JP2004231749A - Sphingoglycolipid-containing composition and its preparation method - Google Patents

Sphingoglycolipid-containing composition and its preparation method Download PDF

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Publication number
JP2004231749A
JP2004231749A JP2003020444A JP2003020444A JP2004231749A JP 2004231749 A JP2004231749 A JP 2004231749A JP 2003020444 A JP2003020444 A JP 2003020444A JP 2003020444 A JP2003020444 A JP 2003020444A JP 2004231749 A JP2004231749 A JP 2004231749A
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Prior art keywords
water
glycosphingolipid
solvent
powder
containing composition
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JP2003020444A
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Japanese (ja)
Inventor
Kenji Miyanishi
健次 宮西
Katsuyuki Mukai
克之 向井
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Unitika Ltd
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Unitika Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To efficiently prepare a powdery sphingoglycolipid-containing composition free from defects such as stickiness or lump formation. <P>SOLUTION: The powdery sphingoglycolipid-containing composition is prepared by bringing a sphingoglycolipid-containing substance into contact with a cyclic oligosaccharide, such as β-cyclodextrin and/or γ-cyclodextrin, in the presence of a solvent having below-described properties (a) and (b) and water in a volume ratio of the solvent to water of (1/50)-3 and then drying the substance. The solvent used is other than water and has such properties that (a) the solvent and water are mutually soluble in each other and (b) the solvent is included by the cyclic oligosaccharide in the presence of water or in an anhydrous state. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明が属する技術分野】
本発明は、粉末状のスフィンゴ糖脂質含有組成物及びその製造方法に関するものである。
【0002】
【従来の技術】
スフィンゴ糖脂質なかでもモノグルコシルセラミドは、植物組織細胞膜等に広範囲に存在し、植物組織体より、有機溶媒抽出により、スフィンゴ糖脂質を含有する組成物を得ることは公知の技術である。近年、このようなモノグルコシルセラミドを含む抽出物、特に植物組織由来のものは、この化合物の特長である、ヒトを含む哺乳動物の皮膚角質層の水和改善効果ゆえに、肌の保湿効果のある食品素材、もしくは化粧品素材として利用されつつある。
【0003】
植物組織より抽出されるスフィンゴ糖脂質含有組成物は、その肌保湿効果を損なわない、公知の方法により、食品乃至化粧品に添加されている。中でも、焼き菓子やタブレットといった固形食品や、ファンデーションなどの固形化粧品に添加される場合、抽出により得られたスフィンゴ糖脂質組成物を、何らかの方法で粉末化したものを添加する方法が、最も好適に用いられる手段であるといえる。
【0004】
しかし、植物組織体よりスフィンゴ糖脂質を抽出するには、有機溶媒を用いる必要があり(例えば、特許文献1参照)、このとき同時に他の脂質成分も抽出されるため、植物組織体より得られるスフィンゴ糖脂質含有組成物は、通常、オイル状の高粘性液体もしくは蝋状の半固形物であり、極めて粉末化しがたい問題があった。さらに具体的には、当該スフィンゴ糖脂質類含有組成物を固形食品や固形化粧品に応用する場合、賦形剤を用いた粉末化という頻用の手法に関しては、先行特許では、実施例で紹介されている程度にしか見あたらないが(例えば、特許文献2参照)、スフィンゴ糖脂質含有組成物に対し、9〜10倍質量という大量の賦形剤を加えた例が示されているのみで、スフィンゴ糖脂質含有組成物に対し、これより少ない量の賦形剤を用いての粉末化の先行例は見あたらない。
【0005】
【特許文献1】
特開2002−38183号公報
【特許文献2】
特開平11−113530号公報
