JPH0236320B2 - HAISUISHORIHOHO - Google Patents
HAISUISHORIHOHOInfo
- Publication number
- JPH0236320B2 JPH0236320B2 JP2880086A JP2880086A JPH0236320B2 JP H0236320 B2 JPH0236320 B2 JP H0236320B2 JP 2880086 A JP2880086 A JP 2880086A JP 2880086 A JP2880086 A JP 2880086A JP H0236320 B2 JPH0236320 B2 JP H0236320B2
- Authority
- JP
- Japan
- Prior art keywords
- glycerin
- wastewater
- treatment
- bacteria
- activated sludge
- 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.)
- Expired - Lifetime
Links
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- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
(産業上の利用分野)
本発明は廃水の処理方法に関し、更に詳細に
は、特に動植物油を原料として用いる食品工場、
又は油脂を取扱つたり排出する食品処理場ないし
油脂処理工場、又は油脂関連化成品処理工場等か
ら、排出される特にグリセリン含有量の高い廃水
から、グリセリン及びBOD、CODを除去ないし
は低減させる方法に関する。
したがつて本発明は、廃水処理の技術分野のみ
でなく、動植物油を大量に取扱う各種の食品の技
術分野、石けんその他油脂関連化成品の技術分野
において、非常に重要な働きをなすものである。
(従来の技術)
動植物油より脂肪酸を得る際に大量のグリセリ
ンが廃水に混入し、そのまま放流したのでは河川
の高栄養化を起して河川は汚染されてしまう。ま
た、このような廃水を活性汚泥法によつて処理し
ようとしても、大量のグリセリンのために活性汚
泥が充分にその活性を発揮することができず、結
局、活性汚泥法によつても充分な処理はできな
い。
微生物処理を試みても、大半の微生物はグリセ
リンを資化するどころか、高濃度のグリセリンに
よつて微生物自体の生育が阻害されてしまう。こ
のように、微生物のうち、酵母、特にサツカロミ
セス属酵母がグリセリンを資化することは従来未
知のことであり、ましてや、グリセリン含有廃水
処理のために工業的に使用できることにいたつて
は、その示唆すら知られていないのが現状であ
る。
(発明の開示)
このような技術の現状に鑑み、本発明者等は、
高グリセリン含有廃液の工業的処理方法につい
て、化学、生物学、物理学の各方面から検討した
結果、従来は成功に到らなかつたものの、結局、
微生物処理が最も可能性が高いという知見を得
た。
そこで本発明者らはグリセリンを含有し且つ、
高濃度のBODを含む廃水について、悪条件下で
も、これらグリセリン及びBODを分解資化し得
る菌を求めて鋭意検索したところ
Saccharomyces cerevisiae var.ellipsoideusの
変異株を分離することに成功したのである。そし
て、この新知見を基礎にしてスクリーニングした
結果、他のサツカロミセス属酵母にもすぐれたも
のがあることを発見し、そして更に研究を続け、
遂に本発明の完成に到つたのである。
ここに分離された菌株は実質的に
Saccharomyces cerevisiae var.ellipsoideusの
菌学的性質を有し、グリセリンを資化し廃水中の
BODを除去あるいは低減し得る新しい変異株で
ある。
この変異株はSaccharomyces cerevisiae var.
ellipsoideus YS−1と名づけられ、微工研に
FERMP No.4498として寄託されている。
この変異株は、グリセリン資化性以外は実質的
にSaccharomyces cerevisiae var.ellipsoideus
の菌学的性質を有しており、その諸性質はThe
Yeasts.a taxonomic study 2nd edition(J.
