JP2019527220A - 没食子酸プロピル含有ビタミン製剤 - Google Patents
没食子酸プロピル含有ビタミン製剤 Download PDFInfo
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- JP2019527220A JP2019527220A JP2019502160A JP2019502160A JP2019527220A JP 2019527220 A JP2019527220 A JP 2019527220A JP 2019502160 A JP2019502160 A JP 2019502160A JP 2019502160 A JP2019502160 A JP 2019502160A JP 2019527220 A JP2019527220 A JP 2019527220A
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- Prior art keywords
- vitamin
- propyl gallate
- dispersion
- preparation
- powdered
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Abstract
Description
a1) ビタミンを、揮発性の水混和性有機溶媒中、又は水と水混和性有機溶媒との混合物中に、50℃〜200℃の温度で、場合により20バール〜100バールの昇圧下に、10秒未満の期間内溶解させること、
b1) a1)の後に得られた溶液を、コロイドの水性又はコロイド状分散溶液と0℃〜80℃の温度で急速に混合し、ビタミンをコロイド状分散形態で析出させること、
c1) 形成された分散液を、大部分の溶媒を除去し、その後乾燥させることにより乾燥粉末に変換すること
を含む、上記方法を提供する。
30gのシトラナキサンチンを、1.1gのパルミチン酸アスコルビルと共に240gのイソプロパノールに懸濁させ、混合チャンバAにおいて、圧力制限バルブを30バールに設定し、390gのイソプロパノールと連続的に混合した。混合チャンバAにおいては、懸濁液側は6L/h、溶媒側は9L/hの計量速度で、混合温度170℃が確立された。0.3秒の滞留時間後、混合チャンバBにおいて、分子分散溶液を、32gのゼラチン、71.4gのスクロース及び50gのグルコースシロップの水(4000g)中溶液と、100L/hのスループット速度で混合した。蒸留装置中で溶媒を減圧下に除去した後、活性成分分散液を得て、これに8gのヒマワリ油及び8gの没食子酸プロピルを添加した。ここで没食子酸プロピルを200mlの水に予溶解させ、NaOHでpH7に調整した。その後、この分散液を噴霧乾燥により安定な水溶性乾燥粉末に変換した。水に溶解させた後、光子相関分光法(PCS)により、粒径386nm(標準偏差142.5、多分散性指数PDI 0.185、D(95):660nm)が測定された(Malvern Zetasizer Nano ZSP)。
このように製造された粒子の安定性を、ストレス試験において試験した。この目的のため、それぞれ100mgの粒子の試料を製造し、4gのプレミックス混合物を50mLガラス瓶中に秤量した。このプレミックス混合物は、50重量%の微粉石灰(粒径<1000μm)、20重量%のコムギフスマ(粒径<1000μm)、20重量%の50%シリカ支持塩化コリン(粒径<1000μm)及び10重量%の微量元素混合物(粒径100〜500μm)からなり、この微量元素混合物は、46.78重量%のFeSO4×7H2O(100〜500μm)、37.43重量%のCuSO4×5H2O(100〜500μm)、11.79重量%のZnO(<500μm)、3.61重量%のMnO及び0.39重量%のCoO3からなるものであった。全成分の添加後、試料を手動で注意深く混合した。これらの試料を、40℃で空気湿度70%の環境制御チャンバ中に4週間保存した。保存の開始前及び保存の完了後、試料のシトラナキサンチン含有量を決定した。保存前及び保存後のシトラナキサンチン含有量の比を用いて、保持率を計算した。
pHが没食子酸プロピル活性に与える影響
この実験は、没食子酸プロピルの添加に最適なpH範囲が、pH4.5〜pH8.5の範囲内であることを示す。短い滞留時間であっても、8.5超のpH値又はかかるpH値における没食子酸プロピルの予溶解は、没食子酸プロピルの活性を著しく制限するのに十分であった。
没食子酸プロピル濃度が活性成分安定性に与える影響
a). 没食子酸プロピル濃度の増加は、シトラナキサンチン活性成分の安定性を増加させる。しかし、驚くべきことに、製剤中の没食子酸プロピルを10重量%まで増加させる場合、安定性の有意な低下が観察される。製剤中の没食子酸プロピルが4重量%〜9重量%、好ましくは7重量%〜9重量%、最適には8%〜9重量%において、極めて優れた安定化効果が観察された(表3a)。
