JPH08117358A - Method for decomposing polyclorinated biphfenyl - Google Patents

Method for decomposing polyclorinated biphfenyl

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Publication number
JPH08117358A
JPH08117358A JP6284004A JP28400494A JPH08117358A JP H08117358 A JPH08117358 A JP H08117358A JP 6284004 A JP6284004 A JP 6284004A JP 28400494 A JP28400494 A JP 28400494A JP H08117358 A JPH08117358 A JP H08117358A
Authority
JP
Japan
Prior art keywords
polychlorinated biphenyls
chlorinated
pcb
decomposing
polyclorinated
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
Application number
JP6284004A
Other languages
Japanese (ja)
Inventor
Akiko Miya
晶子 宮
Shin Taniguchi
紳 谷口
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP6284004A priority Critical patent/JPH08117358A/en
Publication of JPH08117358A publication Critical patent/JPH08117358A/en
Pending legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)

Abstract

PURPOSE: To provide a method for decomposing polyclorinated biphenyl that is safe and efficient, and allows decomposed substances to be easily dumped. CONSTITUTION: In the decomposition of polyclorinated biphenyl group, a polyclorinated biphenyl in a fluid to be processed is decomposed using a chemical decomposition process, and a dechlorination reaction is stopped at a point when all amount of a high-chlorinated polyclorinated biphenyl to be processed is dechlorinated to be a low chlorinated polyclorinated biphenyl group with mono-, di- or trichloride and the low chlorinated polyclorinated biphenyl group with mono-, di- or trichloride is decomposed using microorganism. To perform a microorganism decomposition, a product or a fractional distillation at 150 to 350 deg.C of the product resulted from a chemical decomposition process and a water solution containing nutrient salts and polyclorinated biphenyl group decomposing fungus are mixed under aerobic condition.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ポリ塩化ビフェニール
類の分解方法に係わり、特に、ポリ塩化ビフェニール類
の塩素を化学的分解方法により脱離して低塩素化した
後、微生物によって分解、無害化するポリ塩化ビフェニ
ール類の分解方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for decomposing polychlorinated biphenyls, and in particular, dechlorinating polychlorinated biphenyls by a chemical decomposing method to reduce chlorine and then decomposing and detoxifying by microorganisms. The present invention relates to a method for decomposing polychlorinated biphenyls.

【0002】[0002]

【従来の技術】PCB(ポリ塩化ビフェニール類)、ダ
イオキシン類、ハロゲン化農薬などのハロゲン化有機化
合物は環境汚染物質として大きな問題となっている。特
にPCBは優れた絶縁性を持ち難燃性であることから、
主として電気絶縁油として大量に生産され広く使われて
きたが、環境中に出たPCBが人体に蓄積されて肝臓障
害などの強い毒性を呈することが判明して、生産及び新
たな使用が禁止されている。PCBは難分解性のために
その処分が困難であり、種々の処分方法が検討されてい
る。例えば高温燃焼法、微生物による分解法、化学的分
解法など様々な処理法が提案されている。
2. Description of the Related Art Halogenated organic compounds such as PCBs (polychlorinated biphenyls), dioxins and halogenated pesticides have become a serious problem as environmental pollutants. In particular, because PCB has excellent insulation and is flame retardant,
Mainly produced in large quantities as an electrical insulating oil and widely used, PCBs released into the environment have been found to accumulate in the human body and exhibit strong toxicity such as liver damage, and production and new use are prohibited. ing. PCB is difficult to dispose because it is difficult to decompose, and various disposal methods have been studied. For example, various treatment methods such as a high temperature combustion method, a microbial decomposition method, and a chemical decomposition method have been proposed.

