JP2001047031A - Agent, method, and apparatus for cleaning polluted environment - Google Patents

Agent, method, and apparatus for cleaning polluted environment

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Publication number
JP2001047031A
JP2001047031A JP22736799A JP22736799A JP2001047031A JP 2001047031 A JP2001047031 A JP 2001047031A JP 22736799 A JP22736799 A JP 22736799A JP 22736799 A JP22736799 A JP 22736799A JP 2001047031 A JP2001047031 A JP 2001047031A
Authority
JP
Japan
Prior art keywords
purifying
polluted environment
environment
oxidase
enzyme
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
JP22736799A
Other languages
Japanese (ja)
Inventor
Koichi Okada
公一 岡田
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.)
Kubota Corp
Original Assignee
Kubota 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 Kubota Corp filed Critical Kubota Corp
Priority to JP22736799A priority Critical patent/JP2001047031A/en
Publication of JP2001047031A publication Critical patent/JP2001047031A/en
Pending legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Abstract

PROBLEM TO BE SOLVED: To provide a technology for removing pollutants effectively from a polluted environment. SOLUTION: An enzyme treatment tank 20 has a treatment space which receives wastewater overflowing from an ozone treatment tank 10 and stores it temporarily, In the space, an diffuser 21 which agitates the wastewater in the tank 20 and various sensors for monitoring the quality of the wastewater are provided to function as a enzyme treatment mechanism. For example, when lignin peroxidase is used as an enzyme, on the basis of the information of enzyme sensors 22a included in the sensors 22, the amount of the enzyme to be supplied from a cleaning agent supply part 23a as a conditioning liquid supply part 23 is controlled, and an enzyme concentration in the tank 20 is kept uniformly at 0.5-500 mg/liter.

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、汚染環境浄化剤及
び浄化方法及び浄化装置に関し、たとえばダイオキシン
等の環境ホルモン、毒性物質に代表される汚染物質に汚
染された土壌、水域等を浄化するための技術に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polluting agent, a method and a device for purifying a polluted environment, for example, for purifying soils, water bodies and the like contaminated with pollutants represented by environmental hormones such as dioxin and toxic substances. Related to the technology.

【0002】[0002]

【従来の技術】従来、たとえば土壌が汚染物質に汚染さ
れたような場合には、その土壌を除去し、汚染されてい
ない土を新たに導入してその土壌を改質する方法が採ら
れている。
2. Description of the Related Art Conventionally, for example, when soil is contaminated with contaminants, a method has been adopted in which the soil is removed and non-contaminated soil is newly introduced to modify the soil. I have.

【0003】[0003]

【発明が解決しようとする課題】しかし、このような方
法によっても、前記汚染物質は消滅するわけではなく、
除去された汚染物質含有土壌の処分方法がさらに問題と
なる。このような土壌はコンクリート密封、溶融、ガラ
ス固化、高温焼却、化学抽出処理等を行い、無害化して
再利用することが試みられているが、その無害化処理に
は高価な装置が必要になったり、多大な労力を必要とし
たりするもので、これに変わる処理技術が望まれてい
る。
However, even by such a method, the contaminants do not disappear.
A further problem is how to dispose of the contaminated soil that has been removed. Such soil is sealed, melted, vitrified, incinerated at high temperature, chemically extracted, etc., and detoxification is attempted. However, detoxification requires expensive equipment. Or requires a great deal of labor, and a processing technique that can replace this is desired.

【0004】そこで、微生物によって上述の汚染物質を
分解除去し無害化する技術が開発されつつあるが、分解
速度が遅い、土壌の性状によって分解能力が変化してし
まうなどの問題点があって、まだ十分であるとは言い難
い。
[0004] Therefore, techniques for decomposing and removing the above contaminants by microorganisms to make them harmless have been developed. However, there are problems such as a low decomposition rate and a change in decomposition ability depending on the properties of soil. It is hardly enough.

【0005】これらの汚染物質の無害化技術は、土壌以
外に、排水処理、水系環境においても同様の状況が見ら
れ、改善が求められている。
[0005] These detoxification techniques for pollutants have been found in wastewater treatment and water-based environments in addition to soil, and there is a need for improvement.

【0006】従って、本発明の目的は、上記実状に鑑
み、汚染環境から汚染物質を有効に除去できる技術を提
供することにある。
Accordingly, an object of the present invention is to provide a technique capable of effectively removing contaminants from a contaminated environment in view of the above situation.

【0007】[0007]

