JPS62195293A - Production of l-isoleucine by fermentation method - Google Patents
Production of l-isoleucine by fermentation methodInfo
- Publication number
- JPS62195293A JPS62195293A JP3800686A JP3800686A JPS62195293A JP S62195293 A JPS62195293 A JP S62195293A JP 3800686 A JP3800686 A JP 3800686A JP 3800686 A JP3800686 A JP 3800686A JP S62195293 A JPS62195293 A JP S62195293A
- Authority
- JP
- Japan
- Prior art keywords
- isoleucine
- glutamic acid
- culture
- threoninehydroxamate
- resistant
- 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.)
- Granted
Links
- AGPKZVBTJJNPAG-WHFBIAKZSA-N L-isoleucine Chemical compound CC[C@H](C)[C@H](N)C(O)=O AGPKZVBTJJNPAG-WHFBIAKZSA-N 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims description 20
- 238000000855 fermentation Methods 0.000 title claims description 7
- 230000004151 fermentation Effects 0.000 title claims description 7
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 229960000310 isoleucine Drugs 0.000 claims abstract description 35
- 229930182844 L-isoleucine Natural products 0.000 claims abstract description 31
- 241000894006 Bacteria Species 0.000 claims abstract description 10
- 244000005700 microbiome Species 0.000 claims description 16
- AYFVYJQAPQTCCC-UHFFFAOYSA-N Threonine Natural products CC(O)C(N)C(O)=O AYFVYJQAPQTCCC-UHFFFAOYSA-N 0.000 claims description 13
- 239000004473 Threonine Substances 0.000 claims description 13
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 claims description 9
- 229930195712 glutamate Natural products 0.000 claims description 6
- AGPKZVBTJJNPAG-UHFFFAOYSA-N isoleucine Natural products CCC(C)C(N)C(O)=O AGPKZVBTJJNPAG-UHFFFAOYSA-N 0.000 claims description 4
- 241000186216 Corynebacterium Species 0.000 abstract description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 6
- 241000186226 Corynebacterium glutamicum Species 0.000 abstract description 5
- 229920001817 Agar Polymers 0.000 abstract description 4
- 239000008272 agar Substances 0.000 abstract description 4
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 4
- 241000186146 Brevibacterium Species 0.000 abstract description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 241001467578 Microbacterium Species 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 abstract description 2
- 241000186063 Arthrobacter Species 0.000 abstract 1
- 229910017053 inorganic salt Inorganic materials 0.000 abstract 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 8
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 6
- CXABZTLXNODUTD-UHFFFAOYSA-N 3-fluoropyruvic acid Chemical compound OC(=O)C(=O)CF CXABZTLXNODUTD-UHFFFAOYSA-N 0.000 description 5
- 239000004475 Arginine Substances 0.000 description 5
- ODKSFYDXXFIFQN-UHFFFAOYSA-N arginine Natural products OC(=O)C(N)CCCNC(N)=N ODKSFYDXXFIFQN-UHFFFAOYSA-N 0.000 description 5
- 229960003121 arginine Drugs 0.000 description 5
- 238000012258 culturing Methods 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 4
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 239000004202 carbamide Substances 0.000 description 4
- JQXXHWHPUNPDRT-WLSIYKJHSA-N rifampicin Chemical compound O([C@](C1=O)(C)O/C=C/[C@@H]([C@H]([C@@H](OC(C)=O)[C@H](C)[C@H](O)[C@H](C)[C@@H](O)[C@@H](C)\C=C\C=C(C)/C(=O)NC=2C(O)=C3C([O-])=C4C)C)OC)C4=C1C3=C(O)C=2\C=N\N1CC[NH+](C)CC1 JQXXHWHPUNPDRT-WLSIYKJHSA-N 0.000 description 4
- 229960001225 rifampicin Drugs 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 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 3
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 229960002685 biotin Drugs 0.000 description 3
- 235000020958 biotin Nutrition 0.000 description 3
- 239000011616 biotin Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000008103 glucose Substances 0.000 description 3
