JPH07308689A - Method for treating waste water containing fats and oils - Google Patents

Method for treating waste water containing fats and oils

Info

Publication number
JPH07308689A
JPH07308689A JP10256494A JP10256494A JPH07308689A JP H07308689 A JPH07308689 A JP H07308689A JP 10256494 A JP10256494 A JP 10256494A JP 10256494 A JP10256494 A JP 10256494A JP H07308689 A JPH07308689 A JP H07308689A
Authority
JP
Japan
Prior art keywords
oils
oil
fats
waste water
fat
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
Application number
JP10256494A
Other languages
Japanese (ja)
Other versions
JP2561441B2 (en
Inventor
Giichi Tsujiwaki
義一 辻脇
Hiroshi Yamamoto
浩志 山本
Kenji Minami
憲二 南
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
UEDA SEIYU KK
Original Assignee
UEDA SEIYU KK
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Priority to JP6102564A priority Critical patent/JP2561441B2/en
Publication of JPH07308689A publication Critical patent/JPH07308689A/en
Application granted granted Critical
Publication of JP2561441B2 publication Critical patent/JP2561441B2/en
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Expired - Fee Related legal-status Critical Current

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Abstract

PURPOSE:To improve reduction efficiency of content of fats and oils by adding Candida famata US-238 to waste water containing fats and oils to culture it under aerobic conditions, thereby reducing content of the fats and oils. CONSTITUTION:Candida famata US-238 is added to waste water containing fats and oils to culture it in an aerobic conditions, at pH 4-9, at culturing temperature of 20-42 deg.C, thereby reducing content of fats and oils in the waste water. The Candida famata US-238 is a strain which is separated from soil of Inno Island, Hiroshima Prefecture, Japan and is isolated by a predetermined screening method. Fats and oils in waste water are extracted with n-hexane, as an extracting agent, and concentration of the fats and oils in the waste water is set in the range of about 200-500mg/l, whereby a preferable result can be obtained. That is, waste water having concentration of 200mg/l or less is processed by concentrating it.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、家庭廃水または食品
加工工場等の産業廃水の浄化処理方法に関し、さらに詳
しくは微生物を用いた油脂含有廃水の処理方法に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying domestic wastewater or industrial wastewater such as food processing plants, and more particularly to a method for treating oil-containing wastewater using microorganisms.

【0002】[0002]

【従来の技術】従来、生物学的廃水処理方法として、活
性汚泥法が知られており、この方法では凝集性の強い細
菌を主体とする活性汚泥フロック表面に、微生物を付着
増殖させて有機物質を分解する。
2. Description of the Related Art Conventionally, an activated sludge method has been known as a biological wastewater treatment method. In this method, microorganisms are adhered to and proliferated on the flocs surface of activated sludge mainly composed of highly cohesive bacteria. Disassemble.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記した従来
の活性汚泥法による廃水処理では、廃水中の有機物のう
ち、蛋白質や糖類を低濃度化処理することに問題はない
が、家庭廃水または食品加工工場等の産業廃水のような
油脂を比較的高濃度に含む廃水を効率よく処理すること
が難しいという問題点がある。
However, in the conventional wastewater treatment by the above-mentioned activated sludge method, there is no problem in reducing the concentration of proteins and sugars among the organic substances in the wastewater, but domestic wastewater or foods. There is a problem in that it is difficult to efficiently treat wastewater containing fats and oils such as industrial wastewater at a processing factory in a relatively high concentration.

【0004】すなわち、従来の廃水処理方法では、油脂
含有廃水を予め油脂分離槽に通過させ、ここで油脂を分
離回収してこれを別途、産業廃棄物として処理している
のが現状であるが、そのような処理工程は複雑であり、
コストもかかるうえ、廃棄物としての取引も敬遠される
傾向が出始めている。
That is, in the conventional wastewater treatment method, the present situation is that the oil / fat-containing wastewater is passed through the oil / fat separation tank in advance, the oil / fat is separated and recovered, and the oil / fat is separately treated as industrial waste. , Such processing steps are complicated,
In addition to costs, transactions as waste are beginning to be shunned.

