JPH064123B2 - Microorganism-derived aggregating agent and aggregating method - Google Patents
Microorganism-derived aggregating agent and aggregating methodInfo
- Publication number
- JPH064123B2 JPH064123B2 JP63240438A JP24043888A JPH064123B2 JP H064123 B2 JPH064123 B2 JP H064123B2 JP 63240438 A JP63240438 A JP 63240438A JP 24043888 A JP24043888 A JP 24043888A JP H064123 B2 JPH064123 B2 JP H064123B2
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- Prior art keywords
- culture
- flocculant
- aggregating
- wastewater
- solution
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- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
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) Field of Industrial Application The present invention relates to a flocculant derived from microorganisms and a flocculation method, and is applicable to various pollutants, various industrial wastewater treatment fields, municipal wastewater, various It is expected to be used in a wide range of applications such as fermentation liquor treatment, oil turbidity treatment, and recovery and utilization 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
は微生物が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/年、カチオン系合成高分子系凝集剤で
9,000トン/年と言われている。2) Prior art Flocculants are widely used in various processes and wastewater fields discharged from them in accordance with the progress of various industries. Flocculants are generally classified into synthetic polymer type (for example, polyacrylamide type), inorganic type flocculants (for example, sulfuric acid band), and biological type flocculants. Among them, the microorganism (production) flocculant is a substance produced by the microorganism and has a property of facilitating the precipitation (precipitation) of other substances by aggregating. Also, from the viewpoint of function, they can be classified into three categories: cationic, nonionic, and anionic. The amount of flocculants produced in Japan is 15,000 tons / year for anionic / nonionic synthetic polymer flocculants, and for cationic synthetic polymer flocculants.
It is said to be 9,000 tons / year.
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。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。Heretofore, these synthetic polymer-based and inorganic-based flocculants have been widely used as clarification treatment agents from the field of wastewater treatment using the activated sludge method or the like to civil engineering dredging work and the like. In addition, the use of coagulants over a very wide range of fields, such as waterworks, waterworks in the field of waterworks, downstream processing fields such as fermentation liquid separation in the fermentation industry and further application to the food industry field Is expected. As described above, since the use of the coagulant is deeply incorporated into today's social life and is indispensable, it is expected that the use will increase even more and more in the future. Therefore, it is considered that the use of the flocculant is directly connected to the environment and human health. However, it is said that synthetic polymer flocculants (eg, polyacrylamide) which are widely used at present are excellent in capacity and economical efficiency, but have been pointed out to have problems in safety and environment. . Furthermore, the use of synthetic polymeric flocculants is considered to be problematic when considering their application to downstream processing in bioindustry.
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
待高まっていた。The development of new flocculants that overcomes and overcomes these drawbacks has been earnestly desired by various parties, and in particular, expectations are high for the development of bioflocculating flocculants that are biodegradable, safe, and free from the risk of secondary pollution. Was there.
ところで、微生物産生凝集剤についてはグラム陽性細菌
に属するロードコッカス属由来の微生物産生凝集剤NO
C−1(日本特許第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 the microorganism-producing flocculant, the microorganism-producing flocculant NO derived from the genus Rhodococcus belonging to Gram-positive bacteria NO
C-1 (Japanese Patent No. 1,096,062) is already known and effective as a flocculant, but a higher yield of microbial-produced flocculant 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
グ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、グラム陰性細菌のアル
カリゲネス・レータス(Alcaligenes latus)B−16株(F
ERM BP-2015号)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つ高い収率で凝集剤
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 Against this background, the present inventors have widely used microorganisms, particularly microorganisms caused by Gram-negative bacteria, in order to solve or overcome the problems of the polymer-based flocculant and the like. A search was performed for a producing flocculant. That is, a safe coagulant having excellent safety and biodegradability and having no fear of secondary pollution, and its coagulating method,
As a result of repeated research and development, the Gram-negative bacterium Alcaligenes latus strain B-16 (F
ERM BP-2015) It has an excellent flocculating effect in the presence of a culture, a culture-treated product, or an inorganic salt or at least one of natural flocculants and that a flocculant can be obtained in a high yield. Heading out, the present invention has been completed.
