JP2006231124A - Selective separation and recovery apparatus and method of bacterial by foam separation method using protein - Google Patents
Selective separation and recovery apparatus and method of bacterial by foam separation method using protein Download PDFInfo
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本発明は、複数の細菌が存在する処理水から選択的に細菌を分離回収する方法であって、とくにタンパク質を用いた泡沫分離法による細菌の選択的な分離回収方法に関するものであり、さらにそれに使用する分離回収装置に関するものである。 The present invention relates to a method for selectively separating and recovering bacteria from treated water containing a plurality of bacteria, and more particularly to a method for selectively separating and recovering bacteria by a foam separation method using proteins. The present invention relates to a separation and recovery device to be used.
現在、水道水の原水となる河川水やプール、公衆浴場、海水浴場における水の中には複数の細菌が比較的低濃度で混在しており、その濃度によって人が使用する許容度が決められている。しかし近年、これらの細菌の中に病原性を示す細菌が混在し、動物や魚介類に感染し、さらに人体に間接的、或いは直接的に感染する事故が発生している。 Currently, the water in river water, pools, public baths, and beaches, which are raw water for tap water, contains a relatively low concentration of bacteria, and the tolerance for human use is determined by the concentration. ing. However, in recent years, there have been accidents in which pathogenic bacteria are mixed in these bacteria, infecting animals and fishery products, and indirectly or directly infecting the human body.
上記の事故防止のため、各種の薬品等による殺菌処理が行なわれているが、例えば塩素やオゾン等は人体には有害であり使用方法にも制限があった。また、これらの細菌を分離する方法としては、寒天平板による平板法が広く採用されているが、細菌を培養するためには少なくとも数日間かかり、また少量の試料しか接種できないため細菌密度が低い処理水の場合には細菌が検出できないという問題点があった。さらに吸引濾過とフィルタによる培養方法もあるが、大量の処理水を濾過する必要があり作業に長時間と労力を要し、しかも吸引の際に細菌の細胞が破壊される惧れがあった。 In order to prevent the above-mentioned accident, sterilization treatment with various chemicals and the like is performed. For example, chlorine and ozone are harmful to the human body and there are restrictions on the usage. In addition, as a method for separating these bacteria, a plate method using an agar plate is widely adopted. However, it takes at least several days to cultivate the bacteria, and since only a small amount of sample can be inoculated, a treatment with low bacterial density is performed. In the case of water, there was a problem that bacteria could not be detected. In addition, there is a culture method using suction filtration and a filter, but it is necessary to filter a large amount of treated water, which requires a long time and labor for the work, and there is a possibility that bacterial cells may be destroyed during the suction.
これらの問題点を解決するために、活性汚泥処理系における糸状性バルキングによる固液分離障害を抑制するための固液分離障害抑制剤および固液分離障害抑制方法が提案されている(特許文献1参照。)。また修飾抗体の結合した細胞液を、カルボキシル基を表面に含有する水不溶性担体と処理して目的細胞を分離する技術も紹介されている(特許文献2参照。)。
しかしながら、上記特許文献1に提案されている固液分離障害抑制方法の場合、界面活性剤と粒状担体とを必要とし、しかも糸状性細菌の処理に限定されるものであり、複数の細菌が比較的低濃度で混在する水道水の原水となる河川水やプール、公衆浴場、海水浴場から選択的に細菌を分離回収できないという問題点がある。また、特許文献2に紹介された技術では、生化学的研究における細胞分離や医療分野において特定の細胞捕集において有用であるものの、上記の処理水に混入した細菌の分離方法としては適しないものである。
However, in the case of the solid-liquid separation failure suppression method proposed in Patent Document 1, a surfactant and a granular carrier are required, and the method is limited to the treatment of filamentous bacteria. There is a problem that bacteria cannot be selectively separated and collected from river water, pools, public baths, and beaches that are raw water of tap water mixed at low concentrations. In addition, the technique introduced in
上記の問題点に鑑み本発明者らは、細菌が生物の粘膜や体表面粘着物などのタンパク質に付着しやすい性質を有することに着目し鋭意研究の結果、種類の異なる細菌に対するタンパク質の吸着特性の違いを利用し、複数の細菌を含む処理水から選択的に細菌を分離回収する装置および回収方法を提供することを目的とする。 In view of the above problems, the present inventors have paid attention to the fact that bacteria tend to adhere to proteins such as biological mucous membranes and adherents on the body surface. It is an object of the present invention to provide an apparatus and a collection method for selectively separating and recovering bacteria from treated water containing a plurality of bacteria.
