JPS6014996A - Treatment of waste water produced in food manufacture and the like - Google Patents

Treatment of waste water produced in food manufacture and the like

Info

Publication number
JPS6014996A
JPS6014996A JP12241283A JP12241283A JPS6014996A JP S6014996 A JPS6014996 A JP S6014996A JP 12241283 A JP12241283 A JP 12241283A JP 12241283 A JP12241283 A JP 12241283A JP S6014996 A JPS6014996 A JP S6014996A
Authority
JP
Japan
Prior art keywords
yeast
waste water
wastewater
treatment
immobilized
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
JP12241283A
Other languages
Japanese (ja)
Other versions
JPH0137986B2 (en
Inventor
Makoto Tadenuma
蓼沼 誠
Makoto Sato
信 佐藤
Kazuo Saito
斎藤 和夫
Tetsuo Hasuo
徹夫 蓮尾
Kiyoshi Yoshizawa
吉沢 淑
Kikuo Noshiro
野白 喜久雄
Takeo Koizumi
武夫 小泉
Kenkichi Kodama
小玉 健吉
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.)
TAX ADM AGENCY
Original Assignee
TAX ADM AGENCY
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by TAX ADM AGENCY filed Critical TAX ADM AGENCY
Priority to JP12241283A priority Critical patent/JPS6014996A/en
Publication of JPS6014996A publication Critical patent/JPS6014996A/en
Publication of JPH0137986B2 publication Critical patent/JPH0137986B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE:To perform treatment of waste water of high concentration and large fluctuation of load efficiently by removing org. substances in waste water produced in food manufacture, etc. by treating with immobilized yeast for metabolizing starch, protein, ethyl alcohol, etc. CONSTITUTION:Metabolizing yeast for at least one selected from starch, protein, fat, sugar, org. acid, amino acid, ethyl alcohol, glycerin, lignin, tannin, and pectin, is immoblized by gel entrapping method, carrier coupling method, or crosslinking polymn. method, etc. The pH of the waste water produced in food manufacture is regulated to 3-8, more pref. <=6 in order to prevent contamination by other microorganisms, and the temp. of the waste water is regulated to 10-45, more pref. 20-35 deg.C. The treatment of the waste water is performed by adding above described immobilized yeast. In addition, sodium hypochlorite, etc. is preferred to be added to the waste water in order to prevent contamination by microorganisms other than the yeast.

Description

【発明の詳細な説明】 本発明は、固定化酵母による食品製造等廃水の処理方法
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating wastewater from food production and the like using immobilized yeast.

発明者等は酵母による食品製造廃水の新I〜い処理方式
を開発し、酵母処理単独あるいは酵母と活性汚泥処理を
組合せることによシ高濃度、かつ、負荷変動の激しい食
品製造廃水を効率的に処理できることを明らかにした。
The inventors have developed a new treatment method for food manufacturing wastewater using yeast, and efficiently treat food manufacturing wastewater with high concentrations and large load fluctuations by using yeast treatment alone or by combining yeast and activated sludge treatment. It has been shown that it can be effectively processed.

〔吉沢:農化、J−J。[Yoshizawa: Agriculture, J-J.

70j〜7//(/りg/)〕 酵母処理法の要点は、−足以上(辿常108/m1以上
)の酵母密度を維持していくことであるが、条件によっ
ては、添加した酵母の他の微生物による侵襲又は捕食、
他の細菌との廃水中の栄養摂取の競合及び他の酵母によ
る汚染等の原因により、目的とする酵母が一定の酵母密
度を維持できなくなることがある。
70j~7//(/g/)] The key point of the yeast treatment method is to maintain a yeast density of -108/ml or higher (usually 108/ml or higher), but depending on the conditions, the added yeast invasion or predation by other microorganisms,
The target yeast may not be able to maintain a constant yeast density due to competition with other bacteria for nutrients in the wastewater and contamination by other yeasts.

