JPH08278A - Production of cellulosic substance - Google Patents

Production of cellulosic substance

Info

Publication number
JPH08278A
JPH08278A JP16485494A JP16485494A JPH08278A JP H08278 A JPH08278 A JP H08278A JP 16485494 A JP16485494 A JP 16485494A JP 16485494 A JP16485494 A JP 16485494A JP H08278 A JPH08278 A JP H08278A
Authority
JP
Japan
Prior art keywords
culture
liquid
cellulosic
cellulosic substance
culture solution
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
Application number
JP16485494A
Other languages
Japanese (ja)
Inventor
Takeshi Akao
剛 赤尾
Hikotaka Hashimoto
彦尭 橋本
Keiko Mimura
桂子 三村
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.)
Kikkoman Corp
Original Assignee
Kikkoman Corp
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 Kikkoman Corp filed Critical Kikkoman Corp
Priority to JP16485494A priority Critical patent/JPH08278A/en
Publication of JPH08278A publication Critical patent/JPH08278A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To produce a cellulosic substance in high efficiency by flow-down culture. CONSTITUTION:Cells produced by liquid culture are scattered on a sheet-formed culture member 4 made of e.g. polypropylene nonwoven fabric. The culture member 4 is suspended on a supporting member 3 in a culture vessel 1 and a culture liquid 2 is sprayed to the top of the culture member 4 with a culture liquid feeding pump 8 and allowed to flow down along the surface. The microorganisms are brought into contact with the culture liquid 2 to produce a cellulosic substance.

Description

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

【0001】[0001]

【産業上の利用分野】本願発明は、流下培養によりセル
ロース性物質を効率良く製造する方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for efficiently producing a cellulosic substance by flow-down culture.

【0002】[0002]

【従来の技術】従来、微生物よりゲル状をしたセルロー
ス性物質を製造する方法として、「ナタデココの製造方
法」(特開昭61−149055)、および「微生物に
よるセルロース性物質の製造方法」(特開平5−682
36)等を挙げることができる。まず前者は、ココナッ
ツ果汁と糖類との混合物に酢酸菌を接種し、酸性で静置
培養して得られるゼリー状固形物から酸成分を除去する
ことにより、味、舌触り、歯触りの良好なナタデココを
製造する方法である。一方後者は、セルロース性物質を
生産する微生物を液体培地に接種し静置培養しながら表
面に液体培地又は該微生物と培地を混合した液を連続的
または間欠的に添加することにより、セルロース性物質
を製造する方法である。
2. Description of the Related Art Conventionally, as a method for producing a gelled cellulosic substance from microorganisms, "Nata de coco production method" (Japanese Patent Laid-Open No. 61-149055) and "Microbe production of cellulosic material" (special Kaihei 5-682
36) and the like. First, the former is inoculated with acetic acid bacteria in a mixture of coconut juice and sugar, and by removing the acid component from the jelly-like solid product obtained by stationary culture under acidic conditions, nata de coco with good taste, texture and texture. Is a method of manufacturing. On the other hand, the latter is a method of inoculating a cellulosic substance-producing microorganism into a liquid medium and performing static culture while continuously or intermittently adding a liquid medium or a mixture of the microorganism and the medium to the cellulosic substance. Is a method of manufacturing.

【0003】[0003]