【0005】そこで、この発明の課題は、上記した問題
点を解決して、油脂含有廃水の処理方法を、低コスト化
が可能である比較的簡単な処理方法によって、効率よく
油脂含有量を低減させることである。
Therefore, an object of the present invention is to solve the above-mentioned problems and efficiently reduce the fat and oil content by a relatively simple treatment method which can reduce the cost of the fat and oil-containing wastewater. It is to let.

【0006】[0006]

【課題を解決するための手段】本願の発明者は、油脂含
有廃水の処理方法について検討を重ねた結果、特定の微
生物、即ちキャンディダ・ファマタ US−238を利
用することにより、廃水中の油脂含有量を効率よく低減
することができることを見いだし、この発明を完成させ
るに至った。
The inventor of the present application has made extensive studies on a method for treating oil-and-fat-containing wastewater, and as a result, by utilizing a specific microorganism, namely Candida famata US-238, It was found that the content can be efficiently reduced, and the present invention has been completed.

【0007】すなわち、前記の課題を解決するため、こ
の発明においては、油脂を含有する廃水にキャンディダ
・ファマタ US−238(FERM P−1397
4)を添加し、好気的条件で培養して前記廃水中の油脂
含有量を低下させたのである。
In other words, in order to solve the above-mentioned problems, in the present invention, wastewater containing oil and fat is added to Candida Famata US-238 (FERM P-1397).
4) was added and cultured under aerobic conditions to reduce the fat and oil content in the waste water.

【0008】また、上記手段において、培養する条件を
pH4〜9とし、または培養温度条件を20〜42℃と
することが好ましい。
In the above means, it is preferable that the culture condition is pH 4-9 or the culture temperature condition is 20-42 ° C.

【0009】以下に、その詳細を述べる。この発明に用
いるキャンディダ・ファマタ US−238(Cand
idafamata US−238)は、本願の発明者
が日本各地で採取された土壌から微生物を分離して、そ
の油脂に対する資化能を調べた結果、本願発明の目的を
最も効率よく達成できるものとして採用された菌株であ
り、これは広島県因島の土壌から分離し、次のスクリー
ニング方法により単離したものである。
The details will be described below. Candida Famata US-238 (Cand used for this invention
idafamata US-238) was adopted by the inventor of the present application as the one that most efficiently achieves the object of the present invention as a result of separating microorganisms from soil collected in various parts of Japan and examining their assimilation ability for oils and fats. The isolated strain was isolated from the soil of Innoshima Island, Hiroshima Prefecture, and was isolated by the following screening method.

【0010】[キャンディダ・ファマタ US−238
のスクリーニング方法]土壌の分離サンプルを下記組成
の培地Aに添加し、30℃で2〜3日培養した後、微生
物の増殖が見られるものについて、同じ培地で集積培養
を行ない、油脂資化能の強い菌を集積させた。そして、
培養液を遠心分離処理することによって上層にある油脂
の減少量を確認し、最も油脂資化能の強い菌を含む培養
液を同様な組成で構成した平板培地上に塗布し、培養
後、コロニーを単離し分取して目的とする菌株を得た。
[Candida Famata US-238
Screening method] The soil separation sample was added to the medium A having the following composition, and the mixture was cultured at 30 ° C. for 2 to 3 days. Then, for those in which the growth of microorganisms was observed, the accumulation culture was performed in the same medium to obtain the oil and fat assimilation ability. Accumulated strong bacteria. And
Confirm the reduction amount of oil and fat in the upper layer by centrifuging the culture solution, apply the culture solution containing the bacteria with the highest oil and fat assimilation ability on a plate medium composed of the same composition, after culturing, colonies Was isolated and fractionated to obtain the target strain.

