JPH03290194A - Production of d-isocitric acid by fermentation - Google Patents

Production of d-isocitric acid by fermentation

Info

Publication number
JPH03290194A
JPH03290194A JP8887590A JP8887590A JPH03290194A JP H03290194 A JPH03290194 A JP H03290194A JP 8887590 A JP8887590 A JP 8887590A JP 8887590 A JP8887590 A JP 8887590A JP H03290194 A JPH03290194 A JP H03290194A
Authority
JP
Japan
Prior art keywords
acid
isocitric acid
yeast
fermentation
acids
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
Application number
JP8887590A
Other languages
Japanese (ja)
Other versions
JP2877430B2 (en
Inventor
Kuniki Kino
邦器 木野
Yasuhiro Tomiyoshi
冨吉 康弘
Yoshiyuki Kurato
倉都 祥行
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.)
KH Neochem Co Ltd
Original Assignee
Kyowa Hakko Kogyo 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 Kyowa Hakko Kogyo Co Ltd filed Critical Kyowa Hakko Kogyo Co Ltd
Priority to JP8887590A priority Critical patent/JP2877430B2/en
Publication of JPH03290194A publication Critical patent/JPH03290194A/en
Application granted granted Critical
Publication of JP2877430B2 publication Critical patent/JP2877430B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

PURPOSE:To obtain d-isocitric acid useful as a food additive, etc., at a low cost in high yield by fermenting with a yeast in a medium containing fumaric acids or maleic acids. CONSTITUTION:The objective acid can be produced by using a medium containing preferably 0.01-0.3mol of fumaric acids or maleic acid and fermenting with a yeast (e.g. Candida lipolytica).

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、発酵法によるd−イソクエン酸の製造法に関
する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for producing d-isocitric acid by fermentation.

d−イソクエン酸は医薬品あるいは食品添加物などとし
て有用な有機酸である。
d-isocitric acid is an organic acid useful as a pharmaceutical or food additive.

従来の技術 従来、d−イソクエン酸の製造法としては、酵母を用い
る発酵法が知られている〔日本農芸化学会誌、 44 
(11) 、 493−498(1970) 、英国特
許1199700 、フランス特許1596056]。
Conventional technology Conventionally, fermentation using yeast has been known as a method for producing d-isocitric acid [Journal of the Japanese Society of Agricultural Chemistry, 44
(11), 493-498 (1970), British Patent No. 1199700, French Patent No. 1596056].

d−イソクエン酸生産性の高い変異株を収得することを
目的として、カンテ′イダ・リポリテイカ(Candi
da 1ipolytica)からフルオロ酢酸耐性変
異株の誘導が試みられ、フルオロ酢酸の阻害部位である
アコニターセ活性の上昇した株は取得できたが、この菌
株はd−イソクエン酸比率の向上した株ではなかった。
For the purpose of obtaining mutant strains with high d-isocitric acid production, Cantheida lipolyteica (Candi
Attempts were made to induce a fluoroacetic acid-resistant mutant strain from A. da 1ipolytica), and a strain with increased activity of aconitase, which is an inhibition site for fluoroacetic acid, was obtained, but this strain was not a strain with an improved ratio of d-isocitric acid.

〔日本農芸化学、 4B(10)、 543548 5
49−554(1974) ]。
[Japan Agricultural Chemistry, 4B(10), 543548 5
49-554 (1974)].

また、酵母菌を使用する発酵法によるd−イソクエン酸
の製造において、d−イソクエン酸生産量比を向上させ
るためイタコン酸を添加する方法〔日本農芸化学会大会
要旨集、 348(1976) 、特公昭56−391
94号公報〕 カンディダ・ゼイラノイデス(Candida 1ey
lanoides)を用いた発酵法によるd−イソクエ
ン酸の製造において、黄血塩を添加する方法〔ジャーナ
ル・オフ・ファーメンテ−ジョン・テクノロジー(J、
 FermentTechnol)、 52(8)、 
542−550(1974) 〕が知られている。
Furthermore, in the production of d-isocitric acid by a fermentation method using yeast, a method of adding itaconic acid to improve the production ratio of d-isocitric acid [Japan Society of Agricultural Chemistry Abstracts, 348 (1976), special Kosho 56-391
Publication No. 94] Candida zeylanoides (Candida 1ey
A method of adding yellow blood salt in the production of d-isocitric acid by fermentation using lanoides [Journal of Fermentation Technology (J,
Ferment Technol), 52(8),
542-550 (1974)] is known.