【0006】
【発明が解決しようとする課題】
本発明は、保湿効果を有する有用なスフィンゴ糖脂質含有物を、べとつきやダマ形成ない粉末として得ることを目的とするものである。
【0007】
【課題を解決するための手段】
本発明者らは、上記課題を解決するため、スフィンゴ糖脂質含有物を粉末化する際に添加する賦形剤について検討を加えた結果、特定の物質を賦形剤とし特定の条件下で粉末化を行えば、なるべく少ない量の添加で、効率よく、べとつきやダマ形成などの問題のない粉末を得ることができることを見出し、本発明を完成させるに至った。
【0008】
すなわち、本発明の第一は、環状オリゴ糖を賦形剤として含み、粉末状であることを特徴とするスフィンゴ糖脂質含有組成物を要旨とするものであり、好ましくは、環状オリゴ糖が、β−シクロデキストリン又は/及びγ−シクロデキストリンである。本発明の第二は、以下の(a)及び(b)の性質を有する水以外の溶媒が、容量比で水に対し、1/50以上、3倍以下の割合で共存する状態において、スフィンゴ糖脂質含有物と環状オリゴ糖を接触させたのち、乾燥することを特徴とする請求項1〜3に記載されたいずれかのスフィンゴ糖脂質含有組成物の製造方法。
(a)水と相互溶解すること
(b)水との共存下又は無水状態において、使用する環状オリゴ糖に包接されること
【0009】
【発明の実施の形態】
以下、本発明を詳細に説明する。
本発明におけるスフィンゴ糖脂質は、微生物を含む動植物組織体に含まれるものであり、溶媒抽出による公知の方法によって得られるものである(例えば、特開2002−38183号参照)。抽出原料としては、病原菌やウイルスの問題を考慮すると、植物組織体が好ましい。さらに含有量などを考慮するとこんにゃく芋が好ましく、具体的にはこんにゃく芋、こんにゃく精粉、こんにゃく荒粉、こんにゃくトビ粉などが挙げられる。
本発明においては、スフィンゴ糖脂質の成分中、モノグルコシルセラミドが0.1〜90質量%含有されているものが好ましく、さらに、1.0〜30質量%含まれているものが好ましく用いられる。
【0010】
本発明において、スフィンゴ糖脂質含有物の粉末化に用いる賦形剤は、環状オリゴ糖であることが必要であり、その誘導体も用いることが可能である。具体的には、α−、β−、γ−の各シクロデキストリンおよびそのメチル誘導体、ヒドロキシプロピル誘導体やスルホブチルエーテル誘導体などの、修飾シクロデキストリン類、デキストリン類の重合度が8を越えるような高重合度シクロデキストリン類などが挙げられる。この中では、世界的に生産量が多く、価格も安いβ−シクロデキストリン若しくはγ−シクロデキストリン又はこれらの混合物が好適に用いられる。
【0011】
本発明の粉末状のスフィンゴ糖脂質含有組成物中の賦形剤は、10〜90質量%含有していることが好ましく、30〜80質量%がさらに好ましい。
【0012】
本発明の粉末状のスフィンゴ糖脂質含有組成物は、べとつきやダマ形成性のない粉末であり、粒度は、用いる粉末化装置により異なってくるが、概ね5mm以下のものが出来る。また、得られた粉末は、任意の粉砕機により、さらに細かくすることが可能である。そのような粉砕機としては、石臼、ボールミル、カッターミルなどが挙げられる。
【0013】
本発明の製造方法は、水と水以外の溶媒の共存下に、スフィンゴ糖脂質含有物と上記の環状オリゴ糖を接触させ、その後乾燥して粉末化することにより粉末状のスフィンゴ糖脂質含有組成物を得る方法である。
本発明の製造方法に用いられる水以外の溶媒は、(a)水と相互溶解すること、及び(b)水との共存下又は無水状態において、使用する環状オリゴ糖に包接されること、の性質を満たすものである。さらに、より色調の均一な粉末をより速く、収率よく得るためには、なるべく、スフィンゴ糖脂質混合物をよりよく溶解あるいは均一に分散させられるもの、沸点が低く、容易に留去が可能なもの、環状オリゴ糖とあまりにも強く相互作用をしないもの(すなわち、包接に伴うギブスエネルギーの減少が小さいもの)が好ましい。そのような溶媒としては、たとえば、環状オリゴ糖がβ−シクロデキストリンあるいは、γ−シクロデキストリン、もしくはこれらの混合物のいずれかの場合、エタノール、n−ブタノール、イソプロパノールなどが挙げられ、特に、最終的に得られる粉末を経口用途に用いる場合は、この中では、エタノールが最も好ましく用いられる。
【0014】
水と上記した水以外の溶媒との割合は、溶媒が水に対し容量比で1/50以上、3倍以下であることが必要であり、1/20以上、2倍以下であることが好ましい。上記した水以外の溶媒が、容量比で水の3倍を超えると、できあがる粉末がべとつき、固着してしまうおそれがあり、逆に溶媒が水に対し1/50未満であると、粉末化の進行が遅くなるおそれがあり、どちらも採用できない。
【0015】
水及び水以外の溶媒を併せた総量は、賦形剤として用いる環状オリゴ糖が、充分分散するに足りる量であることが望ましいが、不必要に溶媒量を増やすと、粉末化完了までの必要時間がいたずらに延びてしまう。好適な水および溶媒の総量は、環状オリゴ糖1重量部(g)に対し、1倍量(mL)以上、50倍量(mL)以下、さらに好適には1倍量(mL)以上、20倍量(mL)以下である。
【0016】
賦形剤の添加量は、スフィンゴ糖脂質含有物1重量部に対して、好ましくは1/10重量部以上、10重量部以下、より好ましくは1/2重量部以上、5重量部以下となるようにする。
【0017】
スフィンゴ糖脂質含有物、環状オリゴ糖、溶媒及び水はあらかじめよく混合しておいてから乾燥することが望ましい。この際、この4種類の物質の混合順序は、スフィンゴ糖脂質含有物が、溶解乃至均一分散する範囲内で、任意でよく、この条件が満たされている限り、いずれの順序で混合していっても白濁乳液状乃至、元のスフィンゴ糖脂質含有物が着色している場合は、その着色がかかった乳液状ゾルとなる。全体が均一となったら撹拌をやめ、乳液状ゾルをそのまま静置する。
静置後数分以内に、乳液状ゾルは、急激な粘度上昇を起こし、均一なまま粘液状〜半固形状に固まり、賦形剤の沈降などは見られなくなる。この状態で乾燥を開始すれば、べとつきや表面付着性、ダマ形成性のない粉末状のスフィンゴ糖脂質含有組成物が得られる。