【課題を解決するための手段】この目的を達成するため
の本発明の汚染環境浄化剤の特徴構成は、酸化酵素含有
組成物からなる点にあり、前記酸化酵素含有組成物が、
リグニンパーオキシダーゼ、マンガンパーオキシダー
ゼ、ラッカーゼから選ばれる少なくとも一種の酸化酵素
を含有することが好ましく、前記酸化酵素含有組成物が
キレート剤、もしくは、界面活性剤を含むものであれば
尚好ましく、前記酸化酵素含有組成物が、酸化酵素生産
菌を含むものであってもよい。さらに、本発明の汚染環
境浄化方法の特徴手段は、浄化対象部に前記汚染環境浄
化剤を供給する酵素処理工程を含む点にあり、汚染環境
からの抽出流体由来の浄化対象部に含まれる成分を生分
解処理する生物処理工程を含むことが望ましい。さら
に、汚染環境からの抽出流体由来の浄化対象部に含まれ
る成分をヒドロキシルラジカル処理する(ヒドロキシラ
ジカルとは、オゾン処理、オゾン/uv処理、オゾン/
22処理、オゾン/UV/H22処理、その他の手法
で生成する分解性の高い活性物質(・OH)を総称する
ものとする)ヒドロキシラジカル処理工程を含むことが
望ましい。本発明の汚染環境浄化装置の特徴構成は、汚
染環境からの抽出流体由来の浄化対象部に、前記汚染環
境浄化剤を供給する浄化剤供給部を備えた点にあり、汚
染環境からの抽出流体由来の浄化対象部に含まれる成分
を生分解処理する生物処理機構を設けた点にある。汚染
環境からの抽出流体由来の浄化対象部に含まれる成分を
ヒドロキシラジカル処理するヒドロキシラジカル処理機
構を設けてあれば好ましい。
A feature of the polluting environment purifying agent of the present invention for achieving this object resides in that it comprises an oxidase-containing composition.
It is preferable to contain at least one oxidase selected from lignin peroxidase, manganese peroxidase, and laccase, and it is more preferable that the oxidase-containing composition contains a chelating agent or a surfactant. The enzyme-containing composition may contain an oxidase-producing bacterium. Further, the characteristic means of the method for purifying a polluted environment according to the present invention is characterized in that the method includes an enzyme treatment step of supplying the polluted environment purifying agent to the portion to be purified, and the components contained in the portion to be purified derived from a fluid extracted from the polluted environment. It is desirable to include a biological treatment step of performing biodegradation treatment. Furthermore, the components contained in the purification target part derived from the extraction fluid from the polluted environment are subjected to hydroxyl radical treatment (hydroxyl radicals include ozone treatment, ozone / uv treatment, and ozone /
H 2 O 2 treatment, ozone / UV / H 2 O 2 treatment, shall be collectively referred to decompose highly active substances formed by other methods (· OH)) preferably includes a hydroxy radical treatment process. The characteristic configuration of the polluted environment purifying apparatus of the present invention is characterized in that a purifying agent supply unit that supplies the contaminated environmental purifying agent is provided in a purification target portion derived from a fluid extracted from the polluted environment. The present invention is characterized in that a biological treatment mechanism for biodegrading components contained in a target part to be purified is provided. It is preferable to provide a hydroxy radical treatment mechanism for treating the components contained in the purification target portion derived from the extraction fluid from the polluted environment with hydroxy radicals.

【0008】〔作用効果〕つまり、従来の微生物を汚染
環境浄化剤として用いる汚染環境浄化方法においては、
前記微生物が酸化酵素を生産することにより、種々の汚
染物質をその酸化分解するという、無害化機構を持って
いるものと考えられている。そこで、本発明者らは、こ
れら微生物による無害化の速度が遅いのは、微生物自体
の増殖能力に依存して酸化酵素の生産量が十分でない場
合があり、それに伴い、汚染物質の酸化分解が十分に行
われていない場合があるのではないかと考え、鋭意研究
の結果本発明に想到した。つまり、前記汚染環境浄化剤
として酸化酵素含有組成物を用いると、前記微生物が酸
化酵素を生産して汚染物質を酸化分解させるのに比べ
て、直接的に汚染物質の分解除去が行えるから、前記汚
染環境浄化剤の使用量に応じた無害化の能率が達成でき
るのである。
[Effects] In other words, in a conventional method for purifying a polluted environment using a microorganism as a polluted environment purifying agent,
It is considered that the microorganism has a detoxification mechanism in which various contaminants are oxidatively decomposed by producing oxidizing enzymes. Therefore, the present inventors have found that the rate of detoxification by these microorganisms is low, because the production amount of oxidase may not be sufficient depending on the growth ability of the microorganism itself, and accordingly, oxidative degradation of pollutants may occur. We thought that there might be cases where this was not performed sufficiently, and as a result of earnest research, came to the present invention. In other words, when the oxidase-containing composition is used as the contaminated environment purifying agent, the microorganism can directly decompose and remove the contaminant, compared to the case where the microorganism produces the oxidase and oxidatively decomposes the contaminant. The efficiency of detoxification can be achieved in accordance with the amount of the pollutant used.

【0009】ここで、前記酸化酵素含有組成物として、
リグニンパーオキシダーゼ、マンガンパーオキシダー
ゼ、ラッカーゼ、セロビオースデヒドロゲナーゼから選
ばれる少なくとも一種の酸化酵素を含有させておけば、
前記酸化酵素として入手容易でかつ汚染物質の酸化分解
に高い能力を発揮する。尚、ダイオキシンに対する酵素
反応を想定する場合には、脱塩素反応を可能とする一電
子酸化反応を行う酵素またはラジカルを生成する酵素を
適用することが望ましい。またさらに、種々の化学修飾
を行った酸化酵素であっても用いることが出来る。
Here, as the oxidase-containing composition,
Lignin peroxidase, manganese peroxidase, laccase, if it contains at least one oxidase selected from cellobiose dehydrogenase,
It is easily available as the oxidizing enzyme and exhibits high ability in oxidative decomposition of pollutants. When an enzymatic reaction to dioxin is assumed, it is desirable to use an enzyme that performs a one-electron oxidation reaction that enables a dechlorination reaction or an enzyme that generates a radical. Furthermore, oxidases that have been subjected to various chemical modifications can also be used.