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、
アルカリゲネス・レータス(Alcaligenes latus)B−16
株で、FERM BP-2015号として寄託されている。4) Means for Solving the Problems The strain used in the present invention belongs to the genus Alcaligenes,
Alcaligenes latus B-16
The stock has been deposited as FERM BP-2015.
以下、本発明に使用する菌株(FERM BP-2015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、
バージー・マニュアル・システマテック・バクテリオロ
ジー 第1巻(Bergey's Manual of Systematic Bacter
iology Volume 1),(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
(ATCC29712)においては、表1における ・デオキシリボヌクレアーゼ, ・クエン酸, ・アルギニンデハイドロラーゼ, ・アクリルアミダーゼ, ・糖より酸の生成, ・菌体外ポリマー生産能, 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。The mycological properties of the strain (FERM BP-2015) used in the present invention are shown in Table 1 below. From the mycological properties shown in Table 1,
Bergey's Manual of Systematic Bacter
Physiology Volume 1), (1984) p.372, it was found to belong to the genus Alcaligenes. In the type strain (ATCC29712), there is no description in Table 1 of "deoxyribonuclease,""citricacid,""argininedehydrolase,""acrylamidase,""production of acid from sugar,""production of extracellular polymer". The other strains have the same type strain as the strain of the present application.
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
及びオリーブ油等の油類の炭素源が好ましくは用いられ
る。さらに、尿素,塩安,硝安硫安等の無機体窒素源、
トリプトン,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。 As a carbon source of such strains, in addition to monosaccharides and oligosaccharides such as fructose, glucose and sucrose, carbon sources of natural polymers such as hemicellulose, starch, corn starch and oils such as olive oil are preferably used. To be In addition, inorganic nitrogen sources such as urea, ammonium chloride, ammonium nitrate and ammonium sulfate,
Organic nitrogen sources such as tryptone, yeast extract, meat extract, peptone, and malt extract, as well as inorganic salts such as potassium phosphate, magnesium sulfate, and salt are used as medium constituents.
培養は液体培養でもよい。培養は初発pHが4〜10、温度
15〜40℃の範囲で行われ、通常は通気攪拌培養で行なわ
れる。培養は炭素源等の種類にもよるが培養1日から1
0日間の間で行われ、この間で最大凝集活性時期が設定
される。The culture may be liquid culture. Culture has an initial pH of 4-10, temperature
It is carried out at a temperature in the range of 15 to 40 ° C., and usually aeration and agitation culture. Culture depends on the type of carbon source etc.
It is carried out for 0 days, during which the period of maximum aggregation activity is set.
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1,000〜15,000c
psである。粘度の測定は100倍の水(20℃)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 light yellow solid,
It is an anionic polymer and its viscosity is about 1,000-15,000c.
ps. To measure viscosity, add 100 times water (20 ℃),
Perform with a rotary viscometer while completely absorbing water.
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℃にて一夜放置し
た沈殿物をNo.2紙にて過を行い集め、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が
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。By performing the culture, a culture having an aggregating ability is obtained. Double the amount of ethanol was added to the culture solution, the precipitate was left overnight at 5 ° C, filtered with No.2 paper and collected, then 70%.
After washing with ethanol three times and further with distilled water three times on paper, the aggregated substances whose water has been removed by freeze-drying or the like can be recovered as a culture-treated product. However, in the present invention, the culture itself can be used as it is without using the culture-treated product thus separated and purified.
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
トサンが有利に用いられる。Further, as the inorganic salt used together for further promoting the aggregation effect, those capable of forming cations in water are desirable, and those capable of forming multivalent cations having two or more valences are preferable, for example, chlorination. Those that produce calcium ions such as calcium are advantageously used. As a natural flocculant used in combination, chitosan extracted from such as crab is advantageously used.
