JPH0364103B2 - - Google Patents
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- Publication number
- JPH0364103B2 JPH0364103B2 JP62283133A JP28313387A JPH0364103B2 JP H0364103 B2 JPH0364103 B2 JP H0364103B2 JP 62283133 A JP62283133 A JP 62283133A JP 28313387 A JP28313387 A JP 28313387A JP H0364103 B2 JPH0364103 B2 JP H0364103B2
- Authority
- JP
- Japan
- Prior art keywords
- chitosan
- culture solution
- solution
- culture
- added
- 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
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- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Description
産業上の利用分野
本発明は発酵工業において培養液中から微生物
菌体を効率良く分離する為、特定分子量のキトサ
ンとポリアクリル酸塩を併用する事により微生物
菌体を凝集させる方法に関するものである。
従来の技術
抗生物質、ホルモン、酸素等を利用する目的で
微生物を培養する発酵工業は数多い。これら発酵
工業における培養方法は、各種の栄養を含む培養
液中に微生物を浮遊させて行う方法が一般的であ
る。培養が終了した段階で加熱やPH調整を行つた
後、デカンターやプリコートフイルター等による
微生物菌体と培養液を分離する。
従来の技術の問題点
上記培養液中の微生物は過性が悪い為、多量
の硅藻土を過助剤やプリコート剤として使用す
るが、これら硅藻土の混入した菌体は焼却もでき
ず投棄する他はなかつた。菌体が必要な場合はデ
カンターを用いるが、微生物菌体の沈降性は悪
く、処理能力が低い上、菌体ケーキの含水率も高
かつた。
問題点を解決する方法
菌体を凝集さする事により分離効果は大幅に高
まる。
この為、培養液中の菌体を凝集させる各種の方
法が提案されている。水処理の分野において凝集
剤は公知のものであり各種の凝集剤が使用されて
いる。
中でもキチンの脱アセチル化により製造される
キトサンは天然のカチオン性高分子であり、安全
性が高い事から培養液中の菌体分離にも適用せん
とする試みがなされている。例えば特開昭50−
71878及び特開昭51−128474には微生物菌体をキ
トサンで凝集させる方法が開示されており、特公
昭53−25027には細菌培養液にキトサンとポリア
ニオンを添加した後、PH調整を行う事により共沈
させる方法が開示されている。
しかし、これらは凝集力が弱かつたり再現性に
欠ける等の恨みがあり実用に供されていない。本
発明者は凝集理論に基づき各種検討の結果、適度
の分子量を有するキトサンを培養液に添加混合
後、ポリアクリル酸塩を添加する事により、実用
に耐える凝集能力を持たせる事に成功した。本発
明に適用されるキトサンは、1規定食塩水中にお
けるキトサン濃度1%溶液の粘度が、温度25℃PH
4.0の状態で2〜200CPの範囲にある事が必要で
あり5〜100CPの範囲が特に望ましい。通常市販
されているキトサンはキチンの脱アセチル化処理
のみを行つており、同一の条件で粘度を測定する
と1000CP以上である。かかる高分子量のキチン
又はキトサンを原料として所望の分子量とするに
は、酸アルカリで加水分解する方法、酸化剤で分
解切断する方法等が公知であり、例えば、特開昭
54−148890や特開昭62−184002に記載の方法等が
適用される。これらキトサンは、塩酸、酢酸、ス
ルフアミン酸等の1塩基性酸としての水溶性を付
与し0.2〜2%濃度の水溶液として添加される。
添加量は菌体乾物に対し、1〜10重量%が望ま
しく添加量が多すぎると電荷の逆転による再分解
を招く。
市販の高分子量キトサンは同様の条件で添加す
ると系状に折出し、培養液中に均一分散しない。
これに対し、本発明におけるキトサンを添加撹
拌した場合は凝結作用により微細なフロツクを形
成する。この微細フロツクにポリアクリル酸塩溶
液を添加撹拌すると架橋吸着作用により粗大フロ
ツクを形成し、過性沈降性ともに大幅に改善さ
れる。本目的に使用されるポリアクリル酸塩は、
ナトリウム、カリウム、アンモニウム等の1価カ
チオン塩であり、PH7.0温度25℃の1規定食塩水
中におけるポリアクリル酸濃度1%溶液の粘度が
10PC以上である事が必要である。ポリアクリル
酸塩は菌体乾物あたり0.2%以上添加する。
本凝集操作を行うにあたり培養液のPHは4.5〜
8.0の範囲が望ましく、培養液のPHが菌体の等電
点以下になつたりキトサンの解離PH以上になつた
場合は凝集しない。
培養液は通常50〜80℃の加熱処理後に各種分離
操作を行うが、凝集剤添加時の培養液温度は任意
に設定できる。凝集剤の添加混合は専用の凝集槽
を用いて行う事が最も好ましいが、ポンプのサク
シヨンに注入したり、配管中の乱流により混合す
る事等も可能である。
凝集菌体はデカンター、フイタープレス、ベル
トフイルター、ベルトプレス等既知の固液分離機
により容易に母液と分離される。
パイプ等の過助剤を併用する事も本発明を逸
脱するものではない。
作 用
廃水処理においては高分子量のキトサンが凝集
剤として使われているにもかかわらず培養液中の
微生物菌体の凝集に高分子量キトサンが不適当で
ある理由は次の様に考えられる。
廃水処理における生物処理汚泥は菌体の集合物
であり懸濁物の粒径が大きい事から架橋吸着作用
の強い高分子量のキトサンが使用される。
しかし、培養液中では菌体は個々バラバラに分
散している為粒径が小さい。この為、高分子量キ
トサンの水溶液を培養液に添加すると、キトサン
水溶液表面に菌体が付着し、培養液中に分散する
事なく糸状に析出する。
これに対し、低分子量キトサン水溶液の場合
は、培養液中に均一に分散し菌体表面の電荷の中
和等に有効に利用される。この結果、菌体は集合
して微細フロツクをつくり、ポリアクリル酸塩に
よる架橋吸着が有効に働き、過性沈降性にすぐ
れた粗大フロツクをつくる。
培養液は生産性を向上させるため、通常5%以
上、少なくとも1%以上の菌体濃度で分離工程へ
送られる。この様に菌体濃度が高く、しかも微粒