【0010】ところで、前記汚染物質としては、水溶性
のものの他、水不溶性の場合もあるが、前記酸化酵素の
働く環境は、水に溶解した状態であることが有効であ
り、また、他の重金属成分等の影響を受けない状態で作
用させることが有効と考えられる。そこで、前記酸化酵
素含有組成物がキレート剤、もしくは、界面活性剤を含
むものであれば、水に不溶な汚染物質であっても可溶化
し、重金属等の影響を受けにくい状態で酸化酵素を働か
せられるので有利である。尚、キレート剤は、主に重金
属に配位して前記酸化酵素に対して悪影響を与えるのを
防止する機能が高く、前記界面活性剤は、主に不溶性の
汚染物質であっても溶解条件下で作用させられる点で有
用であるものと考えられる。
The contaminants may be water-soluble or water-insoluble, but it is effective that the environment in which the oxidase works is dissolved in water. It is considered effective to operate in a state not affected by heavy metal components and the like. Therefore, if the oxidase-containing composition contains a chelating agent or a surfactant, the oxidase is solubilized even in the case of water-insoluble contaminants, and the oxidase is not easily affected by heavy metals and the like. It is advantageous because it can work. The chelating agent has a high function of mainly coordinating with heavy metals to prevent the oxidizing enzyme from being adversely affected, and the surfactant is used under conditions of dissolution even if it is mainly an insoluble contaminant. It is considered useful in that it can be acted on.

【0011】また、本発明の汚染環境浄化剤によると、
従来の微生物を用いる場合に比べて、即効性を発揮させ
られる点で有用であるものと考えられるが、一旦汚染環
境浄化剤を作用させた環境では、前記酸化酵素がすでに
消耗しており、さらに汚染物質による汚染を受けた場合
には、汚染物質の無害化作用を得にくい場合が想定され
る。しかし、前記酸化酵素含有組成物が、酸化酵素生産
菌を含むものであれば、初期的に酸化酵素の高い作用を
得ながらも、その環境下に含有される前記酸化酵素生産
菌が、酸化酵素を継続的に供給し続ける状況が想定され
るため、長期的な視野に立っての環境浄化を行う上で有
用となる。尚、このような微生物としては、白色腐朽菌
や、その遺伝子組換体等が用いられ、その他酸化酵素を
生産する生産菌であれば、有用に用いられる。
Further, according to the polluting environment purifying agent of the present invention,
Compared to the case of using conventional microorganisms, it is considered to be useful in that it can exhibit immediate effect, but in an environment where a contaminated environmental purification agent has been once acted, the oxidase has already been consumed, and When contaminated by contaminants, it is assumed that it is difficult to obtain the detoxifying effect of the contaminants. However, if the oxidase-containing composition contains an oxidase-producing bacterium, the oxidase-producing bacterium contained in the environment, while obtaining a high action of the oxidase at the initial stage, is oxidase It is assumed that a situation where the supply of wastewater is continuously provided is useful in carrying out environmental purification from a long-term perspective. As such a microorganism, a white rot fungus, a recombinant thereof, or the like is used, and any other microorganism that produces an oxidase is usefully used.

【0012】尚、前記酸化酵素含有組成物には、クレ
ー、ベントナイト、ふすま等の増量剤を添加してもよい
し、土壌、灰分、種々調整剤、緩衝液、その他、特に、
微生物を併用するような場合には、グルコース、セルロ
ース、リグニンなどの栄養源や、培養基材を添加してあ
ることが望ましい。また、このような組成物は、ポリア
ルギン酸等を用いてカプセル化した製剤や、グラニコー
ル、粉末、液体、フロアブル製剤として用いてもよい。
The oxidase-containing composition may contain an extender such as clay, bentonite, bran, etc., soil, ash, various regulators, buffers, etc.
When a microorganism is used in combination, a nutrient such as glucose, cellulose, or lignin, or a culture substrate is preferably added. Further, such a composition may be used as a preparation encapsulated with polyalginic acid or the like, or as granicol, powder, liquid, or flowable preparation.

【0013】さらに、本発明の汚染環境浄化方法によれ
ば、浄化対象部に前記汚染環境浄化剤を供給する酵素処
理工程を含むから、汚染された土壌や水系に含まれる汚
染物質に対して前記酸化酵素が働き、その汚染物質を無
害化することができる。
Further, according to the method for purifying a polluted environment of the present invention, an enzymatic treatment step of supplying the polluted environment purifying agent to a portion to be purified is included. The oxidizing enzyme works to make the pollutants harmless.

