Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS6035113B2 - Method for producing sorbitol using microorganisms - Google Patents
[go: Go Back, main page]

JPS6035113B2 - Method for producing sorbitol using microorganisms - Google Patents

Method for producing sorbitol using microorganisms

Info

Publication number
JPS6035113B2
JPS6035113B2 JP18245283A JP18245283A JPS6035113B2 JP S6035113 B2 JPS6035113 B2 JP S6035113B2 JP 18245283 A JP18245283 A JP 18245283A JP 18245283 A JP18245283 A JP 18245283A JP S6035113 B2 JPS6035113 B2 JP S6035113B2
Authority
JP
Japan
Prior art keywords
sorbitol
bacterial cells
glucose
microorganisms
producing sorbitol
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
JP18245283A
Other languages
Japanese (ja)
Other versions
JPS6075291A (en
Inventor
典秋 小泉
昇一 木瀬
英勝 前田
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP18245283A priority Critical patent/JPS6035113B2/en
Publication of JPS6075291A publication Critical patent/JPS6075291A/en
Publication of JPS6035113B2 publication Critical patent/JPS6035113B2/en
Expired legal-status Critical Current

Links

Landscapes

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

Description

【発明の詳細な説明】 本発明はブドウ糖から微生物法によりソルビトールを製
造する方法に関し、より詳しくアゾトバクター属、ベィ
ジェリンキィア属またはミコバクテリゥム属に属し、ソ
ルビトール生産能を有する微生物を用いて、ソルビトー
ルを効率よく製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing sorbitol from glucose by a microbial method. It relates to an efficient manufacturing method.

ソルビトールは特有の甘味を有すると共に反応性に乏し
く、無害であって湿潤調節作用を有するため、そのまま
食品、歯みがき、化粧品等に添加物として使用される他
、ビタミンC、界面活性剤製造の中間原料として広く使
用されている。
Sorbitol has a unique sweet taste, has low reactivity, is harmless, and has a moisturizing effect, so it is used as an additive in foods, toothpaste, cosmetics, etc., and is also used as an intermediate raw material in the production of vitamin C and surfactants. It is widely used as

ソルビトールは現在、工業的にはブドウ糖をラネーニッ
ケル等のNj触媒を用いて接触還元して製造されている
が、このような方法によれば反応条件が必然的に高温(
16000)、高圧(170k9/均)となりエネルギ
ーを多く消費する他、耐圧容器を必要とし、更に水素を
取扱う関係上爆発の危険が内在している。本発明者らは
上記万法とは発想を異にし、グルコースを微生物学的に
還元することにより緩和な条件でソルビトールを製造す
る方法を試みた。
Sorbitol is currently produced industrially by catalytic reduction of glucose using an Nj catalyst such as Raney nickel, but such a method inevitably requires high temperature (
16,000), high pressure (170k9/average), which consumes a lot of energy, requires a pressure-resistant container, and has the inherent danger of explosion due to the handling of hydrogen. The present inventors differed from the above-mentioned methods and attempted a method for producing sorbitol under mild conditions by microbiologically reducing glucose.

フドゥ糖をソルビトールに還元する機構、は動物細胞系
では羊の精のう中(日.G.Hem Biochem.
Bioph松.Acta37(1960)127一13
8)あるいはレンズ中(M.lou Biochem.
BiophyS.Acta 141(1967)547
一559)にその存在が知られているが、微生物ではソ
ルビトールを生産した例がなくわずかに特公昭45一2
4834号及び46一23038号にキシロースをキシ
リトールに好気的に発酵して還元する方法が開示されて
いるにすぎない。また、上記発明に開示された菌株をグ
ルコース培地中で培養してもソルビトールを得ることは
できなかった。そこで、本発明者らは多種類の微生物に
ついて、試験を行った結果、五炭糠中で培養増殖せしめ
たアゾトバクター属、ベィジェリンキィア属又はミコバ
クテリゥム属に属する細菌の培養体、菌体、あるいは菌
体抽出物、凍結乾燥菌体が基質グルコースをソルビート
ールに高収率に還元することを見出して本発明を完成す
るに至った。
The mechanism for reducing fudu sugar to sorbitol has been demonstrated in animal cell systems in the spermatozoa of sheep (Japanese G. Hem Biochem.
Bioph pine. Acta37 (1960) 127-13
8) Or in a lens (M.lou Biochem.
BiophyS. Acta 141 (1967) 547
Its existence is known in 1559), but there is no example of microorganisms producing sorbitol, and only a few
No. 4834 and No. 46-23038 only disclose a method for aerobically fermenting and reducing xylose to xylitol. Further, even if the strain disclosed in the above invention was cultured in a glucose medium, sorbitol could not be obtained. Therefore, the present inventors conducted tests on many types of microorganisms, and found that cultures, cells, or We have completed the present invention by discovering that bacterial cell extracts and freeze-dried bacterial cells reduce the substrate glucose to sorbitol in high yield.

