JPH07108216B2 - Microorganism-produced flocculant and wastewater flocculation method - Google Patents
Microorganism-produced flocculant and wastewater flocculation methodInfo
- Publication number
- JPH07108216B2 JPH07108216B2 JP4270755A JP27075592A JPH07108216B2 JP H07108216 B2 JPH07108216 B2 JP H07108216B2 JP 4270755 A JP4270755 A JP 4270755A JP 27075592 A JP27075592 A JP 27075592A JP H07108216 B2 JPH07108216 B2 JP H07108216B2
- Authority
- JP
- Japan
- Prior art keywords
- strain
- kym
- genus
- wastewater
- ferm
- 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.)
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Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Activated Sludge Processes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は微生物産生凝集剤及び排
水凝集処理方法に関し、更に詳しくは活性汚泥法等によ
る排水凝集処理方法において新規な微生物産生凝集剤を
用いて活性汚泥のバルキングを防止して活性汚泥と処理
水との分離を効率的に行う排水凝集処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a microbial-produced flocculant and a wastewater flocculation treatment method, and more specifically, in a wastewater flocculation treatment method such as an activated sludge method, a novel microbial-produced flocculant is used to prevent bulking of activated sludge. The present invention relates to a wastewater coagulation treatment method for efficiently separating activated sludge from treated water.
【0002】[0002]
【従来の技術及びその問題点】従来、各種有機物を含む
排水の処理方法として活性汚泥方式が広く使用されてい
る。この活性汚泥方式は効率の高い処理方法であり、良
質な処理水が経済的に得られることから最も広く普及し
ている処理方法である。2. Description of the Related Art Conventionally, an activated sludge system has been widely used as a method for treating wastewater containing various organic substances. This activated sludge system is a highly efficient treatment method, and is the most widely used treatment method because it produces high quality treated water economically.
【0003】上記活性汚泥方式において残された最も重
要な問題は、処理後の処理水と活性汚泥との分離であ
り、処理水と活性汚泥とは沈澱槽である分離領域におい
て活性汚泥が速やかに沈降分離することが望ましいが、
分離領域において静置時に糸状菌等の発生によるバルキ
ング現象やデフロック現象が生じて活性汚泥の凝集フロ
ック作用が低下し、活性汚泥の沈降分離が不十分とな
り、活性汚泥の流出という問題が生じる。The most important problem remaining in the activated sludge system is the separation of the treated water and the activated sludge after treatment, and the treated water and the activated sludge are rapidly separated in the separation area which is a settling tank. It is desirable to separate by sedimentation,
In the separation area, a bulking phenomenon or a deflocculation phenomenon occurs due to the generation of filamentous fungi or the like when standing still, and the flocculating floc action of the activated sludge is reduced, and the sedimentation and separation of the activated sludge becomes insufficient, causing a problem of the activated sludge outflow.
【0004】活性汚泥と処理水との分離を促進させる方
法として、カチオンポリマー等の高分子凝集剤や多価金
属イオン等の無機凝集剤を使用する方法が知られている
が、これらの凝集剤は生物分解性が不十分である為、処
理水と共に放水されることにより環境汚染の問題が派生
する。従って本発明の目的は、排水凝集処理方法におい
て、活性汚泥のバルキング現象を生じることなく効率的
に活性汚泥を分離することが出来る微生物産生凝集剤及
び排水凝集処理方法を提供することである。As a method for promoting the separation of activated sludge and treated water, a method of using a polymer flocculant such as a cationic polymer or an inorganic flocculant such as a polyvalent metal ion is known. These flocculants are known. Since its biodegradability is insufficient, the problem of environmental pollution is caused by being discharged together with the treated water. Therefore, an object of the present invention is to provide a microbial-produced flocculant and a effluent flocculation method capable of efficiently separating activated sludge without causing the bulking phenomenon of activated sludge in the effluent flocculation treatment method.