- 235000013922 glutamic acid Nutrition 0.000 description 3
- 239000004220 glutamic acid Substances 0.000 description 3
- REKYPYSUBKSCAT-UHFFFAOYSA-N 3-hydroxypentanoic acid Chemical compound CCC(O)CC(O)=O REKYPYSUBKSCAT-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- ODKSFYDXXFIFQN-BYPYZUCNSA-N L-arginine Chemical compound OC(=O)[C@@H](N)CCCN=C(N)N ODKSFYDXXFIFQN-BYPYZUCNSA-N 0.000 description 2
- FFEARJCKVFRZRR-BYPYZUCNSA-N L-methionine Chemical compound CSCC[C@H](N)C(O)=O FFEARJCKVFRZRR-BYPYZUCNSA-N 0.000 description 2
- GHSJKUNUIHUPDF-BYPYZUCNSA-N L-thialysine Chemical compound NCCSC[C@H](N)C(O)=O GHSJKUNUIHUPDF-BYPYZUCNSA-N 0.000 description 2
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 description 2
- 239000004472 Lysine Substances 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 229940024606 amino acid Drugs 0.000 description 2
- 235000001014 amino acid Nutrition 0.000 description 2
- 150000001413 amino acids Chemical class 0.000 description 2
- 235000019270 ammonium chloride Nutrition 0.000 description 2
- 229960003589 arginine hydrochloride Drugs 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 235000019441 ethanol Nutrition 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 229930182817 methionine Natural products 0.000 description 2
- 150000007524 organic acids Chemical class 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000011218 seed culture Methods 0.000 description 2
- 230000035945 sensitivity Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-N 0.000 description 1
- UKAUYVFTDYCKQA-UHFFFAOYSA-N -2-Amino-4-hydroxybutanoic acid Natural products OC(=O)C(N)CCO UKAUYVFTDYCKQA-UHFFFAOYSA-N 0.000 description 1
- 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
- HMVYERAUBSAVAX-UHFFFAOYSA-N 1-nitro-1-nitrosoguanidine Chemical compound NC(=N)N(N=O)[N+]([O-])=O HMVYERAUBSAVAX-UHFFFAOYSA-N 0.000 description 1
- YYAYLSOQGBAUHK-UHFFFAOYSA-N 2-(1,3-thiazol-2-ylamino)propanoic acid Chemical compound OC(=O)C(C)NC1=NC=CS1 YYAYLSOQGBAUHK-UHFFFAOYSA-N 0.000 description 1
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 1
- JRHWHSJDIILJAT-UHFFFAOYSA-N 2-hydroxypentanoic acid Chemical compound CCCC(O)C(O)=O JRHWHSJDIILJAT-UHFFFAOYSA-N 0.000 description 1
- LGVJIYCMHMKTPB-UHFFFAOYSA-N 3-hydroxynorvaline Chemical compound CCC(O)C(N)C(O)=O LGVJIYCMHMKTPB-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 229930024421 Adenine Natural products 0.000 description 1
- GFFGJBXGBJISGV-UHFFFAOYSA-N Adenine Chemical compound NC1=NC=NC2=C1N=CN2 GFFGJBXGBJISGV-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 1
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- XUJNEKJLAYXESH-REOHCLBHSA-N L-Cysteine Chemical compound SC[C@H](N)C(O)=O XUJNEKJLAYXESH-REOHCLBHSA-N 0.000 description 1
- 239000004201 L-cysteine Substances 0.000 description 1
- GGLZPLKKBSSKCX-YFKPBYRVSA-N L-ethionine Chemical compound CCSCC[C@H](N)C(O)=O GGLZPLKKBSSKCX-YFKPBYRVSA-N 0.000 description 1
- UKAUYVFTDYCKQA-VKHMYHEASA-N L-homoserine Chemical compound OC(=O)[C@@H](N)CCO UKAUYVFTDYCKQA-VKHMYHEASA-N 0.000 description 1
- ROHFNLRQFUQHCH-YFKPBYRVSA-N L-leucine Chemical compound CC(C)C[C@H](N)C(O)=O ROHFNLRQFUQHCH-YFKPBYRVSA-N 0.000 description 1
- ROHFNLRQFUQHCH-UHFFFAOYSA-N Leucine Natural products CC(C)CC(N)C(O)=O ROHFNLRQFUQHCH-UHFFFAOYSA-N 0.000 description 1
- PVNIIMVLHYAWGP-UHFFFAOYSA-N Niacin Chemical compound OC(=O)C1=CC=CN=C1 PVNIIMVLHYAWGP-UHFFFAOYSA-N 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- 108010009736 Protein Hydrolysates Proteins 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- 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 1
- 229930006000 Sucrose Natural products 0.000 description 1