【発明が解決しようとする課題】しかし、前記従来例
は、何れも静置培養法であり効率的な方法とは言い難
い。すなわち、静置培養法においては、生成されたセル
ロースは、厚みがほぼ均一な層を形成し、その上面は液
面と同じ面まで浮上する。新しいセルロースは、酸素の
接種にもっとも有利なセルロース層の最上面で生成さ
れ、古いセルロースすなわち下面側が順次下方である液
中に押し下げられる。セルロースの生成に必要な栄養
は、培養液からセルロース層全体を通過して、セルロー
ス層の最上面へと移動する。従って、生成されたセルロ
ース層が厚くなる程栄養補給に関し、菌体への抵抗が増
大しセルロースの成長が阻害されるのである。また、同
培養法では、培養促進のため培養液を攪拌するとセルロ
ース層が形成されず、培養のコントロールができない等
の欠点があり改善が望まれていた。
However, all of the above-mentioned conventional examples are static culture methods and cannot be said to be efficient methods. That is, in the stationary culture method, the produced cellulose forms a layer having a substantially uniform thickness, and the upper surface thereof floats to the same surface as the liquid surface. Fresh cellulose is produced at the top of the cellulose layer, which is most advantageous for oxygen inoculation, and is pushed down into the old cellulose, the liquid with the bottom side down in sequence. The nutrients required for the production of cellulose pass from the culture solution through the entire cellulose layer and move to the uppermost surface of the cellulose layer. Therefore, the thicker the formed cellulose layer is, the more the resistance to the bacterial cells is increased and the growth of the cellulose is inhibited in terms of nutritional supplementation. Further, in the same culturing method, there is a defect that the cellulose layer is not formed when the culture solution is stirred to promote the culturing, and the culturing cannot be controlled.

【0004】そこで本願発明者は、培養部材を垂直また
は傾斜して配置し、そこに菌体を接種して、その培養部
材の表面に沿って培養液を流せば、酸素ならびに栄養の
補給が容易に成され、また培養液の供給量、栄養成分、
あるいは温度、さらにはシート部材の傾斜度等を適宜変
えることにより培養条件のコントロールが可能なことを
知見した。本願発明は、この知見に基ずいて完成された
ものである。
Therefore, the inventor of the present invention can easily supply oxygen and nutrients by arranging the culture member vertically or inclined, inoculating the bacterial cells into the culture member, and flowing the culture solution along the surface of the culture member. , The amount of culture solution supplied, nutritional components,
Alternatively, they have found that the culture conditions can be controlled by appropriately changing the temperature and the inclination of the sheet member. The present invention has been completed based on this finding.

【0005】すなわち、本願発明は、アセトバクター属
に属しセルロース性物質の生産能を有する微生物を着生
させた培養部材を垂直または傾斜させて配置し、培養液
を培養部材の頂部に供給してその表面に沿って流下させ
前記微生物と培養液を接触させてセルロース性物質を製
造することを特徴とするセルロース性物質の製造方法で
ある。
That is, according to the present invention, a culture member on which a microorganism belonging to the genus Acetobacter and having a cellulosic substance-producing ability is grown is arranged vertically or inclined and the culture solution is supplied to the top of the culture member. It is a method for producing a cellulosic substance, characterized by producing a cellulosic substance by allowing it to flow down along the surface and contacting the microorganism with a culture solution.

【0006】[0006]

【課題を解決するための具体的手段】まず、本願発明に
おいて使用される微生物は、アセトバクターに属しセル
ロース性でゲル状の物質を生産する微生物であればどの
ようなものでもよく、例えばAcetobacter Pasteurianu
s,Acetobacter Hanseni,及びAcetobacter xylinum 等を
挙げることができる。
First, the microorganism used in the present invention may be any microorganism as long as it belongs to Acetobacter and produces a cellulosic, gel-like substance, for example, Acetobacter Pasteurianu.
s, Acetobacter Hanseni, and Acetobacter xylinum.