【0005】[0005]
【問題点を解決する為の手段】上記目的は以下の本発明
によって達成される。即ち、本発明は、シュウドモナス
属シュウドモナス・フルオレセンスKYM−1株(FERM
P-11333) 又はシュウドモナス・セパシアKYM−2株
(FERM P-11334) 、アシネトバクター属、アグロバクテ
リウム属アグロバクテリウムKYM−4株(FERM P-113
36) 、エンテロバクター属、オーレオバクテリウム属及
びオエルスコビア属からなる群から選ばれる少なくとも
1属又は1属を含むことを特徴とする凝集剤産生微生物
の培養物又は培養処理物を主成分とする微生物産生凝集
剤、該微生物産生凝集剤を懸濁物含有排水に接触せしめ
ることを特徴とする排水凝集処理方法、及び活性汚泥方
法による排水凝集処理方法において、上記微生物産生凝
集剤を処理系に存在させ、活性汚泥と処理水との分離領
域において、活性汚泥のバルキングを防止することを特
徴とする排水凝集処理方法である。The above object can be achieved by the present invention described below. That is, the present invention relates to Pseudomonas fluorescens KYM-1 strain (FERM).
P-11333) or Pseudomonas cepacia KYM-2 strain (FERM P-11334), Acinetobacter genus, Agrobacterium genus Agrobacterium KYM-4 strain (FERM P-113
36), containing as a main component a culture or a culture-treated product of a flocculant-producing microorganism characterized by containing at least one genus or one genus selected from the group consisting of Enterobacter, Aureobacteria and Oerscovia. Microorganism producing flocculant, in the wastewater flocculating treatment method characterized by contacting the microorganism producing flocculant with the suspension-containing wastewater, and the wastewater flocculating treatment method by the activated sludge method, the microorganism producing flocculant is present in the treatment system In the separation area of activated sludge and treated water, the activated sludge is prevented from bulking.
【0006】[0006]
【作用】活性汚泥を用いる排水凝集処理方法において、
凝集物質生産菌として新規な菌が産生する凝集剤を使用
することによって、バルキング現象の主たる原因である
糸状菌の発生が抑制され、活性汚泥と処理水との分離が
効率的となる。更に好ましい実施態様では分離領域のp
Hを特定の範囲とすることによって活性汚泥と処理水の
分離が著しく促進される。[Function] In a wastewater coagulation treatment method using activated sludge,
By using a flocculant produced by a new bacterium as a flocculant-producing bacterium, the generation of filamentous fungi, which is the main cause of the bulking phenomenon, is suppressed, and the separation of activated sludge and treated water becomes efficient. In a further preferred embodiment, the isolation region p
By setting H to a specific range, the separation of activated sludge and treated water is significantly promoted.
【0007】[0007]
【好ましい実施態様】次に好ましい実施態様を挙げて本
発明を更に詳しく説明する。本発明者は、公知の多数の
凝集剤産生菌ロードコッカス・エリスロポレスをフラク
トース培地で培養し、その凝集効果(力値)を測定して
行く過程で、力価が通常の2倍以上上昇する培養液が存
在することを見出した。この培養液には数種の菌が混在
しており、これらの菌を分離したところ、特に優れた力
価を示す菌を発見した。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in more detail with reference to the preferred embodiments. The present inventor cultivates a large number of known flocculant-producing bacteria Rhodococcus erythropoles in a fructose medium, and in the process of measuring the flocculating effect (potency value), a culture in which the titer increases more than twice as much as usual. It was found that liquid was present. Several kinds of bacteria were mixed in this culture solution, and when these bacteria were separated, a bacteria showing a particularly excellent titer was found.
【0008】上記本発明の凝集剤産生菌は、シュウドモ
ナス属シュウドモナス・フルオレセンスKYM−1株
(FERM P-11333) 又はシュウドモナス・セパシアKYM
−2株(FERM P-11334) 、アシネトバクター属、アグロ
バクテリウム属アグロバクテリウムKYM−4株(FERM
P-11336) 、エンテロバクター属、オーレオバクテリウ
ム属及びオエルスコビア属からなる群から選ばれる少な
くとも1属に属する凝集剤生産能を有する菌であり、従
来公知のロードコッカス・エリスロポレスKR−256
−2、FERM−PNo. 3923及びロードコッカス・
エリスロポレスKR−S−1、FERM−P No.353
0等とは異なる属に属し、その凝集能力はこれらの公知
菌の2〜3倍或いはそれ以上である。The above flocculant-producing bacterium of the present invention is Pseudomonas fluorescens KYM-1 strain (FERM P-11333) or Pseudomonas cepacia KYM.
