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JPS6336B2 - - Google Patents
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JPS6336B2 - - Google Patents

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Publication number
JPS6336B2
JPS6336B2 JP10219980A JP10219980A JPS6336B2 JP S6336 B2 JPS6336 B2 JP S6336B2 JP 10219980 A JP10219980 A JP 10219980A JP 10219980 A JP10219980 A JP 10219980A JP S6336 B2 JPS6336 B2 JP S6336B2
Authority
JP
Japan
Prior art keywords
cod
culture
gallic acid
penicillium chrysogenum
tannin
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
Application number
JP10219980A
Other languages
Japanese (ja)
Other versions
JPS5726591A (en
Inventor
Hajime Kawahara
Satoshi Serita
Yoko Hidaka
Masahiro Michama
Chikae Yokogawa
Hirohiko Ikeda
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.)
Showa Kako Co Ltd
Original Assignee
Showa Kako 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 Showa Kako Co Ltd filed Critical Showa Kako Co Ltd
Priority to JP10219980A priority Critical patent/JPS5726591A/en
Publication of JPS5726591A publication Critical patent/JPS5726591A/en
Publication of JPS6336B2 publication Critical patent/JPS6336B2/ja
Granted legal-status Critical Current

Links

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はタラタンニン含有培地中でペニシリウ
ム クリソゲナムを培養し(以下この工程を第1
工程と云う)、ついでその培養物を37〜60℃で温
置する(以下この工程を第2工程と云う)ことを
特徴する没食子酸の新規改良製法に関する。 ペニシリウム クリソゲナムを培養して没食子
酸を製造することは特公昭47−41550号公報に記
載されている。この方法はタラタンニン含有培地
中でペニシリウム クリソゲナムを培養してタン
ナーゼを蓄績せしめ、このタンナーゼの作用によ
りタラタンニンを没食子酸とキナ酸とに分解して
没食子酸を単離することからなる没食子酸の製造
法である。しかしこの従来法では、タラタンニン
を完全に分解するには長時間要し、また培地の高
温滅菌時にタラ粉末中の高分子物質が溶出して高
粘度を呈し、この培地にペニシリウム クリソゲ
ナムを培養した場合増殖した菌体と高分子物質と
で泥状となり、その為に菌体の分離あるいは没食
子酸の精製等の後処理に支障をきたし、この方法
は没食子酸の工業的製法として満足すべきもので
はなかつた。 そこで本発明者らは更に工業的に有利な没食子
酸の製法を確立すべく種々検討した結果、ペニシ
リウム クリソゲナムの培養条件とタンナーゼの
最適作用条件とが異なることに注目し、両条件を
合理的に組み合わせることにより簡便でしかも効
率よく没食子酸を製造できるとの知見を得、本発
明を完成した。 第1工程の目的はタラタンニン含有固体培地に
ペニシリウム クリソゲナムを培養してタンナー
ゼを蓄績せしめながらタラタンニンを分解するこ
とにあり、第2工程の目的は未分解タラタンニン
および/または後に説明する追加タラタンニンの
分解を完結せしめることにある。 第1工程はタラタンニンを担体とを混合し、こ
れに硫酸マグネシウム、リン酸塩、尿素、塩化ア
ンモニウム、硫安の如き塩類の溶液を、含水率が
40〜60%となるように散布し、滅菌した後ペニシ
リウム クリソゲナムの種こうじを加えて固体培
養することにより行なえる。タラタンニンは、タ
ラ(Caesalpina Spinosa)の粉末あるいはその
抽出物の形で用いてもよい。担体としては、ケイ
ソウ土やパーライトの如きケイ酸塩類、もみが
ら、おがくずまたはこれらの混合物がその例とし
て挙げられる。担体の使用量は、担体およびタラ
タンニンの種類等で異なるが、滅菌中あるいは培
養中に粘結や団粒化が生じない程度用いられる。
例えば、タラタンニンとしてタラ粉末を用いる場
合には、通常タラ粉末の25〜100%重量の担体が
用いられる。ペニシリウム クリソゲナムとして
は、例えば、微工研に寄託されているWH−3株
(寄託番号第499号)が好ましく用いられる。第1
工程の培養は、第1表に示すようなペニシリウム
クリソゲナムの生育最適条件下、すなわち5〜
37℃、なかんずく約30℃において、通常24時間前
後行なうのが好ましい。
The present invention involves culturing Penicillium chrysogenum in a medium containing taratannin (hereinafter referred to as the first step).
The present invention relates to a new and improved method for producing gallic acid, which is characterized in that the culture is incubated at 37 to 60° C. (hereinafter this step is referred to as the second step). The production of gallic acid by culturing Penicillium chrysogenum is described in Japanese Patent Publication No. 47-41550. This method involves culturing Penicillium chrysogenum in a medium containing taradannin to accumulate tannase, and the action of this tannase decomposes tartannin into gallic acid and quinic acid to isolate gallic acid. This is the manufacturing method. However, with this conventional method, it takes a long time to completely decompose cod tannin, and when the