JP2002059145A - Decomposition treatment method for hardly decomposable organic compounds - Google Patents
Decomposition treatment method for hardly decomposable organic compoundsInfo
- Publication number
- JP2002059145A JP2002059145A JP2000246421A JP2000246421A JP2002059145A JP 2002059145 A JP2002059145 A JP 2002059145A JP 2000246421 A JP2000246421 A JP 2000246421A JP 2000246421 A JP2000246421 A JP 2000246421A JP 2002059145 A JP2002059145 A JP 2002059145A
- Authority
- JP
- Japan
- Prior art keywords
- organic compound
- hardly decomposable
- decomposable organic
- decomposing
- heating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 150000002894 organic compounds Chemical class 0.000 title claims abstract description 95
- 238000000034 method Methods 0.000 title claims description 50
- 238000000354 decomposition reaction Methods 0.000 title description 33
- 238000010438 heat treatment Methods 0.000 claims description 53
- 238000010894 electron beam technology Methods 0.000 claims description 35
- 239000002023 wood Substances 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 4
- 239000004033 plastic Substances 0.000 claims description 4
- 229920003023 plastic Polymers 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 150000003071 polychlorinated biphenyls Chemical class 0.000 abstract description 36
- 238000001704 evaporation Methods 0.000 description 15
- 230000008020 evaporation Effects 0.000 description 15
- 239000003921 oil Substances 0.000 description 13
- 238000012545 processing Methods 0.000 description 10
- 238000011084 recovery Methods 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- 231100000987 absorbed dose Toxicity 0.000 description 5
- 239000003990 capacitor Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 150000002013 dioxins Chemical class 0.000 description 4
- 238000009835 boiling Methods 0.000 description 3
- 230000001678 irradiating effect Effects 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 239000000460 chlorine Substances 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001784 detoxification Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010891 electric arc Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- 102100033040 Carbonic anhydrase 12 Human genes 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 101000867855 Homo sapiens Carbonic anhydrase 12 Proteins 0.000 description 1
- 101100219325 Phaseolus vulgaris BA13 gene Proteins 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000006298 dechlorination reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000002837 defoliant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000005674 electromagnetic induction Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000009489 vacuum treatment Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/82—Recycling of waste of electrical or electronic equipment [WEEE]
Landscapes
- Fire-Extinguishing Compositions (AREA)
- Processing Of Solid Wastes (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
(57)【要約】
【課題】 電気部材からPCB等を除去して無害化でき
ると共に回収したPCB等を効率良く安価な設備で分解
処理する。
【解決手段】 PCB等の難分解性有機化合物を含有し
た電気部材1を減圧下で加熱して難分解性有機化合物を
蒸発除去し、この蒸発除去された気体状の難分解性有機
化合物を電子線照射によって分解する。
(57) [Summary] [PROBLEMS] To remove PCBs and the like from electric members and render them harmless, and to disassemble and recover the collected PCBs and the like efficiently and at low cost. SOLUTION: An electric member 1 containing a hardly decomposable organic compound such as PCB is heated under reduced pressure to evaporate and remove the hardly decomposable organic compound. Decomposes by irradiation.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、PCB(ポリ塩素
化ビフェニル)等の難分解性有機化合物を含有するトラ
ンスやコンデンサ等の電気部材から難分解性有機化合物
を除去して分解する難分解性有機化合物の分解処理方法
に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a hardly decomposable organic compound such as a PCB (polychlorinated biphenyl) which is hardly decomposable by removing the hardly decomposable organic compound from an electric member such as a transformer or a capacitor. The present invention relates to a method for decomposing organic compounds.
【0002】[0002]
【従来の技術】我国においては、PCBやダイオキシン
等の難分解性有機化合物の無害化処理技術の開発が行わ
れている。特に、PCBは製造、輸入、使用等に関して
各種の指導および規制が行われ、PCBが使用されるコ
ンデンサやトランスなどの電気部材は使用者が厳重に保
管および管理することが義務付けられている。しかし、
PCBを含む電気部材の保管および管理の継続は安全上
のリスクが伴うのはもちろんのこと、経済的にも難しく
なりつつあり、環境安全面および経済効果面から安全な
処理方法の確立が望まれている。また、これら電気部材
は貴重な資源である銅や鉄などからなり、再利用の観点
からもこれに付着あるいは含浸しているPCBを安全な
処理方法で除去し、電気部材を無害化することが望まれ
ている。2. Description of the Related Art In Japan, techniques for detoxifying insoluble organic compounds such as PCB and dioxin have been developed. In particular, various instructions and regulations are given to the manufacture, import, use, etc. of PCBs, and it is mandatory for users to strictly store and manage electrical members such as capacitors and transformers in which PCBs are used. But,
Continuation of storage and management of electrical components including PCBs involves not only safety risks but also economic difficulties, and it is desired to establish safe treatment methods from the viewpoint of environmental safety and economic effects. ing. In addition, these electric members are made of precious resources such as copper and iron, and from the viewpoint of reuse, it is possible to remove PCBs adhered or impregnated by safe processing methods to make the electric members harmless. Is desired.
【0003】このような状況下、配電用柱上トランスか
ら抜油した後に、真空加熱によりPCB等を蒸発して回
収する方法が提案されている(特開平9−192534
号公報および特開平9−192535号公報参照)。ま
た、PCB等を含有するトランスやコンデンサを抜油す
ることなく真空加熱して、PCB等を蒸発させ回収する
方法が提案されている(特開平11−309222号公
報参照)。Under such circumstances, a method has been proposed in which after removing oil from a transformer on a power distribution pole, PCBs or the like are evaporated and recovered by vacuum heating (JP-A-9-192534).
