JPH08206685A - Waste water treatment - Google Patents
Waste water treatmentInfo
- Publication number
- JPH08206685A JPH08206685A JP7041404A JP4140495A JPH08206685A JP H08206685 A JPH08206685 A JP H08206685A JP 7041404 A JP7041404 A JP 7041404A JP 4140495 A JP4140495 A JP 4140495A JP H08206685 A JPH08206685 A JP H08206685A
- Authority
- JP
- Japan
- Prior art keywords
- yeast
- waste water
- wastewater
- tank
- treated
- 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
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
- Activated Sludge Processes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、排水処理方法に関する
ものであり、更に詳細には、高濃度排水を効率的に処理
ししかも余剰汚泥の生成量を大幅に減少することのでき
る新規な排水処理方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater treatment method, and more particularly, to a novel wastewater capable of efficiently treating high-concentration wastewater and significantly reducing the amount of excess sludge produced. It relates to a processing method.
【0002】[0002]
【従来の技術】有機性排水の処理方法としては、従来よ
り、生物学的方法、化学的方法、物理的ないし機械的方
法が知られており、例えば食品製造排水、醸造排水、農
産製造排水等の処理には活性汚泥法といった生物学的方
法が多用されている。しかしながら、これら既知の方法
は、まだ充分に満足できるものではない。2. Description of the Related Art As a method for treating organic wastewater, biological methods, chemical methods, physical or mechanical methods have been conventionally known. For example, food manufacturing wastewater, brewing wastewater, agricultural production wastewater, etc. A biological method such as an activated sludge method is frequently used for the treatment of sewage. However, these known methods are not yet fully satisfactory.
【0003】[0003]
【発明が解決しようとする問題点】河川の汚濁防止等公
害防止上の観点から、近年、特に排水に対する規制が強
化され、当業界において、効率の高いすぐれた排水処理
方法の確立が強く望まれている。[Problems to be Solved by the Invention] From the viewpoint of pollution prevention such as river pollution prevention, in particular, regulations on wastewater have been strengthened in recent years, and establishment of an efficient and excellent wastewater treatment method is strongly desired in the industry. ing.
【0004】一方、活性汚泥法等生物学処理において
は、排水処理後に多量の汚泥が副生し、排水自体の処理
だけでなく副生汚泥も効率的に処理しなければ二次公害
が発生する危険性にも本発明者らははじめて着目した。On the other hand, in biological treatment such as activated sludge method, a large amount of sludge is produced as a byproduct after wastewater treatment, and secondary pollution occurs unless not only wastewater itself but also byproduct sludge is not efficiently treated. For the first time, the present inventors also paid attention to the risk.
【0005】本発明は、これらの問題点を一挙に解決す
る目的でなされたものである。The present invention has been made for the purpose of solving these problems all at once.
【0006】[0006]
【問題点を解決するための手段】上記目的達成のために
各方面から検討の結果、高濃度排水を効率的に処理する
ためには、直接活性汚泥で処理する前に酵母で処理する
方法あるいは酵母単独で処理する方法が必要であること
に先ず着目した。[Means for Solving the Problems] As a result of studies from various fields to achieve the above object, in order to efficiently treat high-concentration wastewater, a method of treating with yeast before directly treating with activated sludge or We first focused on the need for a method of treating yeast alone.
【0007】酵母としては、排水中の汚濁質に対して分
解能の高い酵母であればすべての酵母が単用又は2種以
上併用することができる。使用可能な酵母は、例えば、
ハンゼヌラ属酵母、例えばハンゼヌラ・アノラマ、及び
クルイベロマイセス属酵母、例えばクルイベロマイセス
・マルキシアヌス、K.ラクチス、及びキャンディダ属
酵母、及びトリコスポロン属酵母である。As yeasts, all yeasts can be used alone or in combination of two or more, as long as they are yeasts having a high ability to decompose pollutants in wastewater. The yeast that can be used is, for example,
Hansenula yeasts such as Hansenula anorama, and Kluyveromyces yeasts such as Kluyveromyces marxianus, K. et al. Lactis, Candida yeast, and Trichosporon yeast.
