JPH10313854A - Culture of microbial cell - Google Patents
Culture of microbial cellInfo
- Publication number
- JPH10313854A JPH10313854A JP9124385A JP12438597A JPH10313854A JP H10313854 A JPH10313854 A JP H10313854A JP 9124385 A JP9124385 A JP 9124385A JP 12438597 A JP12438597 A JP 12438597A JP H10313854 A JPH10313854 A JP H10313854A
- Authority
- JP
- Japan
- Prior art keywords
- microbial cell
- culture
- dissolved oxygen
- culturing
- aerobic microbial
- 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.)
- Pending
Links
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- Fire-Extinguishing Compositions (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、簡易な装置により実施
しうる、効率のよい微生物菌体の培養方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an efficient method for culturing microbial cells which can be carried out with a simple apparatus.
【0002】[0002]
【従来の技術】近年、土壌汚染環境問題の解決策とし
て、トリクロロエチレンなどの有機物質等の汚染物質を
除去するための種々の試みがなされており、例えば、土
壌汚染物質を真空ポンプを用いて吸引し、活性炭処理す
る方法が提案されている。しかしながら、汚染物質を活
性炭で吸着して除去する方法では、汚染物質を吸着した
使用済みの活性炭の再処理の問題もあって、より効率的
な処理が求められていた。2. Description of the Related Art In recent years, various attempts have been made to remove contaminants such as organic substances such as trichlorethylene as a solution to the environmental problem of soil contamination. For example, suction of soil contaminants using a vacuum pump has been made. Then, a method of performing activated carbon treatment has been proposed. However, in the method of removing contaminants by adsorption with activated carbon, there has been a problem of reprocessing of the used activated carbon having adsorbed the contaminants, so that more efficient treatment has been required.
【0003】一方、汚染物質を分解する微生物を含有す
るバイオリアクターによって汚染物質を分解させ、しか
る後、液体成分と空気とを排出する方法も提案されてお
り、この方法によれば、トリクロロエチレンの如き有機
成分を効率よく抽出し、処理することができる。さらに
汚染物質を微生物による分解作用を利用して処理するた
め2次汚染の問題がない。[0003] On the other hand, a method has been proposed in which a pollutant is decomposed by a bioreactor containing microorganisms that decompose the contaminant, and thereafter, a liquid component and air are discharged. Organic components can be efficiently extracted and processed. Furthermore, since the pollutants are treated by using the decomposition action of microorganisms, there is no problem of secondary pollution.
【0004】ここに用いられる微生物菌体としては、シ
ュードモナス(Pseudomonas)菌類が知られている。シュ
ードモナス(Pseudomonas)菌類は好気性の菌体であり、
トルエンを唯一の炭素源として利用し、増殖させること
ができる。この微生物菌体をトルエンを炭素源として開
放系で培養した場合、経時的に細菌濃度が極端に減少す
ることが知られている。このように生菌数が減少するの
は、微生物菌体を捕食する原生動物が増加するためと考
えられ、上記開放系での培養においては、シュードモナ
ス(Pseudomonas)菌類を捕食する原生動物の固体数増加
が観察されている。[0004] Pseudomonas fungi are known as microbial cells used here. Pseudomonas fungi are aerobic cells,
Toluene can be utilized and grown as the sole carbon source. When this microbial cell is cultured in an open system using toluene as a carbon source, it is known that the bacterial concentration decreases extremely with time. The decrease in the number of viable bacteria is considered to be due to an increase in protozoa that prey on microbial cells. In the open culture, the number of protozoa that prey on Pseudomonas fungi is considered An increase has been observed.
【0005】これを防止する方法として、微生物菌体を
雑菌混入防止装置を組み込んだ閉鎖系の培養槽で培養す
る方法が考えられるが、この方法によれば装置が複雑に
なり、取り扱いも煩雑となるという問題があった。[0005] As a method of preventing this, a method of culturing microbial cells in a closed culture tank incorporating a device for preventing the incorporation of various bacteria can be considered. However, according to this method, the device becomes complicated and handling becomes complicated. There was a problem of becoming.
【0006】[0006]
【発明が解決しようとする課題】本発明の目的は、開放
系の培養槽の如き簡易な装置により実施しうる、目的と
する微生物菌体を効率のよく培養しうる微生物菌体の培
養方法を提供することにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for culturing microbial cells which can be efficiently cultivated by a simple apparatus such as an open culture tank. To provide.