【0011】 培地Aの組成:(pH8.0) 魚油 1 ml グルコース 3.5 mg 硝酸アンモニウム 35 mg リン酸水素二カリウム 14 mg 硫酸マグネシウム 7 mg 酵母エキス 7 mg 水道水 7 ml 前記得られた菌株の菌学的性状は以下の如くである。Composition of medium A: (pH 8.0) Fish oil 1 ml Glucose 3.5 mg Ammonium nitrate 35 mg Dipotassium hydrogen phosphate 14 mg Magnesium sulfate 7 mg Yeast extract 7 mg Tap water 7 ml Bacteria of the strain obtained above The scientific properties are as follows.

【0012】(1) 形態的性質 形態 卵型又は球形 細胞は1個又は数個連な
っている 大きさ (1〜6)×(2〜6)μ 出芽 多極出芽 偽菌糸 コーンミール培地で未発達な偽菌糸の形
成を認める 子嚢胞子 形成を認めず (2) 培養的性質(YM液体培地) 沈澱及び皮膜の形成を認める (3) 巨大コロニーの観察(YM寒天培地) 成育 良好 隆起状態 台状 表面の状態 平滑 色調 乳白色 (4) 生理学的性質 生育pH 3〜9 最適pH 5〜7 生育温度 約42℃まで 最適温度 20〜35 硝酸塩の資化性 − ビタミン欠培地での生育 − ジアゾニウムブルーBの呈色反応 − [発酵性] グルコース − ガラクトース − シュークロース − マルトース − ラクトース − ラフィノース − イノシトール − [資化性] グルコース + ガラクトース + シュークロース + マルトース + セロビオース + トレハロース + ラクトース − ラフィノース + メリチトース + スターチ + D−キシロース + L−アラビノース − D−リボース + L−ラムノース + エリスリトール − リビトール + D−マンニトール + コハク酸塩 + クエン酸塩 + イノシトール − 以上の結果から、分離された菌株は、キャンディダ・フ
ァマタ(Candida famata)であると同定
され、この株をキャンディダ・ファマタ US−238
(Candida famata US−238)と命
名した。
(1) Morphological properties Morphology Oval or globular cells are one or several in series Size (1-6) × (2-6) μ Budding multipolar budding Pseudohyphae Not developed in cornmeal medium Spontaneous mycelium formation is observed No ascospore formation is observed (2) Cultural properties (YM liquid medium) Precipitation and film formation are observed (3) Giant colony observation (YM agar medium) Good growth Upstanding trapezoid Surface condition Smooth tone Milky white (4) Physiological properties Growth pH 3-9 Optimum pH 5-7 Growth temperature Up to about 42 ℃ Optimum temperature 20-35 Nitrate assimilation-Growth in vitamin-deficient medium-Diazonium blue B Color reaction- [fermentability] glucose-galactose-sucrose-maltose-lactose-raffinose-inositol- [assimilation] glucose + galactose + sucrose + Maltose + cellobiose + trehalose + lactose-raffinose + melitithose + starch + D-xylose + L-arabinose-D-ribose + L-rhamnose + erythritol-ribitol + D-mannitol + succinate + citrate- + citrate. From the results, the isolated strain was identified as Candida famata, and this strain was designated as Candida famata US-238.
(Candida famata US-238).

【0013】この菌株は、工業技術院生命工学工業技術
研究所に「微生物受託番号 生命研菌寄第13974号
(FERM P−13974)」として寄託されてい
る。
This strain has been deposited at the Institute of Biotechnology, Institute of Biotechnology, Institute of Industrial Science and Technology as "Microbial Accession No. Life Research Institute No. 13974 (FERM P-13974)".

【0014】この発明における廃水中の油脂は、油脂抽
出溶剤として周知のn−ヘキサンで抽出される物質であ
る。
The oil / fat in the waste water in the present invention is a substance which is well known as an oil / fat extraction solvent and is extracted with n-hexane.

