JP2011131199A - Wastewater treatment method and apparatus - Google Patents

Wastewater treatment method and apparatus Download PDF

Info

Publication number
JP2011131199A
JP2011131199A JP2009295740A JP2009295740A JP2011131199A JP 2011131199 A JP2011131199 A JP 2011131199A JP 2009295740 A JP2009295740 A JP 2009295740A JP 2009295740 A JP2009295740 A JP 2009295740A JP 2011131199 A JP2011131199 A JP 2011131199A
Authority
JP
Japan
Prior art keywords
wastewater
membrane
dye
treatment
colored
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
JP2009295740A
Other languages
Japanese (ja)
Inventor
Akira Ikeda
明 池田
Koichi Nozaki
功一 野崎
Takahisa Kanda
鷹久 神田
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.)
Mimaki Engineering Co Ltd
Original Assignee
Mimaki Engineering Co Ltd
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 Mimaki Engineering Co Ltd filed Critical Mimaki Engineering Co Ltd
Priority to JP2009295740A priority Critical patent/JP2011131199A/en
Publication of JP2011131199A publication Critical patent/JP2011131199A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a means which enables cost reduction and can decolorize colored wastewater under a mild condition without exerting a bad influence on the human body and the environment. <P>SOLUTION: In a wastewater treatment method, dyes in the colored wastewater are reacted with enzymes extracted from a waste mushroom bed after cultivation of basidiomycetes to decompose the dyes, thereby decolorizing the colored wastewater. <P>COPYRIGHT: (C)2011,JPO&amp;INPIT

Description

本発明は、例えば染料工場等から排出される着色排水中の染料を脱色する排水処理方法、および排水処理装置に関する。   The present invention relates to a wastewater treatment method and a wastewater treatment apparatus for decolorizing dyes in colored wastewater discharged from, for example, a dye factory.

近年、環境問題に関連して染色工場などから多量に排出される染料排水(着色排水)が問題となっており、地方自治体等によっても染料排水に対する規制が強化されている。染料は低濃度でも着色性が高く脱色処理が困難であるため、従来から染料排水は専門処理業者によって引き取られて処理委託され、産業廃棄物として処分されるか、あるいは河川等に放流できるまで脱色・浄化等の処理がなされている。このような場合、廃棄処分する場所や排水処理設備のある場所が限定されてしまう上に、上記のような規制強化等に伴って染料排水の処理コストが上昇傾向にあるため、最近では染料を分解する方法として、染料をオゾンと接触させることにより分解する方法(例えば、特許文献1を参照)や微生物を用いた処理方法(例えば、特許文献2を参照)などが注目を集めている。   In recent years, dye wastewater (colored wastewater) discharged in large quantities from dyeing factories or the like has become a problem in relation to environmental problems, and regulations on dye wastewater have been strengthened by local governments and the like. Dye is highly colored and difficult to decolorize even at low concentrations. Conventionally, dye wastewater is taken up by a specialist processor and outsourced to be disposed of as industrial waste or discharged into rivers, etc.・ Purification and other treatments have been made. In such a case, the place where the waste is disposed and the place where the wastewater treatment facility is located are limited, and the treatment cost of the dye wastewater tends to increase due to the above-mentioned tightening regulations. As a method of decomposing, a method of decomposing by contacting a dye with ozone (for example, see Patent Document 1), a treatment method using a microorganism (for example, see Patent Document 2), and the like are attracting attention.

特開平9−239383号公報JP-A-9-239383 特開平2000−287674号公報Japanese Patent Laid-Open No. 2000-287664

しかしながら、オゾンによる排水処理の場合には、発癌性化合物の生成に関与するため人体への影響が指摘されている。一方、微生物による場合には、反応条件を微生物の増殖条件に合わせる必要があるため処理条件の調節が困難であるとともに、活性汚泥(微生物の死骸)の発生により結果的に排水汚染を引き起こす虞があるという問題がある。また、上記いずれの場合にも、設備(オゾン発生装置、バッキ槽)に関して多大な費用を要するという欠点も有している。   However, in the case of wastewater treatment with ozone, it has been pointed out that it affects the human body because it is involved in the production of carcinogenic compounds. On the other hand, in the case of using microorganisms, it is necessary to adjust the reaction conditions to the growth conditions of the microorganisms, and thus it is difficult to adjust the treatment conditions. There is a problem that there is. Moreover, in any of the above cases, there is also a drawback that a great deal of cost is required for the equipment (ozone generator, backing tank).

本発明は、このような問題に鑑みてなされたものであり、コスト低減を図るとともに、人体や環境に悪影響を及ぼすことなく穏和な条件で着色排水を脱色することが可能な構成の排水処理方法、および排水処理装置を提供することを目的とする。   The present invention has been made in view of such problems, and is a wastewater treatment method having a structure capable of decolorizing colored wastewater under mild conditions without adversely affecting the human body and the environment while reducing costs. And an object of the present invention is to provide a wastewater treatment apparatus.

