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JPH0420037B2 - - Google Patents
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JPH0420037B2 - - Google Patents

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Publication number
JPH0420037B2
JPH0420037B2 JP19401582A JP19401582A JPH0420037B2 JP H0420037 B2 JPH0420037 B2 JP H0420037B2 JP 19401582 A JP19401582 A JP 19401582A JP 19401582 A JP19401582 A JP 19401582A JP H0420037 B2 JPH0420037 B2 JP H0420037B2
Authority
JP
Japan
Prior art keywords
unsaturated
oil
fats
oils
purification
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
JP19401582A
Other languages
Japanese (ja)
Other versions
JPS5984992A (en
Inventor
Hideo Ishiwatari
Takeshi Koresawa
Kyoko Koshiba
Masanori Aizawa
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.)
Shiseido Co Ltd
Original Assignee
Shiseido 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 Shiseido Co Ltd filed Critical Shiseido Co Ltd
Priority to JP19401582A priority Critical patent/JPS5984992A/en
Priority to EP83306586A priority patent/EP0108571A3/en
Publication of JPS5984992A publication Critical patent/JPS5984992A/en
Publication of JPH0420037B2 publication Critical patent/JPH0420037B2/ja
Granted legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/10Refining fats or fatty oils by adsorption
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/12Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by hydrogenation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fats And Perfumes (AREA)
  • Cosmetics (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) この発明は化粧料用不飽和油脂類に関し、その
目的は精製直後は勿論少なくとも精製後50±2℃
で30日経過後も過酸化物価を20以下に維持する化
粧料用不飽和油脂類の提供にある。 一般に、化粧料製品の種類は口紅、バニシング
クリーム等多数にわたり、各種類に応じて異なる
複種の原料を組合せて配合するものであり、化粧
料製品に添加される酸化防止剤の種類は配合され
る複数の原料の種類に最も適合するよう選定され
る。 また皮膚に直接使用するものであるから酸化防
止剤の添加量も配合の許す限り少量添加される。 しかしながら、精製直後の汎用的原料は将来他
のいかなる原料と配合されるのかが不明であるか
ら、将来の配合を予測して予め適当な酸化防止剤
を添加して保存しておくことができず、その精製
直後の原料の保存は酸化防止剤を無添加或いは微
量添加の状態で行うべきである。 この発明はかかる着想に基づいてなされたもの
で、精製後から配合に至る少なくとも30日経過後
も酸化防止剤を略無添加で保存できる汎用的な化
粧料用不飽和油脂類の提供を目的とする。 (発明の背景) 一般に、不飽和油脂類は不飽和トリグリセリド
油または不飽和ワツクス型エステル油の構造で天
然に広く存在しており、比較的炭素数が多いにも
拘わらず不飽和度の故に液状あるいは軟質で、多
くの用途を有しており、またオレイルオレエート
の如き不飽和合成油(不飽和ワツクス型エステル
油)も化粧品原料等の材料として広く用いられ
る。 しかしながら、不飽和油脂類の多くは極めて不
安定であり、また前記の如く不飽和油脂類にはト