- 241000319304 [Brevibacterium] flavum Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229960000643 adenine Drugs 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- -1 and propatool Natural products 0.000 description 1
- 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 1
- 229940088129 calcium pantothenate 10 mg Drugs 0.000 description 1
- 229940041514 candida albicans extract Drugs 0.000 description 1
- 235000013877 carbamide Nutrition 0.000 description 1
- 239000003729 cation exchange resin Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 235000018417 cysteine Nutrition 0.000 description 1
- XUJNEKJLAYXESH-UHFFFAOYSA-N cysteine Natural products SCC(N)C(O)=O XUJNEKJLAYXESH-UHFFFAOYSA-N 0.000 description 1
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 235000011087 fumaric acid Nutrition 0.000 description 1
- 239000003102 growth factor Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 150000002519 isoleucine derivatives Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 239000013028 medium composition Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 235000013379 molasses Nutrition 0.000 description 1
- 238000002703 mutagenesis Methods 0.000 description 1
- 231100000350 mutagenesis Toxicity 0.000 description 1
- 230000035772 mutation Effects 0.000 description 1
- 239000011664 nicotinic acid Substances 0.000 description 1
- 235000001968 nicotinic acid Nutrition 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- IKGXIBQEEMLURG-NVPNHPEKSA-N rutin Chemical compound O[C@@H]1[C@H](O)[C@@H](O)[C@H](C)O[C@H]1OC[C@@H]1[C@@H](O)[C@H](O)[C@@H](O)[C@H](OC=2C(C3=C(O)C=C(O)C=C3OC=2C=2C=C(O)C(O)=CC=2)=O)O1 IKGXIBQEEMLURG-NVPNHPEKSA-N 0.000 description 1
- 238000005185 salting out Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 150000004685 tetrahydrates Chemical class 0.000 description 1
- DPJRMOMPQZCRJU-UHFFFAOYSA-M thiamine hydrochloride Chemical compound Cl.[Cl-].CC1=C(CCO)SC=[N+]1CC1=CN=C(C)N=C1N DPJRMOMPQZCRJU-UHFFFAOYSA-M 0.000 description 1
- 229960000344 thiamine hydrochloride Drugs 0.000 description 1
- 235000019190 thiamine hydrochloride Nutrition 0.000 description 1
- 239000011747 thiamine hydrochloride Substances 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000012138 yeast extract Substances 0.000 description 1
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 1
- 229910000368 zinc sulfate Inorganic materials 0.000 description 1
- 239000011686 zinc sulphate Substances 0.000 description 1
- 235000009529 zinc sulphate Nutrition 0.000 description 1
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
本発明はスレオニンハイドロキサメートに耐性を示し、
L−イソロイシン生産能を有するコリネ型グルタミン酸
生産菌に属する微生物を用いるL−イソロイシンの製造
法に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention exhibits resistance to threonine hydroxamate;
The present invention relates to a method for producing L-isoleucine using a microorganism belonging to coryneform glutamic acid-producing bacteria having the ability to produce L-isoleucine.
L−イソロイシンは、アミノ酸製剤として医薬品産業な
どの分野に利用される。L-isoleucine is used in fields such as the pharmaceutical industry as an amino acid preparation.
従来の技術
従来、発酵法によるL−イソロイシンの製造法としては
、ミクロコツカス・グルタミクスに属し、スレオニン、
メチオニン、ホモセリンまたはロイシン要求性を有する
微生物を用いる方法(特公昭38−7091号公報)、
ブレビバクテリウム・フラバムに属し、α−アミノ−β
−ヒドロキシ吉草酸耐性およびアデニンまたはリジン要
求性を有する微生物を用いる方法(特公昭51−623
7号公報)、α−アミノ−β−ヒドロキシ吉草酸および
○−メチルスレオニン耐性を有する微生物を用いる方法
(特公昭51−21077号公報)、ブレビバクテリウ
ム属またはコリネバクテリウム属に属し、α−アミノ−
β−ヒドロキシ吉草酸耐性で、かつエチオニン、2−チ
アゾールアラニンおよびS−(2−アミノエチル)−L
−システィンのうち少なくとも1つに耐性を有する微生
物を用いる方法(特開昭50−101582号公報)、
コリネバクテリウム属に属し、イソロイシンアナログ耐
性で、かつメチオニンまたはリジン要求性を有する微生
物を用いる方法(特公昭54−32070号公報)、コ
リネバクテリウム属に属し、ビタミン−P耐性を有する
微生物を用いる方法(特開昭57−2687号公報)、
コリネバクテリウム属に属し、アルギニン要求性を有す
る微生物を用いる方法(特開昭59−106295号公
報)、コリネバクテリウム属に属し、フルオロピルビン
酸感受性を有する微生物を用いる方法(特開昭59−1
06294号公報)などが知られている。Conventional technology Conventionally, as a method for producing L-isoleucine by a fermentation method, L-isoleucine belonging to Micrococcus glutamicus, threonine,
