JPH0579312B2 - - Google Patents
Info
- Publication number
- JPH0579312B2 JPH0579312B2 JP61085695A JP8569586A JPH0579312B2 JP H0579312 B2 JPH0579312 B2 JP H0579312B2 JP 61085695 A JP61085695 A JP 61085695A JP 8569586 A JP8569586 A JP 8569586A JP H0579312 B2 JPH0579312 B2 JP H0579312B2
- Authority
- JP
- Japan
- Prior art keywords
- mannitol
- culture
- sugar
- culture solution
- producing
- 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 - Fee Related
Links
- FBPFZTCFMRRESA-KVTDHHQDSA-N D-Mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-KVTDHHQDSA-N 0.000 claims description 55
- 229930195725 Mannitol Natural products 0.000 claims description 54
- 239000000594 mannitol Substances 0.000 claims description 54
- 235000010355 mannitol Nutrition 0.000 claims description 54
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims description 24
- 238000004519 manufacturing process Methods 0.000 claims description 20
- 235000000346 sugar Nutrition 0.000 claims description 20
- 241000894006 Bacteria Species 0.000 claims description 15
- 239000004310 lactic acid Substances 0.000 claims description 12
- 235000014655 lactic acid Nutrition 0.000 claims description 12
- KWIUHFFTVRNATP-UHFFFAOYSA-N Betaine Natural products C[N+](C)(C)CC([O-])=O KWIUHFFTVRNATP-UHFFFAOYSA-N 0.000 claims description 6
- KWIUHFFTVRNATP-UHFFFAOYSA-O N,N,N-trimethylglycinium Chemical compound C[N+](C)(C)CC(O)=O KWIUHFFTVRNATP-UHFFFAOYSA-O 0.000 claims description 6
- 229960003237 betaine Drugs 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 5
- 241000186660 Lactobacillus Species 0.000 claims description 3
- 229940039696 lactobacillus Drugs 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 2
- 239000003513 alkali Substances 0.000 claims description 2
- 238000012258 culturing Methods 0.000 claims description 2
- 229930091371 Fructose Natural products 0.000 description 10
- 239000005715 Fructose Substances 0.000 description 10
- 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 10
- 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 10
- 238000000855 fermentation Methods 0.000 description 10
- 230000004151 fermentation Effects 0.000 description 10
- 239000008103 glucose Substances 0.000 description 10
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- 239000000758 substrate Substances 0.000 description 8
- 239000002609 medium Substances 0.000 description 6
- 241000192130 Leuconostoc mesenteroides Species 0.000 description 5
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 5
- 240000001929 Lactobacillus brevis Species 0.000 description 4
- 235000013957 Lactobacillus brevis Nutrition 0.000 description 4
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 4
- 241000222120 Candida <Saccharomycetales> Species 0.000 description 3
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229930006000 Sucrose Natural products 0.000 description 3
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 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