And JP-A-9-192535). In addition, a method has been proposed in which a transformer or a capacitor containing PCB or the like is heated in vacuum without removing oil to evaporate and collect the PCB or the like (see JP-A-11-309222).
【0004】[0004]
【発明が解決しようとする課題】しかしながら、上述し
たPCB等の各除去方法は電気部材から完全にPCB等
を除去し電気部材を無害化するものなので、回収したP
CB等は別途化学処理などにより無害化する必要があ
る。このため、真空加熱装置の他にPCB等の分解処理
装置の設備が必要になってしまい、設備コストが膨大な
ものとなってしまう。また、真空加熱装置と分解処理装
置とは別々の設備であるので、周囲の環境の安全を確実
にするためには別々の安全系の設備が必要となり、安全
設備のための投資も膨大なものになってしまう。However, since each of the above-described methods for removing PCBs and the like completely removes PCBs and the like from electrical members and renders the electrical members harmless, the collected P
CB or the like must be separately rendered harmless by chemical treatment or the like. For this reason, in addition to the vacuum heating device, equipment for a decomposition processing apparatus such as a PCB is required, and the equipment cost is enormous. In addition, since the vacuum heating device and the decomposition treatment device are separate equipment, separate safety equipment is required to ensure the safety of the surrounding environment, and investment in safety equipment is enormous. Become.
【0005】さらに、真空加熱装置と分解処理装置を単
に同一箇所に設置しても、真空加熱方法により蒸発して
きたPCB等は一度冷却回収してから分解処理装置に導
入する必要があるので、熱効率や作業効率は良くない。Further, even if the vacuum heating apparatus and the decomposition processing apparatus are simply installed at the same location, it is necessary to cool and recover the PCB and the like evaporated by the vacuum heating method once and then introduce the same into the decomposition processing apparatus. And work efficiency is not good.
【0006】そこで、本発明は、電気部材からPCB等
を除去して無害化できると共に回収したPCB等を効率
良く安価な設備で分解処理できる難分解性有機化合物の
分解処理方法を提供することを目的とする。Accordingly, the present invention is to provide a method for decomposing a hardly decomposable organic compound, which can remove PCBs and the like from electrical members to make them harmless and can decompose collected PCBs and the like efficiently and at low cost. Aim.
【0007】[0007]
【課題を解決するための手段】かかる目的を達成するた
め、請求項1記載の難分解性有機化合物の分解処理方法
は、難分解性有機化合物を含有した電気部材を減圧下で
加熱して難分解性有機化合物を蒸発除去し、この蒸発除
去された気体状の難分解性有機化合物を電子線照射によ
って分解するようにしている。In order to achieve the above object, a method for decomposing a hardly decomposable organic compound according to the present invention comprises heating an electric member containing the hardly decomposable organic compound under reduced pressure. The decomposable organic compound is removed by evaporation, and the evaporated and hardly decomposable organic compound removed by evaporation is decomposed by electron beam irradiation.
【0008】したがって、PCB等の難分解性有機化合
物を含有したトランスやコンデンサ等の電気部材を減圧
下で加熱(以下、「真空加熱処理」という)して難分解
性有機化合物を蒸発させることにより、電気部材から難
分解性有機化合物を除去することができる。そして、蒸
発された難分解性有機化合物を気体状のままで電子線照
射によって分解処理しているので、電気部材から回収し
た難分解性有機化合物を従来のように冷却して別個の分
解処理装置に移送させることなく分解処理することがで
きる。よって、電気部材からの難分解性有機化合物の除
去と難分解性有機化合物の分解処理を効率良く安価に行
うことができるようになる。Accordingly, electric members such as transformers and capacitors containing a hardly decomposable organic compound such as PCB are heated under reduced pressure (hereinafter referred to as "vacuum heat treatment") to evaporate the hardly decomposable organic compound. In addition, the hardly decomposable organic compound can be removed from the electric member. Since the evaporated hardly decomposable organic compound is decomposed by irradiating an electron beam in a gaseous state, the hardly decomposable organic compound recovered from the electric member is cooled as in the conventional case and a separate decomposer is used. Can be disassembled without being transferred to Therefore, the removal of the hardly decomposable organic compound from the electric member and the decomposition treatment of the hardly decomposable organic compound can be performed efficiently and inexpensively.
【0009】また、請求項2記載の発明は、請求項1記
載の難分解性有機化合物の分解処理方法において、電気
部材の加熱は、100mbar以下の雰囲気中で行われ
るようにしている。ここで、雰囲気を100mbarを
超えるようにした場合は、難分解性有機化合物の加熱蒸
発が良好に行われず処理コストに対する分解効率が悪く
なってしまう。このため、雰囲気を100mbar以下
にする場合が難分解性有機化合物の加熱蒸発を良好に行
うことができる。なお、本明細書中で「真空」とは、完
全な真空(0mbar)を意味するだけでなく、大気圧
より減圧された雰囲気を含めた概念としている。According to a second aspect of the present invention, in the method for decomposing a hardly decomposable organic compound according to the first aspect, the heating of the electric member is performed in an atmosphere of 100 mbar or less. Here, if the atmosphere exceeds 100 mbar, the evaporation of the hardly decomposable organic compound is not performed well, and the decomposition efficiency with respect to the processing cost is deteriorated. Therefore, when the atmosphere is set to 100 mbar or less, the evaporation of the hardly decomposable organic compound can be favorably performed by heating. In this specification, “vacuum” means not only a complete vacuum (0 mbar) but also a concept including an atmosphere reduced in pressure from the atmospheric pressure.
