JP2558185B2 - Solid-liquid separation method for microbial culture - Google Patents

Solid-liquid separation method for microbial culture

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Publication number
JP2558185B2
JP2558185B2 JP3112094A JP11209491A JP2558185B2 JP 2558185 B2 JP2558185 B2 JP 2558185B2 JP 3112094 A JP3112094 A JP 3112094A JP 11209491 A JP11209491 A JP 11209491A JP 2558185 B2 JP2558185 B2 JP 2558185B2
Authority
JP
Japan
Prior art keywords
solid
liquid separation
bentonite
polymer flocculant
microbial culture
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 - Fee Related
Application number
JP3112094A
Other languages
Japanese (ja)
Other versions
JPH04322704A (en
Inventor
礼造 福嶋
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.)
HAIMO KK
Original Assignee
HAIMO KK
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Filing date
Publication date
Application filed by HAIMO KK filed Critical HAIMO KK
Priority to JP3112094A priority Critical patent/JP2558185B2/en
Publication of JPH04322704A publication Critical patent/JPH04322704A/en
Application granted granted Critical
Publication of JP2558185B2 publication Critical patent/JP2558185B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は微生物培養液の固液分離
法に関するものであり、醗酵工業等に適用される。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a solid-liquid separation method for a microbial culture solution, and is applied to the fermentation industry and the like.

【0002】[0002]

【従来の技術】微生物の大きさは1〜10μ mと極めて
小さい為に、培養液中から効率良く分離する為には各種
の前処理法が提案されている。例えば特公昭53−25
027号公報及び特開昭51−128474号公報には
高分子凝集剤を添加する技術が開示され、特開昭49−
86584号公報には鉄塩・アルミニウム塩・カルシウ
ム塩等の金属塩を添加する技術が開示されている。また
特開昭49−133584号公報には無機塩と高分子凝
集剤の併用技術が開示されている。なお硅藻土やパーラ
イトの如き多孔質の非膨潤性固体を濾過助剤として添加
する技術は広く知られている。
2. Description of the Related Art Since the size of microorganisms is extremely small, 1 to 10 .mu.m, various pretreatment methods have been proposed for efficient separation from a culture solution. For example, Japanese Patent Publication 53-25
JP-A-49-128474 and JP-A-51-128474 disclose a technique of adding a polymer flocculant.
Japanese Patent No. 86584 discloses a technique of adding a metal salt such as an iron salt, an aluminum salt, or a calcium salt. Further, JP-A-49-133584 discloses a combined use technique of an inorganic salt and a polymer flocculant. The technique of adding a porous non-swelling solid such as diatomaceous earth or perlite as a filter aid is widely known.

【0003】[0003]

【従来の技術の問題点】硅藻土等の濾過助剤を用いる方
法は、濾過助剤の添加量が多量である為に薬品費と固形
物廃棄の点で問題が多い。高分子凝集剤や無機塩等の凝
集剤を用いる方法は凝集条件の設定が微妙である上、脱
水ケーキの含水率も高くベトベトした状態であり、乾燥
して飼料とするにも焼却処分をするにも適当な形状では
ない。本発明は微生物培養液の固液分離を行うにあた
り、安定した凝集状態と処分し易い脱水ケーキを安価に
得る事を課題とする。
[Problems of the prior art] The method using a filter aid such as diatomaceous earth has many problems in terms of chemical cost and solid waste because the amount of the filter aid added is large. In the method of using a flocculant such as a polymer flocculant or an inorganic salt, the setting of flocculation conditions is delicate, and the water content of the dehydrated cake is high and sticky. Also, it is not a proper shape. An object of the present invention is to obtain a dehydrated cake that is stable and easy to dispose of at a low cost when performing solid-liquid separation of a microorganism culture liquid.

【0004】[0004]

【問題を解決する為の手段】本発明は上記課題を達成す
る為に次の様に構成される。本発明は微生物培養液にベ
ントナイトを添加した後に高分子凝集剤を添加して凝集
させ脱水操作を行う事を特徴とする。また本発明は高分
子凝集剤添加時の微生物培養液のpHが2.0〜4.0
である事を特徴とする。また本発明はベントナイトの添
加量が微生物培養液中の懸濁固型物当たり5〜100重
量%である事を特徴とする。
[Means for Solving the Problems] The present invention is configured as follows to achieve the above object. The present invention is characterized in that after adding bentonite to a microbial culture solution, a polymer flocculant is added to cause flocculation and a dehydration operation is performed. Further, in the present invention, the pH of the microorganism culture solution at the time of adding the polymer flocculant is 2.0 to 4.0.
It is characterized by Further, the present invention is characterized in that the amount of bentonite added is 5 to 100% by weight based on the solid suspension in the microorganism culture solution.

