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JPH0669367B2 - Method of culturing lactic acid bacteria - Google Patents
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JPH0669367B2 - Method of culturing lactic acid bacteria - Google Patents

Method of culturing lactic acid bacteria

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Publication number
JPH0669367B2
JPH0669367B2 JP63328009A JP32800988A JPH0669367B2 JP H0669367 B2 JPH0669367 B2 JP H0669367B2 JP 63328009 A JP63328009 A JP 63328009A JP 32800988 A JP32800988 A JP 32800988A JP H0669367 B2 JPH0669367 B2 JP H0669367B2
Authority
JP
Japan
Prior art keywords
lactic acid
culture
acid bacteria
medium
culturing
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
JP63328009A
Other languages
Japanese (ja)
Other versions
JPH02174674A (en
Inventor
克俊 丹野
孝 山本
哲郎 中村
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.)
Snow Brand Milk Products Co Ltd
Original Assignee
Snow Brand Milk Products Co Ltd
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 Snow Brand Milk Products Co Ltd filed Critical Snow Brand Milk Products Co Ltd
Priority to JP63328009A priority Critical patent/JPH0669367B2/en
Publication of JPH02174674A publication Critical patent/JPH02174674A/en
Publication of JPH0669367B2 publication Critical patent/JPH0669367B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、発酵食品、乳酸菌飲料、乳加工食品等に広く
利用される乳酸菌を高濃度で培養するための方法に関す
る。
TECHNICAL FIELD The present invention relates to a method for culturing a lactic acid bacterium, which is widely used in fermented foods, lactic acid bacterium beverages, processed milk foods, etc., at a high concentration.

従来技術 従来、乳酸菌を培養するには、微生物培養法の手法に従
つて、培養槽内で培地を調整しながら培養する方法が行
われているが、近年、菌の培養に際し生成する阻害物質
の除去の目的で濾過膜を介して菌とその阻害物質を分離
することからなる高濃度培養システムが提案されてい
る。
BACKGROUND ART Conventionally, in order to culture lactic acid bacteria, a method of culturing while adjusting the medium in a culture tank has been performed according to the method of microbial culture method. A high-concentration culture system has been proposed which consists of separating bacteria and their inhibitors through a filtration membrane for the purpose of removal.

このような培養システムとしては、微生物を培養するた
めの培養槽中に内臓させた逆洗可能なフイルターで基質
交換させて、培養により生成した代謝物の濃度を低減す
る方法(特開昭58-47485号)、培養液を筒状のフイルタ
ー内に通過させて代謝物と菌を分離し、菌体を含む培養
液を培養槽へ循環させて連続的に培養を行うための装置
(特開昭62-138184号)等が知られている。
As such a culturing system, a method of reducing the concentration of metabolites produced by culturing by substituting a substrate with a backwashable filter incorporated in a culturing tank for culturing microorganisms (JP-A-58- 47485), an apparatus for continuously culturing by passing the culture solution through a cylindrical filter to separate metabolites and bacteria, and circulating the culture solution containing the bacterial cells to a culture tank (JP-A No. 62-138184) and the like are known.

しかし、上述した公知の培養技術を乳酸菌の培養に利用
した場合、乳酸菌の阻害因子である代謝物を濾過膜(フ
イルター)を介して除去する濾過抽出法に問題があつ
て、乳酸菌の高濃度培養に限界がみられる。
However, when the above-mentioned known culturing technique is used for culturing lactic acid bacteria, there is a problem with the filtration and extraction method that removes metabolites that are inhibitors of lactic acid bacteria through a filtration membrane (filter), resulting in high concentration culture of lactic acid bacteria Is limited.