【0010】さらに、請求項3記載の発明は、請求項1
または2記載の難分解性有機化合物の分解処理方法にお
いて、電気部材の加熱は100〜650℃で行われるよ
うにしている。ここで、電気部材の加熱を100℃未満
にした場合は、難分解性有機化合物が十分に蒸発されな
い。また、電気部材の加熱を650℃を超えるようにし
た場合は、熱効率が悪いと共に加熱炉に高い耐久性が必
要になってしまい実用的でない。このため、電気部材の
加熱温度を100〜650℃にした場合が難分解性有機
化合物の加熱蒸発を最も良好かつ効率良く行うことがで
きる。[0010] Further, the invention according to claim 3 is based on claim 1.
Alternatively, in the method for decomposing a hardly decomposable organic compound described in 2, the electric member is heated at 100 to 650 ° C. Here, when the heating of the electric member is set to less than 100 ° C., the hardly decomposable organic compound is not sufficiently evaporated. If the heating of the electric member is made to exceed 650 ° C., the heat efficiency is low and the heating furnace needs to have high durability, which is not practical. Therefore, when the heating temperature of the electric member is set to 100 to 650 ° C., the evaporation of the hardly decomposable organic compound can be performed best and efficiently.
【0011】また、請求項4記載の発明は、請求項1か
ら3までのいずれか記載の難分解性有機化合物の分解処
理方法において、電子線照射による難分解性有機化合物
の分解は100mbar以下の雰囲気中で行われるよう
にしている。ここで、雰囲気を100mbarを超える
ようにした場合は、難分解性有機化合物の分解が良好に
行われず処理コストに対する分解効率が悪くなってしま
う。このため、雰囲気を100mbar以下とした場合
が難分解性有機化合物の分解を良好に行うことができ
る。According to a fourth aspect of the present invention, in the method for decomposing a hardly decomposable organic compound according to any one of the first to third aspects, the decomposition of the hardly decomposable organic compound by irradiation with an electron beam is 100 mbar or less. It is done in an atmosphere. Here, when the atmosphere exceeds 100 mbar, the decomposition of the hardly decomposable organic compound is not performed well, and the decomposition efficiency with respect to the processing cost is deteriorated. Therefore, when the atmosphere is 100 mbar or less, the decomposition of the hardly decomposable organic compound can be favorably performed.
【0012】一方、請求項5記載の難分解性有機化合物
の分解処理方法は、原姿の電気部材に難分解性有機化合
物の除去処理を施し、その後、処理された電気部材を解
体し、金属やプラスチック類から成る部材を難分解性処
理物として処理すると共に、残りの紙や木類から成る部
材から請求項1から4までのいずれか記載の難分解性有
機化合物の分解処理方法により難分解性有機化合物を除
去し分解するようにしている。この場合、難分解性有機
化合物の除去が比較的困難な紙や木類から成る部材にお
いてもその除去を良好に行えると共に、除去した難分解
性有機化合物の分解処理を効率良く安価に行うことがで
きるようになる。On the other hand, in the method for decomposing a hardly decomposable organic compound according to claim 5, the electric member in its original form is subjected to a process for removing the hardly decomposable organic compound, and then the treated electric member is disassembled to remove metal. And a member made of plastics or the like is treated as a hardly decomposable material, and the remaining member made of paper or wood is hardly decomposed by the method of any one of claims 1 to 4. Organic compounds are removed and decomposed. In this case, it is possible to satisfactorily remove the hardly decomposable organic compound even from a member made of paper or wood from which it is relatively difficult to remove the hardly decomposable organic compound, and efficiently and inexpensively perform the decomposition treatment of the hardly decomposable organic compound. become able to.
【0013】[0013]
【発明の実施の形態】以下、本発明の構成を図面に示す
実施の形態の一例に基づいて詳細に説明する。本発明の
難分解性有機化合物の分解処理方法の第1の実施形態で
は、PCB等の難分解性有機化合物を含有した電気部材
を減圧下で加熱して難分解性有機化合物を蒸発除去し、
この蒸発除去された気体状の難分解性有機化合物を電子
線照射によって分解するようにしている。このため、蒸
発された難分解性有機化合物をそのまま電子線照射によ
って分解処理しているので、電気部材から回収した難分
解性有機化合物を従来のように一旦冷却して別個の分解
処理装置に移送させることなく分解処理することができ
る。よって、電気部材からの難分解性有機化合物の除去
と無害化を効率良く安価に行うことができるようにな
る。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The configuration of the present invention will be described below in detail based on an example of an embodiment shown in the drawings. In the first embodiment of the method for decomposing a hardly decomposable organic compound of the present invention, an electric member containing a hardly decomposable organic compound such as PCB is heated under reduced pressure to evaporate and remove the hardly decomposable organic compound,
The gaseous hardly decomposable organic compound removed by evaporation is decomposed by electron beam irradiation. For this reason, since the evaporated hardly decomposable organic compound is directly decomposed by electron beam irradiation, the hardly decomposable organic compound recovered from the electric member is once cooled and transferred to a separate decomposer as in the conventional case. Decomposition processing can be performed without causing the decomposition. Therefore, it becomes possible to efficiently and inexpensively remove and detoxify the hard-to-decompose organic compound from the electrical member.
【0014】ここでの難分解性有機化合物とは、PCB
及びその誘導体やダイオキシン、農薬(DDTや枯葉
剤)等の難分解性有機化合物およびこれらの化合物を含
有した油を包含した概念としている。電気部材とは、難
分解性有機化合物を含有するトランスやコンデンサ等の
電気機器や難分解性有機化合物に汚染された物品を含む
概念としている。The hardly decomposable organic compound used herein is PCB
And its derivatives, dioxins, hardly decomposable organic compounds such as pesticides (DDT and defoliants), and oils containing these compounds. The term “electric member” is a concept including electric equipment such as a transformer and a capacitor containing a hardly decomposable organic compound and articles contaminated with the hardly decomposable organic compound.