【0014】また、汚染環境からの抽出流体由来の浄化
対象部に含まれる成分を生分解処理する生物処理工程に
供することにより、酸化酵素の働きによって無害化され
た汚染物質を、さらに、低分子の化合物に変換し、より
環境浄化に寄与させる、あるいは、汚染物質をある程度
分解処理して、酸化酵素の働きやすい物質に変換してか
ら無害化処理をはかるなどの効率よくより高度な環境浄
化をはかることが出来る。さらに、汚染環境からの抽出
流体由来の浄化対象部に含まれる成分をヒドロキシルラ
ジカル分解処理するヒドロキシルラジカル処理工程に供
すれば、前記ヒドロキシルラジカル分解処理によっても
汚染物質、あるいは、汚染物質の酵素分解生成物を分解
して低分子化できるので、生物処理工程同様、効率よく
高度な浄化処理をはかることが出来る。尚、前記生物処
理工程は、特に、無害化された汚染物質を、さらに、低
分子の化合物に変換する場合に高い能力を発揮する場合
が多いので、前記酵素処理工程の後に行うことが好まし
く、逆にヒドロキシルラジカル処理工程は、極めて高い
酸化力を持ち、汚染物質をある程度分解処理して、酸化
酵素の働きやすい物質に変換するのに有用である場合が
多いから、前記酵素処理工程の前に行うことが好まし
い。
Further, by subjecting the components contained in the purification target portion derived from the extraction fluid from the polluted environment to a biological treatment process for biodegrading, the pollutants detoxified by the action of the oxidase are further reduced to low molecular weight. To further contribute to environmental purification, or to perform more advanced environmental purification, such as by decomposing pollutants to some extent and converting it to a substance that can easily work with oxidase, and then detoxifying it. You can measure. Furthermore, if the components contained in the purification target portion derived from the extraction fluid from the polluted environment are subjected to a hydroxyl radical treatment step of subjecting the components to a hydroxyl radical decomposition treatment, the hydroxyl radical decomposition treatment also causes the contaminant or the enzymatic decomposition generation of the contaminant. Since the substance can be decomposed to reduce the molecular weight, an advanced purification treatment can be efficiently performed as in the biological treatment step. Incidentally, the biological treatment step, particularly, detoxified contaminants, further, often exhibit a high ability when converting to a low-molecular compound, it is preferable to perform after the enzyme treatment step, Conversely, the hydroxyl radical treatment step has an extremely high oxidizing power, and is often useful for decomposing contaminants to some extent and converting it to a substance that easily acts on an oxidase. It is preferred to do so.

【0015】本発明の汚染環境浄化装置としては、汚染
環境からの抽出流体由来の浄化対象部に、前記汚染環境
浄化剤を供給する浄化剤供給部を備えていれば、前記汚
染環境浄化方法を行う際の酵素処理工程を行え、流体を
用いた連続的な汚染環境浄化が可能となる。また同様
に、汚染環境からの抽出流体由来の浄化対象部に含まれ
る成分を生分解処理する生物処理機構、ヒドロキシルラ
ジカル分解処理するヒドロキシルラジカル処理機構を設
けてあれば先の生物処理工程やヒドロキシルラジカル処
理工程についても流体を用いた連続的な汚染環境浄化が
可能となるため、処理プラントとして効率よく働かせる
ことが可能となる。
In the polluted environment purifying apparatus of the present invention, if a purifying agent supply section for supplying the contaminated environmental purifying agent is provided in a purifying target derived from a fluid extracted from the polluted environment, the contaminated environment purifying method is performed. An enzymatic treatment step can be performed at the time of performing, and continuous purification of the polluted environment using a fluid becomes possible. Similarly, if a biological treatment mechanism for biodegrading components contained in the purification target part derived from the extraction fluid from the polluted environment and a hydroxyl radical treatment mechanism for hydroxyl radical decomposition treatment are provided, Also in the treatment process, it is possible to continuously purify the polluted environment using the fluid, so that it is possible to work efficiently as a treatment plant.

【0016】[0016]

【発明の実施の形態】以下に本発明の実施の形態を図面
に基づいて説明する。本発明の汚染環境浄化装置として
の排水処理装置は、図1に示すように、上流側からオゾ
ン処理槽10、酵素処理槽20、微生物処理槽30、固
液分離槽40を備えてなり、汚染環境から雨水等によっ
て抽出される汚染物質を無害化して周辺環境に放流可能
な構成としてある。
Embodiments of the present invention will be described below with reference to the drawings. As shown in FIG. 1, the wastewater treatment apparatus as the polluted environment purification apparatus of the present invention includes an ozone treatment tank 10, an enzyme treatment tank 20, a microorganism treatment tank 30, and a solid-liquid separation tank 40 from the upstream side. It is configured so that pollutants extracted from the environment by rainwater or the like can be rendered harmless and released to the surrounding environment.

【0017】前記オゾン処理槽10は、処理対象排水を
受け入れる流入口11を設けるとともに、前記処理対象
排水を一時貯留する処理空間を備え、前記処理空間に
は、オゾンばっ気装置12および槽内の処理対象排水を
攪拌する散気装置13を備えるとともに、オゾン濃度を
モニターするオゾンセンサー14内蔵してヒドロキシラ
ジカル処理機構として働く。ここで、前記オゾンばっ気
装置12によるオゾンばっ気量は、前記オゾンセンサー
14の情報に基づきフィードバック制御され、前記オゾ
ン処理槽10内のオゾン濃度を0.01〜5mg/m3
で均一に維持可能に構成してある。尚、オゾン処理槽1
0内のオゾン濃度は、0.01mg/m3以上に設定し
てあれば、効率のよ いオゾン処理が行える。
The ozone treatment tank 10 is provided with an inflow port 11 for receiving the waste water to be treated and has a treatment space for temporarily storing the waste water to be treated. The treatment space includes an ozone aeration device 12 and the inside of the tank. It has an air diffuser 13 for stirring the waste water to be treated, and has a built-in ozone sensor 14 for monitoring the ozone concentration to function as a hydroxy radical treatment mechanism. Here, the amount of ozone aerated by the ozone aeration device 12 is feedback-controlled based on the information of the ozone sensor 14, and the ozone concentration in the ozone treatment tank 10 is adjusted to 0.01 to 5 mg / m 3.
And can be maintained uniformly. In addition, the ozone treatment tank 1
If the ozone concentration in 0 is set to 0.01 mg / m 3 or more, efficient ozone treatment can be performed.