- 230000000694 effects Effects 0.000 description 3
- 239000013028 medium composition Substances 0.000 description 3
- 238000004904 shortening Methods 0.000 description 3
- 239000000600 sorbitol Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000005720 sucrose Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 241000228212 Aspergillus Species 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 241001468194 Leuconostoc mesenteroides subsp. dextranicum Species 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000005515 coenzyme Substances 0.000 description 2
- 238000006911 enzymatic reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000001963 growth medium Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 235000013379 molasses Nutrition 0.000 description 2
- 238000010979 pH adjustment Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 241000235349 Ascomycota Species 0.000 description 1
- 235000016068 Berberis vulgaris Nutrition 0.000 description 1
- 241000335053 Beta vulgaris Species 0.000 description 1
- 241001337994 Cryptococcus <scale insect> Species 0.000 description 1
- FBPFZTCFMRRESA-JGWLITMVSA-N D-glucitol Chemical compound OC[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO FBPFZTCFMRRESA-JGWLITMVSA-N 0.000 description 1
- 108010050375 Glucose 1-Dehydrogenase Proteins 0.000 description 1
- 108020000290 Mannitol dehydrogenase Proteins 0.000 description 1
- 241000228143 Penicillium Species 0.000 description 1
- 241000235070 Saccharomyces Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 230000000181 anti-adherent effect Effects 0.000 description 1
- 230000036772 blood pressure Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- -1 cane molasses Natural products 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000012531 culture fluid Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 230000000378 dietary effect Effects 0.000 description 1
- 239000002934 diuretic Substances 0.000 description 1
- 230000001882 diuretic effect Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000002255 enzymatic effect Effects 0.000 description 1
- 235000003599 food sweetener Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229960004903 invert sugar Drugs 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 235000011118 potassium hydroxide Nutrition 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 150000005846 sugar alcohols Chemical class 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 239000003765 sweetening agent Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Description
〔産業上の利用分野〕
本発明は乳酸菌を用いて、醗酵法により糖類か
らのマンニトールの製造法に関する。
本発明にて製造されるマンニトールは、食品や
医薬品において有用な物質である。即ち、食品分
野においては、マンニトールの有する吸湿性の少
ない性質を利用した粘着防止剤、医薬品分野にお
いては、利尿剤、血圧降下剤等として利用されて
いる。さらにマンニトールはグルコースの60%の
甘味を有し、ダイエツト甘味料としての利用も期
待される。
〔従来の技術〕
現在のマンニトールの生産方法としては以下の
3つの方法が報告されている。
(1) 合成法
マンニトールの工業的生産方法は、現在、シ
ヨ糖を高圧下で電気的、あるいは化学的に還元
することによつて生産されている。しかし、こ
の方法では構造異性体であるソルビトールが生
成し、しかもソルビトールとマンニトールの生
