JPH022597B2 - - Google Patents

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Publication number
JPH022597B2
JPH022597B2 JP56209983A JP20998381A JPH022597B2 JP H022597 B2 JPH022597 B2 JP H022597B2 JP 56209983 A JP56209983 A JP 56209983A JP 20998381 A JP20998381 A JP 20998381A JP H022597 B2 JPH022597 B2 JP H022597B2
Authority
JP
Japan
Prior art keywords
enzyme
threonine
reaction
solution
glycine
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 - Lifetime
Application number
JP56209983A
Other languages
Japanese (ja)
Other versions
JPS58116690A (en
Inventor
Hideaki Yamada
Teruzo Myoshi
Masaaki Kato
Masahisa Ikemi
Haruo Gomi
Yoshiaki Ishimatsu
Noriaki Koizumi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP56209983A priority Critical patent/JPS58116690A/en
Publication of JPS58116690A publication Critical patent/JPS58116690A/en
Publication of JPH022597B2 publication Critical patent/JPH022597B2/ja
Granted legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Enzymes And Modification Thereof (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Description

【発明の詳现な説明】[Detailed description of the invention]

本発明は新芏な酵玠を甚いた−β−ヒドロキ
シアミノ酞の補造法に関する。 近幎皮々の−アミノ酞が発芋されるにしたが
぀お、その生理的意矩が解明され぀぀あり、−
アミノ酞は抗生物質、酵玠阻害剀等の各皮の医
薬、蟲薬類、その他の生理掻性物質の合成原料ず
しお有甚なものが倚い。そしおこれら−アミノ
酞は䞀郚は合成法で補造されたDL−アミノ酞を
光孊分割しお補造されおいるが、倚くは−アミ
ノ酞を䞀旊ラセミ化しおから光孊分割しお補造さ
れおいる。その堎合、−アミノ酞は長い工皋を
経お補造されるために、その手間が倧倉であり、
たた収率も極めお䜎くな぀おいた。 本発明者らは−アミノ酞の特定のものに぀い
お、安䟡で倧量に生産されおいるグリシンずアル
デヒド類から䞀挙に補造する新芏な技術を開発し
た。すなわち、新芏な酵玠である−スレオニン
アルドラヌれを甚いおグリシンずアルデヒドから
䞀挙に察応する−β−ヒドロキシアミノ酞を補
造する方法を開発したのである。これたで、−
スレオニンをグリシンずアセトアルデヒドに分解
する−スレオニンアルドラヌれE.C.4.1.2.5
を甚いおグリシンずアルデヒド類から察応する
−β−ヒドロキシアミノ酞を補造しうるこずは知
られおいる。しかしながら、−β−ヒドロキシ
アミノ酞に぀いおは、その補造の前提ずなる−
スレオニンアルドラヌれの存圚自䜓が党く知られ
おいない。本発明者らは、たたたた特定の埮生物
がこの−スレオニンアルドラヌれを産生しうる
こずを知り、曎に研究を進めた結果この酵玠を甚
いればグリシンずアルデヒド類から察応する−
β−ヒドロキシアミノ酞を䞀挙に補造しうるこず
を芋出しおこれに基いお本発明を完成した。 すなわち本発明は、グリシンず䞀般匏−
CHO䜆し、は氎玠たたは飜和アルキル基を衚
わす。で瀺されるアルデヒド化合物ずを−ス
レオニンアルドラヌれの存圚で反応させるこずを
特城ずする䞀般匏 䜆し、は氎玠たたは飜和アルキル基を衚わ
す。 で瀺される−β−ヒドロキシアミノ酞の補造法
に関するものである。 −スレオニンアルドラヌれは−スレオニン
に䜜甚しおグリシンずアルデヒドに分解する酵玠
で、䟋えばアルカリゲネス・パカリス
Alcaligenes faecalisIFO12669、シナヌドモ
ナスPseudomonasDK−埮工研菌寄第6200
号、およびアリスロバクタヌArthrobacter
DK−19埮工研菌寄第6201号などがこの−スレ
オニンアルドラヌれを産生する胜力を有する。 シナヌドモナスDK−埮工研菌寄第6200号お
よびアリスロバクタヌDK−19埮工研菌寄第6201
号の菌孊的性質を次に瀺す。 (a) 圢態
The present invention relates to a method for producing D-β-hydroxyamino acids using a novel enzyme. As various D-amino acids have been discovered in recent years, their physiological significance is being clarified, and D-
Many amino acids are useful as raw materials for the synthesis of various medicines such as antibiotics and enzyme inhibitors, agricultural chemicals, and other physiologically active substances. Some of these D-amino acids are produced by optically resolving DL-amino acids produced by synthetic methods, but most of them are produced by optically resolving L-amino acids after racemizing them. In that case, D-amino acids are manufactured through a long process, which requires a lot of effort.
Moreover, the yield was also extremely low. The present inventors have developed a new technique for producing specific D-amino acids all at once from glycine and aldehydes, which are produced at low cost and in large quantities. That is, they developed a method for producing the corresponding D-β-hydroxyamino acid from glycine and aldehyde all at once using D-threonine aldolase, a novel enzyme. Until now, L-
L-threonine aldolase (EC4.1.2.5), which breaks down threonine into glycine and acetaldehyde
From glycine and aldehydes using
It is known that -β-hydroxy amino acids can be produced. However, regarding D-β-hydroxyamino acids, D-
The existence of threonine aldolase itself is completely unknown. The present inventors happened to know that a specific microorganism can produce this D-threonine aldolase, and as a result of further research, we found that using this enzyme, we can convert glycine and aldehydes into corresponding D-
The present invention was completed based on the discovery that β-hydroxyamino acids can be produced all at once. That is, the present invention provides glycine and the general formula R-
A general formula characterized by reacting an aldehyde compound represented by CHO (wherein R represents hydrogen or a saturated alkyl group) in the presence of D-threonine aldolase (However, R represents hydrogen or a saturated alkyl group.) This relates to a method for producing a D-β-hydroxyamino acid represented by the following formula. D-threonine aldolase is an enzyme that acts on D-threonine and decomposes it into glycine and aldehyde.
No., and Arthrobacter
DK-19 Microtech Research Institute No. 6201 has the ability to produce this D-threonine aldolase. Pseudomonas DK-2 FEK No. 6200 and Arylobacter DK-19 FEK No. 6201
The mycological properties of this issue are shown below. (a) Form

