JPH0260668A - Method for decomposing halogenated acyclic hydrocarbon compounds - Google Patents
Method for decomposing halogenated acyclic hydrocarbon compoundsInfo
- Publication number
- JPH0260668A JPH0260668A JP63213085A JP21308588A JPH0260668A JP H0260668 A JPH0260668 A JP H0260668A JP 63213085 A JP63213085 A JP 63213085A JP 21308588 A JP21308588 A JP 21308588A JP H0260668 A JPH0260668 A JP H0260668A
- Authority
- JP
- Japan
- Prior art keywords
- acyclic hydrocarbon
- gas
- decomposition
- dichlorodifluoromethane
- reaction vessel
- 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
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- Fire-Extinguishing Compositions (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明はハロゲン化非環式炭化水素化合物、特にフッ素
化炭化水素、塩素化炭化水素あるいはフッ素化、塩素化
混合の非環式炭化水素化合物の分解方法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is directed to the decomposition of halogenated acyclic hydrocarbon compounds, particularly fluorinated hydrocarbons, chlorinated hydrocarbons, or mixed fluorinated and chlorinated acyclic hydrocarbon compounds. Regarding the method.
従来の技術
ハロゲン化非環式炭化水素化合物は一般に非常に安定な
物質であるため、特別の処理を施さない限り自然に分解
することはない。この種の物質は大気中に放出されると
成層圏にまで拡散し、成層圏中にあるオゾン層において
、初めて分解される。BACKGROUND OF THE INVENTION Halogenated acyclic hydrocarbon compounds are generally very stable substances and will not spontaneously decompose unless they are specially treated. When these substances are released into the atmosphere, they diffuse into the stratosphere and are first broken down in the ozone layer within the stratosphere.
この分解において、成層圏中のオゾンが消費され、オゾ
ンに吸収されている太陽光中に含まれる短波長の紫外線
が、直接地表に降り注ぐことになる。その結果、生物に
を害な短波長の紫外線により細胞や遺伝子が傷つけられ
生体系に大きな影響を与えることが憂慮されている。During this decomposition, ozone in the stratosphere is consumed, and short-wavelength ultraviolet rays contained in sunlight that are absorbed by ozone fall directly onto the earth's surface. As a result, there are concerns that short-wavelength ultraviolet rays, which are harmful to living things, may damage cells and genes and have a major impact on biological systems.
これらハロゲン化炭化水素化合物を容易に分解する方法
が強く望まれ、大気中に排出する量を大幅に減少する方
策がとられようとしている。A method for easily decomposing these halogenated hydrocarbon compounds is strongly desired, and measures are being taken to significantly reduce the amount emitted into the atmosphere.
従来、この種の安定なハロゲン化非環式炭化水素化合物
を分解する方法として、1200度以上の高温で燃焼す
る方法がある。この方法では高温に耐え、しかも、燃焼
により発生するハロゲン化水素例えば塩化水素、フッ化
水素に耐える炉が必要であることなどから、大がかりな
設備を要し高価になる欠点がある。この様な欠点を解決
する方法として、ハロゲン化芳香族化合物を水酸化力リ
ュウムの共存下で加熱する方法が提案されている(例え
ば、特公昭51−37831号公報)。Conventionally, as a method of decomposing this kind of stable halogenated acyclic hydrocarbon compound, there is a method of burning it at a high temperature of 1200 degrees or more. This method requires a furnace that can withstand high temperatures and hydrogen halides, such as hydrogen chloride and hydrogen fluoride, generated by combustion, so it requires large-scale equipment and is expensive. As a method for solving these drawbacks, a method has been proposed in which a halogenated aromatic compound is heated in the coexistence of hydroxide (for example, Japanese Patent Publication No. 37831/1983).
発明が解決しようとする課題
この様な従来の方法では、比較的低沸点であるハロゲン
化非環式炭化水素化合物に適用した場合分解率が低く、
さらにバッチ処理が必要であるという欠点を有している
。さらに、低温で回収する方法において、回収装置から
回収漏れの微量のハロゲン化非環式炭化水素を安価に簡
便に無害に分解する方法が望まれている。Problems to be Solved by the Invention In such conventional methods, when applied to halogenated acyclic hydrocarbon compounds having a relatively low boiling point, the decomposition rate is low;
Furthermore, it has the disadvantage of requiring batch processing. Furthermore, in a low-temperature recovery method, there is a need for a method for inexpensively, easily, and harmlessly decomposing trace amounts of halogenated acyclic hydrocarbons that are leaked from recovery equipment.
本発明はこの様な点を改良するためになされたもので、
ハロゲン化非環式炭化水素化合物を高い分解率で連続的
に分解する方法を提供するものである。The present invention was made to improve these points.