子として存在している事から、全菌体表面への均
等な分配を期待すには、本願発明品の如く良好な
分散性が必要である。
試料調整
試験に供したキトサンは共和油脂製フローナツ
クN特開昭54−148890記載の方法に従い粘度調整
を行つた。各サンプルを塩酸で中和し1規定食塩
水中に農度1%PH4に溶解した粘度を表−1にし
めす。
供試キトサン
Industrial Application Field The present invention relates to a method for aggregating microbial cells by using chitosan of a specific molecular weight and polyacrylate in combination in order to efficiently separate microbial cells from a culture solution in the fermentation industry. . Prior Art There are many fermentation industries that cultivate microorganisms for the purpose of utilizing antibiotics, hormones, oxygen, etc. The culture method used in the fermentation industry is generally carried out by suspending microorganisms in a culture solution containing various nutrients. After the culture is completed, heating and pH adjustment are performed, and then the microbial cells and the culture solution are separated using a decanter, precoat filter, etc. Problems with the conventional technology Since the microorganisms in the culture solution mentioned above have poor permanence, a large amount of diatomaceous earth is used as a super-assistant or pre-coating agent, but the microorganisms contaminated with these diatomaceous earths cannot be incinerated. I had no choice but to dump it. When bacterial cells are needed, a decanter is used, but the sedimentation of microbial cells is poor, the treatment capacity is low, and the moisture content of the bacterial cake is high. How to solve the problem: By agglutinating the bacterial cells, the separation effect can be greatly increased. For this reason, various methods have been proposed for aggregating bacterial cells in a culture solution. In the field of water treatment, flocculants are well known and various types of flocculants are used. Among them, chitosan, which is produced by deacetylation of chitin, is a natural cationic polymer, and because it is highly safe, attempts have been made to apply it to the isolation of bacterial cells in culture solutions. For example, Japanese Patent Application Publication No. 1973-
71878 and JP-A-51-128474 disclose a method of flocculating microbial cells with chitosan, and JP-A-53-25027 discloses a method of aggregating microbial cells with chitosan by adding chitosan and polyanion to a bacterial culture solution and then adjusting the pH. A method of co-precipitation is disclosed. However, these methods are not put to practical use because of their weak cohesive force and lack of reproducibility. As a result of various studies based on aggregation theory, the present inventors succeeded in imparting a flocculating ability that is suitable for practical use by adding and mixing chitosan having an appropriate molecular weight to a culture solution, and then adding polyacrylate. The chitosan applied to the present invention has a viscosity of 1% chitosan solution in 1N saline at a temperature of 25°C PH.