すなわち、乳酸菌の培養に当つては、培地に各種ビタミ
ンの他に乳糖を糖分として補給しながら行うが、乳酸菌
は乳糖を利用して乳酸を代謝物として生成し、この乳酸
が耐酸性の低い乳酸菌の生育上の阻害因子となる。した
がつて、乳酸菌の培養上、乳酸の濃度が上がらないよう
にする必要があるが、公知の阻害因子を濾過する培養法
では、乳酸菌数で109〜1010(cfu/ml)程度の濃度の培
養が限界であつた。
That is, in culturing lactic acid bacteria, lactose is supplemented to the medium in addition to various vitamins as sugar, but lactic acid bacteria utilize lactose to produce lactic acid as a metabolite, and this lactic acid is lactic acid bacteria with low acid resistance. It becomes an inhibitory factor on the growth of. Therefore, it is necessary to prevent the concentration of lactic acid from increasing during the culture of lactic acid bacteria. However, in the culture method for filtering known inhibitors, the concentration of lactic acid bacteria is about 10 9 to 10 10 (cfu / ml). Culture was the limit.

また、乳酸菌の濾過培養を行うのに際して用いられる従
来の濾過膜では、熱による劣化を防ぐために殺菌剤によ
る殺菌を行つていたが、無菌化することは不可能であつ
て、長時間の培養工程においては汚染を完全に防止する
ことは困難であつた。
In addition, in the conventional filtration membrane used when performing filtration culture of lactic acid bacteria, sterilization with a bactericide was performed to prevent deterioration due to heat, but it is impossible to sterilize and long-term culture is performed. It was difficult to completely prevent contamination in the process.

発明が解決しようとする課題 本発明は、濾過膜を用いた乳酸菌の培養において、培地
の糖濃度を特定範囲にコントロールして、培養液中に生
成する乳酸濃度を一定以下に抑制することにより、乳酸
菌数1011(cfu/ml)に達する高濃度で乳酸菌を培養す
るための方法を提供することを課題とする。
The present invention, in the culture of lactic acid bacteria using a filtration membrane, by controlling the sugar concentration of the medium to a specific range, by suppressing the concentration of lactic acid produced in the culture solution below a certain level, It is an object of the present invention to provide a method for culturing lactic acid bacteria at a high concentration reaching the number of lactic acid bacteria of 10 11 (cfu / ml).

以下本発明を詳しく説明する。The present invention will be described in detail below.

課題を解決するための手段 本発明では、乳酸菌の培養に際して培地中の糖(乳糖)
濃度を1〜1.5重量%に調整することが重要であつて、
この調整により培養液中に生成する乳酸の量を常時10g
/l以下になし、その結果培養により得られる乳酸菌数
を1011(cfu/ml)の高濃度にすることがで可能であ
る。
Means for Solving the Problems In the present invention, sugar (lactose) in a medium is used for culturing lactic acid bacteria.
It is important to adjust the concentration to 1 to 1.5% by weight,
With this adjustment, the amount of lactic acid produced in the culture solution is always 10 g.
It is possible to increase the concentration of lactic acid bacteria obtained by culturing to a high concentration of 10 11 (cfu / ml).

本発明における乳酸菌としては、発酵食品、乳酸菌飲
料、乳加工食品等の製造において使用される乳酸菌であ
れば、どのようなものでも格別制限を受けることなく使
用される。
As the lactic acid bacterium in the present invention, any lactic acid bacterium used in the production of fermented foods, lactic acid bacterium beverages, milk processed foods and the like can be used without particular limitation.

また、本発明は乳酸菌の培養中において、濾過膜を用い
て培地中に生成した乳酸菌の阻害物質及びその他の廃棄
物を乳酸菌培養液として分離して除去するとともに、乳
酸菌体を含む培養液を培養槽へ循環させ、一方、糖濃度
を上記範囲に調整した新しい培地を補給しながら培養を
行うことも特徴とする。
Further, the present invention, during the culture of lactic acid bacteria, while separating and removing the inhibitory substances of lactic acid bacteria and other wastes generated in the medium using a filtration membrane as a lactic acid bacterium culture solution, culturing a culture solution containing lactic acid bacterium bodies It is also characterized in that it is circulated to the tank and, on the other hand, the culture is carried out while supplementing with a new medium whose sugar concentration is adjusted to the above range.

以下に本発明による培養方法を、それに使用する装置を
例示した第1図に基いて説明する。
Hereinafter, the culture method according to the present invention will be described with reference to FIG. 1 which illustrates an apparatus used for the culture method.

