JPH0475588A - Production of sorbic acid - Google Patents
Production of sorbic acidInfo
- Publication number
- JPH0475588A JPH0475588A JP18914090A JP18914090A JPH0475588A JP H0475588 A JPH0475588 A JP H0475588A JP 18914090 A JP18914090 A JP 18914090A JP 18914090 A JP18914090 A JP 18914090A JP H0475588 A JPH0475588 A JP H0475588A
- Authority
- JP
- Japan
- Prior art keywords
- group
- microorganisms
- sorbic acid
- sorbaldehyde
- acid
- 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
- BEFDCLMNVWHSGT-UHFFFAOYSA-N ethenylcyclopentane Chemical compound C=CC1CCCC1 BEFDCLMNVWHSGT-UHFFFAOYSA-N 0.000 title claims abstract description 31
- 235000010199 sorbic acid Nutrition 0.000 title claims abstract description 31
- 239000004334 sorbic acid Substances 0.000 title claims abstract description 31
- 229940075582 sorbic acid Drugs 0.000 title claims abstract description 31
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 244000005700 microbiome Species 0.000 claims abstract description 30
- 239000003223 protective agent Substances 0.000 claims abstract description 17
- BATOPAZDIZEVQF-MQQKCMAXSA-N (E,E)-2,4-hexadienal Chemical compound C\C=C\C=C\C=O BATOPAZDIZEVQF-MQQKCMAXSA-N 0.000 claims abstract description 16
- BATOPAZDIZEVQF-UHFFFAOYSA-N sorbic aldehyde Natural products CC=CC=CC=O BATOPAZDIZEVQF-UHFFFAOYSA-N 0.000 claims abstract description 16
- 125000003396 thiol group Chemical group [H]S* 0.000 claims abstract description 16
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 claims abstract description 14
- 150000001413 amino acids Chemical class 0.000 claims abstract description 10
- 108090000765 processed proteins & peptides Proteins 0.000 claims abstract description 10
- 150000001298 alcohols Chemical class 0.000 claims abstract description 9
- 102000004196 processed proteins & peptides Human genes 0.000 claims abstract description 9
- 230000001590 oxidative effect Effects 0.000 claims abstract description 8
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 claims abstract description 7
- 235000010323 ascorbic acid Nutrition 0.000 claims abstract description 7
- 229960005070 ascorbic acid Drugs 0.000 claims abstract description 7
- 239000011668 ascorbic acid Substances 0.000 claims abstract description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 4
- DGVVWUTYPXICAM-UHFFFAOYSA-N β‐Mercaptoethanol Chemical compound OCCS DGVVWUTYPXICAM-UHFFFAOYSA-N 0.000 claims description 4
- 108010024636 Glutathione Proteins 0.000 claims description 2
- RWSXRVCMGQZWBV-WDSKDSINSA-N glutathione Chemical compound OC(=O)[C@@H](N)CCC(=O)N[C@@H](CS)C(=O)NCC(O)=O RWSXRVCMGQZWBV-WDSKDSINSA-N 0.000 claims description 2
- 235000001014 amino acid Nutrition 0.000 claims 2
- XUJNEKJLAYXESH-UHFFFAOYSA-N cysteine Natural products SCC(N)C(O)=O XUJNEKJLAYXESH-UHFFFAOYSA-N 0.000 claims 1
- 235000018417 cysteine Nutrition 0.000 claims 1
- VHJLVAABSRFDPM-QWWZWVQMSA-N dithiothreitol Chemical compound SC[C@@H](O)[C@H](O)CS VHJLVAABSRFDPM-QWWZWVQMSA-N 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 abstract description 19
- 230000000694 effects Effects 0.000 abstract description 6
- 230000000813 microbial effect Effects 0.000 abstract description 3
- 230000007246 mechanism Effects 0.000 abstract description 2
- 241000588810 Alcaligenes sp. Species 0.000 abstract 1
- 241000147019 Enterobacter sp. Species 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 230000001681 protective effect Effects 0.000 abstract 1
- 108090000790 Enzymes Proteins 0.000 description 7
- 102000004190 Enzymes Human genes 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 239000000243 solution Substances 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- PXQLVRUNWNTZOS-UHFFFAOYSA-N sulfanyl Chemical class [SH] PXQLVRUNWNTZOS-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 241000589220 Acetobacter Species 0.000 description 3
- 241000588986 Alcaligenes Species 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 3
- 241000186146 Brevibacterium Species 0.000 description 3
- 241000186216 Corynebacterium Species 0.000 description 3
- 241000588722 Escherichia Species 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 241000186359 Mycobacterium Species 0.000 description 3
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 3
- 238000000354 decomposition reaction Methods 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- 241000186063 Arthrobacter Species 0.000 description 2
- 241000193830 Bacillus <bacterium> Species 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 241001149409 Cystobasidium minutum Species 0.000 description 2
