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JPH10156138A - Device for decomposing organic halogen compound - Google Patents

Device for decomposing organic halogen compound

Info

Publication number
JPH10156138A
JPH10156138A JP8322406A JP32240696A JPH10156138A JP H10156138 A JPH10156138 A JP H10156138A JP 8322406 A JP8322406 A JP 8322406A JP 32240696 A JP32240696 A JP 32240696A JP H10156138 A JPH10156138 A JP H10156138A
Authority
JP
Japan
Prior art keywords
dielectric
organic halogen
halogen compound
discharge electrodes
pellet
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.)
Withdrawn
Application number
JP8322406A
Other languages
Japanese (ja)
Inventor
Jiyunnosuke Nakaya
潤之助 仲谷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP8322406A priority Critical patent/JPH10156138A/en
Publication of JPH10156138A publication Critical patent/JPH10156138A/en
Withdrawn legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PROBLEM TO BE SOLVED: To efficiently decompose an org. halogen compd. at ordinary temps. by providing a discharge electrode, a dielectric packed between the discharge electrodes, forming the dielectric with a granular pellet and applying an AC voltage between the discharge electrodes to produce plasma in the void between the dielectric. SOLUTION: A reaction vessel 2 is provided with discharge electrodes 4 and 7 and a bed 5 packed with a pelletized dielectric 6. The discharge electrodes 4 and 7 are formed with a corrosion-resistant material such as platinum, and the dielectric 6 is formed by a granular pellet. The pellet is appropriately made of a material high in dielectric constant. An AC voltage is applied on the packed bed 5 from a high AC voltage generator 3, and then, an org. halogen compd. is introduced into the reaction vessel 2 from a gas inlet 1, passed between the discharge electrodes 4 and 7, treated and discharged from a gas outlet 8. At this time, a very strong electric field strength is obtained closed to the pellet, plasma is produced in the void between the adjacent pellets, and the org. halogen compd. is decomposed.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、有機ハロゲン化合
物分解処理装置に関し、特に、有機溶剤として有機ハロ
ゲン化合物を使用する事業所において排出される排ガス
を分解処理する有機ハロゲン分解処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an organic halogen compound decomposing apparatus, and more particularly to an organic halogen decomposing apparatus for decomposing exhaust gas discharged from an office using an organic halogen compound as an organic solvent.

【0002】[0002]

【従来の技術】従来、有機ハロゲン化合物分解処理装置
については、幾つかのものが知られている。図3にその
一例を示す。この溶剤回収装置では、活性炭層101内
に活性炭102を充填し、活性炭層101に有機ハロゲ
ン化合物を含む排ガスを通気させている。これによっ
て、有機ハロゲン化合物を活性炭102に吸着させてい
た。しかし、この溶剤回収装置では、その回収量は、活
性炭と有機ハロゲン化合物との平衡吸着量によって決定
されるため、回収量に限界があった。また、操作温度
を、通常、低温とするために、エネルギー効率が悪かっ
た。さらに、回収された有機ハロゲン化合物を含む活性
炭を無害化する設備が別途必要であった。
2. Description of the Related Art Heretofore, several organic halogen compound decomposition treatment apparatuses are known. FIG. 3 shows an example. In this solvent recovery apparatus, the activated carbon layer 101 is filled with activated carbon 102, and exhaust gas containing an organic halogen compound is passed through the activated carbon layer 101. Thus, the organic halogen compound was adsorbed on the activated carbon 102. However, in this solvent recovery apparatus, the recovery amount is determined by the equilibrium adsorption amount between the activated carbon and the organic halogen compound, and thus the recovery amount is limited. In addition, since the operating temperature is usually set to a low temperature, energy efficiency is low. Further, equipment for detoxifying the activated carbon containing the collected organic halogen compound was separately required.

【0003】図4に別の例を示す。これは、燃焼炉を用
いたものである。すなわち、燃焼炉201に有機ハロゲ
ン化合物を含む排ガスを通気させることにより、有機ハ
ロゲン化合物を処理していた。しかし、ハロゲンが分子
中に存在すると、燃焼しにくくなるため、処理のため非
常に高温を必要とし、また必要に応じてメタン等の助燃
材を必要とすることとなり、エネルギー効率が悪くなり
がちであった。
FIG. 4 shows another example. This uses a combustion furnace. That is, the organic halogen compound is treated by passing exhaust gas containing the organic halogen compound through the combustion furnace 201. However, if halogens are present in the molecule, it becomes difficult to burn, so a very high temperature is required for processing, and if necessary, an auxiliary material such as methane is required, which tends to deteriorate energy efficiency. there were.