A method using microorganisms having auxotrophy for methionine, homoserine or leucine (Japanese Patent Publication No. 38-7091),
Belongs to Brevibacterium flavum, α-amino-β
- Method using microorganisms having hydroxyvaleric acid resistance and adenine or lysine auxotrophy (Japanese Patent Publication No. 51-623
7), a method using a microorganism resistant to α-amino-β-hydroxyvaleric acid and ○-methylthreonine (Japanese Patent Publication No. 51-21077), which belongs to the genus Brevibacterium or the genus Corynebacterium, Amino
β-hydroxyvaleric acid resistant and ethionine, 2-thiazolealanine and S-(2-aminoethyl)-L
- A method using a microorganism resistant to at least one of cysteine (Japanese Patent Application Laid-Open No. 101582/1982),
A method using a microorganism that belongs to the genus Corynebacterium and is resistant to isoleucine analogs and has a methionine or lysine auxotrophy (Japanese Patent Publication No. 1983-32070); A method that uses a microorganism that belongs to the genus Corynebacterium and has vitamin-P resistance Method (Japanese Unexamined Patent Publication No. 57-2687),
A method using a microorganism belonging to the genus Corynebacterium and having an arginine auxotrophy (JP-A-59-106295), a method using a microorganism belonging to the genus Corynebacterium and having fluoropyruvate sensitivity (JP-A-59-1989) 1
No. 06294) and the like are known.
発明が解決しようとする問題点
アミノ酸製剤として有用なL−イソロイシンを、より収
率よく安価に製造する方法が求められている。Problems to be Solved by the Invention There is a need for a method for producing L-isoleucine, which is useful as an amino acid preparation, with higher yield and at lower cost.
問題点を解決するための手段
本発明者は、L−イソロイシンを収率よく安価に製造す
るためにより優れたL−イソロイシン生産菌の研究を行
った。その結果、スレオニンハイドロキサメートに耐性
を示し、L−イソロイシン生産能を有するコリネ型グル
タミン酸生産菌に属する微生物を用いると、収率よくL
−イソロイシンを得ることができることを見出し、本発
明を完成した。Means for Solving the Problems The present inventor conducted research on better L-isoleucine producing bacteria in order to produce L-isoleucine with high yield and at low cost. As a result, when using a microorganism belonging to the coryneform glutamate-producing bacteria that is resistant to threonine hydroxamate and has the ability to produce L-isoleucine, L-isoleucine can be produced with good yield.
- It was discovered that isoleucine could be obtained, and the present invention was completed.
以下に本発明の詳細な説明する。The present invention will be explained in detail below.
本発明は、コリネ型グルタミン酸生産菌に属し、スレオ
ニンハイドロキサメートに耐性を示し、かつL−イソロ
イシン生産能を有する微生物を培地に培養し、培養物中
にL−イソロイシンを生成蓄積させ、該培養物よりL−
イソロイシンを採取することを特徴とする発酵法による
L−イソロイシンの製造法を提供する。The present invention involves culturing a microorganism belonging to coryneform glutamate-producing bacteria, showing resistance to threonine hydroxamate, and having an ability to produce L-isoleucine in a medium, producing and accumulating L-isoleucine in the culture, and culturing the microorganism in a medium. L- than things
Provided is a method for producing L-isoleucine by a fermentation method characterized by collecting isoleucine.
本発明に使用する微生物の例としては、コリネ型グルタ
ミン酸生産菌に属し、スレオニンハイドロキサメートに
耐性を示し、かつL−イソロイシン生産能を有する微生
物であればいずれも用いることができる。スレオニンハ
イドロキサメートに耐性の菌株は、コリネ型グルタミン
酸生産菌を通常の変異手段により変異させ、スレオニン
ハイドロキサメートを1g/(2以上含有する寒天培地
上で生育してくる菌として得ることができる。好適な例
としては、コリネバクテリウム・グルタミクムH−42
60をあげることができる。As an example of the microorganism used in the present invention, any microorganism that belongs to the coryneform glutamic acid-producing bacteria, exhibits resistance to threonine hydroxamate, and has the ability to produce L-isoleucine can be used. A strain resistant to threonine hydroxamate can be obtained by mutating a coryneform glutamate-producing bacterium by conventional mutation methods and growing on an agar medium containing 1 g/(2 or more) of threonine hydroxamate. A suitable example is Corynebacterium glutamicum H-42.
I can give you 60.
