JPH10174593A - Production of glycolic acid by yeast - Google Patents

Production of glycolic acid by yeast

Info

Publication number
JPH10174593A
JPH10174593A JP8337124A JP33712496A JPH10174593A JP H10174593 A JPH10174593 A JP H10174593A JP 8337124 A JP8337124 A JP 8337124A JP 33712496 A JP33712496 A JP 33712496A JP H10174593 A JPH10174593 A JP H10174593A
Authority
JP
Japan
Prior art keywords
glycolic acid
yeast
medium
genus
ethylene glycol
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
Application number
JP8337124A
Other languages
Japanese (ja)
Inventor
Akira Shimizu
昌 清水
Michihiko Kataoka
道彦 片岡
Mitsuo Kawase
三雄 川瀬
Yuji Kawase
優治 川瀬
Tadahiko Inukai
忠彦 犬飼
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.)
BISEIKEN KK
NGK Insulators Ltd
Original Assignee
BISEIKEN KK
NGK Insulators 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 BISEIKEN KK, NGK Insulators Ltd filed Critical BISEIKEN KK
Priority to JP8337124A priority Critical patent/JPH10174593A/en
Publication of JPH10174593A publication Critical patent/JPH10174593A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for effectively producing a highly pure glycolic acid by utilizing an yeast. SOLUTION: A strain belonging to one of Pichia, Sporobolomyces, Torulopsis, Rhodotorula and Kluyveromyces is cultured in a culturing medium containing ethylene glycol, and the objective glycolic acid is separated and gathered from the culturing medium in the method for producing a highly pure glycolic acid. A continuous filtering production is facilitated by performing the culturing of the strain in a fermenting vessel 1 having a membrane filtering device 2, separating and gathering the glycolic acid in the culturing medium by the membrane filtering device 2, and continuously charging the ethylene glycol to the culturing medium.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、酵母によるグリコ
ール酸の生産方法に関するものである。
[0001] The present invention relates to a method for producing glycolic acid by yeast.

【0002】[0002]

【従来の技術】近年、グリコール酸にしわ防止の効果が
あることが示され、化粧品の原料としての需要の伸びが
期待されている。従来、グリコール酸は化学合成法によ
り生産されていたのであるが、化学合成法で得られたグ
リコール酸には夾雑物としてホルムアルデヒド等の刺激
物質が残存し、化粧品に刺激性が残るという問題があっ
た。
2. Description of the Related Art In recent years, glycolic acid has been shown to have an effect of preventing wrinkles, and demand for raw materials for cosmetics is expected to increase. Conventionally, glycolic acid has been produced by a chemical synthesis method, but glycolic acid obtained by the chemical synthesis method has a problem that irritants such as formaldehyde remain as contaminants and irritancy remains in cosmetics. Was.

【0003】[0003]

【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、化粧品の原料とするに適した高純度
のグリコール酸を、酵母を利用することにより効率的に
生産することができる酵母によるグリコール酸の生産方
法を提供するためになされたものである。
DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned conventional problems, and is intended to efficiently produce high-purity glycolic acid suitable for use as a raw material for cosmetics by utilizing yeast. The purpose of the present invention is to provide a method for producing glycolic acid by a yeast.

【0004】[0004]