【0007】また、液体栄養培地としては、グルコー
ス、シュークロース、フラクトース、マルトース、澱粉
水解物、糖蜜等の炭素源、リン酸アンモニウム、硫酸ア
ンモニウム、塩化アンモニウムなどのアンモニウム塩、
硝酸塩、尿素、ペプトンなどの有機あるいは無機の窒素
源、アミノ酸、ビタミン、脂肪酸、核酸、さらにこれら
を含有する物質などの有機微量栄養源など、およびリン
酸塩、マグネシウム塩、カルシウム塩、鉄塩、マンガン
塩などの無機塩類を適宜組み合わせた合成または半合成
培地等が挙げられる。また、ココナッツミルクなどのフ
ルーツジュース、植物抽出液、および糖液などを主原料
に天然の液体栄養培地を調整し、これを用いてもよい。
これらの培地は、有機または無機の酸を添加してpH3
〜6に調整して使用することが好ましい。
The liquid nutrient medium includes glucose, sucrose, fructose, maltose, starch hydrolysates, carbon sources such as molasses, ammonium salts such as ammonium phosphate, ammonium sulfate and ammonium chloride,
Organic or inorganic nitrogen sources such as nitrates, urea, peptone, organic trace nutrients such as amino acids, vitamins, fatty acids, nucleic acids, substances containing these, and phosphates, magnesium salts, calcium salts, iron salts, Examples thereof include synthetic or semi-synthetic medium in which inorganic salts such as manganese salt are appropriately combined. In addition, a natural liquid nutrient medium may be prepared by using a fruit juice such as coconut milk, a plant extract, a sugar solution, etc. as a main raw material.
These media are adjusted to pH 3 with the addition of organic or inorganic acids.
It is preferable to adjust to ~ 6 before use.

【0008】次に本願発明を添付図を基に具体的に説明
する。図1において、1は、箱状で密閉状に形成された
培養槽で、その底部には菌体の栄養源となる培養液2が
溜められている。培養槽1の内部上方には、図1におい
て前後方向に丸棒状をした支持部材3が等間隔で培養槽
1の天井に平行に設置されており、この支持部材3に菌
体が接種される培養部材4が懸架される。本実施例にお
いては、培養部材4としてシート状のものを示した培養
部材4は、例えば不織布、布材、濾布材、あるいはキャ
ンバス等で形成され、菌体が着生できる程度の粗面度を
有するものであれば材質は問わない。その他、金属ある
いはプラスチック等の剛性を有する部材の表面に前記部
材を張着したものでもよく、また、金属あるいはプラス
チックの表面を粗く処理したものでもよい。
Next, the present invention will be specifically described with reference to the accompanying drawings. In FIG. 1, 1 is a box-shaped, hermetically-formed culture tank in which a culture solution 2 serving as a nutrient source for bacterial cells is stored at the bottom. In the upper part of the inside of the culture tank 1, support members 3 each having a round bar shape in the front-rear direction in FIG. 1 are installed at equal intervals in parallel to the ceiling of the culture tank 1, and the support members 3 are inoculated with cells. The culture member 4 is suspended. In the present embodiment, the culture member 4 shown in the form of a sheet as the culture member 4 is formed of, for example, a non-woven fabric, a cloth material, a filter cloth material, a canvas, or the like, and has a roughness so that the bacterial cells can grow. The material does not matter as long as it has Alternatively, a member having rigidity such as metal or plastic may be attached to the surface of the member, or the surface of metal or plastic may be roughened.

【0009】5は培養液2の分配管で、前記支持部材3
と平行状に対をなして設けられ、図2のごとく支持部材
3と向かい合う面に噴霧ノズル6が設けられており、支
持部材3に懸架された培養部材4の頂部に培養液2を供
給するよう構成されている。分配管5は連結管7により
相互に連通されている。8は、培養液2を培養部材4に
供給するための培養液供給ポンプで、吸引口9は培養槽
1の底部と連結されており、培養液2を吸引できるよう
構成されている。
Reference numeral 5 denotes a distribution pipe for the culture solution 2, which is used as the support member 3
2, a spray nozzle 6 is provided on the surface facing the support member 3 as shown in FIG. 2, and the culture solution 2 is supplied to the top of the culture member 4 suspended by the support member 3. Is configured. The distribution pipes 5 are connected to each other by a connecting pipe 7. Reference numeral 8 denotes a culture solution supply pump for supplying the culture solution 2 to the culture member 4, and the suction port 9 is connected to the bottom of the culture tank 1 so as to be able to suck the culture solution 2.