上記目的を達成するために、本発明に係る排水処理方法は、着色排水中の染料と担子菌栽培後の廃菌床から抽出した酵素とを反応させて、染料を分解処理することにより、着色排水を脱色する構成である。   In order to achieve the above-mentioned object, the wastewater treatment method according to the present invention reacts with a dye in colored wastewater and an enzyme extracted from a waste fungus bed after cultivation of basidiomycetes, and decomposes the dye, thereby coloring the dye. It is the structure which decolors drainage.

なお、上記構成の排水処理方法において、排菌床の酵素によって脱色した排水中から、染料を分解処理した結果生じた生成物を膜濾過により分離して膜濾過水を精製することが好ましい。   In the wastewater treatment method having the above-described configuration, it is preferable to purify the membrane filtrate by separating the product produced as a result of the decomposition treatment of the dye from the wastewater decolorized by the enzyme in the waste bed by membrane filtration.

本発明に係る排水処理装置は、染料を含有する着色排水を脱色する排水処理装置であって、着色排水が導入されるとともに、着色排水中の染料と担子菌栽培後の廃菌床から抽出した酵素とを反応させ、染料を分解処理することにより、着色排水を脱色する分解処理槽を備えて構成される。   The wastewater treatment apparatus according to the present invention is a wastewater treatment apparatus for decolorizing colored wastewater containing a dye, and the colored wastewater is introduced and extracted from the dye in the colored wastewater and the waste fungus bed after basidiomycete cultivation. A decomposition treatment tank for decolorizing the colored waste water by reacting with the enzyme and decomposing the dye is provided.

なお、上記構成の排水処理装置において、分解処理槽において脱色された排水中から、染料を分解処理した結果生じた生成物を膜濾過により分離して膜濾過水を精製する膜分離手段を備えて構成されることが好ましい。   In addition, the wastewater treatment apparatus having the above-described configuration includes membrane separation means for separating the product generated as a result of the decomposition treatment of the dye from the wastewater decolorized in the decomposition treatment tank, and purifying the membrane filtrate by membrane filtration. Preferably, it is configured.

また、上記構成の排水処理装置において、膜分離手段が、分解処理槽において脱色された排水を、染料を分解処理した結果生じた生成物を含む膜濃縮水と膜濾過水とに分離する膜濃縮装置を備えて構成されることが好ましい。   Further, in the wastewater treatment apparatus having the above-described configuration, the membrane separation means separates the wastewater decolorized in the decomposition treatment tank into a membrane concentrated water containing a product resulting from the decomposition treatment of the dye and a membrane filtered water. It is preferable to be provided with an apparatus.

本発明に関する排水処理方法、および排水処理装置によれば、担子菌栽培後に残る廃菌床から抽出した染料分解能力を持つ酵素を有効利用することで、コスト低減を図るとともに、人体や環境に悪影響を及ぼすことなく穏和な条件で着色排水を脱色することが可能になる。   According to the wastewater treatment method and the wastewater treatment apparatus according to the present invention, by effectively using an enzyme having a dye-decomposing ability extracted from a waste fungus bed remaining after cultivation of basidiomycetes, the cost is reduced and the human body and the environment are adversely affected. It becomes possible to decolor the colored wastewater under mild conditions without exerting any effect.

本発明に係る排水処理方法を実施するのに好適な排水処理装置の一例を示すフロー図である。It is a flowchart which shows an example of the waste water treatment apparatus suitable for enforcing the waste water treatment method which concerns on this invention.

以下、本発明の好ましい実施形態について説明する。本発明に係る排水処理方法は、着色排水中の染料と担子菌栽培後の廃菌床から抽出した酵素とを反応させて、染料を分解処理することにより、着色排水を脱色することを特徴とする。   Hereinafter, preferred embodiments of the present invention will be described. The wastewater treatment method according to the present invention is characterized in that the colored wastewater is decolorized by reacting the dye in the colored wastewater with the enzyme extracted from the waste fungus bed after cultivation of basidiomycetes and decomposing the dye. To do.

本発明において対象となる染料としては、アゾ系染料、フタロシアニン系染料、アクリジン系染料、トリフェニルメタン系染料、トリアジン系染料などが適用可能であるが、これに限定されるものではない。その中でも染料として主に使用されるアゾ系染料としては、Acid Orange20やAcid Violet3等のモノアゾ系染料、Direct Blue2等のジアゾ系染料、トリアゾ系、およびテトラアゾ系などが例示されるが、これに限定されるものではない。   As dyes to be used in the present invention, azo dyes, phthalocyanine dyes, acridine dyes, triphenylmethane dyes, triazine dyes, and the like are applicable, but are not limited thereto. Among them, examples of the azo dye mainly used as the dye include monoazo dyes such as Acid Orange 20 and Acid Violet 3, diazo dyes such as Direct Blue 2, triazo dyes, and tetraazo dyes, but are not limited thereto. Is not to be done.

