JPS5853917B2 - Production method of coenzyme Q - Google Patents

Production method of coenzyme Q

Info

Publication number
JPS5853917B2
JPS5853917B2 JP9158478A JP9158478A JPS5853917B2 JP S5853917 B2 JPS5853917 B2 JP S5853917B2 JP 9158478 A JP9158478 A JP 9158478A JP 9158478 A JP9158478 A JP 9158478A JP S5853917 B2 JPS5853917 B2 JP S5853917B2
Authority
JP
Japan
Prior art keywords
coenzyme
extract
extraction
butyl alcohol
concentrated
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
JP9158478A
Other languages
Japanese (ja)
Other versions
JPS5519049A (en
Inventor
邦雄 伊藤
正裕 杉本
和幸 峰浦
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 JP9158478A priority Critical patent/JPS5853917B2/en
Publication of JPS5519049A publication Critical patent/JPS5519049A/en
Publication of JPS5853917B2 publication Critical patent/JPS5853917B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は助酵素Qの製造法に関する。[Detailed description of the invention] The present invention relates to a method for producing coenzyme Q.

さらに詳しくは、助酵素Qを含有する生菌体から助酵素
Qを抽出するに際し、抽出溶媒として5sc−ブチルア
ルコールまたはtert−アミルアルコールを用いるこ
とを特徴とする助酵素Qの製造法にする。
More specifically, the method for producing coenzyme Q is characterized in that 5sc-butyl alcohol or tert-amyl alcohol is used as an extraction solvent when coenzyme Q is extracted from living cells containing coenzyme Q.

従来、補酵素Qを含有する動植物の組織、微生物の菌体
等の水懸濁液をアルカリ性で処理し、しかる抜水と分離
し得る有機溶媒、ブチルアルコール、n−へキサン、イ
ソオクタン、石油ニーfiし、ジクロルエタン、メチル
インブチルケトンまたは酢酸エチル、で抽出して補酵素
Qを含有する疎水性溶媒抽出画分を取得することは知ら
れている(特開昭53−38690号公報)。
Conventionally, aqueous suspensions of animal and plant tissues, microbial cells, etc. containing coenzyme Q have been treated with alkalinity, and the water has been removed and separated using organic solvents such as butyl alcohol, n-hexane, isooctane, and petroleum powder. It is known to obtain a hydrophobic solvent-extracted fraction containing coenzyme Q by extracting with dichloroethane, methyl imbutyl ketone or ethyl acetate (Japanese Unexamined Patent Publication No. 53-38690).

しかしながら、助酵素Qを含有するバクテリアの生菌体
をアルカリ性で処理することなく上記の有機溶媒のうち
、n−ブチルアルコール、ヘキサン、メチルイソブチル
ケトン、酢酸エチル等で抽出しても、助酵素Qの抽出率
は低くかった。
However, even if the living cells of bacteria containing coenzyme Q are extracted with n-butyl alcohol, hexane, methyl isobutyl ketone, ethyl acetate, etc. among the above organic solvents without alkaline treatment, coenzyme Q The extraction rate was low.

本発明者らは、助酵素Qを含有するバクテリアの生菌体
をアルカリ処理することなく助酵素Qを抽出率よく抽出
する際の水と分離できる有機溶媒について種々検討した
結果、特に5ec−ブチルアルコールまたはter t
−アミルアルコールを用いると、バクテリアの生菌体を
従来の様にpH10以上、加熱温度60〜150’C,
加熱時間10分〜10時間でアルカリ処理することなく
、無処理で直接抽出することにより高収率でかつ短時間
に助酵素Qが抽出されることを見出し本発明を完成した
The present inventors have conducted various studies on organic solvents that can be separated from water when extracting coenzyme Q with a good extraction rate without alkali treatment of living bacteria containing coenzyme Q. In particular, 5ec-butyl alcohol or tert
- When amyl alcohol is used, viable bacteria can be grown at a pH of 10 or higher, at a heating temperature of 60 to 150'C, as in the conventional method.
The present invention was completed based on the discovery that coenzyme Q can be extracted in a high yield and in a short time by direct extraction without alkali treatment with a heating time of 10 minutes to 10 hours.

以下に本発明の詳細な説明する。The present invention will be explained in detail below.