【0010】一方、培養液供給ポンプ8の吐出口10
は、濾過機11、および熱交換器12を介して前記分配
管5に連通される。濾過機11は、培養液2の中から挟
雑物を除去するため、また熱交換器12は培養液2の温
度をコントロールするためにそれぞれ設置されている。
そして、培養槽1の下部一側には空気供給口13が、一
方上部他方側には空気排出口が14がそれぞれ開口され
ており、空気供給口13には、その吸引側に無菌フィル
ター15、および熱交換器16を装着された送風機17
が設けられており、菌体に温度コントロールされた酸素
を補給するよう構成されている。
On the other hand, the discharge port 10 of the culture solution supply pump 8
Is connected to the distribution pipe 5 via a filter 11 and a heat exchanger 12. The filter 11 is installed to remove contaminants from the culture medium 2, and the heat exchanger 12 is installed to control the temperature of the culture medium 2.
An air supply port 13 is opened on one side of the lower part of the culture tank 1, and an air discharge port 14 is opened on the other side of the upper part of the culture tank 1. The air supply port 13 has a sterile filter 15 on its suction side. And blower 17 equipped with heat exchanger 16
Is provided and is configured to supply temperature-controlled oxygen to the bacterial cells.

【0011】かくして、図1,2に示す装置で微生物に
よるセルロース性物質を製造するわけであるが、まず、
培養部材4に菌体を接種する。この際、培養部材4全面
に均等にセルロース性物質が生成されることが好まし
く、この点からみると、培養部材4に液体培養した菌体
を噴霧したり、液体培地に該部材4を浸すこと等が挙げ
られる。その他、菌体をカンテン培地等で培養した場
合、培養部材4に塗付する方法等がある。
Thus, the cellulosic substance is produced by the microorganisms using the apparatus shown in FIGS.
The culture member 4 is inoculated with the bacterial cells. At this time, it is preferable that the cellulosic substance is evenly generated on the entire surface of the culture member 4. From this point, it is possible to spray the liquid-cultured bacterial cells on the culture member 4 or soak the member 4 in a liquid medium. Etc. In addition, when the bacterial cells are cultivated in agar medium or the like, there is a method of applying them to the culture member 4.

【0012】菌体は、培養部材4に1×102 〜1×1
6 個/cm2 程度接種すればよい。培養液2の濃度は
糖濃度として1〜15%(V/V)で、温度は20〜3
5℃に保持する。そして、培養液2を培養部材4に供給
する割合であるが、培養部材4の単位面積当たり0.1
〜10ml/hr・cm2 が適当である。
[0012] The microbial cells are added to the culture member 4 in the range of 1 × 10 2 to 1 × 1
It is sufficient to inoculate about 0 6 cells / cm 2 . The concentration of the culture solution 2 is 1 to 15% (V / V) as the sugar concentration, and the temperature is 20 to 3
Hold at 5 ° C. The ratio of the culture solution 2 supplied to the culture member 4 is 0.1 per unit area of the culture member 4.
-10 ml / hr · cm 2 is suitable.

【0013】次に、図3に培養部材4を傾斜させて設置
した例を示す。本実施例はの場合は、図1と同様に設置
された上部支持部材18と、これの真下より図3におい
て例えば左方に設置された下部支持部材19に、平板状
をした支持板20をスベリ台状に設置する。そして、こ
の支持板20の上面に培養部材4を張着し、そこに菌体
を接種した後培養部材4の頂部より培養液を供給する。
以下図1の実施例と同様に菌体を培養し、セルロース性
物質を生成させる。本実施例では、培養部材4の培養面
は減少するが、培養液2の流下速度をより広い範囲でコ
ントロールできる利点がある。
Next, FIG. 3 shows an example in which the culture member 4 is installed while being inclined. In the case of this embodiment, an upper support member 18 installed in the same manner as in FIG. 1 and a lower support member 19 installed right below the upper support member 18 in FIG. It is installed in a sliding table. Then, the culture member 4 is adhered to the upper surface of the support plate 20, the cells are inoculated into the culture member 4, and the culture solution is supplied from the top of the culture member 4.
Thereafter, the cells are cultured in the same manner as in the example of FIG. 1 to produce a cellulosic substance. In the present embodiment, the culture surface of the culture member 4 is reduced, but there is an advantage that the flow rate of the culture solution 2 can be controlled in a wider range.