It is necessary that it is in the range of 2 to 200 CP in the state of 4.0, and the range of 5 to 100 CP is particularly desirable. Commercially available chitosan only undergoes deacetylation treatment of chitin, and its viscosity is over 1000CP when measured under the same conditions. In order to obtain a desired molecular weight from such high-molecular-weight chitin or chitosan as a raw material, methods such as hydrolyzing it with an acid alkali and decomposing and cutting it with an oxidizing agent are known.
54-148890 and the method described in JP-A-62-184002 is applicable. These chitosan impart water solubility as a monobasic acid such as hydrochloric acid, acetic acid, or sulfamic acid, and are added as an aqueous solution with a concentration of 0.2 to 2%. The amount added is desirably 1 to 10% by weight based on the dry matter of the bacterial cells, and if the amount added is too large, re-decomposition will occur due to charge reversal. If commercially available high molecular weight chitosan is added under similar conditions, it will precipitate in a system and will not be uniformly dispersed in the culture solution. On the other hand, when chitosan in the present invention is added and stirred, fine flocs are formed due to coagulation. When a polyacrylate solution is added to the fine flocs and stirred, coarse flocs are formed due to cross-linking and adsorption, and both transient sedimentation properties are greatly improved. The polyacrylate used for this purpose is
It is a monovalent cation salt such as sodium, potassium, ammonium, etc., and the viscosity of a 1% solution of polyacrylic acid in 1N saline at a pH of 7.0 and a temperature of 25℃ is
Must be 10 PCs or more. Polyacrylate should be added in an amount of 0.2% or more based on the dry matter of the bacterial cells. When performing this agglutination operation, the pH of the culture solution is 4.5 ~
A range of 8.0 is desirable, and if the pH of the culture solution is below the isoelectric point of the bacterial cells or above the dissociation pH of chitosan, no aggregation will occur. The culture solution is usually subjected to various separation operations after heat treatment at 50 to 80°C, but the temperature of the culture solution at the time of adding the flocculant can be set arbitrarily. It is most preferable to add and mix the flocculant using a dedicated flocculation tank, but it is also possible to inject it into the suction of a pump or mix it by turbulent flow in piping. The aggregated bacterial cells are easily separated from the mother liquor using a known solid-liquid separator such as a decanter, filter press, belt filter, or belt press. It does not deviate from the present invention to use a super-aiding agent such as a pipe. Effect Although high-molecular-weight chitosan is used as a flocculant in wastewater treatment, the reason why high-molecular-weight chitosan is unsuitable for flocculating microbial cells in culture fluid is thought to be as follows. Biologically treated sludge in wastewater treatment is an aggregate of bacterial cells and the suspended particles have large particle sizes, so high-molecular-weight chitosan with strong cross-linking and adsorption properties is used. However, since the bacterial cells are individually dispersed in the culture solution, the particle size is small. Therefore, when an aqueous solution of high molecular weight chitosan is added to a culture solution, bacterial cells adhere to the surface of the aqueous chitosan solution and precipitate in the form of threads without being dispersed in the culture solution. On the other hand, in the case of a low-molecular-weight chitosan aqueous solution, it is uniformly dispersed in the culture solution and is effectively used for neutralizing charges on the surface of bacterial cells. As a result, the bacterial cells aggregate to form fine flocs, and cross-linking adsorption by polyacrylate works effectively to form coarse flocs with excellent transient sedimentation properties. In order to improve productivity, the culture solution is sent to the separation step at a bacterial cell concentration of usually 5% or more, at least 1% or more. Since the microbial cell concentration is thus high and is present in the form of fine particles, good dispersibility as in the product of the present invention is required in order to expect uniform distribution over the entire microbial cell surface. Sample Preparation The viscosity of the chitosan used in the test was adjusted according to the method described in Kyowa Yushi's Flownac N JP-A-54-148890. Table 1 shows the viscosity of each sample neutralized with hydrochloric acid and dissolved in 1% PH4 in 1N saline. Chitosan sample
【表】【table】
【表】 供試ポリアクリル酸ソーダ【table】 Sample sodium polyacrylate
【表】
実施例 1
グルコース、酸母エキス、栄養塩からなる培養
液にてカンデイダ・ユテイリスを培養したPH6.6
菌体濃度5%の液を試験に供した。
本培養液200mlを容量300mlのガラスビーカーに
とり、ジヤーテスターにより回転数150rpmで凝
集剤を混合する。
キトサン添加後、2分間撹拌した後ポリアクリ
ル酸ソーダを添加し1分間撹拌する。キトサンは
0.1N酢酸溶液に濃度1%となる様溶解し、ポリ
アクリル酸ソーダは0.2%水溶液を用いる。
凝集菌体は直径7cmのブフナーロートにNo2
紙をしき、700mmHgの減圧下液過に用する時間
を測定した。結果を表−3に示す。
過試験結果[Table] Example 1 Candida utilis was cultured in a culture solution consisting of glucose, acid mother extract, and nutrient salts at pH 6.6.