- 241000588914 Enterobacter Species 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 241001467578 Microbacterium Species 0.000 description 2
- 230000010718 Oxidation Activity Effects 0.000 description 2
- 241001057811 Paracoccus <mealybug> Species 0.000 description 2
- 239000001888 Peptone Substances 0.000 description 2
- 108010080698 Peptones Proteins 0.000 description 2
- 241000588769 Proteus <enterobacteria> Species 0.000 description 2
- 241000589516 Pseudomonas Species 0.000 description 2
- 241000190932 Rhodopseudomonas Species 0.000 description 2
- 241000187747 Streptomyces Species 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 238000012258 culturing Methods 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 235000019319 peptone Nutrition 0.000 description 2
- 239000008363 phosphate buffer Substances 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 241000589212 Acetobacter pasteurianus Species 0.000 description 1
- 241000193755 Bacillus cereus Species 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- 241000186145 Corynebacterium ammoniagenes Species 0.000 description 1
- 241000186226 Corynebacterium glutamicum Species 0.000 description 1
- 241001058146 Erium Species 0.000 description 1
- 241000589565 Flavobacterium Species 0.000 description 1
- 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 1
- 241000588748 Klebsiella Species 0.000 description 1
- 241000588747 Klebsiella pneumoniae Species 0.000 description 1
- 241000191948 Kocuria rosea Species 0.000 description 1
- 241000192041 Micrococcus Species 0.000 description 1
- 241000187654 Nocardia Species 0.000 description 1
- 241000187681 Nocardia sp. Species 0.000 description 1
- 241000902235 Oides Species 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 241000589597 Paracoccus denitrificans Species 0.000 description 1
- 241000588770 Proteus mirabilis Species 0.000 description 1
- 241000223252 Rhodotorula Species 0.000 description 1
- 241000607720 Serratia Species 0.000 description 1
- 241000319304 [Brevibacterium] flavum Species 0.000 description 1
- IKHGUXGNUITLKF-XPULMUKRSA-N acetaldehyde Chemical compound [14CH]([14CH3])=O IKHGUXGNUITLKF-XPULMUKRSA-N 0.000 description 1
- 235000019270 ammonium chloride 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
- 230000003698 anagen phase Effects 0.000 description 1
- 239000000872 buffer Substances 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 235000013877 carbamide Nutrition 0.000 description 1
- 239000005515 coenzyme Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 150000001879 copper Chemical class 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 229940099112 cornstarch Drugs 0.000 description 1
- MLUCVPSAIODCQM-NSCUHMNNSA-N crotonaldehyde Chemical compound C\C=C\C=O MLUCVPSAIODCQM-NSCUHMNNSA-N 0.000 description 1
- MLUCVPSAIODCQM-UHFFFAOYSA-N crotonaldehyde Natural products CC=CC=O MLUCVPSAIODCQM-UHFFFAOYSA-N 0.000 description 1
- 238000012136 culture method Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 235000019249 food preservative Nutrition 0.000 description 1
- 239000005452 food preservative Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 230000012010 growth Effects 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 159000000014 iron salts Chemical class 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 150000002596 lactones Chemical class 0.000 description 1
- 159000000003 magnesium salts Chemical class 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000002504 physiological saline solution Substances 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- 238000000746 purification Methods 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
- 230000035484 reaction time Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 230000000284 resting effect Effects 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 150000003751 zinc Chemical class 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:よエチレンジアミン四酢酸又;ユアスコルヒン
酸又はメルカプト基を持つアルコール類、アミノ酸類、
若しくはペプチド類から選ばれるメルカプト基保護剤の
少なくとも一種をソルブアルデヒトを微生物で酸化4゛
る系中に共存させてソルビン酸を製造する方法に関する
しのである。[Detailed Description of the Invention] [Industrial Field of Application The present invention: ethylenediaminetetraacetic acid; alcohols, amino acids, etc. having yascorhinic acid or mercapto groups;
The present invention relates to a method for producing sorbic acid by allowing at least one mercapto group protecting agent selected from peptides to coexist in a system in which sorbaldehyde is oxidized by microorganisms.
