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JPH0416160B2 - - Google Patents
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JPH0416160B2 - - Google Patents

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Publication number
JPH0416160B2
JPH0416160B2 JP3060982A JP3060982A JPH0416160B2 JP H0416160 B2 JPH0416160 B2 JP H0416160B2 JP 3060982 A JP3060982 A JP 3060982A JP 3060982 A JP3060982 A JP 3060982A JP H0416160 B2 JPH0416160 B2 JP H0416160B2
Authority
JP
Japan
Prior art keywords
solution
pineapple
sugar
glutamic acid
yield
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 - Lifetime
Application number
JP3060982A
Other languages
Japanese (ja)
Other versions
JPS58149692A (en
Inventor
Minoru Yoshimura
Tsugio Takeyama
Yasutsugu Yamada
Shigeo Ikeda
Hiroi Yoshii
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.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co Inc
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 Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP3060982A priority Critical patent/JPS58149692A/en
Publication of JPS58149692A publication Critical patent/JPS58149692A/en
Publication of JPH0416160B2 publication Critical patent/JPH0416160B2/ja
Granted legal-status Critical Current

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Description

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

この発明は発酵法によるL−グルタミン酸の製
造方法に関する。 本発明者らは、パイナツプルモラセスとケーン
モラセス又はデンプン糖化液とを1:4から1:
1迄の範囲のいずれかの割合になるようにパイナ
ツプルモラセスとケーンモラセス又はデンプン糖
化液を炭素源として併用することにより、両者を
併用したときに理論上計算される収率よりも高い
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いて更に研究の結果完
成されるに到つたものである。 即ち、この発明は、パイナツプルモラセスとケ
ーンモラセス又はデンプン糖化液とが1:4から
1:1迄の範囲のいずれかの割合になるようにパ
イナツプルモラセスとケーンモラセス又はデンプ
ン糖化液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方法である。 パイナツプルモラセスとはパイナツプルの果実
より果汁を搾つた後の加工残渣等に加水し、これ
を搾汁後、加熱・濃縮して得られたものである。 ケーンモラセスは、さとうきびの圧搾汁に消石
灰を加え、いわゆるライミングした後、濾過して
得られたシロツプを濃縮し、砂糖を除いた残液を
再び濃縮して得られたものである。 デンプン糖化液は、コーン、タピオカ、甘露、
馬鈴薯等のデンプン質原料に水を加えて乳化し、
該乳化液に (1) 塩酸、硫酸等の酸を加えて加水分解し、水酸
化ナトリウム等のアルカリで中和し、 (2) 液化アミラーゼ、次いで糖化アミラーゼを加
えて反応させる、 ことにより得られる、グルコールを主成分とする
液である。 本発明において使用されるL−グルタミン酸生
産菌は、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
ATCC 14020 ブレビバクテリウム・フラブム ATCC 14067 ブレビバクテリウム・ラクトフアーメンタム
ATCC 13869 コリネバクテリウム・アセトアシドフイルム
ATCC 13870 コリネバクテリウム・グルタミクム ATCC 13032 ミクロバクテリウム・アンモニアフイルム
ATCC 15354 パイナツプルモラセスとケーンモラセス又はデ
ンプン糖化液は予め1:4ないし1:1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、パイナツプルモラセスとケーンモ
ラセス又はデンプン糖化液が1:4ないし1:1
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)又はデンプン糖化液
(GL)とパイナツプルモラセス(PM)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 mixed pineapple molasses and cane molasses or starch saccharified liquid from 1:4 to 1:1.
By using pineapple pulmolasses and cane molasses or starch saccharified liquid together as carbon sources at a ratio within the range of 1 to 1, it is possible to obtain a yield higher than that theoretically calculated when both are used together. I learned that L-glutamic acid is produced at a certain rate. This invention was completed as a result of further research based on this knowledge. That is, this invention provides pineapple pulmolasses and cane molasses or starch saccharified liquid such that the ratio of pineapple pulmolasses and cane molasses or starch saccharified liquid is in the range of 1:4 to 1:1. This is a method for producing L-glutamic acid by a fermentation method, which is characterized by culturing L-glutamic acid-producing bacteria in combination as a carbon source. Pineapple pulmolasses is obtained by adding water to the processing residue after extracting the juice from pineapple fruit, squeezing the juice, and then heating and concentrating it. Cane molasses is obtained by adding slaked lime to the pressed juice of sugar cane, performing so-called liming, filtering the resulting syrup, concentrating the resulting syrup, and removing the sugar and concentrating the remaining liquid again. Starch saccharified liquid is corn, tapioca, honeydew,
Water is added to starchy raw materials such as potatoes to emulsify them,
It is obtained by (1) adding an acid such as hydrochloric acid or sulfuric acid to the emulsion for hydrolysis, neutralizing it with an alkali such as sodium hydroxide, and (2) adding liquefied amylase and then saccharifying amylase for reaction. , a liquid whose main component is glycol. There are many examples of L-glutamic acid producing bacteria used in the present invention, which are so-called coryneform bacteria. Some examples are shown below. Brevibacterium deivalicatum
ATCC 14020 Brevibacterium flavum ATCC 14067 Brevibacterium lactofamentum
ATCC 13869 Corynebacterium acetoacid film
ATCC 13870 Corynebacterium glutamicum ATCC 13032 Microbacterium ammonia film
ATCC 15354 Pineapple pulmolasses and cane molasses or starch saccharified liquid may be mixed in advance at a ratio of 1:4 to 1:1 and then mixed with other medium components,
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, pineapple molasses and cane molasses or starch saccharification solution are mixed at 1:4 to 1:1.
It may be additionally added to the medium so that the ratio is as follows. Example 1 Table 1 shows cane molasses (CM) or starch saccharified liquid (GL) and pinenut plum molasses (PM).
Five types of sugar solutions (A to E) were prepared by mixing in the proportions shown below.