発明が解決しようとする課題 医薬品あるいは食品添加物などとして有用な(1イソク
エン酸を、工業的により効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 industrially producing 1-isocitric acid, which is useful as a pharmaceutical or food additive, more efficiently and at lower cost.

課題を解決するための手段 本発明は、酵母菌を使用する発酵法によるdイソクエン
酸の製造において、培地にフマル酸類またはマレイン酸
類を存在せしめることを特徴とするd−イソクエン酸の
製造法を提供する。
Means for Solving the Problems The present invention provides a method for producing d-isocitric acid, which is characterized in that fumaric acids or maleic acids are present in the medium in the production of d-isocitric acid by a fermentation method using yeast. do.

ここで、フマル酸類とは、フマル酸またはその塩、ある
いは加水分解によって容易にフマル酸に変換しうる誘導
体を意味し、マレイン酸類とは、マレイン酸またはその
塩、あるいは加水分解によって容易にマレイン酸に変換
しうる誘導体を意味する。
Here, fumaric acids refer to fumaric acid or its salts, or derivatives that can be easily converted to fumaric acid by hydrolysis, and maleic acids refer to maleic acid or its salts, or derivatives that can be easily converted to fumaric acid by hydrolysis. means a derivative that can be converted into

本発明で用いられる酵母菌としては、(1−イソクエン
酸生産能を有する菌株であればいずれでもよい。d イ
ソクエン酸生産能を有する酵母は、を胞子酵母あるいは
無胞子酵母を問わず多数存在するが、なかでもカンディ
ダ属(Candida)、ピヒア属(Pichia) 
、)ルT)プシス属(Torulopsis)、ツンカ
ロミセス属(SaccharomyceS)、チゴサッ
カロミセス属(ZygosaccharomyceS)
、デバリオミセス属(Debaryomyces) 、
ロイコスポリシウム属(Leucosporidium
) 、プレタノミセス属(Brettanomyces
)、ハンゼヌラ属(目ansenul’a)に属する酵
母が有効に利用される。代表的な酵母菌としては、下記
に示す菌株をあげることができる。
The yeast used in the present invention may be any strain as long as it has the ability to produce 1-isocitric acid. (d) There are many yeasts that have the ability to produce isocitrate, regardless of whether they are spore yeast or non-spore yeast. However, among them, the genus Candida and the genus Pichia.
, ) RuT) Torulopsis, SaccharomyceS, ZygosaccharomyceS
, Debaryomyces ,
Leucosporidium spp.
), Brettanomyces
), yeasts belonging to the genus Hansenula (order ansenul'a) are effectively used. Typical yeast strains include the strains shown below.