本発明において使用される担子菌(バシディオミセテス)としては、上記染料の分解能力を有する酵素を持つ担子菌であれば特に限定しないが、例えば、トキイロヒラタケ(Pleurotus salmoneostramineus)、ツクリタケ(Agaricus bisporus)、ナラタケ(Armillariella mellea)、エノキタケ(Flammulina velutipes)、シイタケ(Lentinus edodes)、ムキタケ(Pnellus serotinus)、エリンギ(Pleurotus eryngii)、ヒラタケ(Pleurotus ostreatus)等の食用キノコ類が例示される。なお、担子菌の中でも木材腐朽菌、白色腐朽菌が好適に用いられる。   The basidiomycete used in the present invention is not particularly limited as long as it is a basidiomycete having an enzyme capable of degrading the dye. For example, Pleurotus salmoneostramineus, Agaricus edible mushrooms such as bisporus, armillariella mellea, enokitake (Flammulina velutipes), shiitake (Lentinus edodes), mushroom (Pnellus serotinus), eringi (Pleurotus eryngii), oyster mushroom (Pleurotus ostreatus), etc. Among basidiomycetes, wood-rotting fungi and white-rotting fungi are preferably used.

担子菌の廃菌床とは、例えば担子菌の人工栽培後に残る菌床(培地)であって、オガ粉、培地添加物(栄養添加物)、および水等の混合物であるため、人体や環境に悪影響を及ぼすことはない。また、従来大量に廃棄されていた担子菌廃菌床の有効活用を図ることもできる。   The waste bed of basidiomycetes is, for example, a bed (medium) remaining after artificial cultivation of basidiomycetes, and is a mixture of sawdust, medium additive (nutrient additive), water, etc. Will not be adversely affected. Moreover, effective utilization of the basidiomycetes waste microbial bed conventionally discarded in large quantities can also be aimed at.

本発明で利用される担子菌由来の酵素は、担子菌が一般に生成するラッカーゼ(特に、木材腐朽菌や白色腐朽菌等に多く存在する)であり、このラッカーゼ(Laccase)は基本的には種々の基質(例えばフェノール性の化合物)の一電子酸化を触媒する活性酵素である。なお、同じラッカーゼという名前の酵素であっても、上記担子菌の種類によってその性質は異なり、好適に作用する基質や、最適温度、最適pHなどの活性条件が異なってくる。また、同じ担子菌でも性質の異なる複数のラッカーゼを有することもある。よって、上記担子菌群の廃菌床から抽出される少なくとも1種以上のラッカーゼが用いられる。すなわち、複数種のラッカーゼを組み合わせて用いてもよい。   The basidiomycete-derived enzyme used in the present invention is a laccase generally produced by basidiomycetes (especially abundantly in wood-rotting fungi and white-rotting fungi), and this laccase is basically various. It is an active enzyme that catalyzes the one-electron oxidation of a substrate (for example, a phenolic compound). In addition, even if it is the enzyme named the same laccase, the property changes with kinds of said basidiomycete, and active conditions, such as a substrate which acts suitably, optimal temperature, and optimal pH, differ. Moreover, the same basidiomycete may have a plurality of laccases having different properties. Therefore, at least one or more types of laccase extracted from the waste fungus bed of the basidiomycete group are used. That is, you may use combining multiple types of laccase.

ラッカーゼの作用としては、例えば染料中のフェノール類(電子供与体)から電子(水素)を引き抜き、その電子を酸素分子(電子受容体)に渡して水を生成する化学反応の触媒をしている。この過程において、染料の発色団に関係する構造が破壊され、染料の脱色が生じると推定される。このラッカーゼの反応に関しては、穏和な条件下で反応を進行させることが可能である。   As an action of laccase, for example, an electron (hydrogen) is extracted from phenols (electron donor) in a dye, and the electron is passed to an oxygen molecule (electron acceptor) to catalyze a chemical reaction that generates water. . In this process, it is presumed that the structure related to the chromophore of the dye is destroyed and decolorization of the dye occurs. With regard to this laccase reaction, it is possible to proceed under mild conditions.

ここで、上記酵素を用いた脱色能力(脱色活性)の測定法としては、一定時間ごとに着色排水を採取して、当該染料の最大吸収波長の吸光度(吸光度減少率)を測定し、これを脱色率として推定するのが好ましい。   Here, as a method of measuring the decoloring ability (decoloring activity) using the above enzyme, colored waste water is collected at regular intervals, and the absorbance (decrease rate of absorbance) of the maximum absorption wavelength of the dye is measured. It is preferable to estimate the decolorization rate.

