JP3416751B2 - Detoxification of organic chlorine compounds - Google Patents
Detoxification of organic chlorine compoundsInfo
- Publication number
- JP3416751B2 JP3416751B2 JP23876492A JP23876492A JP3416751B2 JP 3416751 B2 JP3416751 B2 JP 3416751B2 JP 23876492 A JP23876492 A JP 23876492A JP 23876492 A JP23876492 A JP 23876492A JP 3416751 B2 JP3416751 B2 JP 3416751B2
- Authority
- JP
- Japan
- Prior art keywords
- organic chlorine
- chlorine compound
- compounds
- compound
- organic
- 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.)
- Expired - Fee Related
Links
Landscapes
- Processing Of Solid Wastes (AREA)
- Treating Waste Gases (AREA)
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は有機塩素化合物の無害化
処理法に関する。詳しくは、本発明は、絶縁材として使
用されたPBC、有機溶剤として使用されたトリクロロ
エチレン等の有機塩素化合物及び塩化ビニル等のごみ焼
却炉の運転中に発生したダイオキシン等を安全な無機化
合物に変化する有機塩素化合物の無害化処理法に関す
る。
【0002】これらの有機塩素化合物は、その安全な処
理技術が確立していないため、現在容器に貯蔵されたま
まになっている。これらの化合物を長期間容器で貯蔵し
ているが、容器の腐食が始まり環境汚染の恐れが生じて
いる。その他、これまでに有機塩素化合物を溶剤として
長期間使用しているうちに土壌及び地下水の汚染も問題
になっている。これらの有害物質の処理法が確立されれ
ば、公害問題の解消が期待される。
【0003】
【従来の技術】PBC、トリクロロエチレン等の有機塩
素化合物を直接焼却する方法については、現在開発中で
あって、これらの有機塩素化合物の実際の処理は未だ行
われていない。従来のごみ焼却炉で有機塩素化合物を焼
却する際に発生するダイオキシンの発生抑制のため、燃
焼条件の把握、発生したダイオキシンの捕集技術はかな
り進んでいるものの、ダイオキシンの処理技術が確立し
ていないため、捕集物は保管されたままになっている。
【0004】従来、有機塩素化合物を空気中で燃焼させ
る技術開発が行われてきた。その方法は、燃焼時に腐食
性の強い塩化水素及び塩素ガスを発生する上、高温を発
生するため炉材料の腐食が著しく実処理には至っていな
い。
【0005】
【発明が解決しようとする課題】本発明の目的は、有機
塩素化合物中の塩素を酸化銅中の銅と反応させて塩化銅
を生成させ、一方、有機塩素化合物を無害な化合物に変
化させる方法を提供することにある。
【0006】
【課題を解決するための手段】本願発明者は、この目的
達成のため鋭意研究の結果、有機塩素化合物を不活性雰
囲気又は低酸素雰囲気で400〜500℃に加熱して該
有機塩素化合物を気化させ、気体状の有機塩素化合物を
750〜800℃の温度において酸化銅と反応させて該
有機塩素化合物を脱塩素化することから成る有機塩素化
合物の無害化処理法を発明するに至った。
【0007】本願発明の方法においては、不活性雰囲気
中で有機塩素化合物を熱媒体に一定量を連続的に供給す
る。熱媒体は400〜500℃に加熱してあるため、有
機塩素化合物の大部分は気体となる。熱媒体としては、
塩素に耐食性のアルミナ、川砂等を用いる。ガス状の有
機塩素化合物は、予め750〜800℃に加熱した脱塩
素反応装置に不活性ガスで同伴して脱塩素反応を行う。
【0008】この反応は、不活性雰囲気または低酸素分
圧下で行うため、有機物の燃焼熱が少なく、炉材料の腐
食を抑制できる。塩素は銅と反応してガス状の塩化銅が
生成し、スクラバを通して塩化銅を回収、再利用を行
う。排ガスは活性炭を通過させた後、ブロワーを用いて
熱媒体に循環させる。循環系の装置を用いることで、毒
性の強い危険物の漏洩を防止するとともに不活性ガス及
び熱の有効利用を図ることができる。
【0009】
【実施例】本願発明を実施例によって具体的に説明す
る。図1は有機塩素化合物に汚染された土壌の改良に用
いた流動層式反応装置を示す。
【0010】流動層2の部分をマイクロ波加熱装置で約
500℃に加熱する。流動媒体には川砂を用いアルゴン
ガスで流動化した。脱塩素反応装置3は電熱器で約80
0℃に加熱した。次に、汚染模擬試料はホッパー1より
スクリューフィダを用いて流動層2内に約0.5Kg/
h供給した。有機塩素化合物は流動層2内で気化し、酸
化銅を設置した脱塩素反応装置3内で塩化銅を生成す
る。塩化銅はスクラバー4で捕集され水酸化銅として回
収された。排ガスは活性炭ガス清浄塔5を通過し循環ブ
ロワ6で流動層2に導入した。流動層部のハロゲンモニ
ターで塩素が存在しないことを確認して、模擬土壌を取
り出した。
【0011】本願発明の方法の重要な効果は、脱塩素反
応は不活性雰囲気で行われるので有機物の激しい燃焼熱
を伴わないこと、反応熱が小さいため炉材料の腐食抑制
が期待できること、更に、塩化銅を再生して利用できる
ため二次廃棄物の発生を伴わないことである。Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for detoxifying an organic chlorine compound. Specifically, the present invention converts PBC used as an insulating material, organic chlorine compounds such as trichloroethylene used as an organic solvent, and dioxins generated during the operation of a refuse incinerator such as vinyl chloride into safe inorganic compounds. To a method for detoxifying organic chlorine compounds. [0002] These organochlorine compounds are currently stored in containers because their safe treatment technology has not been established. Although these compounds have been stored in containers for long periods of time, corrosion of the containers has begun and there is a risk of environmental pollution. In addition, while organic chlorine compounds have been used as solvents for a long period of time, contamination of soil and groundwater has become a problem. If a treatment method for these harmful