【0018】前記酵素処理槽20は、前記オゾン処理槽
10からの処理対象排水をオーバーフローで受けて一時
貯留する処理空間を備え、前記処理空間には、酵素処理
槽20内の処理対象排水を攪拌する散気装置21を備え
るとともに、その処理対象排水の水質をモニターする各
種センサー22を内蔵し、酵素処理機構として働く。ま
た、前記処理空間に、酸、塩基、金属塩、酸化酵素等の
液性調整剤を供給し、前記処理対象排水の液性を調整す
る調整液供給部23を設けてある。ここで、前記調整液
供給部23からの液性調整剤の供給は、前記各種センサ
ー22からの情報に基づきフィードバック制御され、た
とえば、前記酵素としてリグニンパーオキシダーゼを用
いた場合には、前記各種センサ酵素センサ22に含まれ
る酵素センサ22aの情報に基づき、前記調整液供給部
23としての浄化剤供給部23aからの酵素供給量を調
整し、前記酵素処理槽20内の酵素濃度を0.5〜50
0mg/リットルで均一に維持可能に構成してある。
尚、酸化酵素としてリグニンパーオキシダーゼ、マンガ
ンパーオキシダーゼ、ラッカーゼ等を用いる場合には、
前記酵素濃度は0.5mg/リットル以上あれば、連続
的に安定な処理が行える。また、他の液性調整剤として
は、過酸化水素、バリルアルコール、界面活性剤等が挙
げられ、それぞれの液性調整剤を前記酵素処理槽に投入
する調整液供給部23と、それに対応する各種センサー
を設けてあるものとし、pH、温度等についても同様の
フィードバック制御を行う。たとえば、前記過酸化水素
は、酵素の汚染物質分解能力を高めるものとして加えら
れ、30μM〜5mMに調整され、バリルアルコール濃
度は、5mM以下に調整する、さらに、界面活性剤とし
てTween80を使う場合には、50%濃度のものを
0.01〜0.1%添加する。また、重金属等の影響に
よる酵素阻害が予想される場合にはEDTA、EGTA
等のキレート剤を0.1〜50mg/リットル添加す
る。また、前記酵素処理槽20には、エアリフトポンプ
24を備え、沈殿汚泥や汚染物質の酵素処理に伴って発
生する不溶性生成物等を前記オゾン処理槽に返送して、
さらに分解処理を行える構成としてある。
The enzyme treatment tank 20 is provided with a treatment space for receiving the wastewater to be treated from the ozone treatment tank 10 by overflow and temporarily storing the wastewater, and agitating the wastewater to be treated in the enzyme treatment tank 20 in the treatment space. In addition to an air diffuser 21, various sensors 22 for monitoring the water quality of the wastewater to be treated are built in, and function as an enzyme treatment mechanism. Further, an adjustment liquid supply unit 23 for supplying a liquid property adjusting agent such as an acid, a base, a metal salt, and an oxidase to the processing space to adjust the liquid property of the wastewater to be processed is provided. Here, the supply of the liquid property adjusting agent from the adjusting liquid supply unit 23 is feedback-controlled based on information from the various sensors 22. For example, when lignin peroxidase is used as the enzyme, Based on the information of the enzyme sensor 22a included in the enzyme sensor 22, the enzyme supply amount from the purifying agent supply unit 23a as the adjustment liquid supply unit 23 is adjusted, and the enzyme concentration in the enzyme treatment tank 20 is set to 0.5 to 50
It is configured so that it can be maintained uniformly at 0 mg / liter.
In addition, when using lignin peroxidase, manganese peroxidase, laccase, etc. as the oxidase,
If the enzyme concentration is 0.5 mg / liter or more, stable processing can be performed continuously. Further, examples of the other liquid property adjusting agents include hydrogen peroxide, valyl alcohol, a surfactant, and the like, and a liquid adjusting section 23 for supplying each liquid property adjusting agent to the enzyme treatment tank, It is assumed that various sensors are provided, and similar feedback control is performed for pH, temperature, and the like. For example, the hydrogen peroxide is added to enhance the ability of the enzyme to decompose contaminants, and is adjusted to 30 μM to 5 mM. The valyl alcohol concentration is adjusted to 5 mM or less. Is added at a concentration of 50% from 0.01 to 0.1%. When enzyme inhibition due to the influence of heavy metals or the like is expected, EDTA, EGTA
0.1 to 50 mg / liter. Further, the enzyme treatment tank 20 is provided with an air lift pump 24, and returns insoluble products and the like generated due to the enzyme treatment of settling sludge and contaminants to the ozone treatment tank.
Further, the configuration is such that a decomposition process can be performed.

