JPH0355114B2 - - Google Patents
Info
- Publication number
- JPH0355114B2 JPH0355114B2 JP1035981A JP1035981A JPH0355114B2 JP H0355114 B2 JPH0355114 B2 JP H0355114B2 JP 1035981 A JP1035981 A JP 1035981A JP 1035981 A JP1035981 A JP 1035981A JP H0355114 B2 JPH0355114 B2 JP H0355114B2
- Authority
- JP
- Japan
- Prior art keywords
- rice
- sugar
- culture
- glutamic acid
- medium
- 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
Links
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 claims description 20
- 241000209094 Oryza Species 0.000 claims description 19
- 235000007164 Oryza sativa Nutrition 0.000 claims description 19
- 235000009566 rice Nutrition 0.000 claims description 19
- 239000007788 liquid Substances 0.000 claims description 15
- 229960002989 glutamic acid Drugs 0.000 claims description 11
- 235000013379 molasses Nutrition 0.000 claims description 10
- 241000894006 Bacteria Species 0.000 claims description 7
- 238000000855 fermentation Methods 0.000 claims description 5
- 230000004151 fermentation Effects 0.000 claims description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 4
- 238000012258 culturing Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 claims description 3
- 239000002609 medium Substances 0.000 description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 5
- 239000001963 growth medium Substances 0.000 description 5
- 238000002156 mixing Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 229920001214 Polysorbate 60 Polymers 0.000 description 3
- 238000005273 aeration Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000012533 medium component Substances 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- 241000186146 Brevibacterium Species 0.000 description 2
- 241001485655 Corynebacterium glutamicum ATCC 13032 Species 0.000 description 2
- 241000807905 Corynebacterium glutamicum ATCC 14067 Species 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 235000013922 glutamic acid Nutrition 0.000 description 2
- 239000004220 glutamic acid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 241000186031 Corynebacteriaceae Species 0.000 description 1
- 241000186216 Corynebacterium Species 0.000 description 1
- 241000186226 Corynebacterium glutamicum Species 0.000 description 1
- 241001467578 Microbacterium Species 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
この発明は発酵法によるL−グルタミン酸の製
造法に関する。
本発明者らは、米糖化液とケーンモラセスとを
25:75から75:25迄の範囲のいずれかの割合にな
るように米糖化液とケーンモラセスを炭素源とし
て併用することにより、米糖化液又はケーンモラ
セスを単独で用いる場合より、高い収率でL−グ
ルタミン酸が生産されることを知つた。
この発明はこの知見に基づいて更に研究の結果
完成されるに至つたものである。
即ち、この発明は、米糖化液とケーンモラセス
とが、25:75から75:25迄の範囲のいずれかの割
合になるように米糖化液とケーンモラセスを炭素
源として併用してL−グルタミン酸生産菌を培養
することを特徴とする発酵法によるL−グルタミ
ン酸の製造法である。
米糖化液は、精米、砕米等を望ましくは50メツ
シユより細かく、より望ましくは100メツシユよ
り細かくなるように粉砕し、これを水にけん濁し
て、常法により酵素糖化すればよい。糖化後糖化
液を一旦濾過して使用してもよいが、濾過せずに
使用することもできる。
本発明において使用されるL−グルタミン酸生
菌は、いわゆるコリネフオームバクテリアに多く
の例がある。以下にその一部を例示する。
ブレビバクテリウム・デイバリカタム
ATCC14020
ブレビバクテリウム・フラブム ATCC14067
ブレビバクテリウム・ラクトフアーメンタム
ATCC13869
コリネバクテリウム・アセトアシドフイルム
ATCC13870
コリネバクテリウム・グルタミクム ATCC13032
ミクロバクテリウム・アンモニアフイルム
ATCC15354
米糖化液とケーンモラセスは予め25:75ないし
75:25の割合で混合してのち他の培地成分と混合
してもよいが、別々に他の培地成分と混合しても
よい。
本発明において用いられる培地は、上記特定の
炭素源を含有する以外は、L−グルタミン酸発酵
においてよく使用されている培地成分を含有する
通常の培地を用いることができる。
L−グルタミン酸生産菌の培養方法においても
従来の方法と格別異る方法を採用する必要はな
い。培養の間、米糖化液とケーンモラセスが25:
75ないし75:25の割合になるように培地に追補添
加してもよい。
実施例 1
ケーンモラセス(CM)と米糖化液を表−1に
示すような割合で混合し糖液5種(A〜E)を調
製した。