【0007】[0007]
【課題を解決するための手段】本出願に係わる請求項1
記載の発明は、目的とする好気性微生物菌体を開放系で
培養する方法であって、該好気性微生物菌体の培養液に
供給する溶存酸素量の供給量を、該好気性微生物菌体の
培養に必要な量であり、且つ、該好気性微生物菌体を捕
食する原生動物の増殖を防止し得る量の範囲に制御する
ことを特徴とする微生物菌体の培養方法に関する。Means for Solving the Problems Claim 1 according to the present application
The described invention is a method for culturing a target aerobic microbial cell in an open system, wherein the supply amount of dissolved oxygen supplied to a culture solution of the aerobic microbial cell is controlled by the aerobic microbial cell. The present invention relates to a method for culturing microbial cells characterized by controlling the amount of the microbial cells required for culturing of the aerobic microbial cells so as to prevent the growth of protozoa that feed on the aerobic microbial cells.
【0008】本出願はより具体的には、好気性微生物菌
体がシュードモナス(Pseudomonas)菌類の一種であり、
前記溶存酸素量の供給量を1リットルあたり0.005
〜0.5mgの範囲に制御することを特徴とする微生物
菌体の培養方法に関する。[0008] More specifically, the present application relates to a method wherein the aerobic microbial cells are a kind of Pseudomonas fungi,
The supply amount of the dissolved oxygen amount is 0.005 per liter.
The present invention relates to a method for culturing microbial cells, wherein the method is controlled to a range of 0.5 mg.
【0009】本発明おける微生物菌体の培養方法は、シ
ュードモナス(Pseudomonas)菌類の如き好気性微生物菌
体の培養に開放系の培養槽を用い、その培養液中に供給
する溶存酸素量の量を、前記好気性微生物菌体の必要量
であり、且つ、これを捕食する原生動物の増殖を防止し
得る範囲に制御しており、この制御は常法により簡易に
行い得るため、原生動物の増殖に伴う生菌数の減少がな
く、効率のよい連続的な培養を行うことができる。In the method for culturing microbial cells of the present invention, an open system culture tank is used for culturing aerobic microbial cells such as Pseudomonas, and the amount of dissolved oxygen supplied to the culture solution is determined. The required amount of the aerobic microbial cells is controlled to a range that can prevent the growth of protozoa that prey on the aerobic microbial cells. This control can be easily performed by a conventional method. Therefore, efficient continuous culture can be carried out without a decrease in the number of viable bacteria.
【0010】[0010]
【実施例】以下、本発明を具体例を挙げて更に詳しく説
明するが、本発明はこれに制限されるものではない。 (実施例1)本発明の微生物菌体の培養方法について詳
細に説明する。The present invention will be described below in more detail with reference to specific examples, but the present invention is not limited thereto. (Example 1) The method for culturing microbial cells of the present invention will be described in detail.
【0011】ここで培養に用いるのはシュードモナスエ
スピー(Pseudomonas sp.)である。このシュードモナス
エスピーは、例えば、特公昭63−7752号や特公平
5−88106号に記載のシュードモナス属に属する菌
体であってもよい。培養液としてイオン交換水1000
mlに下記に示す培地組織を加えて滅菌したものにさら
にトルエンを追加し、培養液の溶存酸素量を測定するた
めの溶存酸素電極を備えた開放系の培養槽内で、20℃
にて8日間培養を行った。The culture used here is Pseudomonas sp. The Pseudomonas sp. May be, for example, a cell belonging to the genus Pseudomonas described in JP-B-63-7752 and JP-B-5-88106. Ion-exchanged water 1000 as a culture solution
Toluene was added to the following medium tissue and sterilized by adding the following.Toluene was further added to the culture medium at 20 ° C. in an open system culture tank equipped with a dissolved oxygen electrode for measuring the amount of dissolved oxygen in the culture solution.
For 8 days.
