JPH03266977A - Incubation of beta-tyrosinase-containing microbe - Google Patents

Incubation of beta-tyrosinase-containing microbe

Info

Publication number
JPH03266977A
JPH03266977A JP6689890A JP6689890A JPH03266977A JP H03266977 A JPH03266977 A JP H03266977A JP 6689890 A JP6689890 A JP 6689890A JP 6689890 A JP6689890 A JP 6689890A JP H03266977 A JPH03266977 A JP H03266977A
Authority
JP
Japan
Prior art keywords
tyrosinase
medium
microbe
incubation
beta
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
JP6689890A
Other languages
Japanese (ja)
Inventor
Makoto Goto
誠 後藤
Shoichi Nara
昭一 奈良
Koichi Uchida
内田 康一
Masato Terasawa
真人 寺沢
Hideaki Yugawa
英明 湯川
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.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical 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 Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP6689890A priority Critical patent/JPH03266977A/en
Publication of JPH03266977A publication Critical patent/JPH03266977A/en
Pending legal-status Critical Current

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  • Enzymes And Modification Thereof (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

PURPOSE:To obtain in high yield microbe containing a high concentration of beta-tyrosinase by incubation in a medium with the glucose concentration falling between 0.3 and 0.01% (W/V). CONSTITUTION:beta-tyrosinase-contg. microbe belonging to Escherichia sp. such as Escherichia coli TD-001 (FERM P-10838) is aerobically incubated, while stirring under aeration, in a medium containing (A) a nitrogen source such as ammonium sulfate, (B) an inorganic salt such as potassium hydrogenphosphate, (C) a growth promotor such as thiamine, and (D) L- or DL-tyrosine. During this process, glucose is either continuously or intermittently added to the medium so that the glucose concentration in the medium be maintained within the range 0.3%-0.01% (W/V) throughout the incubation. Thence, after incubation, the culture fluid is centrifuged to recover wet microbe, Thereby, the objective microbe containing a high concentration of beta-tyrosinase can be obtained in high yield, thus producing said microbe in high efficiency.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、エシェリヒア属に属するβ−チロシナーゼ含
有菌を培養するに際し、培地中のグルコース濃度を調整
して、β−チロシナーゼを高濃度に含有する菌体を高収
量で得る培養方法に関する。
Detailed Description of the Invention [Industrial Application Field] The present invention is directed to culturing a β-tyrosinase-containing bacterium belonging to the genus Escherichia by adjusting the glucose concentration in the medium to increase the concentration of β-tyrosinase. The present invention relates to a culture method for obtaining high yields of bacterial cells.

[従来の技術] L−チロシンは、甲状腺機能亢進剤等の合成原料として
重要なアミノ酸であり、より安価な製造法の確立が期待
されている。
[Prior Art] L-tyrosine is an important amino acid as a raw material for the synthesis of thyroid function enhancers and the like, and it is expected that a cheaper manufacturing method will be established.

従来、L−チロシンは、大豆タンパク質の加水分解物か
らの抽出法や発酵法により製造されてきたが、精製コス
トが高いことや廃液の廃棄方法等に問題があり、近年、
β−チロシナーゼ含有菌体を使用した酵素法によるし一
チロシンの製造法が注目されている。
Conventionally, L-tyrosine has been produced by extraction from soy protein hydrolyzate or fermentation, but in recent years there have been problems such as high purification costs and waste disposal methods.
A method for producing tyrosine by an enzymatic method using β-tyrosinase-containing bacterial cells is attracting attention.

しかしながら、β−チロシナーゼを高濃度に含有する菌
体を高収量で調製する方法については殆んど報告がない
However, there are almost no reports on methods for preparing bacterial cells containing high concentrations of β-tyrosinase in high yields.

[発明が解決しようとする課題] 本発明の目的は、β−チロシナーゼを高濃度に含有する
菌体な高収量で得る効率的な培養方法を提供することに
ある。
[Problems to be Solved by the Invention] An object of the present invention is to provide an efficient culture method for obtaining a high yield of bacterial cells containing β-tyrosinase at a high concentration.

[課題を解決するための手段] 本発明は、エシェリヒア属に属するβ−チロシナーゼ含
有菌を培養するに際し、L−又はD Lチロシンを含有
する培地に、培養期間中の培地のグルコース濃度が0.
3%〜0.01%FW/V)の範囲内に保たれるように
グルコースを添加して培養することを特徴とするβ−チ
ロシナーゼ含有菌の培養方法である。
[Means for Solving the Problems] In the present invention, when culturing a β-tyrosinase-containing bacterium belonging to the genus Escherichia, a medium containing L- or D-L tyrosine is provided with a glucose concentration of 0.000 during the culture period.
This is a method for culturing β-tyrosinase-containing bacteria, which is characterized by culturing while adding glucose so that the concentration is maintained within the range of 3% to 0.01% FW/V).