【0004】[0004]

【発明が解決しようとする課題】したがって、本発明の
目的は、常温で有機ハロゲン化合物を処理することを可
能とし、かつ高いエネルギー効率を持つ有機ハロゲン化
合物分解処理装置を提供することにある。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide an organic halogen compound decomposition treatment apparatus which can treat an organic halogen compound at room temperature and has high energy efficiency.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するた
め、請求項1に記載された発明は、有機ハロゲン化合物
分解処理装置であって、放電電極と、その放電電極間に
充填した誘電体とを含み、該誘電体を粒状のペレットで
構成し、上記放電電極間に交流電圧を印加することによ
り上記誘電体の空隙にプラズマを生成させ、該空隙を通
過する有機ハロゲン化合物を分解するようにしたことを
特徴とする。
Means for Solving the Problems To achieve the above object, an invention according to claim 1 is an apparatus for decomposing an organic halogen compound, comprising a discharge electrode and a dielectric filled between the discharge electrodes. Comprising, the dielectric is composed of granular pellets, by applying an AC voltage between the discharge electrodes to generate plasma in the gap of the dielectric, so as to decompose the organic halogen compound passing through the gap It is characterized by having done.

【0006】[0006]

【発明の実施の形態】図1に本発明にかかる有機ハロゲ
ン化合物分解処理装置の一実施の形態を示す。この実施
の形態では、反応容器2に設けた第1の放電電極4,第
2の電極7と、それらの放電電極4,7間に誘電体6を
充填したペレット充填層5とを備えている。放電電極
4,7は、通常白金等の耐腐食性素材で構成する。誘電
体6は粒状のペレットで構成する。ペレットの素材は、
比誘電率の高い材質が好適であり、特にチタン酸バリウ
ムが好適である。そして、ペレット間の空隙率は、0.
4程度が好ましい。また、粒径は、2〜5mmの範囲が
好ましい。
FIG. 1 shows an embodiment of an apparatus for decomposing an organic halogen compound according to the present invention. In this embodiment, a first discharge electrode 4 and a second electrode 7 provided in a reaction vessel 2 and a pellet filling layer 5 filled with a dielectric 6 between the discharge electrodes 4 and 7 are provided. . The discharge electrodes 4 and 7 are usually made of a corrosion-resistant material such as platinum. The dielectric 6 is composed of granular pellets. The material of the pellet is
A material having a high relative permittivity is preferable, and barium titanate is particularly preferable. And the porosity between the pellets is 0.1.
About 4 is preferable. Further, the particle size is preferably in the range of 2 to 5 mm.

【0007】図示のように離間して配置した放電電極
4,7間のペレット充填層5には、交流高電圧発生装置
3によって交流電圧(20kV以下が好ましい)を印加
することができるように構成している。処理されるべき
有機ハロゲン化合物はガス入口1より反応容器2に導入
され、電極4,7間に通気され、処理後にガス出口8よ
り排出される。
As shown, an AC high voltage generator 3 is used to apply an AC voltage (preferably 20 kV or less) to the pellet filling layer 5 between the discharge electrodes 4 and 7 that are spaced apart from each other. doing. The organic halogen compound to be treated is introduced into the reaction vessel 2 from the gas inlet 1, is ventilated between the electrodes 4 and 7, and is discharged from the gas outlet 8 after the treatment.

【0008】このように通気している間、放電電極4,
7間のペレット充填層5に印加された交流電圧によっ
て、誘電体6を構成するペレット同士の間で分極が生じ
る。その結果、ペレットの近傍で非常に高い電界強度が
得られ、ペレット間同士の空隙にプラズマが発生する。
このプラズマは、非平衡プラズマであり、質量の大きい
イオンは電界によって加速されず、質量の軽い電子のみ
が電界によって加速され、高いエネルギーを得る。この
プラズマの作用によって空気中の酸素等からラジカルが
発生し、そのような分子種によって通気された有機ハロ
ゲン化合物が分解される。このように、投入されるエネ
ルギーの大部分が、有機ハロゲン化合物の分解に寄与す
る電子の加速にのみ使用されるため、エネルギー効率が
良い。かつ、これらの作用は大気圧下に常温で生じる。
すなわち、本発明にかかる有機ハロゲン化合物分解処理
装置は、常温で有機ハロゲン化合物を処理することを可
能とし、かつ高いエネルギー効率を持つこととなる。
During the ventilation, the discharge electrodes 4,
The alternating voltage applied to the pellet filling layer 5 between 7 causes polarization between the pellets constituting the dielectric 6. As a result, a very high electric field strength is obtained in the vicinity of the pellet, and plasma is generated in a gap between the pellets.
This plasma is a non-equilibrium plasma, and ions having a large mass are not accelerated by an electric field, and only electrons having a small mass are accelerated by an electric field to obtain high energy. Radicals are generated from oxygen and the like in the air by the action of this plasma, and the aerated organic halogen compounds are decomposed by such molecular species. As described above, most of the input energy is used only for accelerating the electrons that contribute to the decomposition of the organic halogen compound, so that the energy efficiency is high. And these actions occur at normal temperature under atmospheric pressure.
That is, the organic halogen compound decomposition treatment apparatus according to the present invention can process an organic halogen compound at room temperature and has high energy efficiency.