medium is sterilized at high temperature, the polymer substances in cod powder elute and become highly viscous, making it difficult to cultivate Penicillium chrysogenum in this medium. In this case, the multiplied bacterial cells and the polymeric substance form a slurry, which hinders post-processing such as separating the bacterial cells or purifying gallic acid, and this method is not satisfactory as an industrial method for producing gallic acid. Nakatsuta. Therefore, the present inventors conducted various studies to establish an industrially advantageous method for producing gallic acid, and as a result, they focused on the fact that the culture conditions for Penicillium chrysogenum and the optimal operating conditions for tannase are different. The present invention was completed based on the knowledge that gallic acid could be produced simply and efficiently by combining the two methods. The purpose of the first step is to cultivate Penicillium chrysogenum on a solid medium containing taradannin to accumulate tannase while degrading taradannin, and the purpose of the second step is to decompose undegraded taratannin and/or additional ingredients as will be explained later. The purpose is to complete the decomposition of tartannin. The first step is to mix Taratannin with a carrier, and add a solution of salts such as magnesium sulfate, phosphate, urea, ammonium chloride, and ammonium sulfate to this mixture until the moisture content
This can be done by spraying at a concentration of 40 to 60%, sterilizing it, and then adding Penicillium chrysogenum seed koji to solid culture. Tara tannin may be used in the form of cod (Caesalpina spinosa) powder or its extract. Examples of carriers include silicates such as diatomaceous earth and perlite, rice husks, sawdust or mixtures thereof. The amount of carrier used varies depending on the type of carrier and tartannin, but it is used to the extent that caking or agglomeration does not occur during sterilization or culturing.
For example, when cod powder is used as cod tannin, a carrier that weighs 25 to 100% of the cod powder is usually used. As Penicillium chrysogenum, for example, the WH-3 strain (deposit number 499) deposited with the Institute of Fine Technology is preferably used. 1st
The culture in the process is carried out under the optimum growth conditions for Penicillium chrysogenum as shown in Table 1, i.e.
It is preferable to carry out the reaction at 37°C, especially about 30°C, for about 24 hours.

【表】【table】

【表】 第2工程は、第1工程の培養物を37〜50℃で温
置することにより行なわれる。第2工程は、タン
ナーゼの活性が最も強く発揮され、しかも効率よ
く利用される条件下で行なうべきである。その為
に例えば、タンナーゼの至適PHおよび温度で温置
するとか、あるいは温置の前にタラタンニンを追
加補充してタンナーゼの利用率を高めるとか、が
行なわれる。なお、タンナーゼの活性は第2表お
よび第3表に示すように、37〜50℃、特に40〜45
℃で、PH5〜8、なかんずくPH6.5〜7.5において
最も強く発揮される。
[Table] The second step is carried out by incubating the culture from the first step at 37-50°C. The second step should be carried out under conditions in which the tannase activity is exhibited most strongly and is utilized efficiently. For this purpose, for example, incubation is performed at the optimum pH and temperature for tannase, or additional cod tannin is supplemented before incubation to increase the utilization rate of tannase. In addition, as shown in Tables 2 and 3, the activity of tannase is 37 to 50℃, especially 40 to 45℃.
It is most strongly exerted at pH 5 to 8, especially pH 6.5 to 7.5.

