JPS5921599B2 - Method for producing D(-)-β-hydroxyisobutyric acid - Google Patents

Method for producing D(-)-β-hydroxyisobutyric acid

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Publication number
JPS5921599B2
JPS5921599B2 JP14425279A JP14425279A JPS5921599B2 JP S5921599 B2 JPS5921599 B2 JP S5921599B2 JP 14425279 A JP14425279 A JP 14425279A JP 14425279 A JP14425279 A JP 14425279A JP S5921599 B2 JPS5921599 B2 JP S5921599B2
Authority
JP
Japan
Prior art keywords
methacrylic acid
acid
manufacturing
hydroxyisobutyric acid
microorganisms
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
Application number
JP14425279A
Other languages
Japanese (ja)
Other versions
JPS5668394A (en
Inventor
淳三 長谷川
茂樹 濱口
肇 川原田
清 渡辺
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.)
Kanegafuchi Chemical Industry Co Ltd
Original Assignee
Kanegafuchi Chemical Industry Co Ltd
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 Kanegafuchi Chemical Industry Co Ltd filed Critical Kanegafuchi Chemical Industry Co Ltd
Priority to JP14425279A priority Critical patent/JPS5921599B2/en
Priority to GB8033532A priority patent/GB2063873B/en
Priority to US06/201,337 priority patent/US4310635A/en
Priority to DE19803041224 priority patent/DE3041224A1/en
Priority to NL8006026A priority patent/NL192833C/en
Priority to IT50073/80A priority patent/IT1188962B/en
Priority to IE2291/80A priority patent/IE50473B1/en
Priority to ES496563A priority patent/ES8200400A1/en
Priority to FR8023612A priority patent/FR2468646B1/en
Priority to CH8221/80A priority patent/CH647806A5/en
Publication of JPS5668394A publication Critical patent/JPS5668394A/en
Publication of JPS5921599B2 publication Critical patent/JPS5921599B2/en
Expired legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】 本発明は、光学活性炭素を有する種々の天然物または、
医薬品などの生理活性物質を合成する際に有用な反応中
間体の1つである光学活性なD(→一β−ヒドロキシイ
ソ酪酸を微生物のもつ特殊な能力を利用して工業的に有
利に製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides various natural products having optically active carbon or
Optically active D(→-mono-β-hydroxyisobutyric acid), which is one of the reaction intermediates useful in the synthesis of physiologically active substances such as pharmaceuticals, can be industrially advantageously produced by utilizing the special ability of microorganisms. It's about how to do it.

β−ヒドロキシイソ酪酸の製造法に関しては、合成法と
してメチルマロン酸モノメチルエステルの還元法を始め
として数種の方法が知られているが、いづれも光学的に
不活性なDL出体であり、光学活性をもつ種々の物質製
造の原料としては難点が多いのに加え、製造コストも高
い。
Regarding the production of β-hydroxyisobutyric acid, several synthetic methods are known, including the reduction method of methylmalonic acid monomethyl ester, but all of them are optically inactive DL products. In addition to being difficult to use as a raw material for producing various optically active substances, it is also expensive to produce.

一方、光学活性なβ−ヒドロキシイソ酪酸の製造法に関
して、シュードモナス・プチダ(Pseudomona
sputida)等によるイソ酪酸から行なう方法があ
るが(BiotechnologyandBioeng
ineering)13、203、1971)、これら
はいづれもL(−l)体のβ−ヒドロキシイソ酪酸であ
りDH体のそれは得られていない。従来、D(→体のβ
−ヒドロキシイソ酪酸の工業的に有利な製造方法は適当
なものがなく、本発明者等はその製造方法の開発に着目
し、研究の結果、従来の微生物代謝の知見になかつたメ
タクリル酸をDH−β−ヒドロキシイソ酪酸へ変換する
代謝経路をもつ微生物が、キヤンデイダ(Candid
a)属に属するものの中に存在する事実を発見し、微生
物によるメタクリル酸より光学活性なD(→−β−ヒド
ロキシイソ酪酸を製造する方法を完成した。
On the other hand, regarding the production method of optically active β-hydroxyisobutyric acid, Pseudomonas putida (Pseudomonas putida)
There is a method using isobutyric acid such as B. sputida (Biotechnology and Bioeng).
(ineering) 13, 203, 1971), these are all β-hydroxyisobutyric acids in the L(-l) form, and the DH form has not been obtained. Conventionally, D (→ body β
-There is no suitable industrially advantageous manufacturing method for hydroxyisobutyric acid, and the present inventors focused their attention on the development of the manufacturing method, and as a result of their research, they found that methacrylic acid, which was not found in the conventional knowledge of microbial metabolism, was - A microorganism with a metabolic pathway that converts it to β-hydroxyisobutyric acid is Candidia
a) We discovered the fact that D(→-β-hydroxyisobutyric acid) exists in the genus D(→-β-hydroxyisobutyric acid), which is more optically active than methacrylic acid, using microorganisms.