b). 30gのカンタキサンチンを、1.1gのパルミチン酸アスコルビルと共に240gのイソプロパノールに懸濁させ、混合チャンバAにおいて、圧力制限バルブを30バールに設定し、390gのイソプロパノールと連続的に混合した。混合チャンバAにおいては、懸濁液側は6L/h、溶媒側は9L/hの計量速度で、混合温度170℃が確立された。0.3秒の滞留時間後、混合チャンバBにおいて、分子分散溶液を、32gのゼラチン及び121.4gのスクロースの水(4000g)中溶液と、100L/hのスループット速度で混合した。蒸留装置中で溶媒を減圧下に除去した後、活性成分分散液を得て、これに、8gのヒマワリ油及びいずれの場合も表3bに特定される量の没食子酸プロピルを添加した。ここで没食子酸プロピルを200mlの水に予溶解させ、NaOHでpH7に調整した。その後、この分散液を噴霧乾燥により安定な水溶性乾燥粉末に変換した。水に溶解させた後、PCSにより、粒径290nm(標準偏差140、多分散性指数PDI 0.193、D(95):594nm)が測定された(Malvern Zetasizer Nano ZSP)。
混合トコフェロール及びD,L α-トコフェロールが安定性に与える効果
合成源及び天然源に由来するトコフェロールは、それらの低い水溶性により、活性成分を含む相に溶解される。いずれの場合も、天然トコフェロール又は合成トコフェロールのみがそのまま添加される場合、それらの抗酸化剤としての保護効果及びそれらのカロテノイド又はレチノイドの安定化に差異はない。
a). 没食子酸プロピルとトコフェロール間の相乗効果
没食子酸プロピルとトコフェロールとの組み合わせに関して、この系については、安定性を喪失することなく製剤中の抗酸化剤の総濃度を低下させ得ることが見出された。この系について、4%没食子酸プロピルを含む製剤についての安定性(61.2%)と4%混合トコフェロールを含む製剤についての安定性(48.7%)とを互いに比較した場合、没食子酸プロピルが明らかにより優れた抗酸化剤である。対照的に、4%没食子酸プロピルを4%混合トコフェロールと混合して、それらの安定性(80.3%)を、8%没食子酸プロピルを含む製剤の安定性(83.3%)と比較した場合、個々の値からは予想され得なかった相乗効果が明らかである。この相乗効果は、没食子酸プロピル含有量が一定で、混合トコフェロールの濃度が4%から2%へと低下する場合に、さらにより顕著となる。この系については80.6%の安定性が測定される一方、6%没食子酸プロピルを含む系については71.3%の安定性しか得られない。これは明らかに、製剤中の抗酸化剤含有量を低下させながら安定性の有意な上昇を得るためには、特定の濃度の混合トコフェロールのみが必要とされることを示す。
30gのシトラナキサンチンを、1.1gのパルミチン酸アスコルビル及び9gの混合トコフェロールと共に240gのイソプロパノールに懸濁させ、混合チャンバAにおいて、圧力制限バルブを30バールに設定し、390gのイソプロパノールと連続的に混合した。混合チャンバAにおいては、懸濁液側は6L/h、溶媒側は9L/hの計量速度で、混合温度170℃が確立された。0.3秒の滞留時間後、混合チャンバBにおいて、分子分散溶液を、pH9に調整された、32gのゼラチン、71.4gのスクロース、50gのグルコースシロップ及び9gの没食子酸プロピルの水(4100g)中溶液と、100L/hのスループット速度で混合した。蒸留装置中で溶媒を減圧下に除去した後、活性成分分散液を得て、これに9gのヒマワリ油を添加した。その後、この分散液を噴霧乾燥により安定な水溶性乾燥粉末に変換した。水に溶解させた後、PCSにより、粒径280nm(標準偏差142.5、多分散性指数PDI 0.185)が測定された(Malvern Zetasizer Nano ZSP)。
その後、この分散液を噴霧乾燥により安定な水溶性乾燥粉末に変換した。水に溶解させた後、PCSにより、粒径290nm(標準偏差140、多分散性指数PDI 0.180)が測定された(Malvern Zetasizer Nano ZSP)。
Claims (23)
- ビタミンが本質的に0.7μm未満の粒径を有する粉末状ビタミン製剤であって、前記製剤が有効量の没食子酸プロピルを含む、前記粉末状ビタミン製剤。
- 使用される有効量が、製剤の総量に対して没食子酸プロピル3.5重量%〜9.5重量%であり、ここで製造中の没食子酸プロピルとビタミンとの重量比が0.21〜2.63である、請求項1に記載の粉末状ビタミン製剤。
