JP3247543B2 - Alkali decomposition method for halogenated aromatic compounds - Google Patents
Alkali decomposition method for halogenated aromatic compoundsInfo
- Publication number
- JP3247543B2 JP3247543B2 JP12169094A JP12169094A JP3247543B2 JP 3247543 B2 JP3247543 B2 JP 3247543B2 JP 12169094 A JP12169094 A JP 12169094A JP 12169094 A JP12169094 A JP 12169094A JP 3247543 B2 JP3247543 B2 JP 3247543B2
- Authority
- JP
- Japan
- Prior art keywords
- alkali
- halogenated aromatic
- aromatic compound
- less
- mixture
- 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
Classifications
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D3/00—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances
- A62D3/30—Processes for making harmful chemical substances harmless or less harmful, by effecting a chemical change in the substances by reacting with chemical agents
- A62D3/36—Detoxification by using acid or alkaline reagents
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62D—CHEMICAL MEANS FOR EXTINGUISHING FIRES OR FOR COMBATING OR PROTECTING AGAINST HARMFUL CHEMICAL AGENTS; CHEMICAL MATERIALS FOR USE IN BREATHING APPARATUS
- A62D2101/00—Harmful chemical substances made harmless, or less harmful, by effecting chemical change
- A62D2101/20—Organic substances
- A62D2101/22—Organic substances containing halogen
Landscapes
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Business, Economics & Management (AREA)
- Emergency Management (AREA)
- Fire-Extinguishing Compositions (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Description
【0001】[0001]
【産業上の利用分野および目的】環境保全の上で、ハロ
ゲン化芳香族化合物を完全かつ安全に分解せしめること
は従来20年余りに亘って、重大な関心事である。本方
法は、化学的に上記目的を達しめる方法に関する。BACKGROUND OF THE INVENTION Completely and safely decomposing halogenated aromatic compounds for environmental protection has been a serious concern for more than 20 years. The present method relates to a method for achieving the above objective chemically.
【0002】[0002]
【従来の技術】従来、ハロゲン化芳香族化合物の除去あ
るいは分解に関して、多くの努力が成された。その数例
を示すと、アルカリとの反応に関しては、U.S.P.
2,951,804で、アルミナ−アルカリ法が示され
ている。更にU.S.P.4,532,028では、ア
ルキルあるいはアルキレンスルホオキシドとポリオール
との混合物中で、アルカリと50,000ppm以下の
PCBとを200℃以下で反応させて、数ppmとする
方法が示されている。そのほか、ナトリウムの溶融物を
用いるカナダ特許408,116や、ポリエチレングリ
コールを吸着したアルカリ土類金属を用いるイタリア特
許22,215等があるが、未だに実質的に安全な濃度
にまでPCBを除去することは実現されていない。最近
では、パラフィンを水素源とする還元法も研究されてい
るが、この方法はPCBの残存率が1ppm程度であ
り、しかも反応温度が高いという欠点を有している。2. Description of the Related Art Hitherto, many efforts have been made regarding removal or decomposition of halogenated aromatic compounds. Some examples are shown in U.S. Pat. S. P.
2,951,804 describes the alumina-alkali method. Further, U. S. P. No. 4,532,028 discloses a method in which an alkali and 50,000 ppm or less of PCB are reacted at 200 ° C. or less in a mixture of an alkyl or alkylene sulfoxide and a polyol to give several ppm. Other examples include Canadian Patent 408,116 which uses a melt of sodium and Italian Patent 22,215 which uses an alkaline earth metal adsorbed with polyethylene glycol, but still removes PCBs to a substantially safe concentration. Has not been realized. Recently, a reduction method using paraffin as a hydrogen source has also been studied, but this method has a drawback that the residual ratio of PCB is about 1 ppm and the reaction temperature is high.
