JPH03259090A - Production of difructose dianhydride iii - Google Patents
Production of difructose dianhydride iiiInfo
- Publication number
- JPH03259090A JPH03259090A JP2059699A JP5969990A JPH03259090A JP H03259090 A JPH03259090 A JP H03259090A JP 2059699 A JP2059699 A JP 2059699A JP 5969990 A JP5969990 A JP 5969990A JP H03259090 A JPH03259090 A JP H03259090A
- Authority
- JP
- Japan
- Prior art keywords
- inulin
- strain
- arthrobacter
- cultured
- enzyme
- 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
Links
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 title claims abstract description 5
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 229920001202 Inulin Polymers 0.000 claims abstract description 20
- JYJIGFIDKWBXDU-MNNPPOADSA-N inulin Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)OC[C@]1(OC[C@]2(OC[C@]3(OC[C@]4(OC[C@]5(OC[C@]6(OC[C@]7(OC[C@]8(OC[C@]9(OC[C@]%10(OC[C@]%11(OC[C@]%12(OC[C@]%13(OC[C@]%14(OC[C@]%15(OC[C@]%16(OC[C@]%17(OC[C@]%18(OC[C@]%19(OC[C@]%20(OC[C@]%21(OC[C@]%22(OC[C@]%23(OC[C@]%24(OC[C@]%25(OC[C@]%26(OC[C@]%27(OC[C@]%28(OC[C@]%29(OC[C@]%30(OC[C@]%31(OC[C@]%32(OC[C@]%33(OC[C@]%34(OC[C@]%35(OC[C@]%36(O[C@@H]%37[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O%37)O)[C@H]([C@H](O)[C@@H](CO)O%36)O)[C@H]([C@H](O)[C@@H](CO)O%35)O)[C@H]([C@H](O)[C@@H](CO)O%34)O)[C@H]([C@H](O)[C@@H](CO)O%33)O)[C@H]([C@H](O)[C@@H](CO)O%32)O)[C@H]([C@H](O)[C@@H](CO)O%31)O)[C@H]([C@H](O)[C@@H](CO)O%30)O)[C@H]([C@H](O)[C@@H](CO)O%29)O)[C@H]([C@H](O)[C@@H](CO)O%28)O)[C@H]([C@H](O)[C@@H](CO)O%27)O)[C@H]([C@H](O)[C@@H](CO)O%26)O)[C@H]([C@H](O)[C@@H](CO)O%25)O)[C@H]([C@H](O)[C@@H](CO)O%24)O)[C@H]([C@H](O)[C@@H](CO)O%23)O)[C@H]([C@H](O)[C@@H](CO)O%22)O)[C@H]([C@H](O)[C@@H](CO)O%21)O)[C@H]([C@H](O)[C@@H](CO)O%20)O)[C@H]([C@H](O)[C@@H](CO)O%19)O)[C@H]([C@H](O)[C@@H](CO)O%18)O)[C@H]([C@H](O)[C@@H](CO)O%17)O)[C@H]([C@H](O)[C@@H](CO)O%16)O)[C@H]([C@H](O)[C@@H](CO)O%15)O)[C@H]([C@H](O)[C@@H](CO)O%14)O)[C@H]([C@H](O)[C@@H](CO)O%13)O)[C@H]([C@H](O)[C@@H](CO)O%12)O)[C@H]([C@H](O)[C@@H](CO)O%11)O)[C@H]([C@H](O)[C@@H](CO)O%10)O)[C@H]([C@H](O)[C@@H](CO)O9)O)[C@H]([C@H](O)[C@@H](CO)O8)O)[C@H]([C@H](O)[C@@H](CO)O7)O)[C@H]([C@H](O)[C@@H](CO)O6)O)[C@H]([C@H](O)[C@@H](CO)O5)O)[C@H]([C@H](O)[C@@H](CO)O4)O)[C@H]([C@H](O)[C@@H](CO)O3)O)[C@H]([C@H](O)[C@@H](CO)O2)O)[C@@H](O)[C@H](O)[C@@H](CO)O1 JYJIGFIDKWBXDU-MNNPPOADSA-N 0.000 claims abstract description 20
- 229940029339 inulin Drugs 0.000 claims abstract description 20
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- 241000894006 Bacteria Species 0.000 description 12
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- 239000000243 solution Substances 0.000 description 10
- 241000894007 species Species 0.000 description 9
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 6
- 241000186063 Arthrobacter Species 0.000 description 5
- 210000004027 cell Anatomy 0.000 description 5
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 229920002472 Starch Polymers 0.000 description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
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- HYPYXGZDOYTYDR-HAJWAVTHSA-N 2-methyl-3-[(2e,6e,10e,14e)-3,7,11,15,19-pentamethylicosa-2,6,10,14,18-pentaenyl]naphthalene-1,4-dione Chemical compound C1=CC=C2C(=O)C(C/C=C(C)/CC/C=C(C)/CC/C=C(C)/CC/C=C(C)/CCC=C(C)C)=C(C)C(=O)C2=C1 HYPYXGZDOYTYDR-HAJWAVTHSA-N 0.000 description 3
- 229930091371 Fructose Natural products 0.000 description 3
- 239000005715 Fructose Substances 0.000 description 3
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 3