The present invention provides a method for continuously decomposing halogenated acyclic hydrocarbon compounds at a high decomposition rate.
課題を解決するための手段
上記課題を解決するためハロゲン化非環式炭化水素化合
物の気体と少なくとも酸素を含む気体との混合気体中で
無声放電させ、ハロゲン化非環式炭化水素化合物を分解
するものである。Means for Solving the Problems In order to solve the above problems, the halogenated acyclic hydrocarbon compound is decomposed by silently discharging it in a mixed gas of the halogenated acyclic hydrocarbon compound gas and a gas containing at least oxygen. It is something.
作用
本発明によれば、ハロゲン化非環式炭化水素化合物の気
体と少なくとも酸素を含む気体の混合気体中で無声放電
させることにより、ハロゲン化非環式炭化水素化合物を
酸化分解する。このため、高い分解率で、害の少ない°
化合物、あるいは回収の容易な化合物に分解することが
可能となる。According to the present invention, a halogenated acyclic hydrocarbon compound is oxidatively decomposed by silently discharging it in a mixed gas of a gas of the halogenated acyclic hydrocarbon compound and a gas containing at least oxygen. Therefore, it has a high decomposition rate and is less harmful.
It becomes possible to decompose it into compounds or compounds that can be easily recovered.
実施例 以下本発明の実施例を図面とともに説明する。Example Embodiments of the present invention will be described below with reference to the drawings.
図面は本発明の方法を実証するために使用した装置の模
式図である。図中1はガラス製反応容器、2はガラス製
反応容器の外周に銅線を巻いた銅線製コイル電極、3は
ガラス製反応容器の中空部に1したステンレス製電極、
4はハロゲン化非環式炭化水素化合物の気体と少なくと
も酸素を含む気体の混合物を導入する導入口、5は分解
ガスの排出口を示す。分解時には、3.2間に15kV
の電圧を印加する。The drawing is a schematic representation of the apparatus used to demonstrate the method of the invention. In the figure, 1 is a glass reaction vessel, 2 is a copper wire coil electrode wrapped around the outer periphery of the glass reaction vessel, 3 is a stainless steel electrode placed in the hollow part of the glass reaction vessel,
Reference numeral 4 indicates an inlet for introducing a mixture of a gas of a halogenated acyclic hydrocarbon compound and a gas containing at least oxygen, and 5 indicates an outlet for cracked gas. During disassembly, 15kV between 3.2
Apply a voltage of
(実施例1)
前記の装置を用いて、1100PPのジクロロジフロロ
メタンを含む空気(100R/hrs)を導入口4から
ガラス製反応容器1に導入し、無声放電による分解を行
なった。排出口5から排出されるガス成分をガスクロマ
トグラムにより分析した結果、IPPMのジクロロジフ
ロロメタン、−酸化炭素、二酸化炭素、塩酸、フッ酸な
どが検出された。この様な反応装置を多段に設置するか
、反応装置内での気体の滞留時間を制御すれば効率よく
分解することが可能である。(Example 1) Using the above-mentioned apparatus, air containing 1100 PP dichlorodifluoromethane (100 R/hrs) was introduced into the glass reaction vessel 1 from the inlet 4, and decomposition was performed by silent discharge. As a result of gas chromatogram analysis of the gas components discharged from the outlet 5, IPPM dichlorodifluoromethane, carbon oxide, carbon dioxide, hydrochloric acid, hydrofluoric acid, and the like were detected. Efficient decomposition can be achieved by installing such reactors in multiple stages or by controlling the residence time of the gas within the reactor.
(実施例2)
実施例1の条件と同様に、ジクロロジフロロメタンを供
給し、排出口から排出される気体を水を充填したガス吸
収瓶に導入し、塩化水素とフッ化水素を回収した。ガス
吸収瓶をへた気体を分析するとジクロロジフロロメタン
の濃度は0.9PPMであった。(Example 2) Dichlorodifluoromethane was supplied under the same conditions as in Example 1, and the gas discharged from the outlet was introduced into a gas absorption bottle filled with water to recover hydrogen chloride and hydrogen fluoride. . Analysis of the gas discharged from the gas absorption bottle revealed that the concentration of dichlorodifluoromethane was 0.9 PPM.
(実施例3)
500PPMのフロン113を含む空気(100R/h
rs)をガス導入口4からガラス製反応容器1に導入し
、無声放電による分解を行なった。(Example 3) Air containing 500 PPM of Freon 113 (100 R/h
rs) was introduced into the glass reaction vessel 1 through the gas inlet 4 and decomposed by silent discharge.
排出口5から排出されるフロン113は5PPMであっ
た。The Freon 113 discharged from the discharge port 5 was 5 PPM.