【0003】[0003]
【発明が解決しようとする課題】先にあげた従来の技術
はそれぞれ特徴があり、かなり効果のあることになって
いるが、実際には、溶剤が大量のアルカリ物質に対し
て、150℃以上の高い温度ではとても耐えるものでな
いこと等、工業的に実施できる技術ということはできな
い。本発明者等は、アルカリの作用に関して特に多くの
実験を行った結果、これらの問題を解決するに至った。The above-mentioned prior arts have their respective features and are expected to be quite effective. However, in practice, the solvent is not suitable for a large amount of alkaline substances at 150 ° C. or more. It cannot be said that it is a technology that can be implemented industrially, such as that it cannot withstand very high temperatures. The present inventors have conducted many experiments particularly on the action of alkali, and as a result, have solved these problems.
【0004】[0004]
【課題を解決するための手段】本発明者等は、特別の高
沸点かつ耐熱、耐アルカリ性の極性溶剤を選び、ハロゲ
ン化芳香族化合物と該極性溶剤に溶解する量を大幅に越
えた量比のアルカリ物質とを150℃以上300℃以下
で接触させる方法が、ハロゲン化芳香族化合物を実質的
に、現在知られる方法による検出限界以下に分解する有
効な手段であることを見出した。Means for Solving the Problems The present inventors have selected a special polar solvent having a high boiling point, heat resistance, and alkali resistance, and have a ratio of the halogenated aromatic compound and the amount which is much larger than the amount dissolved in the polar solvent. It has been found that the method of contacting with an alkali substance at 150 ° C. or more and 300 ° C. or less is an effective means for substantially decomposing a halogenated aromatic compound below the detection limit of a currently known method.
【0005】ここに選ばれた極性溶剤は、市販で容易に
入手できるもので、その中でも毒性が低く、耐熱、耐ア
ルカリの強い性質のものであるが、何よりもまずハロゲ
ン化芳香族化合物をよく溶解する。反応が進行して、溶
剤中のハロゲン化芳香族化合物が数mg/kgの濃度か
らさらに検出限界以下(0.5ppb以下)に反応を完
結させるべく進行させる働きが要求される。本発明はま
さにそれを解決した。The polar solvents selected here are those which are readily available on the market and have low toxicity, high heat resistance and strong alkali resistance. Dissolve. As the reaction progresses, it is required that the halogenated aromatic compound in the solvent be advanced from the concentration of several mg / kg to the detection limit or less (0.5 ppb or less) to complete the reaction. The present invention has solved just that.
【0006】本発明に有効な耐熱、耐アルカリ性、かつ
毒性の低い非プロトン極性溶剤は、1,3−ジメチル−
2−イミダゾリジノン(以下DM1と略す)、テトラメ
チレンスルフォン(以下スルフォランと略す)のいずれ
かあるいはこの両者の任意の割合の混合物を主とし、さ
らに場合によっては、ジメチルスルフォキシド、N−メ
チルピロリドン、テトラメチル尿素、ジエチレングリコ
ールジメチルエーテル、ポリエチレングリコールジメチ
ルエーテルなる群から選ばれた一つあるいは二つ以上の
混合物を全体の35%以下まで混入しても、実質的には
差し支えない。The aprotic polar solvent effective in the present invention, which is heat-resistant, alkali-resistant and low in toxicity, is 1,3-dimethyl-
Either 2-imidazolidinone (hereinafter abbreviated as DM1), tetramethylene sulfone (hereinafter abbreviated as sulfolane), or a mixture of both in an arbitrary ratio, and in some cases, dimethyl sulfoxide, N-methyl It is practically possible to mix up to 35% or less of one or more mixtures selected from the group consisting of pyrrolidone, tetramethylurea, diethylene glycol dimethyl ether and polyethylene glycol dimethyl ether.
【0007】本発明を最も有効ならしめるのは、上記非
プロトン極性溶剤に対して、5,000mg/kg以
上、特に好ましくは7,000mg/kg以上のアルカ
リを共存させる組合せにある。What makes the present invention most effective is a combination in which an alkali of 5,000 mg / kg or more, particularly preferably 7,000 mg / kg or more, coexists with the aprotic polar solvent.