リグリセリドとワツクス型エステルとがあるが、
後者の方が前者より酸化され易く、臭いもどりが
生じ易い。 更に近年では、このように経時変化した油脂類
は皮膚に障害を起こし、POV(過酸化物価)20以
上は好ましくないとされている。 そこで、化粧品原料としては、特に不飽和ワツ
クス型エステルについての安定化が、当業界では
より大きな課題であつた。 (従来技術) これらの不飽和油脂類を天然油脂類原料または
合成粗製油より精製するにはバツチ法による酸化
漂白や活性白土及び/又は活性炭を添加加熱攪拌
の後、これらを濾別する処理方法、あるいは必要
に応じてこれらにウインタリング・分子蒸留など
の手段を加えて行なうことが工業的に一般におこ
なわれ食用油脂等はこの様な精製で商品化され各
種食品に供されており、また経時安定性の向上に
はこの精製油脂用酸化防止剤の添加が有効手段と
されている。 実際このような従来技術としては、「油化学」
(日本油脂工業協会編集)雑誌に、原料油脂類を
精製する技術として水素添加処理が開示され、し
かも水素添加処理の前に触媒毒を除去するために
アルカリ精製、活性白土吸着処理(第19巻第8号
第26頁)することが記載されている。 更に当該「油化学」誌の当該号第36頁乃至第39
頁には、前記活性白土吸着処理を水素添加処理の
前及び後に行なう技術が開示され、実際食用不飽
和油脂(不飽和トリグリセライド油)類等の精製
不飽和油脂類はこのような精製手段で製造されて
いる。 しかしながら、これらの従来の精製手段では不
飽和油脂類の特長を生かしながら、その特有の嗅
気・色相特に経時的な酸化劣変に対する安定性を
高度に改良して化粧料用不飽和油脂類とすること
はできない。 特に不飽和ワツクス型エステル油は、一般に人
間が消化できずもし食すると下痢や脂漏症の原因
にになり、食用には適さないが化粧用には好適で
あるにも関わらず、その性状不安定の故に未だ公
知技術では解決しうるものが見られない。 その理由は、水素添加処理の前に行なう活性白
土処理は単に触媒毒を除去する目的で行なうもの
であるからその目的が異なりそこでその論究はさ
ておいても、主なる理由は水素添加処理後に行な
う活性白土処理が濾過工程を必要とする添加混合
方式であるのが通常であるためである。 そこで、このような欠点を解消せんとする試案
例が特公昭42−23589号公報で「食用硬化油(飽
和トリグリセライド油)の高度精製脱臭法」とし
て提案されている。 成る程、この方法は従来の如く、活性白土と水
添処理後の油脂とを単に混合してその後濾過する
方法ではなく、水添処理後の油脂を活性ケイ酸の
層に通液する技術であるから前記従来技術よりも
その精製度が改善される。 実際、該公報においては、歩留り率90%でしか
も食用油脂(飽和トリグリセライド油)としては
充分な品質を持つ精製油が記載されている。 しかしながら、この試案例方法の精製不飽和油
脂は食用油脂としては充分な安定性を持つていて
も、精製直後は勿論50℃で30日間経過後も酸化防
止剤を略添加することなく色変、臭いもどりなし
に保存する必要が有る化粧料用不飽和油脂類とし
ては充分であるとはいえないものであつた。 特に不飽和ワツクス型エステル油の安定性につ
いては、上記の公知の技術のみにて、到底実現し
得ないものである。 すなわち前記精製処理された不飽和油脂類は未
だ原油特有の臭気を残すことがあるとともに経時
的にはさらに酸化劣化によつて所謂“臭い戻り”
現象が著しく、過酸化物価の上昇も改善されがた
いのが常であつて、化粧料用不飽和油脂類として
は極めて不満足な精製油脂類であつた。 このことは主として不飽和ワツクス型エステル
構造の油脂であるオレンジラフイー油や、抹香鯨
油において特に顕著な傾向である。 不飽和油脂類の安定性に関する研究は古くより
おこなわれており、その不安定性の原因は不飽和
結合自体の変成、すなわち空気および熱・光・微
量重金属の存在における初期酸化反応を契機とし
て、複雑な酸化分解・重合反応などが連鎖的に誘
導されることに基づくとされている。 しかしながら、不飽和油脂類のもつ不飽和度の
ゆえに液状あるいは軟質であるという特徴を消失
させるまで水素添加処理をすることはできない。 従つて一口に不飽和油脂類といつても、不飽和
度の大小・不飽和結合の位置・幾何異性体などに
よつてその安定性に大差を生ずることは当然で例
えばオレイン酸は適当な酸化防止剤の添加により
ほぼ実用的に安定化されるがリノール酸・リノレ
ン酸等は実用化しにくいものである。 そこで、このような不飽和脂肪酸の安定化方法
のひとつとして精製不飽和油脂類中に存在する微
量または少量の不飽和結合2ケ以上のポリエン成
分を共役型・非共役型を問わず選択的に封鎖、経
時安定性を飛躍的向上させるために不飽和油脂類
のポリエン成分の選択的水素添加法が存在する。 しかしながらこの方法においては化粧品原料な
ど特に高品位の要求される場合には選択的水素添
加処理油では残臭気の問題よりなお不十分であつ
てさらに徹底した脱色・脱臭・および安定性の向
上が必要であつた。 例えば硬化牛脂(飽和トリグリセライド油)あ
るいはそれより得られる精製ステアリン酸といえ
ども、なお特有の嗅気を有しやむを得ず使用され