【0003】化学的分解処理方法としては、例えば高沸
点油を溶剤及び水素供与体として使用し、ハロゲン化有
機化合物を還元的に脱ハロゲン化して無害化する方法
(国際特許出願番号PCT/US/01112や特願平
6−39332号など)が提案されている。これらの方
法で高塩素化PCBを処理する場合、高温燃焼法と比べ
て低温の条件において、高塩素化PCBは短時間で分解
され、かつ残存するPCBも3塩素化PCBまで脱塩素
化されるという特徴がある。しかし、通常の化学反応と
同様に残存PCB濃度は反応時間に対して指数関数的に
減少するため、残存する3塩素化PCBを完全に脱塩素
化し、分解するためには、はじめの高塩素化PCBが分
解され、かつ残存するPCBが3塩素化PCBまで脱塩
素化されるまでに要した時間及びエネルギー以上の、多
くの処理時間及びエネルギーを要するという問題があ
る。
As a chemical decomposition treatment method, for example, a high boiling point oil is used as a solvent and a hydrogen donor, and a halogenated organic compound is reductively dehalogenated to render it harmless (International Patent Application No. PCT / US / 01112 and Japanese Patent Application No. 6-39332). When treating highly chlorinated PCBs by these methods, the highly chlorinated PCBs are decomposed in a short time and the residual PCBs are also dechlorinated to trichlorinated PCBs at a temperature lower than that of the high temperature combustion method. There is a feature called. However, the residual PCB concentration decreases exponentially with the reaction time as in the normal chemical reaction. Therefore, in order to completely dechlorinate and decompose the remaining trichlorinated PCB, the first high chlorination There is a problem in that much processing time and energy are required, which is more than the time and energy required for the PCB to be decomposed and the residual PCB to be dechlorinated to the trichlorinated PCB.

【0004】一方、環境中に放出されたPCBは微生物
によって徐々に分解されることが知られており、PCB
を分解する微生物として、既に多種類の細菌や放線菌が
単離されている。これらのPCB分解微生物の多くは、
好気条件下で3塩素化以下の低塩素化PCBを容易に分
解することができるが、4塩素化以上のPCBの分解性
は悪く、特に5塩素化PCBを分解できる細菌は極めて
限られた種類の細菌であることが確認されている(App
l. Environ. Microbiol., 35, 223, 1978、Basic Life
Sci., 45, 253, 1988) 。
On the other hand, it is known that PCBs released into the environment are gradually decomposed by microorganisms.
Many kinds of bacteria and actinomycetes have already been isolated as microorganisms that decompose lactic acid. Many of these PCB-degrading microorganisms
Under aerobic conditions, it is possible to easily decompose low chlorinated PCBs with trichlorination or lower, but the degradability of PCBs with 4 chlorination or higher is poor, and the number of bacteria capable of degrading pentachlorinated PCBs is extremely limited. Confirmed to be a type of bacteria (App
l. Environ. Microbiol., 35, 223, 1978, Basic Life
Sci., 45, 253, 1988).

【0005】自然界では1又は2塩素化PCBがほとん
ど検出されず、比較的高塩素化のPCBの検出頻度が高
いことも、これを裏付けている。また自然環境中では、
嫌気条件下で高塩素化PCBが微生物によって徐々に脱
塩素化されることが知られているが、これらの嫌気性微
生物はまだ単離されていない。以上のように一般に高塩
素化PCBは微生物分解が難しいこと、また高濃度のP
CBは分解不可能なことから、従来はPCBの分解方法
として微生物分解法は実用化研究が行なわれていなかっ
た。
This is supported by the fact that almost no mono- or di-chlorinated PCBs are detected in the natural world and the frequency of detection of relatively highly chlorinated PCBs is high. In the natural environment,
It is known that highly chlorinated PCBs are gradually dechlorinated by microorganisms under anaerobic conditions, but these anaerobic microorganisms have not yet been isolated. As described above, in general, highly chlorinated PCB is difficult to be decomposed by microorganisms and high concentration of P
Since CB cannot be decomposed, a microbial decomposition method has not hitherto been studied as a method for decomposing PCB.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解決し、微生物分解処理法を化学的分解処
理方法と組み合わせることにより、安全性に優れ効率よ
く、また分解処理物の廃棄処分も容易にできるPCBの
分解方法を提供することを課題とする。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art and combines a microbial decomposition treatment method with a chemical decomposition treatment method to provide excellent safety and efficiency, and a decomposition-treated product. An object of the present invention is to provide a method for disassembling a PCB that can be easily disposed of.