また、上記のように酵素(ラッカーゼ)と染料とを反応させると、その結果物として染料の成分に応じた生成物(残留物)が生じる。したがって、染料の分解処理の後段に、脱色処理された排水と上記生成物とを分離するための膜分離手段を設けることが好ましい。膜分離手段としては、生成物を濃縮した膜濃縮水と透過水とに分離する膜濃縮法が好適である。   When the enzyme (laccase) and the dye are reacted as described above, a product (residue) corresponding to the component of the dye is generated as a result. Therefore, it is preferable to provide a membrane separation means for separating the decolored waste water from the product after the dye decomposition treatment. As the membrane separation means, a membrane concentration method in which the product is separated into concentrated membrane water and permeated water is preferable.

次に、本発明の排水処理方法を実施するために好適な排水処理装置について説明する。図1に本実施形態に係る排水処理装置の一例を示すフロー図を示しており、この図を参照して排水処理装置の概略構成を説明する。   Next, a waste water treatment apparatus suitable for carrying out the waste water treatment method of the present invention will be described. FIG. 1 is a flowchart showing an example of a wastewater treatment apparatus according to the present embodiment, and a schematic configuration of the wastewater treatment apparatus will be described with reference to this figure.

排水処理装置1は、大別的には、染料を含む排水(以下、着色排水と称する)を一時的に貯留する貯留槽2と、貯留槽2から送給される着色排水を脱色処理する分解処理槽4と、分解処理槽4で脱色された処理液中に残留する生成物を捕捉する膜濃縮装置11とを備えて構成される。   The waste water treatment apparatus 1 is broadly divided into a storage tank 2 for temporarily storing waste water containing dye (hereinafter referred to as colored waste water), and a decomposition for decolorizing the colored waste water supplied from the storage tank 2. A treatment tank 4 and a membrane concentrator 11 that captures a product remaining in the treatment liquid decolorized in the decomposition treatment tank 4 are configured.

貯留槽2は、例えば印刷装置や染色工場等から排出される着色排水(染料排水)を原水として一時的に貯留する。貯留槽2の着色排水は送給ポンプ3によって吸い上げられて分解処理槽4へ送給される。なお、分解処理槽4での処理の効率化のために、分解処理槽4に導入する前の貯留槽2に滞留する着色排水を、予め酵素活性に適した水温に予熱するための予熱手段を設けてもよい。   The storage tank 2 temporarily stores, as raw water, colored wastewater (dye wastewater) discharged from, for example, a printing apparatus or a dyeing factory. The colored wastewater in the storage tank 2 is sucked up by the feed pump 3 and fed to the decomposition treatment tank 4. In order to increase the efficiency of the treatment in the decomposition treatment tank 4, a preheating means for preheating the colored wastewater staying in the storage tank 2 before being introduced into the decomposition treatment tank 4 to a water temperature suitable for the enzyme activity in advance. It may be provided.

分解処理槽4は、送給ポンプ3によって導入された染色排水で満たされており、この染色排水中に染料を分解するための酵素(ラッカーゼ)を含有する排水処理剤6が投入されている。排水処理剤6に使用する酵素については、担子菌の廃菌床もしくはこれを粉砕したものに緩衝液を加えて攪拌することで当該酵素を溶出された後、濾過等によって抽出する。   The decomposition treatment tank 4 is filled with the dye wastewater introduced by the feed pump 3, and the wastewater treatment agent 6 containing an enzyme (laccase) for decomposing the dye is introduced into the dye wastewater. The enzyme used in the wastewater treatment agent 6 is extracted by filtration or the like after the enzyme is eluted by adding a buffer solution to a basidiomycete waste bed or a pulverized product thereof and stirring.

緩衝液としては、例えば酢酸アンモニウムや燐酸などが適用され、抽出対象の酵素活性が維持されればpHは特に限定されない。排水処理剤6としては、緩衝液からの抽出液を遠心分離して得た上澄み液である酵素液や、この酵素液を凍結乾燥処理した酵素製剤などが例示される。酵素製剤は、粉末化したものや、これを整形して錠剤化(タブレット化)したものが例示される。特に、排水処理剤6を錠剤にすれば、その取り扱いが容易になるとともに、1個当たりの重量が一定になるため、処理対象の着色排水に対して適切な投与量(添加量)を錠剤の個数をもって算定することができる。なお、排水処理剤6を、例えば所定時間間隔で分解処理槽4内に自動的に投与する処理剤投入装置を設けて構成してもよい。   As the buffer, for example, ammonium acetate or phosphoric acid is applied, and the pH is not particularly limited as long as the enzyme activity to be extracted is maintained. Examples of the waste water treatment agent 6 include an enzyme solution which is a supernatant obtained by centrifuging an extract from a buffer solution, and an enzyme preparation obtained by freeze-drying the enzyme solution. Examples of the enzyme preparation include powdered ones and those obtained by shaping the tablets into tablets (tablets). In particular, if the wastewater treatment agent 6 is made into a tablet, its handling becomes easy and the weight per one becomes constant. Therefore, an appropriate dose (addition amount) for the colored wastewater to be treated is set to the tablet. It can be calculated with the number. In addition, you may comprise the processing agent injection | throwing-in apparatus which administers the waste water processing agent 6 automatically in the decomposition processing tank 4 at predetermined time intervals, for example.