てはいるが、業界においては潜在的にその品質向
上に関する要望が強い。 更にこの選択的水素添加処理法の問題点として
は経時的な酸化劣変の問題が未だ残存し、長期間
の保存に耐え得ず経時的酸化劣変による臭い戻り
や着色による品質の劣化という問題があつた。 実際、前記特公昭42−23589号公報における試
案例「食用硬化油の高度精製脱臭法」の実施例に
おいても、水素添加した食用硬化油を、活性ケイ
酸層を通過させて精製した後、更に選択的水素添
加処理し、この油脂を再度活性ケイ酸層を通過さ
せた油が食用としてもこの試案例法の精製油脂よ
りも更に品質に優れることが実施例(2)として開示
されている。 この試案例法は前記した如く不飽和油脂類の精
製法としては、特に吸着処理が、吸着剤を混合添
加して吸着処理する従来例に較べ、n−ヘキサン
に油脂を溶解し、この溶解した油脂を活性ケイ酸
層を通過させて処理するという工程において、別
途従来例である特願昭53−102910号公報で開示さ
れた脱ガム植物油を少なくとも一回活性炭層を通
過させる技術と同様、吸着処理法の点では優れて
いるものであつた。 しかしながら、この特公昭42−23589号公報開
示の試案例方法である、精製油を再度選択水素添
加した後吸着処理する方法にも次のような欠点が
有つた。 すなわち、選択的水素添加の条件が不十分で、
たとえ、試料沃素価が81.6にも拘わらず水素後沃
素価が75.8の如き処理によつて得た油脂類であつ
ても経時的な過酸化物価の上昇をさけ難く食用油
としては充分であつても50℃で30日経過後も酸化
防止剤を略添加することなく色変、臭いもどりな
しに保存する必要がある化粧料用不飽和油脂類と
しては適さない。 その上活性ケイ酸という吸着特性に優れた吸着
剤を使用しているため除去を必要とする不純物以
外の成分が吸着除去されている嫌いが有り結果最
終精製物の歩留りが70%台と極めて低く、工業的
精製法に適さないという欠点があつた。 また、これら公知技術はいずれも食用油脂(不
飽和トリグリセライド油)の精製法に関するもの
であつて、不飽和トリグリセライド油よりも更に
不安定な不飽和ワツクス型エステル油について、
精製直後は勿論、少なくとも精製後50℃で30日経
過後も過酸化物価を20以下に維持する性状を有す
る油脂の記載及びそのような油脂を精製する条件
等も何ら具体的に開示されておらず、前述した化
粧料原料特有の課題を何ら解決しうるものでもな
かつた。 (解決手段) そこでこの発明者らは、不飽和油脂類の特徴で
ある液状あるいは軟質性を消失させることなく、
しかも50℃で30日経過後も酸化防止剤を略無添加
で保存できる化粧料用不飽和油脂類について、鋭
意研究を重ねた。 その結果、この発明者らは高級アルコールと高
級脂肪酸との不飽和エステル油であつて、前記高
級アルコールと高級脂肪酸のうちどちらか一方又
は両方の炭化水素部分には二重結合が2ケ以上含
有されてなるとともに多少の過酸化物をも含有さ
れてなる不飽和エステル油を原料油脂類とし、こ
の原料油脂類を選択的水素添加工程とカラムクロ
マトグラフ的精製工程との組合せで精製すること
により得られ、精製直後は勿論少なくとも精製後
50±2℃で30日経過後も過酸化物価を20以下に維
持する化粧料用不飽和油脂類であつてかつ不飽和
結合2ケ以上のポリエン脂肪酸又は/及びポリエ
ン脂肪酸アルコールの炭化水素部分が選択的にモ
ノエン体に変性され、かつ多少含まれている過酸
化物が還元されてなることを特徴とする化粧料用
不飽和油脂類を完成したものである。 これは、この発明者らが知得した驚くべき発
見、即ち不飽和精製油脂類を選択的水素処理した
だけの不飽和油脂類、カラムクロマトグラフ的精
製による(循環式精製及びバツチ式の精製のいず
れもを含む)精製処理のみによる油脂類等にそれ
ぞれ較べて、この発明による複合特定条件下での
両者の組合せ精製により得られた不飽和油脂類で
は飛躍的に経時的酸化劣変を防止できるという知
得に基くものである。 詳しくは、選択的水素添加処理、及びカラムク
ロマト的精製処理の両処理間に前後関係はなく、
その複合特定条件下の結合わせ処理により得られ
たものである。 (発明の構成) この発明において出発原料とされる高級アルコ
ールと高級脂肪酸との不飽和エステル油として
は、例えばオレンジラフイーオイル・抹香鯨油、
更にはオレイルオレエート等が好適に使用され、
高級アルコールと高級脂肪酸のうちどちらか一方
又は両方の炭化水素部分には二重結合が2ケ以上
含有され且つ多少の過酸化物をも含有されてなる
不飽和エステル油が使用される。 この発明で実施する選択的水素添加工程とは、
不飽和結合が2ケ以上のポリエン脂肪酸又は/及
びポリエン脂肪族アルコール部分を選択的にモノ
エン体に変性するとともに、多少含まれている過
酸化物を還元できる工程をいい、その好適な具体
例を示すと加圧条件が、ゲージ圧3気圧以下、加
熱温度は100乃至200℃で、処理時間は1乃至4hr
程度で触媒存在下の選択的水素添加方法であれば
よく、この触媒としては具体例を示すとニツケル
系触媒または銅−クロム系触媒が使用するのが望
ましく、その最も望ましい具体例としては
NIKKIN103B(日揮社(株)製)が挙げられる。 またこの発明において触媒添加量は少量とする
