JPH0290903A - Flocculant derived from microbe and flocculation method - Google Patents

Flocculant derived from microbe and flocculation method

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Publication number
JPH0290903A
JPH0290903A JP63240438A JP24043888A JPH0290903A JP H0290903 A JPH0290903 A JP H0290903A JP 63240438 A JP63240438 A JP 63240438A JP 24043888 A JP24043888 A JP 24043888A JP H0290903 A JPH0290903 A JP H0290903A
Authority
JP
Japan
Prior art keywords
culture
flocculant
treated
alcaligenes
wastewater
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.)
Granted
Application number
JP63240438A
Other languages
Japanese (ja)
Other versions
JPH064123B2 (en
Inventor
Ryuichiro Kurane
隆一郎 倉根
Tomoo Suzuki
智雄 鈴木
Yasuhiro Nobata
靖浩 野畑
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.)
HAKUTOU KAGAKU KK
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
HAKUTOU KAGAKU KK
Agency of Industrial Science and Technology
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Filing date
Publication date
Application filed by HAKUTOU KAGAKU KK, Agency of Industrial Science and Technology filed Critical HAKUTOU KAGAKU KK
Priority to JP63240438A priority Critical patent/JPH064123B2/en
Publication of JPH0290903A publication Critical patent/JPH0290903A/en
Publication of JPH064123B2 publication Critical patent/JPH064123B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

PURPOSE:To attain flocculation effect in a wide range covering inorganic to organic various emulsions and oily emulsions by preparing a flocculant mainly consisting of alcaligenes faecalis culture or its treated product. CONSTITUTION:The culture or treated one of strains which belong to alcaligenes and are able to produce a flocculant originated from microbe, as a typical example the culture of alcaligenes-lettuce B-16 strain (FERM BP 2015), is prepared. The treated culture has characteristic of a transparent or light yellow solid, an anionic polymer, and about 1000-15000cps viscosity. Ethanol is added to the culture fluid, the product is then separated, washed with water, and freeze-dried to obtain a treated culture product. Generally, flocculation is carried out by adding the culture of alcaligenes faecalis or a treated one in a prescribed amount to various kinds of emulsions.

Description

【発明の詳細な説明】 1)産業上の利用分野 本発明は、微生物由来の凝集剤及び凝集方法に関するも
のであり、各種の汚濁物質の処理、各種工業の排水処理
分野、都市下水、各種の醗酵液の処理、油濁物質の処理
、さらには有用物質等の回収利用等広範囲にわたり利用
が期待される。
Detailed Description of the Invention 1) Industrial Application Field The present invention relates to a flocculant derived from microorganisms and a flocculation method, and is applicable to the treatment of various pollutants, the wastewater treatment field of various industries, urban sewage, and various types of agglomeration. It is expected to be used in a wide range of applications, including the treatment of fermentation liquids, treatment of oily substances, and even the recovery and use of useful substances.

2)従来技術 凝集剤は各種工業の進展に伴い、各種工程及びそれらか
ら排出される廃水分野に広く使用されている。凝集剤は
一般的に合成高分子系(例えば、ポリアクリルアミド系
等)、無機系凝集剤(例えば、硫酸バンド等)及び生物
系凝集剤に大別される。このうち微生物(産生)凝集剤
は微生物か生産する物質で他の物質を凝集させ沈殿(沈
降)し易くさせる性能を有する物質である。また、機能
面よりとらえると、カチオン系、ノニオン系、アニオン
系の3つに分類することができる。我が国における凝集
剤の生産量は、アニオン・ノニオン系合成高分子系凝集
剤で15,000 トン7年、カチオン系合成高分子系
凝集剤で9,000 トン7年と言われている。
2) Prior art With the progress of various industries, flocculants are widely used in various processes and the wastewater discharged from them. Flocculants are generally classified into synthetic polymer-based flocculants (eg, polyacrylamide-based, etc.), inorganic-based flocculants (eg, sulfuric acid, etc.), and biological-based flocculants. Among these, microorganism (produced) flocculants are substances produced by microorganisms that have the ability to flocculate other substances and make them easier to precipitate (sediment). From a functional standpoint, they can be classified into three types: cationic, nonionic, and anionic. The production volume of flocculants in Japan is said to be 15,000 tons for 7 years for anionic/nonionic synthetic polymer flocculants and 9,000 tons for 7 years for cationic synthetic polymer flocculants.