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って決められる
のが望ましく一般的に特に制約されるものではない。However, the added amounts of the inorganic salt and the natural flocculant used in combination are preferably determined depending on the kind of the object to be flocculated, and are not particularly limited in general.
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含んだコークス排水、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, the target of aggregation is not particularly limited. As a representative example, kaolin (white clay) suspension, which is a kind of clay as an inorganic material,
Coke wastewater containing poisonous substances such as phenol, coloring,
Examples include papermaking wastewater containing fine suspensions, and organic food wastewater. Generally, it is preferably carried out 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・レータスB−16株培養
物、又は培養処理物を加えるか、あるいは、各種懸濁液
に本発明によるアルカリゲネス・レータスB−16株培
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pHを中性から微アルカリ性にする場合も
あるが、特にpH調整を行わなくてもよい。The method of the present invention is generally carried out by adding the culture of Alcaligenes retus B-16 strain of the present invention or a culture-treated product to various suspensions, or by adding Alcaligenes of the present invention to various suspensions. -It is carried out by adding a culture or a culture-treated product of Rattus B-16 strain, and then adding an inorganic salt or a natural flocculant to be used in combination. There is no particular limitation on how to implement these. Further, the pH of the mixed solution at the time of aggregation may be changed from neutral to slightly alkaline, but it is not particularly necessary to adjust the pH.
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 agglutination activity of the suspension or the like according to the present invention is determined by measuring the absorbance of the treatment liquid, the COD measurement and the S
It was determined by the S (suspending fine solids) removal rate and the like.
(イ)吸光度による凝集活性測定法 本活性測定法は日本農業化学会誌欧文誌(Agric.Biol.C
hem.)50巻9号2310頁に記載されている倉根等の方法に
基づいて行った。すなわちカオリン5,000ppm懸濁液80ml
に20倍〜100倍に希釈した培養物(又は培養処理物)10m
lを加え、さらに塩化カルシウム10ml(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。(B) Method of measuring agglutination activity by absorbance This activity measuring method is based on the journal of the Japanese Society of Agricultural Chemistry (Agric.Biol.C).
hem.) Vol. 50, No. 9, page 2310, based on the method of Kurane et al. That is, kaolin 5,000ppm suspension 80ml
20m to 100x diluted culture (or culture processed product) 10m
After adding l, and further adding 10 ml (1%) of calcium chloride, the pH was adjusted to 7.0 and the reaction solution was allowed to stand for 5 minutes in a 100 ml graduated cylinder, and the absorbance of the supernatant of the treatment solution was measured at a wavelength of 550 nm.
Was measured by using a spectrophotometer. After measuring each absorbance, the aggregation activity (FA) was calculated by the following formula.
なお、コトロールのO.D.550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。 The OD 550 of Kotrol is the value of the absorbance at 0 hours of culture, that is, the medium was replaced with the above-mentioned culture, and all other conditions were the same as those described 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550nm
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 obtained by the method described above, but depending on the target wastewater, the wavelength of the absorbance measurement was 550 nm.
Was appropriately converted from each of the samples and measured at each most preferable wavelength.
(ロ)COD(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。(B) COD (Chemical Oxygen Demand) measurement of aggregation activity:
The COD was measured according to JIS standard.
(ハ)SS(Suspended Solid:微細懸濁
固体物)による凝集活性測定:SSは1μmのグラスフ
ィルター過残渣物の重量を測定することによって行っ
た。(C) Aggregation activity measurement by SS (Suspended Solid): SS was carried out by measuring the weight of 1 μm glass filter residue.
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 described in more detail with reference to Examples.