【0014】次に図4に培養部材4を筒状に形成した例
を示す。同図において、25はプラスチック、あるいは
鉄材等で筒状に形成された支柱で、上部は解放され、下
部には培養液2の通液口26が開口され、培養槽1の底
部に立設されている。培養部材4は、この支柱25の外
周および内周に設置されており、その頂部より図1と同
様に噴霧ノズル6が、各培養部材4に対応して設けられ
ている。培養部材4の内部27に供給された培養液2
は、培養部材4に沿って流下し、通液口26を通り循環
するよう構成されている。
Next, FIG. 4 shows an example in which the culture member 4 is formed in a cylindrical shape. In the figure, reference numeral 25 is a column formed of a plastic or iron material in a cylindrical shape, the upper part of which is opened, the lower part of which is provided with a passage port 26 for the culture solution 2 and which is erected at the bottom of the culture tank 1. ing. The culture members 4 are installed on the outer circumference and the inner circumference of the column 25, and from the top thereof, the spray nozzles 6 are provided corresponding to the respective culture members 4 as in FIG. The culture solution 2 supplied to the inside 27 of the culture member 4.
Are configured to flow down along the culture member 4 and circulate through the liquid passage port 26.

【0015】次に比較実験例を示し、本願発明の優位性
を数値的にしめす。 A.本願発明の方法 1.装置:図1,2に示す装置。 2.培養部材 材質:レーヨン不織布 面積:80cm2 (一側面) 設置数:1基(培養面1面) 設置形態:垂直 3.菌体:Acetobacter xylinum ATCC 10821を5×10
4 個/cm2 接種 4.培養液:ココナッツミルクの濾過液を、シュークロ
ース10%、リン酸アンモニウム0.5%、酢酸1.0
%、pH4.0に調整したもの。 5.培養条件 培養温度:30℃ 培地供給量:0.5ml/hr・cm2 (培養部材の
単位面積当たり) 酸素濃度:通常の空気中の濃度 培養期間:14日
Next, comparative examples will be shown to numerically show the superiority of the present invention. A. Method of the present invention 1. Device: The device shown in FIGS. 2. Culture material: Rayon non-woven fabric Area: 80 cm 2 (one side) Number of installations: 1 unit (one culture surface) Installation form: vertical 3. Cells: Acetobacter xylinum ATCC 10821 5 × 10
4 cells / cm 2 inoculation 4. Culture medium: Coconut milk filtrate, sucrose 10%, ammonium phosphate 0.5%, acetic acid 1.0
%, Adjusted to pH 4.0. 5. Culture conditions Culture temperature: 30 ° C. Medium supply: 0.5 ml / hr · cm 2 (per unit area of culture member) Oxygen concentration: Normal concentration in air Culture period: 14 days

【0016】B.従来法(静置培養法) 本願発明の方法と同じ培養液1100mlを直径23.
3cmのシャーレに入れ(表面積426cm2 、深さ
2.6cmとなる)スラントで3日間培養した後、pH
5.0の同培養液で1日振とうしたAcetobacter xylinu
m ATCC 10821を8.7×104 個/ml接種した。単位
表面積あたりでは2.3×105 個/cm2 となる。3
0℃で14日間静置培養後、培養液表面に厚さ1.8c
mのゲル状セルロースが生成された。これを採取し流水
洗浄を3日間行い、培地および菌体などの不純物を除去
した。この湿重量を計量し、さらに105℃で恒量にな
るまで乾燥させ、乾燥量を計量した。
B. Conventional method (stationary culture method) 1100 ml of the same culture solution as the method of the present invention was used to prepare a solution of 23.
Put in a 3 cm Petri dish (surface area 426 cm 2 , depth 2.6 cm) and incubate with slant for 3 days, then pH
Acetobacter xylinu shaken in the same culture solution of 5.0 for 1 day
m ATCC 10821 was inoculated at 8.7 × 10 4 cells / ml. The unit surface area is 2.3 × 10 5 pieces / cm 2 . Three
After static culture at 0 ° C. for 14 days, the culture solution has a thickness of 1.8 c on the surface.
m of gel-like cellulose was produced. This was collected and washed with running water for 3 days to remove impurities such as medium and cells. The wet weight was weighed, further dried at 105 ° C. until a constant weight was obtained, and the dried amount was weighed.