即ち本発明は、メタクリル酸に、このものをD(ト)一
β−ヒドロキシイソ酪酸に変換する能力を有するキヤン
デイダ属に属する微生物、その微生物を資化しうる栄養
培地で培養して得た培養液またぱその菌体懸濁液を作用
せしめることを特徴とするD(ハ)−β−ヒドロキシイ
ソ酪酸の製造法に関するものである。本発明に使用され
るメタクリル酸より?→−β一ヒドロキシイソ酪酸へ変
換する代謝系をもつ微生物としてはキヤンデイダ・ルゴ
ーザ(CandidarugOsa)、キヤンデイダ・
パラプシロシス(CandidaparapsilOs
is)、キヤンデイダ・ウチリス(Candidaut
ilis)等があり、この培養には通常、これらの菌が
資化しうる栄養源であれば何んでも使用しうる。
That is, the present invention provides a microorganism belonging to the genus Candeida that has the ability to convert methacrylic acid into D(tri)-β-hydroxyisobutyric acid, and a culture solution obtained by culturing the microorganism in a nutrient medium capable of assimilating it. The present invention also relates to a method for producing D(c)-β-hydroxyisobutyric acid, which is characterized in that it is treated with a suspension of bacterial cells of Paso. From methacrylic acid used in the present invention? Examples of microorganisms with a metabolic system that converts →-β-hydroxyisobutyric acid include Candida rugosa, Candida rugosa, and Candida rugosa.
Candidaparapsilosis
is), Candida utilis
In general, any nutrient source that can be assimilated by these bacteria can be used for this culture.

例えばグルコース、シユクロース、マンニツト等の炭水
化物、エタノール等のアルコール、パラフイン、オレフ
イン等の炭化水素、酢酸、プロピオン酸等の有機酸、大
豆油等の炭素源またはこれらの混合物、酵母工キズ、ペ
プトン、コーンステイープリカ一、硫安、アンモニア等
の含窒素無機有機栄養源、リン酸塩、マグネシウム、カ
リウム、鉄、マンガン等の無機栄養源、およびビオチン
等のビタミン類等を適宜配合した通常の培地が用いられ
る。培養の方法としては栄養培地のPHを4.0〜9.
5の範囲で好気的に20〜40℃の範囲で1〜5日間培
養する。
For example, carbohydrates such as glucose, sucrose, and mannitrate, alcohols such as ethanol, hydrocarbons such as paraffin and olefin, organic acids such as acetic acid and propionic acid, carbon sources such as soybean oil, or mixtures thereof, yeast scratches, peptone, and corn. A normal culture medium containing an appropriate amount of nitrogen-containing inorganic organic nutrients such as staple powder, ammonium sulfate, and ammonia, inorganic nutrients such as phosphate, magnesium, potassium, iron, and manganese, and vitamins such as biotin is used. It will be done. The culture method is to adjust the pH of the nutrient medium to 4.0-9.
5 and aerobically at 20 to 40°C for 1 to 5 days.