【0008】一般に反応を完結せしめるべく、一方の安
価な薬品を過剰に用いる手段は、よく知られているが、
本発明における大幅に過剰なアルカリの存在は、表1に
より明らかなごとく、ただ単に分解されるべきハロゲン
化芳香族化合物に対するアルカリの比の問題でなく、非
プロトン極性溶剤の働きを本来のものとする上で、重要
なのである。Means for excessively using one of the inexpensive chemicals in order to complete the reaction is generally well known.
The presence of a large excess of alkali in the present invention, as evident from Table 1, is not merely a matter of the ratio of alkali to halogenated aromatic compound to be decomposed, but rather the action of the aprotic polar solvent. It is important in doing.
【0009】本発明において行われる化学反応の本質的
な機構を学理的に説明することは、今の段階では完全に
は出来ないが、本発明の方法を行うことで、出発物質の
ハロゲン化芳香族化合物が100%から数mg/kgに
希釈された広い範囲において、実質的に検出不可能な濃
度にまで分解されるのである。It is not possible at this stage to fully explain the essential mechanism of the chemical reaction carried out in the present invention, but by carrying out the method of the present invention, the starting halogenated aromatic compound can be obtained. Group compounds are degraded to a substantially undetectable concentration over a wide range from 100% to a few mg / kg.
【0010】[0010]
【実施例】ハロゲン化芳香族化合物を除去・分解する方
法は、前述のようにして行われるが、本発明の方法を基
本に多くの変法を検討したが、その各々について説明を
することは、本発明の趣旨を明らかにするために必ずし
も適当でないので、以下に基本的な実施例を表1に比較
例を表2に示す。これらの実施例においては、顕著な効
果が示されたが、比較例においては、アルカリ濃度が低
い場合、PCBの分解効果が顕著でないことを示してい
る。EXAMPLES The method for removing and decomposing halogenated aromatic compounds is carried out as described above. A number of modifications were studied on the basis of the method of the present invention. However, since it is not always appropriate to clarify the gist of the present invention, Table 1 shows a basic example and Table 2 shows a comparative example. In these Examples, a remarkable effect was shown, but in Comparative Examples, when the alkali concentration was low, it was shown that the decomposition effect of PCB was not remarkable.
【0011】[0011]
【表1】 [Table 1]
【0012】[0012]
【表2】 [Table 2]
【0013】実施例1 PCB80ppmを含む絶縁油50g、DMI100
g、そしてアルカリとして粉末状のNaOHを2g添加
する。系のアルカリ濃度をおよそ13,000ppmと
して、全体をよくかき混ぜつつ200℃にて6時間保っ
た。次いで、室温に冷却して、下層のDMIを除き、油
層のPCBをガスクロマトグラフィ質量分析計(以下G
C−MSと略す)によって分析したところ、N.D.
(GC−MSの検出限界以下、即ち0.5ppb[0.
5μg/kg]以下)まで減少していた。一方、比較例
の1においては、実施例1と同条件で反応させたが、添
加したアルカリ濃度だけが2,000mg/kg(2,
000ppm)と低い。この場合、6時間反応させて、
油層の残存PCB濃度をGC−MSで分析したところ、
4,000ppb(4,000μg/kg)であり、ア
ルカリ濃度を高くすることの効果が歴然としている。Example 1 50 g of insulating oil containing 80 ppm of PCB, DMI 100
g, and 2 g of powdered NaOH as alkali. The system was adjusted to an alkali concentration of about 13,000 ppm, and kept at 200 ° C. for 6 hours while thoroughly stirring the whole. Next, the mixture was cooled to room temperature, and the DMI in the lower layer was removed, and the PCB in the oil layer was subjected to gas chromatography mass spectrometry (hereinafter referred to as G
C-MS). D.