【0015】このような油脂を含有する被処理廃水中の
油脂含有量は、特に限定されるものではないが、油脂濃
度が200〜5000mg/lの廃水を処理して良好な
結果を得ている。すなわち、油脂濃度が比較的高濃度の
廃水は、そのまま処理してもよいが、油脂濃度が200
mg/l未満といった低濃度の廃水は、油脂を濃縮し、
例えば5000mg/l程度まで油脂含有量を高めたも
のを処理すれば処理量が少なく、効率的である。
The content of fats and oils in the wastewater to be treated containing such fats and oils is not particularly limited, but good results have been obtained by treating wastewater having a fats and oils concentration of 200 to 5000 mg / l. . That is, wastewater having a relatively high fat concentration may be treated as it is,
Wastewater of low concentration such as less than mg / l concentrates fats and oils,
For example, if the oil and fat content is increased to about 5000 mg / l, the treatment amount is small and it is efficient.

【0016】油脂を含有する廃水の場合、前処理とし
て、自然浮上や加圧浮上装置で油脂を分離除去する油脂
分離槽を設けているが、この発明では、油脂分離槽を培
養槽として用い、所要量のキャンディダ・ファマタ U
S−238を添加し、pH4〜9、好ましくはpH6〜
7、温度20〜42℃、好ましくは30〜35℃で通気
攪拌をすることにより、油脂の分解除去を行なう。
In the case of wastewater containing fats and oils, as a pretreatment, a fats and oils separation tank for separating and removing fats and oils by a natural flotation device or a pressure flotation device is provided. In the present invention, the fats and oils separation tank is used as a culture tank. Required amount of Candida Famata U
S-238 is added, pH 4-9, preferably pH 6-
7. The oil and fat is decomposed and removed by aeration and stirring at a temperature of 20 to 42 ° C, preferably 30 to 35 ° C.

【0017】このようにして、油脂分を低減させた処理
水に活性汚泥を加えて周知の活性汚泥装置のエアレーシ
ヨンタンクに送り、油脂以外の有機物を分解除去するこ
とができる。
In this way, the activated sludge can be added to the treated water with reduced fat and oil and sent to the air race tank of the known activated sludge apparatus to decompose and remove organic substances other than fat and oil.

【0018】また、比較的油脂含有量が低い場合、例え
ば200mg/lの廃水では、上記したような前処理を
行わず、第1沈殿池を出た廃水に活性汚泥と共に本菌を
添加し、エアレーションタンクで適当なpHおよび温度
条件で処理し、油脂およびその他の有機物を同時に分解
除去することができる。そして、このように処理された
水は、第2沈殿池へ送って、上澄水を放流する。
When the oil / fat content is relatively low, for example, with 200 mg / l of waste water, the above pretreatment is not carried out, and the present bacteria are added to the waste water discharged from the first settling tank together with the activated sludge, By treating with an aeration tank under appropriate pH and temperature conditions, fats and oils and other organic substances can be decomposed and removed at the same time. Then, the water treated in this way is sent to the second settling tank, and the supernatant water is discharged.

【0019】通常、油脂含有廃水には、窒素、リン、微
量栄養素も含まれているので、キャンディダ・ファマタ
US−238の生育は、これらによって維持される
が、必要に応じてビタミン、ミネラル等の栄養素を添加
してもよい。特に、前処理として本菌単独で油脂分の低
減を行なう場合には、効率のよい培養条件にするため、
本菌の充分な生育を維持できる栄養条件に調整すること
が望ましい。
Normally, the fat-and-oil-containing wastewater also contains nitrogen, phosphorus, and micronutrients, so that the growth of Candida famata US-238 is maintained by these, but if necessary, vitamins, minerals, etc. Nutrients may be added. In particular, when the oil and fat content is reduced by the present bacterium alone as a pretreatment, in order to achieve efficient culture conditions,
It is desirable to adjust the nutritional conditions to maintain the sufficient growth of this bacterium.