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 3
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 3
- 235000011130 ammonium sulphate Nutrition 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 239000004202 carbamide Substances 0.000 description 3
- 238000005119 centrifugation Methods 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 239000012153 distilled water Substances 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- WCRXHNIUHQUASO-UVZVDVBNSA-N menaquinone-9 Chemical compound C1=CC=C2C(=O)C(C/C=C(C)/CC/C=C(C)/CC/C=C(C)/CC/C=C(C)/CC/C=C(C)/CC/C=C(C)/CC/C=C(C)/CC/C=C(C)/CCC=C(C)C)=C(C)C(=O)C2=C1 WCRXHNIUHQUASO-UVZVDVBNSA-N 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 229910052700 potassium Inorganic materials 0.000 description 3
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- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
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- 239000004472 Lysine Substances 0.000 description 2
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Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ジフルクトース・ジアンヒドリド■(以下、
rDFAI[[Jという)の製造法に関するものである
。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to difructose dianhydride (hereinafter referred to as
The present invention relates to a method for producing rDFAI [[referred to as J].
〔従来技術及び発明が解決しようとする問題点〕DFA
Iはフルクトース2分子が1−2’、2−3′の間で脱
水縮合した構造をもつ2糖類であり、ジャクスンらによ
り1929年番こ単離同定されている(Bur、5ta
nd、J、Res、J、 27.1929)。[Prior art and problems to be solved by the invention] DFA
I is a disaccharide with a structure in which two fructose molecules are dehydrated and condensed between 1-2' and 2-3', and was isolated and identified in 1929 by Jackson et al. (Bur, 5ta).
nd, J, Res, J, 27.1929).
D F A、 IIIは、動物体内では代謝されず、非
発酵性の糖であるため低カロリー甘味剤として着目され
ており、今後美容食等多方面に利用されることが予想さ
れる。Since DFA, III is a non-fermentable sugar that is not metabolized in the animal body, it is attracting attention as a low-calorie sweetener, and it is expected that it will be used in many fields such as beauty foods in the future.
ジャクソンらは、フルクトースを主構成とする多糖であ
るイヌリンを酸加水分解することによりDFAI[lを
得ているが、収率はわずか2%弱であり、効率的な方法
とは言えない。Jackson et al. obtained DFAI[l] by acid hydrolyzing inulin, a polysaccharide mainly composed of fructose, but the yield was only a little less than 2%, and it cannot be said to be an efficient method.
また田中らは1972年 アルスロバクタ−・ウレアフ
ァシェンスの産生ずるイヌリン分解酵素を用いてイヌリ
ンからD FAII[を生成させている(Biochi
m、Biophys、Acta、284,248,19
72 )。In 1972, Tanaka et al. produced DFAII from inulin using an inulin-degrading enzyme produced by Arthrobacter ureafaciens (Biochi et al.
m, Biophys, Acta, 284,248,19
72).
しかし本酵素は温度に対する安定性が低く、60°Cを
越えると象、激な失活がおき、工業化を行う際に適切な
酵素であるとは言えない。However, this enzyme has low stability against temperature, and is severely inactivated at temperatures exceeding 60°C, so it cannot be said to be an appropriate enzyme for industrialization.
本発明者らはこれらの点を解決すべく種に研究をXねた
結果、アルスロバクター・エスピー(Arthroba
cter SP、) (M CI 2496 )微工
研菌寄第11288号(FERMP−11288)由来
のイヌリン分解酵素が効率よ(DFAIIIを生産し、
しかも従来のものに比べて熱に対する安定性が高いので
、工業的にDFAI[Iの連続生産を行わせる際効率的
に行わせることができることを知得し、本発明を完成す
るに至った。The present inventors conducted extensive research on species to solve these problems, and as a result, they discovered that Arthrobacter sp.
cter SP, ) (MCI 2496) The inulin-degrading enzyme derived from FERMP-11288 (FERMP-11288) efficiently (produces DFAIII,
Moreover, since it has higher thermal stability than conventional products, it was found that continuous industrial production of DFAI[I can be carried out efficiently, leading to the completion of the present invention.