【0015】また、電気部材の加熱は100mbar以
下の雰囲気中で行われることが好ましい。雰囲気が10
0mbarを超えるようにした場合は処理コストに対す
る蒸発効率が悪くなってしまうが、雰囲気を100mb
ar以下とすることにより難分解性有機化合物の加熱蒸
発を良好に行うことができる。The heating of the electric member is preferably performed in an atmosphere of 100 mbar or less. Atmosphere is 10
If it exceeds 0 mbar, the evaporation efficiency with respect to the processing cost will be deteriorated.
By setting the ratio to ar or less, the heat evaporation of the hardly decomposable organic compound can be favorably performed.
【0016】そして、電気部材の真空加熱雰囲気は、難
分解性有機化合物が蒸発している最中は真空度が余り上
がらず、蒸発が終わると真空度が上がるようになる。し
かし、実際には、0.01mbarよりも減圧しようと
すると膨大なエネルギや大掛かりな設備が必要になるこ
とから、コストおよび効率の観点から真空度は最高でも
0.01mbar程度にすることが好ましい。In the vacuum heating atmosphere of the electric member, the degree of vacuum does not increase so much during the evaporation of the hardly decomposable organic compound, and the degree of vacuum increases after the evaporation is completed. However, in practice, if the pressure is reduced below 0.01 mbar, enormous energy and large-scale equipment are required. Therefore, from the viewpoint of cost and efficiency, it is preferable that the degree of vacuum be at most about 0.01 mbar.
【0017】ここで、常圧でのPCBや絶縁油の平均沸
点は約350℃、このときの最高沸点は約450℃であ
る。これを真空(0.05mbar)状態に換算すると
約120℃になる。したがって、100℃未満で電気部
材の真空加熱を行っても効果が低く実用的でない。ま
た、650℃を超える雰囲気で電気部材の加熱を行うこ
とは、熱効率が悪いと共に加熱炉に高い耐久性が必要に
なってしまい実用的でない。したがって、電気部材の加
熱は100〜650℃で行われることが好ましい。Here, the average boiling point of PCB and insulating oil at normal pressure is about 350 ° C., and the maximum boiling point at this time is about 450 ° C. This is about 120 ° C. when converted to a vacuum (0.05 mbar) state. Therefore, even if vacuum heating of the electric member is performed at a temperature lower than 100 ° C., the effect is low and it is not practical. Further, it is not practical to heat the electric member in an atmosphere exceeding 650 ° C. because the heat efficiency is low and the heating furnace needs to have high durability. Therefore, the heating of the electric member is preferably performed at 100 to 650 ° C.
【0018】また、電気部材の加熱処理は250〜40
0℃で行うことがより好ましい。この条件によれば、例
えば真空度100mbarで400℃の条件は常圧の約
530℃に相当するので、PCBの常圧の最高沸点(約
450℃)まで十分に加熱することができ、例えば柱上
トランス以外に用いられるような高濃度PCBを蒸発加
熱することが可能になる。しかも、この温度範囲であれ
ば、電気部材の紙や木あるいはプラスチックが炭化し、
熱効率および蒸発処理の観点からより好ましい加熱処理
を実現することができる。Further, the heat treatment of the electric member is 250 to 40.
More preferably, it is performed at 0 ° C. Under these conditions, for example, a condition of 400 ° C. at a degree of vacuum of 100 mbar corresponds to about 530 ° C. of normal pressure, so that the PCB can be sufficiently heated to the maximum boiling point of normal pressure (about 450 ° C.). It becomes possible to evaporate and heat high-concentration PCBs used for other than the upper transformer. Moreover, within this temperature range, the paper, wood or plastic of the electrical member is carbonized,
A more preferable heat treatment can be realized from the viewpoint of heat efficiency and evaporation treatment.
【0019】電子線照射としては、難分解性有機化合物
を分解するために電子を照射することの全般を含み、ア
ーク放電やコロナ放電等の放電現象も含む概念としてい
る。この電子線照射により難分解性有機化合物を分解し
て無害な物質に変換することができる。ここで、この分
解処理方法では、電子線照射により難分解性有機化合物
を完全に分解して無害化することには限られず、分解に
より低塩素化物に変質させるようにしても良い。この場
合、電子線照射の作業を、廃棄物処理法で定められてい
る化学処理法を適用し易くする前処理として有効に活用
することができる。The term “electron beam irradiation” includes a general concept of irradiating electrons to decompose a hardly decomposable organic compound, and also includes a discharge phenomenon such as arc discharge or corona discharge. By this electron beam irradiation, the hardly decomposable organic compound can be decomposed and converted into a harmless substance. Here, this decomposition treatment method is not limited to completely decomposing the hardly decomposable organic compound by electron beam irradiation to render it harmless, but it may be changed to a low chlorinated product by decomposition. In this case, the operation of the electron beam irradiation can be effectively utilized as a pretreatment for facilitating the application of the chemical treatment method defined in the waste treatment method.
【0020】また、電子線照射による分解は100mb
ar以下の雰囲気中で行われることが好ましい。雰囲気
を100mbarを超えるようにした場合は処理コスト
に対する分解効率が悪くなってしまうので、雰囲気を1
00mbar以下とすることにより難分解性有機化合物
の分解を最も良好に行うことができる。そして、実際に
は、0.01mbarよりも減圧しようとすると膨大な
エネルギや大掛かりな設備が必要になることから、コス
トおよび効率の観点から真空度は最高でも0.01mb
ar程度にすることが好ましい。Decomposition by electron beam irradiation is 100 mb
It is preferably performed in an atmosphere of ar or less. If the atmosphere exceeds 100 mbar, the decomposition efficiency with respect to the processing cost deteriorates.