【0018】
乾燥することによる粉末化の方法は、特に限定されず、公知の方法を任意に使うことが出来る。そのような方法および装置としては、スプレードライ法、減圧下での混合撹拌、ドラムドライヤーや、横軸回転型乾燥機のような薄膜型乾燥装置を用いる方法、振動乾燥装置を用いる方法などが挙げられる。スフィンゴ糖脂質含有組成物中に含まれる成分の融点、分解温度などを考慮すると、この中では、スフィンゴ糖脂質含有組成物が高温にさらされる恐れの少ない、粉末化容器内部が減圧状態となるような装置である、減圧下での混合撹拌装置、薄膜型乾燥装置、振動乾燥機などを用いる方法がより好ましい。
【0019】
具体的な条件としては、内部を減圧に出来るジャケット付混合撹拌装置を用いる場合、均一ゾルを仕込んで、乾燥装置内温が、好ましくは常温以上100℃以下、より好ましくは30℃以上80℃以下となるような条件で、減圧下、撹拌を行いながら、乾燥、粉砕を行うようにすればよい。また、ドラムドライヤーのような薄膜型乾燥装置を用いる場合、ドラムドライヤーのドラム表面のように、被粉末化物が薄膜を形成する表面の温度を、好ましくは70〜120℃、さらに好ましくは、80〜110℃とし、減圧下、被粉末化物を投入すればよい。
【0020】
また、本発明の製造方法においては、他の賦形剤、表面潤滑剤などの、他の粉末化助剤を別途加えながら、粉末化することも出来る。そのような粉末化助剤として、デキストリン、コーンスターチ、セルロースなどの多糖類、炭酸カルシウム、炭酸マグネシウム、シリカ、アルミナなどの無機微粒子などが挙げられる。
【0021】
上記により得られた粉末は、さらに細かくするため、粉砕機等で粉砕することも出来る。そのような粉砕装置・粉砕方法として、石臼、凍結粉砕器、カッターミル、ボールミルなどの公知の装置・方法が可能である。
【0022】
最終的に得られる粉末状のスフィンゴ糖脂質含有組成物は、べとつき、付着性のないさらさらの粉であり、乾燥雰囲気下でなくとも、長期間の保存によるダマの形成などは見られないものである。
【0023】
本発明のスフィンゴ糖脂質含有組成物の粉末は、食品をはじめ、医薬品その他の製剤物、あるいは、化粧品などに配合可能である。配合するにあたって望ましい形態は、クッキー、ビスケットなどの焼き菓子類やパン、うどん、パスタなどの麺類、チュアブル、タブレット、錠剤、カプセル製剤などが考えられる。
【0024】
【実施例】
以下、本発明を実施例により具体的に説明するが、本発明はこれに限定されるものではない。
なお、製造装置(粉末化装置)として以下のものを用いた。
(1)減圧混合撹拌器タイプ:株式会社カワタ製 スーパーミキサー SMV−20A型
(2)ドラムドライヤータイプ:中央化工機株式会社製 DD−1型
【0025】
また、スフィンゴ糖脂質の定量方法は以下の通りである。
スフィンゴ糖脂質の定量には高速液体クロマトグラフィー(HPLC)を用いた。Waters社製 LC Module1を用い、カラムはGLサイエンス社製Inertsil SIL100Aを用いた。溶媒はクロロホルム:メタノール=9:1(容量比)を用い、流速1.0mL/分で25℃で測定した。検出には光散乱検出器(ALLTECH社製 500ELSD)を用いた。
【0026】
実施例1
こんにゃくトビ粉1kgを、エタノール2Lを用いて、2時間抽出し、溶媒留去後の抽出物10.3g(スフィンゴ糖脂質含有率6.43重量%)を得た。この抽出物を、40mLのエタノールに溶かし濃褐色の溶液Aとした。これとは別に、βーシクロデキストリン20gを水20mLと混ぜ合わせ、ペーストBを得た。溶液Aの中にペーストBをよくかき混ぜながら導入し、均一になるまでよくかき混ぜ、肌色のゾルCを得た。この肌色のゾルCは、5分間の静置により、生クリーム状に固まるのを確認した後、70℃で、8時間真空乾燥した後、粉砕器(家庭用ミル)で粉砕し、黄色の均一な色調を有する粉末30.1gを得た。得られた粉末は、べとつきがなく、少量を、ポリエチレン手袋をした手でこねたが、ダマにはならなかった。
【0027】
実施例2
こんにゃくトビ粉1kgを、エタノール2Lを用いて、2時間抽出し、溶媒留去後の抽出物10.3g(スフィンゴ糖脂質含有率6.43重量%)を得た。この抽出物を、エタノール30mLに溶解させ、水80mL中で水洗を2時間行った後、食塩15gを加え、加熱沸騰させ、水相上部に浮上してきた油相を回収した。回収油相をエタノール30mLに溶かし、不溶分除去の後、エタノール可溶分6.6gを回収した(スフィンゴ糖脂質含有率9.32重量%)。これを40mLのエタノールに溶かし濃褐色の溶液Aとした。これとは別に、βーシクロデキストリン20gを水20mLと混ぜ合わせ、ペーストBを得た。溶液Aの中にペーストBをよくかき混ぜながら導入し、均一になるまでよくかき混ぜ、肌色のゾルCを得た。この肌色のゾルCは、5分間の静置により、生クリーム状に固まるのを確認した後、70℃で、8時間真空乾燥した後、粉砕器(家庭用ミル)で粉砕し、黄色の均一な色調を有する粉末30.1gを得た。得られた粉末は、べとつきがなく、少量を、ポリエチレン手袋をした手でこねたが、ダマにはならなかった。
【0028】
実施例3
こんにゃくトビ粉1kgを、エタノール2Lを用いて、2時間抽出し、溶媒留去後の抽出物10.3g(スフィンゴ糖脂質含有率6.43重量%)を得た。この抽出物を、エタノール30mLに溶解させ、水80mL中で水洗を2時間行った後、食塩15gを加え、加熱沸騰させ、水相上部に浮上してきた油相を回収した。回収油相をエタノール30mLに溶かし、不溶分除去の後、エタノール可溶分6.6gを回収した(スフィンゴ糖脂質含有率9.32重量%)。これを40mLのエタノールに溶かし濃褐色の溶液Aとした。これとは別に、γーシクロデキストリン20gを水20mLと混ぜ合わせ、ペーストBを得た。溶液Aの中にペーストBをよくかき混ぜながら導入し、均一になるまでよくかき混ぜ、肌色のゾルCを得た。この肌色のゾルCは、5分間の静置により、生クリーム状に固まるのを確認した後、70℃で、8時間真空乾燥した後、粉砕器(家庭用ミル)で粉砕し、黄色の均一な色調を有する粉末30.3gを得た。得られた粉末は、べとつきがなく、少量を、ポリエチレン手袋をした手でこねたが、ダマにはならなかった。