【表】 別に表−2に示すような組成を有する溶液
(S1)と表−3に示すような組成を有する溶液
(S2)を調製した。溶液(S1)はCMとPMを併
用する時に、溶液(S2)はGLとPMを併用する
時に使用した。
[Table] Separately, a solution (S1) having the composition shown in Table 2 and a solution (S2) having the composition shown in Table 3 were prepared. Solution (S1) was used when CM and PM were used together, and solution (S2) was used when GL and PM were used together.

【表】【table】

【表】 糖液(A〜E)50mlと溶液(S1)又は溶液
(S2)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。培養中培地中のシユク
ロース濃度が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
を少量づつ添加し、シユクロース濃度を2〜4%
に保ち、36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−4と表−5に示した。 併せてCM又はGLとPMを併用した実験区2〜
5について、対糖収率がCM又はGL又はPM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又はGLとPMの混合使用による相乗効果であ
る。
[Table] 50 ml of sugar solution (A to E) and 250 ml of solution (S1) or solution (S2) were mixed to prepare 300 ml of five types of media. 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 sucrose concentration in the medium fell below 3%, the sugar solution was added to the medium little by little by adding sugar solution A to experimental area 1 and B to experiment group 2, and increasing the sucrose concentration from 2 to 3%. 4%
and cultured for 36 hours. The amount of sugar solution added was unified to 80 ml in each experimental group. During the culture, when a predetermined amount of bacteria was reached, the surfactant Tween 60 was added to the medium at a concentration of 0.6%. The fermentation results obtained are shown in Tables 4 and 5. Experimental area 2 where CM or GL and PM were used together
Regarding No. 5, the calculated yield calculated assuming that the sugar yield is the weighted average of the sugar yield in the case of CM, GL, or PM alone is also shown. The difference between the experimental value and the calculated value is
This is the synergistic effect of mixed use of CM or GL and PM.

【表】【table】

【表】 実施例 2 CM又はGLとPMを表−6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 or GL and PM in the proportions shown in Table 6.

【表】 別に表−7に示すような組成を有する溶液
(S3)と表−8に示すような組成を有する溶液
(S4)を調製した。溶液(S3)はCMとPMを併
用する時に、溶液(S4)はGLとPMを併用する
時に使用した。
[Table] Separately, a solution (S3) having the composition shown in Table 7 and a solution (S4) having the composition shown in Table 8 were prepared. Solution (S3) was used when CM and PM were used together, and solution (S4) was used when GL and PM were used together.

【表】【table】

【表】【table】

【表】 糖液(F〜J)100mlと溶液(S3)又は溶液
(S4)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と表−10に示し、併せて実験
区2〜5については、実施例1同様に計算収率と
対比した。
[Table] 100 ml of sugar solution (F to J) and 200 ml of solution (S3) or solution (S4) 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 Corynebacterium glutamicum ATCC13032, 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 at a concentration of 0.3% based on the volume of the medium. The amount of glutamic acid produced and the sugar yield obtained during 32 hours of culture are shown in Tables 9 and 10, and the calculated yields for Experimental Groups 2 to 5 were compared in the same manner as in Example 1.