のが望ましく、その具体量としては、還元を要す
る不飽和エステル油に対して重量比で2〜3%程
度以下の添加量をいい、使用する油脂類の精製
度・種類・水添条件等によつて適宜勘案して定め
ればよい。 又、この発明で上記選択的水素添加工程の前処
理又は後処理として行うクロマトグラフ的精製工
程で使用する吸着剤として好適なものは、シリカ
ゲル、アルミナゲル、活性アルミナ、ケイ酸アル
ミニウム、ケイ酸マグネシウム、活性白土、酸性
白土、ゼオライト及びこれらの混合物が挙げら
れ、原料油脂の種類、品質に応じて適宜選択す
る。また、この発明では非極性溶剤としては、石
油エーテル、n−ヘキサン、n−ペンタンのよう
な脂肪族炭化水素および四塩化炭素のようなハロ
ゲン化炭化水素が好適に用いられる。 ここでカラムクロマトグラフ的精製工程とは、
上記非極性溶媒に溶解した不飽和油脂類を上記吸
着剤を充填した吸着塔に、少なくとも一回以上通
液して極性不純物を除去する手法をいう。 尚、通液の回数は不飽和油脂類の種類、必要と
される精製度、非極性溶媒の種類、特性、吸着剤
の種類、特性に応じて定めればよい。 最後に回収した溶液中から溶媒を留去する。 前述の如く、このカラムクロマトグラフ的精製
工程は、選択的水素添加工程の前処理又は後処理
として行う。 (発明の効果) この発明は高級アルコールと高級脂肪酸との不
飽和エステル油であつて、前記高級アルコールと
高級脂防酸のうちどちらか一方又は両方の炭化水
素部分には二重結合が2ケ以上含有されてなると
ともに多少の過酸化物をも含有されてなる不飽和
エステル油を原料油脂類とし、この原料油脂類を
選択的水素添加工程とカラムクロマトグラフ的精
製工程との組合せで精製することにより得られ、
精製直後は勿論少なくとも精製後50±2℃で30日
経過後も過酸化物価を20以下に維持する化粧料用
不飽和油脂類であつてかつ不飽和結合2ケ以上の
ポリエン脂肪酸又は/及びポリエン脂肪族アルコ
ールの炭化水素部分が選択的にモノエン体に変性
され、かつ多少含まれている過酸化物が還元され
てなることを特徴とする化粧料用不飽和油脂類で
あるから、以下の効果を奏する。 すなわち、精製後から配合に至る少なくとも50
℃で30日経過後も酸化防止剤を無添加で保存で
き、将来他のいかなる原料と組合わせて配合され
る場合であつても、その配合に応じて最も適合す
る酸化防止剤を配合時に必要最低量だけ入れて調
製することができ、更には臭いもどり現象及び変
色も長期間有効に防止でき、皮膚に直接用いられ
るとともに色、香が最も重要な要素である化粧料
原料として極めて有効である。 又、後述の実施例でも示す如く、経時的な耐酸
化劣変性においては、それぞれ選択的水素添加工
程、カラムクロマトグラフ的精製工程の単独処理
による精製不飽和油脂類の経時的安定度に較べて
飛躍的な安定度が確保できる。 以下、実施例を示すことによつて、この発明の
効果をより一層明確なものとする。 実施例 1乃至2 原材料として橙色透明で強い魚油臭をもつ不飽
和ワツクス型エステル油であるオレンジラフイー
オイルを用いた。このオレンジラフイーオイルは
酸価0.19、ケン化価102.8、ヨウ素価89.5であつ
た。 このオレンジラフイー油を次表第1表に示す条
件で選択的水素添加処理した。
(Field of Industrial Application) This invention relates to unsaturated oils and fats for cosmetics, and its purpose is to maintain the temperature at 50±2°C immediately after refining as well as at least after refining.
The purpose of the present invention is to provide unsaturated oils and fats for cosmetics that maintain a peroxide value of 20 or less even after 30 days have passed. In general, there are many types of cosmetic products such as lipsticks and vanishing creams, and each type is formulated with a combination of different raw materials, and the types of antioxidants added to cosmetic products vary. Selected to best suit multiple raw material types. Furthermore, since it is used directly on the skin, the amount of antioxidant added is as small as the formulation allows. However, since it is not known what other