【0029】
実施例4
こんにゃくトビ粉50kgを、エタノール100Lを用いて、2時間抽出し、溶媒留去後の抽出物496g(スフィンゴ糖脂質含有率6.63重量%)を得た。この抽出物を、2Lのエタノールに溶かし濃褐色の溶液Aとした。これとは別に、βーシクロデキストリン1kgを水1Lと混ぜ合わせ、ペーストBを得た。株式会社カワタ製スーパーミキサーSMV−20A型の本体に、溶液Aを投入し、さらにペーストBを、かき混ぜながら導入した後、均一になるまでよくかき混ぜ、肌色のゾルCを得た。この肌色のゾルCは、5分間の静置により、生クリーム状に固まるのを確認した後、ジャケット循環水温度70℃で、8時間減圧下で撹拌を行い、最終的に、黄肌色の均一な色調を有する、粉末1449gを払い出した。得られた粉末は、べとつきがなく、少量を、ポリエチレン手袋をした手でこねたが、ダマにはならなかった。
【0030】
実施例5
こんにゃくトビ粉50kgを、エタノール100Lを用いて、2時間抽出し、溶媒留去後の抽出物496g(スフィンゴ糖脂質含有率6.63重量%)を得た。この抽出物を、2Lのエタノールに溶かし濃褐色の溶液Aとした。これとは別に、βーシクロデキストリン1kgを水1Lと混ぜ合わせ、ペーストBを得た。空のタンクに、溶液Aを投入し、さらにペーストBを、かき混ぜながら導入した後、均一になるまでよくかき混ぜ、肌色のゾルCを得た。この肌色のゾルCは、5分間の静置により、生クリーム状に固まるのを確認した後、中央化工機株式会社製ドラムドライヤーDD−1型で粉末化を行った。内部を減圧にし、ドラム表面温度を95℃に、ドラムを1回転/分に設定し、生クリーム状に固まったゾルCを上部ホッパーから順次投入し、順次粉末化を行っていったところ、最終的に、黄肌色の均一な色調を有する、粉末1481gを払い出した。得られた粉末は、べとつきがなく、少量を、ポリエチレン手袋をした手でこねたが、ダマにはならなかった。
【0031】
実施例6
脱脂米糠1kgを、エタノール2Lを用いて、2時間抽出し、溶媒留去後の抽出物14.2g(スフィンゴ糖脂質含有率1.41重量%)を得た。この抽出物を、60mLのエタノールに溶かし黄褐色の溶液Aとした。これとは別に、βーシクロデキストリン40gを水40mLと混ぜ合わせ、ペーストBを得た。溶液Aの中にペーストBをよくかき混ぜながら導入し、均一になるまでよくかき混ぜ、薄黄色のゾルCを得た。このゾルCは、5分間の静置により、生クリーム状に固まるのを確認した後、70℃で、8時間真空乾燥した後、粉砕器(家庭用ミル)で粉砕し、薄黄色の均一な色調を有する粉末51.8gを得た。得られた粉末は、べとつきがなく、少量を、ポリエチレン手袋をした手でこねたが、ダマにはならなかった。
【0032】
比較例1
こんにゃくトビ粉1kgを、エタノール2Lを用いて、2時間抽出し、溶媒留去後の抽出物10.3g(スフィンゴ糖脂質含有率6.43重量%)を得た。この抽出物を、100mLのエタノールに溶かし褐色の溶液Aとした。これとは別に、βーシクロデキストリン20gを水20mLと混ぜ合わせ、ペーストBを得た。溶液Aの中にペーストBをよくかき混ぜながら導入し、均一になるまでよくかき混ぜ、肌色のゾルCを得た。この肌色のゾルCは、撹拌をやめるとすぐに、シクロデキストリンの沈殿を生じ透明な上清と分離し、全体の粘度が上昇することもなかった。ゾルCをそのまま70℃で、8時間真空乾燥した後、粉砕器(家庭用ミル)で粉砕し、黄土色の、やや濃淡のまだらのある色調を有する物質26.6gを得たが、粉砕器側面に、べっとりとこびりついた粘着性の高い未粉砕物も見受けられた。得られたものは、べとつきが強く、少量を、ポリエチレン手袋をした手でこねたが、ダマになり、元の粉末状態に戻すことは出来なかった。
【0033】
比較例2
こんにゃくトビ粉1kgを、エタノール2Lを用いて、2時間抽出し、溶媒留去後の抽出物10.3g(スフィンゴ糖脂質含有率6.43重量%)を得た。この抽出物を、40mLのエタノールに溶かし褐色の溶液Aとした。これとは別に、コーンスターチ20gを水20mLと混ぜ合わせ、ペーストBを得た。溶液Aの中にペーストBをよくかき混ぜながら導入し、均一になるまでよくかき混ぜ、肌色のゾルCを得た。この肌色のゾルCは、撹拌をやめるとすぐに、コーンスターチの沈殿を生じ透明な上清と分離し、全体の粘度が上昇することもなかった。ゾルCをそのまま70℃で、8時間真空乾燥した後、粉砕器(家庭用ミル)で粉砕し、黄土色の、やや濃淡のまだらのある色調を有する物質27.2gを得たが、粉砕器側面に、べっとりとこびりついた粘着性の高い未粉砕物も見受けられた。得られたものは、べとつきが強く、少量を、ポリエチレン手袋をした手でこねたが、ダマになり、元の粉末状態に戻すことは出来なかった。
【0034】
比較例3
こんにゃくトビ粉1kgを、エタノール2Lを用いて、2時間抽出し、溶媒留去後の抽出物10.3g(スフィンゴ糖脂質含有率6.43重量%)を得た。この抽出物を、40mLのテトラヒドロフランに溶かし褐色の溶液Aとした。これとは別に、βーシクロデキストリン20gを水20mLと混ぜ合わせ、ペーストBを得た。溶液Aの中にペーストBをよくかき混ぜながら導入したが、充分混合しても、均一なゾルとはならず、シクロデキストリンの不規則な大きさのダマが沈降し、上部に溶液が浮いた状態の不安定なゾルCを得た。この、ゾルCをそのまま70℃で、8時間真空乾燥した後、粉砕器(家庭用ミル)で粉砕したが、黄土色の、べとつきの強いダマが形成されるだけで、粉末まで砕くことは出来なかった。
【0035】
【発明の効果】
本発明によれば、スフィンゴ糖脂質類含有組成物の粉末化において、べとつきが強い、表面の付着性の高さゆえ、ダマになりやすいといった、従来の問題点が全くない、さらさらの粉末を得ることが出来る。
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a powdery glycosphingolipid-containing composition and a method for producing the same.