【表】【table】

【表】 実施例 3 CM又はGLとPMを表−11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 or GL and PM were mixed in the proportions shown in Table 11 to prepare five types of sugar solutions (K to O).

【表】 別に表−12に示すような組成を有する溶液
(S5)と表−13に示すような組成を有する溶液
(S6)を調製した。溶液(S5)はCMとPMを併
用する時に、溶液(S6)はGLとPMを併用する
時に使用した。
[Table] Separately, a solution (S5) having the composition shown in Table 12 and a solution (S6) having the composition shown in Table 13 were prepared. Solution (S5) was used when CM and PM were used together, and solution (S6) was used when GL and PM were used together.

【表】【table】

【表】【table】

【表】 培養35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−14と表−15に示し、併せて実験
区2〜5については、実施例1、2と同様に計算
収率と対比した。
[Table] The amount of glutamic acid produced and the sugar yield obtained during 35 hours of culture are shown in Table-14 and Table-15. In addition, for Experimental Groups 2 to 5, calculations were made in the same manner as in Examples 1 and 2. The yield was compared.

【表】【table】

【表】 以上の実施例が示す如く、パイナツプルモラセ
スとケーンモラセス又はデンプン糖化液とが1:
4から1:1迄の範囲のいずれかの割合になるよ
うにパイナツプルモラセスとケーンモラセス又は
デンプン糖化液を炭素源として併用すると、両者
を併用したときに理論上計算される収率よりも高
い収率でL−グルタミン酸が生産されることが判
明した。
[Table] As shown in the above examples, pineapple molasses and cane molasses or starch saccharified liquid are mixed in 1:
When pineapple pulmolasses and cane molasses or starch saccharified liquid are used together as carbon sources at a ratio ranging from 4 to 1:1, the yield is higher than the theoretically calculated yield when both are used together. It was found that L-glutamic acid was produced in high yield.

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

第1図〜第6図は、明細書中の表−4、表−
5、表−9、表−10、表−14及び表−15に示され
る結果をそれぞれ示したものである。 図中、実線×――×はケーンモラセス(CM)又
はデンプン糖化液(GL)を100%用いた場合の対
糖収率とパイナツプルモラセス(PM)を100%
用いた場合の対糖収率を直線で結んだもの、つま
り理論値を示す。
Figures 1 to 6 are Table-4 and Table-4 in the specification.
5. The results shown in Table 9, Table 10, Table 14 and Table 15 are shown respectively. In the figure, the solid line ×――× indicates the sugar yield when using 100% of cane molasses (CM) or starch saccharification liquid (GL) and the yield of 100% of pineapple molasses (PM).
This shows the theoretical value, which is a straight line connecting the yields based on sugar when used.

Claims (1)

【特許請求の範囲】[Claims] 1 パイナツプルモラセスとケーンモラセス又は
デンプン糖化液とが、1:4から1:1迄の範囲
のいずれかの割合になるように、パイナツプルモ
ラセスとケーンモラセス又はデンプン糖化液を炭
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
タミン酸の製造方法。
1 Pineapple pulmolasses and cane molasses or starch saccharified liquid are used as carbon sources so that the ratio of pineapple pulmolasses and cane molasses or starch saccharified liquid is in the range of 1:4 to 1:1. A method for producing L-glutamic acid by a fermentation method, which comprises culturing L-glutamic acid-producing bacteria in combination.
JP3060982A 1982-03-01 1982-03-01 Preparation of l-glutamic acid by fermentation Granted JPS58149692A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3060982A JPS58149692A (en) 1982-03-01 1982-03-01 Preparation of l-glutamic acid by fermentation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3060982A JPS58149692A (en) 1982-03-01 1982-03-01 Preparation of l-glutamic acid by fermentation

Publications (2)

Publication Number Publication Date
JPS58149692A JPS58149692A (en) 1983-09-06
JPH0416160B2 true JPH0416160B2 (en) 1992-03-23

Family

ID=12308610

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3060982A Granted JPS58149692A (en) 1982-03-01 1982-03-01 Preparation of l-glutamic acid by fermentation

Country Status (1)

Country Link
JP (1) JPS58149692A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4956641B2 (en) * 2010-03-29 2012-06-20 古河電気工業株式会社 Insulated pipe for fluid transfer

Also Published As

Publication number Publication date
JPS58149692A (en) 1983-09-06

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