この様に安定なハロゲン化非環式炭化水素化合物が分解
されるのは、無声放電により脱ハロゲン反応と炭素−炭
素結合の切断反応が起こるためと推定される。The reason why the stable halogenated acyclic hydrocarbon compound is decomposed in this way is presumed to be that the silent discharge causes a dehalogenation reaction and a carbon-carbon bond cleavage reaction.
実施例において、ジクロロジフロロメタンとフロン11
3について説明したが、他のハロゲン化非環式炭化水素
化合物においても、有効であることは自明である。また
、反応容器を多段にし分解率を向上することも可能であ
る。さらに、実施例の説明では、反応・容器としてガラ
ス製を用いたが、分解酸生物であるフッ化水素に対して
耐食性をもつ材料を用いるか、そのような材料で容器内
をコーティングすればよい。なお、回収装置は湿式法を
説明したが、乾式法においても同様の効果があることは
自明である。In the examples, dichlorodifluoromethane and Freon 11
Although 3 was explained, it is obvious that other halogenated acyclic hydrocarbon compounds are also effective. It is also possible to increase the decomposition rate by using multiple reaction vessels. Furthermore, in the explanation of the examples, glass was used as the reaction/container, but a material that is corrosion resistant to hydrogen fluoride, which is a decomposing acid organism, may be used, or the inside of the container may be coated with such a material. . In addition, although the wet method was explained as the recovery device, it is obvious that the same effect can be obtained in the dry method.
発明の効果
以上のように本発明によれば、ハロゲン化非環式炭化水
素化合物を高い効率で分解する事が可能である。したが
って、ハロゲン化非環式炭化水素化合物を洗浄工程に使
用している電子工業の工場などにおいて、排ガス中に含
まれる前述の化合物を処理することが可能となり、成層
圏におけるオシン層破壊に歯止めをかけることが可能と
なるなど産業上きわめて有益である。Effects of the Invention As described above, according to the present invention, it is possible to decompose halogenated acyclic hydrocarbon compounds with high efficiency. Therefore, it will be possible to treat the above-mentioned compounds contained in exhaust gas at electronics industry factories that use halogenated acyclic hydrocarbon compounds in the cleaning process, and this will put a brake on the destruction of the ossine layer in the stratosphere. It is extremely useful for industry as it makes it possible to
図は本発明の一実施例のハロゲン化非環式炭化水素化合
物の分解法を具体化する分解装置の略図である。
1・・ガラス製反応容器、2・・銅線製コイル電極、3
・・ステンレス製電極、4・・導入口、5・・排出口。
代理人の氏名 弁理士 粟野重孝 はか1名=437
?、aI7煤製コイオ鵠The figure is a schematic diagram of a decomposition apparatus embodying a method for decomposing a halogenated acyclic hydrocarbon compound according to an embodiment of the present invention. 1... Glass reaction vessel, 2... Copper wire coil electrode, 3
...Stainless steel electrode, 4.Inlet, 5.Outlet. Name of agent: Patent attorney Shigetaka Awano 1 person = 437? , aI7 soot Koio goose
Claims (1)
素を含む気体の混合物に無声放電させることを特徴とす
るハロゲン化非環式炭化水素化合物の分解方法。1. A method for decomposing a halogenated acyclic hydrocarbon compound, which comprises silently discharging a mixture of a gas of the halogenated acyclic hydrocarbon compound and a gas containing at least oxygen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63213085A JPH0260668A (en) | 1988-08-26 | 1988-08-26 | Method for decomposing halogenated acyclic hydrocarbon compounds |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63213085A JPH0260668A (en) | 1988-08-26 | 1988-08-26 | Method for decomposing halogenated acyclic hydrocarbon compounds |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0260668A true JPH0260668A (en) | 1990-03-01 |
Family
ID=16633306
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63213085A Pending JPH0260668A (en) | 1988-08-26 | 1988-08-26 | Method for decomposing halogenated acyclic hydrocarbon compounds |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0260668A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006129900A (en) * | 2004-11-02 | 2006-05-25 | Kanazawa Inst Of Technology | Detoxification treatment method for PCB-containing oil and detoxification treatment apparatus for PCB-containing oil |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5110173A (en) * | 1974-07-15 | 1976-01-27 | Sumitomo Chemical Co | Haigasuchuno harogenkatankasuisono jokyoho |
-
1988
- 1988-08-26 JP JP63213085A patent/JPH0260668A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5110173A (en) * | 1974-07-15 | 1976-01-27 | Sumitomo Chemical Co | Haigasuchuno harogenkatankasuisono jokyoho |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006129900A (en) * | 2004-11-02 | 2006-05-25 | Kanazawa Inst Of Technology | Detoxification treatment method for PCB-containing oil and detoxification treatment apparatus for PCB-containing oil |
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