分解処理槽4においては、着色排水中の染料と排水処理剤6の酵素とが反応して、当該染料(着色排水)が脱色される。この分解処理槽4内には着色排水を攪拌させるための攪拌装置5が設置されており、これにより着色排水の染料と排水処理剤6の酵素との接触の機会を増大させている。また、染料と酵素との反応を促進させるために、着色排水の温度を調整する水温調整手段や、着色排水に塩酸や燐酸液等を加えてpHを調整するpH調整手段を設けてもよい。   In the decomposition treatment tank 4, the dye in the colored wastewater reacts with the enzyme of the wastewater treatment agent 6 to decolorize the dye (colored wastewater). A stirring device 5 for stirring the colored waste water is installed in the decomposition treatment tank 4, thereby increasing the chance of contact between the dye of the colored waste water and the enzyme of the waste water treatment agent 6. Further, in order to promote the reaction between the dye and the enzyme, a water temperature adjusting means for adjusting the temperature of the colored waste water, or a pH adjusting means for adjusting the pH by adding hydrochloric acid or phosphoric acid solution to the colored waste water may be provided.

また、分解処理槽4には、脱色処理後の排水(以下、処理水と称する)の吸光度を計測する吸光度計測装置7が接続されている。この吸光度計測装置7は、処理水の一部を間欠的もしくは連続的に抜き出して処理水の吸光度を測定し、この測定情報を制御部8へ出力する。吸光度計測装置7としては、例えばフローセル型紫外可視吸光光度計が例示される。この吸光光度計は、染料の色素波長と同じ波長帯域の光を透過させて、当該透過率を計測することで染料の吸光度を求めるものである。   The decomposition treatment tank 4 is connected with an absorbance measuring device 7 for measuring the absorbance of the waste water after decoloring treatment (hereinafter referred to as treated water). The absorbance measurement device 7 intermittently or continuously extracts part of the treated water, measures the absorbance of the treated water, and outputs this measurement information to the control unit 8. As the absorbance measuring device 7, for example, a flow cell type ultraviolet visible absorptiometer is exemplified. This absorptiometer transmits light in the same wavelength band as the dye pigment wavelength and measures the transmittance to determine the absorbance of the dye.

制御部8は、吸光度計測装置7から入力される計測情報に基づいて、計測された吸光度が予め設定された所定値以下、すなわち脱色処理が十分に行われていると判定すると、分解槽に設けられた電磁弁9を開いて送給ポンプ10を介して分解処理槽4と膜濃縮装置11とを連通させる。なお、吸光度計測装置7を設けることなく、例えば、タイマカウンタによって分解処理槽4での着色排水の滞留時間(処理時間)を計測して、規定の滞留時間の経過に伴って電磁弁9を開弁させる構成としてもよい。   When the control unit 8 determines that the measured absorbance is equal to or less than a predetermined value set in advance based on the measurement information input from the absorbance measurement device 7, that is, the decolorization process is sufficiently performed, the control unit 8 is provided in the decomposition tank. The opened electromagnetic valve 9 is opened, and the decomposition treatment tank 4 and the membrane concentrator 11 are communicated with each other via the feed pump 10. For example, the residence time (treatment time) of the colored wastewater in the decomposition treatment tank 4 is measured by a timer counter without providing the absorbance measurement device 7, and the electromagnetic valve 9 is opened as the prescribed residence time elapses. It is good also as a structure made to valve.

分解処理槽4で脱色された処理水は、送給ポンプ10によって吸い上げられて次段の膜濃縮装置11へ送給される。ここで、染料の脱色とは、無色透明への脱色のみに限定されるものではなく、変色や減色をも含む概念である。   The treated water decolorized in the decomposition treatment tank 4 is sucked up by the feed pump 10 and fed to the membrane concentrator 11 at the next stage. Here, decolorization of a dye is not limited to decolorization to colorless and transparent, but is a concept including discoloration and color reduction.

膜濃縮装置11は、排水処理剤6によって脱色された処理水を膜透過水W1と膜濃縮液W2とに分離するための分離膜12を有している。分離膜12としては、精密濾過膜(マイクロフィルタ)或いは限外濾過膜等の有機膜や無機膜が適用可能である。また、分離膜12の形態は、膜モジュールとして平膜型、中空糸型、スパイラル型、円筒(管状)型、プリーツ型等を適宜採用することができる。分離膜の孔径としては、例えば精密濾過膜の場合と限外濾過膜の場合で異なるが、トラップ対象の生成物に応じて適宜なものが選定される。   The membrane concentrating device 11 has a separation membrane 12 for separating the treated water decolorized by the waste water treatment agent 6 into the membrane permeated water W1 and the membrane concentrated liquid W2. As the separation membrane 12, an organic membrane or an inorganic membrane such as a microfiltration membrane (microfilter) or an ultrafiltration membrane can be applied. In addition, as the form of the separation membrane 12, a flat membrane type, a hollow fiber type, a spiral type, a cylindrical (tubular) type, a pleat type, and the like can be appropriately employed as the membrane module. The pore size of the separation membrane varies depending on, for example, the case of the microfiltration membrane and the case of the ultrafiltration membrane, but an appropriate one is selected according to the product to be trapped.