また、廃水によっては必ずしも、単一の酵母のを みて廃水中の全ての有機物0資化分解するだけでは不十
分で、数種の酵母を混合して使用した方が効果的なもの
がある。その場合、数種の酵母が常に安定した菌相を示
すとは限らず、むしろ、強力な生存力を有する単一酵母
菌株が他の酵母を抑えてしまう場合が多い。
Furthermore, depending on the wastewater, it may not be sufficient to use a single yeast to completely decompose all the organic matter in the wastewater, and it may be more effective to use a mixture of several types of yeast. In such cases, several types of yeast do not always exhibit a stable bacterial flora; rather, a single yeast strain with strong viability often suppresses other yeasts.

そこで、所望の酵母を常に安定した密度に保つ方法につ
き鋭意、検討した結果、廃水処理用酵母を固定化酵母と
して用いることにより、従来の酵母処理法の問題点を全
て解決できることを見いだし、本発明を完成1〜た。
Therefore, as a result of intensive study on a method for keeping the desired yeast at a stable density, it was discovered that by using wastewater treatment yeast as an immobilized yeast, all the problems of conventional yeast treatment methods could be solved, and the present invention was developed. Completed 1~.

以下、不発明の詳細な説明する。Hereinafter, the non-invention will be explained in detail.

本発明に用いる酵母は、発明者等が用いている廃水処理
用酵母ならいずれでもよい。食品製造廃水中の有機物は
、主としてデンプン、タンパク質、脂肪、それらの中間
分解物並びにそれらの構成単位である糖類、有機酸等か
らなっており、その他に酒類製造廃水ではエチルアルコ
ールやグリセロール等のアルコール類も主要な有機物と
して含まれ、ワインやブランデー製造廃水ではリグニン
やタンニンが、果汁等の製造廃水ではペクチンがそれぞ
れ難分解性有様物として含まれている。
The yeast used in the present invention may be any yeast for wastewater treatment used by the inventors. Organic matter in food manufacturing wastewater mainly consists of starch, protein, fat, their intermediate decomposition products, and their constituent units, such as sugars and organic acids.In addition, alcohol manufacturing wastewater contains alcohols such as ethyl alcohol and glycerol. Wastewater from the production of wine and brandy contains lignin and tannin, and wastewater from the production of fruit juice and the like contains pectin as non-degradable substances.

1〜たがって、対象とする廃水の組成によって、例えば
第1表に示した各種有機物の資化能を有する酵母を固定
化1〜、廃水によっては2種以上の酵母をそれぞれ固定
化したものの混合物又は2種以上の酵母を混合後、固定
化したもので処理することにより効果的に1児水を処理
することができる。
1- Therefore, depending on the composition of the target wastewater, for example, yeast having the ability to assimilate various organic substances shown in Table 1 may be immobilized.1- Depending on the wastewater, a mixture of two or more types of yeast may be immobilized. Or, by mixing two or more types of yeast and then treating with the immobilized yeast, single-child water can be effectively treated.

固定化酵母を用いれば、2種以上の酵母の混合比率を廃
水の種類によって自由に選ぶことができ、また、常に安
定した比率を保つことができる。
If immobilized yeast is used, the mixing ratio of two or more types of yeast can be freely selected depending on the type of wastewater, and a stable ratio can always be maintained.

対象とする廃水は、主として食品製造廃水が適するが、
第1表に示す有機物を含む廃水であれば十分処理可能で
ある。例えば、油脂を原料とする工業ではその廃水中に
有機酸やグリセロールが多量に含まれ、これらの有機物
を資化分解する固定化酵母を使用することにより、廃水
中の有機物を大幅に減少させることができる。
The target wastewater is mainly food manufacturing wastewater, but
Any wastewater containing organic substances shown in Table 1 can be sufficiently treated. For example, in industries that use fats and oils as raw materials, wastewater contains large amounts of organic acids and glycerol, and by using immobilized yeast that assimilates and decomposes these organic substances, organic substances in wastewater can be significantly reduced. Can be done.