【0005】[0005]

【作用】微生物菌体は蛋白質で構成されている為に等電
点以上のpHにおいては負に帯電し、等電点以下のpH
においては正に帯電する。ベントナイトは負に帯電して
いる為にpHの低い状態では微生物と電気的に結合す
る。またベントナイトはpHの低い状態ではイオン交換
作用により膨潤性を失う。この様にして凝結した懸濁物
は高分子凝集剤により容易に凝集し脱水性の良好なフロ
ックを形成する。ベントナイトは無毒であり飼料とする
事も問題無い。硅藻土等の濾過助剤と比較して少ない添
加量で有効であり、薬品費は安価である。
Since the microbial cells are composed of proteins, they are negatively charged at a pH above the isoelectric point and have a pH below the isoelectric point.
At, it is positively charged. Since bentonite is negatively charged, it is electrically coupled to microorganisms in a low pH state. Bentonite loses its swelling property due to an ion exchange action in a low pH state. The suspension thus coagulated easily aggregates with the polymer flocculant to form flocs with good dehydratability. Bentonite is non-toxic and can be used as feed. Compared with filter aids such as diatomaceous earth, it is effective with a small addition amount, and the chemical cost is low.

【0006】[0006]

【実施例】本発明の対象となる微生物培養液は酵母・カ
ビ・細菌等の培養によりアルコール・核酸・アミノ酸・
酵素・抗生物質等を生産する工程で発生する。 該培養
液の固液分離にはベルトプレスやフィルタープレス等の
加圧濾過機、ベルトフィルターやオリバーフィルターの
様な真空濾過機、あるいはデカンターの様な遠心分離機
等の公知の脱水機を使用する事ができる。
[Examples] A microbial culture solution which is the subject of the present invention is prepared by culturing yeast, mold, bacteria, etc.
It is generated in the process of producing enzymes and antibiotics. For solid-liquid separation of the culture broth, a pressure filter such as a belt press or a filter press, a vacuum filter such as a belt filter or an Oliver filter, or a known dehydrator such as a centrifuge such as a decanter is used. I can do things.

【0007】本発明に用いるベントナイトは膨潤性の高
い微細粒子が好ましいが市販のベントナイトは支障なく
使用できる。 添加形体は5〜10%のスラリーとして
使用するのが最も便利ではあるが、粉末を直接投入する
事も可能であり任意の添加方法を選ぶ事ができる。
The bentonite used in the present invention is preferably fine particles having a high swelling property, but commercially available bentonite can be used without any trouble. It is most convenient to use the added form as a slurry of 5 to 10%, but it is also possible to directly add the powder, and any adding method can be selected.

【0008】本発明に用いる高分子凝集剤は水処理用薬
品として市販されている公知の物質を用いる事ができ、
アニオン性高分子としてはアクリルアミド・アクリル酸
塩共重合物、アクリルアミド・アクリルアミド2メチル
プロパンスルホン酸塩、ポリアクリル酸塩等を例示し、
カチオン系高分子凝集剤としてはジアルキルアミノアル
キル(メタ)アクリレートの塩または四級化物あるいは
ジアルキルアミノアルキル(メタ)アクリルアミドの塩
または四級化物等のカチオンモノマーの(共)重合物、
ポリジメチルジアリルアンモニウムクロライド、キトサ
ン、ポリアクリルアミドのマンニッヒ変性物、ポリビニ
ルアミン等を例示する事ができる。
As the polymer flocculant used in the present invention, known substances commercially available as water treatment chemicals can be used.
Examples of the anionic polymer include acrylamide / acrylate copolymer, acrylamide / acrylamide 2-methylpropanesulfonate, polyacrylate, and the like.
As the cationic polymer flocculant, a (co) polymer of a cationic monomer such as a salt or quaternary salt of dialkylaminoalkyl (meth) acrylate or a salt or quaternary salt of dialkylaminoalkyl (meth) acrylamide,
Examples thereof include polydimethyldiallylammonium chloride, chitosan, Mannich modified products of polyacrylamide, and polyvinylamine.