[実施例1] 〈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、K2HPO
44.4g、MgSO4・7H2O0.2g、食塩0.1g、尿
素0.5g、酵母エキス0.5gを蒸留水1に溶かし、培地
をpH7.2〜7.6に調整した。培地50mlを、300mlの三角フ
ラスコにとり、オートクレーブにより、120℃,15分間
無菌殺菌した後、アルカリゲネス・レータスB−16株
(FERM 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 1] <Culture of flocculant-producing bacterium and recovery of flocculant> Fructose 15 g, KH 2 PO 4 8.4 g, K 2 HPO
4 4.4g, MgSO 4 · 7H 2 O0.2g, salt 0.1 g, urea 0.5g, dissolved yeast extract 0.5g distilled water 1 was adjusted medium PH7.2~7.6. 50 ml of the medium was placed in a 300 ml Erlenmeyer flask and sterilized by autoclave at 120 ° C. for 15 minutes, and then Alcaligenes retus B-16 strain (FERM BP-2015) was transferred to the flask in an amount of 1 platinum loop. Rotary culture is performed at ℃. The rotation speed is
It 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660nm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 under the combined use of calcium chloride with the above-mentioned kaolin as an index. The growth of the cells was determined by measuring the turbidity at a wavelength of 660 nm.
結果を表2に示す。The results are shown in Table 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。 As is clear from Table 2, the present aggregating activity reaches its maximum in the logarithmic growth phase of the growth of the bacterium, and the activity decreases as it enters the stationary phase.
この最大凝集活性を示す3日目の培養液より、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℃にて一夜放置し沈殿物を得た。沈殿物をNo.
2の紙にて過を行い集め、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1当り約12g(乾燥重量)
の凝集物質を得た。Aggregated substances were recovered from the 3rd day culture medium showing the maximum aggregation activity. That is, twice the amount of ethanol of the culture solution was added and the mixture was left overnight at 5 ° C. to obtain a precipitate. Precipitate No.
After collecting with 2 paper, wash with 70% ethanol 3 times, wash with distilled water 3 times on paper, and then remove water by freeze-drying etc. Thing). By using the above medium by these operations, about 12 g (dry weight) per culture solution
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 preparation (aggregation substance) obtained in Example 1 was completely dissolved in a hot alkaline solution to prepare a 10% aqueous solution of aggregation substance.
5,000ppmカオリン懸濁液80mlに上記の10%凝集物質水溶
液を10ml加えゆるやかに混和し、さらに蒸留水10ml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。To 80 ml of a 5,000 ppm kaolin suspension, 10 ml of the above 10% aqueous solution of aggregating substance was added and gently mixed, 10 ml of distilled water was further added, and the mixture was gently mixed again, and then allowed to stand for 5 minutes for aggregation activity (F.
A.) was measured. For comparison, the measurement was carried out by using hot alkaline water containing no freeze-dried preparation as a control.
結果を表3に示す。The results are shown in Table 3.
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(FERM BP-2015号)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、カオリン懸濁液は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, Alcaligenes.
The kaolin suspension forms flocs after 5 minutes by adding the freeze-dried flocculent substance aqueous solution obtained by culturing the lethaces bacterium B-16 strain (FERM BP-2015), and the flocculated kaolin flocculates. It became clear that it would precipitate.
[実施例3] コークス工場排水は、炭化物の微細な懸濁物(SS)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SS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] The coke factory wastewater contains a very large amount of fine carbide suspensions (SS) and also contains toxic phenols, etc. It is said that the wastewater does not easily agglomerate, and has a high fine SS content and a high COD (chemical oxygen demand).
このコークス排水90ml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10ml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量と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 drainage, 10 ml of a 5 times diluted culture solution obtained in Example 1 was added, and then the reaction solution containing calcium chloride added to have a concentration of 1% was allowed to stand for 5 minutes. The SS amount and COD of the clear liquid were measured. As a control, 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, the fine carbonized suspension in the coke drainage was efficiently removed by coagulation sedimentation and COD in the coke drainage.
[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 coagulant solution was applied to a paper processing plant wastewater as a colored wastewater containing a dye and containing a large amount of organic fine suspension. This organic fine suspension is fine starch particles in the coated paper manufacturing process, and the dye is a blue dye for printing.
この排水90ml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10ml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。10 ml of a 5-fold dilution of the culture broth obtained in Example 1 was added to 90 ml of this waste water, and then extracted from the shells of crustaceans such as crabs as a natural flocculant, which was produced through a processing step. Chitosan was added at a concentration of 150 ppm, and the coagulation effect of the combined use of this coagulant and a natural coagulant was investigated. The results are shown in Table 5.