Lodder著1970)562,596頁に記載される如くで
あるが、その概要は次の通りである。
増殖は多極出芽による、細胞は一般に楕円形、
偽菌糸を形成、4ケの子のう胞子形成。皮膜形成
せず、硝酸塩資化−、arbutin分解−の諸性質を
示す。糖類資化(発酵)性は次のとおりである。
galucose+(+) lactose−(−)
galactose+(+) raffinose+(++)
sucrose+(+) arabinose+
maltose+(+)
次に脂肪酸製造廃水(BOD:24000ppm、
COD:18000ppm、グリセリン:8900ppm、PH
5.0)に本菌株、及びその対照として、
Hansenula anomala Y−1、Kluyveromyces
sp.KL−5、Hansenula anomala AM−6を用
いて各菌数107ケ/mlあて接種し、30℃で40時間
培養した。その結果は次の表に示される。
(Industrial Application Field) The present invention relates to a wastewater treatment method, and more particularly, to a food factory using animal and vegetable oils as raw materials,
Or it relates to a method for removing or reducing glycerin, BOD, and COD from wastewater with a particularly high glycerin content discharged from food processing plants or fat processing plants that handle or discharge fats and oils, or processing plants for oil-related chemical products, etc. . Therefore, the present invention plays an extremely important role not only in the technical field of wastewater treatment, but also in the technical field of various foods that handle large quantities of animal and vegetable oils, and the technical field of soap and other oil-related chemical products. . (Prior Art) When fatty acids are obtained from animal and vegetable oils, large amounts of glycerin are mixed into wastewater, and if the wastewater is discharged as is, the rivers become highly nutrient-rich and polluted. Furthermore, even if such wastewater is treated by the activated sludge method, the activated sludge cannot fully demonstrate its activity due to the large amount of glycerin, and in the end, even the activated sludge method cannot fully demonstrate its activity. Cannot be processed. Even if microbial treatment is attempted, most microorganisms do not assimilate glycerin, and the growth of the microorganisms themselves is inhibited by the high concentration of glycerin. Thus, among microorganisms, it was previously unknown that yeast, especially yeast of the genus Satucharomyces, could assimilate glycerin, and furthermore, there is no suggestion that it could be used industrially for the treatment of glycerin-containing wastewater. The current situation is that it is not even known. (Disclosure of the invention) In view of the current state of technology, the present inventors have
As a result of studying various aspects of chemistry, biology, and physics regarding industrial treatment methods for high-glycerin-containing wastewater, although no success had been achieved in the past, in the end,
We found that microbial treatment was the most likely option. Therefore, the present inventors prepared a solution containing glycerin and
We conducted an intensive search for bacteria that can decompose and assimilate glycerin and BOD even under adverse conditions in wastewater containing high concentrations of BOD.
They succeeded in isolating a mutant strain of Saccharomyces cerevisiae var.ellipsoideus. As a result of screening based on this new knowledge, they discovered that other yeasts of the genus Satucharomyces also had excellent properties, and continued their research.
The present invention has finally been completed. The strains isolated here are essentially
It has the mycological properties of Saccharomyces cerevisiae var.
This is a new mutant strain that can eliminate or reduce BOD. This mutant strain is Saccharomyces cerevisiae var.
It was named ellipsoideus YS-1 and was sent to the Institute of Fine Technology.
Deposited as FERMP No. 4498. This mutant strain is essentially Saccharomyces cerevisiae var.ellipsoideus except for its ability to assimilate glycerin.
It has the mycological properties of
Yeasts.a taxonomic study 2nd edition (J.
The outline is as follows: Proliferation is by multipolar budding; cells are generally oval;
Formed pseudohyphae and formed 4 ascospores. It does not form a film and exhibits properties of nitrate assimilation and arbutin decomposition. The sugar assimilation (fermentation) properties are as follows. galucose+(+) lactose-(-) galactose+(+) raffinose+(++) sucrose+(+) arabinose+ maltose+(+) Next, fatty acid production wastewater (BOD: 24000ppm,
COD: 18000ppm, glycerin: 8900ppm, PH
5.0), this strain, and as a control,
Hansenula anomala Y-1, Kluyveromyces
KL-5 and Hansenula anomala AM-6 were inoculated at 107 bacteria/ml and cultured at 30°C for 40 hours. The results are shown in the following table.