【0008】代表菌株としては、次のものが例示され
る:ハンゼヌラ・アノラマ(Hansenula an
omala)J−224(FERMP−7671)、同
J622、同J−45−0、ハンゼヌラ・ファビアニ
(H.fabianii)J−640:クルイベロマイ
セス・マルキシアヌス(Kluyveromyces
marxianus)J−673(FERM P−10
385):キャンディダスピーシーズ(Candida
sp.)(FERM P−3965):トリコスポロ
ン スピーシーズ(Trichosporon s
p.)AN−161。Examples of representative strains include the following: Hansenula an
omala) J-224 (FERMP-7671), J622, J-45-0, H. fabianii J-640: Kluyveromyces marxianus (Kluyveromyces)
marxianus) J-673 (FERM P-10
385): Candida Species
sp. ) (FERM P-3965): Trichosporon species
p. ) AN-161.
【0009】このようにして酵母処理することによって
有機排水は充分に処理されるが、更に高度に処理したり
あるいは酵母だけでは充分に処理し得ない成分が含まれ
る場合には、活性汚泥処理を更に併用すればよい。活性
汚泥処理は常法にしたがって適宜実施することができ
る。Although the organic waste water is sufficiently treated by treating with yeast in this way, if it is treated to a higher degree or contains components that cannot be treated sufficiently with yeast, activated sludge treatment is required. It may be used together. The activated sludge treatment can be appropriately performed according to a conventional method.
【0010】しかしながら、本発明においては、酵母処
理によって排水を浄化した後、更に酵母溶解菌で処理し
たところ、増殖した酵母が溶解することはもちろんのこ
と、排水中の固形分の消化が大幅に促進され、BOD値
も大幅に減少して、更に高度な排水処理が行われるとい
う有用な新知見を得た。また、酵母溶解菌処理を併用す
ることによって余剰汚泥の発生を大幅に抑制し、汚泥に
起因する二次公害の発生が防止できることも確認した。
しかも更に、酵母溶解菌処理が活性汚泥処理にも何らの
悪影響を及ぼさないことを確認し、これらの有用新知見
に基づき、効率的な総合的排水システムが構築されたの
である。However, in the present invention, when the wastewater is purified by yeast treatment and further treated with yeast-dissolving bacteria, the grown yeast is not only dissolved, but also the digestion of solids in the wastewater is significantly reduced. It was promoted, the BOD value was greatly reduced, and useful new knowledge was obtained that more advanced wastewater treatment is performed. It was also confirmed that the combined use of yeast lysing treatment can significantly suppress the generation of excess sludge and prevent the generation of secondary pollution due to sludge.
Moreover, it was confirmed that the yeast lysate treatment had no adverse effect on the activated sludge treatment, and based on these useful new findings, an efficient integrated drainage system was constructed.
【0011】本発明においては、酵母を溶解しうる微生
物であればすべてのものが使用できるが、例えば酵母溶
解菌YLM−1(Rarobacter faecitabidusと命名され
た)は本発明において使用する微生物として好適なもの
のひとつである。In the present invention, any microorganism can be used as long as it can dissolve yeast. For example, yeast lysing bacterium YLM-1 (named Rarobacter faecitabidus) is suitable as the microorganism used in the present invention. It is one of the things.