メタクリル酸からD(ト)一β−ヒドロキシイソ酪酸へ
の変換にぱ、6,0〜9.0のPH範囲が好ましい。ま
たD(ハ)−β−ヒドロキシイソ酪酸製造の方法として
は、菌体の培養と並行して行なう方法として、例えばメ
タクリル酸を唯一の炭素源とするか、または上記の炭素
源との共存下でPH4.O〜9.5の範囲で好気的に培
養し、培養液中にD(ハ)−β−ヒドロキシイソ酪酸を
蓄積させる方法があり、また菌体の培養とメタクリル酸
からD(ハ)−β−ヒドロキシイソ酪酸への変換反応を
分け2段階にて行なう方法、例えば菌体の生産を炭素源
としてメタクリル酸単独、あるいは資化しうるバラフイ
ン等の上記の炭素源、またはこれらの混合物の栄養培地
でPH4.O〜9.5の範囲で好気的に培養し、得られ
た培養液にメタクリル酸を添加し、PHを6.0〜9.
5に保持して好気的に反応せしめる方法、または得られ
た培養液から遠心分離等で菌体を集め菌体を適当な組成
の液、例えばM/15リン酸緩衝液(PH8.5)に懸
濁し、メタクリル酸と少量のグルコースを加え好気的に
PH6.O〜9.5の範囲で反応を行なう方法がある。
この場合の菌体は、反応速度を早める為にトルエン処理
等の適当な前処理を加えたものも使用できる。培養及び
反応で得られたD(ハ)−β−ヒドロキシイソ酪酸の採
取方法としては、通常の公知の抽出精製方法が利用しう
るが、次の如き方法も使用しうる。
For the conversion of methacrylic acid to D(tri)-β-hydroxyisobutyric acid, a pH range of 6.0 to 9.0 is preferred. In addition, as a method for producing D(c)-β-hydroxyisobutyric acid, for example, methacrylic acid is used as the sole carbon source, or in coexistence with the above carbon sources, as a method carried out in parallel with the cultivation of bacterial cells. At PH4. There is a method of culturing aerobically in the range of O to 9.5 and accumulating D(c)-β-hydroxyisobutyric acid in the culture solution. A method in which the conversion reaction to β-hydroxyisobutyric acid is carried out in two separate stages, such as using methacrylic acid alone as a carbon source produced by bacterial cells, or using the above-mentioned carbon sources such as assimilable baraffin, or a nutrient medium containing a mixture of these. At PH4. The pH was adjusted to 6.0-9.5 by adding methacrylic acid to the resulting culture solution.
5 and react aerobically, or collect the bacterial cells from the obtained culture solution by centrifugation, etc., and transfer the bacterial cells to a solution of an appropriate composition, such as M/15 phosphate buffer (PH 8.5). methacrylic acid and a small amount of glucose and aerobically adjusted to pH 6. There is a method of carrying out the reaction in the range of 0 to 9.5.
In this case, the bacterial cells may be subjected to appropriate pretreatment such as toluene treatment in order to accelerate the reaction rate. As a method for collecting D(c)-β-hydroxyisobutyric acid obtained by culturing and reaction, conventional extraction and purification methods can be used, but the following methods can also be used.

例えば、得られたD(ハ)−β−ヒドロキシイソ酪酸含
有液のPHを硫酸等で1.0付近まで下げ、更に飽和と
なる様に硫酸アンモニウムを加える。しかる後、2倍容
量の酢酸エチルで3回抽出を行なう。これを低温、減圧
下、溶剤を除き、D(ハ)一β−ヒドロキシイソ酪酸含
有物を褐色油状で得、更にこのものを少量のベンゼンに
溶解し、ベンゼン−アセトン混合溶剤で溶出するシリカ
ゲルカラムクロマトグラフイ一を行なう事により容易に
他の不純物と分離する事ができる。また、ジアゾメタン
等と反応させる公知の方法にてエステル化してD(へ)
−β−ヒドロキシイソ酪酸メチルエステルとした後、分
別蒸留する方法によつても分離しうる。D(へ)−β−
ヒドロキシイソ酪酸の定量は、ジエームズ・アール・シ
ューファー(James,.RlSchaeffer)
等の方法(BiOtechnOlOgyandBlOe
mgimerimg、13、203、1971)に準じ
て行つた。
For example, the pH of the resulting D(c)-β-hydroxyisobutyric acid-containing solution is lowered to around 1.0 with sulfuric acid or the like, and ammonium sulfate is added to achieve saturation. Thereafter, extraction is carried out three times with twice the volume of ethyl acetate. The solvent is removed at low temperature and under reduced pressure to obtain a substance containing D(iii)-β-hydroxyisobutyric acid in the form of a brown oil, which is then dissolved in a small amount of benzene and eluted with a benzene-acetone mixed solvent through a silica gel column. It can be easily separated from other impurities by chromatography. In addition, D(to) can be esterified by a known method of reacting with diazomethane etc.
-β-Hydroxyisobutyric acid methyl ester can also be separated by fractional distillation. D(to)-β-
Quantification of hydroxyisobutyric acid was performed by James, Rl Schaeffer.
etc. method (BiOtechnOlOgyandBlOe
mgimerimg, 13, 203, 1971).

次に本発明を実施例によつて説明するが本発明は実施例
のみに限定されるものではない。
Next, the present invention will be explained with reference to Examples, but the present invention is not limited only to the Examples.

