JP2001327943A - Treatment device for decomposing nonmetal member constituting transformer, capacitor or the like contaminated by pcb or pressure-sensitive paper containing pcb and method using this device - Google Patents
Treatment device for decomposing nonmetal member constituting transformer, capacitor or the like contaminated by pcb or pressure-sensitive paper containing pcb and method using this deviceInfo
- Publication number
- JP2001327943A JP2001327943A JP2000151090A JP2000151090A JP2001327943A JP 2001327943 A JP2001327943 A JP 2001327943A JP 2000151090 A JP2000151090 A JP 2000151090A JP 2000151090 A JP2000151090 A JP 2000151090A JP 2001327943 A JP2001327943 A JP 2001327943A
- Authority
- JP
- Japan
- Prior art keywords
- pcb
- slurry
- contaminated
- pressure
- supercritical
- 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.)
- Pending
Links
- 239000003990 capacitor Substances 0.000 title claims abstract description 23
- 229910052755 nonmetal Inorganic materials 0.000 title claims abstract description 17
- 238000000034 method Methods 0.000 title claims description 15
- 239000002002 slurry Substances 0.000 claims abstract description 46
- 238000000354 decomposition reaction Methods 0.000 claims abstract description 32
- 239000004033 plastic Substances 0.000 claims abstract description 10
- 229920003023 plastic Polymers 0.000 claims abstract description 10
- 239000002023 wood Substances 0.000 claims abstract description 10
- 238000005805 hydroxylation reaction Methods 0.000 claims description 27
- 230000033444 hydroxylation Effects 0.000 claims description 26
- 239000007788 liquid Substances 0.000 claims description 21
- 238000006864 oxidative decomposition reaction Methods 0.000 claims 2
- 239000000123 paper Substances 0.000 abstract description 30
- 239000012530 fluid Substances 0.000 abstract description 6
- 239000000126 substance Substances 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 2
- 239000000470 constituent Substances 0.000 abstract 1
- 230000000266 injurious effect Effects 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 17
- 238000010298 pulverizing process Methods 0.000 description 13
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 10
- 150000003071 polychlorinated biphenyls Chemical class 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000007800 oxidant agent Substances 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 5
- 239000002184 metal Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- 230000003301 hydrolyzing effect Effects 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- -1 and if necessary Substances 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 238000001784 detoxification Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000003094 microcapsule Substances 0.000 description 2
- 125000000962 organic group Chemical group 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- 102100033040 Carbonic anhydrase 12 Human genes 0.000 description 1
- 102100033041 Carbonic anhydrase 13 Human genes 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 101000867855 Homo sapiens Carbonic anhydrase 12 Proteins 0.000 description 1
- 101000867860 Homo sapiens Carbonic anhydrase 13 Proteins 0.000 description 1
- 229910000990 Ni alloy Inorganic materials 0.000 description 1
- 101100219325 Phaseolus vulgaris BA13 gene Proteins 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 150000003841 chloride salts Chemical class 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002843 nonmetals Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000011802 pulverized particle Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/54—Improvements relating to the production of bulk chemicals using solvents, e.g. supercritical solvents or ionic liquids
-
- 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
- Y02W30/78—Recycling of wood or furniture waste
Landscapes
- Fire-Extinguishing Compositions (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、ポリ塩化ビフェニ
ル(以下、「PCB」と略称する)で汚染されたトラン
ス、コンデンサ等を構成する非金属部材またはPCBを
含む感圧紙を分解する装置および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 an apparatus and a method for disassembling pressure-sensitive paper containing non-metal members or PCBs constituting transformers, capacitors and the like contaminated with polychlorinated biphenyl (hereinafter abbreviated as "PCB"). It is about.
【0002】[0002]
【従来の技術】PCBは、耐熱性、化学的安定性および
絶縁性に優れているため、以前はコンデンサー、トラン
ス等の電気機器の絶縁油として、または感圧紙(ノンカ
ーボン紙)の発色剤の溶剤として広く用いられていた。
しかしながら、PCBは毒性が強いため、我が国では1
972年に製造、輸入および使用が原則として禁止され
た。2. Description of the Related Art PCBs are excellent in heat resistance, chemical stability and insulating properties. Therefore, they were previously used as insulating oil for electric equipment such as capacitors and transformers, or as a coloring agent for pressure-sensitive paper (non-carbon paper). It was widely used as a solvent.
However, PCB is highly toxic, and is one of the most common in Japan.
In 972, production, import and use were banned in principle.
