JPH03285676A - Flocculant-producing new microorganism and treatment of waste water - Google Patents
Flocculant-producing new microorganism and treatment of waste waterInfo
- Publication number
- JPH03285676A JPH03285676A JP2083078A JP8307890A JPH03285676A JP H03285676 A JPH03285676 A JP H03285676A JP 2083078 A JP2083078 A JP 2083078A JP 8307890 A JP8307890 A JP 8307890A JP H03285676 A JPH03285676 A JP H03285676A
- Authority
- JP
- Japan
- Prior art keywords
- ferm
- flocculant
- genus
- strain
- kym
- 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
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 29
- 244000005700 microbiome Species 0.000 title claims abstract description 21
- 239000010802 sludge Substances 0.000 claims abstract description 33
- 238000000034 method Methods 0.000 claims abstract description 31
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 16
- 238000005189 flocculation Methods 0.000 claims abstract description 13
- 230000016615 flocculation Effects 0.000 claims abstract description 13
- 238000000926 separation method Methods 0.000 claims abstract description 13
- 241000589516 Pseudomonas Species 0.000 claims abstract description 8
- 241000589540 Pseudomonas fluorescens Species 0.000 claims abstract description 4
- 241000589513 Burkholderia cepacia Species 0.000 claims abstract description 3
- 241000894006 Bacteria Species 0.000 claims description 29
- 238000005345 coagulation Methods 0.000 claims description 9
- 230000015271 coagulation Effects 0.000 claims description 9
- 241000588914 Enterobacter Species 0.000 claims description 8
- 241001467578 Microbacterium Species 0.000 claims description 8
- 241000589291 Acinetobacter Species 0.000 claims description 7
- 241000589158 Agrobacterium Species 0.000 claims description 6
- 125000002091 cationic group Chemical group 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 238000003672 processing method Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 6
- 230000035755 proliferation Effects 0.000 abstract description 3
- 239000000243 solution Substances 0.000 description 9
- 241000316848 Rhodococcus <scale insect> Species 0.000 description 5
- 230000004520 agglutination Effects 0.000 description 5
- 239000008394 flocculating agent Substances 0.000 description 5
- 238000004220 aggregation Methods 0.000 description 4
- 230000002776 aggregation Effects 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000005995 Aluminium silicate Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000005715 Fructose Substances 0.000 description 2
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 2
- 229930091371 Fructose Natural products 0.000 description 2
- 235000012211 aluminium silicate Nutrition 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 2
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000009897 systematic effect Effects 0.000 description 2
- 239000012085 test solution Substances 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 241001641159 bacterium R-3 Species 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- -1 calcium ions Chemical class 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 229920006317 cationic polymer Polymers 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000012258 culturing Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000012138 yeast extract Substances 0.000 description 1
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
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Activated Sludge Processes (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は凝集剤生産新規微生物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
法において新規な凝集剤生産菌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。Detailed Description of the Invention (Industrial Field of Application) The present invention relates to a new flocculant-producing microorganism and a wastewater flocculation treatment method, and more specifically, to a wastewater flocculation treatment method using an activated sludge method or the like using a novel flocculant-producing microorganism. The present invention relates to a wastewater coagulation treatment method that prevents bulking of activated sludge and efficiently separates activated sludge from treated water.
(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(普及している処理方法である。(Prior Art and its Problems) Conventionally, activated sludge systems have been widely used as a method for treating wastewater containing various organic substances. This activated sludge method is a highly efficient treatment method and is the most widely used treatment method because it can economically obtain high-quality treated water.
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 above activated sludge method is:
After treatment, the treated water and activated sludge are separated, and it is desirable that the activated sludge quickly settles and separates the treated water and activated sludge in the separation area, which is a settling tank. A bulking phenomenon and a differential lock phenomenon occur due to the generation of sludge, and the flocculation effect of the activated sludge is reduced, and the sedimentation and separation of the activated sludge becomes insufficient, resulting in the problem of activated sludge flowing out.
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。The use of polymeric flocculants such as cationic polymers and inorganic flocculants such as polyvalent metal ions is known as a method of promoting the separation of activated sludge and treated water, but these flocculants cannot be biodegraded. Due to insufficient properties, water is discharged together with treated water, leading to environmental pollution problems.
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凝集剤生産新規微生物及び
排水凝集処理方法を提供することである。Therefore, an object of the present invention is to provide a new flocculant-producing microorganism and a wastewater flocculation treatment method that can efficiently separate activated sludge without causing the activated sludge bulking phenomenon in the wastewater flocculation treatment method.
(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。(Means for solving problems) The above objects are achieved by the present invention as described below.