カンデイダ・リポリテイカ(Candida 1ipo
lytica)カンディダ・セイラノイデス(c、 z
eylanoides)、カンディダ・ギヤマンデイ(
C,guilliermondii)、カンディダ・ア
ルビカンス(C,albicans) 、カンディダ・
フミコラ(C,humicola) 、カンディダ・パ
ラプシロンス(C9parapsilosis) 、カ
ンデイダ・ブルムプヂ(C,brumpti i)なと
のカンディダ属の酵母、ピヒア・ファリノt (Pic
hia farinosa)、ピヒア・オーメリ (p
、 ollmeri)などのピヒ′r属の[51、)ル
ロブンス・キンリヌス(Toruloρ5ISxyli
nus)、トルロプンス・ファマタ (T、 fama
ta)などのトルロプンス属の酵母、ザソカロミセス・
セレビジアエ(Saccharomyccs cerc
visiac)などのヅッカロミセス属の酵母、チゴサ
ッカロミセス0チクマエンシス(Zygosaccha
romyces tikumaensis)などのチゴ
サッカロミセス属の酵母、デバリオミセス°ハンゼ=’
 (Debaryomyces hansenii)な
どのデバリオミセス属の酵母、Uイコスポリジウム・カ
プスリゲヌム(Leucosporidium cap
suligenum)などのロイコスポリジウト属の酵
母、プレタノミセス゛ランビクス(Brettanom
yces Iambicus)などのプレタノミセス属
の酵母、ハンゼヌラ・γノマラ(llansenula
 anomala)などのハンゼヌラ属の酵母。
Candida lipolyteica (Candida 1ipo)
lytica) Candida seiranoides (c, z
eylanoides), Candida gearmandei (
C. guilliermondii), C. albicans, Candida albicans
Yeasts of the genus Candida, such as C. humicola, C. parapsilosis, and C. brumpti, Pichia farinot (Pic)
hia farinosa), Pichia ohmeri (p.
[51,) of the genus Pihy'r, such as Toruloρ5ISxyli,
nus), Torlopuns famata (T, fama
Yeasts of the genus Torulopuns such as ta), Thesocalomyces
cerevisiae (Saccharomyccs cerc)
Yeasts of the genus Duccharomyces, such as Zygosaccharomyces
Yeasts of the genus Chigosaccharomyces, such as S. romyces tikumaensis),
Yeasts of the genus Debaryomyces such as Debaryomyces hansenii, Leucosporidium cap
Yeasts of the genus Leucosporidium such as P. suligenum, Brettanomyces errambicus
yeasts of the genus Pletanomycetes, such as Yces ambicus;
Yeasts of the genus Hansenula such as Anomala).

もらろん、これらの酵母菌から誘導された変異株の中か
ら選ばれた菌株も、d−イソクエン酸の生産能を有する
かぎり、いずれも使用され得る。
Of course, any strain selected from mutant strains derived from these yeasts may also be used as long as it has the ability to produce d-isocitric acid.

その変異は自然的に行われたものであっても、また紫外
線照射やN−メチル−N′−二1−Tl1−Nニトロソ
クアニジン処理などの化学処理など通常用いられる変異
処理方法によって行なわれたものでもよい。
The mutation may be caused naturally or by commonly used mutation processing methods such as ultraviolet irradiation or chemical treatments such as N-methyl-N'-21-Tl1-N nitrosocanidine treatment. It may also be something you have.

本発明によるd−イソクエン酸の生産は、フマル酸類ま
たはマレイン酸類を培養液中に存在させることを除けば
、通常の有機酸生産のための培養法で実施可能である。
The production of d-isocitric acid according to the present invention can be carried out using conventional culture methods for producing organic acids, except that fumaric acids or maleic acids are present in the culture solution.

使用培地は、用いられる酵母の性質に応じて適宜選択さ
れるが、炭素源、窒素源、無機物その他使用菌株の必要
とする栄養素をほどよく含有するものならば、合成培地
または天然培地いずれも使用可能である。
The medium to be used is selected as appropriate depending on the properties of the yeast used, but either synthetic or natural media can be used as long as it contains adequate amounts of carbon sources, nitrogen sources, inorganic substances, and other nutrients required by the strain used. It is possible.

炭素源としては、クルコース、シュークロース、糖蜜、
澱粉加水分解物などの炭水化物、エタノル、クリセロー
ルなどのアルコール類、酢酸などの有機酸、オレイン酸
などの脂肪酸、大豆油、魚油などの油脂類あるいはブト
ラブカン、ヘキサデカンなどのパラフィン系炭化水素、
その他酵母が資化利用し得る広範囲な有機化合物が使用
され、単独または混合状態で用いることができる。
Carbon sources include crucose, sucrose, molasses,
Carbohydrates such as starch hydrolysates, alcohols such as ethanol and chrycerol, organic acids such as acetic acid, fatty acids such as oleic acid, fats and oils such as soybean oil and fish oil, or paraffinic hydrocarbons such as butrabucane and hexadecane,
A wide range of other organic compounds that can be assimilated by yeast are used and can be used alone or in mixtures.