従来、これら合成高分子系及び無機系凝集剤は活性汚泥
法等を用いた廃水処理分野から土木浚渫工事等への清澄
処理剤として多用されてきた。
Conventionally, these synthetic polymer-based and inorganic flocculants have been widely used as clarification agents in the field of wastewater treatment using activated sludge methods and the like, as well as in civil engineering dredging work and the like.

また、上水道、中水道の造水分野、醗酵工業における醗
酵液と培養菌体の分離といったダウンストリームプロセ
ッシング分野からさらには食品工業分野への適用という
ように非常に広範囲な分野にわたって凝集剤の使用は期
待されている。このように、凝集剤の使用は今日の社会
生活に深く組み込まれており、なくてはならないもので
あるがゆえに、さらに今後ますますその使途が多岐にわ
たり使用量が増加するものと予想される。このため凝集
剤の使用は環境面ひいては人間の健康にも直結している
と考えられる。しかしながら、現在広く用いられる合成
高分子系凝集剤(例えば、ポリアクリルアミド)等は能
力、経済性の点で優れているが安全性及び環境面での問
題点も指摘されていると言われている。さらに、バイオ
インダストリーにおけるダウンストリームプロセッシン
グへの適用を考えると合成高分子系凝集剤の使用には問
題があると考えられる。
In addition, flocculants are used in a very wide range of fields, from the water production field of water and middle water supplies, downstream processing fields such as the separation of fermentation liquor and cultured bacteria in the fermentation industry, to the food industry field. It is expected. As described above, the use of flocculants is deeply integrated into today's social life and is indispensable, and it is expected that their uses will become more diverse and the amount used will increase in the future. Therefore, the use of flocculants is considered to have a direct connection to the environment and even to human health. However, although the currently widely used synthetic polymer flocculants (e.g., polyacrylamide) are superior in terms of performance and economy, they are said to have safety and environmental problems. . Furthermore, when considering the application to downstream processing in bioindustry, the use of synthetic polymer flocculants is thought to be problematic.

これらの欠点を解消・克服する新規凝集剤の開発は、各
方面より切望されており、特に生分解性を持ち安全でか
つ二次公害の恐れのない生物由来の凝集剤の開発への期
待が高まっていた。
The development of a new flocculant that eliminates or overcomes these shortcomings is desperately needed from various fields, and there are particularly high hopes for the development of a biologically derived flocculant that is biodegradable, safe, and free from the risk of secondary pollution. It was increasing.

ところで、微生物産生凝集剤についてはグラム陽性細菌
に属するロードコツカス属由来の微生物産生凝集剤N0
C−1(日本特許箱1,096,062号)がすでに知
られており、凝集剤として有効であるが、より高い収率
の微生物産生凝集剤が求められていた。
By the way, regarding microorganism-produced flocculants, microorganism-produced flocculant N0 derived from the genus Rhodococchus, which belongs to Gram-positive bacteria.
C-1 (Japanese Patent Box No. 1,096,062) is already known and effective as a flocculant, but a microorganism-produced flocculant with a higher yield has been sought.

3)発明が解決しようとする問題点 このような背景のもとに、本発明者らは高分子系凝集剤
等のもつ問題点を解消・克服すべく、広く微生物、特に
ダラム陰性細菌による微生物産生凝集剤を求めて検索を
行った。即ち、安全性、生分解性が優れており二次公害
の恐れのない安全な凝集剤及びその凝集方法について、
種々の研究開発を重ねたところ、ダラム陰性細菌のアル
カリゲネス(Alkaligenes)属に属する細菌
培養物又は培養処理物或いはそれらと無機塩もしくは天
然系凝集剤の少なくとも1種との存在下で優れた凝集効
果を有することかっ高収率で凝集剤が得られることを見
出し、本発明を完成させるに至った。
3) Problems to be solved by the invention Based on this background, the present inventors have developed a wide range of microorganisms, particularly microorganisms such as Durum-negative bacteria, in order to solve and overcome the problems of polymer-based flocculants, etc. A search was conducted for the produced flocculant. In other words, regarding a safe flocculant that has excellent safety and biodegradability and does not cause secondary pollution, and a flocculation method using the same,
Through various research and development efforts, we have found that bacterial cultures belonging to the genus Alkaligenes, Durham-negative bacteria, or culture-treated products, or their presence in the presence of at least one inorganic salt or natural flocculant, have an excellent flocculating effect. The present inventors have discovered that a flocculant can be obtained in high yield by having the following properties, and have completed the present invention.