raw materials will be mixed with general-purpose raw materials immediately after purification, it is not possible to predict the future combination and add an appropriate antioxidant in advance for storage. The raw material immediately after its purification should be stored without or with a trace amount of antioxidant added. This invention was made based on this idea, and aims to provide general-purpose unsaturated oils and fats for cosmetics that can be preserved without adding antioxidants even after at least 30 days have elapsed from purification to formulation. . (Background of the Invention) In general, unsaturated oils and fats exist widely in nature with the structure of unsaturated triglyceride oil or unsaturated wax-type ester oil, and although they have a relatively large number of carbon atoms, they are liquid due to the degree of unsaturation. Alternatively, it is soft and has many uses, and unsaturated synthetic oils (unsaturated wax-type ester oils) such as oleyl oleate are also widely used as raw materials for cosmetics. However, many unsaturated fats and oils are extremely unstable, and as mentioned above, unsaturated fats and oils include triglycerides and wax-type esters.
The latter is more easily oxidized than the former, and the smell is likely to return. Furthermore, in recent years, it has been said that oils and fats that have changed over time can cause skin damage, and that POV (peroxide value) of 20 or more is not desirable. Therefore, stabilization of unsaturated wax-type esters as raw materials for cosmetics has been a major issue in the industry. (Prior art) These unsaturated oils and fats can be purified from natural oil and fat raw materials or synthetic crude oils by oxidative bleaching using a batch method, or by adding activated clay and/or activated carbon, heating and stirring, and then filtering them out. Or, if necessary, it is commonly carried out industrially to add means such as wintering or molecular distillation to these processes, and edible oils and fats are commercialized by such refining and used in various foods. Addition of antioxidants for refined oils and fats is considered an effective means for improving stability. In fact, such conventional technology is called "oil chemistry".