【0017】 表1より本願発明の方が従来法よりwet状における収
量も多く、またdry状における比率も高いものが生成
される。
[0017] As shown in Table 1, the present invention produces a higher yield in the wet form and a higher ratio in the dry form than the conventional method.

【0018】次に実施例を示し、本願発明をより具体的
に説明する。 実施例1 まず、培養部材に液体培養されたAcetobacter xylinum
ATCC 10821を2×105 個/cm2 散布する。そして、
図1に示す培養槽において1600cm2 (培養面積1
500cm2 )でポリプレン不織布で形成されたシート
状の培養部材10枚を支持部材に懸架する。次にココナ
ッツミルクを主成分とする培養液を培養液供給ポンプで
培養部材に7.5l/hrを培養部材の頂部より散布す
る。このとき培養液は、熱交換器により28℃に保持す
る。一方、送風機により28℃にコントロールされた空
気を供給する。以上の状態で16日間培養し、培養部材
の表面に平均して25mmのセルロース性物質が生成さ
れた。
Next, the present invention will be described more specifically with reference to examples. Example 1 First, Acetobacter xylinum liquid-cultured on a culture member
Spray 2 × 10 5 pieces of ATCC 10821 / cm 2 . And
In the culture tank shown in FIG. 1, 1600 cm 2 (culture area 1
Ten sheet-shaped culture members made of polypropylene non-woven fabric are suspended at 500 cm 2 ) on a support member. Next, 7.5 l / hr of the culture solution containing coconut milk as a main component is sprayed onto the culture member from the top of the culture member by the culture solution supply pump. At this time, the culture solution is kept at 28 ° C. by a heat exchanger. On the other hand, air controlled at 28 ° C. is supplied by a blower. After culturing for 16 days in the above state, a cellulosic material of 25 mm on average was produced on the surface of the culture member.

【0019】実施例2 まず、培養部材に液体培養されたAcetobacter xylinum
ATCC 10821を7×104 個/cm2 散布する。そして、
図3に示す培養槽において1600cm2 でナイロン濾
布で形成された培養部材5枚を上下の支持部材に支持さ
れた支持板の面上に張着する。このとき培養部材は水平
面より45度の起立させた。次に、ココナッツミルクを
主成分とする培養液を培養液供給ポンプで培養部材に
3.8l/hrを培養部材の頂部より散布する。このと
き培養液は、熱交換器により30℃に保持する。一方、
送風機により30℃にコントロールされた空気を供給す
る。以上の状態で17日間培養し、培養部材の表面に平
均して厚さ19mmのセルロース性物質が生成された。
Example 2 First, Acetobacter xylinum liquid-cultured on a culture member
Spray 7 × 10 4 pieces / cm 2 of ATCC 10821. And
In the culture tank shown in FIG. 3, 5 culture members formed of nylon filter cloth at 1600 cm 2 are attached to the surfaces of the support plates supported by the upper and lower support members. At this time, the culture member was erected at 45 degrees from the horizontal plane. Next, 3.8 l / hr of the culture solution containing coconut milk as a main component was sprayed onto the culture member from the top of the culture member by the culture solution supply pump. At this time, the culture solution is kept at 30 ° C. by a heat exchanger. on the other hand,
The air controlled at 30 ° C. is supplied by a blower. After culturing for 17 days in the above state, a cellulosic material having an average thickness of 19 mm was produced on the surface of the culture member.