[0002]
[Prior art]
Among glycosphingolipids, monoglucosylceramide is widely present in plant tissue cell membranes and the like, and it is a known technique to obtain a composition containing glycosphingolipids from a plant tissue by extraction with an organic solvent. In recent years, such extracts containing monoglucosylceramide, especially those derived from plant tissues, have a moisturizing effect on the skin due to the effect of improving the hydration of the skin stratum corneum of mammals including humans, which is a feature of this compound. It is being used as a food material or cosmetic material.
[0003]
Glycosphingolipid-containing compositions extracted from plant tissues are added to foods or cosmetics by a known method that does not impair the skin moisturizing effect. Among them, when added to solid foods such as baked goods and tablets, and solid cosmetics such as foundations, a method of adding a powdered glycosphingolipid composition obtained by extraction in some way is most preferably used. It can be said that it is the means used.
[0004]
However, in order to extract glycosphingolipids from plant tissues, it is necessary to use an organic solvent (for example, see Patent Document 1). At this time, other lipid components are also extracted at the same time. Glycosphingolipid-containing compositions are usually high viscous liquids in the form of oil or semisolids in the form of wax, and have a problem that they are extremely difficult to be powdered. More specifically, when the glycosphingolipid-containing composition is applied to solid foods and solid cosmetics, the frequently used technique of pulverization using excipients is described in Examples in the preceding patents. Although it is found only to a certain extent (see, for example, Patent Document 2), only an example in which a large amount of an excipient of 9 to 10 times the mass is added to a glycosphingolipid-containing composition is shown, There is no prior example of powdering lipid-containing compositions with lower amounts of excipients.
[0005]
[Patent Document 1]
JP 2002-38183 A [Patent Document 2]
JP-A-11-113530
[Problems to be solved by the invention]
An object of the present invention is to obtain a useful glycosphingolipid-containing substance having a moisturizing effect as a powder free of stickiness and lump formation.
[0007]
[Means for Solving the Problems]
The present inventors have studied the excipients to be added when pulverizing the glycosphingolipid-containing substance in order to solve the above-mentioned problems. It has been found that powdering can efficiently produce powder having no problems such as stickiness and lump formation with the addition of as small an amount as possible, thereby completing the present invention.
[0008]
That is, the first of the present invention is to include a glycosphingolipid-containing composition characterized by being in powder form, comprising a cyclic oligosaccharide as an excipient, and preferably, the cyclic oligosaccharide is β-cyclodextrin and / or γ-cyclodextrin. The second aspect of the present invention is that sphingo is used in a state where a solvent other than water having the following properties (a) and (b) coexists at a volume ratio of 1/50 to 3 times with respect to water. The method for producing a glycosphingolipid-containing composition according to any one of claims 1 to 3, wherein the glycolipid-containing composition is brought into contact with a cyclic oligosaccharide and then dried.
(A) Mutual dissolution with water (b) Inclusion with the cyclic oligosaccharide to be used in the presence of water or in an anhydrous state
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, the present invention will be described in detail.
The glycosphingolipid in the present invention is contained in animal and plant tissues including microorganisms, and is obtained by a known method by solvent extraction (for example, see JP-A-2002-38183). As an extraction raw material, a plant tissue is preferable in consideration of the problem of pathogenic bacteria and viruses. Further, konjac potato is preferable in consideration of the content and the like, and specific examples include konjac potato, konjac fine powder, konjac coarse powder, konjac tobi powder and the like.
In the present invention, among the components of glycosphingolipids, those containing monoglucosylceramide in an amount of 0.1 to 90% by mass are preferable, and those containing 1.0 to 30% by mass are more preferably used.
[0010]
In the present invention, the excipient used for powdering the glycosphingolipid-containing substance needs to be a cyclic oligosaccharide, and a derivative thereof can also be used. Specifically, α-, β-, and γ-cyclodextrins and their methyl derivatives, hydroxypropyl derivatives, sulfobutyl ether derivatives, and other modified cyclodextrins and dextrins, which have a high degree of polymerization of more than 8 And cyclodextrins. Among them, β-cyclodextrin or γ-cyclodextrin, which are produced in large quantities worldwide and are inexpensive, or mixtures thereof are preferably used.
[0011]
The excipient in the powdery glycosphingolipid-containing composition of the present invention preferably contains 10 to 90% by mass, more preferably 30 to 80% by mass.
[0012]
The powdery glycosphingolipid-containing composition of the present invention is a powder having no stickiness or lump formation, and the particle size varies depending on the powdering apparatus used, but is generally about 5 mm or less. Further, the obtained powder can be further finely divided by an arbitrary pulverizer. Examples of such a crusher include a stone mill, a ball mill, a cutter mill and the like.
[0013]
The production method of the present invention is to provide a powdery glycosphingolipid-containing composition by bringing a glycosphingolipid-containing substance into contact with the above-mentioned cyclic oligosaccharide in the presence of water and a solvent other than water, followed by drying and powdering. It is a way to get things.