第1図において、1は培養槽であつてその中に撹拌機11
を備えており、培養槽1の底部は濾過膜3の下部とパイ
プにより連通しており、また、該濾過膜3の上部は培養
槽1の上部とパイプにより連通している。また、培養槽
3の上部には新鮮な培地を補給するためのラインが通じ
ている。図中4は濾過膜を介して菌の阻害物質を除去す
るためのポンプであり、5は培養槽内の培地のレベルを
コントロールするためのレベル計を示し、6は培地供給
のためのポンプを示し、7は中和剤を培地に供給するた
めのポンプを、8は窒素ガスの供給口及び9は窒素ガス
の排出口をそれぞれ示す。10は、濾過膜を介して除去さ
れる阻害物質及びその他廃棄物の排出口を示す。
In FIG. 1, reference numeral 1 is a culture tank in which an agitator 11 is provided.
The bottom of the culture tank 1 is in communication with the lower part of the filtration membrane 3 by a pipe, and the upper part of the filtration membrane 3 is in communication with the upper part of the culture tank 1 by a pipe. In addition, a line for replenishing a fresh medium is connected to the upper part of the culture tank 3. In the figure, 4 is a pump for removing the inhibitory substance of the bacteria through the filtration membrane, 5 is a level meter for controlling the level of the medium in the culture tank, and 6 is a pump for supplying the medium. 7 shows a pump for supplying the neutralizing agent to the medium, 8 shows a supply port of nitrogen gas, and 9 shows a discharge port of nitrogen gas. Reference numeral 10 represents an outlet for the inhibitor and other wastes removed through the filtration membrane.

上記のように構成された装置を用いて乳酸菌を培養する
には、まず、糖濃度を1〜1.5重量%に調整した新しい
培地を仕込み、これに乳酸菌を接種し撹拌しながら培養
する。この間pH計をみながら適宜中和剤を添加して培地
のpHをコントロールする。培養の経過とともに培地の乳
酸が生成して乳酸菌に対する阻害が発現するので、ポン
プ2を介して培地を濾過膜3を通過させて乳酸を含む培
地をポンプ4を介して乳酸菌と分離して10より排出さ
せ、一方乳酸菌を含む培地(乳酸菌は濾過膜により流出
されない)は培養槽1へ戻される。この際、培養槽では
レベル計5により培地の流出分に相当する量の新鮮培地
がポンプ6を介して補給される。なお、培養槽1は温度
計により一定温度に保持されるようになつている。
In order to culture lactic acid bacteria using the apparatus configured as described above, first, a new medium in which the sugar concentration is adjusted to 1 to 1.5% by weight is charged, and the lactic acid bacteria are inoculated and cultured with stirring. During this period, the pH of the medium is controlled by appropriately adding a neutralizing agent while observing the pH meter. Since lactic acid in the medium is produced with the progress of the culture and inhibition against lactic acid bacteria is expressed, the medium is passed through the filtration membrane 3 via the pump 2 and the medium containing lactic acid is separated from the lactic acid bacteria via the pump 4 to obtain 10 On the other hand, the medium containing lactic acid bacteria (the lactic acid bacteria are not discharged by the filtration membrane) is returned to the culture tank 1 while being discharged. At this time, in the culture tank, the level meter 5 supplies a fresh medium in an amount corresponding to the outflow of the medium through the pump 6. The culture tank 1 is kept at a constant temperature by a thermometer.

上記培養操作において、培養開始から乳酸生成による阻
害現象が表われる経過時間以降では、培養供給速度を経
時的に増加方向へ変化させる必要がある。
In the above-mentioned culture operation, it is necessary to change the culture supply rate in the increasing direction with time after the lapse of time from the start of culture when the inhibition phenomenon due to lactic acid production appears.

この操作により、生菌数の上昇とともに栄養源、糖等の
必要量増加に対処するとともに、生成される乳酸の増加
に対しても量的抑制が行われる。
By this operation, it is possible to cope with an increase in the required amount of nutrients, sugars, etc. as well as an increase in the number of viable bacteria, and to quantitatively suppress the increase in lactic acid produced.