即ち、本発明は、シュウドモナス属、アシネトバクタ−
属、アグロバクテリウム属、エンテロバクタ−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属を含むことを特徴とする凝集
剤生産微生物、上記の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、
上記微生物又は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、上記の
微生物又は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。That is, the present invention is directed to the use of Pseudomonas, Acinetobacter
A flocculant-producing microorganism characterized by containing at least one genus selected from the group consisting of the genus Agrobacterium, the genus Enterobacter, the genus Aureobacterium, and the genus Oerscobia, a culture of the above microorganism, or a culture treatment. A microorganism-produced flocculant whose main component is a microbial coagulant, a wastewater coagulation treatment method characterized by bringing the microorganism or microbial-produced flocculant into contact with suspended matter-containing wastewater, and a wastewater coagulation treatment method using an activated sludge method. This wastewater flocculation treatment method is characterized in that microorganisms or microorganism-produced flocculants are present in the treatment system to prevent bulking of activated sludge in a region where activated sludge and treated water are separated.
(イ乍 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又は該菌が産生ずる凝集剤を使用
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。(For use) In a wastewater flocculation treatment method using activated sludge, the generation of filamentous bacteria, which is the main cause of the bulking phenomenon, can be suppressed by using new bacteria or flocculants produced by these bacteria as flocculant-producing bacteria. This makes the separation of activated sludge and treated water more efficient. In a further preferred embodiment, the separation region p
, H within a specific range, separation of activated sludge and treated water is significantly promoted.
(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。(Preferred Embodiments) Next, the present invention will be described in more detail by citing preferred embodiments.
本発明者は、公知の多数の凝集剤生産菌ロードコツカス
・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。The present inventor cultivated a large number of known flocculant-producing bacteria, Rhodococcus erythropores, in a fructose medium, and in the process of measuring the flocculation effect (power value), found that the titer was 2.
It has been found that there are culture solutions in which the increase is more than double. This culture solution contained several types of bacteria, and when these bacteria were separated, they discovered one that showed particularly high titer.
上記本発明の凝集剤生産菌は、シュウドモナス属、アシ
ネトバクタ−属、アグロバクテリウム属、エンテロバク
タ−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ツカス・
エリスロポレスKR−256−2、FERM−PNo、
3923及びロードコツカス・エリスロポレスKR−3
1、FERM−P No、3530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。これらの属のうち、シュウドモナス属、
アシネトバククー属、アクロバタテリウム属、エンテロ
バクタ−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(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11.333号(FERM P−113331
、同第1 ]−3334号FERM P−11334)
、同第11335号(FERMP−11335)、同第
11336号(FERM P−11336)、同第11
337号(FERM P−1,1337)、同第113
57号(FERM P−11357)及び同第1135
8号(FERM P1135g)として寄託されている
。The flocculant-producing bacteria of the present invention have a flocculant-producing ability that belongs to at least one genus selected from the group consisting of the genus Pseudomonas, the genus Acinetobacter, the genus Agrobacterium, the genus Enterobacter, the genus Aureobacterium, and the genus Oerscobia. It is a bacterium that has the
Erythropores KR-256-2, FERM-PNo,
3923 and Rhodococcus erythropores KR-3
It belongs to a different genus from 1, FERM-P No. 3530, etc., and its agglutination ability is 2 to 3 times or more than those of these known bacteria. Among these genera, Pseudomonas spp.
In the present invention, a group of microorganisms including one genus selected from the group consisting of Acinetobacterium, Acrobatherium, Enterobacter, Aureobacterium, and Oelscobia is referred to as R-3 in the present invention. FERM P-113331 has already been published.
, No. 1]-3334 FERM P-11334)
, same No. 11335 (FERMP-11335), same No. 11336 (FERM P-11336), same No. 11
No. 337 (FERM P-1, 1337), FERM No. 113
57 (FERM P-11357) and FERM P-1135
No. 8 (FERM P1135g).
上記凝集剤生産新規微生物は、以下の菌学的性質を有し
ている。The above flocculant-producing novel microorganism has the following mycological properties.
(以下余白)
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−・マニュアル・システマチック・バクチオ
ロジー第1.2巻(Bergey ’ sManual
of Systematic Bacteriolog
y 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−11,3331
として寄託されている。(Left below) The mycological properties shown in Table 1 above are described in Bergey's Manual Systematic Bactiology Volume 1.2, which is a bacterial identification book.
of Systematic Bacteriology
y Volume 1゜2), (1984), the KYM-1 strain is consistent with Pseudomonas fluorescens described on page 165 of the same book, and KYM-1
The strain was identified as Pseudomonas fluorescens and was published in FERM P-11,3331.