膜濃縮装置11において、導入された処理水の一部は、膜間差圧によって分離膜12を透過して膜透過水W1として膜透過水受入槽13に流入される。膜透過水受入層13へ導かれた膜透過水W1は、例えばpH処理された後、最終的には河川等に放流される。一方、前段の酵素分解によって生じた生成物等の不純物は分離膜12によって阻止されて、膜濃縮水W2として系外へ排出される。膜濃縮装置11より間欠的もしくは連続的に系外に引き抜かれた膜濃縮水W2(生成物)は、例えば脱水装置14によって脱水された上で廃棄される。   In the membrane concentrator 11, a part of the treated water introduced permeates the separation membrane 12 by the transmembrane pressure and flows into the membrane permeate receiving tank 13 as the membrane permeate W1. The membrane permeated water W1 guided to the membrane permeated water receiving layer 13 is finally discharged into a river or the like after being subjected to pH treatment, for example. On the other hand, impurities such as products produced by the previous enzymatic decomposition are blocked by the separation membrane 12 and discharged out of the system as membrane concentrated water W2. The membrane concentrated water W2 (product) drawn out of the system intermittently or continuously from the membrane concentrator 11 is dehydrated by, for example, the dehydrator 14 and then discarded.

以上説明したように、本実施形態に係る排水処理方法、および排水処理装置によれば、担子菌の栽培後に残る廃菌床から抽出した染料分解能力を持つ酵素(ラッカーゼ)を有効利用することで、コスト低減を図るとともに、人体や環境に悪影響を及ぼすことなく穏和な条件で着色排水を脱色することを可能にした排水処理手段を提供することができる。   As described above, according to the wastewater treatment method and wastewater treatment apparatus according to the present embodiment, by effectively using an enzyme (laccase) having a dye-decomposing ability extracted from a waste fungus bed remaining after cultivation of basidiomycetes. In addition to reducing costs, it is possible to provide wastewater treatment means capable of decolorizing colored wastewater under mild conditions without adversely affecting the human body and the environment.

また、脱色処理の結果生じた生成物を捕捉する膜濃縮装置(膜分離手段)を設けることにより、脱色された処理水を河川等公共用水に放流可能な水質にまで浄化することが可能である。   In addition, by providing a membrane concentrating device (membrane separation means) that captures a product generated as a result of the decolorization treatment, it is possible to purify the decolorized treated water to a quality that can be discharged into public water such as rivers. .

これまで本発明の好ましい実施形態について説明したが、本発明はこの実施形態に限定されるものではない。例えば、上述の実施形態においては、脱色の対象となる着色排水を一旦、貯留槽2に導入する構成を例示して説明したが、これに限定されるものではなく、分解処理槽4に直接導入する構成であってもよい。   Although the preferred embodiment of the present invention has been described so far, the present invention is not limited to this embodiment. For example, in the above-described embodiment, the configuration in which the colored wastewater to be decolorized is once introduced into the storage tank 2 has been described as an example. However, the present invention is not limited to this and is directly introduced into the decomposition treatment tank 4. It may be configured to.

また、上述の実施形態においては、分解処理槽4を1つのみ設けた構成を例示して説明したが、これに限定されるものではなく、例えば、複数の分解処理槽を直列に接続して設け、これらをダーティタンクとクリーンタンクとに分けて構成したり、複数の分解処理槽の間を循環させる構成であってもよい。   Moreover, in the above-mentioned embodiment, although the structure which provided only one decomposition treatment tank 4 was illustrated and demonstrated, it is not limited to this, For example, a some decomposition treatment tank is connected in series It may be provided and divided into a dirty tank and a clean tank, or may be configured to circulate between a plurality of decomposition treatment tanks.

さらに、上述の実施形態においては、分解処理手段の後段に膜濾過手段として膜濃縮装置11を備えた構成を例示して説明したが、これに限定されるものではなく、例えば、膜濾過手段として1段目に精密濾過膜(マイクロフィルタ)を配置し、2段目に限外濾過膜を配置した2段構成の膜濾過手段としてもよい。また、例えば、膜濾過手段の前段もしくは後段に、沈降分離法(沈殿池)や加圧浮上法といった固液分離手段を更に設けて構成してもよい。   Furthermore, in the above-described embodiment, the configuration provided with the membrane concentrating device 11 as the membrane filtration means at the subsequent stage of the decomposition processing means has been described as an example. However, the present invention is not limited to this. A membrane filtration means having a two-stage configuration in which a microfiltration membrane (microfilter) is arranged in the first stage and an ultrafiltration membrane is arranged in the second stage may be used. Further, for example, a solid-liquid separation means such as a sedimentation separation method (sedimentation basin) or a pressure flotation method may be further provided before or after the membrane filtration means.