以下、本発明をさらに具体的に説明する。The present invention will be explained in more detail below.

本発明に使用するエシェリヒア属に属するβ−チロシナ
ーゼ含有菌としては特に限定されるものではないが、例
えば、エシェリヒア・コリ(Escherichia 
coli)T D −001(F E RMP−108
38)が好適に用いられる。
The β-tyrosinase-containing bacteria belonging to the genus Escherichia used in the present invention are not particularly limited, but include, for example, Escherichia coli (Escherichia coli).
coli) TD-001 (FE RMP-108
38) is preferably used.

上記のエシェリヒア属に属するβ−チロシナーゼ含有菌
は、以下の炭素源、窒素源、無機塩、成長促進物質等の
栄養分を含む培地で培養することができる。
The β-tyrosinase-containing bacteria belonging to the genus Escherichia described above can be cultured in a medium containing the following nutrients such as a carbon source, a nitrogen source, an inorganic salt, and a growth promoting substance.

培地に含ませる窒素源としては、例えば、硫酸アンモニ
ウム、塩化アンモニウム、硫酸アンモニウム、燐酸アン
モニウム等のアンモニウム塩:硝酸カリ、硝酸ナトリウ
ム、硝酸アンモニウム等の硝酸塩;グルタミン酸、グル
タミン、アスパラギン酸、アスパラギン等の有機窒素:
アンモニアなどを単独もしくは混合して用いることがで
き、無機塩としては、例えば、リン酸−水素カリウム、
リン酸二水素カリウム、硫酸マグネシウム、硫酸鉄、硫
酸マンガンなどを単独もしくは混合して用いることがで
きる。該微生物の成長促進物質としては、ヂアミン、ビ
オチン等のビタミン類;メチオニン、システィン等のア
ミノ酸:あるいはこれらの全部もしくは一部を含有する
酵母エキス、ポリペプトン、肉エキス、コーンステイー
プリカー、カザミノ酸等が用いられる。
Nitrogen sources to be included in the medium include, for example, ammonium salts such as ammonium sulfate, ammonium chloride, ammonium sulfate, and ammonium phosphate; nitrates such as potassium nitrate, sodium nitrate, and ammonium nitrate; organic nitrogen such as glutamic acid, glutamine, aspartic acid, and asparagine;
Ammonia etc. can be used alone or in combination, and examples of inorganic salts include potassium hydrogen phosphate,
Potassium dihydrogen phosphate, magnesium sulfate, iron sulfate, manganese sulfate, and the like can be used alone or in combination. Substances that promote the growth of microorganisms include vitamins such as diamine and biotin; amino acids such as methionine and cysteine; or yeast extracts containing all or part of these, polypeptone, meat extracts, cornstap liquor, casamino acids, etc. is used.

培地に添加するし−又はDL−ヂロシン量は、0.01
−2%(W/V) 、 サラニ好マL<ハ005〜05
%FW/V)である。
The amount of DL-dyrosine added to the medium is 0.01
-2% (W/V), Sarani Favorite L<Ha005~05
%FW/V).

培地へのグルコースの添加は、培養期間中の培地中のグ
ルコースの濃度が03%〜0.01%FW/Vl の範
囲内に保たれるように連続的にあるいは間欠的に培地に
添加する。
Glucose is added to the medium continuously or intermittently so that the concentration of glucose in the medium during the culture period is maintained within the range of 0.3% to 0.01% FW/Vl.

培地温度は10〜45°C1好ましくは25〜40°C
の範囲であり、培地のpHは3〜10、好ましくは5〜
9の範囲である。培養中のpHに変化がある場合には、
アンモニア、苛性ソーダ、苛性カリなどで上記の範囲内
で一定に保持することが望ましい。培養時間は通常5〜
48時間行なわれる。
Medium temperature is 10-45°C, preferably 25-40°C
The pH of the medium is 3 to 10, preferably 5 to 10.
It is in the range of 9. If there is a change in pH during culture,
It is desirable to maintain the temperature constant within the above range using ammonia, caustic soda, caustic potash, etc. Culture time is usually 5~
It will be held for 48 hours.