【0009】アニオン系高分子凝集剤とカチオン系高分
子凝集剤を併用すると凝集力が増し、フロック強度が強
まる。 添加量は対懸濁固型物当たり0.1〜2.0重
量%程度であり、凝集状態により適宜選定する。
When the anionic polymer flocculant and the cationic polymer flocculant are used in combination, the cohesive force increases and the floc strength increases. The addition amount is about 0.1 to 2.0% by weight based on the solid suspension, and is appropriately selected depending on the aggregation state.

【0010】高分子凝集剤を添加する前に鉄、アルミニ
ウム、カルシウム、マグネシウム等の多価金属塩を添加
する事により、pH4以上の状態でも凝集処理を行う事
は可能であるが、脱水性の低下や金属による汚染等が問
題になる場合もあり、ベントナイトの非膨潤化手段とし
ては酸によるpH調整が最も好ましい。 pHの調整時
期はベントナイト添加の前後を問わない。 以下に具体
的に実施例を示す。
By adding a polyvalent metal salt of iron, aluminum, calcium, magnesium or the like before adding the polymer flocculant, it is possible to perform the flocculation treatment even at a pH of 4 or more, but the dehydration In some cases, deterioration or contamination with metals may be a problem, and pH adjustment with an acid is most preferable as a non-swelling means for bentonite. The pH may be adjusted before or after the addition of bentonite. Specific examples will be shown below.

【0011】実施例−1 グルコース、酵母エキス、栄養塩からなる培養液を用い
て、カンディダ・ユティリスを培養し、pH6.6で菌
体を含む懸濁固形物濃度が5.2%の培養液を得た。
本培養液200mlを容量300mlのガラスビーカー
に取り、pHを硫酸又は苛性ソーダにより調整した後ベ
ントナイトを加え、150rpmの撹拌強度で1分間撹
拌を行い、次いで高分子凝集剤を逐次加え、150rp
mにて20秒間撹拌を行う。この時形成されたフロック
の直径を測定する。 この様にして凝集させた菌体培養
液を直径7cmのブフナー漏斗にNo.2の濾紙をしい
て、700mmHgの減圧下に100mlの濾液を得る
までの時間を測定する。本実験で用いたベントナイト
は、国峯礦化工業(株)製のクニゲルV1であり、5%
分散液に調整した。 高分子凝集剤は、(株)協立有機
工業研究所製のアニオン系高分子凝集剤ハイモロックS
S−120及びカチオン系高分子凝集剤ハイモロックM
P−173Hであり、それぞれ、0.1%に溶解して使
用した。 ハイモロックSS−120はポリアクリルア
ミド部分加水分解物(アニオン化率40モル% 極限粘
度 25 dl/g )であり、ハイモロックMP−173H
はポリメタクリロイロキシエチルトリメチルアンモニウ
ムクロライド(極限粘度5.4 dl/g )である。 得ら
れた実験結果を表−1に示す。この頁以下余白
Example 1 Candida utilis was cultivated using a culture solution containing glucose, yeast extract, and nutrient salts, and a suspension containing suspended cells and having a solids concentration of 5.2% at pH 6.6. Got
200 ml of the main culture solution was placed in a glass beaker having a volume of 300 ml, pH was adjusted with sulfuric acid or caustic soda, bentonite was added, and the mixture was stirred at a stirring intensity of 150 rpm for 1 minute. Then, a polymer flocculant was sequentially added to 150 rp.
Stir for 20 seconds at m. The diameter of the flock formed at this time is measured. The bacterial cell culture liquid thus aggregated was placed in a Buchner funnel having a diameter of 7 cm. The filter paper of No. 2 is filtered, and the time required to obtain 100 ml of filtrate under a reduced pressure of 700 mmHg is measured. The bentonite used in this experiment was Kunigel V1 manufactured by Kunimine Sekika Kogyo Co., Ltd.
The dispersion was adjusted. The polymer coagulant is an anionic polymer coagulant Hymolok S manufactured by Kyoritsu Organic Industry Research Institute Co., Ltd.
S-120 and cationic polymer flocculant Hymolok M
P-173H, each of which was dissolved in 0.1% before use. Hymolok SS-120 is a polyacrylamide partial hydrolyzate (anionization rate 40 mol%, intrinsic viscosity 25 dl / g), and Hymolok MP-173H
Is polymethacryloyloxyethyltrimethylammonium chloride (intrinsic viscosity 5.4 dl / g). The experimental results obtained are shown in Table 1. Margins below this page

【0012】[0012]

【表−1】 凝集剤添加量 MP−173H 300ppm SS−120 50ppm 注)凝集剤を添加しない場合はベントナイト添加の有無
にかかわらず濾過不能であった。
[Table-1] Amount of flocculant added MP-173H 300ppm SS-120 50ppm Note) When no coagulant was added, filtration was impossible regardless of whether bentonite was added.