成比は65%対35%と平衡がソルビトールに片よ
つている。このため生成したマンニトールを得
るためにはイオン交換樹脂によつて分離、精製
しなければならず経済的には不利と考えられ
る。
(2) 醗酵法
微生物を用いてマンニトールを生産する方法
は19世紀以来数多く報告されている。
乳酸菌
マンニトールを生産する乳酸菌としては、
ラクトバチルスブレビス(lactobacillus
brevis)、ロイコノストツメセンテロイデス
(leuconostocmesente roides)、ラクトバチ
ルスフアーメンタム(lactobacillus
fermentem)、ロイコノストツクデキストラ
ンカム(leuconostoc dextranicum)等のヘ
テロ醗酵型の乳酸菌が知られている。
グルコースとフラクトースを基質として、
濃度をそれぞれ1:2の割合でまぜて上記に
示した菌を接種すると、フラクトースが高収
率でマンニトールになることが知られてい
る。しかし、これは初発な糖濃度が低い時だ
けであつて、その生産量は低い。それを解決
するために、初発の糖濃度を10%以上にし、
マンニトールの生産を行なつた報告がある
が、(Zeitschriftfu¨r Allg.Mikrobiologie、
6.4.(1966)323−328)培養液中に糖が高濃
度残つているにもかかわらず、マンニトール
の生成は途中で止まつてしまう。つまり高収
率、高蓄積のマンニトールの生産は不可能で
あつた。
酵母
マンニトールを生産する酵母としては、サ
ツカロマイセスサケ(Saccharomyces
Seke;4.15g、J.Ferment.Technol 16;
597−598(1937))トルロプシス
(Torulopsis・species;0.5〜2.2g/dl
Applied Microbiol.161841−1852(1968))、
クリプトコツカスネオフオルミス
(Cryptococcus neoformis;0.13g/dl;
Torulopsis属と同じ)、耐糖性酵母(グリセ
ルールとあわせて65%の対糖収率;1984年醗
酵工学会講演要旨、p168)等で報告されて
いる。しかし、今まで報告されている酵母に
よるマンニトール生産は収率が30%以下と低
く、マンニトール以外の糖アルコールが副生
するという欠点がある。
かび
マンニトールを生産するかびとしては、アス
ペルギウス(Aspergillus)属、ペニシリウム
(Penicillium)属等の子のう菌類で報告されて
いる。その中で、アスペルギウスキヤンデイダ
ス(Aspergillus candidas)で8.4g、50%と
いう高生産株が見い出されているが
(Biotechnol Bioengineer、9 365−374
(1967))培養時間が12日間と長く経済的に不利
である。
(3) 酵素法
フラクトースを基質とし、マンニトール脱水
素酵素を作用させてマンニトールを生産する方
法も知られている。乳酸菌、酵母、かび、酢酸
菌等からこの酵素はすでに精製されている。弱
酸性から中性付近にかけて(PH4〜7)、これ
らの精製酵素はマンニトール生成の至適PHを持
つているが、醗酵によるマンニトール生産の至
適PHに関しては不明である。酵素法によるマン
ニトール生産では高価な補酵素が必要である。
しかも酵素によるマンニトール生産反応ではこ
の補酵素が還元型から酸化型にかわるので、酸
化型を還元型へ再成するシステムが必要となつ
てくる。再生システムとしてグルコース脱水素
酵素を使う方法も報告されているが、まだ数m
M程度の基質濃度であり実用的ではない。
〔本発明が解決しようとする問題点〕
上記の(2)、で示したように、乳酸菌によるマ
ンニトール醗酵の場合、生産性向上のために培養
開始時に炭素源としての糖を10%以上にした時、
マンニトールの生成は培養途中でとまり、培養液
中に糖が残存する。このためマンニトールの高収
率、高生産性は望めない。また、培養日数も4日
間と長い。
本研究は、これらの問題を解決し、短時間で高
収率、高生産のマンニトールを製造することを目
的とする。
<発明の構成>
〔問題点を解決するための手段〕
本発明者らは上述の事情を鑑み、培養液中に10
%以上の濃度の糖が存在する時の乳酸菌によるマ
ンニトールの醗酵時間を短縮せしめ、残糖を減少
あるいは消失させることを目的として種々の培養
条件を検討した結果、乳酸菌を用いて培養開始時
からPHを5.0からPH6.0の範囲に保つことによりマ
ンニトールの生産性が高められ、残糖がほぼ消失
することを、また、この時ベタインを培養液中に
添加することによりマンニトールの醗酵時間が短
縮されることを発見し、本発明を完成した。すな
わち本発明は、乳酸菌を用いるマンニトールの醗
酵生産において基質である糖の初発濃度が低い
時、基質は消失するがマンニトールの生産量は低
く、また生産量を増やすために、初発の基質濃度
を上げることによつておこるマンニトールの醗酵
の停止という問題を解決する目的で、培養液中の
基質である糖濃度が10%以上存在する時に、培養
中のPHを5以下に下がらないようにするが、PH6
以上になつた場合PHを6.0以下にPHコントロール
することによつて、すなわち5から6に保つこと
により、マンニトールの生産性を高め、培養液中
に残る糖を減少あるいは消失させ、その上培養中
にベタインを加えることによつてマンニトール醗
酵時間を短縮せしめることを特徴とするマンニト
ール製造法に関するものである。
本発明において用いる微生物としては、乳酸菌
に属するマンニトール生産菌であれば種や菌株を
問わず使用することができるが、好適な例として
は、ラクトバチルスブレビス(lactobacillus
brevis、IFO 3960、3345)、ロイコノストツクメ
センテロイデス(Leuconostoc mesenteroides
IFO 3426)等があげられる。
本発明における培養は静置あるいはゆるい撹拌
もしくはゆるい振とうで行なわれるか、静置で空
気を送り込む条件下で行なえば良く、温度は15℃
ないし40℃好ましくは25℃から37℃であり、培養
時間は18時間ないし144時間、好ましくは36時間
から96時間の間である。左記の条件は使用菌と倍
地により適宜至適な条件を選べば良い。
炭素源としてはグルコース、フラクトース、シ
ヨ糖をそれぞれ単独に用いた場合、あるいはフラ
クトースとグルコースを混合したもので、その比
はフラクトース2に対してグルコース1の条件が
もつともよい。またフラクトース及びグルコース
含有物としては、シヨ糖の転化糖、グルコースの
異性化糖を天然の物としてはケーンモラセス、ビ
ートモラセス等及びその分解物質等をあげること
ができる。
本発明においては培養液中の初発PHはどうでも
よく、培養液中のPHを5.0から6.0の範囲に調整す