【0003】トランス等の電気機器から抜き出したPC
Bや、PCBにより汚染された紙や木材等のPCB汚染
物を処理する方法としては、米国内では環境庁(EP
A)の認可を受けた焼却炉で焼却する方法が採用されて
いる。しかし、焼却時にダイオキシン等の有害物質が発
生する恐れがあるため、日本国内ではPCBおよびPC
B汚染物を焼却処分することは行なわれていない。[0003] PC extracted from electrical equipment such as a transformer
As a method for treating PCB contaminants such as paper and wood contaminated with B and PCBs, the United States Environmental Protection Agency (EP)
The method of incineration in an incinerator approved by A) is adopted. However, harmful substances such as dioxin may be generated during incineration.
There is no incineration of B contaminants.
【0004】従って、現在の日本では、PCBが充填さ
れたトランス、コンデンサ等の電気機器やPCBを含む
感圧紙は、そのまま特別管理の産業廃棄物として厳重に
保管されているだけであり、PCBの無害化の処理はほ
とんど行なわれていないのが現状である。しかし、保管
が必ずしも厳密に行なわれているとはいえず、保管され
たPCBによる環境汚染が懸念されるため、早急にPC
Bが充填されたトランス、コンデンサ等の電気機器を対
象とした安全で効率的なPCBの無害化処理が求められ
ている。[0004] Therefore, in Japan at present, pressure-sensitive paper containing PCBs and electrical equipment such as transformers and capacitors, and PCBs containing PCBs are only strictly stored as specially-managed industrial wastes. At present, detoxification is hardly performed. However, the storage is not always strictly performed, and there is a concern that the stored PCB may cause environmental pollution.
There is a need for safe and efficient PCB detoxification processing for electrical equipment such as transformers and capacitors filled with B.
【0005】PCBを含むトランス、コンデンサ等から
絶縁油としてのPCBを抜き出しトランス、コンデンサ
を洗浄してPCBを除染し、金属部品を回収する方法は
知られている。しかし、トランス、コンデンサは、内部
に構成部材として木材、紙、プラスチック等の非金属部
材を有しており、有害物質を発生させずにこれらの非金
属部材を効率的かつ有効に分解処理する装置や方法は知
られていなかった。There is known a method of extracting a PCB as insulating oil from a transformer, a capacitor or the like containing the PCB, washing the transformer and the capacitor, decontaminating the PCB, and collecting metal parts. However, transformers and capacitors have non-metallic members such as wood, paper, and plastic as components inside, and these devices efficiently and effectively disassemble these non-metallic members without generating harmful substances. And how it was not known.
【0006】また、PCBを含む感圧紙を効率的かつ有
効に分解処理する装置や方法も知られていなかった。[0006] Further, there has been no known apparatus or method for efficiently and effectively decomposing pressure-sensitive paper containing PCB.
【0007】[0007]
【発明が解決しようとする課題】上記した現状に鑑み、
本発明が解決しようとする課題は、PCBで汚染された
トランス、コンデンサ等を構成する非金属部材またはP
CBを含む感圧紙を、有害物質を発生させず効率的かつ
有効に分解する装置および方法を提供することにある。In view of the above situation,
The problem to be solved by the present invention is that a non-metallic member or P
An object of the present invention is to provide an apparatus and a method for efficiently and effectively decomposing pressure-sensitive paper containing CB without generating harmful substances.
【0008】[0008]
【課題を解決するための手段】上記課題を解決するため
の請求項1に記載した本発明は、PCBで汚染されたト
ランス、コンデンサ等を構成する紙、木材、プラスチッ
クからなる非金属部材を粗粉砕する粗粉砕手段と、前記
粗粉砕手段により粗粉砕された非金属部材をスラリー化
する粉砕スラリー手段と、前記粉砕スラリー手段により
得られるスラリー液を超臨界水酸化分解処理する超臨界
水酸化分解手段を有することを特徴とするPCBで汚染
されたトランス、コンデンサ等を構成する非金属部材の
分解処理装置に関するものである。According to the first aspect of the present invention, a non-metallic member made of paper, wood, plastic, etc., which constitutes a transformer, a capacitor, etc., contaminated with PCB is provided. Coarse pulverizing means for pulverizing, pulverizing slurry means for turning a non-metal member coarsely pulverized by the coarse pulverizing means into a slurry, and supercritical hydrolytic decomposition for supercritically hydrolyzing a slurry liquid obtained by the pulverizing slurry means The present invention relates to an apparatus for disassembling non-metal members constituting transformers, capacitors, etc., contaminated with PCB, characterized by having means.
【0009】上記課題を解決するための請求項2に記載
した本発明は、PCBを含む感圧紙スラリー化するスラ
リー手段と、前記スラリー手段により得られるスラリー
液を超臨界水酸化分解処理する超臨界水酸化分解手段を
有することを特徴とするPCBを含む感圧紙の分解処理
装置に関するものである。According to a second aspect of the present invention, there is provided a slurry means for forming a pressure-sensitive paper slurry containing PCB, and a supercritical solution for subjecting a slurry obtained by the slurry means to a supercritical hydroxylation decomposition treatment. The present invention relates to an apparatus for decomposing pressure-sensitive paper containing PCB, which has a hydroxylation decomposing means.