【0013】実施例−2 麦焼酎製造工程より排出される蒸留残さ(懸濁固形物濃
度3.9%)を試料として 実施例−1と同一の凝集濾
過実験を行った。 用いた高分子凝集剤は、(株)協立
有機工業研究所製のカチオン系高分子凝集剤ハイモロッ
クMP−173H(前述)とアニオン系高分子凝集剤ハ
イモロックSS−190(ポリアクリル酸ソ−ダ 極限
粘度 15 dl/g )である。 溶解濃度は、それぞれ
0.2%に調整し使用した。 得られた実験結果を表−
2に示す。
Example 2 The same coagulation filtration experiment as in Example 1 was carried out using the distillation residue (suspended solids concentration 3.9%) discharged from the barley shochu manufacturing process as a sample. The polymer flocculants used were the cationic polymer flocculant Hymolok MP-173H (described above) and the anionic polymer flocculant Hymolok SS-190 (polyacrylic acid soda) manufactured by Kyoritsu Organic Industry Research Institute Co., Ltd. It has an intrinsic viscosity of 15 dl / g). The dissolved concentration was adjusted to 0.2% and used. Table of the obtained experimental results
It is shown in FIG.

【0014】[0014]

【表−2】 凝集剤添加量 MP−173H 150ppm SS−190H 50ppm [Table-2] Flocculant addition amount MP-173H 150ppm SS-190H 50ppm

【0015】[0015]

【発明の効果】表−1および表−2から明かな様にベン
トナイト添加量の増加によりフロックの直径は増大し濾
過時間は減少する。 pH2.0〜4.0の範囲で特に
凝集効果が著しい。 この凝集効果により簡易な装置に
より微生物培養液の固液分離を行う事が出来る。
As is clear from Tables 1 and 2, the floc diameter increases and the filtration time decreases as the amount of bentonite added increases. The aggregation effect is particularly remarkable in the range of pH 2.0 to 4.0. Due to this aggregation effect, solid-liquid separation of the microorganism culture liquid can be performed with a simple device.

フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C12R 1:72) Continuation of front page (51) Int.Cl. 6 Identification code Office reference number FI technical display area C12R 1:72)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 微生物培養液にベントナイトを添加した
後に高分子凝集剤を添加して凝集させ、脱水操作を行う
事を特徴とする微生物培養液の固液分離法。
1. A solid-liquid separation method for a microorganism culture liquid, which comprises adding bentonite to a microorganism culture liquid, then adding a polymer flocculant to cause aggregation, and performing a dehydration operation.
【請求項2】 高分子凝集剤添加時の微生物培養液のp
Hが2.0〜4.0である事を特徴とする請求項1に記
載する微生物培養液の固液分離法。
2. The p of the microbial culture solution when the polymer flocculant is added.
H is 2.0-4.0, The solid-liquid separation method of the microorganism culture solution of Claim 1 characterized by the above-mentioned.
【請求項3】 ベントナイトの添加量が微生物培養液中
の懸濁固型物当たり5〜100重量%である事を特徴と
する請求項1に記載する微生物培養液の固液分離法。
3. The method for solid-liquid separation of a microbial culture solution according to claim 1, wherein the amount of bentonite added is 5 to 100% by weight based on the solid suspension in the microbial culture solution.
JP3112094A 1991-04-18 1991-04-18 Solid-liquid separation method for microbial culture Expired - Fee Related JP2558185B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3112094A JP2558185B2 (en) 1991-04-18 1991-04-18 Solid-liquid separation method for microbial culture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3112094A JP2558185B2 (en) 1991-04-18 1991-04-18 Solid-liquid separation method for microbial culture

Publications (2)

Publication Number Publication Date
JPH04322704A JPH04322704A (en) 1992-11-12
JP2558185B2 true JP2558185B2 (en) 1996-11-27

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JP3112094A Expired - Fee Related JP2558185B2 (en) 1991-04-18 1991-04-18 Solid-liquid separation method for microbial culture

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Country Link
JP (1) JP2558185B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4587856B2 (en) * 2005-03-29 2010-11-24 株式会社興人 Method for cultivating vegetables with reduced nitrate nitrogen content
JP5359971B2 (en) * 2010-04-01 2013-12-04 トヨタ自動車株式会社 Aggregation and separation method of algae

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