(edited by Japan Oil and Fat Manufacturers Association) magazine discloses hydrogenation treatment as a technology for refining raw material oils and fats, and also includes alkali purification and activated clay adsorption treatment (Volume 19) to remove catalyst poisons before hydrogenation treatment. No. 8, p. 26). Furthermore, pages 36 to 39 of the issue of the "Oil Chemistry" magazine
Page discloses a technique for performing the activated clay adsorption treatment before and after hydrogenation treatment, and in fact, refined unsaturated oils and fats such as edible unsaturated oils and fats (unsaturated triglyceride oils) are manufactured by such refining methods. has been done. However, these conventional refining methods take advantage of the characteristics of unsaturated oils and fats, while highly improving their unique odor and color, especially their stability against oxidative deterioration over time, to produce unsaturated oils and fats for cosmetics. I can't. In particular, unsaturated wax-type ester oils are generally indigestible by humans and can cause diarrhea or seborrhea if eaten. Due to its stability, no known technology has yet found a solution. The reason for this is that the activated clay treatment that is performed before the hydrogenation treatment is performed simply to remove catalyst poisons, so its purpose is different. This is because clay treatment is usually an additive mixing method that requires a filtration process. Therefore, an example of an attempt to overcome these drawbacks is proposed in Japanese Patent Publication No. 42-23589 as ``Advanced Purification and Deodorization Method for Edible Hydrogenated Oil (Saturated Triglyceride Oil)''. Indeed, this method is not a conventional method of simply mixing activated clay and hydrogenated fats and oils and then filtering it, but a technology in which the hydrogenated fats and oils are passed through a layer of activated silicic acid. Because of this, the degree of purification is improved over that of the prior art. In fact, this publication describes a refined oil with a yield rate of 90% and sufficient quality as an edible fat (saturated triglyceride oil). However, even though the refined unsaturated oils and fats produced by this proposed method have sufficient stability as edible oils and fats, they do not change color immediately after purification or even after 30 days at 50°C without adding any antioxidants. This could not be said to be sufficient as an unsaturated oil or fat for cosmetics, which needs to be stored without returning to its odor. In particular, the stability of unsaturated wax-type ester oil cannot be achieved using only the above-mentioned known techniques. In other words, the unsaturated oils and fats that have undergone the refining process may still retain the odor characteristic of crude oil, and over time, due to further oxidative deterioration, the so-called "odor return" occurs.
The phenomenon is remarkable, and the increase in peroxide value is usually difficult to improve, making refined oils and fats extremely unsatisfactory as unsaturated oils and fats for cosmetics. This tendency is particularly noticeable in orange roughy oil and fragrant whale oil, which are mainly oils and fats with an unsaturated wax type ester structure. Research on the stability of unsaturated oils and fats has been conducted for a long time, and the cause of their instability is a complex process triggered by the denaturation of the unsaturated bonds themselves, that is, the initial oxidation reaction in the presence of air, heat, light, and trace heavy metals. This is said to be based on the chain induction of oxidative decomposition and polymerization reactions. However, due to the degree of unsaturation of unsaturated fats and oils, hydrogenation treatment cannot be performed until they lose their liquid or soft characteristics. Therefore, even though unsaturated oils and fats are referred to as unsaturated fats and oils, it is natural that their stability varies greatly depending on the degree of unsaturation, the position of the unsaturated bond, geometric isomer, etc. Addition of an inhibitor can stabilize it for practical purposes, but linoleic acid, linolenic acid, etc. are difficult to put into practical use. Therefore, one method for stabilizing unsaturated fatty acids is to selectively remove trace or small amounts of polyene components with two or more unsaturated bonds, whether conjugated or non-conjugated, that exist in refined unsaturated fats and oils. There is a method of selectively hydrogenating the polyene component of unsaturated oils and fats in order to dramatically improve the sequestration and stability over time. However, in cases where particularly high quality is required, such as cosmetic raw materials, selectively hydrogenated oil is still insufficient due to the problem of residual odor, and more thorough decolorization, deodorization, and stability improvement are required. It was hot. For example, hardened beef tallow (saturated triglyceride oil) or purified stearic acid obtained from it still has a unique odor and is unavoidably used, but there is a strong demand in the industry for potentially improving its quality. Furthermore, the problem with this selective hydrogenation treatment method is that the problem of oxidation deterioration over time still remains, and the problem is that it cannot withstand long-term storage and quality deteriorates due to return of odor and coloring due to oxidation deterioration over time. It was hot. In fact, in the example of the draft example "Advanced purification and deodorization method for edible hydrogenated oil" in the above-mentioned Japanese Patent Publication No. 42-23589, hydrogenated