【表】
上記結果からも明らかなように、本菌が極めて
有効的にグリセリンを資化しBODを低下させた
ことが分る。
本発明は、上記したサツカロミセス・セレビシ
エーバル エリプソイデユウス YS−1
FERM−P No.4498(以下、「YS−1」菌という
場合もある)のほか、サツカロミセスに属する各
菌が適宜使用され、その例としては例えば次のも
のが挙げられる:Saccharomyces bayanus IFO
2027;S.bisporus ATCC 8381;S.chevalieri
NRRL Y−1547;S.rosei IFO 1180;S.rouxii
IFO 0846;S.uvarum NRRL Y−1005。
本発明における廃水処理は、グリセリン含有廃
水そのもの、その希釈液、あるいは濾過、遠心分
離、化学的処理等の前処理を行つたものに、サツ
カロミセス属菌を接種して行う。サツカロミセス
属菌は、純粋培養して得た菌体、菌体を分離する
ことなく種菌から大量培養して得た培養物を使用
してもよいし、実際に廃水処理を行つて大量増殖
した菌体を返送して使用してもよい。接種量は菌
体106〜107ケ/ml程度がよいが、培養時間の長短
によつて接種量は変更される。培養条件は20〜35
℃程度が好ましいが、20℃以下でも長時間培養す
れば廃水処理は可能である。培養は撹拌通気等、
好気的に行なわれる。本発明の処理において、必
要とあらば酵母の栄養剤としてリン源又は窒素源
たとえば尿素等を添加してもよい。
本発明によつて処理された廃水は、そのまま河
川に放流することができるが、これを更に、従来
より行われている下水、汚水処理で再度処理する
ことも可能である。
例えば、本発明菌体によつて処理されたグリセ
リン含有廃水は、そのままもしくはCODの低減
された廃水等を適宜混合した後、活性汚泥槽に送
りこまれ、より有効にCODを除去される。この
際、廃水中に多量存在する菌体は分離してもよい
が、サツカロミセス属菌はビール酵母、パン酵母
等として食品工業において多用されているもので
あるので安全且つ無害であり、したがつてこれら
の菌体は特に分離除去する必要はなく、直接、そ
のまま活性汚泥槽に送り込んでも何ら差支えない
し、またその方が廃水処理操作上からも便利であ
る。しかも活性汚泥処理槽に送り込まれた酵母は
活性汚泥の栄養源となつて汚泥の活性が高めら
れ、構造体からの汚泥の剥離もなく活性汚泥処理
にきわめて好都合となり、有利である。
活性汚泥処理槽としては普通に使用されてい
る、ラグーン、散水濾床などのようなものでも広
く使用できるが、使用に便利なのはハニカム等の
構造体に活性汚泥を付着させたタイプの活性汚泥
処理槽である。
活性汚泥処理は菌体を含有させたまま散気管に
よつて通気しながら固定床に付着した活性汚泥帯
を循環させて行なわれる。
この処理によつて処理廃水のCOD6000ppm(酵
母菌体を含む)が20〜50ppm(微生物の自然沈降
後)程度にまで低減される。この際、自然沈降を
待たずに凝集剤による凝集沈澱や遠心分離機によ
る遠心分離等によつて強制的に微生物を分離して
もよいのは当然のことである。
凝集剤による凝集沈澱の処理方法としては常法
が適宜使用でき、例えば塩化第二鉄、ポリ塩化ア
ルミニウムおよびポリアクリルアミドの併用によ
る凝集沈澱法が有効である。
この凝集沈澱法では菌体を含有した処理廃水を
撹拌しながら塩化第二鉄を添加する。この添加に
よりPHは減少するので苛性ソーダ等のアルカリ液
によつてPHを6.5〜7.5、好ましくは7.0に調節す
る。このPHは巨大フロツク生成のための必要条件
である。鉄イオンの増加によりCOD残量は減少
する、しかし多量の添加は経済的ではなく、また
鉄イオンの処理液残留を来すので好ましくない。
好適には第二鉄イオンで100〜300ppmの濃度分の
添加が必要である。
上記PH調節のもとでポリ塩化アルミニウムを10
%液で廃水1m3当り200〜300ml程度添加し、更に
ポリアクリルアミドを10ppm程度追加してフロツ
クの巨大化を行なわせる。生成されたフロツクの
定速沈降速度は大きく5〜6m/時であり、凝集
沈澱によるフロツク分離除去は十分に可能であ
る。得られた沈澱は濾過によつて容易に分離され
る。廃水の最終COD、BODは共に5〜30ppmと
なり、そのまま放流できるようになる。
サツカロミセス属菌は単用してもよいが、必要
に応じて各種の菌を同種内で又は異種間で併用し
てもよい。併用の場合には、各菌の混合培養物を
予じめ調整しておくと便利である。
(発明の効果)
以上詳述したように、本発明は、従来処理する
ことが困難であつたグリセリン含有廃水を、YS
−1菌をはじめとするグリセリン資化性サツカロ
ミセス属菌で処理することにより、はじめて工業
的に且つ大量に処理することを可能にしたもので
あつて、廃水処理、特に食品工場の廃水処理にお