本明細書において、コリネ型グルタミン酸生産菌とは、
コリネバクテリウム属、ブレビバクテリウム属、ミクロ
バクテリウム属またはアースロバフタ−属に属する一群
のグルタミン酸生産菌をいう〔「発酵と工業」第40巻
、102.1982年参照〕。As used herein, coryneform glutamate-producing bacteria are
A group of glutamic acid-producing bacteria belonging to the genus Corynebacterium, Brevibacterium, Microbacterium, or Arthrobacterium [see "Fermentation and Industry" Vol. 40, 102, 1982].
以下に、上記のスレオニンハイドロキサメート耐性株の
取得方法の具体例を示す。A specific example of the method for obtaining the above-mentioned threonine hydroxamate-resistant strain is shown below.
コリネバクテリウム・グルタミン酸ムH−3501〔ア
ルギニン要求性、S−(2−アミノエチル)−L−シス
ティン耐性、リファンピシン耐性、フルオロピルビン酸
感受性、本菌株は昭和60年7月16日付で工業技術院
微生物工業技術研究所(以下微工研という)にFERM
BP−848として寄託されている。〕を〕N−メ
チルーN′〜ニトローN−二トロソグアニジンNTG)
による変異処理(200x/ml、 30℃、30分間
)した後、以下に示す最少寒天培地に2g/βのスレオ
ニンハイドロキサメートを添加した培地で生育しつるよ
うな菌株を採取することにより行うことができる。得ら
れたスレオニンハイドロキサメート耐性株50株をL−
イソロイシンの生産試験(実施例の方法)にかけ、親株
よりL−イソロイシン生産性が著しくすぐれた菌株を選
んだ。そのうちの1株がコリネバクテリウム・グルタミ
クムH−4260(アルギニン要求性、5−(2−アミ
ノエチルiL−システィン耐性、リファンピシン耐性、
フルオロピルビン酸感受性、スレオニンハイドロキサメ
ート耐性〕である。Corynebacterium glutamate H-3501 [arginine auxotrophic, S-(2-aminoethyl)-L-cysteine resistant, rifampicin resistant, fluoropyruvate sensitive, this strain was approved by the Agency of Industrial Science and Technology on July 16, 1985. FERM to the Microbial Technology Research Institute (hereinafter referred to as FERM)
It has been deposited as BP-848. ] N-methyl-N' ~ nitro N-nitrosoguanidine NTG)
After mutagenesis treatment (200x/ml, 30°C, 30 minutes), collect a strain that grows and vines on the following minimal agar medium supplemented with 2g/β threonine hydroxamate. I can do it. The obtained 50 threonine hydroxamate resistant strains were transformed into L-
A strain was selected which was subjected to an isoleucine production test (method in the example) and had significantly better L-isoleucine productivity than the parent strain. One of the strains was Corynebacterium glutamicum H-4260 (arginine auxotrophy, 5-(2-aminoethyl iL-cysteine resistant, rifampicin resistant,
Sensitive to fluoropyruvate, resistant to threonine hydroxamate].
本菌株は昭和61年2月13日付で微工研にFERM
BP−986として寄託されている。This strain was FERMed to the Microtech Institute on February 13, 1986.
It has been deposited as BP-986.
培地組成ニゲルコース0.5%、(NH4)2S0゜0
.15%、K H2P O* 0.15%、K2HP0
゜0.05%、NaCJ! 0.01%、Mg5C)
s ・7H200,05%、CaC#z’2HzO1
x/m15MnCl1z・4H207xr/ml、Fe
50< 1H2010g/m+、チアミン塩酸塩Q、
lB/ml、ビオチンQ、 03■/ml 、アルギニ
ン塩酸塩0.01%、寒天1.5%、pH7,2上記微
生物を炭素源、窒素源、無機塩類、生育因子などを含有
する合成培地または天然培地を用いて培養することによ
りL−イソロイシンを培養物中に蓄積させ、これを採取
することによりL−イソロイシンを製造することができ
る。Medium composition Nigelcose 0.5%, (NH4)2S0゜0
.. 15%, K H2P O* 0.15%, K2HP0
゜0.05%, NaCJ! 0.01%, Mg5C)
s ・7H200,05%, CaC#z'2HzO1
x/m15MnCl1z・4H207xr/ml, Fe
50<1H2010g/m+, thiamine hydrochloride Q,
1B/ml, biotin Q, 03■/ml, arginine hydrochloride 0.01%, agar 1.5%, pH 7.2 The above microorganisms were placed in a synthetic medium containing carbon sources, nitrogen sources, inorganic salts, growth factors, etc. L-isoleucine can be produced by accumulating L-isoleucine in the culture by culturing in a natural medium and collecting it.