【0009】[0009]

【実施例】実施例1 図1に示した装置を用いて、クロロベンゼンの分解試験
を行った。結果を図2に示す。クロロベンゼンの濃度が
50ppmの空気を、15リットル/hの流速で供給し
た。電極間には、0〜20kVの電圧を印加し、充填層
5には空隙率約0.4、粒径2〜5mmでチタン酸バリ
ウムのペレット((株)高純度化学研究所製)を充填し
た。ペレット充填層5は、直径36mmで長さは、1.
5cmとした。図2から了解されるように、本発明にか
かる有機ハロゲン化合物分解処理装置を使用することに
より、消費電力その他の条件を適宜設定して、90%以
上の分解率を達成することができた。すなわち、常温で
有機ハロゲン化合物を処理することを可能とし、かつ高
いエネルギー効率であることが確認された。
EXAMPLE 1 Using the apparatus shown in FIG. 1, a decomposition test of chlorobenzene was carried out. The results are shown in FIG. Air having a chlorobenzene concentration of 50 ppm was supplied at a flow rate of 15 l / h. A voltage of 0 to 20 kV is applied between the electrodes, and the filling layer 5 is filled with barium titanate pellets (manufactured by Kojundo Chemical Laboratory Co., Ltd.) having a porosity of about 0.4 and a particle size of 2 to 5 mm. did. The pellet filling layer 5 has a diameter of 36 mm and a length of 1.
It was 5 cm. As understood from FIG. 2, by using the organic halogen compound decomposition treatment apparatus according to the present invention, it was possible to achieve a decomposition rate of 90% or more by appropriately setting power consumption and other conditions. That is, it was confirmed that it was possible to treat the organic halogen compound at room temperature and that the energy efficiency was high.

【0010】[0010]

【発明の効果】上記したところから明かなように、本発
明によれば、常温で有機ハロゲン化合物を処理すること
を可能とし、かつ高いエネルギー効率を持つ有機ハロゲ
ン化合物分解処理装置が提供される。
As is apparent from the above description, according to the present invention, there is provided an organic halogen compound decomposition treatment apparatus which can treat an organic halogen compound at normal temperature and has high energy efficiency.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明にかかる有機ハロゲン化合物分解処理装
置の一実施の形態を示す概念的断面図である。
FIG. 1 is a conceptual sectional view showing an embodiment of an organic halogen compound decomposition treatment apparatus according to the present invention.

【図2】本発明にかかる有機ハロゲン化合物分解処理装
置を用いて行ったクロロベンゼンの分解試験の結果を示
すグラフである。
FIG. 2 is a graph showing the results of a chlorobenzene decomposition test performed using the organic halogen compound decomposition treatment apparatus according to the present invention.

【図3】従来の有機ハロゲン化合物分解処理装置の一例
を示す断面図である。
FIG. 3 is a sectional view showing an example of a conventional organic halogen compound decomposition treatment apparatus.

【図4】従来の有機ハロゲン化合物分解処理装置の他の
一例を示す模式図である。
FIG. 4 is a schematic view showing another example of a conventional organic halogen compound decomposition treatment apparatus.

【符号の説明】[Explanation of symbols]

1 ガス入口 2 反応容器 3 交流高電圧発生装置 4 第1の放電電極 5 ペレット充填層 6 誘電体 7 第2の放電電極 8 ガス出口 DESCRIPTION OF SYMBOLS 1 Gas inlet 2 Reaction vessel 3 AC high voltage generator 4 First discharge electrode 5 Pellet packed layer 6 Dielectric 7 Second discharge electrode 8 Gas outlet

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 放電電極と、その放電電極間に充填した
誘電体とを含み、該誘電体を粒状のペレットで構成し、
上記放電電極間に交流電圧を印加することにより上記誘
電体の空隙にプラズマを生成させ、該空隙を通過する有
機ハロゲン化合物を分解するようにしたことを特徴とす
る有機ハロゲン化合物分解処理装置。
1. A discharge electrode comprising: a discharge electrode; and a dielectric filled between the discharge electrodes, wherein the dielectric is formed of granular pellets,
An apparatus for decomposing an organic halogen compound, wherein an AC voltage is applied between the discharge electrodes to generate plasma in a gap of the dielectric, and an organic halide compound passing through the gap is decomposed.
JP8322406A 1996-12-03 1996-12-03 Device for decomposing organic halogen compound Withdrawn JPH10156138A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8322406A JPH10156138A (en) 1996-12-03 1996-12-03 Device for decomposing organic halogen compound

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8322406A JPH10156138A (en) 1996-12-03 1996-12-03 Device for decomposing organic halogen compound

Publications (1)

Publication Number Publication Date
JPH10156138A true JPH10156138A (en) 1998-06-16

Family

ID=18143317

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8322406A Withdrawn JPH10156138A (en) 1996-12-03 1996-12-03 Device for decomposing organic halogen compound

Country Status (1)

Country Link
JP (1) JPH10156138A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101297604B1 (en) * 2011-05-03 2013-08-19 제주대학교 산학협력단 Apparatus and methods for destroying sulfur hexafluoride by using dielectric barrier discharge activated alumina

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101297604B1 (en) * 2011-05-03 2013-08-19 제주대학교 산학협력단 Apparatus and methods for destroying sulfur hexafluoride by using dielectric barrier discharge activated alumina

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Effective date: 20040203