(Below the detection limit of GC-MS, that is, 0.5 ppb [0.
5 μg / kg or less). On the other hand, in Comparative Example 1, the reaction was carried out under the same conditions as in Example 1, but only the added alkali concentration was 2,000 mg / kg (2,
000 ppm). In this case, let it react for 6 hours,
When the residual PCB concentration of the oil layer was analyzed by GC-MS,
It is 4,000 ppb (4,000 μg / kg), and the effect of increasing the alkali concentration is obvious.
【0014】実施例2 表1に示す条件で実施例1と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 2 The same treatment as in Example 1 was performed under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0015】実施例3 表1に示す条件で実施例1と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 3 The same treatment as in Example 1 was performed under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0016】実施例4 表1に示す条件で実施例1と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 4 The same treatment as in Example 1 was carried out under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0017】実施例5 表1に示す条件で実施例1と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 5 The same treatment as in Example 1 was performed under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0018】実施例6 表1に示す条件で実施例1と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 6 The same treatment as in Example 1 was carried out under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0019】実施例7 表1に示す条件で実施例1と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 7 The same treatment as in Example 1 was performed under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0020】実施例8 表1に示す条件で、実施例1と同様の処理を行う。ただ
し、この場合、絶縁油が少量のため、DMI層に溶け込
んでしまうので、DMI中のPCBの分析をGC−MS
で行う。始めにアルカリとして、粉末状のNaOHを1
3g添加してアルカリ濃度を130,000mg/kg
(130,000ppm)と高い濃度にして、よくかき
まぜつつ5時間反応させた。この後、DMI中の残存P
CBの分析を行ったところ、N.D.(0.5ppb)
まで減少していた。Example 8 The same processing as in Example 1 is performed under the conditions shown in Table 1. However, in this case, since a small amount of insulating oil was dissolved in the DMI layer, the analysis of PCB in DMI was performed by GC-MS.
Do with. First, as an alkali, add powdery NaOH to 1
Add 3g to increase alkali concentration to 130,000mg / kg
(130,000 ppm) and reacted for 5 hours with good stirring. After this, the remaining P in the DMI
When CB was analyzed, N.V. D. (0.5ppb)
Had decreased to
【0021】実施例9 表1に示す条件で実施例8と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 9 The same treatment as in Example 8 was performed under the conditions shown in Table 1. D. (Less than 0.5 ppb).
【0022】実施例10 表1に示す条件で実施例8と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 10 The same treatment as in Example 8 was performed under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0023】実施例11 表1に示す条件で実施例8と同様であるが、絶縁油を全
く入れないで、処理を行ったところ、残存PCBはN.
D.(0.5ppb以下)まで減少していた。Example 11 The same treatment as in Example 8 was performed under the conditions shown in Table 1 except that no insulating oil was added.
D. (Less than 0.5 ppb).
【0024】実施例12 表1に示す条件で実施例11と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 12 The same treatment as in Example 11 was performed under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0025】実施例13 表1に示す条件で実施例11と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 13 The same treatment as in Example 11 was performed under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0026】実施例14 表1に示す条件で実施例11と同様の処理を行ったとこ
ろ、残存PCBはN.D.(0.5ppb以下)まで減
少していた。Example 14 The same treatment as in Example 11 was performed under the conditions shown in Table 1, and the remaining PCB D. (Less than 0.5 ppb).