また、上述の実施形態においては、分解処理槽4で脱色された処理液を送給ポンプ10によって膜濃縮装置11に導入する構成を例示して説明したが、これに限定されるものではなく、例えば、分解処理槽4の上澄み液が膜濃縮装置11に供給されるものであってもよい。   In the above-described embodiment, the configuration in which the treatment liquid decolorized in the decomposition treatment tank 4 is introduced into the membrane concentrator 11 by the feed pump 10 has been described as an example, but is not limited thereto. For example, the supernatant liquid of the decomposition treatment tank 4 may be supplied to the membrane concentration apparatus 11.

さらに、上述の実施形態においては、酵素(ラッカーゼ)を含有する排水処理剤6を用いた構成を例示して説明したが、例えば、廃菌床自体(廃菌床を適宜な大きさに加工したもの等)を排水処理剤として用いてもよい。また、排水処理剤に酵素活性(ラッカーゼ活性)を促進させる添加剤を添加して構成してもよい。   Furthermore, in the above-mentioned embodiment, although the structure using the waste water treatment agent 6 containing an enzyme (laccase) was illustrated and demonstrated, for example, the waste microbial bed itself (the waste microbial bed was processed into an appropriate size) May be used as a wastewater treatment agent. Moreover, you may comprise by adding the additive which accelerates | stimulates enzyme activity (laccase activity) to a waste water treatment agent.

1 排水処理装置
2 貯留槽
3 送給ポンプ
4 分解処理槽
5 攪拌装置
6 排水処理剤
7 吸光度計測装置
8 制御部
9 電磁弁
10 送給ポンプ
11 膜濃縮装置(膜分離手段)
12 分離膜
13 膜透過水受入槽
14 脱水装置
W1 膜透過水
W2 膜濃縮水
DESCRIPTION OF SYMBOLS 1 Waste water treatment device 2 Storage tank 3 Feeding pump 4 Decomposition processing tank 5 Stirring device 6 Waste water treatment agent 7 Absorbance measuring device 8 Control part 9 Electromagnetic valve 10 Feeding pump 11 Membrane concentrator (membrane separation means)
12 Separation membrane 13 Membrane permeate receiving tank 14 Dehydrator W1 Membrane permeate W2 Membrane concentrate

Claims (5)

着色排水中の染料と担子菌栽培後の廃菌床から抽出した酵素とを反応させて、前記染料を分解処理することにより、前記着色排水を脱色することを特徴とする排水処理方法。   A wastewater treatment method comprising: decolorizing the colored wastewater by reacting the dye in the colored wastewater with an enzyme extracted from a waste fungus bed after cultivation of basidiomycetes to decompose the dye. 前記排菌床の酵素によって脱色した排水中から、前記染料を分解処理した結果生じた生成物を膜濾過により分離して膜濾過水を精製することを特徴とする請求項1に記載の排水処理方法。   The wastewater treatment according to claim 1, wherein a product obtained as a result of decomposing the dye is separated by membrane filtration from the wastewater decolorized by an enzyme in the waste bed to purify the membrane filtrate. Method. 染料を含有する着色排水を脱色する排水処理装置であって、
前記着色排水が導入されるとともに、前記着色排水中の染料と担子菌栽培後の廃菌床から抽出した酵素とを反応させ、前記染料を分解処理することにより、前記着色排水を脱色する分解処理槽を備えて構成されることを特徴とする排水処理装置。
A wastewater treatment device for decolorizing colored wastewater containing a dye,
Decomposition treatment that decolorizes the colored wastewater by introducing the colored wastewater, reacting the dye in the colored wastewater with the enzyme extracted from the waste fungus bed after basidiomycete cultivation, and decomposing the dye A waste water treatment apparatus comprising a tank.
前記分解処理槽において脱色された排水中から、前記染料を分解処理した結果生じた生成物を膜濾過により分離して膜濾過水を精製する膜分離手段を備えて構成されることを特徴とする請求項3に記載の排水処理装置。   Membrane separation means for separating the product resulting from the decomposition treatment of the dye from the waste water decolorized in the decomposition treatment tank by membrane filtration to purify the membrane filtered water is provided. The wastewater treatment apparatus according to claim 3. 前記膜分離手段が、前記分解処理槽において脱色された排水を、前記染料を分解処理した結果生じた生成物を含む膜濃縮水と膜濾過水とに分離する膜濃縮装置を備えて構成されることを特徴とする請求項4に記載の排水処理装置。   The membrane separation means includes a membrane concentrating device that separates the waste water decolorized in the decomposition treatment tank into a membrane concentrated water containing a product resulting from the decomposition treatment of the dye and a membrane filtered water. The waste water treatment apparatus according to claim 4.
JP2009295740A 2009-12-25 2009-12-25 Wastewater treatment method and apparatus Pending JP2011131199A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2009295740A JP2011131199A (en) 2009-12-25 2009-12-25 Wastewater treatment method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2009295740A JP2011131199A (en) 2009-12-25 2009-12-25 Wastewater treatment method and apparatus