【0019】[0019]

【発明の効果】本願発明は以上のごとく構成されてお
り、培養液の供給量、濃度、あるいは温度等をコントロ
ールすることが可能で、菌を最適な条件で培養すること
ができ、従来に比較し収量も多く、また、生成されたゲ
ル状セルロース性物質は、セルロース分が濃厚なものが
得られる。
EFFECTS OF THE INVENTION The invention of the present application is constructed as described above, and it is possible to control the supply amount, concentration, temperature, etc. of the culture broth, and it is possible to culture the bacterium under optimum conditions. The yield is high, and the gelled cellulosic material produced is rich in cellulose content.

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

【図1】 本願発明に関する装置の正面断面図FIG. 1 is a front sectional view of an apparatus according to the present invention.

【図2】 図1の2−2視図FIG. 2 is a 2-2 view of FIG.

【図3】 他の実施例の正面断面図FIG. 3 is a front cross-sectional view of another embodiment.

【図4】 培養部材の他の実施例図FIG. 4 is a diagram of another embodiment of the culture member.

【符号の説明】[Explanation of symbols]

1 培養槽 2 培養液 4 培養部材 6 噴霧ノズル 8 培養液供給ポンプ 11 濾過機 12 熱交換器 15 無菌フィルター 1 Culture Tank 2 Culture Liquid 4 Culture Material 6 Spray Nozzle 8 Culture Liquid Supply Pump 11 Filter 12 Heat Exchanger 15 Aseptic Filter

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 アセトバクター属に属しセルロース性物
質の生産能を有する微生物を着生させた培養部材を垂直
または傾斜させて配置し、培養液を培養部材の頂部に供
給しその表面に沿って流下させ前記微生物と培養液を接
触させてセルロース性物質を製造することを特徴とする
セルロース性物質の製造方法。
1. A culture member on which a microorganism belonging to the genus Acetobacter and capable of producing a cellulosic substance is grown is arranged vertically or slanted, and a culture solution is supplied to the top of the culture member along the surface thereof. A method for producing a cellulosic substance, which comprises allowing the microorganism to flow down and bringing the culture solution into contact with the culture medium to produce a cellulosic substance.
【請求項2】 請求項1において、培養部材がシート状
をしているセルロース性物質の製造方法。
2. The method for producing a cellulosic material according to claim 1, wherein the culture member has a sheet shape.
【請求項3】 請求項1において、培養部材が筒状をし
ているセルロース性物質の製造方法。
3. The method for producing a cellulosic material according to claim 1, wherein the culture member has a tubular shape.
JP16485494A 1994-06-24 1994-06-24 Production of cellulosic substance Pending JPH08278A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16485494A JPH08278A (en) 1994-06-24 1994-06-24 Production of cellulosic substance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16485494A JPH08278A (en) 1994-06-24 1994-06-24 Production of cellulosic substance

Publications (1)

Publication Number Publication Date
JPH08278A true JPH08278A (en) 1996-01-09

Family

ID=15801183

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16485494A Pending JPH08278A (en) 1994-06-24 1994-06-24 Production of cellulosic substance

Country Status (1)

Country Link
JP (1) JPH08278A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008061532A (en) * 2006-09-05 2008-03-21 Kenji Nakamura Hydrous gel sheet, method for producing the same and applications thereof
JP2010284150A (en) * 2009-06-11 2010-12-24 Food Industry Research & Development Institute Bioreactor for producing microbial cellulose, and method for producing the same

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008061532A (en) * 2006-09-05 2008-03-21 Kenji Nakamura Hydrous gel sheet, method for producing the same and applications thereof
JP2010284150A (en) * 2009-06-11 2010-12-24 Food Industry Research & Development Institute Bioreactor for producing microbial cellulose, and method for producing the same

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