4)問題点を解決するための手段 本発明に使用される菌株は、アルカリゲネス属に属し、
微生物産生凝集剤生産能を有する菌株であればよいが、
その代表例示菌株は、アルカリゲネス・レータス(Al
caligenes Iatus) B −16株で、
FEl?M BP−2015号として寄託されている。
4) Means for solving the problems The bacterial strain used in the present invention belongs to the genus Alcaligenes,
Any strain can be used as long as it has the ability to produce a microbial flocculant, but
The representative strain is Alcaligenes latus (Al
caligenes Iatus) B-16 strain,
FEl? It has been deposited as M BP-2015.

以下、本発明に使用する代表株(FERMBl)−20
15号)の菌学的性質を表1に示す。この表1に示す菌
学的性質から、バージ−・マニュアル・システマチック
・バクテリオロジー 第1巻(Bergey ’ sM
anual of Systematic Bacte
riology Volume l)。
Below, representative strain (FERMBl)-20 used in the present invention
Table 1 shows the mycological properties of No. 15). From the mycological properties shown in Table 1, Bergey's Manual Systematic Bacteriology Volume 1 (Bergey's M
annual of Systematic Bacte
riology Volume I).

(1984年)372頁により、アルカリゲネス属に属
することが判明した。タイプストレイン(ATCC29
712)においては、表1におけるデオキシリボヌクレ
アーゼ。
(1984) p. 372, it was found that it belongs to the genus Alcaligenes. Type strain (ATCC29
712), the deoxyribonucleases in Table 1.

クエン酸。citric acid.

アルギニンデバイドロラーゼ。Arginine dividerolase.

アクリルアミダーゼ。Acrylamidase.

糖より酸の生成。Production of acid from sugar.

菌体外ポリマー生産能。Extracellular polymer production ability.

の記載は見当らないが、他の諸性質は本願の株とタイプ
ストレインは一致する。
Although there is no description of this, the type strain matches the strain of the present application in other properties.

表 1 菌学的性質 表 (続き) このような菌株の炭素源としては、フラクトース、グル
コース、シュークロース等の単糖類・少糖類の他に、ヘ
ミセルロース、でん粉、コーンスターチ等の天然高分子
及びオリーブ浦等の油類の炭素源が好ましくは用いられ
る。さらに、尿素。
Table 1 Mycological properties (continued) Carbon sources for such strains include monosaccharides and oligosaccharides such as fructose, glucose, and sucrose, as well as natural polymers such as hemicellulose, starch, and corn starch, and Preferably, carbon sources of oils such as the following are used. Additionally, urea.

塩安、硝安、硫安等の無機体窒素源、トリプトン。Inorganic nitrogen sources such as ammonium chloride, ammonium nitrate, ammonium sulfate, and tryptone.

酵母エキス、肉エキス、ペプトン、麦芽エキス等の有機
窒素源、その他、リン酸カリ、硫酸マグネシウム、食塩
等の無機塩類が培地構成成分として使用される。
Organic nitrogen sources such as yeast extract, meat extract, peptone, and malt extract, as well as inorganic salts such as potassium phosphate, magnesium sulfate, and common salt, are used as culture medium components.

培養は液体培養でもよい。培養は初発pl+が4〜10
、温度15〜40℃の範囲で行われ、通常は通気撹拌培
養で行なわれる。培養は炭素源等の種類にもよるが培養
10から10口間の間で行われ、この間で最大凝集活性
時期が設定される。
The culture may be a liquid culture. Initial pl+ of culture is 4-10
The cultivation is carried out at a temperature in the range of 15 to 40°C, and is usually carried out by aerated stirring culture. Cultivation is carried out for between 10 and 10 incubations, depending on the type of carbon source, etc., and the maximum flocculation activity period is set during this period.

培養処理物の性状は、無色透明あるいは薄黄色の固体、
アニオン性高分子であり、その粘度は約i 、 ooo
〜15,000epsである。粘度の測定は100倍の
水(20°C)を添加し、完全に吸水した状態で回転粘
度計で行う。
The properties of the cultured product are colorless and transparent or pale yellow solid;
It is an anionic polymer, and its viscosity is approximately i, ooo
~15,000 eps. The viscosity is measured by adding 100 times as much water (20°C) and using a rotational viscometer in a state where the water is completely absorbed.