【表】【table】

【表】【table】

【表】 以上の説明から明らかなように、本発明の最も
好ましい実施の態様はタラタンニン含有固体培地
中でペニシリウム クリソゲナムWH−3株を約
30℃で24時間前後培養し、その培養物にタラタン
ニンを追加補充しPH6.5〜7.5で、40〜45℃におい
て温置することである。 かくして生成する没食子酸は、第2工程の反応
物を熱水で抽出し、更に再結晶することにより単
離できる。熱水抽出は、第2工程をカラム中で行
ない、ついでこれに熱水を通して行なうのが工業
上有利である。 次に実施例を挙げて本発明を更に詳細に説明す
る。なお、各実施例における収率はタラ粉末また
はその抽出物中のタラタンニンからの没食子酸の
収量から算出した。 実施例 1 300mlのビーカに7.8gのタラタンニンを含有す
るタラ粉末20g、パーライト5g、もみがら10g
をとり、これに尿素0.8、燐酸一カリウム0.24g、
燐酸二カリウム0.24g、硫酸マグネシウム0.04g
を含有する溶液15mlを加えてよく混和した後100
℃で30分間滅菌する。冷後2.8%水酸化ナトリウ
ム水溶液20mlを散布し、別に5日間、タラ粉末を
加えたふすまに培養して得られたペニシリウム
クリソゲナムWH−3株の種こうじ1gを加え、
よく混合して30℃で24時間培養し6g(収率77.2
%)の没食子酸を含む培養物を得る。ついでこの
培養物を45℃で24時間温置し6.7g(収率85.3%)
の没食子酸を含む反応物67gを得る。 実施例 2 実施例1と同様にして得た培養物20gに0.1N
−NaOH溶液を加えて径20mmのカラムに充填す
る。これを45℃で24時間温置して2.3g(収率
96.3%)の没食子酸を含む反応物を得る。カラム
に3倍量の熱水を通し(流速SV=1)、2.2g
(収率93%)の没食子酸を含む抽出液を得る。な
お抽出濃度は最高5.8%であつた。 実施例 3 第1工程の培養および第2工程の温置の条件を
種々変化させた場合の没食子酸の収率をみ、次の
結果を得た。
[Table] As is clear from the above description, the most preferred embodiment of the present invention is to grow Penicillium chrysogenum WH-3 strain in a solid medium containing taratannin.
The culture is cultured at 30°C for about 24 hours, and the culture is further supplemented with taratannin and incubated at 40-45°C at pH 6.5-7.5. The gallic acid thus produced can be isolated by extracting the reaction product of the second step with hot water and further recrystallizing it. For hot water extraction, it is industrially advantageous to carry out the second step in a column and then to pass hot water through this column. Next, the present invention will be explained in more detail with reference to Examples. Note that the yield in each Example was calculated from the yield of gallic acid from cod tannin in cod powder or its extract. Example 1 20 g of cod powder containing 7.8 g of cod tannin, 5 g of perlite, and 10 g of rice hulls in a 300 ml beaker
Take this, add 0.8g of urea, 0.24g of monopotassium phosphate,
Dipotassium phosphate 0.24g, magnesium sulfate 0.04g
After adding 15 ml of solution containing 100
Sterilize for 30 min at °C. After cooling, 20 ml of 2.8% sodium hydroxide aqueous solution was sprinkled on the Penicillium, which was then cultured for 5 days on bran to which cod powder was added.
Add 1 g of seeds of Chrysogenum WH-3 strain,
Mix well and culture at 30℃ for 24 hours to obtain 6g (yield 77.2
%) of gallic acid is obtained. This culture was then incubated at 45°C for 24 hours to yield 6.7g (85.3% yield).
67 g of a reaction product containing 50% gallic acid was obtained. Example 2 0.1N to 20g of culture obtained in the same manner as Example 1
- Add NaOH solution and fill into a column with a diameter of 20 mm. This was incubated at 45℃ for 24 hours and 2.3g (yield
96.3%) of gallic acid is obtained. Pass 3 times the amount of hot water through the column (flow rate SV = 1) and add 2.2g
An extract containing gallic acid (yield 93%) is obtained. The maximum extraction concentration was 5.8%. Example 3 The yield of gallic acid when the conditions of cultivation in the first step and incubation in the second step were varied were obtained, and the following results were obtained.