即ち本発明の要旨は、イヌリン含有溶液中、イヌリンを
アルスロバクター・エスピー(MCI2496)微工研
菌寄第11288号(FERMP−11288)由来の
イヌリン分解酵素と反応させることを特徴とするジフル
クトース・ジアンヒドリド四の製造方法に存する。That is, the gist of the present invention is to produce difructose, which is characterized by reacting inulin with an inulin-degrading enzyme derived from Arthrobacter sp. (MCI2496) FERMP-11288 in an inulin-containing solution.・It consists in the production method of dianhydride 4.
以下本発明を説明するに、本発明で使用するイヌリン分
g酵素は、アルスロバクター・エスピー(MCI249
6)微工研菌寄第11288号(FERMP−1128
8)由来のものである。To explain the present invention below, the inulin component enzyme used in the present invention is Arthrobacter sp. (MCI249).
6) FERMP-1128 No. 11288 (FERMP-1128)
8) It is derived from
本発明のアルスロバクター・エスピー(MCI2496
号菌)は、本発明者等により、天然土壌から分離された
細菌であり、その菌学的性状は次の通りである。Arthrobacter sp. (MCI2496) of the present invention
Bacterium No.) is a bacterium isolated from natural soil by the present inventors, and its mycological properties are as follows.
1、形態的性状
○ハートインフュージョン寒天培地上、30°C11週
間のコロニーの特徴
工)外形 ・ 円形
2)大きさ ・ 2〜311I113)表面の
隆起 : 凸状
4)表面の形状 : 平滑
5)光沢 ・ 鈍光
6)色調 ・ 黄味灰色
7)透明度 ・ 不透明
8)周縁 金縁
Oハートインフュージョン寒天培地上、30’C13〜
48時間培養中の形態的性質
1)細胞形態:培養後6〜12時間ぐらいまでは、細胞
は不均一に伸長し、長い桿状になる。その後中央部に隔
壁が形成され、細胞は湾曲状に曲がり、漸次分節を繰り
返す。18時間以降はほとんどの細胞が短稈状の斉一な
形態に変化する。1. Morphological characteristics Characteristics of colonies grown on heart infusion agar medium at 30°C for 11 weeks Work) External shape: circular 2) Size: 2-311I113) Surface ridges: convex 4) Surface shape: smooth 5) Gloss / Dull light 6) Color tone / Yellowish gray 7) Transparency / Opaque 8) Periphery Gold-rimmed O heart infusion agar medium, 30'C13~
Morphological properties during 48-hour culture 1) Cell morphology: Until about 6 to 12 hours after culture, cells elongate unevenly and become long rod-shaped. After that, a septum is formed in the center, and the cell bends into a curved shape and repeats gradual segmentation. After 18 hours, most of the cells change to a uniform short culm shape.
2)細胞分裂様式: Bending type3)
運動性 : なし
4)胞子形成 : なし
5)ダラム染色 : 陽性
陰性
6)抗酸性 ・
26生理的性質
】)嫌気条件下での生育
2)空気中での生育
3)カタラーゼ
4)オキシダーゼ
5)O−Fテスト
ロ)ゼラチンの加水分解
7)リドマス・ミルク
8)硝酸塩の還元
9)メチルレッドテスト
10)VPテスト
11)インドールの生成
12)硫化水素の生成
13)デンプンの加水分解
14)クエン酸の利用
(クリスランセン 培地上)
15)無機窒素源の利用
16)ウレアーゼ
陰性
陽性
陽性
陰性
酸生成せず
陽性
変色なし、
ペプトン化あり
陰性
陰性
陰性
陰性
陰性
陰性
陽性
: 陽性
: 陰性
17)
18)
19)
20)
21)
22)
23)
24)
25)
カゼインの加水分解 :
DNa s eの生産 :
5%塩化ナトリウム中:
での生育
色素の生成
生育温度域
生育pH
7’ween80の分解:
チロシン分解性
各種Ii類からの酸の生成
陽性
陰性
陰性
陰性
10〜37°C
pH5〜10
陽性
陽性
(つづき有)
(つづき有)
O培養後1〜3週間観察
O十:生成能有、±:疑わしい、−:生成能無26)有
機酸の資化性
○培養後1〜3週間観察
O十:資化能有、−:資化能無
3、化学分類学的性状
1)DNA中のCC含量 67%
2)細胞壁のアミノ酸組成
モル比
リジン 1
アラニン 3
スレオニン l
グルタミン酸 1
3)ペプチドグリカン架橋構造
Lys−Ala−Thr−AI
または
Lys−Thr−Alaz
4)細胞壁の糖組成
ラムノース
ガラクトース
5)グリコレート・テスト
アセチル型
6)主要メナキノン
MK 9 (Hz )
4、分類学的考察
○属しベルの同定
本菌株(MCI2496号菌)は、
1発生ル・サイクル(cell cycle)に桿状〜
短棒状(Rods−coccus)の多形性を有する。2) Cell division mode: Bending type 3)