-2 strain (FERM P-11334), Acinetobacter genus, Agrobacterium genus Agrobacterium KYM-4 strain (FERM P-11334)
P-11336), a bacterium belonging to at least one genus selected from the group consisting of the genus Enterobacter, the genus Aureobacterium, and the genus Oerscovia, and having the ability to produce a flocculant, which is a conventionally known Rhodococcus erythropoles KR-256
-2, FERM-P No. 3923 and Road Coccus
Erythropoles KR-S-1, FERM-P No.353
It belongs to a genus different from 0, and its aggregating ability is 2-3 times or more than those of these known bacteria.
【0009】これらの属のうち、シュウドモナス属シュ
ウドモナス・フルオレセンスKYM−1株又はシュウド
モナス・セパシアKYM−2株、アシネトバクター属、
アグロバクテリウム属アグロバクテリウムKYM−4株
(FERM P-11336) 、エンテロバクター属、オーレオバク
テリウム属及びオエルスコビア属からなる群から選ばれ
る少なくとも1属を含む微生物群を本発明ではR−3と
称しているが、夫々既に微工研菌寄第11333号(FER
M P-11333)、同第11334号(FERM P-11334)、同第1
1335号(FERM P-11335)、同第11336号(FERM P-
11336)、同第11337号(FERM P-11337)、同第113
57号(FERM P-11357)及び同第11358号(FERM P-11
358)として寄託されている。上記凝集剤産生新規微生物
は、以下の菌学的性質を有している。Of these genera, Pseudomonas sp. Pseudomonas fluorescens KYM-1 strain or Pseudomonas cepacia KYM-2 strain, Acinetobacter spp.
In the present invention, a microorganism group containing at least one genus selected from the group consisting of Agrobacterium genus Agrobacterium KYM-4 strain (FERM P-11336), Enterobacter genus, Aureobacterium genus and Oerscovia genus is R-3 in the present invention. However, each of them has already been published by Micro Inst.
No. 11334), No. 11334 (FERM P-11334), No. 1
No. 1335 (FERM P-11335), No. 11336 (FERM P-
11336), No. 11337 (FERM P-11337), No. 113.
No. 57 (FERM P-11357) and No. 11358 (FERM P-11
358). The above flocculant-producing novel microorganism has the following mycological properties.
【0010】[0010]
【表1】 [Table 1]
【0011】[0011]
【表2】(表1の続き) [Table 2] (Continued from Table 1)
【0012】[0012]
【表3】(表1の続き) [Table 3] (Continued from Table 1)
【0013】[0013]
【表4】(表1の続き) [Table 4] (Continued from Table 1)
【0014】上記第1表に示す菌学的性質について、細
菌の同定書であるバージー・マニュアル・システマチッ
ク・バクテオロジー第1、2巻(Bergey's Manualof Sys
tematic Bacteriology Volume 1、2)、 (1984 年) で検討
した結果、KYM−1株は同書165頁に記載されてい
るシュウドモナス・フルオレセンスと一致し、KYM−
1株はシュウドモナス・フルオレッセンスと同定し、微
工研菌寄第11333号(FERM P-11333)として寄託され
ている。KYY−2株は同書175頁記載のシュウドモ
ナス・セパシアと考えると妥当であり、微工研菌寄第1
1334号(FERM P-11334)として寄託されている。KY
M−3株は同書303頁記載のアシネトバクター属細菌
と一致し、微工研菌寄第11335号(FERM P-11335)と
して寄託されている。Regarding the mycological properties shown in Table 1 above, Bergey's Manual of System of Bacteriological Bacteology Vol.