実施例 1 グルコース2%、イーストエキス0.5%、ペプトン0
.3%、肉工キズ0.3%、メタクリル酸0.1%を含
む培地(PH6.O)11にキヤンデイダ・ルゴーザI
FOO75O(CandidarugOsa)、同1F
00591、キャンデイダ・パラプシロシスIFOO7
O8(CandidapanapsilOsis)を植
菌し、31容ミニジャーフアーメンタ一で30℃、通気
1VVM1攪拌500rpmで20時間培養した。
Example 1 Glucose 2%, yeast extract 0.5%, peptone 0
.. Quandida Rugosa I in a medium (PH6.O) containing 3%, 0.3% meat scratches, and 0.1% methacrylic acid (PH6.O).
FOO75O (CandidarugOsa), 1F
00591, Candida parapsilosis IFOO7
O8 (CandidapanapsilOsis) was inoculated and cultured for 20 hours at 30°C in a 31-volume mini jar fermenter with aeration of 1 VVM and 1 stirring at 500 rpm.

その後、各培養液にメタクリル酸20f7を添加し、カ
セイソーダでPHを8.5に調整、更に48時間培養を
同一条件で反応を行なつた。得られた各反応液を硫酸で
PHl.Oとし、硫酸アンモニウムを加え飽和溶液とし
た。次に等量の酢酸エチルで3回抽出し、抽出液を無水
硫酸ナトリウムで脱水し、これを減圧下、40℃以下で
溶剤を除き、黄褐色油状物質を得た。この油状物質を重
量の5倍のシリカゲル(ワコーゲルQ5O)を用いベン
ゼンで調整したカラムにかけた。
Thereafter, methacrylic acid 20f7 was added to each culture solution, the pH was adjusted to 8.5 with caustic soda, and the reaction was further cultured for 48 hours under the same conditions. Each of the obtained reaction solutions was diluted with sulfuric acid to PHL. O, and ammonium sulfate was added to make a saturated solution. Next, the mixture was extracted three times with equal amounts of ethyl acetate, the extract was dehydrated over anhydrous sodium sulfate, and the solvent was removed under reduced pressure below 40°C to obtain a yellowish brown oil. This oily substance was applied to a column using 5 times the weight of silica gel (Wako Gel Q5O) adjusted with benzene.

最初カラム容量の4倍のベンゼンリアセトン(9:1)
溶剤で洗浄し、未反応のメタクリル酸を溶出除去、次に
ベンゼンリアセトン(3:1)溶剤でレ→−β−ヒドロ
キシイソ酪酸を溶出した。得られたD(ハ)−β−ヒド
ロキシイソ酪酸画分を集め、減圧下、溶剤を除去しシロ
ツプ状の物質を得た。この様に得られたものは、ガスク
ロマトグラフイ一、シリカゲル薄層クロマトグラフイ一
、?分析等で高純度なβ−ヒドロキシイソ酪酸である事
が確認された。
Benzeneliacetone (9:1) at 4 times the initial column volume
It was washed with a solvent to elute and remove unreacted methacrylic acid, and then eluted with benzenelyacetone (3:1) solvent to elute -β-hydroxyisobutyric acid. The obtained D(c)-β-hydroxyisobutyric acid fractions were collected and the solvent was removed under reduced pressure to obtain a syrup-like substance. What was obtained in this way was gas chromatography, silica gel thin layer chromatography, etc. Analysis and other analysis confirmed that it was highly pure β-hydroxyisobutyric acid.

これをユニオン技研製のデイジタル自動旋光度計PMl
Olにて測定した結果、表1の如く、DH−β−ヒドロ
キシイソ酪酸である事が確認された。実施例 2 ノルマルパラフイン3%、リン酸二アンモニウム1.3
%、リン酸−カリウム0.7%、塩化ナトリウム0.0
1%、硫酸亜鉛0,006%、硫酸第二鉄0.009%
、イーストエキス0.5%含有培地(PH6.5)11
にキヤンデイダ・ルゴーザIFOO75Oを植菌し、3
1容ミニジャーフアーメンタ一にて30℃、通気1.5
VVM、攪拌700rpmで72時間培養し、得られた
培養液を遠心分離により菌体を集め、更に0.9%食塩
水で2回洗浄した菌体を得た。
This is a digital automatic polarimeter PMl manufactured by Union Giken.
As shown in Table 1, it was confirmed that it was DH-β-hydroxyisobutyric acid. Example 2 Normal paraffin 3%, diammonium phosphate 1.3
%, potassium phosphate 0.7%, sodium chloride 0.0
1%, zinc sulfate 0,006%, ferric sulfate 0.009%
, medium containing 0.5% yeast extract (PH6.5) 11
inoculated with Quyandida Rugoza IFOO75O, 3
1 volume mini jar fermenter at 30℃, ventilation 1.5
The cells were cultured for 72 hours using VVM and stirring at 700 rpm, and the resulting culture solution was centrifuged to collect cells, which were further washed twice with 0.9% saline to obtain cells.