本発明に用いられる微生物はいずれも市販の株でよくア
ゾトバクター属としては例えばアゾトバクタ ー ピ
ネ ラ ンデイ(Azoto舷ctervinela
ndii)が挙げられるが、中でもアゾトバクター ビ
ネランデイlAMI078が好ましい。
Any microorganism used in the present invention may be a commercially available strain, and examples of the Azotobacter genus include, for example, Azotobacter pinella landii (Azotobacter pinelandii).
ndii), among which Azotobacter vinelandii AMI078 is preferred.

ベイジヱリンキィア属としてはベイジェリンキィァ ィ
ンディカ(氏jerinckiaindica)が挙げ
られるが、中でもベイジェリンキイア インデイカlA
MII95が好ましい。ミコバクテリウム属としてはミ
コバクテリウムフレィ(Myco舷cterimmph
lei)が挙げられるが、中でもミコバクテリウム フ
レイlAM12064が好ましい。
The genus Beijerinckia includes Beijerinckia indica (Mr. jerinckiaindica), among which Beijerinckia indica lA
MII95 is preferred. The genus Mycobacterium is Mycobacterium freyi (Mycocterimph).
lei), among which Mycobacterium freyi AM12064 is preferred.

本発明に係るアゾトバクター属、ベィジェリンキィア属
菌を増殖させるにあたっては、炭素源として2〜15%
○−キシロース、D−アラビノース、D−リボース等の
五炭糖を含有し、他にK2HP04、CaC03、Mg
S04、NaC1、FeS04、Na2Moo4等の無
機塩のみを含む無窒素培地を用いる。
In growing Azotobacter and Beijerinchia bacteria according to the present invention, 2 to 15% carbon source is used.
○ Contains pentose such as xylose, D-arabinose, D-ribose, and also K2HP04, CaC03, Mg
A nitrogen-free medium containing only inorganic salts such as S04, NaCl, FeS04, Na2Moo4, etc. is used.

また、ミコバクテリウム属菌を増殖させるにあたっては
、炭素源として2〜15%Dーキシロース、Dーアラビ
ノ−ス、D−リボース等の五炭糖を含有し、イーストエ
キス又はコーンステイ−プリカ一等を添加した液体培地
を用いる。培養は25〜30ooで2〜10日間行う。
培養法は通気培養、振濠培養、回転ドラム法等好気的条
件であればいずれも採用できる。また、培地に上記成分
の他、各種ビタミン、無機質や適当な有機物を加えるこ
とにより増殖率を高めることもできる。次いで、このよ
うにして得られた培養体とグルコースを接触させること
によりソルビトールを得ることができるが、菌体を洗浄
して得た生菌をそのまま使用してもある程度の効果は認
められる。
In addition, when growing Mycobacterium bacteria, 2 to 15% of pentose such as D-xylose, D-arabinose, and D-ribose are used as a carbon source, and yeast extract or corn stay plica is added. Use the added liquid medium. Cultivation is carried out at 25-30 oo for 2-10 days.
Any culture method can be adopted as long as it is under aerobic conditions, such as aeration culture, shaking moat culture, and rotating drum method. The growth rate can also be increased by adding various vitamins, minerals, and appropriate organic substances to the medium in addition to the above-mentioned components. Next, sorbitol can be obtained by contacting the culture thus obtained with glucose, but a certain degree of effectiveness can be observed even if the live bacteria obtained by washing the cells are used as they are.

しかし、凍結乾燥菌体、凍結融解菌体、アセトン、エー
テル等の有機溶媒処理した菌体等の処理菌体を用いた方
がはるかに効果的である。また、超音波処理、ピブロゲ
ンセルミル等の破砕機を用いて調製した菌体破砕物およ
び菌体抽出物を用いることもできる。グルコ−スの還元
にあたっては、上記方法で得られた処理菌体、菌体破砕
物又はこれから分離した菌体抽出物あるいはこれらの混
合物を1〜60%濃度のブドウ糖液に加え、10〜60
oC、望ましくは25〜35qoで反応させる。
However, it is much more effective to use treated bacterial cells such as freeze-dried bacterial cells, freeze-thawed bacterial cells, and treated bacterial cells with organic solvents such as acetone and ether. Furthermore, crushed bacterial cells and bacterial cell extracts prepared by ultrasonication or using a crusher such as a pibrogen cell mill can also be used. To reduce glucose, add the treated bacterial cells, crushed bacterial cells, bacterial cell extracts isolated therefrom, or mixtures thereof obtained in the above method to a glucose solution with a concentration of 10 to 60%.
The reaction is carried out at oC, preferably 25 to 35 qo.