Temic Bacteriology Volume 1, 2), (1984), the KYM-1 strain was consistent with Pseudomonas fluorescens described on page 165 of the same document, and KYM-
One strain was identified as Pseudomonas fluorescens and has been deposited as Microindustrial Research Institute No. 11333 (FERM P-11333). The KYY-2 strain is appropriate when considered to be Pseudomonas cepacia described on page 175 of the same document, and is based on
Deposited as 1334 (FERM P-11334). KY
The M-3 strain is consistent with the bacterium of the genus Acinetobacter described on page 303 of the same document, and has been deposited as Microindustrial Research Institute No. 11335 (FERM P-11335).
【0015】KYM−4株は同書254頁記載のアグロ
バクテリウム・レイデオバクターと殆ど記載は一致する
ものの、糖の資化性等細かい点で少し異なるので同種の
近縁類と考えるのが分類学的に妥当であり、本菌は微工
研菌寄第11336号(FERMP-11336)として寄託されて
いる。KYM−5株は同書465頁記載のエンテロバク
ター属細菌と属レベルで完全に一致し、微工研菌寄第1
1337号(FERM P-11337)として寄託されている。KY
M−6株は同書1323頁記載のオーレオバクテリウム
属細菌、KYM−7株は同書1489頁記載のオエルス
コビア属細菌と夫々属レベルの記載は一致する。KYM
−6株は、微工研菌寄第11357号(FERM P-11357)、
KYM−7株は、微工研菌寄第11358号(FERM P-11
358)として夫々寄託されている。Although the description of KYM-4 strain is almost the same as that of Agrobacterium reideobacter described on page 254 of the same document, it is classified as a related species because it is slightly different in details such as sugar assimilation. It is scientifically valid, and this bacterium has been deposited as Microorganism Research Institute No. 11336 (FERMP-11336). The KYM-5 strain was completely in genus level with the Enterobacter bacteria described on page 465 of the same document, and was
Deposited as 1337 (FERM P-11337). KY
The M-6 strain is the same as the aureobacterium bacterium described on page 1323 of the same document, and the KYM-7 strain is the same as the Oerscovia bacterium described on page 1489 of the same document at the genus level. KYM
-6 strain is Microcosm Institute of Microbiology No. 11357 (FERM P-11357),
The KYM-7 strain is microbial strain No. 11358 (FERM P-11
358), respectively.
【0016】本発明の凝集剤は、以上の少なくとも1属
を含む微生物の培養物又は培養処理物を主成分とするも
のであって、培養液そのもの、その濃縮物、濾液、その
濾過残渣、それらの乾燥物等いずれの形態でもよい。
又、上記凝集剤にはカルシウムイオン等のカチオン性無
機塩を1種以上含有させたり、或いは使用時に含有させ
ることによって、それらの凝集能を更に向上させること
が出来る。本発明の排水凝集処理方法の特徴は、上記の
凝集剤を少なくとも1種以上使用にする点であり、適用
される排水は懸濁物を含むいずれの排水でもよいが、特
に活性汚泥を使用する排水凝集処理方法において、活性
汚泥と処理水との分離領域においてバルキングの主たる
原因となる糸状菌の発生及びその増殖が抑えられる。従
って本発明は処理水中において糸状菌が発生し易い排水
の処理に特に有効である。The flocculant of the present invention is mainly composed of a culture or a culture-treated product of the above-mentioned microorganism containing at least one genus, and the culture solution itself, a concentrate thereof, a filtrate, a filtration residue thereof, and the like. Any form such as dried product of
In addition, the aggregating ability can be further improved by incorporating one or more cationic inorganic salts such as calcium ions into the aggregating agent or by incorporating them at the time of use. The feature of the wastewater coagulation treatment method of the present invention is that at least one kind of the above-mentioned coagulant is used, and the wastewater to be applied may be any wastewater containing a suspended matter, but particularly activated sludge is used. In the wastewater coagulation treatment method, generation and growth of filamentous fungi, which are the main cause of bulking, can be suppressed in the separation area between activated sludge and treated water. Therefore, the present invention is particularly effective for treating wastewater in which filamentous fungi are easily generated in treated water.