Solvents other than water used in the production method of the present invention are: (a) mutually soluble with water; and (b) inclusion in the cyclic oligosaccharide to be used in the coexistence with water or in an anhydrous state; It satisfies the property of Furthermore, in order to obtain a powder having a more uniform color tone faster and with a higher yield, it is preferable that the glycosphingolipid mixture be dissolved or dispersed uniformly, and that the boiling point is low and that it can be easily distilled off. Those that do not interact too strongly with the cyclic oligosaccharide (that is, those that have a small decrease in Gibbs energy upon inclusion) are preferred. Examples of such a solvent include, when the cyclic oligosaccharide is β-cyclodextrin or γ-cyclodextrin, or any mixture thereof, ethanol, n-butanol, isopropanol, and the like. When the powder obtained in (1) is used for oral use, among them, ethanol is most preferably used.
[0014]
The ratio of water to the solvent other than the above-mentioned water needs to be 1/50 or more and 3 times or less, and preferably 1/20 or more and 2 times or less, with respect to water. . If the solvent other than water is more than three times the volume of water, the resulting powder may be sticky and stick, and if the solvent is less than 1/50 with respect to water, There is a risk that progress will be slow, and neither can be adopted.
[0015]
It is desirable that the total amount of water and the solvent other than water be sufficient to sufficiently disperse the cyclic oligosaccharide used as an excipient. Time is unnecessarily extended. A preferable total amount of water and a solvent is 1 part by weight (mL) or more and 50 times or less (mL) or less, more preferably 1 time or more (mL) or more, with respect to 1 part by weight (g) of the cyclic oligosaccharide. It is less than double volume (mL).
[0016]
The amount of the excipient to be added is preferably 1/10 to 10 parts by weight, more preferably 1/2 to 5 parts by weight, based on 1 part by weight of the glycosphingolipid-containing substance. To do.
[0017]
It is preferable that the glycosphingolipid-containing substance, the cyclic oligosaccharide, the solvent and the water are well mixed in advance and then dried. At this time, the mixing order of the four types of substances may be any within a range in which the glycosphingolipid-containing substance is dissolved or uniformly dispersed, and as long as this condition is satisfied, the mixing is performed in any order. Even when the milky milky liquid or the original glycosphingolipid-containing substance is colored, a colored milky sol is obtained. When the whole becomes uniform, stop stirring and leave the emulsion sol as it is.
Within a few minutes after standing, the emulsion sol undergoes a sharp increase in viscosity, solidifies in a viscous to semi-solid state while keeping uniformity, and no sedimentation of excipients is observed. If drying is started in this state, a powdery glycosphingolipid-containing composition having no stickiness, surface adhesion or lump formation can be obtained.
[0018]
The method of powdering by drying is not particularly limited, and any known method can be used. Examples of such a method and apparatus include a spray drying method, mixing and stirring under reduced pressure, a drum dryer, a method using a thin film type drying apparatus such as a horizontal axis rotating type dryer, a method using a vibration drying apparatus, and the like. Can be Considering the melting point, decomposition temperature, and the like of the components contained in the glycosphingolipid-containing composition, among these, the glycosphingolipid-containing composition is less likely to be exposed to high temperatures, and the inside of the powdered container is in a reduced pressure state. More preferably, a method using a mixing and stirring device under reduced pressure, a thin film type drying device, a vibration drying device, or the like, which is a simple device, is more preferable.
[0019]
As a specific condition, when using a mixing and stirring device with a jacket capable of reducing the pressure inside, a uniform sol is charged, and the internal temperature of the drying device is preferably room temperature to 100 ° C, more preferably 30 ° C to 80 ° C. Drying and pulverization may be performed while stirring under reduced pressure under the following conditions. When a thin film type drying device such as a drum dryer is used, the temperature of the surface on which the material to be powdered forms a thin film, such as the drum surface of the drum dryer, is preferably 70 to 120 ° C., and more preferably 80 to 120 ° C. The temperature may be 110 ° C., and the substance to be powdered may be charged under reduced pressure.
[0020]
In addition, in the production method of the present invention, powdering can be performed while separately adding other powdering aids such as other excipients and surface lubricants. Examples of such powdering aids include polysaccharides such as dextrin, corn starch, and cellulose, and inorganic fine particles such as calcium carbonate, magnesium carbonate, silica, and alumina.
[0021]
The powder obtained as described above can be pulverized with a pulverizer or the like to further reduce the size. As such a crushing device and crushing method, known devices and methods such as a stone mill, a freeze crusher, a cutter mill, and a ball mill can be used.
[0022]
The powdery glycosphingolipid-containing composition finally obtained is a sticky, non-sticky, free-flowing powder, and even under a dry atmosphere, there is no formation of lumps due to long-term storage. is there.
[0023]
The powder of the glycosphingolipid-containing composition of the present invention can be blended in foods, pharmaceuticals and other preparations, cosmetics, and the like. Desirable forms for blending include baked goods such as cookies and biscuits, noodles such as bread, udon and pasta, chewable tablets, tablets and capsule preparations.
[0024]
【Example】
Hereinafter, the present invention will be described specifically with reference to Examples, but the present invention is not limited thereto.
In addition, the following was used as a manufacturing apparatus (powdering apparatus).
(1) Vacuum mixing stirrer type: Super mixer SMV-20A type manufactured by Kawata Corporation (2) Drum dryer type: DD-1 type manufactured by Chuo Kakoki Co., Ltd.
The method for quantifying glycosphingolipids is as follows.
Glycosphingolipids were quantified by high performance liquid chromatography (HPLC). LC Module 1 manufactured by Waters was used, and Inertsil SIL100A manufactured by GL Sciences was used as a column. As a solvent, chloroform: methanol = 9: 1 (volume ratio) was used and measured at 25 ° C. at a flow rate of 1.0 mL / min. A light scattering detector (500 ELSD manufactured by ALLTECH) was used for detection.