- ビタミンが、ビタミンD、E、K若しくはQ又はそれらの誘導体、例えば、酢酸トコフェロール、トコトリエノールなどのビタミンEエステル、ビタミンK1、ビタミンK2、コエンザイムQ10及び、β-カロテン、カンタキサンチン、シトラナキサンチン、アスタキサンチン及びエステル誘導体、ゼアキサンチン及びエステル誘導体、ルテイン及びエステル誘導体、リコペン、アポカロテン酸及びエステル誘導体、アポカロテナールなどのカロテノイド、並びにこれらの混合物からなる群から選択される、請求項1又は2に記載の粉末状ビタミン製剤。
- 製剤が、ブチルヒドロキシトルエン又は合成及び/若しくは天然トコフェロールを含む、請求項1〜3のいずれか1項に記載の粉末状ビタミン製剤。
- トコフェロールが天然トコフェロールである、請求項4に記載の粉末状ビタミン製剤。
- 没食子酸プロピルとトコフェロールが、製剤中に9:1〜1:2の比で存在する、請求項4又は5に記載の粉末状ビタミン製剤。
- 没食子酸プロピルとブチルヒドロキシトルエンが、製剤中に8:1〜1:4の比で存在する、請求項4に記載の粉末状ビタミン製剤。
- 請求項1〜7のいずれか1項に記載の粉末状ビタミン製剤であって、ストレス試験において4週間後の、没食子酸プロピルではなく同量のエトキシキンを含む比較サンプル中の活性ビタミンの比(B2/B1)に対する該粉末状ビタミン製剤中の活性ビタミンの比(A2/A1)が少なくとも0.75であり、ここで該活性ビタミンの割合は、いずれの場合も、製造された製剤100mgと、50重量%の微粉石灰(<1000μm)、20重量%のコムギフスマ(<1000μm)、20重量%の50%シリカ支持塩化コリン(<1000μm)及び10重量%の微量元素混合物(100〜500μm)(前記微量元素混合物は、46.78重量%のFeSO4×7H2O(100〜500μm)、37.43重量%のCuSO4×5H2O(100〜500μm)、11.79重量%のZnO(<500μm)、3.61重量%のMnO及び0.39重量%のCoCO3からなる)の混合物4gとを50mLガラス容器中に秤量し、該成分を混合してこれらを40℃及び湿度70%の環境制御チャンバ中に4週間保存し、保存開始前のビタミン含有量(A1)及び(B1)並びに保存終了時のビタミン含有量(A2)及び(B2)を決定し、比A2/A1及びB2/B1から活性ビタミンの割合を計算することにより確認される、前記粉末状ビタミン製剤。
- ビタミンが本質的に0.7μm未満の粒径を有する微細粉末状ビタミン製剤の製造方法であって、以下のステップ:
a1) 該ビタミンを、揮発性の水混和性有機溶媒中、又は水と水混和性有機溶媒との混合物中に、50℃〜200℃の温度で、場合により昇圧下に、10秒未満の期間内溶解させるステップ、
a2) a)の後に得られた溶液を、コロイドの水性又はコロイド状分散溶液と0℃〜50℃の温度で急速に混合し、ビタミンをコロイド状分散形態で析出させるステップ、
a3) 形成された分散液を、大部分の溶媒を除去し、その後乾燥させることにより乾燥粉末に変換するステップ、
又は
a2) 該ビタミンを、揮発性の水不混和性有機溶媒中に、30〜150℃の温度で、場合により昇圧下に溶解させ、
b2) a)の後に得られた溶液を、コロイドの水性又はコロイド状分散溶液と混合し、エマルションを形成するステップ、
c2) 該エマルションから有機溶媒を除去し、形成された懸濁液/分散液を、水を除去し、その後乾燥させることにより乾燥粉末に変換するステップ、
又は
a3) 該ビタミンを、その融点超に加熱するか若しくはこれを油中に溶解させることにより、又はこれを室温で温置することにより液体に変換するステップ、
b3) a3)の後に得られた融液を、コロイドの水性又はコロイド状分散溶液と混合し、エマルションを形成するステップ、
c3) 形成された分散液を、水を除去し、その後乾燥させることにより乾燥粉末に変換するステップ、
を含み、該方法が有効量の没食子酸プロピルの存在下で行われる、前記方法。 - ビタミンが本質的に0.7μm未満の粒径を有する微細粉末状ビタミン製剤を製造するための請求項9に記載の方法であって、以下のステップ:
a1) 該ビタミンを、揮発性の水混和性有機溶媒中、又は水と水混和性有機溶媒との混合物中に、50℃〜200℃の温度で、場合により昇圧下に、10秒未満の期間内溶解させるステップ、
b1) a1)の後に得られた溶液を、コロイドの水性又はコロイド状分散溶液と0℃〜50℃の温度で急速に混合し、ビタミンをコロイド状分散形態で析出させるステップ、
c1) 形成された分散液を、大部分の溶媒を除去し、その後乾燥させることにより乾燥粉末に変換するステップ、
又は
a2) ビタミンを、揮発性の水不混和性有機溶媒中に、30〜150℃の温度で、場合により昇圧下に溶解させるステップ、
b2) a2)の後に得られた溶液を、コロイドの水性又はコロイド状分散溶液と混合し、エマルションを形成するステップ、
c2) 該エマルションから有機溶媒を除去し、形成された分散液を、水を除去し、その後乾燥させることにより乾燥粉末に変換するステップ、
又は