A solution with a bacterial cell concentration of 5% was used for the test. Transfer 200 ml of the main culture solution to a 300 ml glass beaker, and mix the flocculant with a jar tester at a rotation speed of 150 rpm. After adding chitosan and stirring for 2 minutes, sodium polyacrylate was added and stirred for 1 minute. Chitosan is
Dissolve in 0.1N acetic acid solution to a concentration of 1%, and use a 0.2% aqueous solution of sodium polyacrylate. Aggregated bacterial bodies were placed in a Buchner funnel with a diameter of 7 cm No.2.
The time required for the paper to be filtered under reduced pressure of 700 mmHg was measured. The results are shown in Table-3. Overtest results
【表】【table】
【表】
実施例 2
グルコース、酵母エキス、栄養塩からなる培養
液にてストレプトミセス・グリセウスを培養した
PH6.8菌体濃度6%の液を試験に供した。
実施例1と同様の過試験を行つた結果を表−
2に示す。
過試験結果[Table] Example 2 Streptomyces griseus was cultured in a culture solution consisting of glucose, yeast extract, and nutrients.
A solution with a pH of 6.8 and a bacterial cell concentration of 6% was used for the test. The results of an overtest similar to Example 1 are shown in the table below.
Shown in 2. Overtest results
【表】【table】
【表】
実施例 3
グルコース、酵母エキス、栄養塩からなる培養
液にてアスペルギルス・ニガーを培養したPH6.5
菌体濃度5.5%の液を試験に供した。
実施例1と同様の過試験を行つた結果を表−
5に示す。
過試験結果[Table] Example 3 Aspergillus niger was cultured in a culture solution containing glucose, yeast extract, and nutrients at pH 6.5.
A solution with a bacterial cell concentration of 5.5% was used for the test. The results of an overtest similar to Example 1 are shown in the table below.
5. Overtest results
【表】【table】
Claims (1)
度1重量%溶液の粘度が2〜200センチポイズで
あるキトサンを培養液に添加混合後、ポリアクリ
ル酸ソーダを添加混合し、微生物菌体を凝集せし
むる事を特徴とする、発酵工業における微生物菌
体と培養母液の分離促進方法。1 Chitosan, which has a viscosity of 2 to 200 centipoise of a 1% polymer solution in 1N saline at pH 4.0, was added to the culture solution and mixed, and then sodium polyacrylate was added and mixed to aggregate the microbial cells. A method for promoting the separation of microbial cells and culture mother liquor in the fermentation industry, which is characterized by mulching.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28313387A JPH01128782A (en) | 1987-11-11 | 1987-11-11 | Separation enhancement of microorganisms |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP28313387A JPH01128782A (en) | 1987-11-11 | 1987-11-11 | Separation enhancement of microorganisms |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01128782A JPH01128782A (en) | 1989-05-22 |
| JPH0364103B2 true JPH0364103B2 (en) | 1991-10-03 |
Family
ID=17661653
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP28313387A Granted JPH01128782A (en) | 1987-11-11 | 1987-11-11 | Separation enhancement of microorganisms |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH01128782A (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS50126784A (en) * | 1974-03-27 | 1975-10-06 | ||
| JPS5535111A (en) * | 1978-08-31 | 1980-03-12 | Diesel Kiki Co Ltd | Combined governor for internal combustion engine |
-
1987
- 1987-11-11 JP JP28313387A patent/JPH01128782A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01128782A (en) | 1989-05-22 |
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