JPH101496A - Avermectin purification method - Google Patents
Avermectin purification methodInfo
- Publication number
- JPH101496A JPH101496A JP8152596A JP15259696A JPH101496A JP H101496 A JPH101496 A JP H101496A JP 8152596 A JP8152596 A JP 8152596A JP 15259696 A JP15259696 A JP 15259696A JP H101496 A JPH101496 A JP H101496A
- Authority
- JP
- Japan
- Prior art keywords
- avermectin
- water
- solvent
- miscible
- purifying
- 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.)
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- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Saccharide Compounds (AREA)
Abstract
(57)【要約】
【課題】 クロマトグラフィーを用いない簡便・安価か
つ精製効率が高いアベルメクチンB1aの精製法の提供。
【解決手段】 アベルメクチン含有物を水と混ざり合う
溶媒と接触させてアベルメクチンを抽出した後、該抽出
液を濃縮し、次いで再度水と混ざり合う溶媒および塩を
添加し、不溶物を取得することを特徴とするアベルメク
チンB1aの精製法を提供する。PROBLEM TO BE SOLVED: To provide a simple, inexpensive and highly purified purification method of avermectin B1a without using chromatography. SOLUTION: After extracting avermectin by bringing an avermectin-containing substance into contact with a solvent miscible with water, the extract is concentrated, and then a solvent and a salt miscible with water are added again to obtain an insoluble substance. A method for purifying avermectin B1a is provided.
Description
【0001】[0001]
【発明の属する技術分野】本発明は、アベルメクチンの
発酵培養液から、工業的に煩雑なクロマトグラフィーを
用いずに簡便に高純度のアベルメクチンB1aを精製する
方法に関する。The present invention relates to a method for easily and simply purifying high-purity avermectin B1a from a fermentation broth of avermectin without using industrially complicated chromatography.
【0002】[0002]
【従来の技術】アベルメクチンは、寄生虫薬イベルメク
チン等のアベルメクチン誘導体を合成する際の合成原料
として、またそれ自体家畜動物用の寄生虫薬として広く
使用されている。アベルメクチンを得る際、アベルメク
チンの発酵培養液中には、抗寄生虫活性が高いアベルメ
クチンB1a以外にも類縁体および他の不純物が多く含ま
れている。BACKGROUND OF THE INVENTION Avermectin is widely used as a raw material for synthesizing avermectin derivatives such as ivermectin, a parasite drug, and itself as a parasite drug for livestock animals. When avermectin is obtained, the fermentation broth of avermectin contains many analogs and other impurities in addition to avermectin B1a having high antiparasitic activity.
【0003】一般的なアベルメクチンの精製方法として
は、アベルメクチンの発酵培養液、または発酵培養液を
遠心分離、濾過等に付して得られるアベルメクチンを含
む不溶物に有機溶媒を添加してアベルメクチンを抽出し
た後、シリカゲル、酸化アルミナ、デキストランゲル等
の担体を用いたクロマトグラフィーに付してアベルメク
チンを含む画分を濃縮乾固する方法が知られている。ま
た、濃縮乾固して得られる残渣にメタノール−エチレン
グリコール混合溶媒を加え、メタノールを濃縮留去し、
冷却後結晶を得る方法も知られている(特公平2−17
558)。しかしながら、これらのクロマトグラフィー
を用いる方法では、担体への負荷量が低いため多量のク
ロマト単体および有機溶媒を使用しなければならず、生
産性も低く、得られたアベルメクチン精製品は高価なも
のとなり、工業的には必ずしも満足のいく精製法ではな
い。[0003] As a general method for purifying avermectin, avermectin is extracted by adding an organic solvent to a fermentation broth of avermectin or an insoluble substance containing avermectin obtained by subjecting the fermentation broth to centrifugation, filtration or the like. After that, a method is known in which a fraction containing avermectin is subjected to chromatography using a carrier such as silica gel, alumina oxide, or dextran gel to concentrate and dry the fraction containing avermectin. Further, a methanol-ethylene glycol mixed solvent was added to the residue obtained by concentration to dryness, and methanol was concentrated and distilled off.
A method of obtaining crystals after cooling is also known (Japanese Patent Publication No. 2-17)
558). However, in these methods using chromatography, since the load on the carrier is low, a large amount of chromatographic simple substance and organic solvent must be used, the productivity is low, and the purified avermectin purified product is expensive. However, it is not always an industrially satisfactory purification method.