edible hydrogenated oil is purified by passing through an activated silicic acid layer, and then further It is disclosed in Example (2) that the oil obtained by selectively hydrogenating and passing this fat and oil through the activated silicic acid layer again is even better in quality than the refined fat and oil produced by this draft example method even when used for human consumption. As mentioned above, this proposed method is a method for refining unsaturated fats and oils, in particular, the adsorption treatment is performed by dissolving fats and oils in n-hexane. In the process of treating fats and oils by passing them through an activated silicic acid layer, similar to the technology disclosed in Japanese Patent Application No. 53-102910, which is a conventional example, in which degummed vegetable oil is passed through an activated carbon layer at least once, adsorption is performed. It was an excellent treatment method. However, the method disclosed in Japanese Patent Publication No. 42-23589, in which the refined oil is selectively hydrogenated again and then subjected to adsorption treatment, also had the following drawbacks. In other words, the conditions for selective hydrogenation are insufficient,
Even though the sample iodine value is 81.6, the iodine value after hydrogenation is 75.8. Even if the oil is obtained through a treatment such that the iodine value after hydrogenation is 75.8, it is difficult to avoid an increase in peroxide value over time and it is sufficient as an edible oil. However, it is not suitable as unsaturated oils and fats for cosmetics, which need to be stored without changing color or returning odor even after 30 days at 50°C without adding antioxidants. Furthermore, since activated silicic acid, an adsorbent with excellent adsorption properties, is used, components other than the impurities that need to be removed may be adsorbed and removed, resulting in an extremely low yield of the final purified product at around 70%. However, it had the disadvantage that it was not suitable for industrial purification methods. In addition, all of these known techniques relate to methods for refining edible fats and oils (unsaturated triglyceride oil), and regarding unsaturated wax-type ester oil, which is more unstable than unsaturated triglyceride oil,
There is no specific description of oils and fats that maintain a peroxide value of 20 or less not only immediately after purification, but also at least 30 days after purification at 50°C, and the conditions for refining such oils and fats. However, it was not possible to solve the above-mentioned problems unique to cosmetic raw materials. (Solution) Therefore, the present inventors solved the problem without losing the liquid or soft properties characteristic of unsaturated oils and fats.
In addition, we have conducted extensive research into unsaturated oils and fats for cosmetics that can be preserved without adding antioxidants even after 30 days at 50°C. As a result, the present inventors found that an unsaturated ester oil of a higher alcohol and a higher fatty acid contains two or more double bonds in the hydrocarbon moiety of either or both of the higher alcohol and the higher fatty acid. By using an unsaturated ester oil which has been processed and also contains some peroxide as a raw material oil and fat, and refining this raw material oil and fat by a combination of a selective hydrogenation process and a column chromatographic purification process. obtained, not only immediately after purification, but also at least after purification.
Selected unsaturated oils and fats for cosmetics that maintain a peroxide value of 20 or less even after 30 days at 50±2℃, and the hydrocarbon moiety of a polyenoic fatty acid or/and polyenoic fatty acid alcohol that has two or more unsaturated bonds. This is a completed unsaturated oil and fat for cosmetics, which is characterized by being denatured into a monoene form, and by reducing some of the peroxide contained therein. This is due to the surprising discovery made by the inventors, namely, that unsaturated refined oils and fats can be produced by selective hydrogen treatment, and column chromatographic purification (refined by cyclic purification and batch purification). Compared to oils and fats that are obtained by refining alone (including both types of oils and fats), unsaturated oils and fats obtained by the combined refining of both under complex specific conditions according to the present invention can dramatically prevent oxidative deterioration over time. It is based on this knowledge. Specifically, there is no relationship between the selective hydrogenation treatment and the column chromatographic purification treatment;
This was obtained through a combination process under specific conditions. (Structure of the Invention) Examples of the unsaturated ester oil of higher alcohol and higher fatty acid used as starting materials in this invention include orange roughy oil, matcha whale oil,
Furthermore, oleyl oleate etc. are preferably used,
An unsaturated ester oil containing two or more double bonds in the hydrocarbon moiety of one or both of the higher alcohol and higher fatty acid and also contains some peroxide is used. The selective hydrogenation step carried out in this invention is:
It refers to a process in which a polyene fatty acid or/and a polyene aliphatic alcohol moiety having two or more unsaturated bonds is selectively modified into a monoene form, and at the same time, a certain amount of peroxide contained therein can be reduced. Preferred specific examples thereof are as follows. The pressurization conditions are 3 atm gauge pressure or less, heating temperature 100 to 200℃, and processing time 1 to 4 hours.