酵母の固定化は既知の固定化法、例えばゲル包括法、担
体結合法又は架橋重合法のいずれを用いてもよい。
Yeast may be immobilized using any known immobilization method, such as gel entrapment method, carrier binding method, or crosslinking polymerization method.

固定化酵母による廃水の条件としては廃水のpHが3〜
どの広い範囲、好ましくは他の微生物による汚染を防止
するためK pH,4以下とし、処理温度は固定化に用
いた酵母によって異なるが、10〜4t!℃の範囲、好
ましくは20〜33’Cがよい。
The conditions for wastewater produced by immobilized yeast are that the pH of the wastewater is between 3 and 3.
Within a wide range, preferably K pH, 4 or less to prevent contamination by other microorganisms, and the treatment temperature varies depending on the yeast used for immobilization, but is 10-4T! ℃ range, preferably 20 to 33'C.

酵母以外の他の微生物による汚染を防止するためにはp
14調整とともに、次亜塩素酸ナトリウム又は亜硫酸を
それぞれ廃水に20〜30 ppm又Vitt。
To prevent contamination by microorganisms other than yeast, p.
Vitt.

ppmとなるように、毎日又は隔日ごとに65加すると
、より効果的である。
It is more effective to add 65 ppm every day or every other day.

処理槽の材質は、特に限定しないが耐酸性のものが望ま
しい。処理槽はエアーポンプ等により通気かくはんを行
い、場合によってはかくはん様によるかくはんを行えば
、通気効果をさらにあげることができる。食品工場等に
は使用していない空タンクを保有している工場が多く、
それらの空タンクにエアーポンプを付けるだけで固定化
酵母槽として使用できるので、本発明によれば、極めて
安価に廃水処理を行うことができる。
The material of the treatment tank is not particularly limited, but acid-resistant materials are desirable. The treatment tank can be aerated and agitated using an air pump or the like, and in some cases, agitated by an agitator to further increase the aeration effect. Many food factories have empty tanks that are not in use.
Since these empty tanks can be used as immobilized yeast tanks simply by attaching an air pump, according to the present invention, wastewater treatment can be carried out at extremely low cost.

低濃度の有機物を含む廃水の場合は固定化酵母処理のみ
で排水基準を下回る水質とすることができるが、高(震
度の有機物を含む廃水の場合は、固定化酵母処理と活性
汚泥法等の生物処理あるいは活性炭吸着等の物理化学的
処理と併用することにより、それぞれ単独で処理する場
合に比べて設備のだめの場所及び建設費等が大幅に低減
できる0以下の実施例は本発明をさらに例証するもので
あり、本発明は、これらの実施例11rc限定されない
ことを理解されたい。
In the case of wastewater containing low concentrations of organic matter, it is possible to bring the water quality below the wastewater standard with only immobilized yeast treatment, but in the case of wastewater containing organic matter with high (seismic intensity), immobilized yeast treatment and activated sludge method, etc. By using biological treatment or physicochemical treatment such as activated carbon adsorption in combination, the space for equipment storage and construction costs can be significantly reduced compared to the case of each treatment alone.The following examples further illustrate the present invention. It should be understood that the present invention is not limited to these Example 11rc.

実施例/ 第2表に記載の酵母をそれぞれ700m1のYM培地に
/白金耳接種1〜、坂ロフラスコ中で30℃でλ日間振
とり培養した。得られた菌体f100mlの殺菌水で2
回洗浄し、10 句−X / 0 /rn14になるよ
うに殺菌水に懸濁した。
Example/Yeasts listed in Table 2 were each inoculated into 700 ml of YM medium with a platinum loop, and cultured with shaking at 30° C. for λ days in a Sakaro flask. The obtained bacterial cells were sterilized with 100ml of sterilized water.
It was washed twice and suspended in sterilized water to a ratio of 10 x/0/rn14.