表5に示すように、天然系凝集剤の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
させることが可能になった。As shown in Table 5, it was not possible to coagulate and precipitate the fine suspension only with the natural coagulant chitosan, whereas it is possible to coagulate and precipitate with the coagulant and natural coagulant combination section. Became.
同時に波長600nm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 same colored wastewater was measured at a wavelength of 600 nm, a large decrease in the absorbance was observed in the combined use section, and as a result, the blue dye could also be removed by aggregation 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] As a representative example of organic wastewater, the coagulant-precipitation effect of the present coagulant on food factory wastewater was examined. This food factory wastewater is a wastewater containing a large amount of fine plant fiber suspension as the main component.
この食品工場排水80mlに対して実施例1で得られた培養
液の10倍希釈液10ml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100ppm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SS分及びCODを測定した。To 80 ml of this food factory wastewater, 10 ml of the 10-fold dilution of the culture solution obtained in Example 1 was added, and then calcium chloride solution was added to a final concentration of 1% or chitosan solution to a final concentration of 100 ppm for 5 minutes. The solution was allowed to stand and the SS content and COD of the reaction-treated solution (supernatant solution) 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。As a control, a 10-fold diluted medium in which the production strain was not inoculated 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細有機質懸濁物(SS)は効
率良く凝集沈殿することが確認された。As shown in Table 6, in a system to which a culture solution of the present flocculant-producing bacterium has been added, by using a cation (calcium chloride) or a natural flocculant chitosan together, fine organic matter in food wastewater, which is organic wastewater, can be obtained. It was confirmed that the suspension (SS) efficiently aggregated and precipitated.
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。In addition, COD in the wastewater is about
It became clear that a little less than a third can be eliminated.
[実施例6] ロードコッカス・エリスポレスの産出するNOC−1は
油濁エマルジョンに対してあまり有効でなかったため
に、固形性懸濁物ばかりでなく、油濁エマルジョンに対
しても、本凝集剤が凝集効果を示すかどうかについて検
討を加えた。 [Example 6] Since NOC-1 produced by Rhodococcus erythraceus was not very effective against oily emulsions, the present flocculant was applied to not only solid suspensions but also oily emulsions. A study was made as to whether or not the effect of aggregation was exhibited.
油濁エマルジョンは次のように調整した。まず、純水1
に対し、ヤシ油酸(商品名;花王LUNACL-50)2.5gを
加え、ホモゲナイザー(Janke & Kunkelgmbh社製,T
urrax D 7813型)にて毎分10,000回転にて10分間ホモゲ
ナイズさせることによりヤシ油酸エマルジョンを調整し
た。The oil suspension emulsion was prepared as follows. First, pure water 1
To the above, 2.5 g of palm oil acid (trade name; Kao LUNACL-50) was added, and a homogenizer (Janke & Kunkelgmbh, T
A coconut oil emulsion was prepared by homogenizing with a urrax D 7813 type) at 10,000 rpm for 10 minutes.
この調整したエマルジョン液90mlに対し実施例1により
得られた培養液の5倍希釈液10ml、ついでキトサンを最
終濃度100ppmになるように加え、100mlメスシリンダー
にてゆるやかに転倒攪拌を行い、5分間静置し、5分後
の処理液のCODを測定することにより、油濁エマルジ
ョンに対する凝集効果を調べた。なお、油濁エマルジョ
ンは水よりも比重が軽いため、凝集層は表面に浮上す
る。処理液は実施例1〜5と異り、下層に位置する。To 90 ml of this adjusted emulsion, 10 ml of a 5-fold dilution of the culture broth obtained in Example 1 and then chitosan were added to a final concentration of 100 ppm, and the mixture was gently stirred by inversion with a 100 ml graduated cylinder for 5 minutes. The coagulation effect on the oil suspension emulsion was examined by measuring the COD of the treatment liquid after standing for 5 minutes. Since the oily emulsion has a lower specific gravity than water, the aggregation layer floats on the surface. The treatment liquid is located in the lower layer unlike Examples 1 to 5.