【課題を解決するための手段】上記の課題を解決するた
めになされた第1の発明は、エチレングリコール含有培
地に、ピシア(Pichia)属、ロードトルラ(Rhodotorul
a )属、スポロボロマイセス(Sporobolomyces)属、ク
リベロマイセス(Kluyveromyces )属、トルロプシス
(Torulopsis)属に属する一つの酵母の菌株を培養し、
培地中からグリコール酸を分離・採取することを特徴と
するものである。また第2の発明は、エチレングリコー
ル含有培地にピシア・ナガニシイ(Pichia naganishii
)を培養し、培地中からグリコール酸を分離・採取す
ることを特徴とするものである。またこの場合に、酵母
の菌株の培養を膜ろ過装置を備えた発酵槽で行い、膜ろ
過装置で培地中からグリコール酸を分離・採取するとと
もに、培地中にエチレングリコールを連続的に投入し、
生産を繰り返す連続ろ過生産を行わせるようにすること
が好ましい。
Means for Solving the Problems A first invention made to solve the above-mentioned problem is that a medium containing Pichia and Rhodotorulum is added to a medium containing ethylene glycol.
a) culturing a strain of one yeast belonging to the genus, genus Sporobolomyces, genus Kluyveromyces, genus Torulopsis,
It is characterized in that glycolic acid is separated and collected from the medium. In the second invention, Pichia naganishii (Pichia naganishii) was added to a medium containing ethylene glycol.
), And glycolic acid is separated and collected from the medium. In this case, the yeast strain is cultured in a fermenter equipped with a membrane filtration device, and glycolic acid is separated and collected from the medium by the membrane filtration device, and ethylene glycol is continuously introduced into the medium,
It is preferable to perform continuous filtration production that repeats production.

【0005】[0005]

【発明の実施の形態】本発明では、エチレングリコール
を出発物質として培地中に含有させ、酵母を利用してグ
リコール酸を生産させ、培地中から分離・採取する。培
地中のエチレングリコールの濃度は1〜20%が好まし
く、後記する実施例のように5〜10%程度が特に好まし
い。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, ethylene glycol is contained in a medium as a starting material, glycolic acid is produced using yeast, and separated and collected from the medium. The concentration of ethylene glycol in the medium is preferably from 1 to 20%, and particularly preferably from about 5 to 10% as in Examples described later.

【0006】本発明では上記の目的で、ピシア(Pichi
a)属、ロードトルラ(Rhodotorula )属、クリベロマ
イセス(Kluyveromyces )属の何れかに属する一つの酵
母菌株を利用する。ピシア属の菌株としては、実施例に
用いたPichia naganishii(IFO 1670) の他に、Pichia p
olymorpha(IFO 0195) 、Pichia heedii(IFO10019)等を
利用できる。ロードトルラ属の菌株としては、Rhodotor
ula rubra(IFO 0889)、Rhodotorula glutinis(IFO 000
3)等を利用でき、トルロプシス属の菌株としては、Toru
lopsis nitratophila(IFO 10004)、Torulopsis candida
(IFO 0405)を、スポロボロマイセス属の菌株としては、
Sporobolomyces johnsonii(IFO6903)、Sporobolomyces
coralliformis(IFO 1032)を利用できる。さらにクリベ
ロマイセス属の菌株としては、Kluyveromyces lactis(A
TCC 12426)、Kluyveromyces thermotolerans(ATCC 1069
1)等を利用できる。
In the present invention, Pichia is used for the above purpose.
a) One yeast strain belonging to the genus, Rhodotorula or Kluyveromyces is used. Examples of the strains of the genus Pichia include Pichia naganishii (IFO 1670) used in the examples,
olymorpha (IFO 0195), Pichia heedii (IFO10019) and the like can be used. Rhodotor is a strain of Rhodotorula.
ula rubra (IFO 0889), Rhodotorula glutinis (IFO 000
3), etc., and as a strain of the genus Torulopsis, Toru
lopsis nitratophila (IFO 10004), Torulopsis candida
(IFO 0405) as a strain of the genus Sporoboromyces,
Sporobolomyces johnsonii (IFO6903), Sporobolomyces
coralliformis (IFO 1032) is available. Furthermore, Kluyveromyces lactis (A
TCC 12426), Kluyveromyces thermotolerans (ATCC 1069
1) etc. are available.