【表】 実施例 4 実施例1と同様にして得た没食子酸1.0gを含
有する培養物に、タラ粉末の抽出して得たタラタ
ンニンの種々量(変量0〜5.2g)を添加し、PH
6.5、45℃、40時間温置して次表の結果を得た。
[Table] Example 4 Various amounts (varying from 0 to 5.2 g) of cod tannin obtained by extraction of cod powder were added to a culture containing 1.0 g of gallic acid obtained in the same manner as in Example 1, PH
6.5, and incubated at 45°C for 40 hours to obtain the results shown in the following table.

【表】 添加区収量−対照区収量
* 増加率(%)=
[Table] Yield in additive plot - Yield in control plot * Increase rate (%) =

Claims (1)

【特許請求の範囲】 1 タラタンニン含有固体培地中でペニシリウム
クリソゲナムを培養し、ついでその培養物を37〜
50℃で温置することを特徴とする没食子酸の製
法。 2 ペニシリウム クリソゲナムがWH−3株で
ある特許請求の範囲第1項記載の製法。 3 培養温度が5〜37℃である特許請求の範囲第
1または2項記載の製法。 4 温置をPH5〜8において行なう特許請求の範
囲第1項記載の製法。 5 タラタンニンを更に加えた後温置する特許請
求の範囲第1または4項記載の製法。 6 タラタンニンとしてタラ粉末またはその抽出
物を用いる特許請求の範囲第1または5項記載の
製法。 7 タラ粉末またはその抽出物含有培地中でペニ
シリウム クリソゲナムWH−3株を約30℃で24
時間前後培養し、その培養物にタラ粉末またはそ
の抽出物を加えPH6.5〜7.5で40〜45℃で温置する
特許請求の範囲第1〜6項の内のいずれか一項記
載の製法。
[Scope of Claims] 1. Penicillium chrysogenum is cultured in a solid medium containing Taratannin, and then the culture is
A method for producing gallic acid characterized by incubation at 50℃. 2. The production method according to claim 1, wherein the Penicillium chrysogenum is WH-3 strain. 3. The production method according to claim 1 or 2, wherein the culture temperature is 5 to 37°C. 4. The manufacturing method according to claim 1, wherein the incubation is carried out at a pH of 5 to 8. 5. The manufacturing method according to claim 1 or 4, which further comprises adding cod tannin and then incubating it. 6. The production method according to claim 1 or 5, using cod powder or an extract thereof as cod tannin. 7 Penicillium chrysogenum WH-3 strain was incubated at approximately 30°C for 24 hours in a medium containing cod powder or its extract.
The production method according to any one of claims 1 to 6, which comprises culturing for about 30 minutes, adding cod powder or an extract thereof to the culture, and incubating at 40 to 45°C at pH 6.5 to 7.5. .
JP10219980A 1980-07-24 1980-07-24 Preparation of gallic acid Granted JPS5726591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10219980A JPS5726591A (en) 1980-07-24 1980-07-24 Preparation of gallic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10219980A JPS5726591A (en) 1980-07-24 1980-07-24 Preparation of gallic acid

Publications (2)

Publication Number Publication Date
JPS5726591A JPS5726591A (en) 1982-02-12
JPS6336B2 true JPS6336B2 (en) 1988-01-05

Family

ID=14320986

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10219980A Granted JPS5726591A (en) 1980-07-24 1980-07-24 Preparation of gallic acid

Country Status (1)

Country Link
JP (1) JPS5726591A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014083019A (en) * 2012-10-25 2014-05-12 Daicel Corp Method for producing gallic acid-containing composition with low iron content by using microorganism
CN107904219B (en) * 2017-12-29 2020-04-03 集美大学 A kind of preparation method of tannase solid-state fermentation medium and application thereof
CN112662568B (en) * 2020-11-06 2023-01-03 南京师范大学 Penicillium chrysogenum and application thereof in preparing tannase and degrading tannin

Also Published As

Publication number Publication date
JPS5726591A (en) 1982-02-12

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