るPHコントロールを行ない、培養液がPH5.0以下
になつた時、PH調節のために苛性カリ、苛性ソー
ダ、アンモニア水、アンモニア等のアルカリでPH
を5.0以上に調整する。培養液がPH6.0以上になつ
た場合は適宜、硫酸、塩酸、リン酸等の鉱酸ある
いはクエン酸、酢酸等の有機酸を加えてPHを6.0
以下に調整する
マンニトールの製造時間を短縮する効果をもつ
ベタインの量は0.05%から5%、好ましくは0.1
から0.5%が良い。
本発明の方法を実施すれば、最初に培地中に添
加したフラクトースが90%以上の収率でマンニト
ールに変換するが、例としてラクトバチルス、ブ
レビスを用いた場合、グルコース5g/dl、フラ
クトース10g/dlを含む培養液から収率65%、約
9.5g/dl相当のマンニトールが40時間で蓄積し
た。
またロイコノストツクメセンテロイデスを用い
た場合、グルコース10g/dl、フラクトース20
g/dlを含む培養液から収率63%約19g/dl相当
のマンニトールが72時間で蓄積し、さらに0.1%
のベタインをあらかじめ添加しておくと、培養時
間が60時間に短縮できる。かくして得られた培養
液からマンニトールを分別、採集するには公知の
方法が使用出来る。
マンニトール醗酵における残存グルコース、フ
ラクトース、生成物であるマンニトール、乳酸、
酢酸はすべて高速液体クロマトグラフイーによつ
て定量した。
以下、実施例により本発明を更に具体的に説明
するが、これより本発明が限定されるものではな
い。
実施例 1
[Industrial Application Field] The present invention relates to a method for producing mannitol from sugars by fermentation using lactic acid bacteria. Mannitol produced by the present invention is a substance useful in foods and medicines. That is, in the food field, mannitol is used as an anti-adhesive agent that takes advantage of its low hygroscopic properties, and in the pharmaceutical field, it is used as a diuretic, a blood pressure lowering agent, etc. Furthermore, mannitol has 60% the sweetness of glucose and is expected to be used as a dietary sweetener. [Prior Art] The following three methods have been reported as current methods for producing mannitol. (1) Synthesis method Currently, mannitol is produced industrially by electrically or chemically reducing sucrose under high pressure. However, this method produces sorbitol, which is a structural isomer, and the production ratio of sorbitol and mannitol is 65% to 35%, so the equilibrium is tilted toward sorbitol. Therefore, in order to obtain the produced mannitol, it must be separated and purified using an ion exchange resin, which is considered to be economically disadvantageous. (2) Fermentation method Many methods for producing mannitol using microorganisms have been reported since the 19th century. Lactic acid bacteria The lactic acid bacteria that produce mannitol are
Lactobacillus brevis (lactobacillus)
brevis), leuconostocmesente roides, lactobacillus famentum
Heterofermentative lactic acid bacteria such as leuconostoc dextranicum and leuconostoc dextranicum are known. With glucose and fructose as substrates,
It is known that when the above bacteria are inoculated at a ratio of 1:2, fructose can be converted to mannitol at a high yield. However, this occurs only when the initial sugar concentration is low, and the production amount is low. To solve this problem, increase the initial sugar concentration to 10% or more,
There are reports of mannitol production (Zeitschriftfu¨r Allg.Mikrobiologie,
6.4. (1966) 323-328) Despite the high concentration of sugar remaining in the culture solution, the production of mannitol stops midway. In other words, it was impossible to produce mannitol with high yield and high accumulation. Yeast The yeast that produces mannitol is Saccharomyces.