Publications (1)

Publication Number Publication Date
JP2011131199A true JP2011131199A (en) 2011-07-07

Family

ID=44344513

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2009295740A Pending JP2011131199A (en) 2009-12-25 2009-12-25 Wastewater treatment method and apparatus

Country Status (1)

Country Link
JP (1) JP2011131199A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108435144A (en) * 2018-05-22 2018-08-24 安徽三环水泵有限责任公司 A method of preparing domestic sewage treating compound using edible fungi residue
CN111170556A (en) * 2020-01-03 2020-05-19 龙海市永利来食品有限公司 Efficient wastewater treatment method for mushroom production

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10286589A (en) * 1997-04-15 1998-10-27 Takuma Co Ltd Decoloration of wastewater and treatment method of hardly decomposable substance using hydrogen peroxide
JP2004066043A (en) * 2002-08-02 2004-03-04 Toyo Ink Mfg Co Ltd Method of decomposing dye and enzyme for decomposing dye

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10286589A (en) * 1997-04-15 1998-10-27 Takuma Co Ltd Decoloration of wastewater and treatment method of hardly decomposable substance using hydrogen peroxide
JP2004066043A (en) * 2002-08-02 2004-03-04 Toyo Ink Mfg Co Ltd Method of decomposing dye and enzyme for decomposing dye

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108435144A (en) * 2018-05-22 2018-08-24 安徽三环水泵有限责任公司 A method of preparing domestic sewage treating compound using edible fungi residue
CN111170556A (en) * 2020-01-03 2020-05-19 龙海市永利来食品有限公司 Efficient wastewater treatment method for mushroom production

Similar Documents

Publication Publication Date Title
Pulido A review on the use of membrane technology and fouling control for olive mill wastewater treatment
Kurade et al. Monitoring the gradual biodegradation of dyes in a simulated textile effluent and development of a novel triple layered fixed bed reactor using a bacterium-yeast consortium
Zacharof et al. Nanofiltration of treated digested agricultural wastewater for recovery of carboxylic acids
Asgher et al. Decolorization potential of mixed microbial consortia for reactive and disperse textile dyestuffs
Shivajirao Treatment of distillery wastewater using membrane technologies
Kim et al. Decolorization of dye solutions by a membrane bioreactor (MBR) using white-rot fungi
US8741143B2 (en) Process and plant for treating a water stream
Jafari et al. Degradation of a textile reactive azo dye by a combined biological-photocatalytic process: Candida tropicalis Jks2-Tio 2/Uv
Deveci et al. Integrated process of fungal membrane bioreactor and photocatalytic membrane reactor for the treatment of industrial textile wastewater
JP2014061487A (en) Water treatment method and water treatment system
Ferrer-Polonio et al. Brine recovery from hypersaline wastewaters from table olive processing by combination of biological treatment and membrane technologies
David et al. Effect of domestic wastewater as co-substrate on biological stain wastewater treatment using fungal/Bacterial consortia in pilot plant and greenhouse reuse
JP2011131199A (en) Wastewater treatment method and apparatus
JP5117803B2 (en) Decolorization treatment method, decolorization treatment apparatus and decolorization treatment agent for waste water containing dye
Nędzarek et al. Application of ceramic membranes for microalgal biomass accumulation and recovery of the permeate to be reused in algae cultivation
Gómez-Caravaca et al. Recovery of phenolic compounds from olive oil mill wastewaters by physicochemical methodologies
Gholami et al. Textile dye removal by membrane technology and biological oxidation
Liu et al. Variation in the biological characteristics of BAC during ultrasonic regeneration
JP2011131200A (en) Wastewater treatment agent
Ozkan‐Yucel et al. Effect of Initial Azo Dye Concentration and Biomass Acclimation on Sludge Digestion and Dye Co‐treatment
Widiasa et al. Membrane-based recirculating aquaculture system: Opportunities and challenges shrimp farming
CN113015704B (en) Recycling of sodium sulfate in process water from starch processing
KR101622936B1 (en) Apparatus and method for cultivating micro-algae applied ozone oxidation
Janiszewska et al. The possibility for the use of ultrafiltration for the treatment of potato processing water
Zielinska et al. Membrane filtration for valorization of digestate from the anaerobic treatment of distillery stillage

Legal Events

Date Code Title Description
RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20120611

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20121207

A977 Report on retrieval

Effective date: 20130409

Free format text: JAPANESE INTERMEDIATE CODE: A971007

A131 Notification of reasons for refusal

Effective date: 20130507

Free format text: JAPANESE INTERMEDIATE CODE: A131

A02 Decision of refusal

Effective date: 20131015

Free format text: JAPANESE INTERMEDIATE CODE: A02