【0010】上記課題を解決するための請求項3に記載
した本発明は、PCBで汚染されたトランス、コンデン
サ等を構成する紙、木材、プラスチックからなる非金属
部材を粗粉砕し、微細化処理してスラリー化した後、ス
ラリー液を超臨界水酸化分解処理することを特徴とする
PCBで汚染されたトランス、コンデンサ等を構成する
非金属部材の分解処理方法に関するものである。The present invention as set forth in claim 3 for solving the above-mentioned problem is to provide a method for finely pulverizing non-metallic members made of paper, wood, and plastic which constitute a transformer, a capacitor, and the like, which are contaminated with PCB, and performing fine processing. The present invention relates to a method for decomposing non-metal members constituting transformers, capacitors and the like contaminated with PCB, which comprises subjecting a slurry liquid to supercritical hydroxylation decomposition treatment after slurrying.
【0011】上記課題を解決するための請求項4に記載
した本発明は、PCBを含む感圧紙をスラリー化し、ス
ラリー液を超臨界水酸化分解処理することを特徴とする
PCBを含む感圧紙の分解処理方法に関するものであ
る。According to a fourth aspect of the present invention, there is provided a pressure-sensitive paper containing PCB, wherein the pressure-sensitive paper containing PCB is slurried, and the slurry liquid is subjected to a supercritical oxidation decomposition treatment. It relates to a decomposition processing method.
【0012】[0012]
【発明の実施の形態】本発明の処理対象となるPCBで
汚染されたトランス、コンデンサ等を構成する非金属部
材とは、例えばPCBを含むトランスやコンデンサ等の
内部にあってこれらを構成する木材、紙、プラスチック
などをいう。これらの非金属部材は、トランス、コンデ
ンサ等からPCBを抜取り、洗浄する工程で発生するも
のである。また、PCBを含む感圧紙とは、ノンカーボ
ン紙としてマイクロカプセルが塗布された紙であり、発
色剤を溶解する溶媒としてPCBがマイクロカプセル内
に内包されているものである。BEST MODE FOR CARRYING OUT THE INVENTION Non-metal members constituting transformers, capacitors and the like contaminated with PCB to be treated according to the present invention are, for example, woods inside transformers and capacitors containing PCBs and constituting these components. , Paper, plastic, etc. These non-metallic members are generated in the process of removing and cleaning the PCB from a transformer, a capacitor, and the like. The pressure-sensitive paper containing PCB is paper coated with microcapsules as non-carbon paper, and is PCB in which microcapsules are contained as a solvent for dissolving the color former.
【0013】実施形態1 本発明の請求項1に記載された分解処理装置の一実施形
態を図1により説明する。図1中、1の粗粉砕手段と
は、PCBで汚染された金属部品、磁性部品を除く紙、
木材、プラスチックからなる非金属部材をスラリー化す
るための前処理として粗粉砕するものである。粗粉砕手
段としては、PCBで汚染された非金属部材を数ミリ程
度に粉砕できるものであれば特に限定されないが、カッ
ターミル等を挙げることができる。Embodiment 1 An embodiment of the decomposition processing apparatus according to the present invention will be described with reference to FIG. In FIG. 1, 1 coarse crushing means means paper except metal parts and magnetic parts contaminated with PCB,
This is a method of roughly pulverizing non-metal members made of wood and plastic as a pretreatment for making a slurry. The coarse pulverizing means is not particularly limited as long as it can pulverize the non-metal member contaminated with PCB to about several millimeters, and examples thereof include a cutter mill.
【0014】2のスラリー化手段とは、前記粗粉砕手段
で粗粉砕された非金属部材をスラリー化するための手段
であり、例えばミル式粉砕器や回転刃式ホモジナイザー
等の微粉砕装置により非金属部材を1mm以下に微粉砕
し、この微粉砕粒子を水等の液状媒質に攪拌機等を用い
て分散させ、スラリー液とするための手段である。非金
属部材が、プラスチック、木の場合はミル式粉砕器が好
ましく、紙の場合は回転刃式ホモジナイザーが好まし
い。微粉砕装置は、乾式でも湿式であってもよい。適当
な濃度でスラリー化することにより、後述の超臨界水酸
化分解装置への移送を容易に行なうことができ、配管に
閉塞することがない。The slurrying means 2 is a means for slurrying the non-metal member coarsely pulverized by the coarse pulverizing means. For example, the non-metallic member is non-metallized by a fine pulverizing device such as a mill pulverizer or a rotary blade homogenizer. This is a means for finely pulverizing a metal member to 1 mm or less and dispersing the finely pulverized particles in a liquid medium such as water using a stirrer or the like to form a slurry liquid. If the non-metallic member is plastic or wood, a mill-type crusher is preferable, and if it is paper, a rotary blade homogenizer is preferable. The pulverizing device may be a dry type or a wet type. By forming the slurry at an appropriate concentration, it is possible to easily transfer the slurry to a supercritical hydroxylation / decomposition apparatus described below, and the pipe is not blocked.