一方、アルギン酸ナトリウム/7とセルロース首 栃末/1にグjmlの蒸留水を加えて加熱溶解後、室温
までに冷却したものに上記酵母懸濁液夕m13を加え、
よくかくはん後j%塩化カルシウム溶液中に滴下し、直
径約3mmの固定化酵旬を製造した。
On the other hand, 1ml of distilled water was added to sodium alginate/7 and cellulose powder/1ml, heated and dissolved, and then cooled to room temperature, to which was added 13ml of the above yeast suspension,
After stirring well, the mixture was added dropwise into a j% calcium chloride solution to produce immobilized yeast beans with a diameter of about 3 mm.

固定化ゲル中の酵母密度は、J X / 07/ Vか
ら!X / 0′/f/となる。
Yeast density in immobilization gels from JX/07/V! It becomes X/0'/f/.

次に、第2表に記載の各廃水をそれぞれ700m1坂口
フラスコに入れ、各固定化酵母207を入れ、30℃で
振とうした。その結果、第、2表に示すように、固定化
酵母処理後の総有機性炭素(T OC)の除去率はよ乙
〜22%となった。
Next, each of the wastewaters listed in Table 2 was put into a 700 ml Sakaguchi flask, each immobilized yeast 207 was added thereto, and the flasks were shaken at 30°C. As a result, as shown in Table 2, the total organic carbon (TOC) removal rate after the immobilized yeast treatment was ~22%.

なお、洗米Its水上澄液の固定化酵母処理後のCOD
ば30− j、2 ppmとなり、pHさえ微調整すれ
は、その1−1放流しても可能な水質となっている。
In addition, the COD after immobilized yeast treatment of washed rice Its water supernatant
30-j, 2 ppm, and the water quality is such that it is possible to discharge 1-1 as long as the pH is finely adjusted.

実施例1 洗米廃水/θ0m1iにピヒア・ナカザワLKB−33
夕の懸濁液、ザソカロミコプ/ス・フィブリゲラIFO
0103の懸濁液及び両画の混合懸濁液をそれぞれ実施
例/と同様にして固定化したもの各201を入れ、坂ロ
フラスコ中で30℃で21]間振とうした。その結果、
第3表に示すようにそれぞれ単独の酵母を固定化したも
のよりも両者を混合]〜で固定化した方がより効果的な
廃水処理が可能となった。
Example 1 Rice washing wastewater/Pihia Nakazawa LKB-33 in θ0m1i
Evening suspension, Thesocalomicop/S. fibrigera IFO
A suspension of 0103 and a mixed suspension of both were immobilized in the same manner as in Example 201, respectively, and then shaken in a Sakalo flask at 30° C. for 21 hours. the result,
As shown in Table 3, it was possible to treat wastewater more effectively by immobilizing both yeasts by mixing them than by immobilizing each yeast individually.

実施例3 実施例/と同様にして固定化したビヒア・ナヵザワLI
KB−333、ハンセヌラ・アノマラY−/及びサツカ
ロミコプシス・フィブリゲラIFOO/θ3をそれぞれ
単独並びに3種の固定化酵母の混合物者、20?により
、洗米廃水と含酒精廃水(アルコール分約/%含有)の
混合廃水100Qlを30℃で3日間振とうした。その
結果、第を表に示すとおり3釉の固定化酵母の混合物が
、最も効果的な廃水処理が行われることが明らかとなっ
た0 実施例グ 清酒製造場廃水(TOC4LO7’j ppm ) /
 tを実施例/と同様にして固定化(〜たピヒア・ナカ
ザワLKB−33夕4−,200 ?により、3日間通
気かくはん1〜、その上澄液をMLSS4を夕θOpp
mの活性汚泥槽に移し、3日通気かくけんした。その結
果、放流水のTOCは30 ppmとなった。
Example 3 Vihear Nakazawa LI immobilized in the same manner as Example/
KB-333, Hansenula anomala Y-/ and Satucharomycopsis fibrigera IFOO/θ3, respectively, alone and as a mixture of three types of immobilized yeast, 20? Accordingly, 100Ql of mixed wastewater of rice washing wastewater and alcohol-containing refined wastewater (alcohol content: approx./%) was shaken at 30°C for 3 days. As a result, as shown in the table, it was revealed that the most effective wastewater treatment was achieved with the mixture of the three glazes of immobilized yeast.
Immobilization was carried out in the same manner as in Example (~Pichia Nakazawa LKB-33 4-, 200?).
The mixture was transferred to an activated sludge tank and aerated and agitated for 3 days. As a result, the TOC of the effluent water was 30 ppm.