【0007】以上に示した酵母の菌株はいずれもそれ自
体はすでに公知のものであり、記載された寄託番号によ
り公的寄託機関から容易に入手することができるもので
ある。これらのいずれかの属に属する菌株をエチレング
リコール含有培地で培養すれば、他の菌株を使用した場
合よりもグリコール酸を効率よく生産させることができ
る。なお、各属の酵母の特徴については、例えば次の文
献に記載されている。 Pichia naganishii(IFO 1670) J.Ferment.Technol. 5
2:1 (1974) Pichia heedii(IFO 10019) Int.J.Syst.Bacterio
l. 28:326 (1978)
[0007] All of the yeast strains described above are already known per se and can be easily obtained from public depository institutions by the stated deposit numbers. When a strain belonging to any of these genera is cultured in a medium containing ethylene glycol, glycolic acid can be produced more efficiently than when other strains are used. The characteristics of yeasts of each genus are described, for example, in the following documents. Pichia naganishii (IFO 1670) J. Ferment.Technol. 5
2: 1 (1974) Pichia heedii (IFO 10019) Int.J.Syst.Bacterio
l. 28: 326 (1978)

【0008】また、図1に示す装置を使用することによ
って、グリコール酸の連続ろ過生産が可能となる。図1
において、1は発酵槽、2は発酵槽1に接続された膜ろ
過装置、3はエチレングリコールのタンク、4はイオン
交換カラム、5は溶出液のタンクである。発酵槽1の内
部の培地中では前記したいずれかの菌株の酵母が培養さ
れており、培地はポンプ6により膜ろ過装置2へ移送さ
れて培地と菌体とが分離され、菌体は発酵槽1へ戻され
る。その一方、タンク3からエチレングリコールが発酵
槽1へ連続的に投入される。なお、膜ろ過装置2で分離
されたグリコール酸を含む培地はイオン交換カラム4に
通液され、グリコール酸が分離・採取される。以下に本
発明の実施例を示す。
Further, the use of the apparatus shown in FIG. 1 enables continuous filtration and production of glycolic acid. FIG.
, 1 is a fermentation tank, 2 is a membrane filtration device connected to the fermentation tank 1, 3 is an ethylene glycol tank, 4 is an ion exchange column, and 5 is an eluate tank. In the culture medium inside the fermenter 1, yeast of any of the aforementioned strains is cultured, and the culture medium is transferred to the membrane filtration device 2 by the pump 6, where the culture medium and the cells are separated. Returned to 1. On the other hand, ethylene glycol is continuously supplied from the tank 3 to the fermenter 1. The medium containing glycolic acid separated by the membrane filtration device 2 is passed through the ion exchange column 4 to separate and collect glycolic acid. Hereinafter, examples of the present invention will be described.

【0009】[0009]

【実施例】〔実施例1〕 Nutrient broth(DIFCO) 0.8 %、プロピレン・グリコー
ル1%、pH7.0 の組成の培地300ml に、予め同斜面培地
で28℃、2日間培養して得られたPichia属に属する菌株
Pichia naganishii(IFO 1670) の種培養から一白金耳を
接種し、28℃、2日間振とう培養を行った。培養終了
後、遠心分離(8000rpm、20min)により菌体を集菌し、更
に生理食塩水にて洗浄した。得られた菌体に10%エチレ
ングリコールを含む250mM、リン酸バッファー(pH7.0)
を加えて50mlとし、30℃、30時間反応を行った。反応終
了後、遠心分離により菌体を除去し、その上清をHPL
Cにて下記条件にて分析した。その結果、35.3g/Lのグ
リコール酸を得た。 (分析条件) カラム:QAE−2SW(4.6×250 mm) 移動相:1/15M KPB(pH6.4) 検出 :UV210 nm 流速 :1ml/min
Example 1 Example 1 Pichia obtained by previously culturing in 300 ml of a medium having a composition of 0.8% Nutrient broth (DIFCO), 1% propylene glycol, and pH 7.0 on the same slant medium at 28 ° C. for 2 days. Strains belonging to the genus
One platinum loop was inoculated from a seed culture of Pichia naganishii (IFO 1670), and shake culture was performed at 28 ° C. for 2 days. After completion of the culture, the cells were collected by centrifugation (8000 rpm, 20 min), and washed with physiological saline. 250 mM, phosphate buffer (pH 7.0) containing 10% ethylene glycol in the obtained cells
Was added to 50 ml, and the reaction was carried out at 30 ° C. for 30 hours. After completion of the reaction, the cells were removed by centrifugation, and the supernatant was separated by HPL.
C was analyzed under the following conditions. As a result, 35.3 g / L of glycolic acid was obtained. (Analysis conditions) Column: QAE-2SW (4.6 × 250 mm) Mobile phase: 1/15 M KPB (pH 6.4) Detection: UV 210 nm Flow rate: 1 ml / min