Motility: None 4) Sporulation: None 5) Durham staining: Positive and negative 6) Acid-fast 26 Physiological properties]) Growth under anaerobic conditions 2) Growth in air 3) Catalase 4) Oxidase 5) O -F testro) Hydrolysis of gelatin 7) Lidomus milk 8) Reduction of nitrates 9) Methyl red test 10) VP test 11) Formation of indole 12) Formation of hydrogen sulfide 13) Hydrolysis of starch 14) Utilization of citric acid (On Chris Lansen medium) 15) Utilization of inorganic nitrogen source 16) Negative for urease, positive, positive, negative, no acid formation, positive, no discoloration, peptonization, negative, negative, negative, negative, negative, positive: Positive: Negative 17) 18) 19) 20) 21 ) 22) 23) 24) 25) Hydrolysis of casein: Production of DNase: Growth in 5% sodium chloride: Generation of pigment Growth temperature range Growth pH 7'ween 80 Decomposition: Tyrosine degradable From various types Ii Production of acid Positive, negative, negative, negative, negative 10-37°C pH 5-10 Positive, positive (Continued) (Continued) O Observation for 1-3 weeks after incubation O: Possible to produce, ±: Doubtful, -: Not capable of producing 26) Assimilation of organic acids ○ Observation for 1 to 3 weeks after culture O 10: Assimilation ability, -: Assimilation ability 3, Chemotaxonomic properties 1) CC content in DNA 67% 2) Cell wall Amino acid composition molar ratio Lysine 1 Alanine 3 Threonine L Glutamic acid 1 3) Peptidoglycan cross-linked structure Lys-Ala-Thr-AI or Lys-Thr-Alaz 4) Cell wall sugar composition Rhamnose galactose 5) Glycolate testacetyl type 6) Main menaquinone MK 9 (Hz) 4. Taxonomic considerations ○ Identification of genus This strain (MCI No. 2496) has a rod-shaped to cell cycle.
It has short rod-shaped (Rods-coccus) polymorphism.
2)絶対好気性菌である。2) It is an obligate aerobic bacterium.
3)グルコース等のW類から酸を生成しない。3) No acids are generated from Ws such as glucose.
4)DNA中のCC含量は67%と高いGCを示す。4) CC content in DNA is 67%, showing high GC.
5)細胞壁のジアミノ−アミノ酸はリジンを有する。5) Cell wall diamino-amino acids have lysine.
6)主要メナキノンはMK−9(H,)を有するなどの
特徴を示す。6) Main menaquinone exhibits characteristics such as having MK-9 (H, ).
これらの特徴から、氷量はバージエイズ マニュアル
オブ システマティック バクテリオロジ−(Berg
ey’s Mannual of Systemati
c Bacteri。Based on these characteristics, the amount of ice is
of Systematic Bacteriology (Berg
ey's Manual of Systemati
c Bacteri.
1ogy)第2巻に記載されている、多形性、芽胞非形
成、ダラム染色陽性桿菌(Irregular、 No
nsporing、Gram−Positive Ro
ds)群のアルスロバクタ−(Arthrobacte
r)属菌に帰属することが判明した。Pleomorphic, non-spore-forming, Durham stain-positive bacilli (Irregular, No.
nsporing, Gram-Positive Ro
ds) group of Arthrobacter
r) It was found that it belongs to the genus Bacteria.
0種レベルの同定
アルスロバクタ−属菌には、現在約15種が含まれてい
る。これらの種は、各種の往理学的性質、化学分類学的
性質において識別されているが、特に細胞壁の架橋ペプ
チド構造、糖組成、メナキノン組成の相違が種レベルの
重要な分類基準と見なされている。(K、H,5chl
eiber & 0.Kandler、Bacteri
ol、Rev、Vol、36:407−477.197
2.Bergey’s Mannualof Syst
ematic Bacteriology %1o12
)本菌株(MCI2496号菌)は、
l発生要メナキノンとしてMK 9 CHz )を含
有する。Currently, about 15 species of Arthrobacter genus bacteria are identified at the level of 0 species. These species are distinguished by various physical and chemical taxonomic properties, but differences in the cross-linked peptide structure of the cell wall, sugar composition, and menaquinone composition are considered to be important classification criteria at the species level. There is. (K, H, 5chl
eiber & 0. Kandler, Bacteri
ol, Rev, Vol, 36:407-477.197
2. Bergey's Manual of Syst
ematic Bacteriology %1o12
) This strain (MCI2496) contains MK 9 CHz) as a menaquinone required for generation.