【衚】 (b) 各培地における生育状態【table】 (b) Growth status in each medium

【衚】 (c) 生理孊的性質【table】 (c) Physiological properties

【衚】【table】

【衚】 以䞊の菌孊的性質をもずに「バヌゞ゚ヌズ・マ
ニナアル・オブ・デタヌミネむテむブ・バクテリ
オロゞヌ第版1974」を参照しお分類するず、
DK−菌はグラム陰性の桿菌で極鞭毛を有し、
オキシダヌれ陜性、脱窒反応陜性であるずころか
らシナヌドモナス属に属するものず同定した。䞀
方、DK−19菌はグラム染色性が匱い桿菌で、倚
圢性及び呚毛を有し、糖類を資化できないこずか
らアリスロバクタヌ属に属するものず同定した。 −スレオニンアルドラヌれは䟋えばこれらの
埮生物を栄逊培地に培逊すれば生成させるこずが
できる。栄逊培地は现菌を培逊する通垞のもので
よく、炭玠源ずしおはグリコヌス、キシロヌス、
グリセロヌル、糖蜜等の糖類、あるいは酢酞、リ
ンゎ酞等の有機酞など、窒玠源ずしおは硫酞アン
モニりム、塩化アンモニりム、尿玠など、有機栄
逊源ずしお酵母゚キス、ペプトン、肉゚キス、コ
ヌンステむヌプリカヌなど、そしお無機むオンず
しおマグネシりム、鉄、マンガン、カリりム、リ
ン酞塩などを含むものを甚いる。 培逊方法も现菌を培逊する垞法に埓぀お行なえ
ばよく、培地のPHを〜10ずしお菌を接皮埌20〜
60℃で〜日間奜気的に培逊すればよい。 このようにしお−スレオニンアルドラヌれは
䞻に菌䜓内に生成蓄積されるが、反応に䟛する酵
玠源ずしおはこの菌䜓そのものを甚いおもよく、
又菌䜓から−スレオニンアルドラヌれを単離・
粟補する過皋のいかなる段階のものを甚いおもよ
い。培逊液から−スレオニンアルドラヌれを単
離する堎合にはたず菌䜓を機械的方法、酵玠凊理
する方法、自己溶解法などの公知の方法の方法に
よ぀お砎壊し粗抜出液を埗る。それから、この粗
抜出液を硫安沈柱、アセトン又ぱタノヌルなど
による溶媒沈柱、DEAE−セフアロヌス、DEAE
−セフアデツクス、リン酞カルシりムゲル等の
皮々のむオン亀換䜓や吞着剀を甚いたクロマトグ
ラフむヌなどを適宜組合せお粟補するこずによ぀
お高玔床の酵玠暙品を埗るこずができる。本酵玠
の掻性発珟には、補助酵玠ずしおピリドキサヌル
−5′−リン酞を必芁ずするため、反応時には通垞
10-3〜10-5Mで存圚させる。 次に、酵玠補造䟋で埗られた酵玠暙品に぀い
お理化孊的性質を枬定した結果を蚘す。 䜜甚および基質特異性 本酵玠は−スレオニンおよび−アロスレ
オニンを分解しおグリシンずアセトアルデヒド
を生成する。䞀方、−スレオニンおよび−
アロスレオニンにはた぀たく䜜甚しない。 至適PH −スレオニンを基質ずしお各PHにおいお30
℃で10分間反応させ、生成したアルデヒドを定
量したずころ、本酵玠の至適PHは〜にあ぀
た。尚、甚いた緩衝剀はPH〜7.5たでは0.1M
リン酞緩衝液、PH〜たでは0.1Mトリス−
HCl緩衝液及びPH〜11たでは0.1M炭酞゜ヌ
ダ緩衝液である。 安定PH範囲 酵玠溶液を各PHにおいお30℃で時間加枩
埌、溶液䞭の残存掻性を枬定したずころ、本酵
玠の安定PH範囲は〜にあ぀た。尚、甚いた
緩衝液はPH〜7.5たでは0.1Mリン酞緩衝液、
PH〜たでは0.1Mトリス−HCl緩衝液及び
PH〜11たでは0.1M炭酞゜ヌダ緩衝液である。 力䟡の枬定法 酵玠含有液0.1mlを100ÎŒmoleの−スレオニ
ンを含有するPH8.0の0.1Mトリス−塩酞緩衝液
0.9mlに加え、30℃で10分間加枩しお生成した
アセトアルデヒドをPaz法〔Arch.Biochem.
Biophys.、Vol.109、p5481965〕によ぀お定
量しお求めた。尚、分間に1ÎŒmoleの−ス
レオニンを分解する酵玠掻性を1Uずした。 䜜甚適枩の範囲 −スレオニンを基質ずしおPH8.0の0.1Mト
リス−塩酞緩衝液を甚い、各枩床で10分間反応
させ、生成したアセトアルデヒドを枬定したず
ころ、本酵玠の至適枩床は50〜50℃にあ぀た。 熱安定性 PH8.0の0.1Mトリス−塩酞緩衝液に溶解した
酵玠溶液を各枩床で時間加熱埌、溶液䞭の残
存掻性を枬定したずころ、本酵玠の安定枩床は
40℃以䞋であ぀た。 PH、枩床などによる倱掻の条件 本酵玠はPH以䞋、PH11以䞊、および枩床70
℃以䞊では時間に倱掻する。 阻害、掻性化および安定化 本酵玠はメルカプト゚タノヌル、亜硫酞ナト
リりム、亜硫酞氎玠ナトリりム、ゞチオスレむ
トヌル、Mn2+、Co2+、Fe2+、Mg2+によ぀お
掻性化され安定化される。䞀方、Ag1+、Cu2+、
Hg2+、Zn2+、Pd2+、ヒドロキシルアミン、
−クロルマヌキナリヌ安息銙酞によ぀お阻害さ
れる。 補酵玠 本酵玠の補酵玠はピリドキサヌル−5′−リン
酞である。 酵玠補造䟋で埗られた酵玠は以䞊のような理
化孊的性質を有しおいるが、埓来知られおいるス
レオニンアルドラヌれはすべお−スレオニンを
分解するものであ぀お−スレオニンを分解する
ものは党く知られおいないずころから、この酵玠
は党く新しい䜜甚を有する新芏酵玠である。 グリシンずアルデヒド化合物の反応に甚いる酵
玠は、芁は−スレオニンを分解しおグリシンず
アセトアルデヒドを生成しうるものであればよ
い。たた、この酵玠は酵玠掻性を発揮しうる圢態
であればたり、単離された圢に限定されるもので
はない。埓぀お、半粟補品でもよく、粗抜出液、
さらには培逊物、生菌䜓、凍結也燥菌䜓、アセト
ン也燥菌䜓、あるいはこれらの菌䜓の磚砕物等で
あ぀おもよい。さらに、酵玠自䜓あるいは菌䜓の
たた公知の手段で固定化しお甚いおもよい。−
スレオニンアルドラヌれは前述のような埮生物由
来のものに限定されず、他の動怍物由来のもので
あ぀おもよい。 アルデヒド化合物は䞀般匏−CHOのうち
が氎玠たたは飜和アルキル基のものである。炭玠
数は20以䞋のものが奜たしく、䟋えばホルムアル
デヒド、アセトアルデヒド、プロピオンアルデヒ
ド、ブチルアルデヒド、ラりリルアルデヒドなど
が奜適である。 反応は、芁は−スレオニンアルドラヌれずグ
リシンずアルデヒド化合物ずを混合すればよく、
添加の順序は問わない。アルデヒド化合物は酵玠
掻性を著しく阻害しない皋床であればよいが、
0.05〜0.2モル皋床が奜たしい。グリシンは
アルデヒド化合物ず等モル皋床でよいが、グリシ
ンの反応収率を高めるためにはアルデヒド化合物
より少なくするのがよい。反応枩床は10〜70℃䜍
でよいが10〜40℃皋床が奜適である。反応時のPH
は〜9.5皋床奜たしくは、〜に維持するの
がよい。補酵玠ずしお、ピリドキサヌル−5′−リ
ン酞を反応系に添加するず酵玠掻性を高めお反応
を促進させるこずができる。反応はバツチ方匏で
行な぀おもよく、連続方匏で行な぀おもよい。か
くしお、反応は〜50時間皋床で終了する。 反応終了埌は、必芁により遠心分離、過等で
懞濁物を陀去しおから、むオン亀換暹脂凊理、晶
析等で粟補し、掻性炭等で脱色しおこの脱色液を
濃瞮するこずによ぀お−β−ヒドロキシアミノ
酞を単離するこずができる。 次に、酵玠補造䟋を瀺す。なお、は党お重量
である。 酵玠補造䟋  ポリペプトン0.5、酵母゚キス0.5、
KH2PO40.1、MgSO40.05、−グルタミン
酾0.1、および−スレオニン0.1からなるPH
7.5の培地を調補し、容の培逊槜にその
を投入しお120℃で15分間加熱殺菌した。この培
地にアリスロバクタヌDK−19埮工研菌寄第6201