U従来の技術
ソルビン酸は抗カヒカか優れているので食品保存剤とし
て賞用されているか、その工業的な製造法としては通常
クロトンアルデヒドとケトンとを反応させて中間的に形
成されたβ−ラクトンを経てそのポリエステルを製造し
、次いて該ポリエステルを熱分解、酸分解あるいはイ才
)交換樹脂分解してソルビン酸を生成させる方法か実施
されている。U Prior Art Sorbic acid has excellent anti-cajicity properties and is therefore used as a food preservative.The industrial method for producing it is usually made by reacting crotonaldehyde and ketone to form an intermediate β- A method has been practiced in which the polyester is produced through lactone, and then the polyester is decomposed by thermal decomposition, acid decomposition, or exchange resin decomposition to produce sorbic acid.
しかしなから、かかる方法においてはポリニスチル分解
後のソルビン酸の回収あるいは精製操作か面倒で工程面
が長く、複雑な工程管理を必要とする等製造面、経済面
において必ずしも存IIIであると言い難い。However, in such a method, recovery and purification of sorbic acid after decomposition of polynistil is troublesome, the process is long, and complicated process control is required, so it is difficult to say that it is completely viable from a production and economic perspective. .
かかる解決策として、ソルブアルデヒトを特定の微生物
で酸化処理してソルビン酸を製造する方法が提案され、
又本出願人も特許出願を行っているところである。As a solution to this problem, a method has been proposed in which sorbic acid is produced by oxidizing sorbaldehyde using specific microorganisms.
The present applicant is also in the process of filing a patent application.
U発明が解決しようとする課Mコ
しかし戸から、かかる微生物によるソルビン酸の製造方
法では製造されたソルビン酸が反応系に蓄積されていく
のであるが、核酸はソルブアルデヒドを酸化する微生物
内のメルカプト基酵素を阻害して微生物の持つ酸化活性
を抑制するためにソルビン酸の収率は低下する。従って
、工業的規模での実施には未だ問題か残っており、容易
な操作法で反応系中にソルビン酸か蓄積されても微生物
活性が安定化し、ソルビン酸の収率を向上させる創意工
夫が必要とされるのである。However, in the method for producing sorbic acid using microorganisms, the produced sorbic acid accumulates in the reaction system, but the nucleic acid is absorbed by the microorganism that oxidizes sorbaldehyde. The yield of sorbic acid decreases because the oxidative activity of microorganisms is suppressed by inhibiting mercapto group enzymes. Therefore, there are still some problems in implementing it on an industrial scale, and there are ingenious ways to improve the yield of sorbic acid by stabilizing microbial activity even if sorbic acid accumulates in the reaction system using a simple operation method. It is needed.
[課題を解決するための手段]
本発明者等は上記問題を解決すべく鋭意研究を重ねた結
果、ソルブアルデヒドを微生物により酸化してソルビン
酸を製造するに当たり、系中にエチレンジアミン四酢酸
(以後EDTAと略記する)又はアスコルビン酸又はメ
ルカプト基(以後SH基と略記する)を持つアルコール
類、アミノ酸類、若しくはペプチド類から選ばれるSH
基保護剤の少なくとら一種を共存さけてソルビン酸の製
造を行うと、ソルビン酸の収率か向上することを見出し
、本発明を完成するに至った。[Means for Solving the Problems] As a result of intensive research to solve the above problems, the present inventors found that when producing sorbic acid by oxidizing sorbaldehyde with microorganisms, ethylenediaminetetraacetic acid (hereinafter referred to as SH selected from alcohols, amino acids, or peptides having an ascorbic acid or mercapto group (hereinafter abbreviated as SH group);
The present inventors have discovered that the yield of sorbic acid can be improved by producing sorbic acid while avoiding the coexistence of at least one type of group protecting agent, and have completed the present invention.
ソルビン酸は微生物内のメルカプト酵素(以後SH酵素
と略記する)のノスルフィト結合を切り三次構造を崩し
てSH酵素の活性を低下させるのであるか、本発明;よ
微生物でソルブアルデヒドを酸化する系中にE D T
、A又はアスコルビン酸又はS H基をもつアルコー
ル類、アミノ酸類、若しくはペプチド類から選ばれるS
H基保護剤の少なくとも一種を共存させることにより上
記記載のSH酵素阻害機構を該S H基保護剤が防ぐの
で、微生物活性を長期安定化してソルビン酸の収率が向
上することを特徴とする。Does sorbic acid cut the nosulfite bonds of mercapto enzymes (hereinafter abbreviated as SH enzymes) in microorganisms, destroy the tertiary structure, and reduce the activity of SH enzymes?The present invention; ED T
, A or ascorbic acid or S selected from alcohols, amino acids, or peptides having a S H group
By allowing at least one type of H group protecting agent to coexist, the SH enzyme inhibition mechanism described above is prevented by the S H group protecting agent, thereby stabilizing microbial activity over a long period of time and improving the yield of sorbic acid. .