いて極めて顕著な貢献をなすものである。
しかもこのようにして処理された廃水は、従来
より広く用いられている活性汚泥を破壊したりす
ることがないので、引続き、通常使用されている
活性汚泥槽に導いて直接処理することができ、グ
リセリン含有廃水のCOD及びBODを約5〜
30ppm程度にまで容易に低減することができる、
換言すればほとんど完全に近いレベルにまで低減
することができるという著効が得られる。
したがつて、本発明は、廃水、特に脂肪酸関連
製品製造廃水の処理に益するところきわめて大な
るものがある。
またSaccharomyces属菌は、その大半が食用
に供せられるものであつて、毒性の心配が全くな
いために、増殖菌体は動物や家禽の飼料ないし魚
の餌料等にも利用することができ、きわめて有益
である。
次に本発明の試験例及び実施例を示す。
試験例 1
グリセリン含有廃水(COD18000ppm.PH5.0)
50mlを500ml坂口フラスコに入れた。
一方、Saccharomyces cerevisiae var.
ellipsoideus YS−1 FERM−P No.4498を
MY培地50mlに一白金耳づつ接種し、30℃で20時
間振盪培養し、培養終了後菌体を遠心分離し、更
に生理食塩水を用いて洗滌し、接種用菌体とし
た。この菌体を菌数107ケ/mlになるように、前
記フラスコに接種し、30℃で40時間振盪処理し
た。処理前と処理後のCOD(ppm)、グリセリン、
全N(ppm)、全P(ppm)を測定し除去率(%)
を算定した。その結果は次の表に示される。[Table] As is clear from the above results, it can be seen that this bacterium extremely effectively assimilated glycerin and lowered BOD. The present invention relates to the above-mentioned Saccharomyces cerevisiaeval ellipsoideus YS-1.
In addition to FERM-P No. 4498 (hereinafter sometimes referred to as "YS-1" bacteria), various bacteria belonging to Saccharomyces are used as appropriate, such as the following: Saccharomyces bayanus IFO
2027; S. bisporus ATCC 8381; S. chevalieri
NRRL Y-1547; S.rosei IFO 1180; S.rouxii
IFO 0846; S. uvarum NRRL Y-1005. The wastewater treatment in the present invention is carried out by inoculating the glycerin-containing wastewater itself, its diluted solution, or pre-treated water such as filtration, centrifugation, chemical treatment, etc. with Satucharomyces bacteria. Bacteria of the genus Satucharomyces may be used as bacteria obtained by pure culture, cultures obtained by mass culturing from seed bacteria without separating the bacteria, or bacteria grown in large quantities through actual wastewater treatment. The body may be returned and used. The amount of inoculation is preferably about 10 6 to 10 7 cells/ml, but the amount of inoculation is changed depending on the length of culture time. Culture conditions are 20-35
℃ is preferred, but wastewater treatment is possible if cultured for a long time at temperatures below 20℃. For culture, use stirring aeration, etc.