号を接皮し、PH7.5に保ちながら30℃で20時間通
気および撹拌をし぀぀培逊した。 培逊終了埌、培逊液から菌䜓を遠心分離
し、生理食塩氎で回掗滌埌、この湿菌䜓を0.1
ピリドキサヌル−5′−リン酞及び10メル
カプト゚タノヌルを含むPH7.5の0.1Mトリス−塩
酞緩衝液100ml䞭に懞濁した。この菌䜓懞濁液を
20KHzで10分間超音波凊理しお菌䜓を砎壊しおか
ら遠心しお傟瀉し105mlの粗酵玠抜出液を埗た。 埗られた粗酵玠抜出液に硫安を加えお0.3〜0.5
飜和区分を分取し、この区分を䞊蚘緩衝液に察し
お晩透析した。DEAEセフアデツクス−50
100mlを充填し、前蚘の緩衝液で予め平衡化しお
おいたカラムに透析残液を通液しお酵玠を吞着さ
せた埌、塩化ナトリりム溶液を0.1〜0.4Mたで濃
床を倉えおカラムに通液し、溶液の各フラクシペ
ンのうち−スレオニンアルドラヌれ掻性区分を
集めた。この掻性区分は塩化ナトリりムの濃床が
0.3Mの付近にあ぀た。集めた掻性区分をセフア
デツクス−200 200mlを充填したカラムに通液
しおゲル過を行ない、−スレオニンアルドラ
ヌれ掻性区分を集め、メムブラムフむルタヌで濃
瞮し、酵玠濃瞮液15mlを埗た。この酵玠液䞭のタ
ンパク含量は2.4mgで−スレオニンに察す
る比掻性は1.24Umgであり、−アロスレオニ
ンに察する比掻性は3.33Umgであ぀た。䞀方、
−スレオニンおよび−アロスレオニンに察し
おは党く掻性を瀺さなか぀た。 酵玠補造䟋  シナヌドモナスDK−埮工研菌寄第6201号お
よびアルカリゲネス・パカリスIFO12669を甚
い、いずれも酵玠補造䟋ず同じ培地に同様に培
逊し、培逊液から酵玠を分離したずころシナヌド
モナスDK−菌の堎合にはタンパク質濃床2.3
mgmlの酵玠液12mlが、そしおアルカリゲネス・
パカリス菌の堎合には、タンパク質濃床2.1
mgmlの酵玠液11mlが埗られた。この酵玠掻性を
枬定したずころ、前者は−スレオニンに察する
比掻性が1.01Umgであり、−アロスレオニン
に察する比掻性が2.96Umgであ぀た。䞀方、埌
者のそれは−スレオニンに察する比掻性が
0.86Umgであり、−アロスレオニンに察する
比掻性が2.95Umgであ぀た。そしお、いずれも
−スレオニンおよび−アロスレオニンに察し
おは党く掻性を瀺さなか぀た。 以䞋、実斜䟋を瀺す。なお、生成物の定量およ
びスレオ䜓アロ䜓比は、−ブタノヌルメチ
ル゚チルケトン25アンモニア氎比が
の混合物を展開溶媒ずしおペヌパヌクロマトグ
ラフむヌを行ない、ニンヒドリンで発色させおス
ポツトを切りずり、硝酞銅を0.005含むメタノ
ヌルで抜出し、比色定量しお求めた。 実斜䟋  酵玠補造䟋およびず同様に培逊しお埗られ
たアルカリゲネスパカリスIFO12669、シナヌ
ドモナスDK−埮工研菌寄第6200号、およびア
リスロバクタヌDK−19埮工研菌寄第6201号の培
逊液各mlを遠心分離しお菌䜓を集め、いずれも
0.9食塩氎を加えお掗浄する操䜜を回繰返し
た。 各掗滌菌䜓にグリシン200ÎŒmole、アセトアル
デヒド200ÎŒmole、およびPH8.0の0.1Mトリス−塩
酞緩衝液mlよりなる基質溶液を加え30℃で20時
間反応させた。 反応終了埌、溶液䞭の−スレオニンおよび
−アロスレオニンを定量したずころ䞋衚に瀺す劂
き結果が埗られた。
[Table] Based on the above mycological properties, the classification is based on the ``Bergey's Manual of Determinative Bacteriology, 8th edition (1974)''.
DK-2 bacterium is a Gram-negative bacillus with polar flagella.
It was identified as belonging to the genus Pseudomonas because it was positive for oxidase and denitrification. On the other hand, the DK-19 bacterium was identified as belonging to the genus Arilobacter because it is a bacillus with weak Gram staining, is pleomorphic, has pericytium, and cannot assimilate sugars. D-threonine aldolase can be produced, for example, by culturing these microorganisms in a nutrient medium. The nutrient medium may be a normal one for culturing bacteria, and the carbon source may be glycose, xylose,
Sugars such as glycerol and molasses, or organic acids such as acetic acid and malic acid; nitrogen sources such as ammonium sulfate, ammonium chloride, and urea; organic nutritional sources such as yeast extract, peptone, meat extract, and cornstarch liquor; and inorganic sources. Ions containing magnesium, iron, manganese, potassium, phosphate, etc. are used. The culture method can be carried out according to the conventional method for culturing bacteria, and the pH of the medium should be set at 4 to 10, and after inoculating the bacteria,
It may be cultured aerobically at 60°C for 1 to 3 days. In this way, D-threonine aldolase is mainly produced and accumulated within the bacterial body, but the bacterial body itself may also be used as the enzyme source for the reaction.
In addition, D-threonine aldolase was isolated from bacterial cells.