【0020】[0020]

【実施例】次に実施例および比較例によりこの発明をさ
らに詳細に説明する。 〔実施例1〜5〕油脂として菜種油を含有し、これをn
−ヘキサン抽出物として5000mg/l(以下、この
濃度単位をppmと記す)含有する下記組成の培地に対
して、キャンディダ・ファマタ US−238を所定量
添加し、下記の条件で5日間培養後にn−ヘキサン抽出
量を調べ、この結果を表1に示した。
EXAMPLES The present invention will be described in more detail with reference to Examples and Comparative Examples. [Examples 1 to 5] Rapeseed oil was contained as an oil and fat, and n
-A predetermined amount of Candida famata US-238 was added to a medium having the following composition containing 5000 mg / l (hereinafter, this concentration unit is referred to as ppm) as a hexane extract, and after culturing for 5 days under the following conditions: The amount of n-hexane extracted was examined, and the results are shown in Table 1.

【0021】[培地] 菜種油 0.5 g(5000pp
m) 硫酸アンモニウム 0.5 g 硫酸マグネシウム 0.10g 酵母エキス 0.10g 0.25Mリン酸緩衝液 100 ml [実験条件] 供試料 上記培地 菌体添加量 1白金耳 培養方法 振とう培養 供試料容量 100ml(500ml容量の
フラスコ使用) 培養温度 30℃ pH 4、6、7、8、9 培養日数 5日間
[Medium] 0.5 g of rapeseed oil (5000 pp
m) Ammonium sulphate 0.5 g Magnesium sulphate 0.10 g Yeast extract 0.10 g 0.25 M phosphate buffer 100 ml [Experimental conditions] Sample to be tested Medium to be added to the medium 1 Platinum loop Culture method Shake culture Sample volume to be supplied 100 ml (Using a flask with a capacity of 500 ml) Culture temperature 30 ° C. pH 4, 6, 7, 8, 9 Culture days 5 days

【0022】[0022]

【表1】 [Table 1]

【0023】表1の結果からも明らかなように、実施例
1〜5の処理方法ではpH4〜9の条件で油脂処理能力
があり、特にpH6付近(実施例2)が最適の条件であ
ることがわかる。
As is clear from the results shown in Table 1, the treatment methods of Examples 1 to 5 have a fat and oil treating ability under the conditions of pH 4 to 9, and the optimum conditions are around pH 6 (Example 2). I understand.

【0024】〔実施例6〜7〕実施例2において油脂と
して菜種油に代えてラードまたはパーム油を用いたこと
以外は全く同様の条件で5日培養した後、培地中のラー
ドまたはパーム油のn−ヘキサンの抽出量(ppm)を
調べ、結果を表2に示した。
[Examples 6 to 7] After culturing for 5 days under exactly the same conditions except that lard or palm oil was used as the oil and fat in place of rapeseed oil in Example 2, n of lard or palm oil in the medium was used. The amount of hexane extracted (ppm) was examined, and the results are shown in Table 2.

【0025】[0025]

【表2】 [Table 2]

【0026】表2の結果からも明らかなように、常温で
固体の油脂を含有する廃水を処理する場合では、常温で
液体の油脂を含む被処理系の実施例1〜5に比べて油脂
の低減効率は劣るが、廃水処理法としては良好であるこ
とがわかる。
As is clear from the results shown in Table 2, when treating wastewater containing fats and oils that are solid at room temperature, compared to Examples 1 to 5 of the system to be treated that contains fats and oils that are liquid at room temperature, It can be seen that although the reduction efficiency is poor, it is a good wastewater treatment method.