2)細胞壁の架橋ペプチド構造はLys−Ala−Th
r−AlaまたはLys−Thr−Alazである。2) The cross-linked peptide structure of the cell wall is Lys-Ala-Th
r-Ala or Lys-Thr-Alaz.
3)細胞壁の糖としてラムノース、ガラクトースを含有
する。3) Contains rhamnose and galactose as sugars in the cell wall.
4)運動性を示さない
という特徴を持っている。これらの性状と、Berge
y’s Mannual of Systematic
Bacteriology第2巻及び、M、Take
uchi & A、Yokota、J、Gen、App
l、旧crobio1.vo1.35:233−252
.1989に記載されているアルスロバクタ−属の種の
特徴と比較した結果、本菌株はアルスロバクタ−・アラ
レセンス(Arth−robacter auresc
ens)に近縁な種であることが示唆された。しかし、
有機酸の資化性、デンプンの加水分解等の生理的性質に
違いが見られた。正式な種の帰属は、今後アルスロバク
タ−・アラレセンスあるいは類似種と氷量との核酸レベ
ルでの比較をした上で決定することとする。従って現段
階では本菌株(MCI2496号菌)をアル発生バクタ
−・エスピーと同定した。4) It has the characteristic of not exhibiting motility. These properties and Berge
y's Manual of Systematic
Bacteriology Volume 2 and M. Take
uchi & A., Yokota, J., Gen., App.
l, old crobio1. vo1.35:233-252
.. As a result of comparison with the characteristics of species of the genus Arthlobacter described in 1989, this strain was found to be similar to Arth-robacter auresc.
It was suggested that it is a species closely related to S. ens). but,
Differences were observed in physiological properties such as organic acid assimilation and starch hydrolysis. The official species assignment will be determined after comparing Arthrobacter ararecens or similar species with the amount of ice at the nucleic acid level. Therefore, at this stage, this bacterial strain (MCI No. 2496) was identified as Bacterium sp.
さらに、DFAII[生産菌として公知であるアルスロ
バクタ−・グロビフォルミス(Arthrobacte
rIobiformis)及びアルスロバクタ−・ウレ
アファシェンス(Arthrobacter urea
faciens)の菌学的性状と本菌株を対比したとこ
ろ、下記表に示すように架橋ペプチドの構造及び細胞壁
の糖組成などの主要な点において明らかに区別された。Furthermore, DFAII [Arthrobacter globiformis, which is known as a producing bacterium]
rIobiformis) and Arthrobacter ureafaciens (Arthrobacter urea
When we compared the mycological properties of C. faciens) with this strain, they were clearly differentiated in major points such as the structure of the crosslinked peptide and the sugar composition of the cell wall, as shown in the table below.
本発明においては、前記の菌を通常の微生物が利用しう
る栄養物を含有する培地で培養することにより容易に増
殖させることができる。栄養源としては、グルコース、
水あめ、デキストリン、シュクロース、澱粉、糖蜜、動
・植物油等を使用できる。また窒素源として、大豆粉、
小麦胚芽、コーンステイープリカー、綿実粕、肉エキス
、ペプトン、酵母エキス、硫酸アンモニウム、硝酸ソー
ダ、尿素等を使用できる。その他、必要に応し、ナトリ
ウム、カリウム、カルシウム、マグネシウム、コバルト
、塩素、燐酸、硫酸及びその他のイオンを生成すること
のできる無機塩類を添加することは有効である。In the present invention, the above bacteria can be easily grown by culturing them in a medium containing nutrients that can be used by ordinary microorganisms. As a nutritional source, glucose,
Starch syrup, dextrin, sucrose, starch, molasses, animal/vegetable oils, etc. can be used. In addition, soybean flour,
Wheat germ, cornstarch liquor, cottonseed meal, meat extract, peptone, yeast extract, ammonium sulfate, sodium nitrate, urea, etc. can be used. In addition, it is effective to add, if necessary, inorganic salts capable of producing sodium, potassium, calcium, magnesium, cobalt, chlorine, phosphoric acid, sulfuric acid, and other ions.