【0015】スラリー液の濃度は、0.05〜10重量
%、好ましくは0.1〜5重量%の範囲で選択すればよ
い。スラリー濃度が0.05重量%未満の場合は、効率
が悪くなり処理装置が大きくなる点で好ましくない。1
0重量%を超える場合は、濃度が高すぎ粘性が高くなり
スムーズに送液できなくなる可能性や、スラリーが装置
内で閉塞する可能性があり、好ましくない。The concentration of the slurry liquid may be selected in the range of 0.05 to 10% by weight, preferably 0.1 to 5% by weight. If the slurry concentration is less than 0.05% by weight, the efficiency becomes poor and the processing apparatus becomes large, which is not preferable. 1
If it exceeds 0% by weight, the concentration is too high and the viscosity becomes too high to make it possible to feed the solution smoothly, and the slurry may be blocked in the apparatus, which is not preferable.
【0016】超臨界水酸化分解手段3は、公知のものを
採用すればよい。超臨界水酸化分解手段3としては、超
臨界状態の水と酸化剤の存在下に微粉砕された非金属部
材の酸化分解を行う反応器を備えた超臨界水酸化分解装
置を挙げることができる。反応器において行なわれる超
臨界水酸化分解反応は、水を超臨界状態とする温度、圧
力条件であれば特に限定されるものではないが、例え
ば、温度374℃以上、好ましくは550〜650℃、
かつ圧力22MPa以上、好ましくは22〜25MPa
の条件とすればよい。酸化剤としては、例えば空気、純
酸素、過酸化水素、液体酸素を挙げることができ、これ
らの酸化剤は化学量論要求量以上用いればよい。超臨界
水酸化分解を行う反応器は、パイプ(管状)型、ベッセ
ル型のいずれでもよい。PCBを含む非金属部材スラリ
ーを超臨界水酸化分解するに際して、必要に応じてイソ
プロピルアルコール等の補助燃料を用いてもよい。スラ
リー液と、必要であれば水および酸化剤をコンプレッサ
ー等で所定圧力まで昇圧して、反応器に送り込み、超臨
界水酸化分解反応を行なえばよい。As the supercritical hydroxylation decomposition means 3, a known means may be employed. Examples of the supercritical hydroxylation / decomposition means 3 include a supercritical hydroxylation / decomposition apparatus equipped with a reactor for oxidatively decomposing non-metallic members finely pulverized in the presence of supercritical water and an oxidizing agent. . The supercritical hydroxylation decomposition reaction performed in the reactor is not particularly limited as long as the temperature and pressure conditions bring water to a supercritical state. For example, the temperature is 374 ° C or higher, preferably 550 to 650 ° C,
And a pressure of 22 MPa or more, preferably 22 to 25 MPa
Condition. Examples of the oxidizing agent include air, pure oxygen, hydrogen peroxide, and liquid oxygen. These oxidizing agents may be used in a stoichiometrically required amount or more. The reactor for performing the supercritical hydroxylation decomposition may be any of a pipe (tubular) type and a vessel type. When supercritically hydrolyzing a non-metal member slurry containing PCB, an auxiliary fuel such as isopropyl alcohol may be used as necessary. The slurry liquid, and if necessary, water and an oxidizing agent may be pressurized to a predetermined pressure by a compressor or the like, sent to a reactor, and subjected to a supercritical hydroxylation decomposition reaction.
【0017】水は、超臨界状態では、良好な溶媒となる
ため、反応器内では超臨界水、被処理物および酸化剤は
均一相を形成し、超臨界水酸化反応が進行し、極めて短
時間のうちに非金属部材は、H2O、CO2まで酸化分
解される。超臨界水酸化分解処理後の処理流体は、冷却
し、大気圧に開放して、気液分離器により処理水と排ガ
スに分離すればよい。Since water becomes a good solvent in the supercritical state, the supercritical water, the object to be treated, and the oxidizing agent form a homogeneous phase in the reactor, and the supercritical hydroxylation reaction proceeds. In time, the non-metallic components are oxidatively decomposed to H2O and CO2. The processing fluid after the supercritical hydroxylation decomposition treatment may be cooled, released to atmospheric pressure, and separated into treated water and exhaust gas by a gas-liquid separator.