The decomposition of the hardly decomposable organic compound can be performed most preferably by setting the pressure to 00 mbar or less. Actually, if the pressure is reduced to less than 0.01 mbar, enormous energy and large-scale equipment are required. Therefore, from the viewpoint of cost and efficiency, the degree of vacuum is at most 0.01 mbar.
It is preferably about ar.
【0021】そして、難分解性有機化合物は分解により
無害化されているが、必要に応じて無害化後の気体状の
難分解性有機化合物を真空コンデンサや真空オイルシャ
ワー等により冷却および凝縮して回収し完全に除去する
ようにしても良い。The hardly decomposable organic compound is detoxified by decomposition. If necessary, the detoxified gaseous hardly decomposable organic compound is cooled and condensed by a vacuum condenser or a vacuum oil shower or the like. You may make it collect | recover and remove completely.
【0022】さらに、真空加熱処理および電子線照射を
減圧下で行うために排気が発生するが、この排気は活性
炭吸着装置等の排気安全系により清浄化して環境汚染を
確実に防止することが好ましい。Further, since the vacuum heating process and the electron beam irradiation are performed under reduced pressure, exhaust gas is generated. It is preferable that the exhaust gas is cleaned by an exhaust gas safety system such as an activated carbon adsorption device to surely prevent environmental pollution. .
【0023】ところで、ダイオキシン類の生成の条件と
しては、所定量の酸素、塩素、ベンゼン環、並びに40
0℃以上の温度が必要であるが、本実施形態の分解処理
方法によれば、真空下の無酸素状態で加熱および電子線
照射を実施しているので、ダイオキシン類の発生を防止
することができる。すなわち、電子線照射によりPCB
が分解して生成された塩素がPCBの分解物と反応して
も、酸素濃度が低いのでダイオキシン類の発生は無い。The conditions for producing dioxins include a predetermined amount of oxygen, chlorine, a benzene ring,
Although a temperature of 0 ° C. or higher is required, according to the decomposition treatment method of this embodiment, since heating and electron beam irradiation are performed in an oxygen-free state under vacuum, the generation of dioxins can be prevented. it can. That is, PCB irradiation by electron beam irradiation
Even if chlorine generated by the decomposition of the compound reacts with the decomposition product of PCB, no dioxins are generated because the oxygen concentration is low.
【0024】次に、難分解性有機化合物の分解処理方法
の第2の実施形態について説明する。この分解処理方法
では、原姿の電気部材に難分解性有機化合物の除去処理
を施し、その後、処理された電気部材を解体する。ここ
での除去処理法としては、真空加熱処理に限られず、廃
棄物処理法で定められた溶剤洗浄等の方法でも良い。そ
して、金属やプラスチック類から成る部材を難分解性処
理物として処理すると共に、残りの紙や木類から成る部
材から上述した第1の実施形態の分解処理方法により難
分解性有機化合物を除去し分解する。Next, a second embodiment of a method for decomposing a hardly decomposable organic compound will be described. In this decomposition treatment method, the electric member in its original form is subjected to a removal treatment of a hardly decomposable organic compound, and thereafter, the treated electric member is disassembled. The removal method here is not limited to the vacuum heat treatment, but may be a method such as solvent washing defined by the waste treatment method. Then, the member made of metal or plastic is treated as a hardly decomposable material, and the hardly decomposable organic compound is removed from the remaining member made of paper or wood by the decomposition method of the first embodiment described above. Decompose.
【0025】この場合、難分解性有機化合物の除去が比
較的困難な紙や木類から成る部材においてもその除去を
良好に行えると共に、除去した難分解性有機化合物の分
解処理を効率良く安価に行うことができるようになる。In this case, the removal of the hardly decomposable organic compound can be satisfactorily performed even on a member made of paper or wood from which it is relatively difficult to remove the hardly decomposable organic compound. Will be able to do it.
【0026】なお、上述の実施形態は本発明の好適な実
施の一例ではあるがこれに限定されるものではなく本発
明の要旨を逸脱しない範囲において種々変形実施可能で
ある。例えば本実施形態では電子線照射を減圧下で行う
ようにしているが、これには限られず大気圧の雰囲気中
で行うようにしても良い。この場合も、電子線により気
体状の難分解性有機化合物の分解処理を行うことができ
る。The above embodiment is an example of a preferred embodiment of the present invention, but the present invention is not limited to this, and various modifications can be made without departing from the spirit of the present invention. For example, in the present embodiment, the electron beam irradiation is performed under reduced pressure, but is not limited to this, and may be performed in an atmosphere of atmospheric pressure. Also in this case, a gaseous hardly decomposable organic compound can be decomposed by an electron beam.
【0027】また、真空加熱を行う温度や気圧、あるい
は電子線照射を行う気圧は、上述した範囲の値に限られ
ないのは勿論である。The temperature and pressure at which the vacuum heating is performed and the pressure at which the electron beam irradiation is performed are not limited to the above-mentioned range.
【0028】[0028]
【実施例】以下、本発明を実施例により更に具体的に説
明する。EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples.
【0029】図1は、本発明の難分解性有機化合物の分
解処理方法の一実施例における処理プロセスを装置と共
に示すフロー図である。この実施例の装置は、電気部材
1を減圧下で加熱する真空加熱設備2と、気体状の難分
解性有機化合物を分解する電子線照射設備3と、分解に
より得られた生成物を冷却し回収する回収設備4と、真
空系からの排気の無害化を確実にする排気安全対策設備
5とを備えている。FIG. 1 is a flow chart showing a treatment process and an apparatus in one embodiment of the method for decomposing a hardly decomposable organic compound of the present invention. The apparatus of this embodiment includes a vacuum heating facility 2 for heating an electric member 1 under reduced pressure, an electron beam irradiation facility 3 for decomposing gaseous hardly decomposable organic compounds, and cooling a product obtained by decomposition. A recovery facility 4 for recovery and an exhaust safety measure 5 for ensuring the detoxification of the exhaust from the vacuum system are provided.