【0007】[0007]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、ポリ塩化ビフェニール類の分解方法に
おいて、被処理ポリ塩化ビフェニール類の化学的分解処
理方法による脱塩素化反応を、被処理高塩素化ポリ塩化
ビフェニール類の全量を3塩素以下の低塩素化ポリ塩化
ビフェニール類に脱塩素化した時点で止め、生成した3
塩素化以下の低塩素化ポリ塩化ビフェニール類を微生物
分解するものである。このように、本発明においては、
化学的分解処理方法の脱塩素化反応を、被処理高塩素化
PCBの全量が3塩素化以下の低塩素化PCBに脱塩素
化された時点で止め、生成した3塩素化以下の低塩素化
PCBを微生物分解することを特徴とするPCBの分解
方法としたものである。本発明に用いる化学的分解処理
方法としては、化学反応により脱ハロゲン化を行ない、
有害ハロゲン化有機化合物を分解、無害化できる方法で
あればいずれの方法も適用することができる。
In order to solve the above-mentioned problems, in the present invention, in a method for decomposing polychlorinated biphenyls, a dechlorination reaction by a chemical decomposition treatment method for polychlorinated biphenyls to be treated is performed. When the total amount of treated high chlorinated polychlorinated biphenyls was reduced to 3 chlorine or less to low chlorinated polychlorinated biphenyls, it was stopped and produced.
It biodegrades chlorinated polychlorinated biphenyls below chlorination. Thus, in the present invention,
The dechlorination reaction of the chemical decomposition treatment method is stopped when the total amount of highly chlorinated PCBs to be treated has been dechlorinated to a low chlorinated PCB of 3 chlorination or less, and the generated low chlorination of 3 chlorination or less is chlorinated. This is a method for decomposing PCB, which is characterized by biodegrading PCB. The chemical decomposition treatment method used in the present invention includes dehalogenation by a chemical reaction,
Any method can be applied as long as it can decompose and detoxify the harmful halogenated organic compound.

【0008】化学的分解処理方法としては、具体的には
貴金属触媒の存在下で水素を添加して脱ハロゲン化を行
なう水素添加法、金属ナトリウムにより還元的に脱ハロ
ゲン化する金属ナトリウム法、ポリエチレングリコール
と水酸化カリウムを添加して還元的に脱ハロゲン化する
KPEG法などがあるが、特に好適には高沸点油を溶剤
及び水素供与体として使用し、ハロゲン化有機化合物を
還元的に脱ハロゲン化して無害化する方法(国際特許出
願番号PCT/US/01112や特願平6−3933
2号など)を適用することができる。本発明において
は、これら化学的分解処理方法の脱塩素化反応を、有害
ポリ塩素ビフェニール類の全量が3塩素化以下の低塩素
化ポリ塩化ビフェニール類に脱塩素化された時点で止
め、4塩素化以上の化合物が存在しないことを確認した
後、微生物分解方法に供することができる。
Specific examples of the chemical decomposition treatment method include a hydrogenation method in which hydrogen is added for dehalogenation in the presence of a noble metal catalyst, a metal sodium method in which reductive dehalogenation is performed with metal sodium, and polyethylene. There is a KPEG method in which glycol and potassium hydroxide are added to reductively dehalogenate. Particularly preferably, a high boiling point oil is used as a solvent and a hydrogen donor to reductively dehalogenate a halogenated organic compound. To make it harmless (International Patent Application No. PCT / US / 01112 and Japanese Patent Application No. 6-3933)
No. 2) can be applied. In the present invention, the dechlorination reaction of these chemical decomposition treatment methods is stopped when the total amount of harmful polychlorinated biphenyls is dechlorinated into low-chlorinated polychlorinated biphenyls having a trichlorination or less, and 4 chlorine is added. After it is confirmed that the above-described compound does not exist, it can be subjected to a microbial decomposition method.