【0027】〔実施例8〜10、比較例1〕実施例8〜
10については、供試料容量を50ml(100ml容
量のフラスコ使用)とし、油脂として菜種油、ラードま
たはパーム油を採用し、培養温度を20℃、30℃、4
0℃に設定し、スターラーによって攪拌したこと以外の
条件は培養時のpHが6である実施例2の処理条件と全
く同様にして5日培養処理した後、培地中の菜種油、ラ
ードまたはパーム油のn−ヘキサンの抽出量(ppm)
を調べ、結果を表3に示した。
[Examples 8 to 10, Comparative Example 1] Examples 8 to
For No. 10, the sample volume was 50 ml (100 ml volume flask was used), rapeseed oil, lard or palm oil was adopted as the fat and oil, and the culture temperature was 20 ° C, 30 ° C, 4 ° C.
After culturing for 5 days, the conditions were set to 0 ° C. and the stirring was carried out with a stirrer in exactly the same manner as in Example 2 in which the pH was 6 during the culturing, and then rapeseed oil, lard or palm oil in the medium was used. Extraction amount of n-hexane (ppm)
Was examined and the results are shown in Table 3.

【0028】比較例1については、培養温度を10℃と
し、その他の条件については実施例8と全く同様にして
培養して、n−ヘキサンの抽出量(ppm)を調べ、結
果を表3に併記した。
In Comparative Example 1, the culturing temperature was set to 10 ° C., and the other conditions were cultivated in the same manner as in Example 8 to examine the extraction amount (ppm) of n-hexane, and the results are shown in Table 3. I also wrote it down.

【0029】[0029]

【表3】 [Table 3]

【0030】表3の結果からも明らかなように、この発
明の廃水処理方法における処理温度は、20〜40℃と
した場合に処理効率の良いことがわかり、10℃では成
績は良くなかった。
As is clear from the results shown in Table 3, the treatment efficiency in the wastewater treatment method of the present invention was found to be good when the treatment temperature was 20 to 40 ° C, and the result was not good at 10 ° C.

【0031】〔実施例11〜16〕実施例2(pH6)
の処理条件を採用し、油脂濃度が5〜30容量%(w/
V)という非常に高濃度に油脂を含む被処理系を処理し
た場合について、処理5日後のn−ヘキサン抽出量
(g)と、この処理で分解された油脂量(g)を調べ、
結果を表4に示した。
[Examples 11 to 16] Example 2 (pH 6)
The treatment conditions are adopted, and the oil and fat concentration is 5 to 30% by volume (w /
V), when a system to be treated containing oil and fat at a very high concentration was treated, the amount of extracted n-hexane (g) after 5 days of treatment and the amount of oil and fat decomposed by this treatment (g) were examined,
The results are shown in Table 4.

【0032】[0032]

【表4】 [Table 4]

【0033】表4の結果からも明らかなように、実施例
11〜16の処理方法では、油脂濃度の高い条件である
にも拘わらず安定して油脂を低減しており、この発明に
使用した微生物の油脂資化能力は高濃度の油脂中でも殆
ど衰えないことがわかる。
As is clear from the results shown in Table 4, in the treatment methods of Examples 11 to 16, the fats and oils were stably reduced in spite of the high oil and fat concentration conditions, and were used in the present invention. It can be seen that the ability of microorganisms to assimilate fats and oils hardly deteriorates even in a high concentration of fats and oils.

【0034】〔実施例17〕実施例2(pH6)の処理
条件を採用し、すなわち油脂として菜種油を採用し、供
試料容量を8ml(40ml容量の試験管使用)とし、
その他は実施例2と全く同様の条件で処理を行ない、処
理日数毎のn−ヘキサン抽出量を調べ、結果を表5に示
した。
Example 17 The treatment conditions of Example 2 (pH 6) were adopted, that is, rapeseed oil was adopted as the oil and fat, and the sample volume was 8 ml (using a 40 ml test tube),
Other than that, the treatment was carried out under the same conditions as in Example 2, and the extraction amount of n-hexane for each treatment day was examined, and the results are shown in Table 5.