以下本発明について詳しく説明する。The present invention will be explained in detail below.
まず本発明において使用する微生物としては、アルカリ
ゲネス(Alcaligenes)属、エンテロバクタ
−(Enterobacter)属、プロテウス(Pr
oteus)属、ロドシユードモナス(Rhodops
eudomonas )属、コリネバクテリウム(Fl
avobacterium)属、ノカルデイア(Noc
ardia)属、ミコバクテリウム(Mycobact
erium)属、ハクテリノウム(Bacteridi
um)属、ストレプトミセス(Streptomyce
s )属、ノトロバクター(C1trobacter)
属、ツユウドモナス(PseudomonaS)属、ア
セトバクター(、Acetobacter)属、アース
ロバフタ−(^rthrobacter)属、コリネバ
クテリウム(Corynebacterium)属、サ
ノ力ロマイコプノス(Saccharomycopsl
s )属、クレブノエラ(Klebsiella)属、
ロドトルラ(RhodoLorula)属、バチルス(
BacilluS)属、ミクロバクテリウム(Micr
obacterium)属、パラコツカス(Parac
occus )属、セラチア(5erratia)属、
プレヒバクテリウム(Brevibacterium)
属、エノエリヒア(Escherichia)属、ミク
ロコツカス(Micrococcus )属等が挙げら
れ、ソルブアルデヒドを酸化する能力のあるものであれ
ばいずれも実用出来る。First, the microorganisms used in the present invention include the genus Alcaligenes, the genus Enterobacter, and the genus Proteus.
oteus), Rhodoseudomonas (Rhodops)
eudomonas) genus, Corynebacterium (Fl
avobacterium genus, Nocardia (Noc.
ardia), Mycobacterium
erium), Bacteridi
um) genus, Streptomyce
s) genus, Notrobacter (C1trobacter)
Genus, PseudomonaS, Acetobacter, Arthrobacter, Corynebacterium, Saccharomycopsl
s), genus Klebsiella,
Rhodotorula genus, Bacillus (
Bacillus S), Microbacterium (Micr
genus obacterium, Paracoccus
occus ) genus, Serratia (5erratia) genus,
Brevibacterium
Examples include the genus Escherichia, the genus Escherichia, and the genus Micrococcus, and any of them can be put to practical use as long as they have the ability to oxidize sorbaldehyde.
更に、具体的に幾つか例示すれば、アルカリゲネス ユ
ートロファス(Alcaligenes eutrop
hus AT CCI 7699)、エンテロバクタ
−クロアカニ(Enterobactor cloac
aa、IFO12935)、プロテウス ミラビリス(
Proteus ff1irabilis; I F
O13300) 、ロドシュードモナス スフェロイド
(RhodopseudoIIlonas 5pher
oides ; I F O12203) 、フラポバ
クテリウムスアヘオレノス(Flavobacteri
um 5uaveolens ATCC958)、ノ
カルデイア エスピー(Nocardia 5pIFO
+4326)、ミコバクテリウム ロトクロス(Myc
obacterium rhodochrous :
I F Ol 3161 )、バクテリウム サブクラ
ップイス(Bacteridium subgIanc
lis ; I F O31322) 、ストしブトミ
セス アルヒドフラバス(Streptomyces
albidoflavus IF 013010)、
ツユウドモナス ツユウドアルカリゲネス(Pseud
ononas pseudoalcaligenes
、l F 014167)、ツユウドモナス エアルギ
ノサ(Pseudomonas earuginosa
; IFO3445)、アセトバクター アセンデンス
(Acetobactel−ascendens :
l F O3188)、アセトバクター パスチュリア
ヌス サブエスピー ロバニエン(Acetobact
er pasteurianus 5ubsp Io
vanienIFO!3753)、7−7、cyバクタ
ー オキシタンス(Arthrobactor ox
ydans; ATCCl 4359 )、アセトバク
ター アラレセンス(Arthrobactor au
rescens; IFOI 2136)、コリネバク
テリウム ダルタミカム(Corynebacteri
um glutamicum A T CC2+650
)、サブ力ロマイコプノス リポリティ力(Sacch
aromycopsis 1ipolytica ;
I F 01548 )、タレブノエラニュウモニア(
Klebsiella pneumoniae 。Furthermore, to give some specific examples, Alcaligenes eutropus (Alcaligenes eutropus)
hus AT CCI 7699), Enterobacter cloac
aa, IFO12935), Proteus mirabilis (
Proteus ff1irabilis; I F
O13300), Rhodopseudomonas spheroids (Rhodopseudomonas 5pher)
oides ; IFO12203), Flavobacterium aheolenos
um 5uaveolens ATCC958), Nocardia sp.