培養を行うことにより凝集能を有する培養物を得る。培
養液に2倍量のエタノールを加え、5°Cにて一夜放置
した沈殿物をNo、 2 ’(戸紙にてン濾過を行い集
め、その後70%エタノールにて3回洗浄、さらに蒸留
水にて3回?戸紙上で洗浄後、凍結乾燥等により水分を
とばした凝集物質か培養処理物として回収できる。しか
しながら、本発明では、このように分離精製した培養処
理物を使用するまでもなく、培養物そのものをそのまま
使用することができる。
A culture having flocculation ability is obtained by culturing. Add twice the amount of ethanol to the culture solution, leave it overnight at 5°C, collect the precipitate by filtering it with No. After washing on paper for three times, water can be removed by freeze-drying, etc., and the aggregated material or cultured material can be recovered as a cultured material. However, in the present invention, there is no need to use the cultured material separated and purified in this way. , the culture itself can be used as is.

また、ここで凝集効果をさらに促進するために併用され
る無機塩としては、水中でカチオンを生成し得るものが
望ましく、好ましくは2価以上の多価カチオンを生成し
得るものがよく、例えば塩化カルシウム等のカルシウム
イオンを生成するものが有利に用いられる。併用される
天然系凝集剤としてはカニ等のこうらより抽出されるキ
トサンが4r利に用いられる。
In addition, the inorganic salt used in combination to further promote the flocculation effect is desirably one that can generate cations in water, preferably one that can generate polyvalent cations of divalent or higher valences, such as chloride. Those that generate calcium ions, such as calcium, are advantageously used. As a natural flocculant used in combination, chitosan extracted from the shells of crabs and the like is used for 4R purposes.

しかし、これら併用される無機塩及び天然系凝集剤の添
加量は、凝集させるべき対象の種類によ−)で決められ
るのが望ましく一般的に特に制約さイするものではない
However, the amount of the inorganic salt and natural flocculant used in combination is desirably determined depending on the type of object to be flocculated, and is generally not particularly restricted.

本発明において、凝集の対象となるものは特に制約され
るものではない。代表的なものを例示すると、無機性と
しては粘土の一種であるカオリン(白とう土)懸濁液、
フェノール等の毒物を劇んだコークス排水、また着色、
微細懸濁物を含んだだ製紙排水さらには有機性としての
食品排水等が例示される。一般的には各々の凝集対象に
際し、好適に実施される。
In the present invention, there are no particular restrictions on what is to be agglomerated. Typical examples include suspensions of kaolin, a type of clay;
Coke wastewater containing toxic substances such as phenol, and colored,
Examples include papermaking wastewater containing fine suspended matter, and organic food wastewater. Generally, it is carried out suitably for each aggregation target.

本発明の方法は、一般的には各種懸濁液などに対し、本
発明によるアルカリゲネス属細菌の培養物、又は培養処
理物を加えるか、あるいは、各種%i液に本発明による
アルカリゲネス属細菌の培養物又は培養処理物を加え、
ついで併用する無機塩又は天然系凝集剤を加えることに
よって実施される。これらの実施方法は特に制約される
ものではない。さらに、凝集時の混和液のpl+を中性
から微アルカリ性にする場合もあるが、特にplL7!
]整を行わなくてもよい。
The method of the present invention generally involves adding the culture or culture treatment product of the Alcaligenes bacteria according to the present invention to various suspensions, or adding the culture of the Alcaligenes bacteria according to the present invention to various %i solutions. Add the culture or culture treatment,
This is then carried out by adding an inorganic salt or a natural flocculant to be used in combination. These implementation methods are not particularly restricted. Furthermore, pl+ of the mixed solution during aggregation may be made from neutral to slightly alkaline, but especially plL7!
] There is no need to perform adjustment.

なお、以下において示すように本発明による懸濁液など
の凝集活性は、処理液の吸光度測定、COD測定及びS
S(懸濁性微細固体物)除去率等によって求めた。
As shown below, the aggregation activity of the suspension according to the present invention can be determined by measuring the absorbance of the treatment liquid, measuring the COD, and measuring the S
It was determined based on the S (suspended fine solids) removal rate.

(イ)吸光度による凝集活性測定法 水活性A+++定法は日本農業化学会誌欧文誌(Agr
ic、 Biol、 Chem、) 50巻9号231
0頁に記載されている倉根等の方法に基づいて行った。
(a) Aggregation activity measurement method using absorbance The water activity A+++ standard method is the Japanese Agricultural Chemistry Society Journal
ic, Biol, Chem,) Volume 50, No. 9, 231
This was carried out based on the method of Kurane et al. described on page 0.