a3) 該ビタミンを、その融点超に加熱するか若しくはこれを油中に溶解させることにより、又はこれを室温で温置することにより液体に変換するステップ、
b3) a3)の後に得られた融液を、コロイドの水性又はコロイド状分散溶液と混合し、エマルションを形成するステップ、
c3) 形成された分散液を、水を除去し、その後乾燥させることにより乾燥粉末に変換するステップ、
を含み、使用される有効量が該製剤の総量に対して没食子酸プロピル3.5重量%〜9.5重量%であり、ここで該製造中の没食子酸プロピルとビタミンとの重量比は0.21〜2.63である、前記方法。 - 没食子酸プロピルが、有機溶媒含有ビタミン相及び/又はコロイド含有水溶液及び/又は形成された分散液に添加される、請求項9又は10に記載の方法。
- 請求項9〜11のいずれか1項に記載の方法であって、該方法が、pH4.5〜pH8.5のpHで、より好ましくは6.5〜8.5のpHで行われる、前記方法。
- コロイド含有水溶液への没食子酸プロピルの添加後、前記溶液が6.5〜8.5のpHに調整される、請求項12に記載の方法。
- トコフェロールが、有機溶媒含有ビタミン相に添加される、請求項9〜13のいずれか1項に記載の方法。
- トコフェロールが天然トコフェロールである、請求項14に記載の方法。
- 没食子酸プロピルとトコフェロールが9:1〜1:2の比で使用される、請求項14又は15に記載の方法。
- ブチルヒドロキシトルエンが、形成された分散液に添加される、請求項9〜13のいずれか1項に記載の方法。
- 没食子酸プロピルとブチルヒドロキシトルエンが、8:1〜1:4の比で使用される、請求項17に記載の方法。
- ビタミンが、ビタミンD、E、K若しくはQ又はそれらの誘導体、例えば、酢酸トコフェロール、トコトリエノールなどのビタミンEエステル、ビタミンK1、ビタミンK2、コエンザイムQ10及び、β-カロテン、カンタキサンチン、シトラナキサンチン、アスタキサンチン及びエステル誘導体、ゼアキサンチン及びエステル誘導体、ルテイン及びエステル誘導体、リコペン、アポカロテン酸及びエステル誘導体、並びにアポカロテナールなどのカロテノイドからなる群から選択される、請求項9〜18のいずれか1項に記載の方法。
- コロイドが、植物ガム、改変植物ガム、ゼラチン、改変ゼラチン、改変デンプン、リグノスルホネート、キトサン、カラギーナン、カゼイン、カゼイネート、乳清タンパク質、ゼイン、改変セルロース、ペクチン、改変ペクチン、植物タンパク質及び改変植物タンパク質又はそれらの混合物からなる群から選択される、請求項9〜19のいずれか1項に記載の方法。
- 請求項9〜20のいずれか1項に記載の方法により製造される粉末状ビタミン製剤。
- 動物飼料、食品、栄養補助食品、パーソナルケア製品又は医薬組成物中の添加剤としての、請求項1〜8及び21のいずれか1項に記載の粉末状ビタミン製剤の使用。
- 請求項1〜8及び21のいずれか1項に記載の粉末状ビタミン製剤を含む、動物飼料、食品、栄養補助食品、パーソナルケア製品又は医薬組成物。
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JP2022184913A (ja) * | 2016-07-19 | 2022-12-13 | ビーエーエスエフ ソシエタス・ヨーロピア | 没食子酸プロピル含有ビタミン製剤 |
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CN114767708B (zh) * | 2022-05-23 | 2024-01-23 | 珠海凤凰高科生物制药有限公司 | 一种稳定的妇科抑菌组合物及妇科护理液 |
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MX2019000846A (es) | 2019-06-24 |
JP7171542B2 (ja) | 2022-11-15 |
US10835456B2 (en) | 2020-11-17 |
CN109414054A (zh) | 2019-03-01 |
CL2019000123A1 (es) | 2019-04-05 |
AU2017300595B2 (en) | 2021-11-11 |
AU2017300595A1 (en) | 2019-02-28 |
WO2018015346A1 (de) | 2018-01-25 |
KR20190032459A (ko) | 2019-03-27 |
US20190240119A1 (en) | 2019-08-08 |
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EP3487319A1 (de) | 2019-05-29 |
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