この際補酵素として還元型ニコチンアミド、アデニン
ジヌクレオチド、ホスフェイト(以下、「NADPH」
という。)を共存させることによってソルビトールの生
産性はより飛躍的に向上させることができる。NADP
Hの添加量は使用する菌体の調製法あるいは菌体の抽出
操作により大幅に異なり、ブドウ糖1モル当り0.1ミ
リモル〜20モル望ましくは0.1モル〜10モルであ
る。反応に要する時間もまた条件により大きく変動し、
例えば繭体抽出物を用いた場合、30分ないし14日で
反応は完了する。反応終了後、母液からソルビトールの
分離糟裂にあたっては遠心分離法、限外濠過法、イオン
交換法等公知の方法を組合せて利用する。
At this time, reduced nicotinamide and adenine are used as coenzymes.
Dinucleotide, phosphate (hereinafter referred to as "NADPH")
That's what it means. ) can dramatically improve the productivity of sorbitol. NADP
The amount of H added varies greatly depending on the method of preparing the bacterial cells used or the extraction procedure for the bacterial cells, and is 0.1 mmol to 20 mol, preferably 0.1 mol to 10 mol, per mol of glucose. The time required for the reaction also varies greatly depending on the conditions.
For example, when a cocoon extract is used, the reaction is completed in 30 minutes to 14 days. After the reaction is completed, sorbitol is separated from the mother liquor by using a combination of known methods such as centrifugation, ultra-ditching, and ion exchange.

以下、実施例を挙げて本発明を詳述に説明する。Hereinafter, the present invention will be explained in detail with reference to Examples.

なお、生産物の確認は薄層クロマトグラフィー、高速液
体クロマトグラフィーおよびガスクロマトグラフィ一に
よって行った。また定量は高速液体クロマトグラフィー
で行った。実施例 1 500の上客消化フラスコに滅菌した表1に示す組成の
培地50叫を入れ、A.VinelandmAMI07
8珠を1白金耳桶菌し、30oo、6日間培養した。
The product was confirmed by thin layer chromatography, high performance liquid chromatography, and gas chromatography. Quantification was performed using high performance liquid chromatography. Example 1 Fifty centimeters of a sterilized medium having the composition shown in Table 1 were placed in a 500-liter digestion flask. VinelandmAMI07
Eight beads were inoculated into one platinum loop and cultured for 30 days for 6 days.

培養菌体をリン酸緩衝液で2回洗浄し、610n肌にお
ける濁度が25になるようにリン酸緩衝液に懸濁した。
この菌体懸濁液を20分間超音波処理し、14000夕
、20分間遠心分離し、その上清画分をソルビトールの
生産に供した。上記操作で得た上清画分を用いて表2に
示す組成の反応液を調製し、pH7.5とし、30qo
で24時間反応させた。
The cultured bacterial cells were washed twice with phosphate buffer and suspended in phosphate buffer so that the turbidity at 610n skin was 25.
This cell suspension was sonicated for 20 minutes, centrifuged at 14,000 yen for 20 minutes, and the supernatant fraction was used for the production of sorbitol. Using the supernatant fraction obtained in the above procedure, a reaction solution having the composition shown in Table 2 was prepared, the pH was adjusted to 7.5, and 30 qo
The mixture was allowed to react for 24 hours.

その反応液中に0.5夕/そのソルビトールが得られた
。表I 表2 実施例 2 B.indicaI AMII95株を用いた以外は実
施例1と同様に培養し得られた菌体をリン酸緩衝液で2
回洗浄した後、凍結乾燥した。
0.5 sorbitol was obtained in the reaction solution. Table I Table 2 Example 2 B. The cells were cultured in the same manner as in Example 1 except that indicaI AMII95 strain was used.
After washing twice, it was freeze-dried.

得られた凍結乾燥菌体を用いて表3に示した反応組成液
を調製し、30ooで24時間反応させた。
A reaction composition solution shown in Table 3 was prepared using the obtained freeze-dried bacterial cells, and reacted at 30oo for 24 hours.