This invention relates to a method for producing L-glutamic acid by fermentation. The present inventors have discovered that rice saccharification liquid and cane molasses are
By using rice saccharifier and cane molasses together as carbon sources at a ratio between 25:75 and 75:25, higher yields can be achieved than when using rice saccharifier or cane molasses alone. I learned that L-glutamic acid is produced in This invention was completed as a result of further research based on this knowledge. That is, in the present invention, L-glutamic acid is produced by using rice saccharified liquor and cane molasses together as a carbon source so that the ratio of the rice saccharified liquor and cane molasses is in the range of 25:75 to 75:25. This is a method for producing L-glutamic acid by a fermentation method characterized by culturing production bacteria. The rice saccharification solution can be obtained by pulverizing polished or broken rice, preferably to a finer grain of less than 50 mesh, more preferably finer than 100 mesh, suspending it in water, and subjecting it to enzymatic saccharification by a conventional method. The saccharified liquid after saccharification may be used after being filtered, but it may also be used without filtration. There are many examples of L-glutamic acid viable bacteria used in the present invention, which are so-called coryneform bacteria. Some examples are shown below. Brevibacterium deivalicatum
ATCC14020 Brevibacterium flavum ATCC14067 Brevibacterium lactofamentum
ATCC13869 Corynebacterium acetoacid film
ATCC13870 Corynebacterium glutamicum ATCC13032 Microbacterium ammonia film
ATCC15354 Rice saccharification liquid and cane molasses are prepared in advance at 25:75 or
It may be mixed at a ratio of 75:25 and then mixed with other medium components, or it may be mixed separately with other medium components. The medium used in the present invention may be a normal medium containing medium components commonly used in L-glutamic acid fermentation, except for containing the above-mentioned specific carbon source. There is no need to adopt a method that is particularly different from conventional methods for culturing L-glutamic acid producing bacteria. During cultivation, rice saccharification liquid and cane molasses were mixed with 25:
It may be supplemented to the medium at a ratio of 75 to 75:25. Example 1 Cane molasses (CM) and rice saccharification liquid were mixed in the proportions shown in Table 1 to prepare five types of sugar liquid (A to E).
【表】
別に表−2に示すような組成を有する溶液
(S1)を調製した。[Table] A solution (S1) having the composition shown in Table 2 was separately prepared.
【表】
糖液50mlと溶液(S1)250mlを混ぜ、300mlの
培地5種を調製した。
実験区1〜5迄の初発培地(全容300ml)を1
容発酵槽に夫々張込み、115℃にて10分間加熱
殺菌した。これに予め培養したブレビバクテリウ
ム・ラクトフエルメンタムATCC13869を接種し、
31.5℃にてPHをアンモニアガスにて7.8に保ちつ
つ、通気撹拌下培養した。培養中培地中のグルコ
ース濃度が3%を切つた時点から実験区1には糖
液Aを、2にはBをといつた具合に培地に糖液を
少量ずつ添加し、グルコース濃度を2〜4%に保
ち、34時間培養した。添加した糖液量は、各実験
区共80mlに統一した。又培養途中所定の菌量に達
した時点で界面活性剤トウイーン60を培地に対し
0.6%になるよう添加した。得られた発酵成績を
表−3に示した。
併せてCMと米糖化液を併用した実験区2〜4
について、対糖収率が実験区1および5のCM又
は米糖化液単独の場合の対糖収率の加重平均にな
るとして求めた計算収率を併記した。実験値と計
算値との差が、CMと米液化液の混合使用による
相乗効果である。[Table] Five 300 ml media were prepared by mixing 50 ml of sugar solution and 250 ml of solution (S1). Initial culture medium (total volume 300ml) for experimental plots 1 to 5 was added to 1
The mixture was poured into a fermenter and sterilized by heating at 115°C for 10 minutes. This was inoculated with Brevibacterium lactofermentum ATCC13869, which had been cultured in advance.