【0030】真空加熱設備2は真空加熱炉であり、炉体
6と、炉体6の内部を加熱する加熱ヒータ(図示せず)
と、炉体6の内部を減圧する真空ポンプ7とを備えてい
る。加熱ヒータによる加熱方式としては、内部ヒータに
よる直接加熱や、外部ヒータによる間接加熱や、高周波
加熱あるいは電磁誘導加熱などのいずれでも良く、要は
電気部材1が所定の温度にまで加熱されるものであれば
良い。真空ポンプ7は、電子線照射設備3および回収設
備4を介して真空加熱設備2に接続されている。このた
め、真空ポンプ7の稼働により、真空加熱設備2と電子
線照射設備3と回収設備4とから成る真空系が減圧され
て真空状態に維持される。The vacuum heating equipment 2 is a vacuum heating furnace, and includes a furnace 6 and a heater (not shown) for heating the inside of the furnace 6.
And a vacuum pump 7 for reducing the pressure inside the furnace body 6. As a heating method using a heater, any of direct heating by an internal heater, indirect heating by an external heater, high-frequency heating, electromagnetic induction heating, and the like may be used. In short, the electric member 1 is heated to a predetermined temperature. I just want it. The vacuum pump 7 is connected to the vacuum heating equipment 2 via the electron beam irradiation equipment 3 and the recovery equipment 4. Therefore, by operating the vacuum pump 7, the vacuum system including the vacuum heating equipment 2, the electron beam irradiation equipment 3, and the recovery equipment 4 is depressurized and maintained in a vacuum state.
【0031】炉体6の内部に設置された電気部材1は、
減圧下で加熱ヒータにより加熱される。これにより、電
気部材1に含有された難分解性有機化合物(例えばPC
Bを含む絶縁油)が蒸発されて電気部材1から除去され
る。The electric member 1 installed inside the furnace body 6
Heated by a heater under reduced pressure. Thereby, the hardly decomposable organic compound (for example, PC
The insulating oil containing B) is evaporated and removed from the electric member 1.
【0032】電子線照射設備3は、真空状態の中を真空
加熱設備2から真空ポンプ7の方向へ流れる難分解性有
機化合物の原子や分子に電子線を照射する。これによ
り、難分解性有機化合物は脱塩素化や分子構造の破壊に
より分解して無害な物質となる。電子線照射としては、
例えばコロナ放電やアーク放電を利用することができ
る。The electron beam irradiation equipment 3 irradiates the atoms and molecules of the hardly decomposable organic compound flowing in the vacuum state from the vacuum heating equipment 2 toward the vacuum pump 7 with an electron beam. As a result, the hardly decomposable organic compound is decomposed into a harmless substance by dechlorination or destruction of the molecular structure. As electron beam irradiation,
For example, corona discharge or arc discharge can be used.
【0033】回収設備4は、真空コンデンサまたは真空
オイルシャワー、あるいはこれらの組み合わせとしてい
る。そして、回収設備4は、電子線照射設備3により分
解されて無害化された生成物を真空状態で冷却して凝縮
し回収する。さらに、この回収設備4で回収された物質
は、常圧状態に戻されてから必要に応じた適切な方法で
処理する。The recovery equipment 4 is a vacuum condenser or a vacuum oil shower, or a combination thereof. The recovery facility 4 cools, condenses and recovers the decomposed and detoxified product by the electron beam irradiation facility 3 in a vacuum state. Further, the substance recovered by the recovery facility 4 is returned to normal pressure and then processed by an appropriate method as needed.
【0034】排気安全対策設備5としては、通過した排
気が捕集される例えばダストフィルタや活性炭吸着部を
備えたものとしている。真空ポンプ7からの排気は、真
空系に含まれる空気と、真空加熱により分解されて生ず
る軽炭化水素類とを主成分とする分解ガスである。この
分解ガスには難分解性有機化合物は含まれておらず無害
であるが、排気安全対策設備5を通過することにより浄
化してから大気に放出されるので、環境への更なる安全
を確保することができる。The exhaust gas safety equipment 5 is provided with, for example, a dust filter and an activated carbon adsorbing section for collecting the exhaust gas passing therethrough. The exhaust gas from the vacuum pump 7 is a cracked gas mainly composed of air contained in the vacuum system and light hydrocarbons decomposed by vacuum heating. Although this decomposed gas does not contain a hardly decomposable organic compound and is harmless, it is purified by passing through the exhaust safety device 5 and then released to the atmosphere, so that further safety to the environment is ensured. can do.
【0035】上述した図1に示す構成を有する設備を用
いて、本発明の難分解性有機化合物の分解処理方法に従
って難分解性有機化合物の分解・回収実験を行った。Using the equipment having the configuration shown in FIG. 1 described above, a decomposition / recovery experiment of a hardly decomposable organic compound was conducted according to the method for decomposing a hardly decomposable organic compound of the present invention.
【0036】真空加熱設備2にPCB含有の絶縁油を入
れた電気部材1である容器を設置して、真空ポンプ7を
運転して炉体6内を減圧した。そして、炉体6内が1m
bar程度に減圧された時点で、加熱ヒータによる加熱
および電子線照射設備3での電子線照射を開始した。A container as the electric member 1 containing the insulating oil containing PCB was set in the vacuum heating equipment 2, and the inside of the furnace body 6 was depressurized by operating the vacuum pump 7. And the inside of the furnace body 6 is 1 m
When the pressure was reduced to about bar, heating by the heater and electron beam irradiation in the electron beam irradiation equipment 3 were started.