It is done aerobically. In the treatment of the present invention, a phosphorus source or a nitrogen source such as urea may be added as a yeast nutrient, if necessary. Although the wastewater treated according to the present invention can be discharged into a river as it is, it is also possible to treat it again using conventional sewage and sewage treatment. For example, glycerin-containing wastewater treated by the microbial cells of the present invention is sent to an activated sludge tank as it is or after being mixed with wastewater with reduced COD, etc., to more effectively remove COD. At this time, bacterial cells present in large quantities in the wastewater may be separated, but bacteria of the genus Satucharomyces are safe and harmless as they are widely used in the food industry as brewer's yeast, baker's yeast, etc. It is not necessary to separate and remove these microbial cells, and there is no problem in directly feeding them into the activated sludge tank as they are, and this is also more convenient from the standpoint of wastewater treatment. Furthermore, the yeast sent into the activated sludge treatment tank becomes a nutrient source for the activated sludge, increasing the activity of the sludge, and there is no peeling of sludge from the structure, which is extremely convenient for activated sludge treatment, which is advantageous. Although commonly used activated sludge treatment tanks such as lagoons and trickling filters can be widely used, the most convenient type of activated sludge treatment is one in which activated sludge is attached to a structure such as a honeycomb. It's a tank. Activated sludge treatment is carried out by circulating the activated sludge zone adhering to a fixed bed while aerating it through an aeration tube while still containing bacterial cells. Through this treatment, the COD of treated wastewater (including yeast cells) is reduced to about 20 to 50 ppm (after natural sedimentation of microorganisms). In this case, it is a matter of course that the microorganisms may be forcibly separated by coagulation and sedimentation using a flocculant, centrifugation using a centrifuge, etc. without waiting for natural sedimentation. Conventional methods can be used as appropriate for the treatment of coagulation and precipitate using a flocculant; for example, a coagulation and precipitation method using a combination of ferric chloride, polyaluminum chloride and polyacrylamide is effective. In this coagulation-sedimentation method, ferric chloride is added to treated wastewater containing bacterial cells while stirring. This addition reduces the pH, so the pH is adjusted to 6.5 to 7.5, preferably 7.0, using an alkaline solution such as caustic soda. This pH is a necessary condition for the generation of giant flocs. The amount of COD remaining decreases as iron ions increase, but adding a large amount is not economical and also causes iron ions to remain in the treatment solution, which is undesirable.
Preferably, it is necessary to add ferric ions at a concentration of 100 to 300 ppm. 10% polyaluminum chloride under the above pH adjustment
Add about 200 to 300 ml of % solution per 1 m 3 of waste water, and add about 10 ppm of polyacrylamide to make the flocs larger. The constant sedimentation speed of the produced flocs is approximately 5 to 6 m/hour, making it possible to separate and remove the flocs by coagulation and sedimentation. The resulting precipitate is easily separated by filtration. The final COD and BOD of wastewater will both be 5 to 30 ppm, allowing it to be discharged as is. Bacteria of the genus Satucharomyces may be used alone, but various types of bacteria may be used in combination within the same species or between different species, if necessary. When used in combination, it is convenient to prepare a mixed culture of each bacteria in advance. (Effects of the Invention) As detailed above, the present invention can treat glycerin-containing wastewater, which has been difficult to treat with YS
-1 bacteria and other glycerol-assimilating bacteria of the genus Satucharomyces have made it possible for the first time to treat industrially and in large quantities. This is a significant contribution. Furthermore, the wastewater treated in this way does not destroy the activated sludge that has been widely used in the past, so it can be directly treated by being led to a commonly used activated sludge tank. COD and BOD of glycerin-containing wastewater from approximately 5 to
can be easily reduced to around 30ppm,
In other words, it is possible to achieve the remarkable effect of being able to reduce the noise to an almost complete level. Therefore, the present invention has significant benefits in the treatment of wastewater, particularly wastewater from the manufacture of fatty acid-related products. In addition, the majority of Saccharomyces bacteria are edible, and there is no fear of toxicity, so the proliferating bacteria can be used as animal and poultry feed, fish feed, etc. Beneficial. Next, test examples and examples of the present invention will be shown. Test example 1 Glycerin-containing wastewater (COD18000ppm.PH5.0)
50ml was placed in a 500ml Sakaguchi flask. On the other hand, Saccharomyces cerevisiae var.