substances is established, it is expected that the problem of pollution will be resolved. [0003] A method of directly incinerating organic chlorine compounds such as PBC and trichloroethylene is currently under development, and the actual treatment of these organic chlorine compounds has not been performed yet. In order to control the generation of dioxins generated when incinerating organochlorine compounds in conventional refuse incinerators, the combustion conditions have been well understood, and the technology for collecting the generated dioxins has been considerably advanced. There are no collections, so they remain in storage. [0004] Conventionally, techniques for combusting organochlorine compounds in air have been developed. This method generates hydrogen chloride and chlorine gas which are highly corrosive at the time of combustion, and also generates high temperatures, so that the furnace material is significantly corroded and has not been practically treated. An object of the present invention is to react copper in an organic chlorine compound with copper in copper oxide to produce copper chloride, while converting the organic chlorine compound into a harmless compound. It is to provide a way to change it. Means for Solving the Problems The inventors of the present invention have conducted intensive studies to achieve this object. As a result, the organochlorine compound was heated to 400 to 500 ° C. in an inert atmosphere or a low-oxygen atmosphere to produce the organochlorine compound. The present invention has led to the invention of a method for detoxifying an organic chlorine compound, which comprises vaporizing a compound and reacting a gaseous organic chlorine compound with copper oxide at a temperature of 750 to 800 ° C. to dechlorinate the organic chlorine compound. Was. In the method of the present invention, a predetermined amount of an organic chlorine compound is continuously supplied to a heat medium in an inert atmosphere. Since the heat medium is heated to 400 to 500 ° C., most of the organic chlorine compounds become gas. As a heating medium,
Use corrosion-resistant alumina, river sand, etc. for chlorine. The gaseous organic chlorine compound is subjected to a dechlorination reaction by being accompanied by an inert gas in a dechlorination reaction apparatus heated to 750 to 800 ° C. in advance. [0008] Since this reaction is carried out in an inert atmosphere or under a low oxygen partial pressure, the heat of combustion of the organic matter is small and the corrosion of the furnace material can be suppressed. Chlorine reacts with copper to produce gaseous copper chloride, which is recovered and reused through a scrubber. After passing the activated carbon through the exhaust gas, the exhaust gas is circulated through a heat medium using a blower. By using a circulating device, it is possible to prevent leakage of highly toxic dangerous substances and to effectively use inert gas and heat. The present invention will be specifically described with reference to examples. FIG. 1 shows a fluidized bed reactor used for improvement of soil contaminated with organochlorine compounds. The fluidized bed 2 is heated to about 500 ° C. by a microwave heater. River sand was used as a fluid medium and fluidized with argon gas. The dechlorination reactor 3 uses an electric heater for about 80
Heated to 0 ° C. Next, the simulated contamination sample was introduced into the fluidized bed 2 from the hopper 1 using a screw feeder at about 0.5 kg /