It has been deposited as.
KY’+’−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113
34号(FERM P−11334)として寄託されて
いる。It is reasonable to consider that the KY'+'-2 strain is Pseudomonas cepacia described on page 175 of the same book,
No. 34 (FERM P-11334).
KYM−3株は同書303頁記載のアシネトバクタ−属
細菌と一致し、微工研菌寄第11335号(FEBM
P−11335)として寄託されている。The KYM-3 strain corresponds to the Acinetobacter genus bacteria described on page 303 of the same book, and was published in FIKEN Bacteria No. 11335 (FEBM).
P-11335).
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、本圃は微工研菌寄第11
336号(FERM P11336)として寄託されて
いる。Although the description of the KYM-4 strain is almost identical to Agrobacterium leideobacter described on page 254 of the same book, there are slight differences in details such as sugar assimilation ability, so taxonomically it is best to consider it as a close relative of the same species. It is appropriate, and the main field is the 11th
No. 336 (FERM P11336).
KYM−5株は同書465頁記載のエンテロバクタ−属
細菌と属レベルで完全に一致し、微工研菌寄第1133
7号(FERM P−11337)として寄託されてい
る。The KYM-5 strain is completely identical at the genus level to the Enterobacter bacteria described on page 465 of the same book, and is
No. 7 (FERM P-11337).
KYM−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。The KYM-6 strain corresponds to the Aureobacterium genus bacteria described on page 1323 of the same book, and the KYM-7 strain corresponds to the Oerscobia genus bacteria described on page 1489 of the same book at the genus level.
KYM−6株は、微工研菌寄第11.357号(FER
M P−11357)、KYM−7株は、微工研菌寄第
11358号(FERM P−11358)として夫々
寄託されている。The KYM-6 strain was published in FER No. 11.357 (FER
M P-11357) and KYM-7 strains have been deposited as FERM P-11358 (FERM P-11358).
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。The flocculant of the present invention is mainly composed of a culture or cultured product of a microorganism containing at least one of the above genus,
It may be in any form such as the culture solution itself, its concentrate, its filtrate, its filtration residue, or its dried product.
1
2
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。1 2 Furthermore, the flocculating ability of the flocculant can be further improved by containing one or more cationic inorganic salts such as calcium ions, or by incorporating them at the time of use.
本発明の排水凝集処理方法の特徴は、上記の凝集剤生産
菌を少な(とも1種以上使用にする点であり、適用され
る排水は縣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 feature of the wastewater coagulation treatment method of the present invention is that it uses a small number of the above-mentioned coagulant-producing bacteria (at least one kind), and the wastewater to be applied may be any wastewater containing suspended matter, but particularly active In a wastewater flocculation treatment method using sludge, the generation and proliferation of filamentous bacteria, which is the main cause of bulking, can be suppressed in the separation area between activated sludge and treated water.Therefore, the present invention can suppress the generation and proliferation of filamentous bacteria, which are the main cause of bulking. It is particularly effective in treating wastewater.
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出来るものであり、特に
限定されない。Wastewater coagulation treatment methods using activated sludge methods using microorganisms are well known, and the present invention is applicable to any of these well-known wastewater coagulation treatment methods, and is not particularly limited.
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。In a preferred embodiment of the present invention, even better force values are obtained by setting the pH in the separation zone where activated sludge and treated water are to be separated to be in the range of 7 to 9, particularly preferably 8.0 to 8.5. It will be done.
本発明において凝集剤生産菌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
。凝集剤生産菌の濃度が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。In the present invention, the amount of flocculant-producing bacteria added is 0 as the culture solution.
.. The content is 5% by weight or more, preferably 0.5 to 10% by weight. Even when the concentration of flocculant-producing bacteria was added in excess of 10%, the strength value did not improve in accordance with the amount added.
(実施例)
従来公知のロードコツカス・エリスロポレスと、本発明
での凝集剤生産菌の夫々の培養液を下記の液体培地で3
0’Cで振どう培養した。(Example) Culture solutions of the conventionally known Rhodococcus erythropores and the flocculant-producing bacteria of the present invention were cultured in the following liquid medium for 30 minutes.
Culture was performed at 0'C with shaking.