【0012】YLM−1は、下記の性質を有する比較的
小型のグラム陰性の桿菌であって、胞子は観察されなか
った。 (1)細胞の形 桿菌 (2)細胞の大きさ 0.3〜0.4×
0.9〜1.8μm (3)細胞の多形成の有無 なし (4)運動性 あり (5)鞭毛の着生状態 極鞭毛 (6)グラム染色性 陽性 (7)抗酸性 陽性 (8)酵母の溶解性 あり (9)増殖pH 7〜9(増殖最適
pH7) (10)増殖最適温度 30〜35℃YLM-1 is a relatively small Gram-negative bacillus having the following properties, and no spores were observed. (1) Cell shape Bacillus (2) Cell size 0.3 to 0.4 ×
0.9-1.8 μm (3) Presence / absence of cell polymorphism None (4) Motile (5) Flagellation status of polar flagella (6) Gram stain positive (7) Acid-positive (8) Yeast (9) Growth pH 7-9 (growth optimum pH 7) (10) Growth optimum temperature 30-35 ° C
【0013】YLM−1の分離法は次のとおりである:
YNB(イーストナイトロジェンベース、Difco
社)に寒天1%と酵母Hansenula anoma
laJ−45−0を2×107cells/ml程度と
なるように添加する。YNB寒天培地はオートクレーブ
滅菌後、50℃程度まで冷してから、酵母の生菌体を添
加する。分離源試料を適当に希釈して、酵母と同時に接
種し、混合後、シャーレに流し込み培養する。35℃で
5〜10日培養してYLM−1菌を分離し、これを寄託
した(FERM P−6781)。The separation method of YLM-1 is as follows:
YNB (East Nitrogen Base, Difco
1% agar and Hansenula anoma yeast
laJ-45-0 is added at about 2 × 10 7 cells / ml. The YNB agar medium is sterilized in an autoclave, cooled to about 50 ° C., and then live yeast cells are added. The separated source sample is appropriately diluted, inoculated at the same time as yeast, mixed, poured into a petri dish, and cultured. YLM-1 bacteria were isolated by culturing at 35 ° C. for 5 to 10 days and deposited (FERM P-6781).
【0014】YLM−1は、酵母生菌体寒天培地に穿刺
培養すると、30℃3日間の培養で、培地の表面より酵
母の溶菌が観察され、約一週間後、試験管内の培地全体
の酵母が溶菌した。また、YLM−1を酵母生菌体寒天
培地に接種し、試験管中で固めて30℃で培養した結
果、一週間で全面にコロニー及び溶菌斑を検出した。溶
菌スペクトルは、下記表1、表2に示すとおりである。When YLM-1 was stab-cultured on a viable yeast agar medium, lysis of yeast was observed from the surface of the medium at 30 ° C. for 3 days. About one week later, the yeast in the whole medium in a test tube was cultured. Lysed. In addition, YLM-1 was inoculated on a yeast agar medium, solidified in a test tube, and cultured at 30 ° C. As a result, colonies and lytic spots were detected on the entire surface in one week. The lysis spectrum is as shown in Tables 1 and 2 below.
【0015】[0015]
【表1】 [Table 1]
【0016】[0016]
【表2】 [Table 2]
【0017】上記結果から明らかなように、YLM−1
は、これらの表に表示した各種酵母で有機排水を処理し
た後、使用済酵母を効率的に溶菌することができる。ま
た酵母溶解菌が酵母を溶菌するだけでなくその他すぐれ
た排水処理効果を奏することは既に述べたとおりであ
る。As is clear from the above results, YLM-1
After treating the organic wastewater with the various yeasts listed in these tables, the used yeast can be efficiently lysed. As described above, the yeast lysate not only lyses the yeast but also has another excellent wastewater treatment effect.
【0018】酵母溶解菌としては、上記したYLM−1
菌のほか、酵母を溶解しうる微生物であればすべてのも
のが使用可能であって、例えば、オエルスコフィア・ツ
ルバータ(Oerskovia turbata,IF
O 13506)、オエルスコフィア・キサンチネオリ
チカ(Oerskovia xanthineolyt
ica)、オエルスコフィア・シトリア(Oersko
via citrea,FERM P−2003)、オ
エルスコフィア スピーシーズ YS−016(Oer
skovia sp.YS−016,FERM P−1
1737)等が使用可能である。Yeast lysates include YLM-1 described above.
In addition to bacteria, any microorganism can be used as long as it is a microorganism capable of lysing yeast, and examples thereof include Oerskovia turbata (IF).
O 13506), Oerskovia xanthineolyt
ica), Oerskofia Citria (Oersko)
via city, FERM P-2003), Oerskophia species YS-016 (Oer
scovia sp. YS-016, FERM P-1
1737) and the like can be used.