さらに培養は好気的条件下で行ない、培養中の溶存酸素
が律速因子とならないように、通気撹拌をすることが望
ましい。
Furthermore, it is desirable that the culture be carried out under aerobic conditions, with aeration and agitation so that dissolved oxygen during the culture does not become a rate-limiting factor.

「発明の効果] 本発明の培養方法によれば、β−チロシナーゼを高濃度
に含有する菌体な高収量で得ることができ、したがって
、β−チロシナーゼを効率よく生産することができる。
"Effects of the Invention" According to the culture method of the present invention, a high yield of bacterial cells containing a high concentration of β-tyrosinase can be obtained, and therefore β-tyrosinase can be efficiently produced.

[実施例] 以下、実施例を挙げて更に詳細に本発明を説明する。[Example] Hereinafter, the present invention will be explained in more detail with reference to Examples.

以下の実施例において、β−チロシナーゼ活性の測定は
、次の方法で実施した。
In the Examples below, β-tyrosinase activity was measured by the following method.

培養液20−から遠心分離(4,000rpm、15分
間、4°C)した菌体な、50mMのリン酸緩衝液(p
H8,0)20−に懸濁後、再び遠心分離(4,000
rpm、15分間、4℃)して菌体を集める。該集菌体
を上記緩衝液2−に懸濁後、超音波破砕処理(ブランソ
ン製ソニファイヤー200)L、該処理物を遠心分離(
12,00Orpm、40分間、4℃)しだ上清液を供
試酵素液とした。
Cells centrifuged (4,000 rpm, 15 minutes, 4°C) from culture solution 20- were added to 50 mM phosphate buffer (p
After suspending in 20-H8,0) centrifugation again (4,000
rpm, 15 minutes, 4°C) and collect the bacterial cells. After suspending the collected bacteria in the above-mentioned buffer solution 2-, the microorganisms were subjected to ultrasonic disruption treatment (Sonifier 200 manufactured by Branson L), and the treated material was centrifuged (
(12,00 Orpm, 40 minutes, 4°C) The soybean supernatant liquid was used as the test enzyme solution.

反応は、上記酵素液の0.1−を下記反応液の0.9−
に添加後、30℃にて15分間反応させた後、100°
C沸とう水中に1分間浸漬し、さらに該処理液を蒸留水
にて10倍に希釈し、該希釈液を濾過膜(2,2P)を
通して酵素タンパクを分離した。透過液中のし一チロシ
ン量を高速液体クロマトグラフィー(島津LC−5A)
にて定量した。
For the reaction, 0.1- of the above enzyme solution was mixed with 0.9- of the following reaction solution.
After adding to the water, reacting at 30°C for 15 minutes,
The sample was immersed in C boiling water for 1 minute, and the treated solution was further diluted 10 times with distilled water, and the diluted solution was passed through a filtration membrane (2,2P) to separate the enzyme protein. The amount of tyrosine in the permeate was measured by high performance liquid chromatography (Shimadzu LC-5A).
It was quantified.

〈反応液組成〉 5’OmMリン酸緩衝液(pH8,0)1f2中、フェ
ノール    10g L−セリン    40g N H4CQ     10 g EDTA       2g及び N a 2 S Os     4 gを含有。
<Reaction solution composition> Contains 10 g of phenol, 40 g of L-serine, 10 g of NH4CQ, 2 g of EDTA, and 4 g of Na2SOs in 1f2 of 5'OmM phosphate buffer (pH 8,0).

また供試酵素液中のクンバク質量の測定は、Lowry
等の方法(Journal of Biologica
lChemistry、 vol、 193.p、26
5.  (19511)に従った。
In addition, the mass of kumbaku in the test enzyme solution can be measured using Lowry
etc. (Journal of Biologica
lChemistry, vol, 193. p, 26
5. (19511).

培地中のグルコース濃度の測定は、グルコースCテスト
和光[和光純薬玉業■製]を用いて行なった。
The glucose concentration in the medium was measured using Glucose C Test Wako [manufactured by Wako Pure Chemical Industries, Ltd.].

菌体収量は培養液50艷から遠心分離 (8,00Orpm、20分間、4°C)後に回収され
た湿菌体量として測定した。
The bacterial cell yield was measured as the amount of wet bacterial cells collected after centrifugation (8.00 rpm, 20 minutes, 4°C) from 50 cells of the culture solution.