ellipsoideus YS-1 FERM-P No.4498
One platinum loopful was inoculated into 50 ml of MY medium, cultured with shaking at 30°C for 20 hours, and after the cultivation was completed, the bacterial cells were centrifuged and further washed with physiological saline to prepare bacterial cells for inoculation. These bacterial cells were inoculated into the flask at a concentration of 107 cells/ml, and shaken at 30°C for 40 hours. COD (ppm), glycerin, before and after treatment
Measure total N (ppm) and total P (ppm) and remove rate (%)
was calculated. The results are shown in the following table.
【表】
試験例 2
試験例1と処理条件を同様に行ない、下記の各
菌株を菌数107ケ/ml接種し30℃で40時間振盪処
理を行ない処理後のPH、BOD除去率(%)菌数
を測定した。
1 Saccharomyces cerevisiae var.
ellipsoideus YS−1、FERM−P No.4498
2 Hansenula anomala Y−1 FERM−P
No.3594
3 Kluyveromyces sp.KL−5 FERM−P
No.3970
4 Harsenula anomala AM−6
その結果は次の表に示される。[Table] Test Example 2 The same treatment conditions as Test Example 1 were carried out, and the following bacterial strains were inoculated at a number of 107 bacteria/ml and shaken at 30°C for 40 hours to determine the PH and BOD removal rate (%) after treatment. ) The number of bacteria was measured. 1 Saccharomyces cerevisiae var.
ellipsoideus YS-1, FERM-P No.4498 2 Hansenula anomala Y-1 FERM-P
No.3594 3 Kluyveromyces sp.KL-5 FERM-P
No.3970 4 Harsenula anomala AM-6 The results are shown in the following table.
【表】
上表からも明らかなように、本菌が他の菌に比
較して卓越したBOD除去能を示すことがわかる。
試験例 3
MY培地
グルコース 10g
酵母エキス 3g
麦芽エキス 3g
ペプトン 5g
水 1000ml
上記MY培地においてグルコースの代りにグリ
セリン(1%)を用い、この培地をPH4.5に調整
したものを500ml坂口フラスコに100ml入れ、
Saccharomyces cerevisiae var.ellipsoideus YS
−1 FERM−P No.4498を107ケ/ml接種し、
30℃で40時間振盪処理し、処理後のPH、COD、
グリセリン、菌数を測定した。
その結果は次の表に示した。[Table] As is clear from the above table, this bacterium exhibits superior BOD removal ability compared to other bacteria. Test example 3 MY medium Glucose 10g Yeast extract 3g Malt extract 3g Peptone 5g Water 1000ml Use glycerin (1%) instead of glucose in the above MY medium, adjust this medium to pH 4.5, and put 100ml into a 500ml Sakaguchi flask. ,
Saccharomyces cerevisiae var.ellipsoideus YS
-1 FERM-P No.4498 was inoculated at 107 seeds/ml,
After shaking at 30℃ for 40 hours, the PH, COD,
Glycerin and bacterial counts were measured. The results are shown in the table below.