【0004】また、アベルメクチンの発酵培養液を遠心
分離、濾過等に付して得られるアベルメクチンを含む不
溶物に水と混ざり合う溶媒を添加してアベルメクチンを
抽出した後、抽出液に水および塩化ナトリウム等の無機
塩等を添加して析出した沈殿物を取得するアベルメクチ
ンの精製方法が知られている(WO95/0341
9)。しかしながら、この方法では、沈殿物を固液分離
するときの容量が多くなり、工業的製造法とはなり難
い。Avermectin fermentation broth is subjected to centrifugation, filtration, and the like, and a solvent mixed with water is added to an insoluble material containing avermectin to extract avermectin. Then, water and sodium chloride are added to the extract. Avermectin purification method of obtaining a precipitate precipitated by adding an inorganic salt or the like such as is known (WO95 / 0341).
9). However, according to this method, the volume at the time of solid-liquid separation of the precipitate increases, and it is difficult to obtain an industrial production method.
【0005】[0005]
【発明が解決しようとする課題】本発明の目的は、工業
的に煩雑なクロマトグラフィーを用いない簡便・安価か
つ精製効率が高いアベルメクチンB1aの精製法を提供す
ることにある。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for purifying avermectin B1a which is simple, inexpensive and has high purification efficiency without using industrially complicated chromatography.
【0006】[0006]
【課題を解決するための手段】本発明は、アベルメクチ
ン含有物を水と混ざり合う溶媒と接触させてアベルメク
チンを抽出した後、該抽出液を濃縮し、次いで再度水と
混ざり合う溶媒および塩を添加し、不溶物を取得するこ
とを特徴とするアベルメクチンB1aの精製法に関する。
取得した不溶物を水と混ざり合う溶媒と接触させた後、
残留不溶物を除いた溶液を濃縮し、沈殿物を取得するこ
とにより、さらに純度の高いアベルメクチンB1aを得る
ことができる。なお、上記塩は、再度水と混ざり合う溶
媒を添加する前に加えても後に加えても同時に加えても
よい。According to the present invention, an avermectin-containing substance is brought into contact with a solvent miscible with water to extract avermectin, the extract is concentrated, and then a solvent and a salt miscible with water are added again. And a method for purifying avermectin B1a, wherein insoluble matter is obtained.
After contacting the obtained insolubles with a solvent that mixes with water,
Avermectin B1a having higher purity can be obtained by concentrating the solution from which residual insolubles have been removed and obtaining a precipitate. The salt may be added before, after, or simultaneously with the addition of a solvent that is miscible with water.
【0007】[0007]
【発明の実施の形態】アベルメクチン含有物としては、
アベルメクチンの発酵培養液中の不溶物、合成アベルメ
クチン等があげられる。本発明に用いるアベルメクチン
の発酵培養液は、アベルメクチン生産能を有する微生物
を栄養培地で培養した培養液である。アベルメクチン生
産能を有する微生物としては、アベルメクチンB体を主
として生産する微生物が好ましく、例えばストレプトミ
セス・アベルミチルス(Streptomyces avermitilis )
K2038 (FERM BP-2775; 特開平3−254678)等が
あげられる。栄養培地は、アベルメクチン生産能を有す
る微生物を培養するのに通常用いられる培地であればい
ずれでもよく、例えば、特公平2−17558に記載さ
れている培地でもよい。培養は、振盪培養、通気攪拌培
養等の好気的条件下で行う。培養温度は、20〜40℃
で、pHは、6.0〜8.0、好ましくは7.0〜7.
5に調整して行う。発酵培養液中のアベルメクチン濃度
としては、通常0.4g/l以上が好ましく、0.5g
/l以上が特に好ましい。発酵培養液中のアベルメクチ
ンB1a濃度は、0.2g/l以上であることが好まし
く、総アベルメクチン中のアベルメクチンB1a量は30
%以上であることが好ましい。なかでも、発酵培養液中
のアベルメクチンB1a濃度は、0.3g/l以上である
ことが特に好ましく、総アベルメクチン中のアベルメク
チンB1a量は35%以上であることが特に好ましい。BEST MODE FOR CARRYING OUT THE INVENTION As avermectin-containing substances,
Examples include insolubles in a fermentation broth of avermectin, and synthetic avermectin. The fermentation culture solution of avermectin used in the present invention is a culture solution obtained by culturing a microorganism capable of producing avermectin in a nutrient medium. As the microorganism having an avermectin-producing ability, a microorganism that mainly produces avermectin B is preferable. For example, Streptomyces avermitilis ( Streptomyces avermitilis )
K2038 (FERM BP-2775; JP-A-3-254678). The nutrient medium may be any medium that is commonly used for culturing microorganisms having avermectin-producing ability, and may be, for example, the medium described in Japanese Patent Publication No. 17558/1990. The cultivation is performed under aerobic conditions such as shaking culture and aeration / agitation culture. Culture temperature is 20 to 40 ° C
And the pH is 6.0 to 8.0, preferably 7.0 to 7.0.