なお、培地供給速度を生菌数の上昇に合せて上昇させれ
ば培養効率が良く、培養時間も短縮できる。したがつ
て、乳糖濃度は1.5%以下であれば乳酸生成による増殖
速度の低下を阻止できるが、あまり低い濃度では増菌速
度が小さくなり培養時間が長くなるので、効率的培養の
ためには1〜1.5%の範囲の乳糖濃度で培養を行つて、
乳酸による阻害を抑止するとともに増菌速度にも影響の
ない状態を維持するようにする。
If the medium supply rate is increased in accordance with the increase in the viable cell count, the culture efficiency is good and the culture time can be shortened. Therefore, if the lactose concentration is 1.5% or less, the decrease in the growth rate due to lactic acid production can be prevented, but if the concentration is too low, the rate of multiplication will be small and the culture time will be long. Culture at lactose concentration in the range of ~ 1.5%,
Prevent the inhibition by lactic acid and maintain a state that does not affect the multiplication rate.

本発明で使用する装置は、2弗化ビニリデンのような有
機物質からなる濾過膜と培地の循環ラインを備えている
ことが好ましく、培養槽での培養により生成する乳酸に
よる阻害現象が表われるまでは、乳酸菌は培養槽1内の
培地のみで培養され、この間に濾過膜3と循環ラインを
加熱殺菌できるようになつている。そして、乳酸による
阻害現象が発現した以降は循環ラインを稼働して濾過膜
3で乳酸を主とする阻害物質や老廃物を除去するととも
に、ここで除去される液量分に相当する新鮮培地を培養
槽1へ補給するように作動し、一方、濾過膜3で透過し
なかつた乳酸菌含有培地は循環ラインにより培養槽へ戻
される。
The device used in the present invention is preferably equipped with a filtration membrane made of an organic substance such as vinylidene difluoride and a circulation line for the medium, until the inhibition phenomenon by lactic acid produced by the culture in the culture tank appears. The lactic acid bacteria are cultured only in the medium in the culture tank 1, and the filtration membrane 3 and the circulation line can be heat-sterilized during this period. Then, after the inhibition phenomenon due to lactic acid has appeared, the circulation line is operated to remove the inhibitory substances mainly lactic acid and waste products in the filtration membrane 3, and a fresh medium corresponding to the amount of liquid removed here is prepared. The lactic acid bacterium-containing medium, which operates so as to be supplied to the culture tank 1 while not permeating through the filtration membrane 3, is returned to the culture tank by the circulation line.

ここにおいて、培養時間の経過ととも乳酸菌の生育濃度
が上昇するため、濾過膜3における培地の排除量と、培
養槽への新鮮培地の補給分は経時的にそれぞれ増加する
ようになる。
Here, since the growth concentration of lactic acid bacteria increases with the lapse of culture time, the amount of the removed medium in the filtration membrane 3 and the amount of fresh medium supplied to the culture tank increase with time.

本発明における乳酸菌には、特に制限はなく、従来知ら
れている発酵食品、乳酸菌飲料、乳加工食品等に広く利
用される乳酸菌であればどのような乳酸菌でも使用でき
る。このような乳酸菌にはビフィドバクテリウム属、ラ
クトバチルス属あるいはストレプトコッカス属に属する
乳酸菌があり、市販されており容易に入手可能である。
The lactic acid bacterium in the present invention is not particularly limited, and any lactic acid bacterium widely used in conventionally known fermented foods, lactic acid bacterium beverages, processed milk foods and the like can be used. Such lactic acid bacteria include lactic acid bacteria belonging to the genus Bifidobacterium, the genus Lactobacillus or the genus Streptococcus, which are commercially available and easily available.

発明の効果 以上述べたとおり、本発明によると、従来の濾過培養に
みられる汚染問題が解決され、一方、乳酸による阻害現
象を抑制するとともに増菌速度にも影響を及ぼすことな
く、培養できるので、同容量の処理設備でも単位容積当
りの培養菌数を多くすることができ、(1011cfu/mlを
得ることができる)製造コスト及び設備コストの軽減に
も貢献できる。
EFFECTS OF THE INVENTION As described above, according to the present invention, the problem of contamination found in the conventional filtration culture is solved, while on the other hand, it is possible to culture without suppressing the inhibition phenomenon by lactic acid and affecting the multiplication rate. Even with the same capacity of treatment equipment, the number of cultures per unit volume can be increased, which can also contribute to reduction of manufacturing cost (capable of obtaining 10 11 cfu / ml) and equipment cost.