実施例 第1表に示した培地100−を500i容三角フラスコ
に分注し、120°Cで15分間滅菌処理したものに、
50%(W/Vl グルコース溶液(120℃、15分
間滅菌)を無菌的に1i添加後、β−チロシナーゼ生産
菌であるエシェリヒア・コリTD−001,(FERM
  P−10838)を植菌し、37°Cで1日振盪培
養した。
Example 100 of the culture medium shown in Table 1 was dispensed into a 500i Erlenmeyer flask and sterilized at 120°C for 15 minutes.
After aseptically adding 50% (W/Vl glucose solution (sterilized at 120°C for 15 minutes) for 1 i, Escherichia coli TD-001, (FERM
P-10838) was inoculated and cultured with shaking at 37°C for 1 day.

該培養液の20−を同様にして調製した培地1.000
mffに接種し、通気撹拌培養槽を用い、37℃にて回
転数1.OOOrpm、通気量1vvm、pH7,2(
28%アンモニア水で調整)にて8時間培養した。なお
、グルコースは50%FW/V)の水溶液(120℃で
15分間滅菌処理)を用いて、経時的に培養液中のグル
コース濃度を測定しながら、第2表に示した各実験区の
濃度上限を越えないように、無菌的に連続的又は間欠的
に添加し、各実験区の全添加量が20gになった時点で
添加を終了した。
1.000 of a medium prepared in the same manner as 20 of the culture solution
MFF was inoculated and heated at 37°C with a rotational speed of 1. OOOrpm, air flow rate 1vvm, pH 7.2 (
(adjusted with 28% ammonia water) for 8 hours. In addition, while measuring the glucose concentration in the culture solution over time using an aqueous solution (sterilized at 120°C for 15 minutes) of 50% FW/V), the concentration of glucose in each experimental group shown in Table 2 was measured. It was added continuously or intermittently in an aseptic manner so as not to exceed the upper limit, and the addition was stopped when the total amount added in each experimental group reached 20 g.

第1表 L−チロシン KH2PO4 K 2 HP O4 (NH,)  2SO。Table 1 L-tyrosine KH2PO4 K 2 HP O4 (NH,) 2SO.

M g S O4・7H20 FeSO4・7H20 カザミノ酸 (DIFCOI 酵母エキス 蒸留水を加えて 2、0g 1、 6g 5、5g 3.0g 0、1g 0mg 3、0g 3、0g 1、 000− (pH7,2) 培養終了後、 各培養液20−づつから遠心分離 を行ない、前記した方法にてβ−チロシナーゼ活性を測
定した。なお、比較例としては培養初期にグルコース2
0 g/12を添加するのみで培養した菌体を用いた。
M g SO4・7H20 FeSO4・7H20 Casamino acids (DIFCOI Yeast extract Add distilled water 2,0g 1,6g 5,5g 3.0g 0,1g 0mg 3,0g 3,0g 1,000- (pH7,2 ) After the completion of the culture, 20 μl of each culture solution was centrifuged, and β-tyrosinase activity was measured using the method described above.
Bacterial cells cultured only by adding 0 g/12 were used.

第2表 ×比較例(培養初期にグルコース20 g / f2添
加)の活性を1,0とした相対値
Table 2 × Relative value with the activity of comparative example (20 g/f2 added at the beginning of culture) as 1,0

Claims (1)

【特許請求の範囲】[Claims] エシェリヒア属に属するβ−チロシナーゼ含有菌を培養
するに際し、L−又はDL−チロシンを含有する培地に
、培養期間中の培地のグルコース濃度が0.3%〜0.
01%(W/V)の範囲内に保たれるようにグルコース
を添加して培養することを特徴とするβ−チロシナーゼ
含有菌の培養方法。
When culturing β-tyrosinase-containing bacteria belonging to the genus Escherichia, a medium containing L- or DL-tyrosine is used with a glucose concentration of 0.3% to 0.0% during the culture period.
1. A method for culturing β-tyrosinase-containing bacteria, the method comprising culturing with the addition of glucose so that the ratio is maintained within a range of 0.01% (W/V).
JP6689890A 1990-03-19 1990-03-19 Incubation of beta-tyrosinase-containing microbe Pending JPH03266977A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6689890A JPH03266977A (en) 1990-03-19 1990-03-19 Incubation of beta-tyrosinase-containing microbe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6689890A JPH03266977A (en) 1990-03-19 1990-03-19 Incubation of beta-tyrosinase-containing microbe

Publications (1)

Publication Number Publication Date
JPH03266977A true JPH03266977A (en) 1991-11-27

Family

ID=13329213

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6689890A Pending JPH03266977A (en) 1990-03-19 1990-03-19 Incubation of beta-tyrosinase-containing microbe

Country Status (1)

Country Link
JP (1) JPH03266977A (en)

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