炭素源としては、グルコース、シュークロース、糖蜜、
デンプン加水分解物などの糖類、酢酸、プロピオン酸、
ギ酸、フマール酸、リンゴ酸などの有機酸類、メタノー
ル、エタノール、プロパツールなどのアルコール類、炭
化水素などが使用できる。Carbon sources include glucose, sucrose, molasses,
Sugars such as starch hydrolysates, acetic acid, propionic acid,
Organic acids such as formic acid, fumaric acid, and malic acid, alcohols such as methanol, ethanol, and propatool, and hydrocarbons can be used.
窒素源としては硫酸アンモニウム、硝酸アンモニウム、
塩化アンモニウム、リン酸アンモニウム、尿素、アンモ
ニアなどが使用できる。また、栄養要求性を示す変異株
の場合には、栄養物質を純品として、または、それらを
含有する天然栄養物の形で添加することができる。Nitrogen sources include ammonium sulfate, ammonium nitrate,
Ammonium chloride, ammonium phosphate, urea, ammonia, etc. can be used. Furthermore, in the case of mutant strains exhibiting auxotrophy, nutritional substances can be added as pure products or in the form of natural nutrients containing them.
培養は振盪培養あるいは深部通気攪拌培養などの好気的
条件下で行う。培養温度は通常24〜37℃、好ましく
は28〜32℃の範囲で、培地のpHは5〜9の範囲、
好ましくは中性付近に保持することが望ましい。培地の
pH調節は、炭酸カルシウム、無機又は有機の酸、アル
カリ溶液、尿素、炭酸カルシウム、アンモニアガスなど
によって行う。Cultivation is performed under aerobic conditions such as shaking culture or deep aeration agitation culture. The culture temperature is usually in the range of 24 to 37°C, preferably 28 to 32°C, and the pH of the medium is in the range of 5 to 9.
It is desirable to maintain the temperature near neutrality. The pH of the medium is adjusted using calcium carbonate, an inorganic or organic acid, an alkaline solution, urea, calcium carbonate, ammonia gas, or the like.
培養期間は通常2〜7日間で培養物中にL−イソロイシ
ンが生成蓄積する。The culture period is usually 2 to 7 days, and L-isoleucine is produced and accumulated in the culture.
培養終了後、培養液から菌体などの沈殿物を除去し、イ
オン交換処理法、濃縮法、吸着法、塩析法などを併用す
ることにより、培養液からL−イソロイシンを回収する
ことができる。After culturing, L-isoleucine can be recovered from the culture solution by removing precipitates such as bacterial cells from the culture solution and using ion exchange treatment, concentration method, adsorption method, salting out method, etc. .
以下に実施例を示す。Examples are shown below.
実施例1
コリネバクテリウム・グルタミクムH−4260〔アル
ギニン要求性、5−(2−アミノエチル)−L−システ
ィン耐性、フルオロピルビン酸感受性、リファンピシン
耐性、スレオニンハイドロキサメート耐性〕 (FER
M BP 986)を23m1の種培地(グルコー
ス5%、酵母エキス1%、ペプトン1%、尿素0.3%
、NaC10,25%、コーン・スチープ・リカー0.
5%、ビオチン50ttx/l、pH7,2)を含む3
00ml容三角フラスコに接種し、28℃で24時間、
21Orpmのロータリーシェーカー上で振とう培養し
た。Example 1 Corynebacterium glutamicum H-4260 [arginine auxotrophy, 5-(2-aminoethyl)-L-cysteine resistance, fluoropyruvate sensitivity, rifampicin resistance, threonine hydroxamate resistance] (FER
M BP 986) in 23 ml of seed medium (glucose 5%, yeast extract 1%, peptone 1%, urea 0.3%).
, NaC 10.25%, Corn Steep Liquor 0.
5%, biotin 50ttx/l, pH 7,2)
Inoculated into a 00ml Erlenmeyer flask and incubated at 28°C for 24 hours.
Shaking culture was performed on a rotary shaker at 21 rpm.