また、本発明では高温加熱による滅菌処理が可能な有機
物質からなる濾過膜を用いているため、循環ラインを含
めて蒸気による滅菌が可能であつて、殺菌汚染の完全防
止が可能となり、ラインの管理も簡易化される利点があ
る。
Further, in the present invention, since a filtration membrane made of an organic substance that can be sterilized by high temperature heating is used, it is possible to sterilize by steam including a circulation line, and it is possible to completely prevent sterilization and contamination. There is an advantage that management is also simplified.

以下に実施例を示して本発明を具体的に説明する。The present invention will be specifically described below with reference to examples.

実施例1 本例は乳酸菌としてブフィズス菌(ビフィドバクテリウ
ム・ロンガム SBT-2933 R)を用いて培養した場合に
ついて示す。
Example 1 This example shows the case of culturing using Buffybacterium (Bifidobacterium longum SBT-2933 R) as the lactic acid bacterium.

培養槽1に下記組成の培地とビフィズス菌を投入して培
養を開始すると、4時間目頃から乳酸による発育阻害が
出てくるので、濾過膜による阻害物質除去ラインを稼動
させた。
When the culture medium 1 and bifidobacteria were added to the culture tank 1 to start the culture, growth inhibition by lactic acid began to appear from about 4 hours, so the inhibitor removal line using the filtration membrane was operated.

培地組成: 乳糖 1.25% 酵母エキス 1.00% ポリペプトン 1.00% リン酸2カリウム(K2HPO4) 0.5% リン酸2水素カリウム(KH2PO4) 0.1% L−アスコルビン酸ナトリウム 0.1% その際、培地の乳糖濃度を常時1.25重量%になるように
新鮮培地の培養槽1への補給量と濾過膜からの流出量を
コントロールさせた。培養開始から8時間目におけるビ
フィズス菌の生育数は1011cfu/mlに達した。
Medium composition: lactose 1.25% yeast extract 1.00% polypeptone 1.00% dipotassium phosphate (K 2 HPO 4 ) 0.5% potassium dihydrogen phosphate (KH 2 PO 4 ) 0.1% sodium L-ascorbate 0.1% of the medium The supply amount of fresh medium to the culture tank 1 and the outflow amount from the filtration membrane were controlled so that the lactose concentration was always 1.25% by weight. The growth number of Bifidobacterium reached 10 11 cfu / ml 8 hours after the start of culture.

なお、第2図に増菌数の経時的状態を示す。また、この
際の培地における乳糖と乳酸の量の変化は第3図に示す
とおりであつて、乳糖は一時的に欠乏しているが、ビフ
ィズス菌の代謝産物である乳酸は10g/lを超えないこ
とが認められる。
In addition, FIG. 2 shows the time-dependent state of the number of bacteria. The changes in the amounts of lactose and lactic acid in the medium at this time are as shown in Fig. 3. Lactose is temporarily deficient, but lactic acid, which is a metabolite of Bifidobacterium, exceeds 10 g / l. It is recognized that there is no.

なお、濾過開始から培養終了までの新鮮培地の供給速度
(希釈率)は乳酸菌の増加とともに0.4hr-1から4.5hr-1
まで連続的に変化させた。培地中の乳糖濃度の消長と乳
酸生成量及び菌体収量との関係は下記表に示すとおりで
ある。
The supply rate (dilution) of fresh medium from the start of filtration to completion of the culture 4.5Hr -1 from 0.4hr -1 with increasing lactic acid bacteria
Continuously changed until. The relationship between the change in lactose concentration in the medium and the amount of lactic acid produced and the cell yield is shown in the table below.