これをM/15リン酸バツフア一(PH8.5)に懸濁
し、メタクリル酸307、グルコース27添加し、PH
を8.5に調ヤし培養と同一条件で48時間反応させた
。その後、実施例1と同様な方法で抽出精製を行ないD
(ハ)−β−ヒドロキシイソ酪酸13.5y1〔α〕M
−13,45キ(c=12.5エタノール)を得た。実
施例 3 グルコース1.5%、イーストエキス0.5%、ペプト
ン0,3%、肉工キズ0.3%、メタクリル酸0.5%
、炭酸カルシウム0.5含有する培地(PH6.O)1
1にキヤンデイダ・パラプシロシスIFOO7O8を植
菌しミニジャーフアメンタ一にて30℃通気RwMl撹
拌500rpmにて24時間培養し、その後PHを8.
0にカセイソーダで維持し、更に24時間培養した培養
液から実施例1と同様に抽出精製を行ないD(ハ)−β
−ヒドロキシイソ酪酸1.3y1〔α〕甘=−13.4
4ド(c=12。
This was suspended in M/15 phosphate buffer (PH 8.5), 307 ml of methacrylic acid and 27 ml of glucose were added, and the PH
The temperature was adjusted to 8.5 and reacted for 48 hours under the same conditions as culture. After that, extraction and purification was performed in the same manner as in Example 1.
(c)-β-hydroxyisobutyric acid 13.5y1[α]M
-13.45 kg (c=12.5 ethanol) was obtained. Example 3 Glucose 1.5%, yeast extract 0.5%, peptone 0.3%, meat scratches 0.3%, methacrylic acid 0.5%
, medium containing calcium carbonate 0.5 (PH6.O) 1
1 was inoculated with Candeida parapsilosis IFOO7O8 and cultured in a mini jar at 30°C with aeration of RwMl at 500 rpm for 24 hours, and then the pH was adjusted to 8.
D(c)-β was extracted and purified in the same manner as in Example 1 from the culture solution maintained at 0.0 with caustic soda and further cultured for 24 hours.
-Hydroxyisobutyric acid 1.3y1 [α] sweet = -13.4
4 do (c=12.

5エタノール)を得た。5 ethanol) was obtained.

実施例 4 キヤンデイダ・ユチリスIFOO396を使用し、実施
例1と同様に培養及び抽出精製しD(ハ)−β−ヒドロ
キシイソ酪酸を8.8r得た。
Example 4 Using Candeida utilis IFOO396, 8.8 r of D(c)-β-hydroxyisobutyric acid was obtained by culturing, extraction and purification in the same manner as in Example 1.

Claims (1)