窒素源としては、アンモニアまたは塩化アンモニウム、
硫酸アンモニウム、炭酸アンモニウム、酢酸アンモニウ
ムなどの各種無機および有機γンモニウj、塩類あるい
は尿素および他の窒素含有物質ならびにペプトン、肉エ
キス、酵母エキス、コン・スチープ・リカー、カゼイン
加水分解物などの窒素含有有機物など種々のものが使用
可能である。使用する酵母によっては、硝酸塩もまた窒
素源として用いられる。以上の各種窒素源は単独または
2種以上混合しても使用できる。
As a nitrogen source, ammonia or ammonium chloride,
Various inorganic and organic substances such as ammonium sulfate, ammonium carbonate, ammonium acetate, salts or urea and other nitrogen-containing substances and nitrogen-containing organic substances such as peptones, meat extracts, yeast extracts, corn steep liquor, casein hydrolysates, etc. Various types such as the following can be used. Depending on the yeast used, nitrates are also used as a nitrogen source. The various nitrogen sources mentioned above can be used alone or in combination of two or more.

さらに無機物としては、リン酸第−水素カリウム、リン
酸第二水素カリウム、硫酸アンモニウム、塩化アンモニ
ウム、硫酸マグネシウム、塩化ナトリウム、硫酸第一鉄
、硫酸マンガンおよび炭酸カルシウムなどを使用する。
Furthermore, as inorganic substances, potassium hydrogen phosphate, potassium dihydrogen phosphate, ammonium sulfate, ammonium chloride, magnesium sulfate, sodium chloride, ferrous sulfate, manganese sulfate, calcium carbonate, and the like are used.

酵母の生育に必要とするビタミン、アミノ酸源などは、
前記したような他の培地成分によって培地に供給されれ
ば特に加えなくてもよい。
The vitamins and amino acid sources necessary for yeast growth are
It does not need to be added as long as it is supplied to the medium by other medium components as described above.

本発明の実施にあたっては、」1記のような培地にフマ
ル酸類またはマレイン酸類が添加される。
In carrying out the present invention, fumaric acids or maleic acids are added to the medium as described in 1.

培地中の7マル酸類またはマレイン酸類の濃度は、遊離
のフマル酸、マレイン酸換算で0.005モルから05
モル、好ましくは0.01モルから0.3モルで使用さ
れる。フマル酸類またはマレイン酸類を、その塩あるい
は加水分解して容易にフマル酸またはマレイン酸に変換
し得る誘導体の形で用いる場合でも、遊離の7マル酸ま
たは遊離のマレイン酸として上記の濃度を与えるように
添加量を調整すればよい。さらにその添加する時期とし
ては、培養の全期間を通じていずれの時期に添加しても
差支えないが、好ましくは培養開始前の培地中に添加す
るか、あるいは培養中期までに添加する。
The concentration of 7 malic acids or maleic acids in the medium ranges from 0.005 mol to 0.5 mol in terms of free fumaric acid and maleic acid.
It is used in moles, preferably from 0.01 to 0.3 moles. Even when fumaric acids or maleic acids are used in the form of their salts or derivatives that can be easily converted into fumaric acid or maleic acid by hydrolysis, it is necessary to provide the above concentration as free 7-maric acid or free maleic acid. The amount added can be adjusted accordingly. Furthermore, it may be added at any time during the entire culture period, but it is preferably added to the medium before the start of culture, or by the middle stage of culture.

培養は、振盪培養または通気攪拌培養などの好気的条件
下に行う。培養温度は、使用される酵母によって異なる
が、一般に20〜35℃が好適である。培地のpHは、
一般に2.5〜10、好ましくは3〜8の範囲である。
Cultivation is performed under aerobic conditions such as shaking culture or aerated agitation culture. Although the culture temperature varies depending on the yeast used, 20 to 35°C is generally suitable. The pH of the medium is
It generally ranges from 2.5 to 10, preferably from 3 to 8.

培養期間は通常2〜8日間である。The culture period is usually 2 to 8 days.