まず5ec−ブチルアルコールまたはtert−アミル
アルコールが助酵素Q1oの溶解度が高い他の水と分離
できるn−ブチルアルコール、1so−ブチルアルコー
ル、n−アミルアルコール、酢酸エチル、メチルイソブ
チルケトン、メチルエチルケトン、クロロホルム、ヘキ
サン等の有機溶媒に比してバクテリア生菌体からの助酵
素Qzoの抽出率がいかに高いかを示す実験例を以下に
示す。
First, 5ec-butyl alcohol or tert-amyl alcohol can be separated from other waters in which coenzyme Q1o has a high solubility. An experimental example showing how high the extraction rate of the coenzyme Qzo from living bacterial cells is compared to organic solvents such as hexane is shown below.

実験例 バラコツカス・デニトリフィカンスATCC19367
の生菌体水懸濁液(pH11,0)に2倍量の各種有機
溶媒を加え、室温で2時間撹拌した後の助酵素QIOの
抽出率を調べた結果を第1表に示す。
Experimental example Baracoccus denitrificans ATCC19367
Table 1 shows the results of examining the extraction rate of coenzyme QIO after adding twice the amount of various organic solvents to an aqueous suspension of live bacterial cells (pH 11.0) and stirring at room temperature for 2 hours.

一般に、ある物質の抽出率は、該物質の溶解度と関係す
ると考えられるが、第1表から判る様に、各種ブチルア
ルコールの場合、助酵素QIOの溶解度は29〜3.1
?/lとほぼ同じ程度であるが、驚くべきことには、
助酵素QIOの抽出率は5ee−ブチルアルコールが他
のn−ブチルアルコールまたは1so−ブチルアルコー
ルに比べて非常に高くなっている。
Generally, the extraction rate of a certain substance is considered to be related to the solubility of the substance, but as can be seen from Table 1, in the case of various butyl alcohols, the solubility of coenzyme QIO is 29 to 3.1.
? /l, but surprisingly,
The extraction rate of coenzyme QIO is much higher in 5ee-butyl alcohol than in other n-butyl alcohols or 1so-butyl alcohols.

さらに他の有機溶媒よりも抽出率が非常に高くなってい
る。
Furthermore, the extraction rate is much higher than that of other organic solvents.

又ter を−アミルアルコールについてもn−アミル
アルコールに比べて助酵素Q1oの抽出率が非常に高く
、又5ec−ブチルアルコール以外の水と分離できる有
機溶媒に比べても助酵素Q、。
Also, with regard to ter-amyl alcohol, the extraction rate of coenzyme Q1o is much higher than with n-amyl alcohol, and also compared with organic solvents that can be separated from water other than 5ec-butyl alcohol.

の抽出率が高くなっている。The extraction rate is high.

かくの如き、高い抽出率を示すことは従来の公知文献は
荷んら示唆していない。
No prior known literature suggests that such a high extraction rate is exhibited.

本発明に用いられる助酵素Qを含有する生菌体としては
、助酵素Qを含有する細菌を培養した培養物、培養後集
菌した菌体、菌体の水懸濁液等があげられる。
Examples of the viable bacterial cells containing coenzyme Q used in the present invention include a culture of bacteria containing coenzyme Q, bacterial cells collected after culturing, and an aqueous suspension of bacterial cells.

又助酵素Q含有物中の助酵素Qとしてはいかなるもので
あってもよい。
Further, the coenzyme Q in the coenzyme Q-containing material may be of any kind.

5ec−ブチルアルコールまたはtert−アミルアル
コールによる撹拌抽出は室温で1〜数時間行なうのが好
ましい。
The stirring extraction with 5ec-butyl alcohol or tert-amyl alcohol is preferably carried out at room temperature for 1 to several hours.

溶剤の添加量および抽出時間は、原料即ち、助酵素Q含
有物により適宜これを変更し得る。
The amount of solvent added and the extraction time can be changed as appropriate depending on the raw material, that is, the coenzyme Q-containing substance.

抽出の前処理(例えばアルカリ処理等)は必要でなく抽
出時の室温、pHには特に制限はないが、リン脂質の影
響をより少なくする為に室温下pH1・O〜11で行な
うのが最適である。
Pre-treatment for extraction (e.g. alkaline treatment, etc.) is not necessary and there are no particular restrictions on room temperature or pH during extraction, but it is best to perform extraction at room temperature and at pH 1.0 to 11 in order to further reduce the influence of phospholipids. It is.