It may be used at any stage of the purification process. When D-threonine aldolase is isolated from a culture solution, the bacterial cells are first disrupted by a known method such as a mechanical method, an enzyme treatment method, or an autolytic method to obtain a crude extract. Then, this crude extract is subjected to ammonium sulfate precipitation, solvent precipitation with acetone or ethanol, DEAE-Sepharose, DEAE
- Highly pure enzyme preparations can be obtained by purification using appropriate combinations of chromatography using various ion exchangers and adsorbents such as Cephadex and calcium phosphate gel. The activity of this enzyme requires pyridoxal-5'-phosphate as an auxiliary enzyme, so it is normally used during the reaction.
It is present at 10 -3 to 10 -5 M. Next, the results of measuring the physicochemical properties of the enzyme preparation obtained in Enzyme Production Example 1 will be described. Action and Substrate Specificity The enzyme decomposes D-threonine and D-allothreonine to produce glycine and acetaldehyde. On the other hand, L-threonine and L-
It has no effect on allothreonine. Optimal PH: 30 at each PH using D-threonine as a substrate
When the reaction was carried out at ℃ for 10 minutes and the aldehyde produced was quantified, the optimum pH of this enzyme was between 7 and 9. The buffer used was 0.1M for pH 4 to 7.5.
Phosphate buffer, 0.1M Tris for pH 7-9
HCl buffer and pH 9-11 are 0.1M sodium carbonate buffer. Stable PH Range After heating the enzyme solution at 30°C for 1 hour at each PH, the residual activity in the solution was measured, and the stable PH range of this enzyme was 6 to 9. The buffers used were 0.1M phosphate buffer for pH 4 to 7.5;
For pH 7 to 9, use 0.1M Tris-HCl buffer and
For pH 9 to 11, 0.1M sodium carbonate buffer is used. Measurement method for titer: Transfer 0.1 ml of enzyme-containing solution to 0.1 M Tris-HCl buffer with pH 8.0 containing 100 ÎŒmol of D-threonine.
0.9ml and heated at 30℃ for 10 minutes to generate acetaldehyde using the Paz method [Arch.Biochem.
Biophys., Vol. 109, p548 (1965)]. In addition, the enzyme activity that decomposes 1 ÎŒmole of D-threonine per minute was defined as 1 U. Suitable temperature range for action Using D-threonine as a substrate in 0.1M Tris-HCl buffer with a pH of 8.0, the reaction was carried out for 10 minutes at each temperature and the acetaldehyde produced was measured, and the optimum temperature for this enzyme was found to be 50-50. It was ℃. Thermostability After heating an enzyme solution dissolved in 0.1M Tris-HCl buffer at pH 8.0 for 1 hour at each temperature, the residual activity in the solution was measured, and the stable temperature of this enzyme was found to be
The temperature was below 40℃. Conditions for inactivation due to PH, temperature, etc. This enzyme is PH5 or lower, PH11 or higher, and temperature 70.
At temperatures above ℃, it becomes inactive within 1 hour. Inhibition, Activation and Stabilization The enzyme is activated and stabilized by mercaptoethanol, sodium sulfite, sodium bisulfite, dithiothreitol, Mn 2+ , Co 2+ , Fe 2+ , Mg 2+ . On the other hand, Ag 1+ , Cu 2+ ,
Hg 2+ , Zn 2+ , Pd 2+ , hydroxylamine, p