【0027】[0027]
【発明の効果】本発明によって、少量であっても環境保
護に問題とされ、あるいは人体に直接害をもたらすと考
えられているハロゲン化芳香族化合物(主としてPC
B)を、実質的に、害がないとされるまで完全に近く分
解でき、それらを含有する炭化水素油から除去・分解す
ることが可能となった。Industrial Applicability According to the present invention, halogenated aromatic compounds (mainly PCs) which are considered to pose a problem to environmental protection even in a small amount or to cause direct harm to the human body
B) can be substantially completely decomposed until it is considered harmless, and it has become possible to remove and decompose B) from the hydrocarbon oil containing them.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 谷本 文男 京都府京都市左京区下鴨森本町15番地 財団法人生産開発科学研究所内 (72)発明者 九十九 清彦 京都府京都市左京区下鴨森本町15番地 財団法人生産開発科学研究所内 (72)発明者 中村 充彦 千葉県柏市布施新町4−8−6 (72)発明者 矢野 恒夫 埼玉県飯能市川寺413−14 (72)発明者 鈴木 伸洋 東京都調布市西つつじヶ丘2−4−1 東京電力株式会社技術研究所内 (72)発明者 戸澗 敏孔 東京都調布市西つつじヶ丘2−4−1 東京電力株式会社技術研究所内 (72)発明者 古橋 鴻一 滋賀県甲賀郡甲西町大池町1−1 株式 会社ネオス内 (72)発明者 中山 伸之 滋賀県甲賀郡甲西町大池町1−1 株式 会社ネオス内 (56)参考文献 特開 平6−25691(JP,A) 特開 昭49−126651(JP,A) 特開 平7−8572(JP,A) 特表 昭58−500200(JP,A) 特表 平8−511766(JP,A) 米国特許4910353(US,A) (58)調査した分野(Int.Cl.7,DB名) C07B 35/06 A62D 3/00 ZAB ──────────────────────────────────────────────────続 き Continuing on the front page (72) Fumio Tanimoto 15th institute of Shimogamo Morihoncho, Sakyo-ku, Kyoto, Kyoto Prefecture (72) Inventor Kiyohiko Kujuku Kiyohiko Kumogamo, Shimogamo-cho, Sakyo-ku, Kyoto, Kyoto No. 15 Inside the Research Institute for Production Science (72) Inventor Mitsuhiko Nakamura 4-8-6 Fuse Shinmachi, Kashiwa City, Chiba Prefecture (72) Inventor Tsuneo Yano 413-14 Kawadera Hanno City, Saitama Prefecture (72) Inventor Nobuhiro Suzuki Tokyo 2-4-1 Nishi-Atsujigaoka, Tokyo-Chofu City Tokyo Electric Power Co., Inc. (72) Inventor Toshiro Togan 2-4-1, Nishi-Atsujigaoka, Chofu-shi, Tokyo Tokyo Electric Power Co., Inc. (72 ) Inventor Koichi Furuhashi 1-1, Oike-cho, Kosai-cho, Koga-gun, Shiga Prefecture Inside Neos Co., Ltd. (72) Nobuyuki Nakayama 1-1, Oike-cho, Kosai-cho, Koga-gun, Shiga Prefecture Stock Association (56) References JP-A-6-25691 (JP, A) JP-A-49-126651 (JP, A) JP-A-7-8572 (JP, A) JP-A-58-500200 (JP, A) A) JP-A-8-511766 (JP, A) U.S. Pat. No. 4,910,353 (US, A) (58) Fields investigated (Int. Cl. 7 , DB name) C07B 35/06 A62D 3/00 ZAB
Claims (5)
非プロトン極性溶剤中で150℃ないし300℃にて、
1時間ないし10時間接触させ、ハロゲン化芳香族化合
物の残存濃度を1ppbオーダ以下に処理するハロゲン
化芳香族化合物のアルカリ分解方法において、 (i). 系中のアルカリの開始時割合を、非プロトン極性溶
剤に対して5000mg/kg以上とし、かつ、 (ii) .アルカリ比(ハロゲン化芳香族化合物のハロゲン
のモル数に対するアル カリのモル数の比)を、1.0以
上とすること、 を特徴とするハロゲン化芳香族化合物のアルカリ分解方
法。1. A method according to claim 1, wherein the halogenated aromatic compound and the alkali are mixed at 150 ° C. to 300 ° C. in an aprotic polar solvent.