抽出液はシリカゲルカラムクロマトグラフィーで精製し
、エタノールで結晶化せしめる方法、あるいは抽出液を
濃縮後少量のアセトンに溶解し、活性処理による脱色後
冷却し、結晶化せしめる方法等により助酵素Qの結晶が
得られる。
The extract is purified by silica gel column chromatography and crystallized with ethanol, or the extract is concentrated, dissolved in a small amount of acetone, decolorized by activation treatment, cooled, and crystallized to obtain coenzyme Q crystals. is obtained.

以下に実施例を示す。Examples are shown below.

実施例 1 グルコース19/d11 イーストエキス0.59/
dl。
Example 1 Glucose 19/d11 Yeast extract 0.59/
dl.

ペグ1フ1g/di、肉エキス0.5 g/dl、食塩
0、3 g/di、の組成を有するpH7,2の借地1
001をファーメンタ−に入れ殺菌後、同一組成であら
かじめフラスコで倍養したパラコツカス・デニトリフィ
カンスATCC19367の倍養液21を接種し、30
℃で撹拌数15Orpm通気量40に分で96時間好気
培養し、培養液から生菌体を集め、IOAの水に懸濁(
乾燥菌体として750g、助酵素Q含有315■)し、
pH11に調整した後101のsecブチルアルコール
を加え、室温下で1時間撹拌抽出し、遠心分離により5
ec−プチルアルコール層を分離した。
Lease 1 with a pH of 7.2 and a composition of 1 peg 1 g/di, meat extract 0.5 g/dl, and salt 0.3 g/di.
After putting 001 into a fermenter and sterilizing it, inoculate it with culture solution 21 of Paracoccus denitrificans ATCC 19367, which had the same composition and had been cultured in a flask beforehand.
Aerobically cultured at ℃ for 96 hours with stirring number 15 rpm and aeration rate 40 min, live bacterial cells were collected from the culture solution and suspended in IOA water (
750g as dry bacterial cells, 315g containing coenzyme Q),
After adjusting the pH to 11, add 101 sec of butyl alcohol, stir and extract at room temperature for 1 hour, and centrifuge for 5 sec.
The ec-butyl alcohol layer was separated.

この操作を更に1回繰り返えした後、全抽出液を集めた
After repeating this operation once more, all extracts were collected.

この際の抽出液には助酵素Qが289■含まれていた。The extract at this time contained 289 μ of coenzyme Q.

この抽出液を濃縮しシリカゲル101を詰めたカラムに
通塔した後、アセトンで溶出した。
This extract was concentrated, passed through a column packed with silica gel 101, and then eluted with acetone.

助酵素Qの溶出区分を濃縮し、少量の活性炭を加え済過
し、炉液を冷却すると橙黄色の結晶237■が得られた
The eluted fraction of coenzyme Q was concentrated, a small amount of activated carbon was added, and the furnace solution was cooled to obtain 237 cm of orange-yellow crystals.

得られた物質はペーパークロマトグラフィー薄層クロマ
トグラフィー、元素分析、核磁気共鳴スペクトル、融点
の結果より助酵素QIOであることが確認された。
The obtained substance was confirmed to be coenzyme QIO from the results of paper chromatography, thin layer chromatography, elemental analysis, nuclear magnetic resonance spectrum, and melting point.

実施例 2 実施例1と同様にして、シュードモナス・アエルギノー
サATCC15246を培養し、培養物から生菌体を集
め21の水に懸濁(乾燥菌体として160g、助酵素Q
112■含有)し、pH10に調整した後、tert−
アミルアルコール41え加え室温で3時間撹拌抽出し、
遠心分離によりtert−アミルアルコール層を分離し
た。
Example 2 In the same manner as in Example 1, Pseudomonas aeruginosa ATCC 15246 was cultured, and viable cells were collected from the culture and suspended in 21 water (160 g as dry cells, coenzyme Q).
After adjusting the pH to 10, tert-
Added amyl alcohol 41, stirred and extracted at room temperature for 3 hours,
The tert-amyl alcohol layer was separated by centrifugation.

この操作を更に1回繰り返えした後、全抽出液を集めた
After repeating this operation once more, all extracts were collected.