【0018】超臨界水酸化分解反応により、スラリー液
中に含まれるPCBは完全に分解され、水および二酸化
炭素と同時に塩素イオンが生成するため、あらかじめ水
酸化ナトリウム等のアルカリを添加して、処理流体中の
塩素イオンを塩化ナトリウム等の塩化物とすることが好
ましい。The PCB contained in the slurry liquid is completely decomposed by the supercritical hydroxylation decomposition reaction, and chlorine ions are generated at the same time as water and carbon dioxide. Preferably, the chloride ions in the fluid are chlorides such as sodium chloride.
【0019】超臨界水酸化分解後の処理流体は、冷却し
て大気圧に開放し、気液分離し、処理水として排水する
ことができる。The processing fluid after the supercritical hydroxylation decomposition can be cooled and released to atmospheric pressure, gas-liquid separated, and drained as processing water.
【0020】実施形態2 本発明の請求項2に記載された分解処理装置の一実施形
態を、図2を用いて説明する。図2中、4の細断化手段
とはPCBを含む感圧紙を数ミリ幅の短冊状や数ミリ角
の紙片に細断できるものであれば特に限定されないが、
シュレッダーやカッターミル等を挙げることができる。Embodiment 2 An embodiment of the decomposition processing apparatus according to claim 2 of the present invention will be described with reference to FIG. In FIG. 2, the shredding means 4 is not particularly limited as long as it can shred pressure-sensitive paper including PCB into a strip having a width of several millimeters or a piece of paper having a width of several millimeters.
Examples thereof include a shredder and a cutter mill.
【0021】図2中、2のスラリー化手段は、前記した
実施形態1のスラリー化手段と同様のものでよいが、感
圧紙のような繊維質の微粉砕には回転刃式ホモジナイザ
ーが好ましい。湿式の微粉砕装置を使用する場合は、細
断した感圧紙を水に加え攪拌し、水に分散させた後、湿
式の微粉砕装置を用いて、微細化しスラリー液を調製し
てもよい。なお、紙を溶解する薬剤等を添加して、攪拌
することにより紙をそのままスラリー化することもでき
るので、細断化手段4を省略することもできる。なお、
スラリー濃度に関しては、実施形態1と同様である。In FIG. 2, the slurrying means 2 may be the same as the slurrying means of the first embodiment, but a rotary blade homogenizer is preferred for finely pulverizing fibrous materials such as pressure-sensitive paper. When a wet-type pulverizer is used, the shredded pressure-sensitive paper may be added to water, stirred and dispersed in water, and then finely pulverized using a wet-type pulverizer to prepare a slurry liquid. In addition, since the paper can be slurried as it is by adding a chemical that dissolves the paper and stirring, the shredding unit 4 can be omitted. In addition,
The slurry concentration is the same as in the first embodiment.
【0022】図2中、3の超臨界水酸化分解手段は、実
施形態1に同じであるので、説明を省略する。In FIG. 2, the supercritical hydroxylation decomposition means 3 is the same as that of the first embodiment, and the description thereof will be omitted.
【0023】[0023]
【実施例1】実施例1 PCBが1.4重量%含まれている廃感圧紙を、シュレ
ッダー(明光商会(株)製、商品名「MSシュレッダー
231」)により約2mm幅の短冊状に細断した。次い
で、ミキサーを用いて純水中に分散させた後、分散液を
ホモジナイザー((株)マイクロテック・ニチオン製、
商品名「ヒスコトロンNS−50」)で微細均質化し、
スラリー濃度0.2重量%のスラリー液(スラリー粒径
1mm以下)を調製した。スラリー液中のPCB濃度
は、28mg/Lであった。Example 1 Example 1 A waste pressure-sensitive paper containing 1.4% by weight of PCB was narrowed into a strip having a width of about 2 mm by a shredder (trade name “MS Shredder 231” manufactured by Meiko Shokai Co., Ltd.). Refused. Next, after dispersing in pure water using a mixer, the dispersion was homogenized (manufactured by Microtech Nithion Co., Ltd.).
Fine homogenization with product name "Hiscotron NS-50")
A slurry liquid having a slurry concentration of 0.2% by weight (slurry particle diameter: 1 mm or less) was prepared. The PCB concentration in the slurry was 28 mg / L.
【0024】図3に示すような管状の反応器を使用し
て、以下のような手順にそって、スラリー液を超臨界水
酸化分解処理した。Using a tubular reactor as shown in FIG. 3, the slurry liquid was subjected to a supercritical hydroxylation decomposition treatment according to the following procedure.