Contact for 1 hour to 10 hours, and halogenated aromatic compound
Halogen treating residual concentration of substances to less than 1 ppb order
In the alkali decomposition method aromatics, a (i). Beginning proportion of alkali in the system, aprotic polar solvent
5,000 mg / kg or more to the agent , and (ii) the alkali ratio (the halogen of the halogenated aromatic compound)
The ratio of the number of moles of alkali to the number of moles), 1.0 or more
A method for alkali decomposition of a halogenated aromatic compound, characterized by the above .
フェニール類、ポリ塩化ターフェニル類およびポリ臭化
ビフェニール類からなる群から選ばれた少なくとも一種
類あるいは二種類以上の混合物である、請求項1記載の
ハロゲン化芳香族化合物のアルカリ分解方法。2. The method according to claim 1, wherein the halogenated aromatic compound is at least one kind or a mixture of two or more kinds selected from the group consisting of polychlorinated biphenyls, polychlorinated terphenyls and polybrominated biphenyls. A method for alkali decomposition of a halogenated aromatic compound as described above.
が非芳香族系炭化水素である炭化水素油によって、80
%以下2mg/kg以上の範囲で希釈されている、請求
項1記載のハロゲン化芳香族化合物のアルカリ分解方
法。3. The method according to claim 1, wherein the halogenated aromatic compound is a hydrocarbon oil whose main component is a non-aromatic hydrocarbon.
The alkali decomposition method of a halogenated aromatic compound according to claim 1, wherein the compound is diluted in a range of 2% / kg or less to 2mg / kg or more.
酸化カルシウム、水酸化マグネシウムなる群から選ばれ
た少なくとも一つあるいは二つ以上の混合物であること
を特徴とする、請求項1記載のハロゲン化芳香族化合物
のアルカリ分解方法。4. The halogenated fragrance according to claim 1, wherein the alkali is at least one or a mixture of two or more selected from the group consisting of caustic soda, caustic potash, calcium hydroxide, and magnesium hydroxide. For decomposing group III compounds with alkali.
ル−2−イミダゾリジノン、テトラメチレンスルフォン
のいずれかあるいはこの任意の割合の混合物を主成分と
し、さらに場合によっては、ジメチルスルフォキシド、
N−メチルピロリドン、テトラメチル尿素、ジエチレン
グリコール、ポリエチレングリコールジメチルエーテル
なる群から選ばれた一つあるいは二つ以上の混合物を3
5%以下含む、請求項1記載のハロゲン化芳香族化合物
のアルカリ分解方法。5. An aprotic polar solvent comprising 1,3-dimethyl-2-imidazolidinone or tetramethylene sulfone or a mixture in any ratio thereof as a main component, and optionally dimethyl sulfoxide. ,
One or a mixture of two or more selected from the group consisting of N-methylpyrrolidone, tetramethylurea, diethylene glycol, polyethylene glycol dimethyl ether
The alkali decomposition method for halogenated aromatic compounds according to claim 1, which contains 5% or less.