この種培養液2mlを20m1の発酵培地を含む300
m1容三角フラスコに接種して72時間、種培養と同様
の方法で培養した。培養終了後の培養液中のL−イソロ
イシン蓄積量は、13.4g/#であった。対照とした
親株H−3501株〔アルギニン要求性、S−(2−ア
ミノエチル)−L−システィン耐性、フルオロピルビン
酸感受性、リファンピシン耐性〕を用いて同様に培養し
た結果、L〜インロイシンの蓄積量は、11.6g/f
fであった。300ml of this seed culture containing 20ml of fermentation medium
It was inoculated into a 1 m Erlenmeyer flask and cultured for 72 hours in the same manner as the seed culture. The amount of L-isoleucine accumulated in the culture solution after completion of the culture was 13.4 g/#. As a result of culturing in the same manner using the parent strain H-3501 [arginine auxotrophic, S-(2-aminoethyl)-L-cysteine resistant, fluoropyruvate sensitive, rifampicin resistant] as a control, L-inleucine accumulation was observed. The amount is 11.6g/f
It was f.
発酵培地の組成は次のとおり。The composition of the fermentation medium is as follows.
廃ng<グルコース換3iE)70g/Cコーン・スチ
ープ・リカー5g/L塩化アンモニウム20g#、尿素
2g/j!、KH2PO12g/11Mg5O4−7H
200,5g/j2SFeSO4・7H200,01g
//、MnCj!2・4HzO0,01g#2、Cu5
O,・5H200,01g#、CaCff1z・2t(
to O,OXg/l、ZnSO4・7H7H2O1
/n、N 1(1221mg/n、%リブデン酸アンモ
ン・4水塩1mg/I2、Co C(12・6HzO1
mg/f、パントテン酸カルシウム10mg/C二:+
チン酸1mg/#、ビオチン50■/1、アルギニン塩
酸塩0.5g/I2、p H7,4H−4260株を用
いて得たし一インロインン含有培養液200ffllを
遠心分離(3,00Orpm、10分)にかけ、菌体そ
の他の不純物を除いた。Waste ng < glucose conversion 3iE) 70g/C corn steep liquor 5g/L ammonium chloride 20g#, urea 2g/j! , KH2PO12g/11Mg5O4-7H
200,5g/j2SFeSO4・7H200,01g
//, MnCj! 2.4HzO0.01g#2, Cu5
O,・5H200,01g#,CaCff1z・2t(
to O, OXg/l, ZnSO4・7H7H2O1
/n, N 1 (1221 mg/n, % Ammonium ribdate tetrahydrate 1 mg/I2, Co C (12.6 Hz O1
mg/f, calcium pantothenate 10 mg/C2:+
Tinic acid 1 mg/#, biotin 50 μ/1, arginine hydrochloride 0.5 g/I2, pH 7, 200 ffll of a culture solution containing linoin obtained using the 4H-4260 strain was centrifuged (3,00 rpm, 10 minutes). ) to remove bacterial cells and other impurities.
得られた上澄液を強酸性陽イオン交換樹脂ダイヤイオン
5KI(H”型)(三菱化成工業社製)のカラムに通し
、L−イソロイシンを吸着させ、水洗後、0.5規定の
アンモニア水で溶出してL−イソロイシン画分を集めた
。集めた画分を濃縮してpH6,02の等電点て晶出さ
せることにより、純度99%のし一イソロイシン1.4
gを得た。The obtained supernatant liquid was passed through a column of strongly acidic cation exchange resin Diaion 5KI (H" type) (manufactured by Mitsubishi Chemical Industries, Ltd.) to adsorb L-isoleucine, and after washing with water, 0.5 N ammonia water was added. The L-isoleucine fraction was collected by elution.The collected fractions were concentrated and crystallized using an isoelectric point of pH 6.02 to obtain 99% pure L-isoleucine 1.4.
I got g.
発明の効果
本発明方法によれば、収率よくL−イソロイシンを得る
ことができる。Effects of the Invention According to the method of the present invention, L-isoleucine can be obtained in good yield.