+4326), Mycobacterium rotochus (Myc
obacterium rhodochrous:
I F Ol 3161), Bacterium subgIanc
lis; IFO31322), Streptomyces alhydroflavus
albidoflavus IF 013010),
Pseud
ononas pseudoalcaligenes
, l F 014167), Pseudomonas earuginosa
; IFO3445), Acetobacter ascendens:
l F O3188), Acetobacter pasteurianus subsp.
er pasteurianus 5ubsp Io
vanienIFO! 3753), 7-7, Cybacter ox
ydans; ATCCl 4359), Arthrobacter au
IFOI 2136), Corynebacterium daltamicum
um glutamicum AT CC2+650
), sub-power romykopnos lipolyti-power (Sacch
allomycopsis 1ipolytica;
IF 01548), Talebnoella pneumoniae (
Klebsiella pneumoniae.
IFO3321)、ロドトルラ ミヌタ(Rhodot
orulaminuta; IFO1435)、バチル
ス セレウス(Bacillus cereus; I
F 0 13690 )、ミクロバクテリウムアンモ
ニアフィラムfJicrobacterium anm
oniaphilum; ATCC21490) 、パ
ラコツカス デニトリフィカンス(Paracoccu
s denitrificans ; r P 0 1
2442)、セラチア マルセセンス(Serrati
a marcescens; IFO3046)、ブレ
ビバクテリウム ラクトファメンタム(Breviba
cterium lactofermentum A
TCC13655,)、ブレビバクテリウム フラバム
(Brevibacterium flavum; A
T CC21269)、ブレビバクテリウム アンモニ
アゲネス(Brevibacteriumar+IIo
niagenes ; I F OI 2072 )
、エンエリヒアコリ(Escherichia col
i ; I F O3301)、ミクロコツカス ロゼ
ウス(Micrococcus roseus I F
0 3764)等がある。IFO3321), Rhodotorula minuta (Rhodot
orulaminuta; IFO1435), Bacillus cereus (I
F 0 13690), Microbacterium ammoniaphyllum fJicrobacterium amm
oniaphilum; ATCC21490), Paracoccus denitrificans (Paracoccu
s denitrificans ; r P 0 1
2442), Serrati marcescens
a marcescens; IFO3046), Brevibacterium lactofamentum (Breviba
cterium lactofermentum A
TCC13655, ), Brevibacterium flavum (A
T CC21269), Brevibacterium ammoniagenes (Brevibacterium+IIo
niagenes; IFOI 2072)
, Escherichia col
i; I F O3301), Micrococcus roseus I F
0 3764) etc.
勿論、本発明ではこれらのみに限定されるものではない
。Of course, the present invention is not limited to these.
上記、微生物を培養するための培地としては炭素源、窒
素源等を含有し微生物か生育するものであればいずれで
も良い。As the medium for culturing the microorganisms mentioned above, any medium may be used as long as it contains a carbon source, a nitrogen source, etc. and allows the microorganisms to grow.
炭素源としては、微生物のもつソルビン酸生産活性を阻
害しない化合物であれば任意に使用でき、例えばグルコ
ース、ンユークロース、エタノール、エヂレンクリコー
ル、プロピレングリコール、■、4〜ブタンジオール、
グリセリン、アセトアルデヒド、酢酸、プロピオン酸t
とが挙げられる。又、窒素源としては肉エキス、ペプト
ン、コーンステイープリカー、尿素、硫酸アンモニウム
、塩化アンモニウム、硝酸ナトリウムなどを用いること
が出来る。更に、必要に応じてリン酸塩、マグネシウム
塩、カルシウム塩、鉄塩、銅塩、亜鉛塩などの無機塩類
や微生物の生育に必要な栄養物質を培地に適宜加えるこ
とができる。As a carbon source, any compound that does not inhibit the sorbic acid production activity of microorganisms can be used, such as glucose, nuclose, ethanol, ethylene glycol, propylene glycol, 4-butanediol,
Glycerin, acetaldehyde, acetic acid, propionic acid t
Examples include. Further, as the nitrogen source, meat extract, peptone, cornstarch liquor, urea, ammonium sulfate, ammonium chloride, sodium nitrate, etc. can be used. Furthermore, inorganic salts such as phosphates, magnesium salts, calcium salts, iron salts, copper salts, zinc salts, and other nutritional substances necessary for the growth of microorganisms can be added to the medium as necessary.