尚、R−1菌は従来公知のロードコツカス・エリスロポ
レスであり、本発明のR−3菌はKYM1株(FERM
P−11333)、KYM−2株(FERM P−1
1334)、K Y M −3株(FERM P−11
335)、KYM4株(FERM P−11336)、
KYM−5株(FERM P−11337)、KYM−
6株(FERM P−11357)及びKYIII−7
株(FERM P−11358)からなっている。The R-1 bacterium is the conventionally known Rhodococcus erythropores, and the R-3 bacterium of the present invention is the KYM1 strain (FERM
P-11333), KYM-2 strain (FERM P-1
1334), K Y M-3 strain (FERM P-11
335), KYM4 strain (FERM P-11336),
KYM-5 strain (FERM P-11337), KYM-
6 strains (FERM P-11357) and KYIII-7
strain (FERM P-11358).
液生星叫凹皿減
炭素源 10 g/QK、HP
O4’ 5 g/ρKH2PO,2g/
f2
MgSO,0,2g/氾
(NH4)2S0. 0. 5
g#2イースト抽出物 0.5g/ρNa
Cl 0. 1 g/ff(
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日間振どう培養した培養
液を供試液とした。温度は30’Cとした。Liquid Seiko concave dish reduced carbon source 10 g/QK, HP
O4' 5 g/ρKH2PO,2g/
f2 MgSO, 0.2g/Flood (NH4)2S0. 0. 5
g#2 yeast extract 0.5g/ρNa
Cl 0. 1 g/ff(
1) Titer (a) Test solution Using fructose as the carbon source of the liquid medium, p
A culture solution obtained by culturing with shaking for 5 days in a medium whose H value was adjusted to 8.5 was used as a test solution. The temperature was 30'C.
(b)力値の評価法
100mAのメスシリンダーに、カオリン5000mg
/ρ液を80mβ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、0.5NのNaOH
及びHCIでpH7,0にpHを調整した。蒸留水で全
量を100rr+j2とし、再度転倒撹拌後、静置し5
分後の上澄水のOD5.。を測定し、1/Dssoにて
凝集力価を表示した。(b) Force value evaluation method: 5000 mg of kaolin in a 100 mA graduated cylinder.
/ρ solution at 80mβ, added inorganic kaolin and culture solution in predetermined amounts, gently stirred by inverting, and then added 0.5N NaOH.
The pH was adjusted to pH 7.0 with and HCI. Adjust the total volume to 100rr+j2 with distilled water, stir again by turning over, and let stand for 5 minutes.
OD of supernatant water after 5 minutes. . was measured, and the agglutination titer was expressed as 1/Dsso.
R−1菌及びR−3菌の凝集力価の経口変化は第1図示
の通りであった。The oral changes in agglutination titer of R-1 bacteria and R-3 bacteria were as shown in Figure 1.
以上の通り本発明の菌R−3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ツ
カス・エリスロポレス菌である。As described above, the bacterium R-3 of the present invention exhibits significantly superior titer compared to other bacteria. In addition, R-1 is a conventionally known Rhodococcus erythropores bacterium.
(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。(2) pH during aggregation The pH during aggregation was adjusted to 5 to 10, and the optimum aggregation pH was studied.
第2図示の様にpHが5から8に上昇するに従い0D5
5oが低下し、それ以上のpHでは0D55oが上昇し
、培養液の最適凝集i)Hは8.0〜8,5であること
が明らかとなった。As the pH increases from 5 to 8 as shown in the second diagram, 0D5
It was revealed that 0D55o decreased and 0D55o increased at pH higher than that, and the optimal aggregation i)H of the culture solution was 8.0 to 8.5.
(効 果)
以上説明の様に、本発明の凝集剤生産菌は今回新たに凝
集剤生産能があることが発見されたものであり、従来公
知の凝集剤生産菌に比べて特にR−3菌と称されるシュ
ウドモナス属、アシネトバクタ−属、アグロバクテリウ
ム属、エンテロバクタ−属、オーレオバクテリウム属及
びオエルス5
6
コピア属からなる群から選ばれるの少なくとも1属を含
む微生物群は著しく優れた凝集剤生産能を有する。(Effect) As explained above, the flocculant-producing bacteria of the present invention was newly discovered to have flocculant-producing ability, and compared to conventional flocculant-producing bacteria, it has particularly high R-3 A group of microorganisms containing at least one genus selected from the group consisting of the genus Pseudomonas, Acinetobacter, Agrobacterium, Enterobacter, Aureobacterium, and Copia is extremely superior. It has flocculant production ability.
従って、本発明方法によれば、優れた排水処理効果が得
られる。Therefore, according to the method of the present invention, excellent wastewater treatment effects can be obtained.
第1図は凝集力価と経過日数との関係を示す図であり、
第2図は凝集力価とpHとの関係を示す図である。Figure 1 is a diagram showing the relationship between agglutination titer and elapsed days;
FIG. 2 is a diagram showing the relationship between agglutination titer and pH.