Adjust it to 5. The avermectin concentration in the fermentation broth is usually preferably 0.4 g / l or more, more preferably 0.5 g / l.
/ L or more is particularly preferred. The avermectin B1a concentration in the fermentation broth is preferably 0.2 g / l or more, and the amount of avermectin B1a in the total avermectin is 30%.
% Is preferable. Above all, the avermectin B1a concentration in the fermentation broth is particularly preferably 0.3 g / l or more, and the amount of avermectin B1a in the total avermectin is particularly preferably 35% or more.
【0008】アベルメクチンの発酵培養液中の不溶物と
しては、上記製造法で得られるアベルメクチンの発酵培
養液を遠心分離して得られる沈殿物、アベルメクチンの
発酵培養液を濾過して得られる残渣等があげられる。水
と混ざり合う溶媒としては、水より沸点の低いメタノー
ル、アセトン、エタノール等があげられる。アベルメク
チンの発酵培養液中の不溶物を水と混ざり合う溶媒と接
触させてアベルメクチンを抽出する際には、水と混ざり
合う溶媒の濃度を75%以上とし、20〜40℃で15
分〜2時間かけて抽出を行うのが好ましい。抽出液を濃
縮する際には、水と混ざり合う溶媒の濃度が30%以下
となるまで濃縮するのが好ましく、再度水と混ざり合う
溶媒を添加する際には、水と混ざり合う溶媒の濃度が5
0〜70%となるまで添加するのが好ましい。The insoluble matter in the avermectin fermentation broth includes a precipitate obtained by centrifuging the avermectin fermentation broth obtained by the above-mentioned production method, a residue obtained by filtering the avermectin fermentation broth, and the like. can give. Examples of the solvent that can be mixed with water include methanol, acetone, and ethanol having a boiling point lower than that of water. When avermectin is extracted by contacting the insoluble matter in the fermentation broth of avermectin with a solvent that is miscible with water, the concentration of the solvent that is miscible with water is set to 75% or more, and at 20 to 40 ° C.
It is preferred to perform the extraction over a period of minutes to 2 hours. When the extract is concentrated, it is preferable that the concentration of the solvent miscible with water is reduced to 30% or less. When the solvent miscible with water is added again, the concentration of the solvent miscible with water is reduced. 5
It is preferable to add until it becomes 0 to 70%.
【0009】塩としては、塩化ナトリウム、塩化カリウ
ム、リン酸ナトリウム、リン酸カリウム、炭酸水素ナト
リウム等があげられ、なかでも、塩化ナトリウムが好ま
しい。塩濃度は、水と混ざり合う溶媒および塩を添加し
た後に10%以上であるのが好ましい。取得した不溶物
を水と混ざり合う溶媒と接触させる際には、アベルメク
チンB1a濃度が1〜10g/lとなるようにするのが好
ましく、なかでも、4〜10g/lとなるようにするの
が特に好ましい。また、残留不溶物を除いた溶液を濃縮
する際には、アベルメクチンB1a濃度が50〜150g
/lとなるように濃縮するのが好ましい。なお、残留不
溶物の除去は、遠心分離、濾過等により行うことができ
る。Examples of the salt include sodium chloride, potassium chloride, sodium phosphate, potassium phosphate, sodium hydrogencarbonate and the like. Of these, sodium chloride is preferred. The salt concentration is preferably at least 10% after the addition of the solvent and salt miscible with water. When the obtained insoluble matter is brought into contact with a solvent that is mixed with water, it is preferable that the avermectin B1a concentration be 1 to 10 g / l, and particularly preferably 4 to 10 g / l. Particularly preferred. When concentrating the solution from which residual insolubles had been removed, the avermectin B1a concentration was 50 to 150 g.
/ L is preferred. In addition, removal of the residual insoluble matter can be performed by centrifugation, filtration, or the like.