本発明においては、イヌリン或いはキクイモ、ゴボウ等
のイヌリン含有量の高い植物の抽出液を唯一の炭素源と
し、で含む溶液中で、上記アルスロバクター・エスピー
(MCI2496)微工研菌寄第11288号(FER
MP−11288)由来のイヌリン分解酵素を作用させ
る。その際、該細菌そのものを作用させてもよいし、ま
た、該細菌から該酵素を抽出し、それを作用させてもよ
い。In the present invention, inulin or extracts of plants with high inulin content such as Jerusalem artichoke and burdock are used as the sole carbon source, and in a solution containing the above-mentioned Arthrobacter sp. No. (FER
Inulin-degrading enzyme derived from MP-11288) is activated. At this time, the bacteria themselves may be used to act on the enzyme, or the enzyme may be extracted from the bacteria and used to act on the enzyme.
細菌そのものを作用させる場合、炭素源としてのイヌリ
ンを約1〜10%含有し、その他、例えば窒素源として
、大豆粉、小麦胚芽、コーンステイー7’ IJカー、
綿実粕、肉エキス、ペプトン、酵母エキス、硫酸アンモ
ニウム、硝酸ソーダ、尿素等、更に必要に応じ、ナトリ
ウム、カリウム、カルシウム、マグネシウム、コバルト
、塩素、燐酸、硫酸及びその他のイオンを生成すること
のできる無機塩類等を添加した培地に本国を接種し振と
う培養を行う。この際培養温度は20〜37°Cが、ま
た培養時間は12〜40時間が好適である。得られた培
養液を遠心分離により除菌し、その上清を加熱処理によ
り酵素を失活させる。そして濃縮を行い、例えばこれを
活性炭カラムクロマトグラフィーにより活性炭カラムに
吸着させる。蒸留水でフルクトースを溶出させたあと、
5%エタノール水溶液にて溶出を行う。この分画中にD
FAmが得られるので、それを濃縮乾固すると所期のD
FA[rを得ることができる。When the bacteria themselves are used, it contains about 1 to 10% inulin as a carbon source, and other nitrogen sources such as soybean flour, wheat germ, cornstay 7' IJ car,
Cottonseed meal, meat extract, peptone, yeast extract, ammonium sulfate, sodium nitrate, urea, etc. In addition, sodium, potassium, calcium, magnesium, cobalt, chlorine, phosphoric acid, sulfuric acid and other ions can be generated as required. Inoculate the native culture into a medium supplemented with inorganic salts, etc., and perform shaking culture. In this case, the culture temperature is preferably 20 to 37°C, and the culture time is preferably 12 to 40 hours. The resulting culture solution is sterilized by centrifugation, and the supernatant is heated to deactivate the enzyme. Then, it is concentrated and adsorbed onto an activated carbon column by, for example, activated carbon column chromatography. After eluting fructose with distilled water,
Elution is performed with a 5% ethanol aqueous solution. In this fraction, D
Since FAm is obtained, the desired D is obtained by concentrating it to dryness.
FA[r can be obtained.
また酵素を作用させる場合、まず前記方法により培養を
行った培養液を遠心分離により除菌し、得られたろ液に
硫安(65%飽和)を加え塩析を行い、析出した沈澱物
を遠心分離により取得し、少量の水に懸濁させたのち透
析を行い、粗酵素液を得る。この粗酵素液を例えばpH
7,0に調整した0、01〜0.1Mのリン酸緩衝液中
でイヌリンに作用させることによっても所期のDFAI
IIが得られる。In addition, when applying an enzyme, first, the culture solution cultured by the above method is sterilized by centrifugation, ammonium sulfate (65% saturation) is added to the obtained filtrate, salting out is performed, and the precipitated precipitate is centrifuged. After suspending in a small amount of water, dialysis is performed to obtain a crude enzyme solution. This crude enzyme solution is adjusted to pH
The desired DFAI can also be obtained by acting on inulin in a 0.01-0.1M phosphate buffer adjusted to 7.0.
II is obtained.
本粗酵素液は、例えばD E A E −Toyope
arl650 M、 S P−Toyopearl
650 Mカラム(東ソー製)によるイオン交換クロ
マトグラフィーにて精製を行うことにより、電気泳動的
に単一のバンドを示す酵素標品を得ることができる。本
酵素標品の至適pHは5.0で、また60゛Cで最大活
性を示した。pHは4.5〜11.0の広範囲で安定で
あり20分間の熱処理では60°Cまで安定であり高い
温度安定性を示した。This crude enzyme solution can be obtained from, for example, DEA E-Toyope.
arl650 M, S P-Toyopearl
By performing purification by ion exchange chromatography using a 650 M column (manufactured by Tosoh), an enzyme preparation that shows a single band electrophoretically can be obtained. The optimum pH of this enzyme preparation was 5.0, and maximum activity was exhibited at 60°C. The pH was stable over a wide range of 4.5 to 11.0, and after heat treatment for 20 minutes, it was stable up to 60°C, indicating high temperature stability.