【0017】微生物を使用する活性汚泥方式による排水
凝集処理方法自体は周知であり、本発明はこれらの周知
のいずれの排水凝集処理方法においても応用することが
出来るものであり、特に限定されない。本発明の好まし
い実施態様では、活性汚泥と処理水とを分離すべき分離
領域におけるpHを7〜9、特に好ましくは8.0〜
8.5の範囲とすることによって一層優れた力値が得ら
れる。本発明において凝集剤の添加量を培養液として
0.5重量%以上、好ましくは0.5〜10重量%とす
る。凝集剤の濃度が10%を越えて添加しても添加量に
応じて力値が向上するものでもなかった。The method for effluent coagulation treatment by the activated sludge system using microorganisms is well known, and the present invention can be applied to any of these well-known effluent coagulation treatment methods and is not particularly limited. In a preferred embodiment of the present invention, the pH in the separation area where the activated sludge and the treated water are to be separated is 7 to 9, particularly preferably 8.0.
By setting it in the range of 8.5, a more excellent force value can be obtained. In the present invention, the amount of the aggregating agent added is 0.5% by weight or more, preferably 0.5 to 10% by weight, as a culture solution. Even if the coagulant concentration was added in excess of 10%, the strength value did not improve depending on the amount added.
【0018】[0018]
【実施例】従来公知のロードコッカス・エリスロポレス
と、本発明での凝集剤産生菌の夫々の培養液を下記の液
体培地で30℃で振とう培養した。尚、R−1菌は従来
公知のロードコッカス・エリスロポレスであり、本発明
のR−3菌はKYM−1株(FERM P-11333)、KYM−2
株(FERM P-11334)、KYM−3株(FERM P-11335)、KY
M−4株(FERM P-11336)、KYM−5株(FERM P-1133
7)、KYM−6株(FERM P-11357)及びKYM−7株(FER
M P-11358)からなっている。Example A culture solution of each of the conventionally known Rhodococcus erythropoles and the flocculant-producing bacterium of the present invention was shake-cultured at 30 ° C. in the following liquid medium. The R-1 bacterium is a conventionally known Rhodococcus erythropoles, and the R-3 bacterium of the present invention is a KYM-1 strain (FERM P-11333), KYM-2.
Strain (FERM P-11334), KYM-3 strain (FERM P-11335), KY
M-4 strain (FERM P-11336), KYM-5 strain (FERM P-1133)
7), KYM-6 strain (FERM P-11357) and KYM-7 strain (FER
M P-11358).
【0019】液体培地の組成 炭素源 10g/l K2HPO4 5g/l KH2PO4 2g/l MgSO4 0.2g/l (NH4)2SO4 0.5g/l イースト抽出物 0.5g/l NaCl 0.1g/l Composition of liquid medium Carbon source 10 g / l K 2 HPO 4 5 g / l KH 2 PO 4 2 g / l MgSO 4 0.2 g / l (NH 4 ) 2 SO 4 0.5 g / l yeast extract 5 g / l NaCl 0.1 g / l
【0020】(1)力価 (a)供試液 前記液体培地の炭素源としてフラクトースを使用し、p
Hを8.5に調整した培地で5日間振とう培養した培養
液を供試液とした。温度は30℃とした。 (b)力値の評価法 100mlのメスシリンダーに、カオリン5000mg
/l(リットル)液を80ml入れ、無機カオリンと培
養液を所定量添加し、緩やかに転倒撹拌した後、0.5
NのNaOH及びHClでpH7.0にpHを調整し
た。蒸留水で全量を100mlとし、再度転倒撹拌後、
静置し5分後の上澄水のOD550 を測定し、1/D550
にて凝集力価を表示した。(1) Titer (a) Test solution Using fructose as a carbon source of the liquid medium, p
A culture solution obtained by shaking culture for 5 days in a medium in which H was adjusted to 8.5 was used as a test solution. The temperature was 30 ° C. (B) Evaluation method of force value 5000 mg of kaolin was added to a 100 ml measuring cylinder.