【0037】ここで、この真空度での絶縁油とPCBの
蒸発温度は約150℃である。このため、絶縁油の温度
が約150℃程度になると、加熱を続けても蒸発潜熱の
影響で絶縁油の温度上昇は僅かとなる。そこで、真空度
を維持したまま加熱を続けることにより、絶縁油および
PCBを全て蒸発させた。その後も加熱を続けて、容器
の温度が上昇し始めて200℃を越えた時点で加熱を止
めた。そして、回収設備4で回収された絶縁油およびP
CBの分解生成物中のPCBの残留率を求めた。Here, the evaporation temperature of the insulating oil and PCB at this degree of vacuum is about 150 ° C. For this reason, when the temperature of the insulating oil becomes about 150 ° C., the temperature rise of the insulating oil becomes small due to the influence of the latent heat of evaporation even if the heating is continued. Therefore, by continuing heating while maintaining the degree of vacuum, all of the insulating oil and PCB were evaporated. After that, heating was continued, and when the temperature of the container began to rise and exceeded 200 ° C., the heating was stopped. Then, the insulating oil and P
The residual ratio of PCB in the decomposition product of CB was determined.
【0038】上述したPCBの分解・回収実験を電子線
照射設備3での電子線の吸収線量を異ならせて行い、電
子線の吸収線量率とPCB残留率との関係を求めた。そ
の結果を図2に示す。同図に示すように、電子線の吸収
線量が増加するに従いPCB残留率が減少した。特に吸
収線量率を16以上とした場合は、PCB残留率が0と
なり、PCBが完全に分解されたことが判明した。The above-described decomposition / recovery experiment of the PCB was carried out by changing the absorbed dose of the electron beam in the electron beam irradiation equipment 3, and the relationship between the absorbed dose rate of the electron beam and the PCB residual ratio was obtained. The result is shown in FIG. As shown in the figure, the PCB residual ratio decreased as the absorbed dose of the electron beam increased. In particular, when the absorbed dose rate was 16 or more, the PCB residual rate was 0, indicating that the PCB was completely decomposed.
【0039】[0039]
【発明の効果】以上の説明より明らかなように、請求項
1記載の難分解性有機化合物の分解処理方法によれば、
電気部材から難分解性有機化合物を真空処理加熱により
除去すると共に蒸発した難分解性有機化合物に電子線照
射を行うことによって、電気部材の無害化処理と難分解
性有機化合物の分解処理とを連続的に行うことができ
る。このため、電気部材からの難分解性有機化合物の除
去およびその分解を簡単な工程によって効率良く行うこ
とができる。As is clear from the above description, according to the method for decomposing a hardly decomposable organic compound according to the first aspect,
By removing the hard-to-decompose organic compound from the electrical member by vacuum treatment and heating and irradiating the evaporated hard-to-decompose organic compound with an electron beam, the detoxification treatment of the electric member and the decomposition process of the hard-to-decompose organic compound are continuously performed Can be done Therefore, the removal of the hardly decomposable organic compound from the electric member and the decomposition thereof can be efficiently performed by a simple process.
【0040】また、減圧された密閉装置内で全ての反応
が完了するため、作業者に対する作業環境の安全性や一
般公衆に対する安全性が十分に保たれる。そして、少な
くとも真空加熱設備と電子線照射設備が有れば実施でき
るので、装置の小型化を図ることができる。このため、
本装置を移動式プラントにして、例えばトレーラーに積
載して、移送先で難分解性有機化合物の除去およびその
分解を行うオンサイト処理を実現することができる。Further, since all the reactions are completed in the decompressed sealing device, the safety of the working environment for the worker and the safety for the general public are sufficiently maintained. Since the present invention can be implemented as long as there is at least a vacuum heating facility and an electron beam irradiation facility, the apparatus can be downsized. For this reason,
The present apparatus can be a mobile plant, for example, loaded on a trailer to realize on-site processing for removing and decomposing a hardly decomposable organic compound at a transfer destination.
【0041】また、請求項2記載の難分解性有機化合物
の分解処理方法によれば、電気部材の加熱は100mb
ar以下の雰囲気中で行われるようにしているので、難
分解性有機化合物の加熱蒸発を最も良好に行うことがで
きる。Further, according to the method for decomposing a hardly decomposable organic compound according to the second aspect, the electric member is heated at 100 mb.
Since the heat treatment is performed in an atmosphere of ar or less, the heat evaporation of the hardly decomposable organic compound can be best performed.
【0042】さらに、請求項3記載の難分解性有機化合
物の分解処理方法によれば、電気部材の加熱は100〜
650℃で行われるようにしているので、難分解性有機
化合物の加熱蒸発を最も良好かつ効率良く行うことがで
きる。Further, according to the method for decomposing a hardly decomposable organic compound according to the third aspect, the heating of the electric member is 100 to 100.
Since the heat treatment is performed at 650 ° C., the evaporation of the hardly decomposable organic compound by heating can be performed most efficiently and efficiently.
【0043】また、請求項4記載の難分解性有機化合物
の分解処理方法によれば、電子線照射による難分解性有
機化合物の分解は100mbar以下の雰囲気中で行わ
れるようにしているので、難分解性有機化合物の分解を
最も良好に行うことができる。According to the method for decomposing a hardly decomposable organic compound, the decomposition of the hardly decomposable organic compound by electron beam irradiation is performed in an atmosphere of 100 mbar or less. The decomposition of the decomposable organic compound can be performed best.
【0044】一方、請求項5記載の難分解性有機化合物
の分解処理方法によれば、難分解性有機化合物の除去が
比較的困難な紙や木類から成る部材においてもその除去
を良好に行えると共に、除去した難分解性有機化合物の
分解処理を効率良く安価に行うことができるようにな
る。On the other hand, according to the method for decomposing a hardly decomposable organic compound according to the fifth aspect, even a member made of paper or wood from which it is relatively difficult to remove the hardly decomposable organic compound can be satisfactorily removed. At the same time, it becomes possible to efficiently and inexpensively decompose the removed hardly decomposable organic compound.