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12169094A JP3247543B2 (en) | 1994-04-22 | 1994-04-22 | Alkali decomposition method for halogenated aromatic compounds |
| AU22672/95A AU2267295A (en) | 1994-04-22 | 1995-04-20 | Method of decomposing halogenated aromatic compound with alkaline substance |
| EP95916026A EP0711580A1 (en) | 1994-04-22 | 1995-04-20 | Method of decomposing halogenated aromatic compound with alkaline substance |
| PCT/JP1995/000785 WO1995028993A1 (en) | 1994-04-22 | 1995-04-20 | Method of decomposing halogenated aromatic compound with alkaline substance |
| TW84106595A TW288009B (en) | 1994-04-22 | 1995-06-27 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12169094A JP3247543B2 (en) | 1994-04-22 | 1994-04-22 | Alkali decomposition method for halogenated aromatic compounds |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07289656A JPH07289656A (en) | 1995-11-07 |
| JP3247543B2 true JP3247543B2 (en) | 2002-01-15 |
Family
ID=14817471
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12169094A Expired - Fee Related JP3247543B2 (en) | 1994-04-22 | 1994-04-22 | Alkali decomposition method for halogenated aromatic compounds |
Country Status (5)
| Country | Link |
|---|---|
| EP (1) | EP0711580A1 (en) |
| JP (1) | JP3247543B2 (en) |
| AU (1) | AU2267295A (en) |
| TW (1) | TW288009B (en) |
| WO (1) | WO1995028993A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101377105B1 (en) | 2011-11-28 | 2014-03-28 | 안동대학교 산학협력단 | Method for chemical treatment of Polybrominated diphenyl ether |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2942856B2 (en) * | 1996-10-09 | 1999-08-30 | 財団法人生産開発科学研究所 | Cleaning and removal method for persistent chlorine compounds |
| JP4537539B2 (en) * | 2000-06-20 | 2010-09-01 | 利夫 半谷 | Decomposition treatment method and treatment equipment for hazardous substances |
| JP4913366B2 (en) * | 2005-06-21 | 2012-04-11 | 株式会社ネオス | Treatment method of persistent organic halogen compounds |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4910353A (en) | 1983-02-07 | 1990-03-20 | Transformer Service, Inc. | Dehalogenation of polychlorinated biphenyls and other related compounds |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2951804A (en) | 1957-10-22 | 1960-09-06 | Houdry Process Corp | Purification of reformate charge stocks using activated alumina impregnated with alkali or alkaline earth metal hydroxides |
| JPS49126651A (en) * | 1973-04-10 | 1974-12-04 | ||
| CA1181771A (en) | 1982-07-27 | 1985-01-29 | Ontario Hydro | Process for dehalogenation of organic halides |
| IT1206508B (en) | 1983-07-22 | 1989-04-27 | Sea Marconi Decontamin Srl | CONTINUOUS PROCESS FOR THE DECOMPOSITION AND DECONTAMINATION OF ORGANIC COMPOUNDS AND HALOGENATED TOXIC AGENTS. |
| US4532028A (en) | 1983-10-24 | 1985-07-30 | Niagara Mohawk Power Corporation | Method for reducing content of halogenated aromatics in hydrocarbon solutions |
| JP2831869B2 (en) * | 1991-12-27 | 1998-12-02 | 日本ペイント株式会社 | Decomposition method of halogenated hydrocarbon |
| JP2611900B2 (en) * | 1992-06-05 | 1997-05-21 | 財団法人生産開発科学研究所 | Method for removing halogenated aromatic compounds from hydrocarbon oil |
-
1994
- 1994-04-22 JP JP12169094A patent/JP3247543B2/en not_active Expired - Fee Related
-
1995
- 1995-04-20 WO PCT/JP1995/000785 patent/WO1995028993A1/en not_active Ceased
- 1995-04-20 EP EP95916026A patent/EP0711580A1/en not_active Withdrawn
- 1995-04-20 AU AU22672/95A patent/AU2267295A/en not_active Abandoned
- 1995-06-27 TW TW84106595A patent/TW288009B/zh active
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4910353A (en) | 1983-02-07 | 1990-03-20 | Transformer Service, Inc. | Dehalogenation of polychlorinated biphenyls and other related compounds |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101377105B1 (en) | 2011-11-28 | 2014-03-28 | 안동대학교 산학협력단 | Method for chemical treatment of Polybrominated diphenyl ether |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH07289656A (en) | 1995-11-07 |
| TW288009B (en) | 1996-10-11 |
| WO1995028993A1 (en) | 1995-11-02 |
| AU2267295A (en) | 1995-11-16 |
| EP0711580A1 (en) | 1996-05-15 |
| EP0711580A4 (en) | 1996-03-20 |
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