以下に実施例をあげて本発明の方法をさらに具体的に説
明するが、その要旨を越えない限りこれらに限定される
ものではない。The method of the present invention will be explained in more detail with reference to Examples below, but the invention is not limited thereto unless it exceeds the gist thereof.
実施例1
市販イヌリン5%、酵母エキス0.02%、硝酸ナトリ
ウム0.2%、硫酸マグネシウム0.05%、塩化カリ
ウム0.05%、リン酸−カリウム0.05%、塩化第
二鉄0.001%を含んだ培地150s+2をpH1,
0に調整して、120°Cで20分間蒸気滅菌した。こ
の滅菌した溶液に、MCI2496号菌を一白金発撥種
し、160r、p、vx、で30°C130時間培養し
た。Example 1 Commercially available inulin 5%, yeast extract 0.02%, sodium nitrate 0.2%, magnesium sulfate 0.05%, potassium chloride 0.05%, potassium phosphate 0.05%, ferric chloride 0 Medium 150s+2 containing .001% pH 1,
0 and steam sterilized at 120°C for 20 minutes. Into this sterilized solution, MCI No. 2496 was inoculated with a platinum blast and cultured at 160r, p, vx at 30°C for 130 hours.
培養終了後遠心分離により菌体を除去し、培養ろ液を得
た。得られた培養ろ液を10分間加熱処理することによ
り酵素を失活させ、約10腸!にまで減圧濃縮した。こ
の液は活性炭カラム(活性炭30gとセライトNα53
5 60gの混合物を蒸留水にて充てん)に吸着させ、
蒸留水12を流したのち、5%エタノール水溶液で溶出
した。After completion of the culture, the bacterial cells were removed by centrifugation to obtain a culture filtrate. The obtained culture filtrate is heated for 10 minutes to inactivate the enzyme, resulting in approximately 10 intestines! It was concentrated under reduced pressure to . This solution was prepared using an activated carbon column (30 g of activated carbon and Celite Nα53).
5 60g of the mixture is adsorbed in (filled with distilled water),
After flowing distilled water 12 times, elution was carried out with a 5% ethanol aqueous solution.
溶出ピークを集めて減圧濃縮にて乾固してDFAmを得
た。得られたDFAIIIは、原料イヌリンに対して1
0%であった。薄層クロマトグラフィー〔シリカゲルプ
レート(Merck社);展開溶媒n−ブタノール:エ
タノール:水=2 : 1 : 1(V/V/V))に
よると、イヌリンの酸分解にヨリ得うレタ標準(7)D
FAII[とRf値(0,67)が一致した。The eluted peaks were collected and concentrated to dryness under reduced pressure to obtain DFAm. The obtained DFAIII was 1% relative to the raw material inulin.
It was 0%. According to thin layer chromatography [silica gel plate (Merck); developing solvent n-butanol: ethanol: water = 2: 1: 1 (V/V/V)], the standard (7 )D
FAII[ and Rf value (0,67) matched.
実施例2
実施例1で得られた培養ろ液1 rml!を、5%のイ
ヌリンを含む0.05Mリン酸緩衝液4 mlに加えて
30℃で3時間反応させた。Example 2 Culture filtrate 1 rml obtained in Example 1! was added to 4 ml of 0.05M phosphate buffer containing 5% inulin and reacted at 30°C for 3 hours.
反応液を加熱し酵素を失活させた後、活性炭カラムクロ
マトグラフィーを行い、5%エタノールにて溶出させ、
溶出液を減圧濃縮にて乾固してDFAIIIを得た。After heating the reaction solution to inactivate the enzyme, activated carbon column chromatography was performed and eluted with 5% ethanol.
The eluate was concentrated to dryness under reduced pressure to obtain DFAIII.
得られたDFAII[は、原料イヌリンに対して83.
4%であった。The obtained DFAII [was 83% with respect to the raw material inulin.
It was 4%.
〔発明の効果]
本発明のアルスロバクター・エスピー(MCI2496
)微工研菌寄第11288号(FERMP−11288
)由来のイヌリン分解酵素は、良好にイヌリンからDF
AI[[を生産し、また従来のものに比べて熱に対して
高い安定性を有するので、DFAIIIの連続生産を行
わせる際に非常に有効であると考えられる。[Effect of the invention] Arthrobacter sp. of the present invention (MCI2496
) FERMP-11288
) derived inulin-degrading enzyme can be successfully converted from inulin to DF.