【0012】培地組織: 硫酸アンモニウム 2.5g 硫酸マグネシウム 0.2g リン酸1カリウム 1.4g リン酸2ナトリウム 3.6g 硫酸第一鉄 2 mg 塩化カルシウム 10 mg (イオン交換水 1000mlに対して) 培養条件: 培養温度:20℃ 培養pH:7.0〜7.2Culture medium tissue: ammonium sulfate 2.5 g magnesium sulfate 0.2 g monopotassium phosphate 1.4 g disodium phosphate 3.6 g ferrous sulfate 2 mg calcium chloride 10 mg (based on 1000 ml of ion-exchanged water) : Culture temperature: 20 ° C Culture pH: 7.0 to 7.2
【0013】この溶存酸素電極で測定された培養液の溶
存酸素量のデータは酸素供給装置に送られ、培養液の溶
存酸素量を制御するものである。培養液の溶存酸素量を
0.005〜3.0mg/lとなるように条件を変え
て、このとき培養したシュードモナスエスピーの菌類の
菌数、細菌濃度と、溶存酸素量との関連を示すグラフを
図1に示す。The data on the amount of dissolved oxygen in the culture solution measured by the dissolved oxygen electrode is sent to an oxygen supply device to control the amount of dissolved oxygen in the culture solution. A graph showing the relationship between the number of bacteria and the bacterial concentration of the fungi of Pseudomonas sp. Cultured at this time while changing the dissolved oxygen amount of the culture solution to be 0.005 to 3.0 mg / l and the dissolved oxygen amount. Is shown in FIG.
【0014】図1にも明らかなように溶存酸素量を0.
005〜0.5mg/lの範囲に制御すればシュードモ
ナスエスピーを捕食する原生動物の発生、増殖を抑制
し、細菌濃度を高濃度に維持することができる。また、
溶存酸素量が0.5mg/lを超え、特に1.0mg/
l以上になると、原生動物の固体数が増加し、細菌濃度
が低下する傾向が見られた。なお、このグラフにおける
細菌濃度は660nmの波長の光における光学密度(吸
光度)で表し、数値が高いほど細菌濃度が高いことを表
す。原生動物の固体数は1ml当たりの個数を示す。As is clear from FIG.
When the concentration is controlled in the range of 005 to 0.5 mg / l, the generation and growth of protozoa that prey on Pseudomonas sp. Can be suppressed, and the bacterial concentration can be maintained at a high concentration. Also,
The dissolved oxygen content exceeds 0.5 mg / l, especially 1.0 mg / l
At l or more, the number of protozoa was increased and the bacterial concentration tended to decrease. The bacterial concentration in this graph is represented by the optical density (absorbance) of light having a wavelength of 660 nm, and the higher the numerical value, the higher the bacterial concentration. The number of protozoa solids indicates the number per 1 ml.
【0015】このようにして培養されたシュードモナス
エスピーは、バイオリアクターに固定化して、トリクロ
ロエチレン等の有害物質の分解に用いることができる。The Pseudomonas sp. Cultured in this manner can be immobilized in a bioreactor and used for decomposing harmful substances such as trichlorethylene.
【0016】バイオリアクターに用いられる固定化材料
は微生物によって好適なものを選択しうるが、例えば、
ピートモス、ポリウレタン樹脂の如き有機多孔質体等を
用いることができる。汚染物質を抽出した気液との接触
面積を向上させるため、固定化材料はフィルター等の多
孔性構造を有することが好ましい。固定化材料に固定化
された微生物によるバイオリアクターは、1段として用
いてもよいが、処理効率上、バイオリアクターは多段を
形成することが好ましい。[0016] The immobilized material used in the bioreactor can be selected appropriately depending on the microorganism.
Organic porous materials such as peat moss and polyurethane resin can be used. The immobilization material preferably has a porous structure such as a filter in order to improve the contact area with the gas-liquid from which the contaminants have been extracted. The bioreactor using the microorganism immobilized on the immobilization material may be used as one stage, but it is preferable that the bioreactor be formed in multiple stages from the viewpoint of processing efficiency.