【0009】本発明において、化学的分解処理方法によ
って有害PCBが脱塩素化されて生成した3塩素化以下
の低塩素化PCBを分解する微生物としては、3塩素化
以下の低塩素化PCBを好気的に分解できる微生物であ
ればいずれの微生物をも用いることができる。3塩素化
以下の低塩素化PCBを好気的に分解できる微生物とし
ては、ビフェニール分解酵素を持つ一群の微生物、例え
ばアクロモバクター属、シュードモナス属、エアロモナ
ス属、ミクロコッカス属、アシネトバクター属、ビブリ
オ属、アルカリジェネス属、バチルス属、クレブシェラ
属等の細菌があるが、特に好適にはアクロモバクター
属、シュードモナス属、エアロモナス属、アルカリジェ
ネス属の細菌を適用することができる。また、PCB分
解に関与する遺伝子(Appl. Microbiol. Biotechnol. 2
9, 363, 1988) を導入した組換え体を用いることもでき
る。
In the present invention, as a microorganism for decomposing low chlorinated PCBs having a trichlorination or less produced by dechlorinating harmful PCBs by a chemical decomposition treatment method, a low chlorination PCB having a trichlorination or less is preferable. Any microorganism can be used as long as it can be decomposed aerobically. Microorganisms capable of aerobically decomposing low-chlorinated PCBs with a trichlorination or less include a group of microorganisms having a biphenyl degrading enzyme, for example, Achromobacter, Pseudomonas, Aeromonas, Micrococcus, Acinetobacter, Vibrio. , Bacteria of the genus Alcaligenes, genus Bacillus, genus Klebsiella, etc., but particularly preferably bacteria of the genus Achromobacter, genus Pseudomonas, genus Aeromonas, genus Alcaligenes can be applied. In addition, genes involved in PCB degradation (Appl. Microbiol. Biotechnol. 2
9, 363, 1988) can also be used.

【0010】これらの微生物は3塩素化以下の低塩素化
PCBを好気的に分解し、最終生成物として塩化安息香
酸を生成するが、この塩化安息香酸は、通常の有機性排
水処理を行う活性汚泥中に存在する微生物によって容易
に分解することができる。また、これらの微生物はビフ
ェニール分解酵素を持つため、ビフェニールを分解し
て、通常の微生物により容易に分解される安息香酸を生
成する。本発明においては、3塩素化以下の低塩素化P
CBを含有するPCBの化学的分解処理生成物と、栄養
塩類及びPCB分解菌を含有する水溶液とを直接混合
し、好気条件下で反応させ、微生物分解を行なわせるこ
とができる。化学的分解処理生成物が高沸点油中に含有
されている場合には、栄養塩類及びPCB分解菌を含有
する水溶液と混合した濃度として高沸点油濃度が30%
以下、3塩素化以下の低塩素化PCB濃度が500mg
/l以下であることが望ましい。
These microorganisms aerobically decompose low chlorinated PCBs having a trichlorination or less to produce benzoic acid chloride as a final product. The benzoic acid chloride is subjected to ordinary organic wastewater treatment. It can be easily decomposed by microorganisms present in activated sludge. Further, since these microorganisms have a biphenyl degrading enzyme, they decompose biphenyl and produce benzoic acid that is easily degraded by ordinary microorganisms. In the present invention, low chlorinated P of 3 chlorination or less
The CB-containing product of chemical decomposition of PCB is directly mixed with an aqueous solution containing nutrients and PCB-decomposing bacteria and reacted under aerobic conditions to allow microbial decomposition. When the chemical decomposition product is contained in the high boiling point oil, the high boiling point oil concentration is 30% as a concentration mixed with an aqueous solution containing nutrient salts and PCB degrading bacteria.
Below, low chlorinated PCB concentration of less than 3 chlorination is 500 mg
/ L or less is desirable.

【0011】また本発明においては、3塩素化以下の低
塩素化PCBを含有するPCBの化学的分解処理生成物
を分留し、3塩素化以下の低塩素化PCBを沸点150
〜350℃の凝縮液中に濃縮した後、該濃縮液と、栄養
塩類及びPCB分解菌を含有する水溶液とを混合し、好
気条件下で反応させ、微生物分解を行なわせることがで
きる。これにより、化学的分解処理生成物が高沸点油中
に含有されている場合には、微生物分解に供する高沸点
油の容量を大幅に削減することができ、かつ残りの高沸
点油は燃料等に利用することができる。微生物分解の工
程においては、栄養塩類及びPCB分解菌を含有する水
溶液と混合した濃度として、3塩素化以下の低塩素化P
CB濃度が500mg/l以下であることが望ましい。
Further, in the present invention, a chemical decomposition treatment product of PCB containing a low chlorinated PCB having a trichlorination or lower is fractionally distilled, and a low chlorinated PCB having a trichlorination or lower is boiling point 150.
After concentrating in a condensate at ˜350 ° C., the concentrate can be mixed with an aqueous solution containing nutrient salts and PCB-decomposing bacteria and reacted under aerobic conditions to effect microbial decomposition. As a result, when the chemical decomposition product is contained in the high boiling point oil, the capacity of the high boiling point oil used for microbial decomposition can be significantly reduced, and the remaining high boiling point oil is used as fuel or the like. Can be used for. In the step of microbial decomposition, the concentration of a mixture of an aqueous solution containing nutrients and PCB-decomposing bacteria is set to a low chlorination P of 3 chlorination or less.
It is desirable that the CB concentration is 500 mg / l or less.

