JP2016501709A - リン脂質含有乳化剤組成物 - Google Patents
リン脂質含有乳化剤組成物 Download PDFInfo
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- JP2016501709A JP2016501709A JP2015539792A JP2015539792A JP2016501709A JP 2016501709 A JP2016501709 A JP 2016501709A JP 2015539792 A JP2015539792 A JP 2015539792A JP 2015539792 A JP2015539792 A JP 2015539792A JP 2016501709 A JP2016501709 A JP 2016501709A
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- Prior art keywords
- phospholipid
- lecithin
- emulsion
- emulsifier
- oil
- Prior art date
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Abstract
Description
(a)リン脂質含有出発材料を、撹拌しながら、C1〜C3アルコールおよびこれらの混合物から選択される脂肪族アルコールを含む抽出剤と、リン脂質の少なくとも一部分を抽出剤中に移動させるのに十分な期間接触させること、
(b)遠心力を加えることを含む方法によって、得られた混合物を残留ラフィネートからリン脂質富化抽出物に分離すること、ここで、各分離段階からのリン脂質富化抽出物は、前のまたはさらなる上流の混合段階に少なくとも部分的に戻され、最終のリン脂質富化抽出物が第1の残留ラフィネートから分離される、
を含む抽出方法に関する。
好ましくは、ステップ(a)および(b)は、各段階に、i)ローターと、ii)2つの液体流が混合される、ローターに接続された混合室であって、iia)混合室内に配置された静止撹拌器(stationary agitator)、およびiib)混合室により生成される遠心力によって液体流が分離される沈降室とを含む混合室とを備える多段式抽出装置内で、少なくとも部分的に実行される。
有利には、静止撹拌器は静止ディスクを含み、混合は静止ディスクと回転する混合室との間の速度差によって達成される。ステップ(c)において、ラフィネート画分が乳化剤組成物として単離される。
図1は本方法の好ましい一実施形態を示す。ここで、リン脂質フィードタンク(1)および熱交換器(図示せず)を含む抽出剤タンク(2)が、最終抽出剤出口(4)および最終ラフィネート出口(4)を有する多段階遠心液−液抽出機(3)に流体連結されている。抽出剤フィードは、リン脂質フィードに対して向流で抽出機(3)に入り、最終の抽出剤が抽出剤容器(5)およびラフィネート容器(6)に集められる。タンク(1)および(2)の両方に、実際の実験に必要な流量、したがって抽出比を調整および制御するための流量計を備える。温度制御機器を熱交換器および遠心抽出機の入口と出口の両方に設置している。
抽出機:Rousselet Robatel(フランス)から得た多段階遠心液−液抽出機を実験において採用した。抽出機は中央ローターに接続された6つの回転ボウルを備え、最大回転速度は2,900rpm、最大流量(2相)は25〜30l/時であった。ボウルの有効容積は0.39lであった。
粗製大豆レシチンを、それぞれ2.5重量%および4.5重量%の水を含むエタノールで抽出した。表1は、いくつかの運転の適用結果であった条件を示す:
エマルションの調製
市販のアセトンで脱油し分画した大豆レシチン由来の乳化剤(比較例9)を、エタノールによる粗製大豆レシチンの多段階向流抽出から得られ、アセトンを用いた脱油に供しなかった、本発明による乳化剤(例10)と比較した。この2種の乳化剤の組成を表3に示す:
次いで例9および10から得た一次エマルションをコロイドミルに加えた。これらの2/3を加えた後、ビネガーおよびマスタードを加えた。組成物全体をさらに30秒間乳化させて、室温でジャーに充填した。
Claims (18)
- R1が1.2〜2.6の範囲であり、R2が0.6〜1.6の範囲である、請求項1に記載の乳化剤。
- R1が1.9〜2.6の範囲であり、R2が0.8〜1.6の範囲である、請求項1に記載の乳化剤。