ソルブアルデヒドを酸化処理するに当たっては、上記記
載により得られた微生物を用い、EDTA又はアスコル
ビン酸又はSH基を持つアルコール類、アミノ酸類、若
しくはペプチド類から選ばれるSH基保護剤の少なくと
も一種を反応系に共存させて行う。SH基保護剤のうち
S H基を持つアルコール類としてはノチオスレイトー
ル、2−メルカプトエタノール等が挙げられ、S H基
を持つアミノ酸類としてはノスティノ等か、又SH基を
持つペプチド類としては還元型グルタチオン等が例示さ
れる。該SH基保護剤は上記記載の増殖した微生物を含
む培地に共′#−させても、又、−旦該培地から集菌し
、これを水或は生理食塩水、バッファーに懸濁し1ニも
のに共存させても良い。In oxidizing sorbaldehyde, the microorganism obtained as described above is used, and at least one SH group protecting agent selected from EDTA, ascorbic acid, or SH group-containing alcohols, amino acids, or peptides is added to the reaction system. This is done by coexisting with the Among SH group protecting agents, examples of alcohols having an SH group include notiothreitol, 2-mercaptoethanol, etc., examples of amino acids having an SH group include nostino, and examples of peptides having an SH group include nostino, etc. Examples include reduced glutathione. The SH group-protecting agent can be used together with a medium containing the grown microorganisms described above, or it can be collected from the medium and suspended in water, physiological saline, or buffer for one day. It is okay to let things coexist.
ソルブアルデヒドは系中濃度がOI〜100ミリモル、
好ましくは05〜50ミリモル程度の範囲で添加され、
又、該SH基保護剤の系中濃度は003〜30ミリモル
、好ましくは006〜IOミリモル程度の範囲が適して
いる。仕込み方法はいずれも一括、分割、連続等任意に
変更可能であるが、実用上は一括が有利である。The concentration of sorbaldehyde in the system is OI ~ 100 mmol,
It is preferably added in a range of about 05 to 50 mmol,
The concentration of the SH group protecting agent in the system is suitably in the range of about 0.003 to 30 mmol, preferably about 0.006 to IO mmol. The preparation method can be arbitrarily changed such as batch, divided, continuous, etc., but batch is advantageous in practice.
菌体は反応液lρ当たり0.5〜209(乾燥菌)程度
用いられる。Approximately 0.5 to 209 (dry bacteria) cells are used per 1 ρ of the reaction solution.
反応時には撹拌を行い好気的条件を採用する。かかる条
件に設定するには系内に空気や酸素或は必要に応じて他
のガスを混合した混合ガスを吹き込むか、溶液中の酸素
濃度をI ppm以上とするのか望ましい。During the reaction, stir and use aerobic conditions. In order to set such conditions, it is preferable to blow air, oxygen, or a mixed gas containing other gases as necessary into the system, or to set the oxygen concentration in the solution to I ppm or more.
反応温度は10〜70℃好ましくは20〜40℃、反応
時間は01〜200時間程度時間開か有利である。The reaction temperature is preferably 10 to 70°C, preferably 20 to 40°C, and the reaction time is advantageously about 01 to 200 hours.
又、反応液へ必要に応してPQQやSAD (P)等の
補酵素、界面活性剤、有機溶媒等を適宜添加することも
可能である。Furthermore, it is also possible to appropriately add coenzymes such as PQQ and SAD (P), surfactants, organic solvents, etc. to the reaction solution as necessary.
更に、反応は増殖期の微生物を用【)る培養法と休止菌
体による反応を組合せたり、他の固定化菌体、菌体抽出
処理物を用いる反応を単独もしくは上記方法と組合ゼて
行う等種々の態様か可能である。Furthermore, the reaction can be carried out by combining a culture method using microorganisms in the growth phase with a reaction using resting microorganisms, or by using other immobilized microorganisms or a reaction using a microorganism extract, either alone or in combination with the above methods. etc., various aspects are possible.