培養液からd−イソクエン酸を採取する方法は、培養終
了後、菌体を除去して濃縮晶析する方法、活性炭処理あ
るいはイオン交換樹脂処理などの公知の方法によって行
われる。
The method for collecting d-isocitric acid from the culture solution is carried out by a known method such as removing the bacterial cells and concentrating and crystallizing after the completion of the culture, treatment with activated carbon, or treatment with an ion exchange resin.

以下に実施例をあげて、本発明を具体的に説明する。The present invention will be specifically described below with reference to Examples.

実施例1 d−イソクエン酸生産能を有するカンディダ・ゼイラノ
イデス(Candida zeylanoides> 
A T CC20347を用い、寒天斜面培地(麦芽エ
キス10g1酵母エキス4g、グルコース4g、寒天2
0gを水1flに含み、pH6,0に調整した培地)で
30℃、36時間培養して得た菌体を40−の種培地(
組成ニゲルコース 5%、NH,[:ffl  0.2
%、KH2PO40,05%、Mg5O+・7H2[]
 0.05%、酵母エキス 01%、コーン・スチープ
・リカ0.1%、CaCO33,3%、PII5.5 
)を含む250mff容三角フラスコに接種し、30℃
で24時間、210「1mのロータリーシェーカー上で
振盪培養した。
Example 1 Candida zeylanoides having the ability to produce d-isocitric acid
Using AT CC20347, agar slant medium (10 g of malt extract, 4 g of yeast extract, 4 g of glucose, 2 g of agar)
The bacterial cells obtained by culturing at 30°C for 36 hours in a medium containing 0 g in 1 fl of water and adjusted to pH 6.0 were cultured in a 40-
Composition Nigelcose 5%, NH, [:ffl 0.2
%, KH2PO40.05%, Mg5O+・7H2[]
0.05%, yeast extract 01%, corn steep liquor 0.1%, CaCO33.3%, PII5.5
) was inoculated into a 250 mff Erlenmeyer flask and heated at 30°C.
The cells were incubated for 24 hours with shaking on a 210mm rotary shaker.

この種培養液4−を、第1表に示す濃度のフマル酸を添
加した下記組成の発酵培地を含む25〇−容三角フラス
コに接種して、種培養と同様の条件下で7日間培養した
。このとき、フマル酸は溶解度が低いため水酸化す) 
IJウム溶液で溶解後、発酵培地に添加した。
This seed culture solution 4- was inoculated into a 250-capacity Erlenmeyer flask containing a fermentation medium with the following composition supplemented with fumaric acid at the concentration shown in Table 1, and cultured for 7 days under the same conditions as the seed culture. . At this time, fumaric acid is hydroxylated due to its low solubility)
After dissolving in IJum solution, it was added to the fermentation medium.

発酵培地の組成:n−パラフィン(炭素数12から15
を主成分とする混合物、日本鉱業社製)5%、NH,C
ff1 0.4%、KH2PO40,05%、MgSO
4・7H200,05%、ZnSOs’7H202mg
/ R、Mn5O+・4〜68202 mg/ fl、
Fe50<・7)IJ 5 mg/ R1CuSO+・
5)120150μg/ R、ビオチン100μg/ 
j2 。
Composition of fermentation medium: n-paraffin (carbon number 12 to 15
Mixture mainly composed of Nippon Mining Co., Ltd.) 5%, NH, C
ff1 0.4%, KH2PO40.05%, MgSO
4.7H200.05%, ZnSOs'7H202mg
/ R, Mn5O+・4~68202 mg/fl,
Fe50<・7) IJ 5 mg/R1CuSO+・
5) 120150μg/R, biotin 100μg/
j2.

ザイアミン塩酸塩5 mg/ R、CaCO33%(p
H5,5)発酵終了後のd−イソクエン酸、副生ずるク
エン酸の生成量およびフマル酸の残存量は、高速液体ク
ロマトグラフィー法により定量した。なお、クエン酸は
カルシラl、塩として沈澱しているため、0.5規定塩
酸溶液を添加して沈澱を溶解させた後、遠心分離して得
られた上澄液を試料として用いた。
Zyamine hydrochloride 5 mg/R, CaCO33% (p
H5,5) After completion of the fermentation, the amount of d-isocitric acid produced, the amount of by-product citric acid produced, and the amount of remaining fumaric acid were determined by high performance liquid chromatography. In addition, since citric acid was precipitated as calcilyl salt, the precipitate was dissolved by adding 0.5N hydrochloric acid solution, and then the supernatant obtained by centrifugation was used as a sample.