h. The organic chlorine compound is vaporized in the fluidized bed 2 and forms copper chloride in the dechlorination reactor 3 in which copper oxide is installed. The copper chloride was collected by the scrubber 4 and recovered as copper hydroxide. The exhaust gas passed through the activated carbon gas purification tower 5 and was introduced into the fluidized bed 2 by the circulation blower 6. The simulated soil was taken out after confirming that chlorine was not present by a halogen monitor in the fluidized bed. An important effect of the method of the present invention is that the dechlorination reaction is carried out in an inert atmosphere, so that it does not involve intense heat of combustion of organic substances, and that the reaction heat is small, so that corrosion of furnace materials can be expected to be suppressed. Because copper chloride can be recycled and used, secondary waste is not generated.
【図面の簡単な説明】
【図1】有機塩素化合物に汚染された土壌の改良に使用
された流動層式反応装置。
【符号の説明】
1 有機塩素化合物試料供給機
2 流動層
3 脱塩素反応装置
4 スクラバー
5 活性炭ガス清浄層
6 循環ブロワー
7 受器
8 サイクロン
9 アルゴンガスBRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a fluidized bed reactor used for improving soil contaminated with organochlorine compounds. [Description of Signs] 1 Organochlorine compound sample feeder 2 Fluidized bed 3 Dechlorination reactor 4 Scrubber 5 Activated carbon gas cleaning bed 6 Circulating blower 7 Receiver 8 Cyclone 9 Argon gas
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 53/70 A62D 3/00 B09C 1/06 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) B01D 53/70 A62D 3/00 B09C 1/06
Claims (1)
焼却炉運転中に発生した有機塩素化合物を不活性雰囲気
又は低酸素雰囲気で400〜500℃に加熱して該有機
塩素化合物を気化させ、気体状の有機塩素化合物を75
0〜800℃の温度において酸化銅と反応させて該有機
塩素化合物を塩化銅として脱塩素化することから成る有
機塩素化合物の無害化処理法。(57) Claims 1. An organic chlorine compound contaminated soil and an organic chlorine compound generated during the operation of a refuse incinerator are heated to 400 to 500 ° C. in an inert atmosphere or a low oxygen atmosphere. The organic chlorine compound is vaporized by the
A method for detoxifying an organic chlorine compound, which comprises reacting the organic chlorine compound with copper oxide at a temperature of 0 to 800 ° C. to dechlorinate the organic chlorine compound as copper chloride.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23876492A JP3416751B2 (en) | 1992-07-24 | 1992-07-24 | Detoxification of organic chlorine compounds |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP23876492A JP3416751B2 (en) | 1992-07-24 | 1992-07-24 | Detoxification of organic chlorine compounds |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0639242A JPH0639242A (en) | 1994-02-15 |
| JP3416751B2 true JP3416751B2 (en) | 2003-06-16 |
Family
ID=17034919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP23876492A Expired - Fee Related JP3416751B2 (en) | 1992-07-24 | 1992-07-24 | Detoxification of organic chlorine compounds |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3416751B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4609057B2 (en) * | 2004-12-09 | 2011-01-12 | 栗田工業株式会社 | Dioxin decomposition agent and decomposition method |
| JP4639890B2 (en) * | 2005-03-25 | 2011-02-23 | 日立造船株式会社 | Decomposition method of organic halogen compounds |
-
1992
- 1992-07-24 JP JP23876492A patent/JP3416751B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0639242A (en) | 1994-02-15 |
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