Seke; 4.15g, J.Ferment.Technol 16 ;
597-598 (1937)) Torulopsis species; 0.5-2.2 g/dl
Applied Microbiol. 16 1841−1852 (1968)),
Cryptococcus neoformis; 0.13g/dl;
(same as the genus Torulopsis), sugar-tolerant yeast (65% sugar yield including glycerol; Abstracts of the 1984 Fermentation Engineering Society Conference, p. 168), etc. However, mannitol production by yeast that has been reported so far has a low yield of less than 30%, and has the disadvantage that sugar alcohols other than mannitol are produced as by-products. Molds Mannitol-producing molds have been reported to include ascomycetes such as Aspergillus and Penicillium. Among them, a high-producing strain of Aspergillus candidas (8.4 g, 50%) was found (Biotechnol Bioengineer, 9 365-374
(1967)) It takes a long culture time of 12 days, which is economically disadvantageous. (3) Enzymatic method A method is also known in which mannitol is produced by using fructose as a substrate and allowing mannitol dehydrogenase to act. This enzyme has already been purified from lactic acid bacteria, yeast, mold, acetic acid bacteria, etc. These purified enzymes have an optimum pH for mannitol production, ranging from weak acidity to near neutrality (PH4 to 7), but the optimum pH for mannitol production by fermentation is unknown. Mannitol production by enzymatic methods requires expensive coenzymes.
Moreover, in the enzymatic mannitol production reaction, this coenzyme changes from a reduced form to an oxidized form, so a system is required to regenerate the oxidized form into the reduced form. A method using glucose dehydrogenase as a regeneration system has also been reported, but it is still a few meters long.
The substrate concentration is about M, which is not practical. [Problems to be solved by the present invention] As shown in (2) above, in the case of mannitol fermentation using lactic acid bacteria, sugar as a carbon source is increased to 10% or more at the start of culture in order to improve productivity. Time,
Production of mannitol stops during the culture, and sugar remains in the culture solution. For this reason, high yield and high productivity of mannitol cannot be expected. In addition, the culture period is as long as 4 days. The purpose of this research is to solve these problems and produce mannitol with high yield and production in a short time. <Structure of the invention> [Means for solving the problem] In view of the above-mentioned circumstances, the present inventors have prepared
As a result of investigating various culture conditions with the aim of shortening the fermentation time of mannitol by lactic acid bacteria and reducing or eliminating residual sugar when sugar is present at a concentration of By keeping the pH within the range of 5.0 to 6.0, mannitol productivity is increased and residual sugar almost disappears.Also, by adding betaine to the culture medium at this time, the mannitol fermentation time is shortened. They discovered this and completed the present invention. That is, in the fermentation production of mannitol using lactic acid bacteria, the present invention proposes that when the initial concentration of sugar, which is a substrate, is low, the substrate disappears but the production amount of mannitol is low, and in order to increase the production amount, the initial substrate concentration is increased. In order to solve the problem of stopping the fermentation of mannitol, which may occur in some cases, when the substrate sugar concentration in the culture solution is 10% or more, the pH during the culture should not fall below 5. PH6
If the pH exceeds 6.0, by controlling the pH to 5 to 6, the productivity of mannitol can be increased, the sugar remaining in the culture solution can be reduced or eliminated, and in addition, during the culture The present invention relates to a method for producing mannitol, which is characterized by shortening the mannitol fermentation time by adding betaine to the mannitol. As the microorganism used in the present invention, any species or strain of mannitol-producing bacteria belonging to lactic acid bacteria can be used, but a preferred example is Lactobacillus brevis.
brevis, IFO 3960, 3345), Leuconostoc mesenteroides
IFO 3426) etc. The culture in the present invention may be carried out by standing still, with gentle stirring or shaking, or by standing still and introducing air, and the temperature is 15°C.
to 40°C, preferably 25°C to 37°C, and the culture time is 18 to 144 hours, preferably 36 to 96 hours. The conditions listed on the left can be selected as appropriate depending on the bacteria and medium used. As the carbon source, glucose, fructose, and sucrose may be used alone, or a mixture of fructose and glucose may be used, and the ratio may be 2 parts fructose to 1 part glucose. Examples of fructose- and glucose-containing substances include invert sugar of sucrose, isomerized sugar of glucose, and natural products such as cane molasses, beet molasses, and their decomposed substances. In the present invention, the initial PH in the culture solution is not a concern; PH control is performed to adjust the PH in the culture solution to a range of 5.0 to 6.0, and when the pH of the culture solution falls below 5.0, the pH adjustment PH with alkali such as caustic potash, caustic soda, ammonia water, ammonia, etc.
Adjust to 5.0 or higher. If the culture solution reaches a pH of 6.0 or higher, add mineral acids such as sulfuric acid, hydrochloric acid, phosphoric acid, or organic acids such as citric acid or acetic acid to bring the pH to 6.0.