すなわちカオリン5 、000ppm懸濁液80m1に
20倍〜100倍に希釈した培養物(又は培養処理物)
 10m1を加え、さらに塩化カルシウム10m1(1
%)を加えた後、pHを7.0に調整し、 100ml
メスシリンダーにて反応液を5分間静置し、処理液の上
清部の吸光度を波長550nmにて分光光学計を用いて
測定した。各吸光度を測定した後、次式により凝集活性
(F、A、)を計算した。
That is, a culture (or culture treated product) diluted 20 to 100 times in 80 ml of kaolin 5,000 ppm suspension.
Add 10ml of calcium chloride, and add 10ml of calcium chloride (1
%), adjust the pH to 7.0, and add 100 ml
The reaction solution was allowed to stand for 5 minutes in a graduated cylinder, and the absorbance of the supernatant of the treated solution was measured at a wavelength of 550 nm using a spectrophotometer. After measuring each absorbance, the aggregation activity (F, A,) was calculated using the following formula.

なお、コントロールのOlD、55oは培養0時間目の
吸光度の値、すなわち、前述の培養物の代りに培地をお
きかえたものであり、他はすべて前述と同じ方法をとっ
たものである。
Note that the control OLD, 55o is the absorbance value at 0 hours of culture, that is, the culture medium was replaced with the above-mentioned culture, and all other methods were the same as above.

カオリン懸濁液に対しては前述のような方法によって求
めたが、対象廃水によっては吸光度測定の波長を550
nmから適宜変換し、それぞれの最も好ましい波長にて
測定した。
The kaolin suspension was determined using the method described above, but depending on the target wastewater, the wavelength for absorbance measurement may be changed to 550.
The wavelength was appropriately converted from nm and measured at each most preferred wavelength.

■)’C0D(化学的酸素要求量)による凝集活性測定
: CODの測定法はJIS規格によって行った。
(2) Measurement of aggregation activity by 'C0D (chemical oxygen demand): COD was measured according to JIS standards.

(ハ)S S (Suspended 5olid :
微細懸濁固体物)による凝集活性測定:SSは1−のゲ
ラスフイルターン濾過残渣物の重世を測定することによ
って行った。
(c) S S (Suspended 5 solid:
Measurement of flocculation activity using finely suspended solids: SS was performed by measuring the weight of the gelatin filtration residue of 1-.

5)実施例 次に、本発明を実施例により、さらに詳細に説明する。5) Examples Next, the present invention will be explained in more detail with reference to Examples.

[実施例Iコ 〈凝集物質産生菌の培養と凝集物質の回収〉フラクトー
ス15g、KH2PO48,4g、に2HPO44,4
g、 M g SQ  ・7 H200,2g1食塩0
.1g、尿素0.5g、酵母エキス0.5gを蒸留水1
Ωに溶かし、培地をpH7,2〜7.6に調整した。培
地501111を、300m1の三角フラスコにとり、
オートクレーブにより、120°C115分間無菌殺菌
した後、アルカリゲネス・レータスB−16株(PER
M BP−2015号)を1白金耳の量でフラスコに移
植し、30℃にてロータリー回転培養を行う。なお回転
数は180rpmである。
[Example I <Culture of flocculant-producing bacteria and recovery of flocculant> 15 g of fructose, 48.4 g of KH2PO, 44.4 g of 2HPO
g, M g SQ ・7 H200, 2g 1 salt 0
.. 1g, urea 0.5g, yeast extract 0.5g, distilled water 1
The medium was adjusted to pH 7.2-7.6. Transfer medium 501111 to a 300ml Erlenmeyer flask,
After sterilization in an autoclave at 120°C for 115 minutes, Alcaligenes latus strain B-16 (PER
M BP-2015) was transplanted into a flask in an amount of 1 platinum loop, and cultured with rotary rotation at 30°C. Note that the rotation speed is 180 rpm.

この時の培養物0.1mlを用いて凝集活性を前記のカ
オリンを指標にして塩化カルシウム併用下にて培養物の
凝集活性を測定した。また菌体の生育度は波長660n
mにて濁度を測定して求めた。
Using 0.1 ml of the culture at this time, the aggregation activity of the culture was measured using the above-mentioned kaolin as an index in combination with calcium chloride. In addition, the growth rate of bacterial cells is at a wavelength of 660n.
It was determined by measuring the turbidity at m.