【表】
実施例 1
グリセリン含有廃水1.5を処理槽に入れ、こ
れにSaccharomyces cerevisiae var.
ellipsoideus YS−1、FERM−P No.4498を107
ケ/mlとなるように接種して培養後、30℃で通気
撹拌しながら滞留時間48時間になるように廃水を
連続的に送液し処理を行なつた。
20日間の連続処理でBODを平均75%除去し、
CODは平均71%除去し、グリセリンは90%から
95%の除去率を示し、安定して処理水が得られ
た。また引続き、活性汚泥処理槽において滞留時
間48〜72時間で通気処理し、処理された廃水は自
然沈降によつて汚泥と分離した。
上澄液は放流されるが20日間の連続処理で処理
水のCOD及びBODは10〜25ppmであつた。
実施例 2
実施例1において、YS−1菌の代りにサツカ
ロミセス・ウバルムNRRL Y−1005を用いて同
様にグリセリン含有廃水を処理して、河川放流可
能な処理水を得た。[Table] Example 1 1.5% of glycerin-containing wastewater was put into a treatment tank, and Saccharomyces cerevisiae var.
ellipsoideus YS-1, FERM-P No.4498 10 7
After inoculating and culturing at 30° C. with aeration and stirring, wastewater was continuously fed so that the residence time was 48 hours. Removes an average of 75% of BOD in 20 days of continuous treatment,
COD removes an average of 71%, glycerin from 90%
The removal rate was 95%, and treated water was stably obtained. Subsequently, the wastewater was aerated in an activated sludge treatment tank for a residence time of 48 to 72 hours, and the treated wastewater was separated from the sludge by natural sedimentation. The supernatant liquid was discharged, but the COD and BOD of the treated water were 10 to 25 ppm after 20 days of continuous treatment. Example 2 In Example 1, glycerin-containing wastewater was treated in the same manner as in Example 1 using Satucharomyces ubarum NRRL Y-1005 instead of the YS-1 bacteria to obtain treated water that could be discharged into a river.
Claims (1)
酵母をグリセリン含有廃水に添加し、グリセリン
を資化せしめることを特徴とするグリセリン含有
廃水の処理方法。1. A method for treating glycerin-containing wastewater, which comprises adding glycerol-assimilating yeast belonging to the genus Satucharomyces to glycerin-containing wastewater to assimilate glycerin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2880086A JPH0236320B2 (en) | 1986-02-14 | 1986-02-14 | HAISUISHORIHOHO |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2880086A JPH0236320B2 (en) | 1986-02-14 | 1986-02-14 | HAISUISHORIHOHO |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62186998A JPS62186998A (en) | 1987-08-15 |
| JPH0236320B2 true JPH0236320B2 (en) | 1990-08-16 |
Family
ID=12258504
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2880086A Expired - Lifetime JPH0236320B2 (en) | 1986-02-14 | 1986-02-14 | HAISUISHORIHOHO |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0236320B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2007013695A1 (en) * | 2005-07-29 | 2007-02-01 | Nippon Shokubai Co., Ltd. | Method of imparting glycerol-assimilation ability to bacterium |
| JP5366070B2 (en) * | 2007-09-27 | 2013-12-11 | 興人ライフサイエンス株式会社 | Method for producing yeast cells |
| JP5725813B2 (en) * | 2010-11-29 | 2015-05-27 | 渡辺 昌規 | Precipitation method for solid components of rice effluent |
| CN103969303B (en) * | 2014-05-15 | 2017-05-03 | 四川农业大学 | Method for rapidly determining BOD (Biochemical Oxygen Demand) by taking collagenous fiber loaded saccharomyces cerevisiae as biosensor identification element |
-
1986
- 1986-02-14 JP JP2880086A patent/JPH0236320B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62186998A (en) | 1987-08-15 |
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