【0010】得られた不溶物あるいは沈澱物の単離は、
遠心分離、濾過等により行うことができる。以下に、実
施例によって本発明の態様を具体的に説明する。The isolation of the resulting insoluble matter or precipitate is
It can be performed by centrifugation, filtration or the like. Hereinafter, embodiments of the present invention will be specifically described with reference to examples.
【0011】[0011]
【実施例】胞子形成平板培地および生産培地としては、
下記の組成のものを用いた。胞子形成平板培地 麦芽エキス(Difco ) 10g 酵母エキス(Difco ) 4g 可溶性澱粉(Difco ) 4g 寒天 20g 蒸留水 1L 2N水酸化カリウム水溶液でpH7.2 とした後、121 ℃で15
分間オートクレーブにかけた。滅菌終了後、塩化マグネ
シウムおよび硝酸カリウムを、それぞれ10mM、8mM とな
るように加えた。生産培地 グルコース 45g ペプトン化牛乳 24g 酵母自己消化物 2.5ml ポリプロピレングリコール(平均分子量2000) 20g 蒸留水 1L 2N水酸化カリウム水溶液でpH7.2 とした後、121 ℃で15
分間オートクレーブにかけた。EXAMPLES As a sporulation plate medium and a production medium,
The following composition was used. Spore-forming plate medium Malt extract (Difco) 10 g Yeast extract (Difco) 4 g Soluble starch (Difco) 4 g Agar 20 g Distilled water 1 L Adjusted to pH 7.2 with 2 L aqueous 2N potassium hydroxide solution, and then added at 121 ° C to 15
Autoclaved for minutes. After the sterilization was completed, magnesium chloride and potassium nitrate were added so as to be 10 mM and 8 mM, respectively. Production medium Glucose 45 g Peptone milk 24 g Yeast autolysate 2.5 ml Polypropylene glycol (average molecular weight 2000) 20 g Distilled water 1 L Adjusted to pH 7.2 with 2N potassium hydroxide aqueous solution
Autoclaved for minutes.
【0012】また、それぞれの精製段階における総アベ
ルメクチン量およびアベルメクチンB1a量の分析は、純
品を標準品として、以下の条件の高速液体クロマトグラ
フィーで行った。 ガードカラム;Inertsil ODS-2〔GLサイエンス
(株)〕(5μm,4×10mm) 分離カラム;Inertsil ODS-2〔GLサイエンス(株)〕
(5μm,4×250mm) カラム温度;55℃ 移動相;アセトニトリル:メタノール:水=5:3:2 流速;0.6ml/分 検出;UV 243nm 試料注入量;0.2g/lで10μlThe analysis of the total amount of avermectin and the amount of avermectin B1a in each purification step was performed by high performance liquid chromatography under the following conditions using a pure product as a standard. Guard column; Inertsil ODS-2 [GL Science Co., Ltd.] (5 μm, 4 × 10 mm) Separation column; Inertsil ODS-2 [GL Science Co., Ltd.]
(5 μm, 4 × 250 mm) Column temperature; 55 ° C. Mobile phase; Acetonitrile: methanol: water = 5: 3: 2 Flow rate: 0.6 ml / min Detection; UV 243 nm Sample injection volume; 10 μl at 0.2 g / l
【0013】実施例1 胞子形成平板培地で28℃で7日間培養したストレプトミ
セス・アベルミチルス(Streptomyces avermitilis )
K2038 (FERM BP-2775)株の胞子を生産培地30mlを含む30
0ml フラスコ20本に移植し、28℃で210rpm、振幅2.5cm
の条件下で168時間培養した。上記で得られたアベルメ
クチンの発酵培養液500ml(B1a体0.6g、B2a体0.62g 含
有) を濾過し、菌体と共に不溶化しているアベルメクチ
ン混合物を水で洗浄した。得られた固形物(135ml) にメ
タノール470ml を加えて60分間混合した後、濾過を行
い、抽出液 (B1a体0.58g 、B2a体0.6g含有;B1a体の
総アベルメクチンに対する割合45%) を得た。この抽出
液を100ml になるまで濃縮した後、塩化ナトリウム15g
を添加した。このとき、メタノール濃度は15%であり、
上澄み液中のアベルメクチンB1a濃度およびアベルメク
チンB2a濃度はともに0.5g/l以下であった。次いで、メ
タノール150ml を加え、遠心分離により粗アベルメクチ
ンB1aと塩化ナトリウムの混合物 (アベルメクチンB1a
含量100mg/g ;B1a体の総アベルメクチンに対する割合
90%) を得た。得られた混合物にメタノール100ml を加
えて溶解した後、不溶物を濾過し、20mlになるまで濃縮
することにより、純度98%以上のアベルメクチンB1a,4
50mgを得た。Example 1 Streptomyces avermitilis cultured on a spore-forming plate medium at 28 ° C. for 7 days
30 spores of K2038 (FERM BP-2775) strain containing 30 ml of production medium
Transfer to 20 0 ml flasks, 210 rpm at 28 ° C, 2.5 cm amplitude
And cultured for 168 hours. 500 ml of the fermentation broth of avermectin obtained above (containing 0.6 g of B1a body and 0.62 g of B2a body) was filtered, and the avermectin mixture which had been insolubilized together with the cells was washed with water. To the obtained solid (135 ml), 470 ml of methanol was added and mixed for 60 minutes, followed by filtration to obtain an extract (containing 0.58 g of the B1a form and 0.6 g of the B2a form; the ratio of the B1a form to the total avermectin 45%). Was. After concentrating this extract to 100 ml, sodium chloride 15g
Was added. At this time, the methanol concentration is 15%,
The avermectin B1a concentration and the avermectin B2a concentration in the supernatant were both 0.5 g / l or less. Subsequently, 150 ml of methanol was added, and a mixture of crude avermectin B1a and sodium chloride (avermectin B1a) was centrifuged.