【0035】[0035]

【表5】 [Table 5]

【0036】この結果処理日数は1〜2日で充分な油脂
含有量低減効果があることがわかる。
As a result, it can be seen that the number of days of treatment is 1 to 2 days, and there is a sufficient effect of reducing the fat and oil content.

【0037】〔実施例18〕実際の廃水として、n−ヘ
キサン抽出物質を5300mg/l含有する当社(植田
製油株式会社)油脂工場の廃水を被処理廃水として用
い、pH6に調整した後、実施例17(すなわち、実施
例2に同じ)と全く同様の処理条件で3日間処理し、そ
の後のn−ヘキサン抽出量を調べた。
[Example 18] As an actual wastewater, the wastewater of our company (Ueda Oil Co., Ltd.) oil and fat factory containing 5300 mg / l of n-hexane extract was used as the wastewater to be treated, and after adjusting to pH 6, Treatment was carried out for 3 days under the treatment conditions exactly the same as in No. 17 (that is, the same as in Example 2), and the amount of extracted n-hexane after that was examined.

【0038】この結果、上記処理後の廃水に含まれるn
−ヘキサン抽出物質は、150mg/lに減少してお
り、この処理により顕著な油脂含有量低減効果のあるこ
とを確認した。
As a result, n contained in the wastewater after the above treatment
The amount of hexane-extracted substance was reduced to 150 mg / l, and it was confirmed that this treatment had a remarkable effect of reducing the fat and oil content.

【0039】〔比較例2〜10〕実施例17の処理条件
を採用し、キャンディダ・ファマタ US−238に代
えて、脂質資化性酵母として知られた代表的な下記9種
の微生物(菌株)を採用し、その他は実施例17と全く
同様の条件で処理を行ない、処理日数毎のn−ヘキサン
抽出量を調べ、結果を表5に併記した。
[Comparative Examples 2 to 10] Using the treatment conditions of Example 17, instead of Candida famata US-238, the following nine kinds of typical microorganisms (strains) known as lipid-assimilating yeasts were used. ) Was used, and the other conditions were the same as in Example 17, and the amount of n-hexane extracted for each treatment day was examined. The results are also shown in Table 5.

【0040】 [比較例として使用する微生物(菌株)] (1) Candida bombicola IFO 10243 (2) C. famata IFO 0664 (3) C. famata IFO 0856 (4) C. rugosa IFO 0750 (5) Pichia candensis IFO 0973 (6) P. kluyveri IFO 1165 (7) Rodotorula javanica IFO 10285 (8) Trichosporon pullulans IFO 1232 (9) Yarrowia lipolytica IFO 1548 表5の結果からも明らかなように、キャンディダ・ファ
マタ US−238株以外の株を用いた処理法では、油
脂資化効率が充分でなかった。
[Microorganisms (Strains) Used as Comparative Examples] (1) Candida bombicola IFO 10243 (2) C.I. famata IFO 0664 (3) C.I. famata IFO 0856 (4) C.I. rugosa IFO 0750 (5) Pichia candensis IFO 0973 (6) P. kluyveri IFO 1165 (7) Rodotorula javanica IFO 10285 (8) Trichosporon pullulans IFO 1232 (9) Yarrowia lipolytica IFO 1548 As well as the results of Table 5, it is clear that the candida is 38. According to the method, the efficiency of assimilating fats and oils was not sufficient.

【0041】〔比較例11〜19〕実施例11の処理条
件を採用し、油脂濃度が5容量%(w/V)という高濃
度の被処理系を処理した場合について、前記微生物
(1)〜(9)を採用し、処理5日後のn−ヘキサン抽
出量(g)と、この処理で分解された油脂量(g)を調
べ、結果を表6に示した。
[Comparative Examples 11 to 19] Using the treatment conditions of Example 11 and treating a high-to-be-treated system having a fat and oil concentration of 5% by volume (w / V), the microorganisms (1) to Using (9), the amount of extracted n-hexane (g) after 5 days of treatment and the amount of fats and oils decomposed by this treatment (g) were examined, and the results are shown in Table 6.