- Chlormercury is inhibited by benzoic acid. Coenzyme The coenzyme of this enzyme is pyridoxal-5'-phosphate. The enzyme obtained in Enzyme Production Example 1 has the above-mentioned physical and chemical properties, but all conventionally known threonine aldolases decompose L-threonine, but not D-threonine. Since it is completely unknown, this enzyme is a novel enzyme with a completely new action. The enzyme used for the reaction of glycine and an aldehyde compound may be any enzyme as long as it can decompose D-threonine to generate glycine and acetaldehyde. Furthermore, this enzyme is not limited to a form that can exhibit enzymatic activity, and is not limited to an isolated form. Therefore, semi-refined products may be used, crude extracts,
Furthermore, it may be a culture, live bacterial cells, freeze-dried bacterial cells, acetone-dried bacterial cells, or a ground product of these bacterial cells. Furthermore, the enzyme itself or the bacterial cells may be immobilized by known means and used. D-
Threonine aldolase is not limited to those derived from microorganisms as mentioned above, but may be derived from other animals or plants. The aldehyde compound is R in the general formula R-CHO.
is hydrogen or a saturated alkyl group. The number of carbon atoms is preferably 20 or less, and suitable examples include formaldehyde, acetaldehyde, propionaldehyde, butyraldehyde, and laurylaldehyde. The reaction can be carried out by mixing D-threonine aldolase, glycine, and an aldehyde compound.
The order of addition does not matter. The aldehyde compound may be used as long as it does not significantly inhibit enzyme activity.
The amount is preferably about 0.05 to 0.2 mol/degree. The amount of glycine may be about equimolar to that of the aldehyde compound, but in order to increase the reaction yield of glycine, it is preferable to use less than the amount of the aldehyde compound. The reaction temperature may be about 10 to 70°C, but preferably about 10 to 40°C. PH during reaction
is preferably maintained at about 6 to 9.5, preferably 7 to 8. When pyridoxal-5'-phosphate is added to the reaction system as a coenzyme, the enzyme activity can be increased and the reaction can be accelerated. The reaction may be carried out in batch mode or in continuous mode. Thus, the reaction is completed in about 5 to 50 hours. After the reaction is complete, if necessary, remove suspended matter by centrifugation, filtration, etc., then purify by ion exchange resin treatment, crystallization, etc., decolorize with activated carbon, etc., and concentrate this decolorized liquid. D-β-hydroxy amino acids can be isolated. Next, an example of enzyme production will be shown. Note that all percentages are by weight. Enzyme production example 1 Polypeptone 0.5%, yeast extract 0.5%,
PH consisting of KH2PO4 0.1 %, MgSO4 0.05%, L-glutamic acid 0.1%, and D-threonine 0.1%
Prepare the culture medium of 7.5 and place it in a 5 volume culture tank.
was added and heat sterilized at 120°C for 15 minutes. In this medium, Arylobacter DK-19
No. was inoculated and cultured at 30°C for 20 hours with aeration and stirring while maintaining the pH at 7.5. After culturing, centrifuge the cells from culture solution 1, wash once with physiological saline, and remove the wet cells at 0.1
The suspension was suspended in 100 ml of 0.1 M Tris-HCl buffer, pH 7.5, containing mM pyridoxal-5'-phosphate and 10 mM mercaptoethanol. This bacterial suspension