Content 100mg / g; ratio of B1a body to total avermectin
90%). After 100 ml of methanol was added to the obtained mixture to dissolve it, the insoluble matter was filtered and concentrated to 20 ml to obtain avermectin B1a, 4 having a purity of 98% or more.
50 mg were obtained.
【0014】実施例2 胞子形成平板培地で28℃で7日間培養したストレプトミ
セス・アベルミチルス(Streptomyces avermitilis )
K2038 (FERM BP-2775)株の胞子を生産培地300ml を含む
2Lフラスコ28本に移植し、28℃で210rpm、振幅2.5cm の
条件下で192 時間培養した。上記で得られたアベルメク
チンの発酵培養液15L(B1a体24g 、B2a体26g 含有) を
濾過し、菌体と共に不溶化しているアベルメクチン混合
物を水で洗浄した。得られた固形物(5L)にメタノール15
L を加えて2時間撹拌した後、濾過を行い、抽出液 (B
1a体21g 、B2a体23g 含有;B1a体の総アベルメクチン
に対する割合48%) を得た。この抽出液に塩化ナトリウ
ム400gを添加した後、1.5Lになるまで濃縮した。メタノ
ール2Lを加えて1時間撹拌後、遠心分離により粗アベル
メクチンB1aと塩化ナトリウムの混合物 (アベルメクチ
ンB1a含量120mg/g;B1a体の総アベルメクチンに対す
る割合91%) を得た。得られた混合物にメタノール3Lを
加えて1時間撹拌した後、不溶物を濾過し、600ml にな
るまで濃縮することにより、純度97%以上のアベルメク
チンB1a,18g (発酵培養液からの回収率75%)を得た。Example 2 Streptomyces avermitilis cultured at 28 ° C. for 7 days on a spore-forming plate medium
Spores of K2038 (FERM BP-2775) strain contained in 300 ml of production medium
The cells were transferred to 28 2L flasks and cultured at 28 ° C under the conditions of 210 rpm and an amplitude of 2.5 cm for 192 hours. 15 L of the fermentation broth of avermectin obtained above (containing 24 g of B1a body and 26 g of B2a body) was filtered, and the avermectin mixture which had been insolubilized together with the cells was washed with water. Methanol 15 is added to the obtained solid (5 L).
After adding L and stirring for 2 hours, the mixture was filtered and the extract (B
(1g body 21g, B2a body 23g; ratio of B1a body to total avermectin 48%). After adding 400 g of sodium chloride to this extract, it was concentrated to 1.5 L. After adding 2 L of methanol and stirring for 1 hour, a mixture of crude avermectin B1a and sodium chloride (avermectin B1a content 120 mg / g; ratio of B1a form to total avermectin 91%) was obtained by centrifugation. 3 L of methanol was added to the obtained mixture, and the mixture was stirred for 1 hour. The insoluble matter was filtered and concentrated to 600 ml to obtain 18 g of avermectin B1a having a purity of 97% or more (recovery rate from fermentation broth of 75%). ) Got.
【0015】[0015]
【発明の効果】本発明により、クロマトグラフィーを用
いない簡便・安価かつ精製効率が高いアベルメクチンB
1aの精製法が提供される。According to the present invention, avermectin B which is simple, inexpensive and has high purification efficiency without using chromatography
A method for purification of 1a is provided.