反応終了後、ソルビン酸を常法に従って精製し、目的物
を得る。After the reaction is completed, sorbic acid is purified according to a conventional method to obtain the desired product.
[作 用]
本発明は、ソルブアルデヒトを微生物により酸化してソ
ルビン酸を製造するに当たり、系中にエチレンジアミン
四酢酸又はアスコルビン酸又はメルカプト基を持つアル
コール類、アミノ酸類、若しくはペプチド類から選ばれ
るメルカプト基保護剤の少なくとも一種を共存させるこ
とにより、微生物内のメルカプト酵素に対するソルビン
酸の悪影響を軽減し、微生物の酸化活性を長期安定化し
てソルビン酸の収率を向上さける二とが出来る。[Function] In producing sorbic acid by oxidizing sorbaldehyde with microorganisms, the present invention uses ethylenediaminetetraacetic acid, ascorbic acid, or mercapto selected from alcohols, amino acids, or peptides having a mercapto group in the system. By coexisting at least one type of group protecting agent, it is possible to reduce the adverse effect of sorbic acid on the mercapto enzyme in the microorganism, stabilize the oxidation activity of the microorganism over a long period of time, and improve the yield of sorbic acid.
「実施例] 次に実施例を挙げて本発明を更に詳しく説明する。"Example] Next, the present invention will be explained in more detail with reference to Examples.
実施例1〜5
普通栄養培地(肉エキス39、ペプトン109、食塩5
り、水1σ、PH7)50m(!を坂ロフラスコにとり
滅菌処理後、アセトバクター アセンデンス(IFO3
188)を1白金耳接種して37℃、24時間往復振と
う培養した。Examples 1 to 5 Ordinary nutrient medium (meat extract 39, peptone 109, salt 5
water, 1σ, PH7) 50m (!) was placed in a Sakalo flask, and after sterilization, Acetobacter ascendens (IFO3
188) was inoculated into one platinum loop and cultured at 37°C for 24 hours with reciprocal shaking.
培養後、遠心分離法により集菌し、PH7,0,0,1
Mリン酸バッファーで洗浄して、乾燥換算で901の菌
体を得た。After culturing, collect the bacteria by centrifugation and adjust the pH to 7,0,0,1.
After washing with M phosphate buffer, 901 bacterial cells were obtained in dry terms.
次に大型試験管に乾燥換算で601の菌体を入れ、PH
7,0,0,1Mリン酸バッファーをIOm(加えて菌
体を懸濁した後、表1に示すメルカプト基保護剤を所定
量添加し、続いてソルブアルデヒドを10m9添加して
反応を開始した。Next, put 601 bacterial cells on a dry basis into a large test tube and adjust the pH.
After adding IOm of 7,0,0,1M phosphate buffer and suspending the bacterial cells, a predetermined amount of the mercapto group protecting agent shown in Table 1 was added, and then 10m9 of sorbaldehyde was added to start the reaction. .
反応は30℃で20分間行い、I分M?こ200回往復
振とうして反応液を撹拌した。反応終了後、遠心分離法
によって反応液の上澄み液を分取し、これを塩酸でPH
2とし1このち、ガスクロマド分析法にて消費したソル
ブアルデヒドに対するソルビン酸の収率を測定した。The reaction was carried out at 30°C for 20 minutes and I min M? The reaction solution was stirred by shaking back and forth 200 times. After the reaction is complete, separate the supernatant of the reaction solution by centrifugation, and pH it with hydrochloric acid.
2 and 1 Thereafter, the yield of sorbic acid relative to the consumed sorbaldehyde was measured by gas chromad analysis.
結果をまとめて表1に示す。The results are summarized in Table 1.
尚、ガスクロマド9叶の条件は次の通りである。The conditions for Gas Chromado 9 leaves are as follows.
装 置、ヒコーレノト パソカート 5890型力
ラム、メチルノリコン系ワイドボアカラム0.53mm
x I 5mx 8.0μmカラム濃変、80℃、8分
〜昇温(15°C/分)〜210℃、4分
ヘリウム流量+20m(+/分
検 出;FID
実施例6〜II
実施例1において、表2に示す菌株及びメルカプト基保
護剤に変更した以外は実施例1と同様の操作を行った。Equipment, Hikorenoto Paso Cart Model 5890
Ram, Methyl Noricon wide bore column 0.53mm
x I 5 m x 8.0 μm column concentration, 80°C, 8 minutes ~ temperature increase (15°C/min) ~ 210°C, 4 minutes Helium flow rate +20m (+/min detection; FID Examples 6 to II Example 1 The same operations as in Example 1 were performed except that the strain and mercapto group protecting agent shown in Table 2 were changed.