【0010】〔実施例2〕実施例1と同様の条件で、そ
の他の菌株についてもグリコール酸の生産を実施した。
その結果を表1に示す。 表1に示したように、本発明
によりピシア属、ロードトルラ属、サッカロマイセス
属、クリベロマイセス属の何れかに属する酵母の菌株を
用いれば、Hansenula 属やCandida 属の他の菌株を用い
た場合に比較してグリコール酸の生産性が良く、特にピ
シア属はグリコール酸の生産に向いていることが示され
た。
Example 2 Glycolic acid was produced for other strains under the same conditions as in Example 1.
Table 1 shows the results. As shown in Table 1, according to the present invention, when a yeast strain belonging to any of the genus Pichia, Rhodotorula, Saccharomyces, or Kleberomyces was used, the strain was compared with that of other strains of the genus Hansenula or Candida. Thus, it was shown that the productivity of glycolic acid was good, and that the genus Piscia was particularly suitable for the production of glycolic acid.

【表1】 [Table 1]

【0011】〔実施例3〕Nutrient broth(DIFCO) 0.8
%、エチレングリコール5%、pH7.0 の組成の培地3L
に、あらかじめ同培地100ml で28℃、2晩振とう培養し
て得られたPichianaganishii(IFO 1670) の種培養液を
接種し、28℃で0.5 M NaOH でpHを7.0 に調整しながら
40時間培養した。培養終了後、遠心分離により菌体を除
去し、その上清をHPLCにより分析したところ、グリ
コール酸濃度は、28.7g/Lであった。得られた上清は、
陰イオン交換カラム(Diaion PA308)にチャージし、洗浄
後、1M NaCl にて溶出し、グリコール酸溶液を回収
し、脱塩濃縮後、乾燥し、粉末グリコール酸68.8g を得
た。この物質がグリコール酸であることの同定は、H
PLCでの保持時間、赤外吸収スペクトル、核磁気
共鳴スペクトル、において標準のグリコール酸と良く一
致していたことから成された。得られた粉末グリコール
酸のホルムアルデヒド含量を測定したところ、全く検出
されなかった。
[Example 3] Nutrient broth (DIFCO) 0.8
%, Ethylene glycol 5%, pH 7.0, medium 3L
A seed culture of Pichianaganishii (IFO 1670) obtained by shaking culture in 100 ml of the same medium at 28 ° C for 2 nights was inoculated in advance, and the pH was adjusted to 7.0 with 0.5 M NaOH at 28 ° C.
Incubated for 40 hours. After completion of the culture, the cells were removed by centrifugation, and the supernatant was analyzed by HPLC. As a result, the glycolic acid concentration was 28.7 g / L. The resulting supernatant is
After charging to an anion exchange column (Diaion PA308), washing and elution with 1 M NaCl, the glycolic acid solution was recovered, desalted and concentrated, and dried to obtain 68.8 g of powdered glycolic acid. The identity of this substance as glycolic acid was determined by H
This was based on good agreement with standard glycolic acid in retention time in PLC, infrared absorption spectrum, and nuclear magnetic resonance spectrum. When the formaldehyde content of the obtained glycolic acid powder was measured, it was not detected at all.