このため本発明の分離回収方法は、複数の細菌を含む処理水を処理槽に注入し、前記細菌を選択的に吸着するタンパク質を前記処理水に投入するとともに、送気手段によって前記処理水内に気泡を発生させ、前記細菌を前記気泡中の前記タンパク質に選択的に吸着させて分離回収することを特徴とする。 Therefore, in the separation and recovery method of the present invention, treated water containing a plurality of bacteria is injected into a treatment tank, a protein that selectively adsorbs the bacteria is introduced into the treated water, and the inside of the treated water is supplied by an air supply means. Bubbles are generated, and the bacteria are selectively adsorbed to the protein in the bubbles to be separated and recovered.
また、前記分離回収する細菌は、大腸菌1種Esherichia coli、腸球菌1種Enterococcus facalis、レンサ球菌2種Strepttococcus dysgalactia、Streptococcus iniae、パスツレラ菌1種Pastreurella piscucudaのうち少なくとも1種であることを特徴とする。 In addition, the bacteria to be separated and recovered are at least Escherichia coli Escherichia coli, Enterococcus Enterococcus facalis, Streptococcus 2 Streptococcus dysgalactia, Streptococcus iniae, Pasteurella sp. .
そして、本発明の分離回収装置は、複数の細菌を含む処理水を処理槽に注入する手段、前記細菌を選択的に吸着するタンパク質を前記処理水に投入する手段、送気手段によって前記処理水内に気泡を発生させる手段、前記細菌を前記気泡中の前記タンパク質に選択的に吸着させて分離回収する手段、とから構成されることを特徴とする。 The separation and recovery apparatus according to the present invention includes a means for injecting treated water containing a plurality of bacteria into a treatment tank, a means for introducing a protein that selectively adsorbs bacteria into the treated water, and an air supply means. And a means for selectively adsorbing the bacteria to the protein in the bubbles to separate and recover the bacteria.
本発明において、使用されるタンパク質としては魚類体表面粘質物(糖タンパク質)、カゼイン、アルブミン、ヘモグロビン、大豆タンパク、ゼラチン等が挙げられ、とくにカゼインは投入する量が少なくてよく、しかも安価である。 In the present invention, examples of proteins used include fish body surface mucilage (glycoprotein), casein, albumin, hemoglobin, soy protein, gelatin and the like. .
本発明に係るによれば、塩素やオゾン等の有害な物質を使用せずに処理水から細菌を分離回収ができるため、作業が極めて安全であるという優れた効果を有する。 According to the present invention, since bacteria can be separated and recovered from treated water without using harmful substances such as chlorine and ozone, it has an excellent effect that the operation is extremely safe.
また、処理水にタンパク質を投入し、処理水内に気泡を生じさせて前記タンパク質に細菌を選択的に吸着させ分離回収でるため作業時間も短く、また細菌密度の低い処理水であっても効率よく細菌の分離回収が可能であるという優れた効果を有する。 In addition, protein is introduced into the treated water, bubbles are generated in the treated water, and bacteria are selectively adsorbed to the protein for separation and recovery, so the work time is short and even treated water with low bacterial density is efficient. It has an excellent effect that bacteria can be separated and recovered well.
さらに、本発明の分離回収装置は、吸引濾過やフィルタをせず送気手段によって発生する気泡とタンパク質によって細菌を吸着させるため、細菌が破壊されることなく分離回収できるという優れた効果を有する。 Furthermore, since the separation / recovery device of the present invention adsorbs bacteria by bubbles and proteins generated by the air supply means without using suction filtration or filtering, it has an excellent effect that the bacteria can be separated and recovered without being destroyed.