【0019】オエルスコフィア・シトリアは、酵母細胞
壁溶解酵素を産生し、すぐれた酵母溶菌性を示す特徴を
有し、次のような菌学的性質を示す。 (1)形態:培養初期に菌糸を形成し、その後(約24
時間)断裂により細菌状細胞になる細菌細胞の平均の大
きさは0.4〜0.6×1.0〜3.0μであり両端は
まる味を帯びている。古い培養(72時間以後)では球
状または不定形に変化し平均の大きさは0.8〜1.0
×0.8〜1.0μである。 (2)気菌糸:形成しない。 (3)運動性:菌糸の断裂により生じた細菌状細胞中に
運動性の観察されるものが存在する。 (4)内生胞子:形成しない。 (5)鞭毛:細菌状細胞1ケあたり1〜3本の側毛を着
生する。 (6)グラム染色性:陽性 (7)抗酸性:なし (8)酵母の溶解性:ありOerskophia citria produces a yeast cell wall lysing enzyme and is characterized by excellent yeast lytic properties, and exhibits the following mycological properties. (1) Morphology: Hyphae are formed in the early stage of culture and then (about 24
(Time) A bacterial cell becomes a bacterial cell by rupture, and the average size of the bacterial cell is 0.4 to 0.6 × 1.0 to 3.0 μm, and both ends are tinged. In old culture (after 72 hours), it changes to spherical or amorphous and the average size is 0.8 to 1.0.
× 0.8 to 1.0 μ. (2) Aerial mycelium: Does not form. (3) Motility: Bacterial cells that are observed due to rupture of hyphae have motility. (4) Endospores: do not form. (5) Flagella: 1-3 side hairs grow on each bacterial cell. (6) Gram stainability: Positive (7) Anti-acidity: None (8) Yeast solubility: Yes
【0020】オエルスコフィア YS−016は、子の
う菌酵母のほか担子菌類酵母、不完全菌類酵母を溶解す
ることができ、広い溶菌スペクトルを有し、次のような
菌学的性質を示す。 (1)形態:培養初期から中期にかけて菌糸状を呈し、
その後、断裂により短桿菌状から球菌状に分裂する。そ
の平均の大きさは0.3〜0.6×1.3〜3.0≦で
ある。 (2)気菌糸 :なし (3)運動性 :あり (4)胞子の有無 :なし (5)鞭毛 :極鞭毛 (6)グラム染色性:陽性 (7)抗酸性 :なし (8)酵母の溶解性:ありOerskophia YS-016 can dissolve ascomycete yeast, basidiomycete yeast and imperfect fungal yeast, has a broad lytic spectrum, and exhibits the following mycological properties. (1) Morphology: Mycelium is exhibited from the early stage to the middle stage of culture,
After that, due to rupture, it splits from short rod-shaped to coccoid. The average size is 0.3 to 0.6 × 1.3 to 3.0 ≦. (2) Aerial hyphae: None (3) Motility: Yes (4) Presence or absence of spores: None (5) Flagella: Extreme flagella (6) Gram stainability: Positive (7) Anti-acidity: None (8) Yeast lysis Gender: Yes
【0021】酵母も同様であるが、酵母溶解菌も、単用
又は2種以上の併用が可能であり、生菌体はもとより、
死菌体、培養物、及び/又は処理物等が使用可能であ
る。処理物としては、酵母溶解菌を培養して得た培養物
の濃縮物、ペースト化物、乾燥物、希釈物、固液分離し
て得た固形物、及び/又は同液体部等培養物の各種処理
物がすべて包含される。The same applies to yeasts, but yeast lysates can be used alone or in combination of two or more kinds.
Killed cells, cultures, and / or processed products can be used. As the processed product, a concentrate of the culture obtained by culturing yeast lysate, a paste, a dried product, a diluted product, a solid obtained by solid-liquid separation, and / or various cultures such as the liquid part All processed products are included.