【0012】〔実施例4〕膜ろ過装置を備えた発酵槽
(図1)を用いて、実施例3と同様にPichia naganishi
i(IFO 1670) をNutrient broth(DIFCO) 0.8 %、エチレ
ングリコール5%、pH7.0 の組成の培地にて、0.5 M N
aOH でpHを7.0 に調整しながら、28℃で40時間培養し
た。40時間後よりろ過を開始し、菌体はMF膜(Cefilt
0.2 μm :日本碍子製) にて系内にとどまり、生産され
たグリコール酸は、MF膜を通して系外に流出され、こ
れを直列に連結した陰イオン交換カラム(Diaion PA308)
にて吸着した。吸着されたグリコール酸は、洗浄後、1
M NaCl 水溶液で溶出され、回収された。一方、系内に
とどまった菌体を利用し、更にエチレングリコールを連
続的に投入する事により、27.4g/Lのグリコール酸を連
続的に生産することができた。
Example 4 Pichia naganishi in the same manner as in Example 3 using a fermenter (FIG. 1) equipped with a membrane filtration device.
i (IFO 1670) in a medium having a composition of 0.8% Nutrient broth (DIFCO), 5% ethylene glycol, pH 7.0, 0.5M N
The cells were cultured at 28 ° C. for 40 hours while adjusting the pH to 7.0 with aOH. Filtration was started after 40 hours, and the cells were treated with MF membrane (Cefilt).
0.2 μm: made by Nippon Insulator), and the produced glycolic acid flows out of the system through the MF membrane and is connected to the anion exchange column (Diaion PA308).
Was adsorbed. After washing, the adsorbed glycolic acid becomes 1
Eluted with M NaCl aqueous solution and collected. On the other hand, 27.4 g / L of glycolic acid could be continuously produced by using the cells remaining in the system and continuously adding ethylene glycol.

【0013】[0013]

【発明の効果】以上に説明したように、本発明の酵母に
よるグリコール酸の生産方法によれば、高純度のグリコ
ール酸を効率的に生産することができる。しかも、この
ようにして酵母により生産されたグリコール酸は従来の
化学合成法により生産されたグリコール酸とは異なり、
ホルムアルデヒド等の夾雑物が残存することがないの
で、化粧品の原料として使用しても刺激感がない利点が
ある。
As described above, according to the method for producing glycolic acid by yeast of the present invention, high-purity glycolic acid can be efficiently produced. Moreover, glycolic acid produced by yeast in this way is different from glycolic acid produced by conventional chemical synthesis,
Since impurities such as formaldehyde do not remain, there is an advantage that there is no irritation when used as a raw material for cosmetics.

【図面の簡単な説明】[Brief description of the drawings]

【図1】連続ろ過生産装置を説明するブロック図であ
る。
FIG. 1 is a block diagram illustrating a continuous filtration production device.

【符号の説明】[Explanation of symbols]

1 発酵槽、2 膜ろ過装置、3 エチレングリコール
のタンク、4 イオン交換カラム、5 溶出液のタン
ク、6 ポンプ
1. Fermentation tank, 2. Membrane filtration device, 3. Ethylene glycol tank, 4. Ion exchange column, 5. Eluate tank, 6. Pump

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI C12R 1:84) (C12P 7/42 C12R 1:645) (C12P 7/42 C12R 1:88) (72)発明者 川瀬 三雄 愛知県名古屋市瑞穂区須田町2番56号 日 本碍子株式会社内 (72)発明者 川瀬 優治 愛知県名古屋市瑞穂区須田町2番56号 日 本碍子株式会社内 (72)発明者 犬飼 忠彦 愛知県名古屋市西区枇杷島4丁目9番24号──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification symbol FI C12R 1:84) (C12P 7/42 C12R 1: 645) (C12P 7/42 C12R 1:88) (72) Inventor Mitsuo Kawase Inside Insulators Co., Ltd., 2-56, Suda-cho, Mizuho-ku, Nagoya-shi, Aichi (72) Inventor Yuji Kawase Inside Insulators Co., Ltd. 2-56, Suda-cho, Mizuho-ku, Nagoya, Aichi, Japan 4-24-9 Biwajima, Nishi-ku, Nagoya City, Aichi Prefecture