結果を表2に示す。The results are shown in Table 2.

表   2 表2からあきらかのように、本凝集活性は、菌の生育の
対数増殖期に最大となり、定常期に入るにつれてその活
性は減少していく。
Table 2 As is clear from Table 2, this agglutination activity is at its maximum during the logarithmic growth phase of bacterial growth, and the activity decreases as the bacteria enter the stationary phase.

この最大凝集活性を示す30目の培養液より、凝集物質
の回収を行った。即ち、培養液の2倍量のエタノールを
加え、5°Cにて一夜放置し沈殿物を得た。沈殿物をN
o、 2のン戸紙にて?濾過を行い集め、その後70%
エタノールにて3回洗浄を行い、さらに蒸留水にて3回
ン戸紙上にて洗浄を行った後凍結乾燥等により水分をと
ばして凝集物質(培養処理物)を得た。これらの操作に
より前記培地を用いることにより、培養液1Ω当り約1
2g(乾燥重管)の凝集物質を得た。
Agglutinated substances were collected from the 30th culture solution showing the maximum aggregation activity. That is, ethanol in an amount twice that of the culture solution was added, and the mixture was left at 5°C overnight to obtain a precipitate. Precipitate N
o, 2nd door paper? Filter and collect, then 70%
After washing three times with ethanol and three times with distilled water on paper, the water was removed by freeze-drying or the like to obtain an aggregated material (cultured material). By using the above-mentioned medium through these operations, approximately 1
2 g (dry tube) of aggregated material was obtained.

[実施例2] 実施例1にて得られた凍結乾燥標品(凝集物質)を熱ア
ルカリ液にて完全に溶解させ10%凝集物質水溶液を作
製した。
[Example 2] The freeze-dried sample (flocculant) obtained in Example 1 was completely dissolved in a hot alkaline solution to prepare a 10% aqueous solution of flocculant.

5 、000ppmカオリン懸濁液80m1に上記の1
0%凝集物質水溶液を10m1加えゆるやかに混和し、
さらに蒸留水10m1を加え再びゆるやかに混和した後
5分間静置し凝集活性(F、A、)を測定した。なお、
比較のため凍結乾燥標品を加えていない熱アルカリ水を
加えたものをコントロールにして測定した。
5. Add the above 1 to 80ml of kaolin suspension of 5,000ppm.
Add 10ml of 0% flocculant aqueous solution and mix gently.
Furthermore, 10 ml of distilled water was added, and the mixture was gently mixed again, and then left to stand for 5 minutes, and the flocculation activity (F, A,) was measured. In addition,
For comparison, measurements were made using a sample to which hot alkaline water to which no freeze-dried sample was added was used as a control.

結果を表3に示す。The results are shown in Table 3.

表 表3に示すように、本発明区においてアルカリゲネス・
レータス属細菌B−16株(FERN Bl)−201
5吋)を培養し得られた凍結乾燥凝集物質水溶液を添加
することにより、カオリン!V濁液は5分後にフロック
を形成し懸濁状態のカオリンが凝集沈殿してくることが
明らかになった。
As shown in Table 3, in the present invention area, Alcaligenes
Letus bacterium B-16 strain (FERN Bl)-201
Kaolin! It was revealed that the V suspension formed flocs after 5 minutes, and the suspended kaolin coagulated and precipitated.

[実施例3] コークス工場排水は、炭化物の微細な懸濁物(S S)
が非常に多く含まれており、かつ毒性のあるフェノール
等も含まれている排水であり、通常の沈殿処理では非常
に凝集しにくい排水と言われており、微細88分が高く
かつCOD (化学的酸素要求量)も高い排水と言われ
ている。
[Example 3] Coke factory wastewater contains fine suspensions of carbides (SS)
This wastewater contains a very large amount of phenol, which is toxic, and is said to be extremely difficult to coagulate in normal sedimentation treatment. It is said that the wastewater has a high oxygen demand (oxygen demand).

このコークス排水90m1に対して、実施例1により得
られた培養液を5倍希釈した液を10m1加え、ついで
塩化カルシウムを1%濃度になるように加えた反応液を
5分間静置し、上澄液のSS情とCODを測定した。な
お、対照区として、培養液の代りに培地を同様にして用
いた。結果を表4に示す。
To 90 ml of this coke wastewater, 10 ml of a 5-fold dilution of the culture solution obtained in Example 1 was added, and then the reaction solution to which calcium chloride was added to a concentration of 1% was allowed to stand for 5 minutes. The SS content and COD of the clear liquid were measured. In addition, as a control group, a medium was used in the same manner instead of the culture solution. The results are shown in Table 4.