Adjust the amount of betaine, which has the effect of shortening the production time of mannitol, from 0.05% to 5%, preferably 0.1
0.5% is good. When the method of the present invention is carried out, the fructose initially added to the medium is converted to mannitol with a yield of 90% or more. Yield 65% from culture medium containing dl, approx.
Mannitol equivalent to 9.5 g/dl accumulated in 40 hours. In addition, when using Leuconostocmesenteroides, glucose 10g/dl, fructose 20g/dl
Mannitol equivalent to approximately 19 g/dl accumulates in 72 hours with a yield of 63% from a culture solution containing g/dl, and an additional 0.1%
By adding betaine in advance, the culture time can be shortened to 60 hours. Known methods can be used to separate and collect mannitol from the culture fluid thus obtained. Residual glucose, fructose, product mannitol, lactic acid,
All acetic acid was determined by high performance liquid chromatography. EXAMPLES Hereinafter, the present invention will be explained in more detail with reference to Examples, but the present invention is not limited thereto. Example 1
【表】
第1表に示す培地組成(1)の培地5mlを試験管に
入れ、120℃にて、20分間加熱した。この培地に
ラクトバチルスブレビス(IFO 3960)を1白金
耳接種し、30℃の温度で18時間静置培養を行ない
前培養とした。
第1表に示す培地組成(2)の培地50mlを100ml容
の三ツ口のガラス容器に入れ、120℃にて20分間
加熱した。これを上記で示した前培養液を0.5ml
加え、さらに5日間、30℃にて60〜100rpmの撹
拌をともなう微好気的条件下で培養した。
培養PHに関しては、培養開始時より第2表に示
すPHに一定に保つために2NKOHでPHを調節し
た。なお、比較のために培養液のPHを調節せずに
同様の培養を行なつた。得られた培養液中のマン
ニトールを液体クロマトグラフイーで定量した。
結果を第2表に示す。尚、PH調整により培養中
に液量が増えるが、各成分の量は初発液量に換算
した数値で示してある。
第2表より、PH5.5で一定に保ち培養した場合、
マンニトールの収率がもつともよく、残糖が消失
することが認められた。
一方、PHを調整せずに培養した場合には、予め
培地に添加したCaCO3が培養終了時においても
残存していたにもかかわらず、培養液PHが4前後
まで低下し、多量の基質が残存してしまい、マン
ニトールの収率が低かつた。[Table] 5 ml of the medium having the medium composition (1) shown in Table 1 was placed in a test tube and heated at 120°C for 20 minutes. One platinum loop of Lactobacillus brevis (IFO 3960) was inoculated into this medium, and static culture was performed at a temperature of 30° C. for 18 hours to prepare a preculture. 50 ml of the medium having the medium composition (2) shown in Table 1 was placed in a 100 ml three-necked glass container and heated at 120° C. for 20 minutes. Add 0.5ml of the preculture solution shown above.
In addition, the cells were cultured for an additional 5 days at 30° C. under microaerobic conditions with stirring at 60-100 rpm. Regarding the culture pH, the pH was adjusted with 2NKOH to keep it constant at the pH shown in Table 2 from the start of the culture. For comparison, the same culture was performed without adjusting the pH of the culture solution. Mannitol in the obtained culture solution was quantified by liquid chromatography. The results are shown in Table 2. Although the amount of liquid increases during culture due to pH adjustment, the amount of each component is shown as a value converted to the initial amount of liquid. From Table 2, when cultured at a constant pH of 5.5,
It was observed that the yield of mannitol was good and residual sugar disappeared. On the other hand, when culturing was performed without adjusting the pH, the pH of the culture solution decreased to around 4, even though the CaCO 3 added to the medium in advance remained at the end of the culture, and a large amount of substrate was As a result, the yield of mannitol was low.