/ L (liter) liquid was added to 80 ml, a predetermined amount of inorganic kaolin and the culture liquid were added, and the mixture was gently inverted and stirred, and then 0.5
The pH was adjusted to pH 7.0 with N NaOH and HCl. Bring the total volume to 100 ml with distilled water, repeat stirring by inversion,
The OD 550 of the supernatant water after 5 minutes of standing was measured, and 1 / D 550
The cohesive titer was displayed at.
【0021】R−1菌及びR−3菌の凝集力価の経日変
化は図1に示す通りであった。以上の通り本発明におけ
るR−3菌は他の菌に比較して著しく優れた力価を示
す。尚、R−1が従来公知のロードコッカス・エリスロ
ポレス菌である。 (2)凝集時のpH 凝集時のpHを5〜10に調整し、最適凝集pHについ
て検討した。図2に示す様にpHが5から8に上昇する
に従いOD550 が低下し、それ以上のpHではOD550
が上昇し、培養液の最適凝集pHは8.0〜8.5であ
ることが明らかとなった。The daily changes in the agglutination titers of the R-1 and R-3 bacteria were as shown in FIG. As described above, the R-3 bacterium in the present invention exhibits a remarkably excellent titer as compared with other bacteria. Incidentally, R-1 is a conventionally known Rhodococcus erythropoles bacterium. (2) pH during aggregation The pH during aggregation was adjusted to 5 to 10 and the optimum aggregation pH was examined. OD 550 is decreased as pH as shown in FIG. 2 rises from 5 8, OD 550 in more pH
It was revealed that the optimum aggregation pH of the culture solution was 8.0 to 8.5.
【0022】[0022]
【効果】以上説明の様に、本発明によれば、活性汚泥を
用いる排水凝集処理方法において、凝集物質産生菌とし
て新規な菌が産生する凝集剤を使用することによって、
バルキング現象の主たる原因である糸状菌の発生が抑制
され、活性汚泥と処理水との分離が効率的となる。更に
好ましい実施態様では分離領域のpHを特定の範囲とす
ることによって活性汚泥と処理水の分離が著しく促進さ
れる。[Effects] As described above, according to the present invention, in a wastewater coagulation treatment method using activated sludge, by using a flocculant produced by a novel bacterium as a flocculant-producing bacterium,
The generation of filamentous fungi, which is the main cause of the bulking phenomenon, is suppressed, and the separation of activated sludge and treated water becomes efficient. In a further preferred embodiment, the pH of the separation area is set to a specific range, whereby the separation of activated sludge and treated water is significantly promoted.
【0023】[0023]
【図1】凝集力価と経過日数との関係を示す図。FIG. 1 is a graph showing the relationship between agglutination titer and the number of days elapsed.
【図2】凝集力価とpHとの関係を示す図。FIG. 2 is a graph showing the relationship between agglutination titer and pH.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C12R 1:01) 審査官 佐伯 裕子 (56)参考文献 特公 昭52−31434(JP,B1) 植村定次郎他著「発酵と微生物▲III ▼」(株)朝倉書店(昭45.10.10)P. 135−166─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display area C12R 1:01) Examiner Yuko Saeki (56) References Japanese Patent Publication No. 52-31434 (JP, B1) Uemura Sadajiro et al., "Fermentation and Microorganisms III", Asakura Shoten Co., Ltd. (Sho 45.10.10) P. 135-166
Claims (7)
オレセンスKYM−1株(FERM P-11333) 又はシュウド
モナス・セパシアKYM−2株(FERM P-11334) 、アシ
ネトバクター属、アグロバクテリウム属アグロバクテリ
ウムKYM−4株(FERM P-11336) 、エンテロバクター
属、オーレオバクテリウム属及びオエルスコビア属から
なる群から選ばれる少なくとも1属又は1種を含むこと
を特徴とする凝集剤産生微生物の培養物又は培養処理物
を主成分とする微生物産生凝集剤。1. A Pseudomonas sp. Pseudomonas fluorescens KYM-1 strain (FERM P-11333) or a Pseudomonas cepacia KYM-2 strain (FERM P-11334), Acinetobacter sp., Agrobacterium sp. Agrobacterium KYM-4. Strain (FERM P-11336), Enterobacter, Genus Aureobacterium and Oelscovia genus, and at least one genus or one species selected from the group, or a culture or treated culture product of a flocculant-producing microorganism characterized by the above-mentioned. A microbe-produced flocculant containing as a main component.