Since it produces AI[[ and has higher stability against heat than conventional products, it is considered to be very effective in continuous production of DFAIII.
Claims (1)
ー・エスピー(MCI2496)微工研菌寄第1128
8号(FERMP−11288)由来のイヌリン分解酵
素と反応させることを特徴とするジフルクトース・ジア
ンヒドリドIIIの製造法。(1) Inulin was added to Arthrobacter sp. (MCI2496) in an inulin-containing solution.
A method for producing difructose dianhydride III, which comprises reacting with inulin degrading enzyme derived from No. 8 (FERMP-11288).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2059699A JPH03259090A (en) | 1990-03-09 | 1990-03-09 | Production of difructose dianhydride iii |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2059699A JPH03259090A (en) | 1990-03-09 | 1990-03-09 | Production of difructose dianhydride iii |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03259090A true JPH03259090A (en) | 1991-11-19 |
Family
ID=13120722
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2059699A Pending JPH03259090A (en) | 1990-03-09 | 1990-03-09 | Production of difructose dianhydride iii |
Country Status (1)
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JP (1) | JPH03259090A (en) |
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---|---|---|---|---|
WO2004078989A1 (en) * | 2003-03-05 | 2004-09-16 | Nippon Beet Sugar Mfg. Co., Ltd. | Process for purifying difructose-dianhydride iii |
JP2005132774A (en) * | 2003-10-30 | 2005-05-26 | Nippon Beet Sugar Mfg Co Ltd | Method for purifying difructose dianhydride iii |
JP2006223283A (en) * | 2005-02-17 | 2006-08-31 | Mitsui Norin Co Ltd | Composition comprising cyclic inulooligosaccharide and difructose dianhydride |
JP2011147455A (en) * | 2011-04-15 | 2011-08-04 | Nippon Beet Sugar Mfg Co Ltd | Method for producing difructose anhydride iii crystalline particle |
US8039615B2 (en) | 2004-12-28 | 2011-10-18 | Nippon Beet Sugar Manufacturing Co., Ltd. | Process for producing difructose dianhydride III crystals |
-
1990
- 1990-03-09 JP JP2059699A patent/JPH03259090A/en active Pending
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JP4572167B2 (en) * | 2003-03-05 | 2010-10-27 | 日本甜菜製糖株式会社 | Method for purifying difructose dianhydride III |
US7998710B2 (en) | 2003-03-05 | 2011-08-16 | Nippon Beet Sugar Mfg., Co., Ltd. | Process for purifying difructose dianhydride III |
EP1612274A1 (en) * | 2003-03-05 | 2006-01-04 | Nippon Beet Sugar Mfg. Co., Ltd. | Process for purifying difructose-dianhydride iii |
JPWO2004078989A1 (en) * | 2003-03-05 | 2006-06-08 | 日本甜菜製糖株式会社 | Method for purifying difructose dianhydride III |
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JP2010233576A (en) * | 2003-03-05 | 2010-10-21 | Nippon Beet Sugar Mfg Co Ltd | Process for purifying difructose dianhydride iii crystal |
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EP1612274A4 (en) * | 2003-03-05 | 2011-05-11 | Nippon Beet Sugar Mfg | Process for purifying difructose-dianhydride iii |
WO2004078989A1 (en) * | 2003-03-05 | 2004-09-16 | Nippon Beet Sugar Mfg. Co., Ltd. | Process for purifying difructose-dianhydride iii |
JP4617077B2 (en) * | 2003-10-30 | 2011-01-19 | 日本甜菜製糖株式会社 | Method for purifying difructose dianhydride III |
JP2005132774A (en) * | 2003-10-30 | 2005-05-26 | Nippon Beet Sugar Mfg Co Ltd | Method for purifying difructose dianhydride iii |
US8039615B2 (en) | 2004-12-28 | 2011-10-18 | Nippon Beet Sugar Manufacturing Co., Ltd. | Process for producing difructose dianhydride III crystals |
US8304534B2 (en) | 2004-12-28 | 2012-11-06 | Nippon Beet Sugar Manufacturing Co., Ltd. | Process for producing difructose dianhydride III crystals |
JP2006223283A (en) * | 2005-02-17 | 2006-08-31 | Mitsui Norin Co Ltd | Composition comprising cyclic inulooligosaccharide and difructose dianhydride |
JP2011147455A (en) * | 2011-04-15 | 2011-08-04 | Nippon Beet Sugar Mfg Co Ltd | Method for producing difructose anhydride iii crystalline particle |
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