以下、本発明を実施例に基づいて説明するが、本発明が本実施例に限定されないことは言うまでもない。また、後述する本実施例における懸濁水は、上記記載の処理水を示す。 EXAMPLES Hereinafter, although this invention is demonstrated based on an Example, it cannot be overemphasized that this invention is not limited to a present Example. Moreover, the suspending water in a present Example mentioned later shows the said treated water.
図1は、本発明による分離回収装置の一実施例を示しており、分離回収装置1は、略円筒形状の処理槽2と送気ポンプ3とガラスボールフィルタ4とアスピレーター5とから構成され、送気ポンプ3と処理槽2の間には空気流量計6が接続され、泡沫トラップ瓶7はアスピレーター5と処理槽2の間に連結されている。
FIG. 1 shows an embodiment of a separation / recovery device according to the present invention. The separation / recovery device 1 comprises a substantially
処理槽2に注入された原水には、タンパク質投入装置(図示せず)からタンパク質(図示せず)が投入され懸濁水8とされ、送気ポンプ3から送気された空気がガラスボールフィルタ4にて微細気泡とされ処理槽2内の懸濁水8を攪拌し上昇する。懸濁水8に含まれるタンパク質と前記微細気泡により泡沫9が生じ、泡沫9内のタンパク質によって細菌が選択的に吸着される。そして処理槽2の液面に集結した泡沫9は、アスピレーター5にて吸引され、泡沫トラップ瓶7に回収される。以下に本発明に係るタンパク質を用いた泡沫分離法による細菌の選択的な分離回収方法に関してさらに詳細に説明する。
The raw water injected into the
(供試細菌の培養と原水への投入)
大腸菌1種Esherichia coli、腸球菌1種Enterococcus facalis、レンサ球菌2種Strepttococcus dysgalactia、Streptococcus iniae、パスツレラ菌1種Pastreurella piscucudaを細菌培養地500mlに移植し、25℃で24時間培養する。次に培養した細菌を遠心分離機にて6000rpmで30分間処理し集菌を行い、滅菌水(原水)250mlに投入した。さらに所定の濁度まで滅菌水(原水)を投入し希釈を行い懸濁水とした。
(Cultivation of test bacteria and injection into raw water)
E. coli Escherichia coli, Enterococcus enterococcus Enterococcus facalis, Streptococcus species 2 Streptococcus dysgalactia, Streptococcus iniae, Pasteurella piscucuda at 25 ° C. are cultured for 24 hours at 25 ° C. Next, the cultured bacteria were treated with a centrifuge at 6000 rpm for 30 minutes to collect the bacteria, and poured into 250 ml of sterilized water (raw water). Further, sterilized water (raw water) was added to a predetermined turbidity and diluted to obtain suspended water.
(供試タンパク質)
活魚を冷凍装置によって−30℃にて凍結させ、再度解凍させた後エタノール1lに浸漬し5分間放置した。次に活魚表面からゲル状となった粘質物を薬さじにて剥ぎ取り、GF/Cフィルターにて吸引濾過を行い、さらにエタノールにより複数回洗浄し減圧乾燥し粉砕機にて粉末化し魚類体表面粘質物粉末を得た。カゼイン、アルブミン、ヘモグロビン、大豆タンパク、およびゼラチンは市販のものを採用した。ゼラチンは50〜60℃の温蒸留水にて溶解し、その他は0.01molの水酸化ナトリウム水溶液に溶解させタンパク質水溶液を得た。尚、本実施例における活魚はウナギおよびコイを使用した。
(Test protein)
The live fish was frozen at −30 ° C. by a freezer, thawed again, immersed in 1 l of ethanol and left for 5 minutes. Next, the gelled sticky material is peeled off from the surface of the live fish with a spoonful, filtered with suction through a GF / C filter, further washed with ethanol several times, dried under reduced pressure, and powdered with a pulverizer. A viscous powder was obtained. Casein, albumin, hemoglobin, soy protein, and gelatin were commercially available. Gelatin was dissolved in hot distilled water at 50 to 60 ° C., and the others were dissolved in 0.01 mol aqueous sodium hydroxide solution to obtain an aqueous protein solution. In addition, the live fish in a present Example used the eel and the carp.