結果を表2に示す。The results are shown in Table 2.
対照例1
実施例Iにおいてメルカプト基保護剤を共存させずに実
施例1と同様の操作を行った結果、消費し1ニソルブア
ルデヒドに対するソルビン酸の収率は47%に低下した
。Control Example 1 In Example I, the same operation as in Example 1 was carried out without the coexistence of a mercapto group protecting agent, and as a result, the yield of sorbic acid per 1 consumed nisorbaldehyde decreased to 47%.
[効 果]
本発明においては、ソルブアルデヒドを微生物で酸化し
てソルビン酸を製造するに当たり、系中にエチレンジア
ミン四酢酸又はアスコルビン酸又はメルカプト基を持つ
アルコール類、アミノ酸類、若しくはペプチド類から選
ばれるメルカプト基保護剤の少なくとも一種を共存させ
て反応を行うことにより、微生物内のメルカプト酵素に
対するソルビン酸の悪影響を軽減し、微生物の酸化活性
を長期安定化してソルビン酸の収率を向上できるので、
産業上極めて有用である。[Effect] In the present invention, in producing sorbic acid by oxidizing sorbaldehyde with microorganisms, sorbic acid selected from ethylenediaminetetraacetic acid, ascorbic acid, or alcohols, amino acids, or peptides having a mercapto group in the system is used. By carrying out the reaction in the presence of at least one type of mercapto group protecting agent, it is possible to reduce the adverse effect of sorbic acid on the mercapto enzyme in microorganisms, stabilize the oxidation activity of microorganisms over a long period of time, and improve the yield of sorbic acid.
It is extremely useful in industry.
Claims (1)
酸を製造するに当たり、系中にエチレンジアミン四酢酸
又はアスコルビン酸又はメルカプト基を持つアルコール
類、アミノ酸類、若しくはペプチド類から選ばれるメル
カプト基保護剤の少なくとも一種を共存させることを特
徴とするソルビン酸の製造方法。 2、メルカプト基を持つアルコール類としてジチオスレ
イトール、2−メルカプトエタノールを使用することを
特徴とする請求項1記載の製造方法。 3、メルカプト基を持つアミノ酸類としてシステインを
使用することを特徴とする請求項1記載の製造方法。 4、メルカプト基を持つペプチド類として還元型グルタ
チオンを使用することを特徴とする請求項1記載の製造
方法。[Claims] 1. In producing sorbic acid by oxidizing sorbaldehyde with microorganisms, ethylenediaminetetraacetic acid or ascorbic acid or mercapto selected from alcohols, amino acids, or peptides having a mercapto group in the system is used. A method for producing sorbic acid, which comprises coexisting at least one type of group protecting agent. 2. The manufacturing method according to claim 1, characterized in that dithiothreitol and 2-mercaptoethanol are used as the alcohol having a mercapto group. 3. The production method according to claim 1, characterized in that cysteine is used as the amino acid having a mercapto group. 4. The production method according to claim 1, characterized in that reduced glutathione is used as the peptide having a mercapto group.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18914090A JPH0475588A (en) | 1990-07-17 | 1990-07-17 | Production of sorbic acid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP18914090A JPH0475588A (en) | 1990-07-17 | 1990-07-17 | Production of sorbic acid |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0475588A true JPH0475588A (en) | 1992-03-10 |
Family
ID=16236085
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP18914090A Pending JPH0475588A (en) | 1990-07-17 | 1990-07-17 | Production of sorbic acid |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0475588A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1736550A1 (en) * | 2005-06-22 | 2006-12-27 | Adorkem Technology SpA | Chemoenzymatic process for the synthesis of escitalopram |
-
1990
- 1990-07-17 JP JP18914090A patent/JPH0475588A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1736550A1 (en) * | 2005-06-22 | 2006-12-27 | Adorkem Technology SpA | Chemoenzymatic process for the synthesis of escitalopram |
WO2006136521A1 (en) * | 2005-06-22 | 2006-12-28 | Adorkem Technology Spa | Chemoenzymatic process for the synthesis of escitalopram |
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