Claims (1)
ロキサメートに耐性を示し、かつL−イソロイシン生産
能を有する微生物を培地に培養し、培養物中にL−イソ
ロイシンを生成蓄積させ、該培養物よりL−イソロイシ
ンを採取することを特徴とする発酵法によるL−イソロ
イシンの製造法。A microorganism belonging to the coryneform glutamate-producing bacteria, showing resistance to threonine hydroxamate, and having the ability to produce L-isoleucine is cultured in a medium, L-isoleucine is produced and accumulated in the culture, and L-isoleucine is produced and accumulated in the culture. A method for producing L-isoleucine by a fermentation method, characterized by collecting isoleucine.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3800686A JPS62195293A (en) | 1986-02-22 | 1986-02-22 | Production of l-isoleucine by fermentation method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3800686A JPS62195293A (en) | 1986-02-22 | 1986-02-22 | Production of l-isoleucine by fermentation method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62195293A true JPS62195293A (en) | 1987-08-28 |
JPH0555113B2 JPH0555113B2 (en) | 1993-08-16 |
Family
ID=12513485
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3800686A Granted JPS62195293A (en) | 1986-02-22 | 1986-02-22 | Production of l-isoleucine by fermentation method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62195293A (en) |
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---|---|---|---|---|
WO2008044409A1 (en) | 2006-10-10 | 2008-04-17 | Ajinomoto Co., Inc. | Method for production of l-amino acid |
WO2008075483A1 (en) | 2006-12-19 | 2008-06-26 | Ajinomoto Co., Inc. | Process for production of l-amino acid |
WO2008102572A1 (en) | 2007-02-20 | 2008-08-28 | Ajinomoto Co., Inc. | Method for production of l-amino acid or nucleic acid |
WO2009082028A2 (en) | 2007-12-21 | 2009-07-02 | Ajinomoto Co., Inc. | Process for producing (2s,3r,4s)-4-hydroxy-l-isoleucine |
WO2009088049A1 (en) | 2008-01-10 | 2009-07-16 | Ajinomoto Co., Inc. | Method for production of desired substance by fermentation process |
WO2009093703A1 (en) | 2008-01-23 | 2009-07-30 | Ajinomoto Co., Inc. | Method of producing l-amino acid |
WO2011013707A1 (en) | 2009-07-29 | 2011-02-03 | 味の素株式会社 | Method for producing l-amino acid |
WO2014185430A1 (en) | 2013-05-13 | 2014-11-20 | 味の素株式会社 | Method for manufacturing l-amino acid |
WO2015005406A1 (en) | 2013-07-09 | 2015-01-15 | 味の素株式会社 | Method for manufacturing useful substance |
WO2015050234A1 (en) | 2013-10-02 | 2015-04-09 | 味の素株式会社 | Ammonia control apparatus and ammonia control method |
WO2015060391A1 (en) | 2013-10-23 | 2015-04-30 | 味の素株式会社 | Method for producing target substance |
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-
1986
- 1986-02-22 JP JP3800686A patent/JPS62195293A/en active Granted
Cited By (15)
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---|---|---|---|---|
WO2008044409A1 (en) | 2006-10-10 | 2008-04-17 | Ajinomoto Co., Inc. | Method for production of l-amino acid |
WO2008075483A1 (en) | 2006-12-19 | 2008-06-26 | Ajinomoto Co., Inc. | Process for production of l-amino acid |
WO2008102572A1 (en) | 2007-02-20 | 2008-08-28 | Ajinomoto Co., Inc. | Method for production of l-amino acid or nucleic acid |
WO2009082028A2 (en) | 2007-12-21 | 2009-07-02 | Ajinomoto Co., Inc. | Process for producing (2s,3r,4s)-4-hydroxy-l-isoleucine |
EP2749652A2 (en) | 2008-01-10 | 2014-07-02 | Ajinomoto Co., Inc. | A method for producing a target substance by fermentation |
WO2009088049A1 (en) | 2008-01-10 | 2009-07-16 | Ajinomoto Co., Inc. | Method for production of desired substance by fermentation process |
WO2009093703A1 (en) | 2008-01-23 | 2009-07-30 | Ajinomoto Co., Inc. | Method of producing l-amino acid |
WO2011013707A1 (en) | 2009-07-29 | 2011-02-03 | 味の素株式会社 | Method for producing l-amino acid |
WO2014185430A1 (en) | 2013-05-13 | 2014-11-20 | 味の素株式会社 | Method for manufacturing l-amino acid |
WO2015005406A1 (en) | 2013-07-09 | 2015-01-15 | 味の素株式会社 | Method for manufacturing useful substance |
EP3521433A1 (en) | 2013-07-09 | 2019-08-07 | Ajinomoto Co., Inc. | Process for producing l-glutamic acid |
WO2015050234A1 (en) | 2013-10-02 | 2015-04-09 | 味の素株式会社 | Ammonia control apparatus and ammonia control method |
WO2015060391A1 (en) | 2013-10-23 | 2015-04-30 | 味の素株式会社 | Method for producing target substance |
EP3385389A1 (en) | 2017-04-03 | 2018-10-10 | Ajinomoto Co., Inc. | Method for producing l-amino acid from fructose |
WO2023195475A1 (en) | 2022-04-04 | 2023-10-12 | 味の素株式会社 | Method for controlling parasitic plants |
Also Published As
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---|---|
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