[0026]
Example 1
1 kg of konjac flour powder was extracted with 2 L of ethanol for 2 hours to obtain 10.3 g of the extract after distilling off the solvent (glycosphingolipid content: 6.43% by weight). This extract was dissolved in 40 mL of ethanol to obtain a dark brown solution A. Separately, 20 g of β-cyclodextrin was mixed with 20 mL of water to obtain Paste B. The paste B was introduced into the solution A while stirring well, and the mixture was stirred well until the mixture became uniform, thereby obtaining a skin-colored sol C. After confirming that this flesh-colored sol C solidifies in a fresh cream form by standing for 5 minutes, it is vacuum-dried at 70 ° C. for 8 hours, and then pulverized by a pulverizer (household mill) to obtain a yellow uniform color. 30.1 g of a powder having an excellent color tone was obtained. The resulting powder was tack-free and a small amount was kneaded with polyethylene gloved hands, but did not lump.
[0027]
Example 2
1 kg of konjac flour powder was extracted with 2 L of ethanol for 2 hours to obtain 10.3 g of the extract after distilling off the solvent (glycosphingolipid content: 6.43% by weight). This extract was dissolved in 30 mL of ethanol, washed with 80 mL of water for 2 hours, added with 15 g of sodium chloride, heated and boiled, and the oil phase floating on the upper portion of the aqueous phase was recovered. The recovered oil phase was dissolved in 30 mL of ethanol, and after removing insoluble components, 6.6 g of ethanol-soluble components were recovered (glycosphingolipid content: 9.32% by weight). This was dissolved in 40 mL of ethanol to obtain a dark brown solution A. Separately, 20 g of β-cyclodextrin was mixed with 20 mL of water to obtain Paste B. The paste B was introduced into the solution A while stirring well, and the mixture was stirred well until the mixture became uniform, thereby obtaining a skin-colored sol C. After confirming that this flesh-colored sol C solidifies in a fresh cream form by standing for 5 minutes, it is vacuum-dried at 70 ° C. for 8 hours, and then pulverized by a pulverizer (household mill) to obtain a yellow uniform color. 30.1 g of a powder having an excellent color tone was obtained. The resulting powder was tack-free and a small amount was kneaded with polyethylene gloved hands, but did not lump.
[0028]
Example 3
1 kg of konjac flour powder was extracted with 2 L of ethanol for 2 hours to obtain 10.3 g of the extract after distilling off the solvent (glycosphingolipid content: 6.43% by weight). This extract was dissolved in 30 mL of ethanol, washed with 80 mL of water for 2 hours, added with 15 g of sodium chloride, heated and boiled, and the oil phase floating on the upper portion of the aqueous phase was recovered. The recovered oil phase was dissolved in 30 mL of ethanol, and after removing insoluble components, 6.6 g of ethanol-soluble components were recovered (glycosphingolipid content: 9.32% by weight). This was dissolved in 40 mL of ethanol to obtain a dark brown solution A. Separately, 20 g of γ-cyclodextrin was mixed with 20 mL of water to obtain Paste B. The paste B was introduced into the solution A while stirring well, and the mixture was stirred well until the mixture became uniform, thereby obtaining a skin-colored sol C. After confirming that this flesh-colored sol C solidifies in a fresh cream form by standing for 5 minutes, it is vacuum-dried at 70 ° C. for 8 hours, and then pulverized by a pulverizer (household mill) to obtain a yellow uniform color. 30.3 g of a powder having an excellent color tone was obtained. The resulting powder was tack-free and a small amount was kneaded with polyethylene gloved hands, but did not lump.
[0029]
Example 4
50 kg of konjac flying powder was extracted with 100 L of ethanol for 2 hours to obtain 496 g of an extract after distilling off the solvent (glycosphingolipid content: 6.63% by weight). This extract was dissolved in 2 L of ethanol to obtain a dark brown solution A. Separately, 1 kg of β-cyclodextrin was mixed with 1 L of water to obtain a paste B. The solution A was put into the body of a super mixer SMV-20A manufactured by Kawata Corporation, and the paste B was further introduced while stirring, and then stirred well until uniform to obtain a skin-colored sol C. After confirming that the skin color sol C solidifies in a fresh cream form by standing for 5 minutes, the mixture is stirred under reduced pressure at a jacket circulating water temperature of 70 ° C. for 8 hours, and finally, a uniform yellow skin color is obtained. 1449 g of powder having a good color were discharged. The resulting powder was tack-free and a small amount was kneaded with polyethylene gloved hands, but did not lump.
[0030]
Example 5
50 kg of konjac flying powder was extracted with 100 L of ethanol for 2 hours to obtain 496 g of an extract after distilling off the solvent (glycosphingolipid content: 6.63% by weight). This extract was dissolved in 2 L of ethanol to obtain a dark brown solution A. Separately, 1 kg of β-cyclodextrin was mixed with 1 L of water to obtain a paste B. The solution A was put into an empty tank, and the paste B was further introduced while stirring, and then stirred well until uniform, to obtain a skin-colored sol C. After confirming that this skin-colored sol C solidified in a fresh cream state by standing for 5 minutes, it was pulverized with a drum dryer DD-1 manufactured by Chuo Kakoki Co., Ltd. The internal pressure was reduced, the drum surface temperature was set to 95 ° C., the drum was set to 1 revolution / minute, and the sol C solidified in a creamy state was sequentially charged from the upper hopper, and powdered sequentially. First, 1481 g of powder having a uniform yellowish color tone was discharged. The resulting powder was tack-free and a small amount was kneaded with polyethylene gloved hands, but did not lump.
[0031]
Example 6
1 kg of defatted rice bran was extracted with 2 L of ethanol for 2 hours to obtain 14.2 g of an extract (e.g., glycosphingolipid content: 1.41% by weight) after distilling off the solvent. This extract was dissolved in 60 mL of ethanol to obtain a yellow-brown solution A. Separately, 40 g of β-cyclodextrin was mixed with 40 mL of water to obtain Paste B. The paste B was introduced into the solution A with stirring well, and the mixture was stirred well until the mixture became uniform, thereby obtaining a light yellow sol C. After confirming that the sol C was solidified in a fresh cream form by standing for 5 minutes, it was vacuum-dried at 70 ° C. for 8 hours, and then pulverized with a pulverizer (household mill) to obtain a pale yellow uniform 51.8 g of a powder having a color tone were obtained. The resulting powder was tack-free and a small amount was kneaded with polyethylene gloved hands, but did not lump.