【表】
実施例 2
PHを5.5にコントロールし、実施例1で用いた
培地組成(2)の糖濃度を変化させて、ラクトバチル
スブレビス(IFO 3960)によるマンニトール生
産におけるPHコントロールの影響と至適糖濃度と
の関係を調べた。結果は第3表に示す。[Table] Example 2 Effect of PH control on mannitol production by Lactobacillus brevis (IFO 3960) and optimality by controlling the PH to 5.5 and changing the sugar concentration of the medium composition (2) used in Example 1 The relationship with sugar concentration was investigated. The results are shown in Table 3.
【表】
実施例 3
マンニトールを生成する能力を有する乳酸菌で
あるロイコノストツクメセンテロイデス(IFO
3426)を用いて更に、高濃度の糖を用いて実施例
2と同様の実験を行なつた。結果は第4表に示
す。[Table] Example 3 Leuconostocmesenteroides (IFO), a lactic acid bacterium that has the ability to produce mannitol.
3426), and an experiment similar to Example 2 was conducted using a high concentration of sugar. The results are shown in Table 4.
【表】
実施例 4
ロイコノストツクメセンテロイデス(IFO
3426)を用い、ベタインの効果を調べた。実験方
法は、実施例3と同様で、糖濃度はグルコース10
g/dlフラクトース20g/dlで行なつた。結果は
第5表に示す。[Table] Example 4 Leuconostocmesenteroides (IFO
3426) to investigate the effects of betaine. The experimental method was the same as in Example 3, and the sugar concentration was glucose 10
g/dl fructose 20g/dl. The results are shown in Table 5.
Claims (1)
に属し、マンニトール生産能を有する乳酸菌を糖
濃度10%以上の液体培地中に接種し、培養液中の
PHが5以下になつた時にアルカリを加えてPHを5
以上に調整し、培養液中のPHが6.0以上になつた
時に酸を加えてPHを6.0以下に調整しつつ培養を
行ない、培養液中にマンニトールを生成蓄積せし
め、このマンニトールを採取することを特徴とす
るマンニトールの製造法。 2 液体培地がベタインを含有する液体培地であ
る特許請求の範囲第1項記載のマンニトールの製
造法。[Scope of Claims] 1. Lactic acid bacteria belonging to the genus Lactobacillus or Leuconostoccus and capable of producing mannitol are inoculated into a liquid medium with a sugar concentration of 10% or more, and the
When the pH is below 5, add alkali to lower the pH to 5.
After adjusting the above, when the PH in the culture solution becomes 6.0 or higher, add acid to adjust the PH to 6.0 or lower while culturing, producing and accumulating mannitol in the culture solution, and collecting this mannitol. Characteristic manufacturing method of mannitol. 2. The method for producing mannitol according to claim 1, wherein the liquid medium is a liquid medium containing betaine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8569586A JPS62239995A (en) | 1986-04-14 | 1986-04-14 | Production of mannitol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8569586A JPS62239995A (en) | 1986-04-14 | 1986-04-14 | Production of mannitol |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62239995A JPS62239995A (en) | 1987-10-20 |
JPH0579312B2 true JPH0579312B2 (en) | 1993-11-02 |
Family
ID=13865965
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8569586A Granted JPS62239995A (en) | 1986-04-14 | 1986-04-14 | Production of mannitol |
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JP (1) | JPS62239995A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04183395A (en) | 1990-11-15 | 1992-06-30 | Kato Kagaku Kk | Method for separating and purifying mannitol |
EP0486024B1 (en) | 1990-11-15 | 1996-09-18 | Sumitomo Heavy Industries, Ltd | Lactobacillus SP.B001 and method of producing mannitol |
JP5933162B2 (en) * | 2007-05-31 | 2016-06-08 | カゴメ株式会社 | Method for producing fermented food and drink |
CN105002104B (en) * | 2014-04-22 | 2019-03-01 | 中国科学院大连化学物理研究所 | One plant of method for producing the Lactobacillus brevis bacterial strain of mannitol and its producing mannitol |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1296613B (en) * | 1967-01-24 | 1969-06-04 | Bernburg Serum Werk Veb | Process for the microbiological conversion of fructose into mannitol |
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1986
- 1986-04-14 JP JP8569586A patent/JPS62239995A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
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DE1296613B (en) * | 1967-01-24 | 1969-06-04 | Bernburg Serum Werk Veb | Process for the microbiological conversion of fructose into mannitol |
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