表4に示す如く、本凝集方法によりコークス排水中の微
細炭化懸濁物は効率良く凝集沈殿除去されると共にコー
クス排水中のCODも除去されることが認められた。
As shown in Table 4, it was confirmed that by this coagulation method, fine carbonized suspensions in coke wastewater were efficiently coagulated and precipitated, and COD in coke wastewater was also removed.

[実施例4] 染料を含んだ着色排水で、かつ有機性微細懸濁物を多量
に含んでいる実排水として紙加工工場排水に対して、本
凝集剤液を適用した。この有機性微細懸濁物はコート紙
製造工程におけるでん粉微細粒であり、染料は印刷用青
色染料である。
[Example 4] This flocculant solution was applied to paper processing factory wastewater, which was colored wastewater containing dye and contained a large amount of organic fine suspensions. This organic fine suspension is starch fine particles used in the coated paper manufacturing process, and the dye is a blue dye for printing.

この排水90m1に対して実施例1により得られた培養
液の5倍希釈液を10m1加え、ついで、天然系凝集剤
としてカニ等の甲殻類の殻より抽出して加工処理工程を
経てつくられたキトサンを濃度150ppm添加し、本
凝集剤と天然系凝集剤との併用による凝集効果を調べた
。結果を表5に示す。
To 90 ml of this wastewater, 10 ml of a 5-fold dilution of the culture solution obtained in Example 1 was added, and then a natural flocculant was extracted from the shells of crustaceans such as crabs and processed. Chitosan was added at a concentration of 150 ppm, and the flocculating effect of the combined use of this flocculant and a natural flocculant was investigated. The results are shown in Table 5.

表5に示すように、天然系凝集剤キトサンのみでは微細
懸濁物を凝集沈殿させることはできなかったのに対し、
本凝集剤と天然系凝集剤併用区においては凝集沈殿させ
ることか可能になった。
As shown in Table 5, it was not possible to coagulate and precipitate fine suspensions using the natural flocculant chitosan alone.
Coagulation and sedimentation became possible when this flocculant was used in combination with a natural flocculant.

同時に波長600r+mにて着色同排水の吸光度を測定
したところ、併用区において大幅な吸光度の減少がみら
れ、結果として青色染料も凝集沈殿除去できた。
At the same time, when the absorbance of the colored wastewater was measured at a wavelength of 600 r+m, a significant decrease in absorbance was observed in the combined use area, and as a result, the blue dye was also able to be removed by coagulation and precipitation.

[実施例5] 有機性排水の代表例として食品工場排水に対する本凝集
剤の凝集沈殿効果を検討した。本食品工場排水は主成分
として微細な植物性繊維質懸濁物を多く含む排水である
[Example 5] The coagulation-sedimentation effect of this flocculant on food factory wastewater as a representative example of organic wastewater was investigated. This food factory wastewater contains a large amount of fine vegetable fiber suspension as its main component.

この食品工場排水80m1に対して実施例1で得られた
培養液のYO倍希釈液10m1を加え、ついで塩化カル
シウム液を最終濃度1%あるいはキトサン液を最終濃度
1100ppになるように加え、5分間静置を行い、そ
の反応処理液(上澄液)の88分及びCODを測定した
To 80 ml of this food factory wastewater, add 10 ml of the YO-fold diluted culture solution obtained in Example 1, then add calcium chloride solution to a final concentration of 1% or chitosan solution to a final concentration of 1100 pp, for 5 minutes. The reaction mixture was allowed to stand still, and the 88-minute and COD values of the reaction treated liquid (supernatant liquid) were measured.

なお、対照区として、生産菌を植菌していない10倍希
釈培地を用いてコントロールとした。
In addition, as a control, a 10-fold diluted medium without inoculating production bacteria was used as a control.

結果を表6に示した。The results are shown in Table 6.

表6に示したように、本凝集剤生産菌による培養液を添
加した系において、カチオン(塩化カルシウム)あるい
は天然系凝集剤キトサンを併用することにより、有機性
排水である食品排水中の微lTll−]−機質懸濁物(
S S)は効率良く凝集沈殿することか確認された。
As shown in Table 6, in a system containing a culture solution produced by this flocculant-producing bacterium, by using cations (calcium chloride) or chitosan, a natural flocculant, it is possible to reduce the amount of Tll in food wastewater, which is organic wastewater. - ] - Organism suspension (
It was confirmed that SS) coagulated and precipitated efficiently.