【0012】以上のように本発明においては、化学的分
解処理方法の脱塩素化反応を、被処理高塩素化PCBの
全量が3塩素化以下の低塩素化PCBに脱塩素化された
時点で止め、生成した3塩素化以下の低塩素化PCBを
微生物分解することにより、有害な高塩素化PCBを効
率よく分解処理することができる。また、化学的分解処
理方法において生成されると考えられるPCBの脱塩素
化化合物であるビフェニールは、それ自体が有害である
が、本発明においてはPCB分解微生物によりビフェニ
ールも分解することができるので、分解処理物の廃棄処
分も容易にできる。
As described above, in the present invention, the dechlorination reaction of the chemical decomposition treatment method is performed at the time when the total amount of the highly chlorinated PCB to be treated is dechlorinated to the low chlorinated PCB having 3 or less chlorinations. By stopping and microbially decomposing the produced low chlorinated PCB having 3 or less chlorination, harmful highly chlorinated PCB can be efficiently decomposed. Further, biphenyl, which is a dechlorinated compound of PCB that is considered to be produced in the chemical decomposition treatment method, is harmful in itself, but in the present invention, biphenyl can be decomposed by the PCB-degrading microorganisms. It is also possible to easily dispose of decomposition products.

【0013】[0013]

【実施例】以下、本発明を参考例及び実施例により具体
的に説明するが、本発明はこれらに限定されるものでは
ない。 参考例1 PCBの化学的分解処理 3塩化物を主成分とするPCBを、濃度50g/lで溶
解した鉱物油150mlに水酸化ナトリウム20g及び
無定形炭素粉末1.5gを加え、窒素雰囲気下330〜
350℃で加熱攪拌し、一定時間ごとに残留PCBの濃
度及び組成比を調べた。結果を表1に示す。高塩素化P
CBは6時間後に0.05mg/lまで分解処理され
た。
EXAMPLES The present invention will be specifically described below with reference to Reference Examples and Examples, but the present invention is not limited to these. Reference Example 1 Chemical Decomposition Treatment of PCB To 150 ml of mineral oil in which PCB containing 3 chloride as a main component was dissolved at a concentration of 50 g / l, 20 g of sodium hydroxide and 1.5 g of amorphous carbon powder were added, and the mixture was placed under a nitrogen atmosphere at 330 ~
The mixture was heated and stirred at 350 ° C., and the concentration and composition ratio of the residual PCB were examined at regular intervals. The results are shown in Table 1. Highly chlorinated P
CB was decomposed to 0.05 mg / l after 6 hours.

【0014】[0014]

【表1】 [Table 1]

【0015】参考例2 PCBの化学的分解処理 4塩化物を主成分とするPCBを濃度50g/lで溶解
した鉱物油150mlに水酸化ナトリウム12g及び無
定形炭素粉末1.5gを加え、窒素雰囲気下320〜3
40℃で加熱攪拌し、一定時間ごとに残留PCBの濃度
及び組成比を調べた。結果を表2に示す。高塩素化PC
Bは6時間後に1.0mg/lまで分解処理されたので
反応を止めた。
Reference Example 2 Chemical Decomposition Treatment of PCB To 12 ml of sodium hydroxide and 1.5 g of amorphous carbon powder was added to 150 ml of mineral oil in which PCB containing tetrachloride as a main component was dissolved at a concentration of 50 g / l, and nitrogen atmosphere was added. Bottom 320-3
The mixture was heated and stirred at 40 ° C., and the concentration and composition ratio of residual PCB were examined at regular intervals. Table 2 shows the results. Highly chlorinated PC
Since B was decomposed to 1.0 mg / l after 6 hours, the reaction was stopped.