KYM−3株(FERMP-11335) であり、エンテロバクタ
ー属がエンテロバクターKYM−5株(FERMP-11337)
であり、オーレオバクテリウム属がオーレオバクテリウ
ムKYM−6株(FERM P-11357) であり、オエルスコビ
ア属がオエルスコビアKYM−7株(FERM P-11358) で
ある請求項1に記載の微生物産生凝集剤。2. The Acinetobacter genus is Acinetobacter KYM-3 strain (FERMP-11335), and the Enterobacter genus is Enterobacter KYM-5 strain (FERMP-11337).
The microbial production according to claim 1, wherein the genus Aureobacterium is the strain Aureobacterium KYM-6 (FERM P-11357), and the genus Oerscovia is the strain Oerscovia KYM-7 (FERM P-11358). Flocculant.
求項1又は2に記載の微生物産生凝集剤。3. The microorganism-producing flocculant according to claim 1, which contains one or more cationic inorganic salts.
を懸濁物含有排水に接触せしめることを特徴とする排水
凝集処理方法。4. A wastewater coagulation treatment method, which comprises contacting the microbial-produced coagulant according to claim 1 with a suspension-containing wastewater.
おいて、請求項1〜3に記載の微生物産生凝集剤を処理
系に存在させ、活性汚泥と処理水との分離領域におい
て、活性汚泥のバルキングを防止することを特徴とする
排水凝集処理方法。5. In a wastewater coagulation treatment method using an activated sludge method, the microorganism-produced coagulant according to any one of claims 1 to 3 is present in a treatment system, and bulking of the activated sludge is performed in a separation area between activated sludge and treated water. A method for aggregating wastewater, which is characterized by preventing it.
保持する請求項4又は5に記載の排水凝集処理方法。6. The wastewater coagulation treatment method according to claim 4, wherein the pH of the separation area of the activated sludge is maintained at 7 to 9.
ある請求項5又は6に記載の排水凝集処理方法。7. The wastewater coagulation treatment method according to claim 5 or 6, wherein the wastewater to be treated is wastewater that easily generates filamentous fungi.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4270755A JPH07108216B2 (en) | 1992-09-16 | 1992-09-16 | Microorganism-produced flocculant and wastewater flocculation method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4270755A JPH07108216B2 (en) | 1992-09-16 | 1992-09-16 | Microorganism-produced flocculant and wastewater flocculation method |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2083078A Division JPH0661B2 (en) | 1990-03-30 | 1990-03-30 | Flocculant-producing microorganism |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0746981A JPH0746981A (en) | 1995-02-21 |
| JPH07108216B2 true JPH07108216B2 (en) | 1995-11-22 |
Family
ID=17490537
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4270755A Expired - Fee Related JPH07108216B2 (en) | 1992-09-16 | 1992-09-16 | Microorganism-produced flocculant and wastewater flocculation method |
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| Country | Link |
|---|---|
| JP (1) | JPH07108216B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS582850B2 (en) * | 1975-09-01 | 1983-01-19 | 株式会社ボッシュオートモーティブ システム | Shyariyouyoureibo Sochi |
-
1992
- 1992-09-16 JP JP4270755A patent/JPH07108216B2/en not_active Expired - Fee Related
Non-Patent Citations (1)
| Title |
|---|
| 植村定次郎他著「発酵と微生物▲III▼」(株)朝倉書店(昭45.10.10)P.135−166 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0746981A (en) | 1995-02-21 |
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