この表のごとく乳酸の生成を抑制し、かつ菌体収率を高
い位置にするには乳糖の濃度範囲を1〜1.5に抑制する
ことが望ましいことが判る。
As shown in this table, it is desirable to suppress the concentration range of lactose to 1 to 1.5 in order to suppress the production of lactic acid and increase the cell yield.

【図面の簡単な説明】[Brief description of drawings]

第1図は、本発明で使用する装置の概略図を示したもの
である。 第1図において、 1……培養槽 3……濾過膜 4……阻害物質及び老廃物排出用ポンプ 6……新鮮培地供給用ポンプ 11……撹拌機
FIG. 1 shows a schematic view of an apparatus used in the present invention. In Fig. 1, 1 ... Culture tank 3 ... Filtration membrane 4 ... Pump for discharging inhibitor and waste products 6 ... Pump for supplying fresh medium 11 ... Stirrer

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】乳酸菌を培養するに際し、培地の糖濃度を
1〜1.5重量%に調整し、培養により培地中に生成した
菌の阻害物質を培養槽に連通して配設した濾過膜を介し
て除去し、該阻害物質を除去した培養液を培養槽へ循環
させるとともに、上記濾過膜を介して除去された部分に
相当する液量の新鮮な培地を培養槽へ補給することを特
徴とする乳酸菌の培養方法。
1. When culturing a lactic acid bacterium, the sugar concentration of the medium is adjusted to 1 to 1.5% by weight, and an inhibitor of the bacterium produced in the medium by the culturing is passed through a filtration membrane arranged in communication with the culture tank. It is characterized in that the culture broth, which has been removed by removing the inhibitor, is circulated to the culture tank, and at the same time, the culture tank is replenished with a fresh medium of a liquid amount corresponding to the portion removed through the filtration membrane. Method for culturing lactic acid bacteria.
【請求項2】乳酸菌がビフィズス菌である請求項(1)
に記載の乳酸菌の培養方法。
2. The lactic acid bacterium is a bifidobacteria (1).
The method for culturing lactic acid bacteria according to.
【請求項3】培地の糖濃度が乳糖濃度である請求項
(1)に記載の乳酸菌の培養方法。
3. The method for culturing lactic acid bacteria according to claim 1, wherein the sugar concentration of the medium is a lactose concentration.
【請求項4】濾過膜が2弗化ビニリデンから構成される
請求項(1)に記載の乳酸菌の培養方法。
4. The method for culturing lactic acid bacteria according to claim 1, wherein the filtration membrane is composed of vinylidene difluoride.
JP63328009A 1988-12-27 1988-12-27 Method of culturing lactic acid bacteria Expired - Fee Related JPH0669367B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63328009A JPH0669367B2 (en) 1988-12-27 1988-12-27 Method of culturing lactic acid bacteria

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63328009A JPH0669367B2 (en) 1988-12-27 1988-12-27 Method of culturing lactic acid bacteria

Publications (2)

Publication Number Publication Date
JPH02174674A JPH02174674A (en) 1990-07-06
JPH0669367B2 true JPH0669367B2 (en) 1994-09-07

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Country Link
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007097260A1 (en) 2006-02-24 2007-08-30 Toray Industries, Inc. Method of producing chemical product and continuous fermentation apparatus

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4512265B2 (en) * 2000-12-26 2010-07-28 株式会社ヤクルト本社 Lactic acid bacteria culture supernatant, method for producing the same, and external preparation for skin using the supernatant
JP2008125456A (en) * 2006-11-22 2008-06-05 Toray Ind Inc Continuous culture method and continuous culture apparatus
JP2009296921A (en) * 2008-06-12 2009-12-24 Toray Ind Inc Continuous culture device and method for producing chemical
JP5358197B2 (en) * 2009-01-16 2013-12-04 学校法人君が淵学園 Temperature gradient incubator

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
萩原文二等編「膜による分離法」株式会社講談社(1982.10.10)P.256〜261

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007097260A1 (en) 2006-02-24 2007-08-30 Toray Industries, Inc. Method of producing chemical product and continuous fermentation apparatus

Also Published As

Publication number Publication date
JPH02174674A (en) 1990-07-06

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