【0025】管状の反応器33は予熱部、反応部および
冷却部の3つのゾーンに区分されている。まず、スラリ
ー液はダブルプランジャー式のポンプ31で所定圧まで
加圧されて反応器33へ送られる。また、過酸化水素は
ダブルシリンジ式のポンプ32により所定圧まで加圧さ
れ反応器33へ送られる。所定圧力まで加圧されたスラ
リー液と過酸化水素は加熱器34で所定温度まで加熱さ
れる。所定圧力、所定温度条件下で、スラリー液中の純
水は超臨界水となり、反応器33の反応部で超臨界水酸
化分解反応が進行する。超臨界水酸化分解反応後の処理
流体は、冷却器35により冷却される。冷却された処理
流体は、焼結金属フィルター36で固形物を除去した
後、保圧弁37で大気圧に開放され、気液分離器38に
より、処理水と排ガスに分離される。The tubular reactor 33 is divided into three zones: a preheating section, a reaction section and a cooling section. First, the slurry liquid is pressurized to a predetermined pressure by a double plunger pump 31 and sent to a reactor 33. The hydrogen peroxide is pressurized to a predetermined pressure by a double syringe pump 32 and sent to a reactor 33. The slurry liquid and the hydrogen peroxide pressurized to a predetermined pressure are heated to a predetermined temperature by a heater 34. Under a predetermined pressure and a predetermined temperature condition, the pure water in the slurry becomes supercritical water, and the supercritical hydroxylation decomposition reaction proceeds in the reaction section of the reactor 33. The processing fluid after the supercritical hydroxylation decomposition reaction is cooled by the cooler 35. After the solids are removed by the sintered metal filter 36, the cooled processing fluid is opened to the atmospheric pressure by the pressure holding valve 37, and is separated into the processing water and the exhaust gas by the gas-liquid separator 38.
【0026】超臨界水酸化分解を行なった反応器の概要
および反応条件は、以下のとおりである。The outline of the reactor in which the supercritical hydroxylation decomposition was performed and the reaction conditions are as follows.
【0027】(反応器) 形式:環状反応器 材質:Ni合金 内容積:0.54L(内径6.8mm、長さ15m) (ポンプ) 過酸化水素用:ダブルプランジャー式 スラリー液用:ダブルシリンジ式 (反応条件) 酸化剤:過酸化水素 反応温度:650℃ 反応圧力:25MPa 反応時間:1分(Reactor) Model: Ring reactor Material: Ni alloy Inner volume: 0.54 L (inner diameter 6.8 mm, length 15 m) (pump) For hydrogen peroxide: double plunger type For slurry liquid: double syringe Formula (reaction conditions) Oxidizing agent: hydrogen peroxide Reaction temperature: 650 ° C. Reaction pressure: 25 MPa Reaction time: 1 minute
【0028】上記の条件で超臨界水酸化分解処理を行な
ったところ、処理水中のPCB濃度は、0.5ppb以
下(分析下限値以下)であった。When the supercritical hydroxylation decomposition treatment was performed under the above conditions, the PCB concentration in the treated water was 0.5 ppb or less (lower limit of analysis).
【0029】なお、実施例1に準じて、PCBで汚染さ
れたトランス、コンデンサ等を構成する紙、木材、プラ
スチックからなる非金属部材をスラリー化し、このスラ
リーについても超臨界水酸化分解処理を行なったが、同
様に処理水中のPCB濃度は0.5ppb以下(分析下
限値以下)であった。According to the first embodiment, non-metal members made of paper, wood, and plastic, which constitute a transformer, a capacitor, and the like, which are contaminated with PCB, are slurried, and this slurry is also subjected to a supercritical hydroxylation decomposition treatment. However, similarly, the PCB concentration in the treated water was 0.5 ppb or less (the analysis lower limit value or less).
【0030】[0030]
【発明の効果】本発明により、PCBで汚染されたトラ
ンス、コンデンサ等の非金属構成部材やPCBを含む感
圧紙、効率的かつ有害な副生物を発生させることなく、
分解処理することができるので、環境を汚染する心配が
ない。According to the present invention, non-metal components such as transformers and capacitors contaminated with PCB, pressure-sensitive paper containing PCB, and efficient and harmful by-products are not generated.
Since it can be decomposed, there is no concern about polluting the environment.
【図1】本発明の、一実施形態を示すフロー図。FIG. 1 is a flowchart showing one embodiment of the present invention.
【図2】本発明の、一実施形態を示すフロー図。FIG. 2 is a flowchart showing one embodiment of the present invention.
【図3】実施例1で使用した超臨界水酸化分解処理装置
のフロー図。FIG. 3 is a flowchart of a supercritical hydroxylation decomposition treatment apparatus used in Example 1.