(泡沫分離)
懸濁水200mlを300mlのビーカーに投入し、上記準備したタンパク質水溶液をそれぞれ所定の濃度となるように添加し、ジャーテスターにて1分間急速攪拌した。添加濃度は混濁水の表面に泡沫が発生する程度とした。次にこの混濁水を200ml分取し、前記分離回収装置の処理槽に注入し泡沫分離処理を行なった。泡沫分離処理条件としては、送気流量0.3l/分、処理時間3分間とした。分離率は懸濁水原水と分離処理後の処理水の濁度の吸光度から求めた。結果を表1に示す。
(Foam separation)
200 ml of suspended water was put into a 300 ml beaker, the prepared protein aqueous solution was added to a predetermined concentration, and rapidly stirred for 1 minute with a jar tester. The addition concentration was such that foam was generated on the surface of the turbid water. Next, 200 ml of this turbid water was collected and poured into the treatment tank of the separation and recovery device to perform foam separation. The foam separation treatment conditions were an air flow rate of 0.3 l / min and a treatment time of 3 minutes. The separation rate was determined from the absorbance of the turbidity of the raw suspended water and the treated water after separation. The results are shown in Table 1.
表1に示すように、腸球菌、レンサ球菌Strepttococcus dysgalactia、およびパスツレラ菌は上記のタンパク質により選択的に分離回収された。 As shown in Table 1, enterococci, streptococci streptococcus dysgalactia, and pasteurella were selectively separated and recovered by the above proteins.
本発明によるによれば、水道水の原水等の極低密度の細菌試水における病原性細菌の高感度モニタリング技術として利用できる。しかも危険物質である塩素やオゾン等の除菌剤を使用することなく細菌を分離できるため、プール、公衆浴場、あるいは漁港魚市場等の用水の除菌技術として利用できる。 According to the present invention, it can be used as a highly sensitive monitoring technique for pathogenic bacteria in extremely low-density bacterial test water such as tap water raw water. In addition, since bacteria can be separated without using sterilizing agents such as chlorine and ozone, which are dangerous substances, it can be used as a sterilization technique for water in pools, public baths, fishing port fish markets and the like.
1 分離回収装置
2 処理槽
3 ガラスボールフィルター
4 送気ポンプ
5 アスピレーター
6 空気流量計
7 泡沫トラップ瓶
8 懸濁水
9 泡沫
DESCRIPTION OF SYMBOLS 1 Separation and
Claims (3)
Means for injecting treated water containing a plurality of bacteria into a treatment tank; means for introducing a protein that selectively adsorbs the bacteria into the treated water; means for generating bubbles in the treated water by an air supply means; The apparatus for selectively separating and recovering bacteria by a foam separation method using a protein according to claim 1 or 2, comprising means for selectively adsorbing the protein to the protein in the bubbles and separating and recovering the same.
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JP2015029968A (en) * | 2013-08-05 | 2015-02-16 | 国立大学法人京都大学 | Method and apparatus for removing microorganism and organic matter in water |
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JPH06154731A (en) * | 1992-11-17 | 1994-06-03 | Toshiaki Maruyama | Removal of pollutant in liquid |
JPH08257548A (en) * | 1995-03-24 | 1996-10-08 | Toshiaki Maruyama | Removing method for polluting suspended substance in plain water type waste water |
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JPH06154731A (en) * | 1992-11-17 | 1994-06-03 | Toshiaki Maruyama | Removal of pollutant in liquid |
JPH08257548A (en) * | 1995-03-24 | 1996-10-08 | Toshiaki Maruyama | Removing method for polluting suspended substance in plain water type waste water |
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JP2015029968A (en) * | 2013-08-05 | 2015-02-16 | 国立大学法人京都大学 | Method and apparatus for removing microorganism and organic matter in water |
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