Culture was carried out at 31.5°C with aeration and stirring while maintaining the pH at 7.8 with ammonia gas. During culture, from the point when the glucose concentration in the medium fell below 3%, sugar solution was added to the culture medium little by little, such as sugar solution A was added to experimental section 1 and sugar solution B was added to experimental section 2, and the glucose concentration was increased from 2 to 3%. It was maintained at 4% and cultured for 34 hours. The amount of sugar solution added was unified to 80 ml in each experimental group. In addition, when the predetermined amount of bacteria is reached during the culture, the surfactant Tween 60 is added to the medium.
It was added to make it 0.6%. The fermentation results obtained are shown in Table 3. Experimental areas 2 to 4 where CM and rice saccharification liquid were used together.
The calculated yield is also shown assuming that the sugar yield is the weighted average of the sugar yield in the case of CM or rice saccharified liquid alone in Experimental Groups 1 and 5. The difference between the experimental value and the calculated value is the synergistic effect of the mixed use of CM and rice liquefied liquid.
【表】
実施例 2
CMと米糖化液を表−4に示すような割合で混
合し糖液5種(F〜J)を調製した。[Table] Example 2 Five types of sugar solutions (F to J) were prepared by mixing CM and rice saccharification solution in the proportions shown in Table 4.
【表】
別に表−5に示すような組成を有する溶液
(S2)を調製した。[Table] A solution (S2) having the composition shown in Table 5 was separately prepared.
【表】【table】
【表】
糖液(F〜J)100mlと溶液(S2)200mlを混
ぜ、300mlの培地5種を調製した。
実験区1〜5迄の培地(全容300ml)を1容
発酵槽に夫々張込み、120℃にて、10分間加熱殺
菌した。殺菌後の培地に予め培養したコリネバク
テリウム・グルタミクムATCC13032を接種しPH
をアンモニアガスにて7.8に保ちつつ、通気撹拌
下培養した。
培養途中、所定の菌量に達した時点で界面活性
剤トウイーン60を培地液量に対して0.3%になる
ように添加した。
培養30時間で得られたグルタミン酸の生成量と
対糖収率とを表−6に示し、併せて実験区2〜4
については、実施例1と同様に計算収率と対比し
た。[Table] 100 ml of sugar solutions (F to J) and 200 ml of solution (S2) were mixed to prepare five 300 ml media. The culture media for experimental groups 1 to 5 (total volume: 300 ml) were poured into a 1-volume fermenter and sterilized by heating at 120° C. for 10 minutes. Corynebacterium glutamicum ATCC13032 cultured in advance was inoculated into the sterilized medium and PH
While maintaining the temperature of 7.8 with ammonia gas, the culture was carried out under aeration and stirring. During the culture, when a predetermined amount of bacteria was reached, the surfactant Tween 60 was added at a concentration of 0.3% based on the volume of the medium. Table 6 shows the amount of glutamic acid produced and the sugar yield obtained during 30 hours of culture, and also shows the results for experimental groups 2 to 4.
As in Example 1, the yield was compared with the calculated yield.
【表】
実施例 3
CMと米糖化液を表−7に示すような割合で混
合し、糖液5種(K〜O)を調製した。[Table] Example 3 CM and rice saccharified liquid were mixed in the proportions shown in Table 7 to prepare five types of sugar liquid (K to O).
【表】
別に表−8に示すような組成を有する溶液
(S3)を調製した。[Table] A solution (S3) having the composition shown in Table 8 was separately prepared.