【図1】本発明の難分解性有機化合物の分解処理方法の
一実施形態における処理設備を示す概略図である。FIG. 1 is a schematic diagram showing processing equipment in one embodiment of the method for decomposing a hardly decomposable organic compound of the present invention.
【図2】電子線の吸収線量率とPCB残留率との関係を
示すグラフである。FIG. 2 is a graph showing a relationship between an absorbed dose rate of an electron beam and a PCB residual rate.
1 電気部材 2 真空加熱設備 3 電子線照射設備 1 electric member 2 vacuum heating equipment 3 electron beam irradiation equipment
───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 2E191 BA12 BA13 BD11 BD18 4D004 AA21 AB07 CA02 CA08 CA27 CA43 CB04 DA02 DA03 DA06 DA07 4G075 AA37 BA05 BB02 CA02 CA05 CA12 4H006 AA05 AC26 ────────────────────────────────────────────────── ─── Continued on front page F term (reference) 2E191 BA12 BA13 BD11 BD18 4D004 AA21 AB07 CA02 CA08 CA27 CA43 CB04 DA02 DA03 DA06 DA07 4G075 AA37 BA05 BB02 CA02 CA05 CA12 4H006 AA05 AC26
Claims (5)
を減圧下で加熱して前記難分解性有機化合物を蒸発除去
し、この蒸発除去された気体状の前記難分解性有機化合
物を電子線照射によって分解することを特徴とする難分
解性有機化合物の分解処理方法。1. An electric member containing a hardly decomposable organic compound is heated under reduced pressure to evaporate and remove the hardly decomposable organic compound. A method for decomposing a hardly decomposable organic compound, which is decomposed by irradiation.
以下の雰囲気中で行われることを特徴とする請求項1記
載の難分解性有機化合物の分解処理方法。2. The method according to claim 1, wherein the heating of the electric member is performed at 100 mbar.
The method for decomposing a hardly decomposable organic compound according to claim 1, which is performed in the following atmosphere.
℃で行われることを特徴とする請求項1または2記載の
難分解性有機化合物の分解処理方法。3. The heating of the electric member is performed at 100 to 650.
The method for decomposing a hardly decomposable organic compound according to claim 1 or 2, wherein the method is carried out at a temperature of ° C.
の雰囲気中で行われることを特徴とする請求項1から3
までのいずれか記載の難分解性有機化合物の分解処理方
法。4. The method according to claim 1, wherein the electron beam irradiation is performed in an atmosphere of 100 mbar or less.
The method for decomposing a hardly decomposable organic compound according to any one of the above.
化合物の除去処理を施し、その後、処理された前記電気
部材を解体し、金属やプラスチック類から成る部材を難
分解性処理物として処理すると共に、残りの紙や木類か
ら成る部材から請求項1から4までのいずれか記載の難
分解性有機化合物の分解処理方法により難分解性有機化
合物を除去し分解することを特徴とする難分解性有機化
合物の分解処理方法。5. The original electrical member is subjected to a treatment for removing the hardly decomposable organic compound, and then the electric member is disassembled, and a member made of metal or plastic is treated as a hardly decomposed material. The method is characterized by removing the hard-to-decompose organic compound from the remaining paper or wood member by the method for decomposing a hard-to-decompose organic compound according to any one of claims 1 to 4, and decomposing the remaining material. A method for decomposing hardly decomposable organic compounds.
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| JP2000246421A JP3659569B2 (en) | 2000-08-15 | 2000-08-15 | Method for decomposing persistent organic compounds |
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|---|---|---|---|
| JP2000246421A JP3659569B2 (en) | 2000-08-15 | 2000-08-15 | Method for decomposing persistent organic compounds |
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| Publication Number | Publication Date |
|---|---|
| JP2002059145A true JP2002059145A (en) | 2002-02-26 |
| JP3659569B2 JP3659569B2 (en) | 2005-06-15 |
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ID=18736736
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000246421A Expired - Fee Related JP3659569B2 (en) | 2000-08-15 | 2000-08-15 | Method for decomposing persistent organic compounds |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002336836A (en) * | 2001-05-14 | 2002-11-26 | Japan Atom Energy Res Inst | Device for purifying solids contaminated with dioxins and / or polychlorinated biphenyls |
| KR20030083373A (en) * | 2002-04-22 | 2003-10-30 | 유지고하라 | Rebirth device of polyvinylchloride |
| JP2007268423A (en) * | 2006-03-31 | 2007-10-18 | Mitsui Eng & Shipbuild Co Ltd | Method for separating and treating PCB contaminants |
| JP2009233657A (en) * | 2008-03-07 | 2009-10-15 | Hitachi Zosen Corp | Device and method for making pcb-contaminated electrical equipment harmless |
-
2000
- 2000-08-15 JP JP2000246421A patent/JP3659569B2/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002336836A (en) * | 2001-05-14 | 2002-11-26 | Japan Atom Energy Res Inst | Device for purifying solids contaminated with dioxins and / or polychlorinated biphenyls |
| KR20030083373A (en) * | 2002-04-22 | 2003-10-30 | 유지고하라 | Rebirth device of polyvinylchloride |
| JP2007268423A (en) * | 2006-03-31 | 2007-10-18 | Mitsui Eng & Shipbuild Co Ltd | Method for separating and treating PCB contaminants |
| JP2009233657A (en) * | 2008-03-07 | 2009-10-15 | Hitachi Zosen Corp | Device and method for making pcb-contaminated electrical equipment harmless |
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| Publication number | Publication date |
|---|---|
| JP3659569B2 (en) | 2005-06-15 |
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