【0022】このように本発明によれば、排水を酵母で
処理した後、酵母溶解菌で処理し、必要あれば次に活性
汚泥処理を行い(酵母溶解処理と活性汚泥処理とを同時
に平行して行ってもよい)、排水を効率的に浄化するこ
とができる。例えば下記表3に示した処理フローのよう
に、排水に汚濁質分解能の高い酵母を加えて浄化し、次
に、浄化に伴い、増殖した酵母を酵母溶解菌で溶菌処理
して、酵母処理した排水中の固形分を消化し、更に、B
ODを減少させた後、必要あれば低濃度排水と合わせ、
そして活性汚泥で処理すればよい。As described above, according to the present invention, the waste water is treated with yeast, and then with yeast lysing bacteria, and if necessary, activated sludge treatment is performed (the yeast lysing treatment and the activated sludge treatment are simultaneously performed in parallel. The waste water can be efficiently purified. For example, as shown in the treatment flow shown in Table 3 below, yeast having a high degree of degrading pollutants was added to the wastewater to purify it, and then, along with the purification, the yeast that had proliferated was subjected to a lysing treatment with a yeast lysing bacterium to perform yeast treatment. Digests solids in wastewater, and further B
After reducing OD, combine with low-concentration wastewater if necessary,
Then, it may be treated with activated sludge.
【0023】[0023]
【表3】 [Table 3]
【0024】このような処理フローを具体化した1例を
図1に示す。図1は、本発明に係る排水処理方法を実施
するための装置の1実施例であって、その操作は次のと
おりである。先ず、原水槽からポンプPによって有機排
水を酵母槽に導入する。酵母槽において有機排水を酵母
と充分に接触せしめて排水の浄化を行う。必要あれば槽
内を攪拌し、ブロワーBを稼働して通気を行う。また、
酵母槽は、pHコントローラーによって、槽内のpHを
測定し、アルカリ側に傾いたときには硫酸等の酸をポン
プPによって槽内に導入し、最適pHを維持する。更に
また所望するのであれば、酵母槽とは別に調整槽(図示
せず)を設け、pHのコントロール、排水濃度のコント
ロール等を行ってもよい。FIG. 1 shows an example embodying such a processing flow. FIG. 1 is an embodiment of an apparatus for carrying out the wastewater treatment method according to the present invention, the operation of which is as follows. First, the organic waste water is introduced into the yeast tank from the raw water tank by the pump P. The organic wastewater is thoroughly contacted with the yeast in the yeast tank to purify the wastewater. If necessary, the inside of the tank is stirred and blower B is operated to ventilate. Also,
In the yeast tank, the pH in the tank is measured by a pH controller, and when leaning toward the alkali side, an acid such as sulfuric acid is introduced into the tank by the pump P to maintain the optimum pH. Furthermore, if desired, an adjusting tank (not shown) may be provided separately from the yeast tank to control pH, control wastewater concentration and the like.
【0025】このようにして、ハンゼヌラ及びキャンデ
ィダに属する酵母を各種排水(洗米排水(pH4.
0):A、澱粉製造プラントからのクラリファイアー
水:B、モルトウィスキー蒸留廃液:C、希釈した清酒
(10倍):D)で通気攪拌処理した場合の増殖収率
は、下記表4のとおりである。In this manner, yeasts belonging to Hansenula and Candida are treated with various wastewater (washed wastewater (pH 4.
0): A, clarifier water from a starch manufacturing plant: B, malt whiskey distilling waste liquid: C, dilute sake (10 times): D), the growth yield when aerated and stirred is as shown in Table 4 below. Is.