Claims (8)
バクテリウム属、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属を含むことを特徴とする凝集剤生産微生
物。(1) A flocculant-producing microorganism comprising at least one genus selected from the group consisting of Pseudomonas, Acinetobacter, Agrobacterium, Enterobacter, Aureobacterium, and Oelscobia.
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)であり、アシネトバクター属がアシネトバ
クターKYM−3株(FERM P−11335)であ
り、アグロクテリウム属がアグロバクテリウムKYM−
4株(FERM P−11336)であり、エンテロバ
クター属がエンテロバクターKYM−5株(FERM
P−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−11
357)であり、オエルスコビア属がオエルスコビアK
YM−7株(FERM P−11358)である請求項
(1)に記載の凝集剤生産微生物。(2) Pseudomonas genus is Pseudomonas fluorescens KYM-1 strain (FERM P-11333) or Pseudomonas cepacia KYM-2 strain (FERM P-
11334), the genus Acinetobacter is Acinetobacter KYM-3 strain (FERM P-11335), and the genus Agrocterium is Agrobacterium KYM-3.
4 strains (FERM P-11336), and the Enterobacter genus is Enterobacter KYM-5 strain (FERM P-11336).
P-11337), and the genus Aureobacterium is Aureobacterium KYM-6 strain (FERM P-11
357), and the genus Oerscobia is Oerscobia K.
The flocculant-producing microorganism according to claim (1), which is YM-7 strain (FERM P-11358).
又は培養処理物を主成分とする微生物産生凝集剤。(3) A microorganism-produced flocculant whose main component is a culture or cultured product of the microorganism according to claim (1) or (2).
)又は(2)に記載の微生物産生凝集剤。(4) Claim (1) containing one or more cationic inorganic salts
) or the microorganism-produced flocculant according to (2).
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。(5) A wastewater flocculation treatment method, which comprises bringing the microorganism or microorganism-produced flocculant according to claims (1) to (4) into contact with suspended matter-containing wastewater.
請求項(1)〜(4)に記載の微生物又は微生物産生凝
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。(6) In a wastewater coagulation treatment method using an activated sludge method,
A wastewater flocculation characterized in that the microorganism or microorganism-produced flocculant according to claims (1) to (4) is present in a treatment system to prevent bulking of activated sludge in a separation area between activated sludge and treated water. Processing method.
請求項(6)に記載の排水凝集処理方法。(7) The wastewater coagulation treatment method according to claim (6), wherein the pH of the activated sludge separation region is maintained at 7 to 9.
項(7)に記載の排水凝集処理方法。(8) The wastewater coagulation treatment method according to claim (7), wherein the wastewater to be treated is wastewater that is likely to generate filamentous bacteria.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2083078A JPH0661B2 (en) | 1990-03-30 | 1990-03-30 | Flocculant-producing microorganism |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2083078A JPH0661B2 (en) | 1990-03-30 | 1990-03-30 | Flocculant-producing microorganism |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4270755A Division JPH07108216B2 (en) | 1992-09-16 | 1992-09-16 | Microorganism-produced flocculant and wastewater flocculation method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03285676A true JPH03285676A (en) | 1991-12-16 |
JPH0661B2 JPH0661B2 (en) | 1994-01-05 |
Family
ID=13792145
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2083078A Expired - Lifetime JPH0661B2 (en) | 1990-03-30 | 1990-03-30 | Flocculant-producing microorganism |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0661B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011011140A (en) * | 2009-07-01 | 2011-01-20 | Japan Biomass Corp | Method for reducing sludge |
CN102206025A (en) * | 2011-04-15 | 2011-10-05 | 凯翔国际水技术(大连)有限公司 | Method for fully recycling sludge |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5231434A (en) * | 1975-09-01 | 1977-03-09 | Diesel Kiki Co Ltd | Cooler for vehicle |
-
1990
- 1990-03-30 JP JP2083078A patent/JPH0661B2/en not_active Expired - Lifetime
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5231434A (en) * | 1975-09-01 | 1977-03-09 | Diesel Kiki Co Ltd | Cooler for vehicle |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011011140A (en) * | 2009-07-01 | 2011-01-20 | Japan Biomass Corp | Method for reducing sludge |
CN102206025A (en) * | 2011-04-15 | 2011-10-05 | 凯翔国际水技术(大连)有限公司 | Method for fully recycling sludge |
Also Published As
Publication number | Publication date |
---|---|
JPH0661B2 (en) | 1994-01-05 |
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