【0016】[0016]

【表2】 [Table 2]

【0017】実施例1 低塩素化PCBの微生物分解 3塩化物を主成分とするPCBを濃度50g/lで溶解
した鉱物油150mlに水酸化ナトリウム20g及び無
定形炭素粉末1.5gを加え、参考例1と同様に、窒素
雰囲気下330〜350℃で加熱攪拌し、2時間後に反
応を止めた。この反応処理油中には表1に示すように1
及び2塩素化PCBが約500mg/l含有され、3塩
素化以上の高塩素化PCBは含まれていなかった。該反
応処理油20mlを、土壌から分離したPCB分解能を
持つシュードモナス属の培養液80mlと混合し、28
℃、好気条件下で培養した。24時間後、初期濃度約1
00mg/lのPCBが0.05mg/l以下に分解さ
れていることが確認された。また、微生物処理水中には
ビフェニールも存在しないことが確認された。
Example 1 Microbial Degradation of Low Chlorinated PCB To 150 ml of mineral oil in which PCB containing trichloride as a main component was dissolved at a concentration of 50 g / l, 20 g of sodium hydroxide and 1.5 g of amorphous carbon powder were added, and used as a reference. In the same manner as in Example 1, the mixture was heated and stirred at 330 to 350 ° C under a nitrogen atmosphere, and the reaction was stopped after 2 hours. As shown in Table 1, 1
And dichlorinated PCB were contained at about 500 mg / l, and highly chlorinated PCB having trichlorination or higher was not contained. 20 ml of the reaction-treated oil was mixed with 80 ml of a Pseudomonas culture solution having a PCB decomposing ability separated from soil,
C., and cultivated under aerobic conditions. After 24 hours, the initial concentration is about 1
It was confirmed that PCB of 00 mg / l was decomposed to 0.05 mg / l or less. It was also confirmed that biphenyl was not present in the microbially treated water.

【0018】実施例2 低塩素化PCBの分留濃縮液
の微生物分解 3塩化物を主成分とするPCBを濃度50g/lで溶解
した鉱物油150mlに水酸化ナトリウム20g及び無
定形炭素粉末1.5gを加え、参考例1と同様に、窒素
雰囲気下330〜350℃で加熱攪拌し、2時間後に反
応を止めた。この反応処理油中には表1に示すように1
及び2塩素化PCBが約500mg/l含有され、3塩
素化以上の高塩素化PCBは含まれていなかった。該反
応処理油150mlを220〜230℃で加熱し、蒸発
成分を凝縮したところ、凝縮油3mlが得られた。該凝
縮油中には1及び2塩素化PCBが約25g/l含有さ
れていた。また残りの反応処理油中のPCB濃度は検出
限界以下であった。該凝縮油0.2mlを土壌から分離
したPCB分解能を持つシュードモナス属の培養液10
0mlと混合し、28℃、好気条件下で培養した。24
時間後、初期濃度約50mg/lのPCBが0.05m
g/l以下に分解されていることが確認された。また、
微生物処理水中にはビフェニールも存在しないことが確
認された。
Example 2 Microbial Decomposition of Fractionated Distillate Concentrated Liquid of Low Chlorinated PCB 150 g of mineral oil in which PCB containing chloride as a main component was dissolved at a concentration of 50 g / l, 20 g of sodium hydroxide and amorphous carbon powder 5 g was added, and similarly to Reference Example 1, the mixture was heated and stirred at 330 to 350 ° C. in a nitrogen atmosphere, and the reaction was stopped after 2 hours. As shown in Table 1, 1
And dichlorinated PCB were contained at about 500 mg / l, and highly chlorinated PCB having trichlorination or higher was not contained. When 150 ml of the reaction-treated oil was heated at 220 to 230 ° C. to condense the evaporated components, 3 ml of condensed oil was obtained. The condensed oil contained about 25 g / l of 1- and 2-chlorinated PCBs. The PCB concentration in the remaining reaction-treated oil was below the detection limit. A culture fluid of Pseudomonas having a PCB decomposing ability obtained by separating 0.2 ml of the condensed oil from soil
It was mixed with 0 ml and cultured at 28 ° C. under aerobic conditions. 24
After an hour, PCB with an initial concentration of about 50 mg / l was 0.05 m
It was confirmed that it was decomposed to g / l or less. Also,
It was confirmed that biphenyl was not present in the microbial-treated water.