[0032]
Comparative Example 1
1 kg of konjac flour powder was extracted with 2 L of ethanol for 2 hours to obtain 10.3 g of the extract after distilling off the solvent (glycosphingolipid content: 6.43% by weight). This extract was dissolved in 100 mL of ethanol to obtain a brown solution A. Separately, 20 g of β-cyclodextrin was mixed with 20 mL of water to obtain Paste B. The paste B was introduced into the solution A while stirring well, and the mixture was stirred well until the mixture became uniform, thereby obtaining a skin-colored sol C. As soon as the stirring was stopped, the flesh-colored sol C precipitated cyclodextrin and separated from the transparent supernatant, and the overall viscosity did not increase. The sol C was vacuum-dried at 70 ° C. for 8 hours, and then pulverized with a pulverizer (a household mill) to obtain 26.6 g of a substance having an ocher, slightly dark and light mottled color tone. On the side, some sticky, non-crushed material was found sticky and sticky. The obtained product was strongly sticky and a small amount was kneaded with a hand wearing polyethylene gloves. However, it became lumpy and could not be returned to the original powder state.
[0033]
Comparative Example 2
1 kg of konjac flour powder was extracted with 2 L of ethanol for 2 hours to obtain 10.3 g of the extract after distilling off the solvent (glycosphingolipid content: 6.43% by weight). This extract was dissolved in 40 mL of ethanol to obtain a brown solution A. Separately, 20 g of corn starch was mixed with 20 mL of water to obtain Paste B. The paste B was introduced into the solution A while stirring well, and the mixture was stirred well until the mixture became uniform, thereby obtaining a skin-colored sol C. As soon as the stirring was stopped, the flesh-colored sol C precipitated corn starch and separated from the clear supernatant, and the overall viscosity did not increase. The sol C was vacuum-dried at 70 ° C. for 8 hours, and then pulverized with a pulverizer (household mill) to obtain 27.2 g of a substance having an ocher, slightly dark and light mottled color tone. On the side, some sticky, non-crushed material was found sticky and sticky. The obtained product was strongly sticky and a small amount was kneaded with a hand wearing polyethylene gloves. However, it became lumpy and could not be returned to the original powder state.
[0034]
Comparative Example 3
1 kg of konjac flour powder was extracted with 2 L of ethanol for 2 hours to obtain 10.3 g of the extract after distilling off the solvent (glycosphingolipid content: 6.43% by weight). This extract was dissolved in 40 mL of tetrahydrofuran to obtain a brown solution A. Separately, 20 g of β-cyclodextrin was mixed with 20 mL of water to obtain Paste B. The paste B was introduced into the solution A while stirring well. However, even if the mixture was sufficiently mixed, the mixture did not become a uniform sol, and irregularly sized lumps of cyclodextrin were settled and the solution floated on the upper part. Was obtained. This sol C was vacuum-dried at 70 ° C. for 8 hours as it was, and then crushed by a crusher (household mill). Did not.
[0035]
【The invention's effect】
ADVANTAGE OF THE INVENTION According to this invention, in powderization of a glycosphingolipid-containing composition, a sticky powder is obtained, which has no conventional problems such as strong stickiness, high adhesion of a surface, and easy formation of lumps. I can do it.

Claims (4)

環状オリゴ糖を賦形剤として含み、粉末状であることを特徴とするスフィンゴ糖脂質含有組成物。A glycosphingolipid-containing composition comprising a cyclic oligosaccharide as an excipient and being in powder form. 環状オリゴ糖が、β−シクロデキストリン又は/及びγ−シクロデキストリンである請求項1記載のスフィンゴ糖脂質含有組成物。The glycosphingolipid-containing composition according to claim 1, wherein the cyclic oligosaccharide is β-cyclodextrin and / or γ-cyclodextrin. スフィンゴ糖脂質含有組成物が、こんにゃく芋、こんにゃく精粉、こんにゃく荒粉及びこんにゃくトビ粉からなる群から選ばれる少なくとも1種の原料から、溶媒抽出により得られたものである請求項1又は2に記載のスフィンゴ糖脂質含有組成物。The composition according to claim 1 or 2, wherein the glycosphingolipid-containing composition is obtained by solvent extraction from at least one kind of raw material selected from the group consisting of konjac potato, konjac fine powder, konjac coarse powder and konjac tobi powder. The glycosphingolipid-containing composition according to the above. 以下の(a)及び(b)の性質を有する水以外の溶媒が、容量比で水に対し、1/50以上、3倍以下の割合で共存する状態において、スフィンゴ糖脂質含有物と環状オリゴ糖を接触させたのち、乾燥することを特徴とする請求項1〜3に記載されたいずれかのスフィンゴ糖脂質含有組成物の製造方法。
(a)水と相互溶解すること
(b)水との共存下又は無水状態において、使用する環状オリゴ糖に包接されること
In a state in which a solvent other than water having the following properties (a) and (b) coexists at a volume ratio of 1/50 or more to water with respect to water, the glycosphingolipid-containing substance and the cyclic oligosaccharide are mixed. The method for producing a glycosphingolipid-containing composition according to any one of claims 1 to 3, wherein the composition is dried after contacting the sugar.
(A) Mutual dissolution with water (b) Inclusion with the cyclic oligosaccharide to be used in the presence of water or in an anhydrous state
JP2003020444A 2003-01-29 2003-01-29 Sphingoglycolipid-containing composition and its preparation method Pending JP2004231749A (en)

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