【0042】[0042]

【表6】 [Table 6]

【0043】表6の結果からも明らかなように、比較例
11〜19の処理方法では、分解される油脂量は少な
く、これに対して前記したキャンディダ・ファマタ U
S−238株を用いた実施例11の処理方法がきわめて
優位であることがわかる。
As is clear from the results shown in Table 6, in the treatment methods of Comparative Examples 11 to 19, the amount of oil and fat decomposed was small, and in contrast to this, the above-mentioned Candida famata U was used.
It can be seen that the treatment method of Example 11 using the S-238 strain is extremely superior.

【0044】[0044]

【効果】この発明は、以上説明したように、キャンディ
ダ・ファマタの所定菌株を油脂含有廃水に添加し、好気
的条件で培養するといった簡便な方法により、油脂含有
廃水の油脂含有量を効率よく低減させて、低コストで実
用的にも優れた油脂含有廃水処理方法を提供できる利点
がある。
[Effect] As described above, the present invention efficiently increases the oil content of oil-containing wastewater by a simple method of adding a predetermined strain of Candida famata to the oil-containing wastewater and culturing under aerobic conditions. There is an advantage that the oil / fat-containing wastewater treatment method that is well reduced and is low in cost and excellent in practical use can be provided.

【0045】また、培養処理の際に所定のpHおよび温
度条件とすれば、さらに効率よく処理でき、さらに他の
有用微生物を併用すれば、さらに有利な処理方法となる
のであるから、非常に利用価値の高い発明であるといえ
る。
Further, when the culture treatment is carried out under the prescribed pH and temperature conditions, the treatment can be carried out more efficiently, and when other useful microorganisms are used in combination, the treatment method becomes more advantageous. It can be said that this is a high-value invention.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 油脂を含有する廃水にキャンディダ・フ
ァマタ US−238(FERM P−13974)を
添加し、好気的条件で培養して前記廃水中の油脂含有量
を低下させることからなる油脂含有廃水の処理方法。
1. An oil and fat comprising adding Candida Famata US-238 (FERM P-13974) to waste water containing the oil and fat, and culturing under aerobic conditions to reduce the oil and fat content in the waste water. Treatment method of wastewater containing.
【請求項2】 前記培養する条件がpH4〜9である請
求項1に記載の油脂含有廃水の処理方法。
2. The method for treating oil-and-fat-containing wastewater according to claim 1, wherein the culture conditions are pH 4-9.
【請求項3】 前記培養する温度条件が20〜42℃で
ある請求項1に記載の油脂含有廃水の処理方法。
3. The method for treating waste oil-containing wastewater according to claim 1, wherein the temperature condition for culturing is 20 to 42 ° C.
JP6102564A 1994-05-17 1994-05-17 Treatment method of oil-containing wastewater Expired - Fee Related JP2561441B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Application Number Priority Date Filing Date Title
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JP2561441B2 JP2561441B2 (en) 1996-12-11

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11319882A (en) * 1998-05-11 1999-11-24 Oppenheimer Technology Japan:Kk Treatment of oil-containing waste water and treating device
JP2020191802A (en) * 2019-05-27 2020-12-03 三菱ケミカルアクア・ソリューションズ株式会社 Microorganisms, agents and methods for decomposing oil components

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5685783B2 (en) 2012-01-19 2015-03-18 国立大学法人名古屋大学 Novel Yarrowia microorganism, oil decomposing agent and oil decomposing / removing method using the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11319882A (en) * 1998-05-11 1999-11-24 Oppenheimer Technology Japan:Kk Treatment of oil-containing waste water and treating device
JP2020191802A (en) * 2019-05-27 2020-12-03 三菱ケミカルアクア・ソリューションズ株式会社 Microorganisms, agents and methods for decomposing oil components

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