【0017】この培養方法を適用しうるトリクロロエチ
レン等の有機塩化物の分解に有用な微生物菌体として
は、例えば、シュードモナス(Pseudomonas)菌の一種、
シュードモナス・プチダ(Pseudomonas putida )、シュ
ードモナス・セパシア(Pseudomonas cepacia ) 等が挙
げられる。培養に好適な培養液中の溶存酸素量は菌体の
種類に応じて適宜選択することが必要であるが、有害物
質の分解に有用なシュードモナス(Pseudomonas)菌類に
ついては先に述べたように0.005〜0.5mg/l
程度が好ましく用いられる。Microorganisms useful for the decomposition of organic chlorides such as trichloroethylene to which this culturing method can be applied include, for example, a kind of Pseudomonas,
Pseudomonas putida, Pseudomonas cepacia and the like. It is necessary to appropriately select the amount of dissolved oxygen in the culture solution suitable for cultivation according to the type of cells, but Pseudomonas fungi useful for decomposing harmful substances is 0 as described above. 0.005 to 0.5 mg / l
The degree is preferably used.
【0018】かくして培養されたシュードモナス(Pseu
domonas)菌類によって、トリクロエチレンを分解除去す
れば、活性炭等従来の物理的吸着による除去のごとく、
吸着体自体の処理が問題になることがなく処理に伴う2
次汚染の問題もない。The Pseudomonas thus cultured (Pseu
domonas) If fungi are used to decompose and remove trichlorethylene, as with conventional physical adsorption such as activated carbon,
The treatment of the adsorbent itself does not become a problem, and
There is no problem of secondary pollution.
【0019】[0019]
【発明の効果】本発明の微生物菌体の培養方法によれ
ば、複雑な装置を用いることなく、開放系の培養槽を用
いて、目的とする好気性微生物菌体の培養を効率よく行
うことができる優れた効果を示す。According to the method for culturing microbial cells of the present invention, the desired aerobic microbial cells can be efficiently cultured using an open culture tank without using a complicated apparatus. It shows excellent effects that can be achieved.
【図1】シュードモナス菌類を培養した場合の溶存酸素
量と、これを捕食する原生動物の固体数、シュードモナ
ス菌類の細菌濃度との関連を示すグラフである。FIG. 1 is a graph showing the relationship between the amount of dissolved oxygen when a Pseudomonas fungus is cultured, the number of protozoa that prey on the dissolved oxygen, and the bacterial concentration of the Pseudomonas fungus.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C12R 1:38) (72)発明者 北川 正恭 三重県四日市市桜町3690−1 財団法人国 際環境技術移転研究センター内──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FIC12R 1:38) (72) Inventor Masayasu Kitagawa 3690-1 Sakuracho, Yokkaichi-shi, Mie Pref. International Environmental Technology Transfer Research Center
Claims (2)
培養する方法であって、 該好気性微生物菌体の培養液に供給する溶存酸素量を、
該好気性微生物菌体の培養に必要な量であり、且つ、該
好気性微生物菌体を捕食する原生動物の増殖を防止し得
る量の範囲に制御することを特徴とする微生物菌体の培
養方法。1. A method for culturing a target aerobic microbial cell in an open system, wherein the amount of dissolved oxygen supplied to a culture solution of the aerobic microbial cell is:
Culturing of microbial cells which is an amount necessary for culturing the aerobic microbial cells and which is controlled in a range capable of preventing the growth of protozoa that prey on the aerobic microbial cells. Method.
(Pseudomonas)菌類の一種であり、前記培養液に供給す
る溶存酸素量を0.005〜0.5mg/lの範囲に制
御することを特徴とする請求項1に記載の微生物菌体の
培養方法。2. The aerobic microbial cell is a kind of Pseudomonas fungus, and the amount of dissolved oxygen supplied to the culture solution is controlled in the range of 0.005 to 0.5 mg / l. The method for culturing a microbial cell according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9124385A JPH10313854A (en) | 1997-05-14 | 1997-05-14 | Culture of microbial cell |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9124385A JPH10313854A (en) | 1997-05-14 | 1997-05-14 | Culture of microbial cell |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10313854A true JPH10313854A (en) | 1998-12-02 |
Family
ID=14884108
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9124385A Pending JPH10313854A (en) | 1997-05-14 | 1997-05-14 | Culture of microbial cell |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10313854A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6200111B1 (en) * | 2017-03-17 | 2017-09-20 | 有限会社 ホテイ産業研究所 | Toilet sanitizer |
-
1997
- 1997-05-14 JP JP9124385A patent/JPH10313854A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6200111B1 (en) * | 2017-03-17 | 2017-09-20 | 有限会社 ホテイ産業研究所 | Toilet sanitizer |
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