【0019】実施例3 低塩素化PCBの微生物分解 4塩化物を主成分とするPCBを濃度50g/lで溶解
した鉱物油150mlに水酸化ナトリウム12g及び無
定形炭素粉末1.5gを加え、参考例2と同様に、窒素
雰囲気下320〜340℃で加熱攪拌し、3時間後に反
応を止めた。この反応処理油中には表2に示すように
1、2及び3塩素化PCBが約300mg/l含有さ
れ、4塩素化以上の高塩素化PCBは含まれていなかっ
た。該反応処理油20mlを、土壌から分離したPCB
分解能を持つシュードモナス属の培養液80mlと混合
し、28℃、好気条件下で培養した。24時間後、初期
濃度約60mg/lのPCBが0.05mg/l以下に
分解されていることが確認された。また、微生物処理水
中にはビフェニールも存在しないことが確認された。
Example 3 Microbial Degradation of Low Chlorinated PCB To 150 ml of mineral oil in which PCB containing tetrachloride as a main component was dissolved at a concentration of 50 g / l, 12 g of sodium hydroxide and 1.5 g of amorphous carbon powder were added to be used as a reference. In the same manner as in Example 2, the mixture was heated and stirred under a nitrogen atmosphere at 320 to 340 ° C., and the reaction was stopped after 3 hours. As shown in Table 2, the reaction-treated oil contained about 300 mg / l of 1, 2, and 3 chlorinated PCBs, and did not contain highly chlorinated PCBs of 4 chlorination or higher. PCB separated from soil with 20 ml of the reaction-treated oil
It was mixed with 80 ml of a Pseudomonas culture medium having a resolution and cultured at 28 ° C. under aerobic conditions. After 24 hours, it was confirmed that PCB having an initial concentration of about 60 mg / l was decomposed to 0.05 mg / l or less. It was also confirmed that biphenyl was not present in the microbially treated water.

【0020】[0020]

【発明の効果】以上のように本発明においては、化学的
分解処理方法の脱塩素化反応を、被処理高塩素化PCB
の全量が3塩素化以下の低塩素化PCBに脱塩素化され
た時点で止めることにより化学的分解処理方法に必要な
エネルギーを大幅に削減することができ、また短時間で
高塩素化PCBを微生物によって容易に分解できる構造
及び濃度まで変換できるため、生成した3塩素化以下の
低塩素化PCBを微生物分解することにより、有害な高
塩素化PCBを効率よく分解処理することができる。ま
た、本発明においてはPCB分解微生物によりビフェニ
ールも分解することができ、生成される塩化安息香酸及
び/又は安息香酸は通常の微生物によって容易に分解す
ることができるので、分解処理物の廃棄処分も容易にで
きる。
INDUSTRIAL APPLICABILITY As described above, in the present invention, the dechlorination reaction of the chemical decomposition treatment method is performed by treating the highly chlorinated PCB to be treated.
The energy required for the chemical decomposition treatment method can be significantly reduced by stopping when the total amount of chlorinated PCBs is dechlorinated to a low chlorinated PCB of 3 chlorinated or less, and the highly chlorinated PCB can be reduced in a short time. Since it can be converted to a structure and concentration that can be easily decomposed by microorganisms, harmful highly chlorinated PCBs can be efficiently decomposed by microbial decomposition of the produced trichlorinated or less low-chlorinated PCB. Further, in the present invention, biphenyl can also be decomposed by a PCB-decomposing microorganism, and the produced benzoic acid chloride and / or benzoic acid can be easily decomposed by an ordinary microorganism, so that the decomposed product can also be disposed of. You can easily.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 ポリ塩化ビフェニール類の分解方法にお
いて、被処理ポリ塩化ビフェニール類の化学的分解処理
方法による脱塩素化反応を、被処理高塩素化ポリ塩化ビ
フェニール類の全量を3塩素以下の低塩素化ポリ塩化ビ
フェニール類に脱塩素化した時点で止め、生成した3塩
素化以下の低塩素化ポリ塩化ビフェニール類を微生物分
解することを特徴とするポリ塩化ビフェニール類の分解
方法。
1. In the method for decomposing polychlorinated biphenyls, the dechlorination reaction by the chemical decomposition treatment method of the polychlorinated biphenyls to be treated is carried out by reducing the total amount of the highly chlorinated biphenyls to be treated to a low level of 3 chlorine or less. A method for decomposing polychlorinated biphenyls, which comprises stopping at the time of dechlorination to chlorinated polychlorinated biphenyls and microbially degrading the produced low-chlorinated polychlorinated biphenyls having a trichlorination or less.
【請求項2】 前記微生物分解は、3塩素化以下の低塩
素化ポリ塩化ビフェニール類を含有するポリ塩化ビフェ
ニール類の化学的分解処理生成物と、栄養塩類及びポリ
塩化ビフェニール類分解菌を含有する水溶液とを混合し
て好気条件下で行うことを特徴とする請求項1記載のポ
リ塩化ビフェニール類の分解方法。
2. The microbial degradation comprises a chemical degradation treatment product of polychlorinated biphenyls containing polychlorinated biphenyls having a low chlorination level of 3 or less, and nutrient salts and polychlorinated biphenyls degrading bacteria. The method for decomposing polychlorinated biphenyls according to claim 1, which is carried out under aerobic conditions by mixing with an aqueous solution.
【請求項3】 前記微生物分解は、3塩素化以下の低塩
素化ポリ塩化ビフェニール類を含有するポリ塩化ビフェ
ニール類の化学的分解処理生成物を分留し、沸点150
〜350℃の3塩素化以下の低塩素化ポリ塩化ビフェニ
ール類を濃縮して含有する留分の凝縮液と、栄養塩類及
びポリ塩化ビフェニール類分解菌を含有する水溶液とを
混合して好気条件下で行うことを特徴とする請求項1記
載のポリ塩化ビフェニール類の分解方法。
3. The microbial decomposition is carried out by fractionally distilling a chemical decomposition treatment product of polychlorinated biphenyls containing low chlorinated polychlorinated biphenyls having a trichlorination or less, and boiling point 150.
A condensate of a fraction containing concentrated and low-chlorinated polychlorinated biphenyls having a trichlorination level of up to 350 ° C. and an aqueous solution containing nutrient salts and polychlorinated biphenyl degrading bacteria are mixed under aerobic conditions The method for decomposing polychlorinated biphenyls according to claim 1, which is carried out below.
JP6284004A 1994-10-25 1994-10-25 Method for decomposing polyclorinated biphfenyl Pending JPH08117358A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6284004A JPH08117358A (en) 1994-10-25 1994-10-25 Method for decomposing polyclorinated biphfenyl