実施?11夕 洗米廃水(T(JC/g00ppm)/Lを7%ンゼヌ
ラ・アノマラY−/の固定化物、l! 00 gで30
℃λ日間処理1−1その上澄液に粉末活性炭、2f′f
:投入し、1時間時々かくはんしながら放置した後にろ
過1〜、そのろ液のTOCを測定した結果j3洗米廃水
(TOC2gooppm)を塩酸でpHIAOとして7
日放置I−た上澄液(TOC3gOpwm)100ml
をハンセヌラ・アノマラY−7の固定化物20グに添加
し、坂ロフラスコ中で/日室温C20−2タ℃)で振と
う後、処理水を新ししい洗米廃水上澄液と置換する操作
を連続して2か月間行った結果、処理水のTOCばti
o〜70pPの間でほとんど変動がなかった。
implementation? 11 Washed rice wastewater (T (JC/g00ppm)/L with 7% Nzenula anomala Y-/ immobilized product, l!00 g for 30
℃λ day treatment 1-1 Powdered activated carbon, 2f'f to the supernatant liquid
:The result of measuring TOC of the filtrate after 1 hour of stirring and leaving it for 1 hour.
100ml of supernatant liquid left in the sun (TOC3gOpwm)
was added to 20 g of immobilized Hansenula anomala Y-7 and shaken in a Sakalo flask at a temperature of 20-2 degrees Celsius per day, followed by an operation in which the treated water was replaced with fresh rice washing waste water supernatant. As a result of continuous treatment for two months, the TOC of the treated water was
There was almost no variation between o and 70 pP.

特許出願人 国税庁長官 水 野 繁 一一 代理人蓼沼 鴫夕 東京都世田谷区桜丘1丁目1番 1帰来京農業大学内 0発 明 者 小玉健吉゛ 秋田県南秋田郡飯田用町飯塚25 番地小玉合名会社内Patent applicant Shigeru Mizuno, Commissioner of the National Tax Agency 11 Agent Shizuyu Tatonuma 1-1 Sakuragaoka, Setagaya-ku, Tokyo 1Kiraikyo University of Agriculture 0 shots clear by Kenkichi Kodama 25 Iizuka, Iidayo-cho, Minamiakita-gun, Akita Prefecture Address Kodama partnership company

Claims (1)

【特許請求の範囲】 (1)食品製造等廃水を固定化酵母により処理して、廃
水中に含まれる有機物を除去することを特徴とする食品
製造等廃水の処理方法 (,2)固定化酵母が、7種又は2棹以上の固定化酵母
の混合物である特許請求の範囲第1項記載の食品製造等
廃水の処理方法 (3)固定化酵母が、7種又は2種以上の酵母からなる
固定化酵母である特許請求の範囲第1項記載の食品製造
等廃水の処理方法 悴)固定化に供される酵母がデンプン、タンパク質、脂
肪、糖類、有機酸、アミノ酸、エチルアルコール、グリ
セロール、リグニン、タンニン及びペクチンから選ばれ
る7種又は2種以上の資化分解能を有する酵母である特
許請求の範囲第1項から棺3項1でのいずれかに記載の
食品製造等廃水の処理方法
[Claims] (1) A method for treating wastewater from food manufacturing, etc., characterized in that wastewater from food manufacturing, etc. is treated with immobilized yeast to remove organic matter contained in the wastewater (2) Immobilized yeast. is a mixture of seven or more types of immobilized yeast.(3) The method for treating wastewater from food manufacturing, etc., according to claim 1, wherein the immobilized yeast is a mixture of seven or more types of yeast. A method for treating wastewater from food manufacturing, etc., as set forth in claim 1, wherein the yeast is immobilized. The method for treating wastewater from food manufacturing, etc., according to any one of claims 1 to 3, wherein the yeast has the ability to assimilate and decompose seven or more types selected from tannins, tannins, and pectins.
JP12241283A 1983-07-07 1983-07-07 Treatment of waste water produced in food manufacture and the like Granted JPS6014996A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12241283A JPS6014996A (en) 1983-07-07 1983-07-07 Treatment of waste water produced in food manufacture and the like