【0026】[0026]
【表4】 [Table 4]
【0027】酵母溶解菌の混入を防止しつつ酵母処理に
よって浄化された排水は、消化槽に導入される。消化槽
内においては、酵母槽の場合と同様に、攪拌、通気が行
われ、酵母溶解菌(YLM−1等)の作用によって酵母
の溶菌が行われるだけでなく、排水中の固形分が消化さ
れ、また、BODも減少される。ハンゼヌラ酵母を基質
とし、酵母溶解菌としてYLM−1を用いた場合の増殖
収率を下記表5に示す。なおこの場合、酵母菌体のみを
通気攪拌処理しても酵母の内生呼吸のため、TOCが減
少するので、YLM−1の増殖収率を初発の酵母のTO
Cを基準にした場合と酵母のみを振とう培養した後のT
OCを基準とした場合の平均値として算出した。The effluent purified by the yeast treatment while preventing the yeast lysing bacteria from being mixed is introduced into the digestion tank. In the digestion tank, as in the case of the yeast tank, stirring and aeration are performed, not only the yeast is lysed by the action of yeast lysing bacteria (YLM-1, etc.), but also the solid content in the waste water is digested. BOD is also reduced. Table 5 below shows the growth yield when Hansenula yeast was used as the substrate and YLM-1 was used as the yeast lysate. In this case, since TOC is reduced due to the endogenous respiration of the yeast even if only the yeast cells are aerated and agitated, the growth yield of YLM-1 is reduced to the TO of the first yeast.
T based on C and after shaking culture of yeast alone
It was calculated as an average value with OC as a reference.
【0028】[0028]
【表5】 [Table 5]
【0029】消化槽で処理した後、直接、活性汚泥槽で
処理してもよいが、一旦、調整槽内で低濃度排水を添加
したり、pHや濃度の調整等各種の調整を行った後、活
性汚泥処理してもよい。After treatment in the digestion tank, it may be directly treated in the activated sludge tank, but after once adding low-concentration wastewater in the adjusting tank or adjusting the pH and the concentration. The activated sludge may be treated.
【0030】活性汚泥処理は常法にしたがって行えばよ
い。例えば、ポンプPによって調整槽から排水を活性汚
泥槽内に導入し、ブロワーBから通気しながら活性汚泥
と充分に接触せしめて、排水を処理するとともに、酵母
溶解菌の集積、増殖も行う。活性汚泥処理後、沈降槽に
移して固液を分離し、液状部は処理水槽や移送して河川
等に放流する一方、固体部はその一部は返送汚泥として
活性汚泥槽に返送する。このようにして、バッチ処理は
もとより連続処理することも可能となった。The activated sludge treatment may be carried out according to a conventional method. For example, the wastewater is introduced into the activated sludge tank from the adjusting tank by the pump P and is sufficiently contacted with the activated sludge while being aerated from the blower B to treat the wastewater and also to accumulate and proliferate the yeast-dissolving bacteria. After the activated sludge treatment, it is transferred to a settling tank to separate the solid and liquid, and the liquid portion is transferred to the treated water tank or discharged to a river or the like, while the solid portion is partially returned to the activated sludge tank as return sludge. In this way, not only batch processing but also continuous processing became possible.
【0031】本発明においては、各種の有機排水が効率
的に処理され、例えば、洗米排水等の清酒製造排水;各
種の焼酎蒸留廃液;ウィスキー、ブランデー蒸留廃液;
ディスチラーズソリュブル;澱粉製造廃液等各種農産製
造廃液;厨房排水;その他各種の有機排水を広範に処理
することができる。以下、本発明の実施例について述べ
る。In the present invention, various organic wastewaters are efficiently treated. For example, wastewater for sake production such as rice washing wastewater; various shochu distillation waste liquids; whiskey, brandy distillation waste liquids;
Distillers solubles; various agricultural production waste liquids such as starch production waste liquids; kitchen wastewater; and various other organic wastewaters can be treated extensively. Examples of the present invention will be described below.
【0032】[0032]
【実施例1】図1に示した装置を用い、下記表6に示す
性状を有する麦焼酎蒸留粕を濾過して得た濾液(麦焼酎
蒸留粕脱水濾液:その性状を下記表7に示す)を処理し
た。Example 1 A filtrate obtained by filtering a barley shochu distilled lees having the properties shown in Table 6 below using the apparatus shown in FIG. 1 (barley shochu distilled lees dehydrated filtrate: its properties are shown in Table 7 below). Was processed.