1 粗粉砕手段 2 スラリー化手段 3 超臨界水酸化分解手段 4 細断化手段 31 ポンプ 32 ポンプ 33 管状反応器 34 加熱器 35 加熱器 36 焼結金属フィルター 37 保圧弁 38 気液分離器 DESCRIPTION OF SYMBOLS 1 Coarse crushing means 2 Slurry means 3 Supercritical hydroxylation decomposition means 4 Shredding means 31 Pump 32 Pump 33 Tubular reactor 34 Heater 35 Heater 36 Sintered metal filter 37 Holding pressure valve 38 Gas-liquid separator
───────────────────────────────────────────────────── フロントページの続き (72)発明者 鈴木 明 東京都江東区新砂1丁目2番8号 オルガ ノ株式会社内 (72)発明者 安生 徳幸 東京都江東区新砂1丁目2番8号 オルガ ノ株式会社内 (72)発明者 伊藤 新治 東京都江東区新砂1丁目2番8号 オルガ ノ株式会社内 Fターム(参考) 2E191 BA13 BB00 BD11 4D004 AA07 AA12 AA22 AB06 AC05 CA04 CA12 CA13 CA15 CA22 CA32 CA34 CA39 CB01 CB05 CB12 CB13 CC01 CC02 CC03 CC11 CC12 DA03 DA06 DA07 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Akira Suzuki 1-2-8 Shinsuna, Koto-ku, Tokyo Organo Co., Ltd. (72) Inventor Tokuyuki Ansei 1-2-8 Shinsuna, Koto-ku, Tokyo Organo (72) Inventor Shinji Ito 1-2-8 Shinsuna, Koto-ku, Tokyo Organo Corporation F-term (reference) 2E191 BA13 BB00 BD11 4D004 AA07 AA12 AA22 AB06 AC05 CA04 CA12 CA13 CA15 CA22 CA32 CA34 CA39 CB01 CB05 CB12 CB13 CC01 CC02 CC03 CC11 CC12 DA03 DA06 DA07
Claims (4)
サ等を構成する紙、木材、プラスチックからなる非金属
部材を粗粉砕する粗粉砕手段と、前記粗粉砕手段により
粗粉砕された非金属部材をスラリー化する粉砕スラリー
手段と、前記粉砕スラリー手段により得られるスラリー
液を超臨界水酸化分解処理する超臨界水酸化分解手段を
有することを特徴とするPCBで汚染されたトランス、
コンデンサ等を構成する非金属部材の分解処理装置。1. A coarse crushing means for coarsely crushing non-metallic members made of paper, wood, and plastic constituting a transformer, a condenser, etc. contaminated with PCB, and a slurry for non-metallic members coarsely crushed by said coarse crushing means. A transformer contaminated with PCB, comprising: a pulverized slurry means for converting a slurry liquid obtained by the pulverized slurry means and a supercritical hydroxylation decomposition means for performing supercritical hydroxylation decomposition treatment;
Disassembly equipment for non-metallic members that constitute capacitors and the like.
ラリー手段と、前記スラリー手段により得られるスラリ
ー液を超臨界水酸化分解処理する超臨界水酸化分解手段
を有することを特徴とするPCBを含む感圧紙の分解処
理装置。2. A PCB comprising: a slurry means for slurrying pressure-sensitive paper containing PCB; and a supercritical oxidative decomposition means for supercritical oxidative decomposition of a slurry obtained by the slurry means. Pressure-sensitive paper disassembly unit.
サ等を構成する紙、木材、プラスチックからなる非金属
部材を粗粉砕し、微細化処理してスラリー化した後、ス
ラリー液を超臨界水酸化分解処理することを特徴とする
PCBで汚染されたトランス、コンデンサ等を構成する
非金属部材の分解処理方法。3. Non-metallic members made of paper, wood, plastic, etc., constituting transformers, capacitors, etc., which are contaminated with PCB, are roughly pulverized, refined and slurried, and then the slurry liquid is subjected to supercritical hydroxylation decomposition. A method of disassembling a non-metal member constituting a transformer, a capacitor, or the like, which is contaminated with PCB, wherein the method is performed.