その結果を第1表に示す。The results are shown in Table 1.

このうちフマル酸を0.043M添加して得られたd−
イソクエン酸含有培養液21を遠心分離して菌体を除い
た一ヒ澄液を、ダイヤイオン5KlllB(H”型)(
三菱化成社製)の樹脂0.51を用いて脱カチオンし、
IO規定水酸化カリウム溶液でp H3,6に調整後、
活性炭処理して脱色した。これを約100−になるまで
減圧′a縮したところ、d−イソクエン酸モノカリウム
塩が析出した。その重量は46gで純度は95%であっ
た。
Of these, d- obtained by adding 0.043M fumaric acid
The isocitric acid-containing culture solution 21 was centrifuged to remove the bacterial cells, and the clear solution was purified by Diaion 5KlllB (H” type) (
Decationization was performed using resin 0.51 (manufactured by Mitsubishi Kasei Corporation),
After adjusting the pH to 3.6 with IO normal potassium hydroxide solution,
It was decolorized by activated carbon treatment. When this was condensed under reduced pressure to about 100, d-isocitric acid monopotassium salt was precipitated. Its weight was 46g and its purity was 95%.

さらに、その10gの結晶を250mfの水に溶解後、
ダイヤイオンS K” I B (H+型)(三菱化成
社製)の樹脂40m1lを用いて脱カチオンし、常温下
で濃縮したことろ、計算量のd−イソクエン酸を含むペ
ースト状の標品が純品換算で8.35g得られた。これ
を再び水50−に溶解して100℃で30分間加熱処理
を行った後11w6乾固したところ、〔1−イソクエン
酸はラクトン体となって計tマ17i7.57gが15
)られた。
Furthermore, after dissolving 10g of the crystals in 250mf of water,
After decationization using 40 ml of Diaion S K'' I B (H+ type) (manufactured by Mitsubishi Kasei Corporation) resin and concentrating at room temperature, a paste-like preparation containing the calculated amount of d-isocitric acid was obtained. 8.35g was obtained in terms of pure product.This was dissolved again in 50°C of water, heated at 100°C for 30 minutes, and then dried to 11w6. tma 17i7.57g is 15
) was given.

実施例2゜ 実施例1の方法において、フマル酸のかわりに第2表に
示す濃度のマレイン酸を発酵培地に添加して7日間培養
し、発醇銘了後のd−イソクエン酸、副生ずるクエン酸
の生成量およびマレイン酸の残存量を定量した。
Example 2 In the method of Example 1, maleic acid at the concentration shown in Table 2 was added to the fermentation medium instead of fumaric acid, and cultured for 7 days. The amount of citric acid produced and the remaining amount of maleic acid were determined.

その結果を第2表に示す。The results are shown in Table 2.

第   2   表 このうちマレイン酸を0.043M添加して得られた(
j イソクエン酸含有培養液21を、実施例と同様の方
法で処理し、d−イソクエン酸モノカリウl、塩が析出
した。その重量は44gで純度は95%であった。
Table 2 Among these, the one obtained by adding 0.043M of maleic acid (
j The isocitric acid-containing culture solution 21 was treated in the same manner as in the example, and d-isocitric acid monopotassium salt was precipitated. Its weight was 44g and its purity was 95%.

さらに、そのl f+ gの紀品を250m1!の水に
溶解後、ダイヤイオンSK”lB (H”型)(三菱化
成社製)の樹脂40meを用いて脱カチオンし、常温下
で濃縮したところ、計算量のd−イソクエン酸を含むペ
ースト状の標品が純品換算で8.35 g()られた。
In addition, 250m1 of that l f + g item! After dissolving it in water, it was decationized using Resin 40me of Diaion SK"lB (H" type) (manufactured by Mitsubishi Kasei Corporation) and concentrated at room temperature, resulting in a paste containing the calculated amount of d-isocitric acid. The standard sample weighed 8.35 g (in terms of pure product).