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 エチレングリコール含有培地に、ピシア
(Pichia)属、ロードトルラ(Rhodotorula )属、スポ
ロボロマイセス(Sporobolomyces)属、クリベロマイセ
ス(Kluyveromyces )属、トルロプシス(Torulopsis)
属に属する一つの酵母の菌株を培養し、培地中からグリ
コール酸を分離・採取することを特徴とする酵母による
グリコール酸の生産方法。
1. A medium containing ethylene glycol, a genus of Pichia, a genus of Rhodotorula, a genus of Sporobolomyces, a genus of Kluyveromyces, and a tolulopsis.
A method for producing glycolic acid by yeast, comprising culturing a strain of one yeast belonging to the genus, and separating and collecting glycolic acid from the medium.
【請求項2】 エチレングリコール含有培地にピシア・
ナガニシイ(Pichia naganishii )を培養し、培地中か
らグリコール酸を分離・採取することを特徴とする酵母
によるグリコール酸の生産方法。
2. A method for preparing a medium containing ethylene glycol, comprising:
A method for producing glycolic acid by yeast, comprising culturing Pichia naganishii and separating and collecting glycolic acid from the medium.
【請求項3】 酵母の菌株の培養を膜ろ過装置を備えた
発酵槽で行い、膜ろ過装置で培地中からグリコール酸を
分離・採取するとともに、培地中にエチレングリコール
を連続的に投入し、生産を繰り返す連続ろ過生産を行わ
せる請求項1記載の酵母によるグリコール酸の生産方
法。
3. The yeast strain is cultured in a fermenter equipped with a membrane filtration device, and glycolic acid is separated and collected from the medium by the membrane filtration device, and ethylene glycol is continuously introduced into the medium. 2. The method for producing glycolic acid by yeast according to claim 1, wherein continuous filtration production is repeated.
JP8337124A 1996-12-17 1996-12-17 Production of glycolic acid by yeast Pending JPH10174593A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8337124A JPH10174593A (en) 1996-12-17 1996-12-17 Production of glycolic acid by yeast

Publications (1)

Publication Number Publication Date
JPH10174593A true JPH10174593A (en) 1998-06-30

Family

ID=18305674

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH10174593A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005106005A1 (en) * 2004-04-27 2005-11-10 Mitsui Chemicals, Inc. Process for producing hydroxycarboxylic acid
WO2007129466A1 (en) 2006-05-09 2007-11-15 Mitsui Chemicals, Inc. Method of producing hydroxycarboxylic acid by regenerating coenzyme
US9133444B2 (en) 2006-05-09 2015-09-15 Mitsui Chemicals, Inc. Method for producing hydroxycarboxylic acid by enhancing synthesis of coenzyme
US9783809B2 (en) 2011-10-04 2017-10-10 Teknologian Tutkimuskeskus Vtt Oy Eukaryotic cell and method for producing glycolic acid
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US8728780B2 (en) 2004-04-27 2014-05-20 Mitsui Chemicals, Inc. Process for producing hydroxycarboxylic acid
WO2005106005A1 (en) * 2004-04-27 2005-11-10 Mitsui Chemicals, Inc. Process for producing hydroxycarboxylic acid
JPWO2005106005A1 (en) * 2004-04-27 2008-03-13 三井化学株式会社 Method for producing hydroxycarboxylic acids
JP4523939B2 (en) * 2004-04-27 2010-08-11 三井化学株式会社 Method for producing hydroxycarboxylic acids
US9133444B2 (en) 2006-05-09 2015-09-15 Mitsui Chemicals, Inc. Method for producing hydroxycarboxylic acid by enhancing synthesis of coenzyme
US8748157B2 (en) 2006-05-09 2014-06-10 Mitsui Chemicals, Inc. Method for producing hydroxycarboxylic acid by regenerating coenzyme
WO2007129466A1 (en) 2006-05-09 2007-11-15 Mitsui Chemicals, Inc. Method of producing hydroxycarboxylic acid by regenerating coenzyme
US9783809B2 (en) 2011-10-04 2017-10-10 Teknologian Tutkimuskeskus Vtt Oy Eukaryotic cell and method for producing glycolic acid
US11535873B2 (en) 2017-09-07 2022-12-27 The Governing Council Of The University Of Toronto Production of glycolate from ethylene glycol and related microbial engineering
US20220257499A1 (en) * 2021-02-12 2022-08-18 Chanel Parfums Beaute Cosmetic composition comprising a yeast hydrolysate
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