【表】
糖液(K〜O)100mlと溶液(S3)200mlを混
ぜ、300mlの培地5種を調製した。
実験区1〜5迄の培地(全容300ml)を1容
発酵槽に夫々張込み120℃にて10分間加熱殺菌し
た。殺菌後の培地に予め培養したブレビバクテリ
ウム・フラブムATCC14067を接種しPHをアンモ
ニアガスにて7.8に保ちつつ、通気撹拌下培養し
た。
培養途中、所定の菌量に達した時点で界面活性
剤トウイーン60を培地液量に対して0.4%になる
よう添加した。
培養32時間で得られたグルタミン酸の生成量と
対糖収率とを表−9に示し、併せて実験区2〜4
については、実施例1、2と同様に計算収率と対
比した。[Table] 100 ml of sugar solution (K to O) and 200 ml of solution (S3) were mixed to prepare five 300 ml media. The culture media for experimental groups 1 to 5 (total volume: 300 ml) were poured into a 1-volume fermenter and sterilized by heating at 120° C. for 10 minutes. The sterilized medium was inoculated with Brevibacterium flavum ATCC 14067, which had been cultured in advance, and cultured under aeration and agitation while maintaining the pH at 7.8 with ammonia gas. During the culture, when a predetermined amount of bacteria was reached, the surfactant Tween 60 was added to the culture medium at a concentration of 0.4%. Table 9 shows the amount of glutamic acid produced and the sugar yield obtained during 32 hours of culture, and also shows the results for experimental groups 2 to 4.
As in Examples 1 and 2, the yield was compared with the calculated yield.
第1−3図はケンモラセス(CM)と米糖化液
との配合割合に対する対糖収率と計算収率との関
係を示す図面である。縦軸は対糖収率(%)と計
算収率(%)を、横軸はケンモラセス(CM)と
米糖化液との配合割合を示す。
×――×:計算値、●――●:本発明の対糖収
率を示す。
Figures 1-3 are diagrams showing the relationship between the sugar yield and the calculated yield with respect to the blending ratio of Kenmolasses (CM) and rice saccharification liquid. The vertical axis shows the sugar yield (%) and the calculated yield (%), and the horizontal axis shows the blending ratio of Kenmoraces (CM) and rice saccharification liquid. ×---×: Calculated value, ●---●: Indicates the sugar yield of the present invention.
Claims (1)
75:25迄の範囲のいずれかの割合になるように、
米糖化液とケーンモラセスを炭素源として併用し
て、L−グルタミン酸生産菌を培養することを特
徴とする発酵法によるL−グルタミン酸の製造
法。1. Rice saccharification liquid and cane molasses start from 25:75.
So that the ratio is in the range up to 75:25,
A method for producing L-glutamic acid by a fermentation method, which comprises culturing L-glutamic acid-producing bacteria using a combination of rice saccharification liquid and cane molasses as carbon sources.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1035981A JPS57125695A (en) | 1981-01-27 | 1981-01-27 | Preparation of l-glutamic acid by fermentation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1035981A JPS57125695A (en) | 1981-01-27 | 1981-01-27 | Preparation of l-glutamic acid by fermentation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57125695A JPS57125695A (en) | 1982-08-05 |
| JPH0355114B2 true JPH0355114B2 (en) | 1991-08-22 |
Family
ID=11747966
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1035981A Granted JPS57125695A (en) | 1981-01-27 | 1981-01-27 | Preparation of l-glutamic acid by fermentation |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57125695A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5966892A (en) * | 1982-10-05 | 1984-04-16 | Ajinomoto Co Inc | Preparation of l-glutamic acid by fermentation method |
| CN105249410B (en) * | 2015-09-09 | 2017-12-08 | 湖州品创孵化器有限公司 | A kind of technique for manufacturing monosodium glutamate using rice |
-
1981
- 1981-01-27 JP JP1035981A patent/JPS57125695A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57125695A (en) | 1982-08-05 |
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