これを再び水50−に溶解して100℃で30分間加熱
処理を行った後、濃縮乾固したところ、d−イソクエン
酸はラクトン体となって計算量7.57 gが得られた
This was dissolved again in 50°C of water, heated at 100°C for 30 minutes, and then concentrated to dryness. As a result, 7.57 g of d-isocitric acid was obtained as a lactone.

発明の効果 本発明により、収率よく、しかも安価にd−イソクエン
酸を発酵生産することができる。
Effects of the Invention According to the present invention, d-isocitric acid can be fermented and produced with good yield and at low cost.

2

Claims (1)

【特許請求の範囲】[Claims] 酵母菌を使用する発酵法によるd−イソクエン酸の製造
において、培地にフマル酸類またはマレイン酸類を存在
させることを特徴とするd−イソクエン酸の製造法。
1. A method for producing d-isocitric acid by a fermentation method using yeast, characterized in that fumaric acids or maleic acids are present in the medium.
JP8887590A 1990-04-03 1990-04-03 Production method of d-isocitric acid by fermentation method Expired - Lifetime JP2877430B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8887590A JP2877430B2 (en) 1990-04-03 1990-04-03 Production method of d-isocitric acid by fermentation method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8887590A JP2877430B2 (en) 1990-04-03 1990-04-03 Production method of d-isocitric acid by fermentation method

Publications (2)

Publication Number Publication Date
JPH03290194A true JPH03290194A (en) 1991-12-19
JP2877430B2 JP2877430B2 (en) 1999-03-31

Family

ID=13955183

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8887590A Expired - Lifetime JP2877430B2 (en) 1990-04-03 1990-04-03 Production method of d-isocitric acid by fermentation method

Country Status (1)

Country Link
JP (1) JP2877430B2 (en)

Also Published As

Publication number Publication date
JP2877430B2 (en) 1999-03-31

Similar Documents

Publication Publication Date Title
US3843466A (en) Method of producing dicarboxylic acids by fermentation
Berovic et al. Citric acid production
US2749279A (en) Enzymatic production of l-glutamic acid
CA1334515C (en) Fermentation process for carboxylic acids
Milsom Organic acids by fermentation, especially citric acid
CA2075177C (en) Process for the production os sophorosids by fermentation with continuous fatty acids ester or oil supply
Finogenova et al. Properties of Candida lipolytica mutants with the modified glyoxylate cycle and their ability to produce citric and isocitric acid: II. Synthesis of citric and isocitric acid by C. lipolytica mutants and peculiarities of their enzyme systems
US3809611A (en) Process for producing citric acid
US5026641A (en) Bacteria culture and fermentation using the same
JPH03290194A (en) Production of d-isocitric acid by fermentation
US3099604A (en) Method of producing l-threonine by fermentation
JPS592692A (en) Production of alpha-isopropyl malic acid by fermentation
JP3165688B2 (en) Production method of d-isocitric acid by fermentation method
US4310635A (en) Fermentative production of D(-)-β-hydroxyisobutyric acid
FR2483948A1 (en) PRODUCTION OF L-PROLINE BY FERMENTATION
US3619368A (en) Preparation of a cellular material rich in protein
US4155811A (en) Fermentation process for the production of citric acid
Humphrey et al. Industrial fermentation: principles, processes, and products
US3121668A (en) Method for the production of 1-glutamic acid
US3022223A (en) Biosynthesis of alpha-ketoglutaric acid
US3698999A (en) Fermentative preparation of coenzyme a
US2647074A (en) Production of riboflavin by microbiological fermentation
DE2152548C3 (en) Process for the preparation of L-hydroxyphenylalanines
US4286060A (en) Process for production of an amino acid
JP2922213B2 (en) Method for producing 5&#39;-inosinic acid by fermentation method

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080122

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090122

Year of fee payment: 10

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313111

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090122

Year of fee payment: 10

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090122

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100122

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110122

Year of fee payment: 12

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110122

Year of fee payment: 12