抽出液中には助酵素Qが99■含まれていた。The extract contained 99 μ of coenzyme Q.

この抽出液を濃縮後、シリカゲル50gを詰めたカラム
に通塔した後、アセトンで溶出した。
This extract was concentrated, passed through a column packed with 50 g of silica gel, and then eluted with acetone.

助酵素Qを含む溶出区分を濃縮し、少量の活性炭を加え
済過し、滑液を冷却すると橙黄色の結晶71■が得られ
た。
The eluted fraction containing coenzyme Q was concentrated, a small amount of activated carbon was added, and the synovial fluid was cooled, yielding 71 cm of orange-yellow crystals.

本品は逆相薄層クロマトグラフィーによる同定の結果よ
り、助酵素Q、であることが確認された。
This product was identified as Coenzyme Q by reverse phase thin layer chromatography.

実施例 3 実施例1と同様にして、アグロバクテリウム・ツメファ
シェンスATCC4720を培養シ、培養物を遠心分離
法により菌体濃縮を行ない、その菌体懸濁液10A?(
乾燥菌体として62(Bi’、助酵素Q含量341■)
について実施例1と同様にして抽出を行ない、助酵素Q
320■を含む抽出液を得た。
Example 3 In the same manner as in Example 1, Agrobacterium tumefaciens ATCC4720 was cultured, and the culture was concentrated by centrifugation to obtain a 10A cell suspension. (
62 (Bi', coenzyme Q content 341■) as a dry bacterial cell
was extracted in the same manner as in Example 1, and coenzyme Q
An extract containing 320 μm was obtained.

この抽出液を減圧下で濃縮乾固し、残渣を少量のアセト
ンに溶解し、少量の活性炭を加え脱色後そのp液を更に
濃縮し冷却すると、助酵素Q1oの結晶273■が得ら
れた。
This extract was concentrated to dryness under reduced pressure, the residue was dissolved in a small amount of acetone, a small amount of activated carbon was added for decolorization, and the p liquid was further concentrated and cooled to obtain crystals 273 of coenzyme Q1o.

実施例 4 実施例1と同様にしてプロテウス・ブルガリスATCC
19181を培養集菌し、その水懸濁液1M(乾燥菌体
として570g、助酵素Q含量74rnIl)を実施例
1と同様な方法で抽出精製し、助酵素Qの結晶61■を
得た。
Example 4 Proteus vulgaris ATCC was prepared in the same manner as in Example 1.
19181 was cultured and harvested, and a 1M aqueous suspension thereof (570 g as dry cells, coenzyme Q content 74 rnIl) was extracted and purified in the same manner as in Example 1 to obtain 61■ crystals of coenzyme Q.

本品は逆相薄層クロマトグラフィーによる同定の結果、
助酵素Q7であることが解認された。
This product was identified by reversed phase thin layer chromatography.
It was confirmed that it was coenzyme Q7.

Claims (1)

【特許請求の範囲】[Claims] 1 助酵素Qを含有する生菌体から助酵素Qを抽出する
に際し、抽出溶媒として5ec−ブチルアルコールまた
はtert−アミルアルコールを用いることを特徴とす
る助酵素Qの製造法。
1. A method for producing coenzyme Q, which comprises using 5ec-butyl alcohol or tert-amyl alcohol as an extraction solvent when extracting coenzyme Q from living cells containing coenzyme Q.
JP9158478A 1978-07-28 1978-07-28 Production method of coenzyme Q Expired JPS5853917B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9158478A JPS5853917B2 (en) 1978-07-28 1978-07-28 Production method of coenzyme Q

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9158478A JPS5853917B2 (en) 1978-07-28 1978-07-28 Production method of coenzyme Q

Publications (2)

Publication Number Publication Date
JPS5519049A JPS5519049A (en) 1980-02-09
JPS5853917B2 true JPS5853917B2 (en) 1983-12-01

Family

ID=14030587

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9158478A Expired JPS5853917B2 (en) 1978-07-28 1978-07-28 Production method of coenzyme Q

Country Status (1)

Country Link
JP (1) JPS5853917B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6347275A (en) * 1986-08-14 1988-02-29 Tohoku Metal Ind Ltd Winder for toroidal coil

Also Published As

Publication number Publication date
JPS5519049A (en) 1980-02-09

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