さらに、排水中のCODもカチオン併用区においては約
1/3弱が除去できることも明らかになった。
Furthermore, it was also revealed that approximately 1/3 of the COD in wastewater could be removed in the cation-combined treatment area.

Claims (1)

【特許請求の範囲】 1、アルカリゲネス(Alkaligenes)属菌培
養物又はその処理物を主成分とする凝集剤。 2、無機塩或いは天然系懸濁物質凝集剤の少なくとも1
種以上をさらに含有する請求項1の凝集剤。 3、アルカリゲネス属菌がアルカリゲネス、レータス(
Alkaligeneslatus)B−16株(FE
RMBP−2015号)である請求項1又は2の凝集剤
。 4、請求項1〜3のいずれかの凝集剤を被処理物質と接
触させて凝集する方法。 5、請求項1〜3のいずれかの凝集剤を被処理物質と接
触させて脱色する方法。
[Scope of Claims] 1. A flocculant whose main component is a culture of bacteria of the genus Alkaligenes or a processed product thereof. 2. At least one of an inorganic salt or a natural suspended matter flocculant
The flocculant according to claim 1, further comprising at least one species. 3. Bacteria of the genus Alcaligenes are Alcaligenes, Latus (
Alkaligenes latus) B-16 strain (FE
The flocculant according to claim 1 or 2, which is RMBP-2015). 4. A method of bringing the flocculant according to any one of claims 1 to 3 into contact with a substance to be treated to flocculate it. 5. A method of decolorizing the flocculant according to any one of claims 1 to 3 by bringing it into contact with a substance to be treated.
JP63240438A 1988-09-26 1988-09-26 Microorganism-derived aggregating agent and aggregating method Expired - Lifetime JPH064123B2 (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
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Publications (2)

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JPH0290903A true JPH0290903A (en) 1990-03-30
JPH064123B2 JPH064123B2 (en) 1994-01-19

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Country Link
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000140509A (en) * 1998-11-16 2000-05-23 Kansai Kako Kk Novel flocculant and sludge treatment using the same
CN108660178A (en) * 2018-07-19 2018-10-16 佛山皖阳生物科技有限公司 A kind of preparation method of high flocculating rate microbial flocculant
JP2019026763A (en) * 2017-07-31 2019-02-21 甲陽ケミカル株式会社 Composition for organic matter flocculation containing regenerated chitosan

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS494685A (en) * 1972-05-08 1974-01-16
JPS5186189A (en) * 1974-12-25 1976-07-28 Ajinomoto Kk BISEIBUTSUNYORUTANPAKUGYOSHUKATSUSEIBUTSUSHITSUNO SEIZOHO
JPS5924649A (en) * 1982-08-02 1984-02-08 Kokka Kogyo Kk Rubber belt and forming process thereof
JPS6071009A (en) * 1983-09-26 1985-04-22 Sanyo Chem Ind Ltd Preparation of substance having flocculation activity
JPS63126596A (en) * 1986-11-14 1988-05-30 Agency Of Ind Science & Technol Decoloring method for soluble dye by microorganism

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS494685A (en) * 1972-05-08 1974-01-16
JPS5186189A (en) * 1974-12-25 1976-07-28 Ajinomoto Kk BISEIBUTSUNYORUTANPAKUGYOSHUKATSUSEIBUTSUSHITSUNO SEIZOHO
JPS5924649A (en) * 1982-08-02 1984-02-08 Kokka Kogyo Kk Rubber belt and forming process thereof
JPS6071009A (en) * 1983-09-26 1985-04-22 Sanyo Chem Ind Ltd Preparation of substance having flocculation activity
JPS63126596A (en) * 1986-11-14 1988-05-30 Agency Of Ind Science & Technol Decoloring method for soluble dye by microorganism

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000140509A (en) * 1998-11-16 2000-05-23 Kansai Kako Kk Novel flocculant and sludge treatment using the same
JP2019026763A (en) * 2017-07-31 2019-02-21 甲陽ケミカル株式会社 Composition for organic matter flocculation containing regenerated chitosan
CN108660178A (en) * 2018-07-19 2018-10-16 佛山皖阳生物科技有限公司 A kind of preparation method of high flocculating rate microbial flocculant

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