Claims (8)
媒と接触させてアベルメクチンを抽出した後、該抽出液
を濃縮し、次いで再度水と混ざり合う溶媒および塩を添
加し、不溶物を取得することを特徴とするアベルメクチ
ンB1aの精製法。(1) extracting avermectin by bringing the avermectin-containing substance into contact with a solvent miscible with water, concentrating the extract, and then adding a solvent and salt miscible with water again to obtain an insoluble substance; A method for purifying avermectin B1a, comprising:
媒と接触させてアベルメクチンを抽出した後、該抽出液
を濃縮し、次いで再度水と混ざり合う溶媒および塩を添
加して不溶物を取得し、さらに該不溶物を水と混ざり合
う溶媒と接触させた後、残留不溶物を除いた溶液を濃縮
し、沈殿物を取得することを特徴とするアベルメクチン
B1aの精製法。2. After extracting avermectin by bringing the avermectin-containing substance into contact with a solvent miscible with water, concentrating the extract, and then adding a solvent and salt miscible with water again to obtain an insoluble substance, A method for purifying avermectin B1a, further comprising contacting the insoluble matter with a solvent that is mixed with water, and then concentrating the solution from which the remaining insoluble matter has been removed to obtain a precipitate.
発酵培養液中の不溶物である請求項1または2記載のア
ベルメクチンB1aの精製法。3. The method for purifying avermectin B1a according to claim 1, wherein the avermectin-containing substance is an insoluble substance in a fermentation broth of avermectin.
の塩濃度を10%以上とする請求項1〜3記載のアベル
メクチンB1aの精製法。4. The method for purifying avermectin B1a according to claim 1, wherein the salt concentration after adding a solvent and a salt which are mixed with water is adjusted to 10% or more.
水と混ざり合う溶媒と接触させる際、水と混ざり合う溶
媒の濃度を75%以上とする請求項1〜4記載のアベル
メクチンB1aの精製法。5. The method for purifying avermectin B1a according to claim 1, wherein, when the insoluble matter in the fermentation broth of avermectin is brought into contact with a solvent miscible with water, the concentration of the solvent miscible with water is 75% or more. .
の濃度が30%以下となるまで濃縮する請求項1〜5記
載のアベルメクチンB1aの精製法。6. The method for purifying avermectin B1a according to claim 1, wherein the concentration of the solvent mixed with water is reduced to 30% or less when the extract is concentrated.
と混ざり合う溶媒の濃度が50〜70%となるまで添加
する請求項1〜6記載のアベルメクチンB1aの精製法。7. The method for purifying avermectin B1a according to claim 1, wherein when the solvent miscible with water is added again, the concentration of the solvent miscible with water is increased to 50 to 70%.
ンまたはエタノールである請求項1〜7記載のアベルメ
クチンB1aの精製法。8. The method for purifying avermectin B1a according to claim 1, wherein the solvent miscible with water is methanol, acetone or ethanol.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8152596A JPH101496A (en) | 1996-06-13 | 1996-06-13 | Avermectin purification method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8152596A JPH101496A (en) | 1996-06-13 | 1996-06-13 | Avermectin purification method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH101496A true JPH101496A (en) | 1998-01-06 |
Family
ID=15543891
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8152596A Withdrawn JPH101496A (en) | 1996-06-13 | 1996-06-13 | Avermectin purification method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH101496A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100419554B1 (en) * | 1999-10-29 | 2004-02-19 | 주식회사유한양행 | Process for the purification of Avermectin |
| EP2886640A1 (en) | 2013-12-18 | 2015-06-24 | Riga Technical University | Process for isolation of milbemycins A3 and A4 |
| CN106632552A (en) * | 2016-12-23 | 2017-05-10 | 宁夏泰益欣生物科技有限公司 | Extracting method for abamectin B1a |
-
1996
- 1996-06-13 JP JP8152596A patent/JPH101496A/en not_active Withdrawn
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100419554B1 (en) * | 1999-10-29 | 2004-02-19 | 주식회사유한양행 | Process for the purification of Avermectin |
| EP2886640A1 (en) | 2013-12-18 | 2015-06-24 | Riga Technical University | Process for isolation of milbemycins A3 and A4 |
| CN106632552A (en) * | 2016-12-23 | 2017-05-10 | 宁夏泰益欣生物科技有限公司 | Extracting method for abamectin B1a |
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