【0033】[0033]
【表6】 [Table 6]
【0034】[0034]
【表7】 [Table 7]
【0035】酵母処理、消化処理、活性汚泥処理を、下
記表8に示す条件で処理した。酵母としては、Hans
enula anomala J−45−0を用い、酵
母溶解菌としてはYLM−1(FERM P−678
1)を用いた。The yeast treatment, digestion treatment and activated sludge treatment were carried out under the conditions shown in Table 8 below. Hans as yeast
Enula anomala J-45-0 was used, and YLM-1 (FERM P-678 was used as a yeast lysate.
1) was used.
【0036】[0036]
【表8】 [Table 8]
【0037】60日間本装置の稼働を行い、酵母槽、消
化槽における処理水のBOD及び固形分の経日変化を測
定して、それぞれ図2、図3の結果を得た。The apparatus was operated for 60 days, and the BOD of treated water and the solid content of the treated water in the digestion tank were measured over time to obtain the results shown in FIGS. 2 and 3, respectively.
【0038】また、酵母処理水及び消化処理水の性状に
ついても測定を行い、下記表9の結果を得た。更に、酵
母処理に及ぼす容積負荷の影響及び消化処理による固形
分の可溶化については、それぞれ下記表10、表11の
結果が得られた。The properties of yeast treated water and digested treated water were also measured, and the results shown in Table 9 below were obtained. Further, the results of Table 10 and Table 11 below were obtained for the influence of volume load on the yeast treatment and the solubilization of the solid content by the digestion treatment, respectively.
【0039】[0039]
【表9】 [Table 9]
【0040】[0040]
【表10】 [Table 10]
【0041】[0041]
【表11】 [Table 11]
【0042】[0042]
【発明の効果】本発明によれば、酵母処理と酵母溶菌処
理とを組合わせるという新規な構成を採用することによ
って、各種の有機性排水を効率的に処理できるだけでな
く、増殖した酵母を溶菌することによって余剰汚泥の生
成を抑制して汚泥の処理を大幅に軽減して、汚泥に起因
する二次公害を未然に抑制ないし防止することができ
る。EFFECTS OF THE INVENTION According to the present invention, by adopting a novel constitution in which yeast treatment and yeast lysis treatment are combined, not only various organic wastewaters can be efficiently treated, but also proliferated yeast is lysed. By doing so, generation of excess sludge can be suppressed, sludge treatment can be significantly reduced, and secondary pollution caused by sludge can be suppressed or prevented in advance.
【0043】また酵母溶解菌処理によって、使用済の酵
母を溶菌するだけでなく、排水中の固形分を更に消化
し、BODも減少させるという予期せざる新規な効果も
奏され、非常に効率的な排水処理が可能となる。The yeast lysing treatment not only lyses the used yeast, but also further digests the solids in the wastewater and reduces the BOD, resulting in an unexpected new effect, which is very efficient. Wastewater treatment is possible.
【図1】本発明に係る排水処理を実施するための装置の
1実施例を示す。FIG. 1 shows an embodiment of an apparatus for carrying out wastewater treatment according to the present invention.
【図2】酵母槽、消化槽の処理水BODの経日変化を示
す。FIG. 2 shows the daily change of treated water BOD in a yeast tank and a digester tank.
【図3】酵母槽、消化槽での固形分の経日変化を示す。FIG. 3 shows daily changes in solid content in a yeast tank and a digester tank.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 下飯 仁 東京都北区滝野川2丁目6番30号 国税庁 醸造試験所内 (72)発明者 蓼沼 誠 東京都北区滝野川2丁目6番30号 国税庁 醸造試験所内 (72)発明者 鈴木 修 群馬県安中市中宿1443番地 株式会社ティ ーディーイー生物工学研究室内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Jin Shimohan 2-6-30 Takinogawa, Kita-ku, Tokyo Inside the National Tax Agency Brewing Laboratory (72) Inventor Makoto Tatenuma 2-6-30 Takinogawa, Kita-ku, Tokyo National Tax Agency Brewing Test In-house (72) Inventor Osamu Suzuki 1443 Nakajuku, Annaka-shi, Gunma TDI Biotechnology Laboratory
Claims (7)
することを特徴とする排水処理方法。1. A method for treating wastewater, which comprises treating the wastewater with yeast and yeast-lysing bacteria.