【特許請求の範囲】 1 メタクリル酸に、このものをD(−)−β−ヒドロ
キシイソ酪酸に変換する能力を有するキヤンデイダ属に
属する微生物、その微生物を資化しうる栄養培地で培養
して得た培養液またはその菌体懸濁液を作用せしめるこ
とを特徴とするD−(−)−β−ヒドロキシイソ酪酸の
製造法。 2 微生物がキヤンデイダ・ルゴーザ、キヤンデイダ・
パラプシロシスまたはキヤンデイダ・ユチリスである特
許請求の範囲第1項記載の製造法。 3 微生物の炭素源として、メタクリル酸単独、または
これに資化しうる炭水化物、アルコール、有機酸または
炭化水素の一種または二種以上を共存せしめたものを使
用する特許請求の範囲第1項または第2項記載の製造法
。 4 微生物の培養を、pH4.0〜9.5の範囲で行な
う特許請求の範囲第3項記載の製造法。 5 微生物を資化しうる炭水化物、アルコール、有機酸
または炭化水素の一種または二種以上を炭素源として培
養し、得られた培養液または菌体懸濁液をメタクリル酸
に作用せしめる特許請求の範囲第1項または第2項記載
の製造法。 6 微生物の培養をpH4.0〜9.5の範囲で行ない
、培養液または菌体懸濁液とメタクリル酸との反応をp
H6.0〜9.5の範囲で行なう特許請求の範囲第5項
記載の製造法。
[Scope of Claims] 1. A microorganism belonging to the genus Candeida that has the ability to convert methacrylic acid into D(-)-β-hydroxyisobutyric acid, obtained by culturing the microorganism in a nutrient medium capable of assimilating it. A method for producing D-(-)-β-hydroxyisobutyric acid, which comprises reacting with a culture solution or a cell suspension thereof. 2 Microorganisms such as Candeida Rugosa and Candeida Rugosa
The method of manufacturing according to claim 1, wherein the plant is Parapsilosis or Candida utilis. 3. Claims 1 or 2 in which methacrylic acid alone or in combination with one or more carbohydrates, alcohols, organic acids, or hydrocarbons that can be assimilated is used as a carbon source for microorganisms. Manufacturing method described in section. 4. The manufacturing method according to claim 3, wherein the microorganism is cultured at a pH in the range of 4.0 to 9.5. 5. Claim No. 5, which involves culturing one or more types of carbohydrates, alcohols, organic acids, or hydrocarbons that can assimilate microorganisms as a carbon source, and allowing the resulting culture solution or bacterial cell suspension to act on methacrylic acid. The manufacturing method according to item 1 or 2. 6 Cultivate microorganisms at a pH range of 4.0 to 9.5, and react the culture solution or bacterial cell suspension with methacrylic acid at pH 4.0 to 9.5.
The manufacturing method according to claim 5, which is carried out within the range of H6.0 to 9.5.
JP14425279A 1979-11-06 1979-11-06 Method for producing D(-)-β-hydroxyisobutyric acid Expired JPS5921599B2 (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
JP14425279A JPS5921599B2 (en) 1979-11-06 1979-11-06 Method for producing D(-)-β-hydroxyisobutyric acid
GB8033532A GB2063873B (en) 1979-11-06 1980-10-17 Fermentative production of d(-)-hydroxyisobutyric acid
US06/201,337 US4310635A (en) 1979-11-06 1980-10-27 Fermentative production of D(-)-β-hydroxyisobutyric acid
DE19803041224 DE3041224A1 (en) 1979-11-06 1980-11-03 METHOD FOR THE FERMENTATIVE PRODUCTION OF D (-) - (BETA) -HYDROXYISOBUTTERIC ACID
NL8006026A NL192833C (en) 1979-11-06 1980-11-04 Process for preparing a beta-hydroxyisobutyric acid.
IT50073/80A IT1188962B (en) 1979-11-06 1980-11-04 PROCEDURE FOR PRODUCING ACID D (-) - B-HYDROXY-ISOBUTYRIC
IE2291/80A IE50473B1 (en) 1979-11-06 1980-11-05 Fermentative production of d(-)-b-hydroxyisobutyric acid
ES496563A ES8200400A1 (en) 1979-11-06 1980-11-05 Fermentative production of D(-)- beta -hydroxyisobutyric acid
FR8023612A FR2468646B1 (en) 1979-11-06 1980-11-05 PRODUCTION OF D (-) - B-HYDROXYISOBUTYRIC ACID BY FERMENTATION OF ISOBUTYRIC AND / OR METHACRYLIC ACID
CH8221/80A CH647806A5 (en) 1979-11-06 1980-11-05 METHOD FOR PRODUCING D (-) - BETA HYDROXYISOBUTTERIC ACID.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14425279A JPS5921599B2 (en) 1979-11-06 1979-11-06 Method for producing D(-)-β-hydroxyisobutyric acid

Publications (2)

Publication Number Publication Date
JPS5668394A JPS5668394A (en) 1981-06-09
JPS5921599B2 true JPS5921599B2 (en) 1984-05-21

Family

ID=15357767

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14425279A Expired JPS5921599B2 (en) 1979-11-06 1979-11-06 Method for producing D(-)-β-hydroxyisobutyric acid

Country Status (1)

Country Link
JP (1) JPS5921599B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59118092A (en) * 1982-12-23 1984-07-07 Mitsubishi Rayon Co Ltd Preparation of beta-hydroxyisobutyric acid

Also Published As

Publication number Publication date
JPS5668394A (en) 1981-06-09

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