結果を表7に示した。表7に示す如く、本凝集剤生産菌
培養液とキトサンを併用することにより、エマルジョン
は効果的に表面に浮上してくる。油類等が含まれている
排水処理においては一般的に活性汚泥処理にかける前
に、油分を加圧浮上させており、そのための電気代のコ
ストは相当なものと言われている。このような加圧浮上
の代りに本凝集剤を用いることも可能である。The results are shown in Table 7. As shown in Table 7, the combined use of the flocculant-producing fungal culture solution and chitosan effectively floats the emulsion on the surface. In the wastewater treatment containing oils and the like, the oil content is generally floated under pressure before being subjected to the activated sludge treatment, and it is said that the cost of electricity for that is considerable. It is also possible to use the present coagulant instead of such pressure floating.
6)発明の効果 以上より明らかのように、本発明の凝集剤及び凝集方法
を適用することにより、無機性から有機性までの各種懸
濁物や油濁エマルジョンなどの広い対象にわたって効果
的に凝集させうることが判明した。 6) Effects of the Invention As is clear from the above, by applying the flocculant and the flocculation method of the present invention, it is possible to effectively flocculate over a wide range of objects such as various suspensions from inorganic to organic and oil emulsions. It turned out to be possible.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 //(C12P 1/04 C12R 1:05) 7804−4B (72)発明者 野畑 靖浩 三重県四日市市別名6―6―9 伯東化学 株式会社中央研究所内 審査官 川上 美秀 (56)参考文献 特開 昭49−004685(JP,A) 特開 昭51−086189(JP,A) 特開 昭60−071009(JP,A) 特開 昭63−126596(JP,A) 特公 昭59−024649(JP,B2)─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI technical display location // (C12P 1/04 C12R 1:05) 7804-4B (72) Inventor Yasuhiro Nobata Yokkaichi, Mie Prefecture City 6-6-9 Examiner, Central Research Institute, Hakuto Kagaku Co., Ltd. Yoshihide Kawakami (56) Reference JP-A-49-004685 (JP, A) JP-A-51-086189 (JP, A) JP-A-60 -071009 (JP, A) JP 63-126596 (JP, A) JP 59-024649 (JP, B2)
Claims (4)
tus)B−16株(FERM BP-2015号)培養物又はその処理
物を主成分とする凝集剤。1. Alcaligenes lata
tus) B-16 strain (FERM BP-2015) A coagulant mainly composed of a culture or a treated product thereof.
種以上をさらに含有する請求項1の凝集剤。2. At least one of an inorganic salt or a natural flocculant.
The flocculant according to claim 1, further comprising one or more species.
物質と接触させて凝集する方法。3. A method of aggregating by bringing the aggregating agent according to claim 1 into contact with a substance to be treated.
物質と接触させて脱色する方法。4. A method of decolorizing a flocculating agent according to claim 1 by bringing it into contact with a substance to be treated.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63240438A JPH064123B2 (en) | 1988-09-26 | 1988-09-26 | Microorganism-derived aggregating agent and aggregating method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63240438A JPH064123B2 (en) | 1988-09-26 | 1988-09-26 | Microorganism-derived aggregating agent and aggregating method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0290903A JPH0290903A (en) | 1990-03-30 |
| JPH064123B2 true JPH064123B2 (en) | 1994-01-19 |
Family
ID=17059494
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63240438A Expired - Lifetime JPH064123B2 (en) | 1988-09-26 | 1988-09-26 | Microorganism-derived aggregating agent and aggregating method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH064123B2 (en) |
Families Citing this family (3)
| 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 |
| JP7071721B2 (en) * | 2017-07-31 | 2022-05-19 | 甲陽ケミカル株式会社 | Composition for organic matter aggregation 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 |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5511883B2 (en) * | 1972-05-08 | 1980-03-28 | ||
| 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 |
-
1988
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Also Published As
| Publication number | Publication date |
|---|---|
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