ラリー液を超臨界水酸化分解処理することを特徴とする
PCBを含む感圧紙の分解処理方法。4. A method for decomposing pressure-sensitive paper containing PCB, wherein the pressure-sensitive paper containing PCB is slurried, and the slurry liquid is subjected to a supercritical hydroxylation decomposition treatment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000151090A JP2001327943A (en) | 2000-05-23 | 2000-05-23 | Treatment device for decomposing nonmetal member constituting transformer, capacitor or the like contaminated by pcb or pressure-sensitive paper containing pcb and method using this device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000151090A JP2001327943A (en) | 2000-05-23 | 2000-05-23 | Treatment device for decomposing nonmetal member constituting transformer, capacitor or the like contaminated by pcb or pressure-sensitive paper containing pcb and method using this device |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2001327943A true JP2001327943A (en) | 2001-11-27 |
JP2001327943A5 JP2001327943A5 (en) | 2007-04-19 |
Family
ID=18656704
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2000151090A Pending JP2001327943A (en) | 2000-05-23 | 2000-05-23 | Treatment device for decomposing nonmetal member constituting transformer, capacitor or the like contaminated by pcb or pressure-sensitive paper containing pcb and method using this device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2001327943A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008120662A1 (en) * | 2007-03-30 | 2008-10-09 | B Food Science Co., Ltd. | Continuous high-pressure hydrothermal reaction apparatus for biomass treatment |
US8096064B2 (en) * | 2007-01-26 | 2012-01-17 | Forestry And Forest Products Research Institute | Method for drying lumber, method of impregnating lumber with chemicals, and drying apparatus |
JP2014050825A (en) * | 2012-09-10 | 2014-03-20 | Mitsubishi Heavy Ind Ltd | Processing unit of pcb pollutant except for nonferrous metal |
JP5925945B1 (en) * | 2015-08-24 | 2016-05-25 | 株式会社ケンテック研究所 | Waste treatment apparatus and waste treatment method |
-
2000
- 2000-05-23 JP JP2000151090A patent/JP2001327943A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8096064B2 (en) * | 2007-01-26 | 2012-01-17 | Forestry And Forest Products Research Institute | Method for drying lumber, method of impregnating lumber with chemicals, and drying apparatus |
WO2008120662A1 (en) * | 2007-03-30 | 2008-10-09 | B Food Science Co., Ltd. | Continuous high-pressure hydrothermal reaction apparatus for biomass treatment |
JP2014050825A (en) * | 2012-09-10 | 2014-03-20 | Mitsubishi Heavy Ind Ltd | Processing unit of pcb pollutant except for nonferrous metal |
JP5925945B1 (en) * | 2015-08-24 | 2016-05-25 | 株式会社ケンテック研究所 | Waste treatment apparatus and waste treatment method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5075017A (en) | Method for removing polychlorinated dibenzodioxins and polychlorinated dibenzofurans from paper mill sludge | |
US8652404B2 (en) | System and method for processing waste material | |
Hao et al. | Sonochemistry of degrading p-chlorophenol in water by high frequency ultrasound | |
Calgaro et al. | Supercritical extraction of polymers from printed circuit boards using CO2 and ethanol | |
CN104150733A (en) | Method for removing organic pollutants and stabilizing heavy metals based on sludge hydro-thermal treatment | |
JP2001327943A (en) | Treatment device for decomposing nonmetal member constituting transformer, capacitor or the like contaminated by pcb or pressure-sensitive paper containing pcb and method using this device | |
JP3671023B2 (en) | Method and system for treating solid organic matter containing persistent decomposable harmful substances | |
JP6323951B2 (en) | Method for detoxifying solid containing organic halogen compound and organic halogen compound detoxifying agent | |
CN107352762A (en) | A kind of medicament of Treating Municipal Sewage factory sludge and preparation method thereof | |
JP2001129572A (en) | Method for treating hazardous substance and its apparatus | |
JP2001269654A (en) | Treating method of material to which pcb adheres | |
Xin et al. | Hydrothermal deconstruction of single-use personal protective equipment: process design and economic performance | |
JP2003312843A (en) | Slurry supplying system | |
JP2002219376A (en) | Method for crushing sludge | |
JP2001334251A (en) | Method for cleaning polluted soil | |
JP2002045825A (en) | Device for decontaminating/decomposing pcb in electric equipment of vessel filled with pcb | |
JP2003318050A (en) | Method of treating large-sized transformer | |
JP5769610B2 (en) | Activated carbon slurrying apparatus and method | |
JP2003094033A (en) | Treatment system for hazardous substance-containing soil | |
JP2002143825A (en) | Method for treating pcb | |
JP2001047026A (en) | Method for detoxifying substance contaminated with harmful substance | |
JP2003311236A (en) | Organic halide decomposition treatment system | |
JP3913096B2 (en) | Hazardous substance treatment system | |
JP2003311124A (en) | Exhaust gas treatment method and apparatus | |
JP2003326520A (en) | Method and apparatus for grinding waste plastic, method and apparatus for treating waste plastic |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20070305 |
|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20070305 |
|
RD02 | Notification of acceptance of power of attorney |
Free format text: JAPANESE INTERMEDIATE CODE: A7422 Effective date: 20070305 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20090513 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20090526 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20091006 |