反応液中に1.5夕/そソルビトールが得られた。表3
実施例 3 500の‘容消化フラスコに表4に示す組成の培地50
叫を入れて滅菌し、M.phlcilAM12064珠
を楯菌し、30qo、6日間培養した。
1.5 ml of sorbitol was obtained in the reaction solution. Table 3
Example 3 50 liters of medium with the composition shown in Table 4 was placed in a 500' capacity digestion flask.
Sterilize it with M. The phlcil AM12064 beads were plated and cultured for 30 qo for 6 days.

培養菌体をリン酸緩衝液で2回洗浄した後、凍結乾燥し
た。得られた凍結乾燥菌体を用いて表3に示した反応組
成液を調製し30ooで2独特間反応させた。
The cultured cells were washed twice with phosphate buffer and then freeze-dried. A reaction composition solution shown in Table 3 was prepared using the obtained freeze-dried bacterial cells, and the reaction mixture was reacted at 30°C for 2 hours.

Claims (1)

【特許請求の範囲】[Claims] 1 アゾトバクター属、ベイジエリンキイア属またはミ
コバクテリウム属に属し、ソルビトール生産能を有する
微生物を五炭糖類を主炭素源とする培地に培養し、次い
で得られた培養体とブドウ糖を接触せしめてソルビトー
ルを製造することを特徴とする微生物によるソルビトー
ルの製造法。
1. A microorganism belonging to the genus Azotobacter, Beisierinchia, or Mycobacterium and capable of producing sorbitol is cultured in a medium containing pentose as the main carbon source, and then the resulting culture is brought into contact with glucose. A method for producing sorbitol using a microorganism, characterized by producing sorbitol.
JP18245283A 1983-09-30 1983-09-30 Method for producing sorbitol using microorganisms Expired JPS6035113B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18245283A JPS6035113B2 (en) 1983-09-30 1983-09-30 Method for producing sorbitol using microorganisms

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18245283A JPS6035113B2 (en) 1983-09-30 1983-09-30 Method for producing sorbitol using microorganisms

Publications (2)

Publication Number Publication Date
JPS6075291A JPS6075291A (en) 1985-04-27
JPS6035113B2 true JPS6035113B2 (en) 1985-08-13

Family

ID=16118512

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18245283A Expired JPS6035113B2 (en) 1983-09-30 1983-09-30 Method for producing sorbitol using microorganisms

Country Status (1)

Country Link
JP (1) JPS6035113B2 (en)

Also Published As

Publication number Publication date
JPS6075291A (en) 1985-04-27

Similar Documents

Publication Publication Date Title
US4762788A (en) Process for producing cellulolytic enzymes
JP2000513925A (en) Method for producing N-acetyl-D-glucosamine
CN103266152B (en) Method for producing trehalose through utilizing immobilized trehalose synthase
JPS63213501A (en) Production of pectin
JPS5943157B2 (en) Method for producing sorbitol using Pichia bacteria
JPS6035113B2 (en) Method for producing sorbitol using microorganisms
JPS5937076B2 (en) Fermentation method Vitamin B↓1↓2 manufacturing method
KR930001119B1 (en) Process for the preparation of ascorbic acid 2-phosphate
JPS6279777A (en) Production of superoxide dismutase
Tramper et al. Xanthine oxidase activity of arthrobacter x-4 cells immobilized in glutaraldehyde-crosslinked gelatin
JPS62130695A (en) Production of galactooligo saccharide
JPS639829B2 (en)
JPS5934357B2 (en) Method for producing sorbitol using microorganisms
JPS5937075B2 (en) Method for producing sorbitol using Hansenula bacteria
CN118207270A (en) A method for producing β-nicotinamide mononucleotide by Kluyveromyces lactis
JPS5930400B2 (en) Method for producing sorbitol using microorganisms
JPH0889262A (en) Method for producing inositol and method for obtaining antibiotic resistant strain
Imdad et al. Fermentation-Based Production and Immobilization of β-Glucuronidase From Talaromyces pinophilus Li-93 for Efficient Bioconversion of Glycyrrhizin
JPS6319152B2 (en)
JPH05137590A (en) Purification of lactosyl fructoside by microorganism
JPS639830B2 (en)
JPH0419835B2 (en)
JPS5816692A (en) Preparation of l-tryptophan by enzyme
JPS63313592A (en) Production of l-tryptophans
JPH05276970A (en) Production of saccharide solution having high content of xylosylfructoside by microorganism