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6284004A JPH08117358A (en) 1994-10-25 1994-10-25 Method for decomposing polyclorinated biphfenyl

Publications (1)

Publication Number Publication Date
JPH08117358A true JPH08117358A (en) 1996-05-14

Family

ID=17673054

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6284004A Pending JPH08117358A (en) 1994-10-25 1994-10-25 Method for decomposing polyclorinated biphfenyl

Country Status (1)

Country Link
JP (1) JPH08117358A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272118A (en) * 2005-03-29 2006-10-12 Kurita Water Ind Ltd Method for cleaning substance contaminated by organic chlorine compound
JP2013176408A (en) * 2012-02-28 2013-09-09 Ryu Shinke Toxic substance decomposition treatment method of waste oil, and decomposition treatment plant of the same
JP2013220044A (en) * 2012-04-13 2013-10-28 National Institute For Agro-Environmental Science LESS CHLORINATED PCBs DEGRADING ORGANIC CHLORINE BASED COMPOUND DEGRADING BACTERIUM, ORGANIC CHLORINATED COMPOUND DEGRADING MATERIAL, METHOD FOR PRODUCING THE SAME, AND POLLUTED ENVIRONMENT PURIFICATION SYSTEM

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272118A (en) * 2005-03-29 2006-10-12 Kurita Water Ind Ltd Method for cleaning substance contaminated by organic chlorine compound
JP2013176408A (en) * 2012-02-28 2013-09-09 Ryu Shinke Toxic substance decomposition treatment method of waste oil, and decomposition treatment plant of the same
JP2013220044A (en) * 2012-04-13 2013-10-28 National Institute For Agro-Environmental Science LESS CHLORINATED PCBs DEGRADING ORGANIC CHLORINE BASED COMPOUND DEGRADING BACTERIUM, ORGANIC CHLORINATED COMPOUND DEGRADING MATERIAL, METHOD FOR PRODUCING THE SAME, AND POLLUTED ENVIRONMENT PURIFICATION SYSTEM

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