【0019】前記微生物処理槽30は、活性汚泥を収容
し、オーバーフロー流入する処理対象排水を一時貯留し
て微生物により好気分解する処理空間を備え、生物処理
機構として働く。また、前記処理空間には、散気装置3
1を設け、前記活性汚泥に給気、攪拌することにより、
活性汚泥がBODを消化する。これにより汚染物質を含
んだ処理対象排水は、ほぼ完全に無害化され、バイオマ
スとして固定される。尚、前記微生物処理槽内の溶存酸
素量等は、センサー32により管理され、ほぼ一定に維
持すべく前記散気装置31による散気量等が制御され
る。
The microorganism treatment tank 30 has a treatment space for accommodating activated sludge, temporarily storing wastewater to be treated which overflows, and aerobically decomposing it by microorganisms, and functions as a biological treatment mechanism. In addition, an air diffuser 3 is provided in the processing space.
1 is provided, and the activated sludge is supplied and stirred,
Activated sludge digests BOD. As a result, the wastewater to be treated containing the pollutants is almost completely rendered harmless and fixed as biomass. The amount of dissolved oxygen and the like in the microorganism treatment tank is controlled by a sensor 32, and the amount of air diffused by the air diffuser 31 is controlled so as to be kept substantially constant.

【0020】前記固液分離槽40は、前記微生物処理槽
30からの処理対象排水を受けて一時貯留する処理空間
内に、多孔性ポリプロピレン製多孔質膜を有する平膜4
1aをフレーム41bに固定し、前記処理対象排水を吸
引ポンプ41cにより吸引濾過する構成としてある膜分
離装置41を内装するとともに、前記膜分離装置41の
前記平膜41aに給気して、処理対象排水を固液分離し
たときに、濾別される固形成分が、その平膜に付着して
定着するのを防止する散気装置42を設けて構成してあ
る。また、前記処理空間内には、エアリフトポンプ43
を備え、沈殿汚泥等の固形成分等を前記微生物処理槽に
に返送して、さらに分解処理を行える構成としてある。
The solid-liquid separation tank 40 is provided with a flat membrane 4 having a porous polypropylene porous membrane in a treatment space for receiving and temporarily storing wastewater to be treated from the microorganism treatment tank 30.
1a is fixed to a frame 41b, and a membrane separation device 41 configured to suction-filter the waste water to be treated by a suction pump 41c is provided therein, and the flat membrane 41a of the membrane separation device 41 is supplied with air to be treated. An air diffuser 42 is provided to prevent solid components to be separated by filtration when the waste water is subjected to solid-liquid separation. Further, an air lift pump 43 is provided in the processing space.
And a solid component such as settled sludge is returned to the microorganism treatment tank to be further decomposed.

【0021】このような構成の汚染環境浄化装置に、汚
染環境からの抽出雨水を処理対象排水として供給する
と、前記オゾン処理槽10により前記汚染環境に含まれ
ていた汚染物質をヒドロキシラジカル処理するヒドロキ
シラジカル処理工程が行える。次に、前記酵素処理槽2
0においてそのオゾン処理された処理対象排水を酵素処
理により無害化する酵素処理工程が行え、さらに、微生
物処理槽30において生物処理工程が行える。さらに、
前記固液分離槽において固液分離工程が行うと、汚染環
境浄化装置によって汚染環境に含まれていた汚染物質が
無害化されて、環境浄化が達成される。
When the rainwater extracted from the polluted environment is supplied to the polluted environment purifying apparatus as the wastewater to be treated, the ozone treatment tank 10 performs a hydroxyl radical treatment of the pollutants contained in the polluted environment. A radical treatment step can be performed. Next, the enzyme treatment tank 2
At 0, an enzymatic treatment step of detoxifying the ozone-treated wastewater by enzymatic treatment can be performed, and a biological treatment step can be performed in the microorganism treatment tank 30. further,
When the solid-liquid separation step is performed in the solid-liquid separation tank, the pollutants contained in the polluted environment are detoxified by the polluted environment purification device, and the environment is purified.

【0022】〔別実施形態〕以下に別実施形態を説明す
る。先の実施の形態では、オゾン処理槽10、酵素処理
槽20、微生物処理槽30を個別に設け、それぞれの槽
で各無害化工程を順次行う構成としたが、 (1)ヒドロキシルラジカル処理工程と酵素処理工程を
同時に行う (2)酵素処理工程と生物処理工程とを同時に行う (3)ヒドロキシルラジカル処理工程と酵素処理工程と
生物処理工程とを同時に行う こともできる。また、各工程の順序を入れ替えることも
可能である。
[Another Embodiment] Another embodiment will be described below. In the above embodiment, the ozone treatment tank 10, the enzyme treatment tank 20, and the microorganism treatment tank 30 are separately provided, and the respective detoxification steps are sequentially performed in the respective tanks. Simultaneous enzyme treatment step (2) Simultaneous enzyme treatment step and biological treatment step (3) Simultaneous treatment of hydroxyl radical treatment step, enzyme treatment step and biological treatment step. Further, the order of each step can be changed.

