害物質に転換することを特徴とする請求項1または請求項2に記載のPCB含有油の無害化処理方法。   After circulating through the silent discharge space and detoxified, the PCB-containing oil in which the PCB still remains is recovered, and the recovered PCB-containing oil is atomized or dropletized or vaporized again. 2. The PCB-containing oil is converted into a harmless substance by flowing the droplet- or vaporized PCB-containing oil in a silent discharge space during silent discharge operation. The method for detoxifying PCB-containing oil according to claim 2. PCB含有油を霧化または液滴化または蒸気化する手段と、その霧化または液滴化または蒸気化されたPCB含有油が流通する無声放電系と、その無声放電系に無声放電エネルギーを供給する電源部を備えたことを特徴とするPCB含有油の無害化処理装置。   Means for atomizing, dropletizing, or vaporizing PCB-containing oil, silent discharge system through which the atomized, dropletized, or vaporized PCB-containing oil flows, and supplying silent discharge energy to the silent discharge system A PCB-containing oil detoxification processing apparatus comprising a power supply unit that performs the above-described operation. PCB含有油と不活性ガスが供給されて前記PCB含有油を霧化または液滴化または蒸気化する噴霧ノズルと、片面に放電用電極板が装着された複数枚の誘電体の無声放電バリアを間隔を保って並設させ互に向かい合う前記無声放電バリアの間に無声放電空間が形成されその無声放電空間内に前記霧化または液滴化または蒸気化されたPCB含有油が流通する無声放電系を有するリアクタと、その無声放電系に無声放電エネルギーを供給する電源を備えたことを特徴とするPCB含有油の無害化処理装置。   A spray nozzle for atomizing, dropletizing, or vaporizing the PCB-containing oil by supplying PCB-containing oil and an inert gas, and a plurality of dielectric silent discharge barriers each having a discharge electrode plate mounted on one side A silent discharge system in which a silent discharge space is formed between the silent discharge barriers arranged side by side with a space therebetween, and the atomized, dropletized, or vaporized PCB-containing oil circulates in the silent discharge space A PCB-containing oil detoxification treatment apparatus comprising: a reactor having a power source for supplying silent discharge energy to the silent discharge system. リアクタに収まる無声放電系は、片面に放電用電極板が装着された複数枚の誘電体の無声放電バリアがスペーサを介して間隔を保って並設され、その互に向かい合う前記無声放電バリアの間に無声放電空間が形成され、前記無声放電バリアと共に並設状態にある前記放電用電極板が順次交互に選択されて二つの電極グループに形成され、その一方の電極グループを接地電極とし、他方の電極グループを電源出力端子に接続する電極としたことを特徴とする請求項4または請求項5に記載のPCB含有油の無害化処理装置。
The silent discharge system that fits in the reactor is composed of a plurality of dielectric silent discharge barriers, each having a discharge electrode plate mounted on one side, spaced in parallel via a spacer, and between the silent discharge barriers facing each other. A silent discharge space is formed, and the discharge electrode plates in parallel with the silent discharge barrier are alternately selected and formed into two electrode groups, with one electrode group serving as a ground electrode, 6. The PCB-containing oil detoxifying device according to claim 4 or 5, wherein the electrode group is an electrode connected to a power output terminal.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008206801A (en) * 2007-02-27 2008-09-11 Kanji Kokubu Pcb decomposition processing unit
JP2011121900A (en) * 2009-12-10 2011-06-23 Oriental Kiden Kk Treatment apparatus for harmful substance-containing liquid
JP2013519503A (en) * 2010-02-10 2013-05-30 ゾレッジ‐ガレトン,アルフレド Method and apparatus for applying plasma particles to a liquid and use for sterilizing water

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0260668A (en) * 1988-08-26 1990-03-01 Matsushita Electric Ind Co Ltd Method of decomposing acyclic hydrocarbon halide compound
JPH08758A (en) * 1994-06-17 1996-01-09 Toshiba Corp Photodecomposition device for harmful chlorine compound
JPH0857078A (en) * 1994-08-19 1996-03-05 Tokyo Metropolis Innoxious processing method and device for halogenated ethylene
JP2001054721A (en) * 1999-06-04 2001-02-27 Kashiyama Kogyo Kk Method and device for decomposing fluorocarbons
JP2002527666A (en) * 1998-10-13 2002-08-27 マスホルダー,カール・エフ. Method and apparatus for plasma chemical reduction of gaseous and / or solid pollutants in the exhaust gas of an internal combustion engine
JP2002336653A (en) * 2001-05-21 2002-11-26 Daikin Ind Ltd Plasma catalytic reactor, air cleaning apparatus, nitrogen oxide cleaning apparatus, waste combustion gas cleaning apparatus, dioxine decomposing apparatus and fluorocarbon gas decomposing apparatus

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0260668A (en) * 1988-08-26 1990-03-01 Matsushita Electric Ind Co Ltd Method of decomposing acyclic hydrocarbon halide compound
JPH08758A (en) * 1994-06-17 1996-01-09 Toshiba Corp Photodecomposition device for harmful chlorine compound
JPH0857078A (en) * 1994-08-19 1996-03-05 Tokyo Metropolis Innoxious processing method and device for halogenated ethylene
JP2002527666A (en) * 1998-10-13 2002-08-27 マスホルダー,カール・エフ. Method and apparatus for plasma chemical reduction of gaseous and / or solid pollutants in the exhaust gas of an internal combustion engine
JP2001054721A (en) * 1999-06-04 2001-02-27 Kashiyama Kogyo Kk Method and device for decomposing fluorocarbons
JP2002336653A (en) * 2001-05-21 2002-11-26 Daikin Ind Ltd Plasma catalytic reactor, air cleaning apparatus, nitrogen oxide cleaning apparatus, waste combustion gas cleaning apparatus, dioxine decomposing apparatus and fluorocarbon gas decomposing apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008206801A (en) * 2007-02-27 2008-09-11 Kanji Kokubu Pcb decomposition processing unit
JP2011121900A (en) * 2009-12-10 2011-06-23 Oriental Kiden Kk Treatment apparatus for harmful substance-containing liquid
JP2013519503A (en) * 2010-02-10 2013-05-30 ゾレッジ‐ガレトン,アルフレド Method and apparatus for applying plasma particles to a liquid and use for sterilizing water

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