The bacterial cells were destroyed by ultrasonication at 20 KHz for 10 minutes, and then centrifuged and decanted to obtain 105 ml of crude enzyme extract. Add ammonium sulfate to the obtained crude enzyme extract to give a concentration of 0.3 to 0.5
The saturated fraction was separated and this fraction was dialyzed overnight against the above buffer. DEAE Cephadex A-50
Fill the column with 100 ml and equilibrate it with the above buffer before passing the dialysis residue through the column to adsorb the enzyme, then pass through the column with varying concentrations of sodium chloride solution from 0.1 to 0.4M. Then, the D-threonine aldolase activity fraction of each fraction of the solution was collected. This active category has a concentration of sodium chloride.
It was around 0.3M. The collected active fraction was passed through a column packed with 200 ml of Cephadex G-200 for gel filtration, and the D-threonine aldolase active fraction was collected and concentrated using a membrane filter to obtain 15 ml of an enzyme concentrate. The protein content in this enzyme solution was 2.4 mg/mg, the specific activity for D-threonine was 1.24 U/mg, and the specific activity for D-allothreonine was 3.33 U/mg. on the other hand,
It showed no activity against L-threonine and L-allothreonine. Enzyme Production Example 2 Using Pseudomonas DK-2 Microtechnical Research Institute No. 6201 and Alcaligenes haecalis IFO12669, both were cultured in the same medium as in Enzyme Production Example 1, and when the enzyme was separated from the culture solution, Pseudomonas DK- In the case of 2 bacteria, the protein concentration is 2.3
12 ml of enzyme solution of mg/ml and Alcaligenes
In the case of S. falciparum, the protein concentration is 2.1
11 ml of mg/ml enzyme solution was obtained. When the enzyme activity was measured, the former had a specific activity of 1.01 U/mg for D-threonine and 2.96 U/mg for D-allothreonine. On the other hand, the latter has a specific activity toward D-threonine.
The specific activity for D-allothreonine was 2.95 U/mg. In addition, none of them showed any activity against L-threonine and L-allothreonine. Examples are shown below. The quantitative determination of the product and the threo isomer/allo isomer ratio are as follows: t-butanol: methyl ethyl ketone: 25% ammonia water ratio: 4:3:
Paper chromatography was performed using the mixture of No. 1 as a developing solvent, color was developed with ninhydrin, a spot was cut out, extracted with methanol containing 0.005% copper nitrate, and determined by colorimetry. Example 1 Alcaligenes flycharis IFO12669, Pseudomonas DK-2 F.K. No. 6200, and Arylobacter DK-19 F.K. No. 6201 obtained by culturing in the same manner as in Enzyme Production Examples 1 and 2. Centrifuge 1 ml of each culture solution to collect bacterial cells.
The operation of adding 0.9% saline and washing was repeated twice. A substrate solution consisting of 200 Όmoles of glycine, 200 Όmoles of acetaldehyde, and 1 ml of 0.1M Tris-HCl buffer with pH 8.0 was added to each washed bacterial cell and allowed to react at 30° C. for 20 hours. After the reaction, D-threonine and D
- Allothreonine was quantified and the results shown in the table below were obtained.