【0023】この場合、両機能を発揮させるべく、適宜
処理対象排水の液性をコントロールすればよい。また、
各オゾン処理槽10、酵素処理槽20、微生物処理槽3
0は、各一槽づつである必要はなく、それぞれ複数槽で
処理することも可能である。たとえば、生物処理工程に
ついて言えば、嫌気処理槽と、好気処理槽を並設して行
ってもよい。
In this case, the liquid properties of the wastewater to be treated may be appropriately controlled in order to exert both functions. Also,
Each ozone treatment tank 10, enzyme treatment tank 20, microorganism treatment tank 3
0 does not have to be one for each tank, and it is also possible to treat in a plurality of tanks. For example, regarding the biological treatment step, an anaerobic treatment tank and an aerobic treatment tank may be provided side by side.

【0024】尚、前記(2)の場合、用いる微生物とし
ては酸化酵素生産菌あるいは、遺伝子改変等に基づき酸
化酵素を生産可能にしたロドコッカス、シュードモナ
ス、バークホール等を用いることが出来る。
In the case of the above (2), the microorganism to be used may be an oxidase-producing bacterium, or Rhodococcus, Pseudomonas, Barkhole or the like which can produce an oxidase based on genetic modification or the like.

【0025】また、先の実施の形態では、汚染環境とし
て水系のものを例示したが、汚染環境浄化剤を直接土壌
に散布することによっても同様の効果を得ることが出来
る。つまり、 (a) リグニンパーオキシダーゼをクレー、ベントナ
イト等の増量剤とともに製剤化した汚染環境浄化剤 (b) (a)のものに、さらに、キレート剤、界面活
性剤、微量金属、緩衝液の少なくとも一種を添加した汚
染環境浄化剤 (c) (a)、(b)のものに、さらに、酸化酵素生
産菌を添加した汚染環境浄化剤 (d) (c)のものに、さらに、グルコース等の酵素
生産菌の培養基材を添加した汚染環境浄化剤 (e) (a)〜(d)のものを、ポリアルギン酸等に
よりカプセル製剤化した汚染環境浄化剤 のような形態で、粉末、液状にて用いることが出来、直
接土壌に散布、鋤込みすることで効果を発揮させること
が出来る。たとえば、(c)のような場合に酸化酵素生
産菌として白色腐朽菌を用いる場合には、菌糸を数mm
のレベルまで粉砕して用いれば作業性に優れ、好まし
い。
In the above embodiment, a water-based contaminated environment is exemplified. However, a similar effect can be obtained by directly spraying a contaminated environment purifying agent on soil. That is, (a) a contaminated environmental purification agent prepared by formulating lignin peroxidase together with a bulking agent such as clay and bentonite; and (b) at least a chelating agent, a surfactant, a trace metal, and a buffer solution. A contaminated environmental purifying agent to which (c) (a) and (b) are added, and a contaminated environmental purifying agent (d) and (c) to which an oxidase-producing bacterium is added. Contaminated environment purifying agent to which a culture substrate of enzyme-producing bacteria is added (e) Powders and liquids in the form of a contaminated environmental purifying agent obtained by encapsulating the product of (a) to (d) with polyalginic acid or the like It can be used by spraying and plowing directly on the soil to exert its effect. For example, when a white rot fungus is used as an oxidase-producing bacterium in the case of (c), the hypha is several mm thick.
It is preferable to use the material after pulverizing it to the level of excellent workability.

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

【図1】本発明の汚染環境浄化装置の概略図FIG. 1 is a schematic diagram of a polluted environment purification apparatus of the present invention.

【符号の説明】[Explanation of symbols]

10 オゾン処理槽 11 流入口 12 オゾンばっ気装置 13 散気装置 14 オゾンセンサー 20 酵素処理槽 21 散気装置 22 センサー 23 調整液供給部 22a 酵素センサ 23a 浄化剤供給部 24 エアリフトポンプ 30 微生物処理槽 31 散気装置 40 固液分離槽 41a 平膜 41b フレーム 41c 吸引ポンプ 41 膜分離装置 42 散気装置 43 エアリフトポンプ DESCRIPTION OF SYMBOLS 10 Ozone treatment tank 11 Inflow port 12 Ozone aeration apparatus 13 Air diffuser 14 Ozone sensor 20 Enzyme treatment tank 21 Air diffuser 22 Sensor 23 Adjustment liquid supply part 22a Enzyme sensor 23a Purifier supply part 24 Air lift pump 30 Microorganism treatment tank 31 Air diffuser 40 Solid-liquid separation tank 41a Flat membrane 41b Frame 41c Suction pump 41 Membrane separator 42 Air diffuser 43 Air lift pump

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C12N 1/00 C12N 9/02 4D040 9/02 B09B 3/00 E Fターム(参考) 2E191 BA12 BB01 BD20 4B050 CC07 DD02 LL10 4B065 AA01X AC14 CA28 CA54 4D004 AA41 AB07 CA19 CA20 CA36 CC07 CC08 CC11 4D028 AC03 BC12 BC26 BE01 CA09 CD01 CD04 4D040 DD01 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C12N 1/00 C12N 9/02 4D040 9/02 B09B 3/00 EFterm (Reference) 2E191 BA12 BB01 BD20 4B050 CC07 DD02 LL10 4B065 AA01X AC14 CA28 CA54 4D004 AA41 AB07 CA19 CA20 CA36 CC07 CC08 CC11 4D028 AC03 BC12 BC26 BE01 CA09 CD01 CD04 4D040 DD01