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12241283A JPS6014996A (en) 1983-07-07 1983-07-07 Treatment of waste water produced in food manufacture and the like

Publications (2)

Publication Number Publication Date
JPS6014996A true JPS6014996A (en) 1985-01-25
JPH0137986B2 JPH0137986B2 (en) 1989-08-10

Family

ID=14835165

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12241283A Granted JPS6014996A (en) 1983-07-07 1983-07-07 Treatment of waste water produced in food manufacture and the like

Country Status (1)

Country Link
JP (1) JPS6014996A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02227192A (en) * 1988-12-23 1990-09-10 Tax Adm Agency Treatment of waste water
US5206168A (en) * 1991-02-28 1993-04-27 Gregory Boyle Method for small system wastewater denitrification
JPH06182386A (en) * 1992-07-14 1994-07-05 T D Ii:Kk Method for treating kitchen waste water
CN104891677A (en) * 2015-06-26 2015-09-09 内蒙古阜丰生物科技有限公司 Preparation technique of complex fungicide repairing amino acid fermenting wastewater

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02227192A (en) * 1988-12-23 1990-09-10 Tax Adm Agency Treatment of waste water
US5206168A (en) * 1991-02-28 1993-04-27 Gregory Boyle Method for small system wastewater denitrification
JPH06182386A (en) * 1992-07-14 1994-07-05 T D Ii:Kk Method for treating kitchen waste water
CN104891677A (en) * 2015-06-26 2015-09-09 内蒙古阜丰生物科技有限公司 Preparation technique of complex fungicide repairing amino acid fermenting wastewater

Also Published As

Publication number Publication date
JPH0137986B2 (en) 1989-08-10

Similar Documents

Publication Publication Date Title
KR20160018572A (en) Microbial-based waste water treatment compositions and methods of use thereof
JP2017209647A (en) Inclusion carrier of microorganism for water treatment, water treatment method and manufacturing method of inclusion carrier
JPS6014996A (en) Treatment of waste water produced in food manufacture and the like
US1260103A (en) Method of garbage disposal.
JP3607925B2 (en) Method for producing high spore seed sludge
JPS61118189A (en) Method for accelerating action of microbe
JPS6018565A (en) Preparation of erosion
Keluskar et al. Application of a rotating biological contactor and moving bed biofilm reactor hybrid in bioremediating surimi processing wastewater
JP2006231228A (en) Treatment method of sweet potato shochu lees waste water
JPS6136472B2 (en)
JPH07256269A (en) Apparatus for purification of pond for cultivation
JPS62106822A (en) Desulfurizing method utilizing sulfur oxidizing
JPH10277586A (en) Purifying agent using microorganism
JPS61153197A (en) Treatment of waste water
WO2005023963A1 (en) Biopreparation for recultivating soils, method for the production thereof
CN109368931A (en) The modification method of flounder flounder class breeding water
JPS596982A (en) Agent for treatment of waste water
RU2754927C1 (en) Method for immobilizing microorganisms on montmorillonite clays
KR101454895B1 (en) Media for cultivating microorganism including microporus structure and manufacturing method thereof
KR100456451B1 (en) Manufacturing method of Bio-fertilizer using useless sugars
DE10139829A1 (en) Additive to stabilize biomass
JPH01104397A (en) Purifying process of polluted water
WO2001098435A2 (en) Avalon biopreparation for removing petrol and petrol products from environmental sites and method for producing said biopreparation
RU2094459C1 (en) Method of fermentation on solid cultural medium
JPH06198291A (en) Purification of water of bathtub or swimming pool