【衚】 生成スレオニンが−䜓であ぀たこずは各菌ず
もスケヌルで反応させお確認した。すなわ
ち、反応液をH+型のDowex50WX8 500mlを充填
したカラムに通液し、氎掗埌0.2Nアンモニアで
溶離しおスレオニン区分ずグリシン区分に分離し
た。スレオニン区分を濃瞮埌掻性炭で脱色し、脱
色液に゚タノヌルを添加しお結晶を埗た。この結
晶に぀いおNMR、赀倖線吞収スペクトル、元玠
分析、および比旋光床を枬定しお、この結晶が
−スレオニンであるこずを確認した。 䞀方、各反応液に぀いおストレプト・コツカ
ス・パカリスIFO3181を甚いたバむオアツセむ
法で枬定し、反応液には−䜓が党く含たれおい
ないこずを確認した。 実斜䟋  アリスロバクタヌDK−19埮工研菌寄第6201号
の実斜䟋ず同じ培逊液を甚い、菌䜓を遠心分離
しお掗浄埌凍結也燥した。 䞋衚に瀺す各アルデヒド50mole、グリシン
50mole、およびPH8.0の0.1Mトリス−塩酞緩衝
æ¶²500mlよりなる基質溶液に䞊蚘の也燥菌䜓を
宛投入し、それぞれ30℃で40時間反応させた。 反応終了埌、溶液䞭の−β−ヒドロキシアミ
ノ酞定量した結果を䞋衚に瀺す。なお、スレオ
䜓アロ䜓の比は各溶液ずも玄1.6であ぀た。
[Table] It was confirmed that the threonine produced was D-form by reacting each bacteria on a single scale. That is, the reaction solution was passed through a column packed with 500 ml of H + type Dowex 50WX8, washed with water, and then eluted with 0.2N ammonia to separate the threonine fraction and the glycine fraction. After concentrating the threonine fraction, it was decolorized with activated carbon, and ethanol was added to the decolorized solution to obtain crystals. NMR, infrared absorption spectrum, elemental analysis, and specific rotation of this crystal were measured, and it was found that this crystal was D
-Confirmed to be threonine. On the other hand, each reaction solution was measured by a bioassay method using Streptococcus flycallis IFO3181, and it was confirmed that the reaction solution did not contain any L-form. Example 2 Using the same culture solution as in Example 1 of Arylobacter DK-19 FEK No. 6201, the bacterial cells were centrifuged, washed, and freeze-dried. 50 mmole of each aldehyde shown in the table below, glycine
50 mmole and 500 ml of 0.1 M Tris-HCl buffer with pH 8.0.
g each, and reacted at 30°C for 40 hours. After the reaction was completed, the amount of D-β-hydroxyamino acid in the solution was determined and the results are shown in the table below. The ratio of threo isomer to allo isomer was approximately 1.6 in each solution.