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 酸化酵素含有組成物からなる汚染環境浄
化剤。
1. A polluting environment purifying agent comprising an oxidase-containing composition.
【請求項2】 前記酸化酵素含有組成物が、リグニンパ
ーオキシダーゼ、マンガンパーオキシダーゼ、ラッカー
ゼ、セルビオースデハイドロゲナーゼから選ばれる少な
くとも一種の酸化酵素を含有するものである請求項1に
記載の汚染環境浄化剤。
2. The contamination according to claim 1, wherein the oxidase-containing composition contains at least one oxidase selected from lignin peroxidase, manganese peroxidase, laccase, and cellobiose dehydrogenase. Environmental purifier.
【請求項3】 前記酸化酵素含有組成物がキレート剤、
もしくは、界面活性剤を含むものである請求項1〜2の
いずれか1項に記載の汚染環境浄化剤。
3. The composition according to claim 1, wherein the oxidase-containing composition is a chelating agent,
Alternatively, the contaminated environment purifying agent according to any one of claims 1 to 2, which contains a surfactant.
【請求項4】 前記酸化酵素含有組成物が、酸化酵素生
産菌を含むものである請求項〜のいずれか1項に記載の
汚染環境浄化剤。
4. The polluting environment purifying agent according to claim 1, wherein the oxidase-containing composition contains an oxidase-producing bacterium.
【請求項5】 浄化対象部に請求項1から4に記載の汚
染環境浄化剤を供給する酵素処理工程を含む汚染環境浄
化方法。
5. A method for purifying a polluted environment, comprising an enzyme treatment step of supplying the polluted environment purifying agent according to claim 1 to a portion to be purified.
【請求項6】 汚染環境からの抽出流体由来の浄化対象
部に含まれる成分を生分解処理する生物処理工程を含む
請求項5に記載の汚染環境浄化方法。
6. The method for purifying a polluted environment according to claim 5, comprising a biological treatment step of biodegrading components contained in a purification target portion derived from a fluid extracted from the polluted environment.
【請求項7】 汚染環境からの抽出流体由来の浄化対象
部に含まれる成分をヒドロキシラジカル分解処理するヒ
ドロキシラジカル処理工程を含む請求項5〜6のいずれ
か1項に記載の汚染環境浄化方法。
7. The method for purifying a polluted environment according to claim 5, further comprising a hydroxy radical treatment step of subjecting a component contained in a purification target portion derived from an extraction fluid from the polluted environment to a hydroxy radical decomposition treatment.
【請求項8】 汚染環境からの抽出流体由来の浄化対象
部に請求項1から4に記載の汚染環境浄化剤を供給する
浄化剤供給部を備えた酵素処理機構を設けた汚染環境浄
化装置。
8. A polluted environment purifying apparatus provided with an enzyme treatment mechanism provided with a purifying agent supply unit for supplying the polluted environmental purifying agent according to claim 1 to a purifying target portion derived from a fluid extracted from the polluted environment.
【請求項9】 汚染環境からの抽出流体由来の浄化対象
部に含まれる成分を生分解処理する生物処理機構を設け
た汚染環境浄化装置。
9. A polluted environment purification apparatus provided with a biological treatment mechanism for biodegrading components contained in a purification target portion derived from a fluid extracted from a polluted environment.
【請求項10】 汚染環境からの抽出流体由来の浄化対
象部に含まれる成分をヒドロキシラジカル分解処理する
ヒドロキシラジカル処理機構を設けた汚染環境浄化装
置。
10. A contaminated environment purifying apparatus provided with a hydroxy radical treatment mechanism for subjecting a component contained in a purifying target derived from an extraction fluid from a contaminated environment to a hydroxy radical decomposition treatment.
JP22736799A 1999-08-11 1999-08-11 Agent, method, and apparatus for cleaning polluted environment Pending JP2001047031A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22736799A JP2001047031A (en) 1999-08-11 1999-08-11 Agent, method, and apparatus for cleaning polluted environment

Publications (1)

Publication Number Publication Date
JP2001047031A true JP2001047031A (en) 2001-02-20

Family

ID=16859702

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007289956A (en) * 2001-06-29 2007-11-08 Daiwa Kasei Kk Method for decomposing fluorescent brightening agent
ES2425995A1 (en) * 2013-07-26 2013-10-18 Universidade De Santiago De Compostela Procedure of elimination of hydrophobic organic pollutants from contaminated soil using a vegetable oil (Machine-translation by Google Translate, not legally binding)
JP2015009203A (en) * 2013-06-28 2015-01-19 株式会社明電舎 Wastewater treatment method and apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007289956A (en) * 2001-06-29 2007-11-08 Daiwa Kasei Kk Method for decomposing fluorescent brightening agent
JP4516095B2 (en) * 2001-06-29 2010-08-04 大和化成株式会社 Method for decomposing optical brightener
JP2015009203A (en) * 2013-06-28 2015-01-19 株式会社明電舎 Wastewater treatment method and apparatus
ES2425995A1 (en) * 2013-07-26 2013-10-18 Universidade De Santiago De Compostela Procedure of elimination of hydrophobic organic pollutants from contaminated soil using a vegetable oil (Machine-translation by Google Translate, not legally binding)

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