- 少なくとも60重量%のアセトン不溶物含有量、および最大20重量%、好ましくは最大12重量%のホスファチジルコリン含有量を有する、請求項1〜3のいずれか一つに記載の乳化剤。
- 請求項1〜4のいずれか一つに記載の乳化剤組成物を含む油中水型エマルション。
- 請求項5に記載のエマルションを含む水中油中水型エマルション。
- 1種または複数のテクスチャー付与剤(texturing agent)、および/またはカルシウム塩をさらに含む、請求項5または6に記載のエマルション。
- 請求項1〜4のいずれか一つに記載の乳化剤を製造するための向流抽出方法であって、
(a)リン脂質含有出発材料を、撹拌しながら、C1〜C3アルコールおよびこれらの混合物から選択される脂肪族アルコール、好ましくはエタノールを含む抽出剤と、リン脂質の少なくとも一部分を抽出剤中に移動させるのに十分な期間接触させること、
(b)遠心力を加えることを含む方法によって、得られた混合物を残留ラフィネートからリン脂質富化抽出物に分離すること、ここで、各分離段階からのリン脂質富化抽出物は、前のまたはさらなる上流の混合段階に少なくとも部分的に戻され、乳化剤を含む最終のリン脂質富化抽出物が第1の残留ラフィネートから分離される、および
(c)リン脂質の少なくとも一部をラフィネートから単離して、乳化剤を得ること、
を含む方法。 - (a)において、リン脂質含有出発材料を、並流または向流混合操作で抽出剤と接触させる、請求項8に記載の方法。
- 脂肪族アルコール中の水濃度が0〜10重量%、好ましくは0〜5重量%の範囲である、請求項8または9に記載の方法。
- ステップ(a)および(b)が、多段式抽出装置であって、各段階に、
i)ローター、
ii)2つの液体流が混合される、ローターに接続された混合室、
を含み、前記混合質が、
iia)混合室内に配置された静止撹拌器、および
iib)混合室により生成される遠心力によって液体流が分離される沈降室
を含む、多段式抽出装置内で、少なくとも部分的に実行される、請求項8〜10のいずれか一つに記載の方法。 - 静止撹拌器が静止ディスクを含み、静止ディスクと回転する混合室との間の速度差によって混合が達成される、請求項11に記載の方法。
- リン脂質含有フィードが、レシチン、好ましくは、大豆レシチン、トウモロコシレシチン、菜種レシチン、コメ油レシチン、ヒマワリレシチン、綿実レシチン、パーム油レシチン、海洋性油レシチン、バイオマスレシチン、ピーナッツレシチン、卵黄レシチン、乳レシチンおよび/または脳レシチンから選択されるレシチン、好ましくは大豆レシチンを含む、請求項8〜12のいずれか一つに記載の方法。
- リン脂質の少なくとも一部をラフィネートおよび/または抽出相から単離することをさらに含む、請求項8〜13のいずれか一つに記載の方法。
- 油中水型エマルションを製造するための方法であって、
(i)脂質組成物を適量の、請求項1〜4のいずれか一つに記載の乳化剤と接触させて、エマルション安定化脂質組成物を得ること、および
(ii)エマルション安定化脂質組成物を第1の水相と接触させて、油中水型エマルションを形成すること、
を含む方法。 - 油中水型エマルションを第2の水相中に分散させて、油中水中油型エマルションを得ることをさらに含む、請求項15に記載の方法。
- 二次エマルションが、適切な細孔径を有するクロスフロー膜を用いて製造される、請求項16に記載の方法。
- 食品、好ましくはベーカリー製品、栄養補助食品、菓子類、インスタント食品、マーガリン、スプレッド;動物飼料製品;化粧料および/または医薬組成物の製造のための、または離型剤もしくは工業用乳化剤としての、請求項1〜4のいずれか一つに記載の、または請求項8〜14のいずれか一つに記載の方法によって得られる、リン脂質乳化剤の使用。
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WO2020252346A1 (en) * | 2019-06-14 | 2020-12-17 | POWELL, Brooks | Formulations of dihydromyricetin and a permeabilizer |
EP4108098A1 (en) * | 2020-04-17 | 2022-12-28 | Khismetov, Niaz Zainullovich | Method for processing grain to produce food products |
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