【衚】 実斜䟋  酵玠補造䟋で埗られた−スレオニンアルド
ラヌれ含有液mlにグリシン200ÎŒmole、アセト
アルデヒド200ÎŒmole、メルカプト゚タノヌル
100ÎŒmole、及びPH7.5の0.1Mトリス−塩酞緩衝液
mlよりなる基質液を加え30℃で10時間反応させ
た。反応終了埌−スレオニン及び−アロスレ
オニンを定量したずころ−スレオニン
85ÎŒmole、−アロスレオニン53ÎŒmoleであ぀
た。
[Table] Example 3 Add 200 ÎŒmole of glycine, 200 ÎŒmole of acetaldehyde, and mercaptoethanol to 2 ml of the D-threonine aldolase-containing solution obtained in Enzyme Production Example 1.
A substrate solution consisting of 100 Όmole and 5 ml of 0.1M Tris-HCl buffer with pH 7.5 was added and reacted at 30°C for 10 hours. After the completion of the reaction, D-threonine and D-allothreonine were quantified and found that D-threonine
The amount of D-allothreonine was 85 ÎŒmole and 53 ÎŒmole of D-allothreonine.

Claims (1)

【特蚱請求の範囲】  グリシンず䞀般匏−CHO䜆し、は氎玠
たたは飜和アルキル基を衚わす。で瀺されるア
ルデヒド化合物ずを−スレオニンアルドラヌれ
の存圚䞋で反応させるこずを特城ずする䞀般匏 䜆し、は氎玠たたは飜和アルキル基を衚わ
す。 で瀺される−β−ヒドロキシアミノ酞の補造
法。
[Claims] 1. A method characterized by reacting glycine with an aldehyde compound represented by the general formula R-CHO (where R represents hydrogen or a saturated alkyl group) in the presence of D-threonine aldolase. general formula (However, R represents hydrogen or a saturated alkyl group.) A method for producing a D-β-hydroxyamino acid represented by the following.
JP56209983A 1981-12-28 1981-12-28 Preparation of d-beta-hydroxyamino acid Granted JPS58116690A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56209983A JPS58116690A (en) 1981-12-28 1981-12-28 Preparation of d-beta-hydroxyamino acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56209983A JPS58116690A (en) 1981-12-28 1981-12-28 Preparation of d-beta-hydroxyamino acid

Publications (2)

Publication Number Publication Date
JPS58116690A JPS58116690A (en) 1983-07-11
JPH022597B2 true JPH022597B2 (en) 1990-01-18

Family

ID=16581910

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56209983A Granted JPS58116690A (en) 1981-12-28 1981-12-28 Preparation of d-beta-hydroxyamino acid

Country Status (1)

Country Link
JP (1) JPS58116690A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08319939A (en) * 1995-01-19 1996-12-03 Seepex Seeberger Gmbh & Co Screw pump for fluid material to be carried by pump

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3006615B2 (en) * 1989-02-08 2000-02-07 電気化孊工業株匏䌚瀟 Method for producing D-β-hydroxy amino acid
US5266468A (en) * 1990-06-04 1993-11-30 University Of Notre Dame Du Lac Process for preparing β-hydroxy-α amino acids
CN104073506B (en) 2004-10-13 2018-02-13 䞉井化孊株匏䌚瀟 The DNA of enzyme, the preparation method of the enzyme and D serine preparation method of the coding with D serine synthesizing activities

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08319939A (en) * 1995-01-19 1996-12-03 Seepex Seeberger Gmbh & Co Screw pump for fluid material to be carried by pump

Also Published As

Publication number Publication date
JPS58116690A (en) 1983-07-11

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