酵母を用いて浄化し、次に、浄化に伴い、増殖した酵母
を酵母溶解菌で、溶菌処理して、酵母処理した排水中の
固形分を消化し、更に、BODも減少させた後、活性汚
泥で処理すること、を特徴とする排水処理方法。2. In the wastewater treated with yeast, the pollutants in the wastewater are purified by using yeast having a high decomposing ability, and then the yeast that has grown in association with the purification is subjected to a lysing treatment with yeast-dissolving bacteria. The method for treating waste water, which comprises digesting the solid content of, and further reducing BOD, and then treating with activated sludge.
性汚泥処理すること、を特徴とする請求項1又は請求項
2に記載の方法。3. The method according to claim 1 or 2, wherein after the bacteriolysis treatment, low-concentration wastewater is added to perform activated sludge treatment.
マイセス属、キャンディダ属、及び/又は、トリコスポ
ロン属に属する高分解能酵母を使用すること、を特徴と
する請求項1〜請求項3のいずれか1項に記載の方法。4. A high-resolution yeast belonging to the genera Hansenula, Kluyveromyces, Candida, and / or Trichosporone is used as yeast. The method according to item 1.
体、死菌体、培養物、及び/又は、その処理物を使用す
ること、を特徴とする請求項1〜請求項4のいずれか1
項に記載の方法。5. The yeast lysate used is a live bacterium, a dead bacterium, a culture, and / or a treated product of the yeast lysate, which is used in any one of claims 1 to 4. Or 1
The method described in the section.
菌を培養して得た培養物の濃縮物、ペースト化物、乾燥
物、希釈物、固液分離して得た固形物、及び/又は、同
液状物であること、を特徴とする請求項5に記載の方
法。6. A treated product of a yeast lysate culture is a concentrate, a paste, a dried product, a diluted product, a solid product obtained by solid-liquid separation of a culture obtained by culturing a yeast lysate, and The method according to claim 5, wherein the method is the same liquid material.
有するYLM−1を使用すること、を特徴とする請求項
1〜請求項6のいずれか1項に記載の方法。 (1)細胞の形 桿菌 (2)細胞の大きさ 0.3〜0.4×
0.9〜1.8μm (3)細胞の多形成の有無 なし (4)運動性 あり (5)鞭毛の着生状態 極鞭毛 (6)グラム染色性 陽性 (7)抗酸性 陽性 (8)酵母溶菌性 あり7. The method according to any one of claims 1 to 6, wherein YLM-1 having the following mycological properties is used as a yeast lysing bacterium. (1) Cell shape Bacillus (2) Cell size 0.3 to 0.4 ×
0.9-1.8 μm (3) Presence / absence of cell polymorphism None (4) Motile (5) Flagellation status of polar flagella (6) Gram stain positive (7) Acid-positive (8) Yeast Has lytic properties
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010029756A (en) * | 2008-07-25 | 2010-02-12 | Kameda Seika Co Ltd | Method for subjecting rice washing drainage to solid-liquid separation |
JP2012115714A (en) * | 2010-11-29 | 2012-06-21 | Masanori Watanabe | Method of settling solid component in rice washing drainage |
CN103663726A (en) * | 2013-12-09 | 2014-03-26 | 山东华亚环保科技有限公司 | Preparation method of microbiological water purifier |
-
1995
- 1995-02-07 JP JP04140495A patent/JP3691102B2/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010029756A (en) * | 2008-07-25 | 2010-02-12 | Kameda Seika Co Ltd | Method for subjecting rice washing drainage to solid-liquid separation |
JP2012115714A (en) * | 2010-11-29 | 2012-06-21 | Masanori Watanabe | Method of settling solid component in rice washing drainage |
CN103663726A (en) * | 2013-12-09 | 2014-03-26 | 山东华亚环保科技有限公司 | Preparation method of microbiological water purifier |
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