Any selective hydrogenation method in the presence of a catalyst may be sufficient, and as a specific example, it is desirable to use a nickel-based catalyst or a copper-chromium based catalyst, and the most desirable specific example is
An example is NIKKIN103B (manufactured by JGC Corporation). In addition, in this invention, it is desirable to add a small amount of catalyst, and the specific amount is about 2 to 3% by weight or less based on the unsaturated ester oil that requires reduction, and It may be determined by appropriately considering the degree of purification, type, hydrogenation conditions, etc. Further, in this invention, suitable adsorbents for use in the chromatographic purification step performed as a pre-treatment or post-treatment of the selective hydrogenation step are silica gel, alumina gel, activated alumina, aluminum silicate, and magnesium silicate. , activated clay, acid clay, zeolite, and mixtures thereof, and are appropriately selected depending on the type and quality of the raw material oil. Further, in the present invention, aliphatic hydrocarbons such as petroleum ether, n-hexane, and n-pentane, and halogenated hydrocarbons such as carbon tetrachloride are preferably used as the nonpolar solvent. Here, the column chromatographic purification process is
A method in which polar impurities are removed by passing unsaturated oils and fats dissolved in the non-polar solvent through an adsorption tower filled with the adsorbent at least once. The number of times of liquid passage may be determined depending on the type of unsaturated oil and fat, the required degree of purification, the type and characteristics of the nonpolar solvent, and the type and characteristics of the adsorbent. Finally, the solvent is distilled off from the recovered solution. As mentioned above, this column chromatographic purification step is carried out as a pre-treatment or post-treatment of the selective hydrogenation step. (Effects of the Invention) The present invention provides an unsaturated ester oil of a higher alcohol and a higher fatty acid, in which the hydrocarbon moiety of one or both of the higher alcohol and the higher fatty acid-protecting acid has two double bonds. The unsaturated ester oil containing the above-mentioned substances and some peroxides is used as a raw material oil and fat, and this raw material oil and fat is purified by a combination of a selective hydrogenation step and a column chromatographic purification step. obtained by
Unsaturated oils and fats for cosmetics that maintain a peroxide value of 20 or less immediately after purification as well as at least 30 days after purification at 50±2°C, and which have two or more unsaturated bonds and/or polyene fatty acids and/or polyene fats. These unsaturated oils and fats for cosmetics are characterized by selectively modifying the hydrocarbon moiety of group alcohols into monoenes and reducing some of the peroxides contained in them. play. That is, at least 50
Even after 30 days at °C, it can be stored without adding antioxidants, and even if it is combined with any other raw materials in the future, the most compatible antioxidant can be added to the minimum required amount at the time of compounding. It can be prepared by adding only a small amount, and can effectively prevent odor return and discoloration for a long period of time. It can be used directly on the skin and is extremely effective as a raw material for cosmetics in which color and fragrance are the most important factors. In addition, as shown in the examples below, in terms of resistance to oxidative deterioration over time, the stability over time of refined unsaturated oils and fats obtained by the selective hydrogenation step and the column chromatographic refining step alone is higher. Dramatic stability can be ensured. Hereinafter, the effects of this invention will be made clearer by showing examples. Examples 1 and 2 Orange roughy oil, which is an unsaturated wax-type ester oil that is transparent and orange in color and has a strong fish oil odor, was used as a raw material. This orange roughy oil had an acid value of 0.19, a saponification value of 102.8, and an iodine value of 89.5. This orange roughy oil was subjected to selective hydrogenation treatment under the conditions shown in Table 1 below.

【表】 この選択的水素添加処理による不飽和油脂の性
状を第2表に、50±2℃での保存特性を第2−1
表にそれぞれ示す。
[Table] Table 2 shows the properties of unsaturated oils and fats obtained by this selective hydrogenation treatment, and Table 2-1 shows the storage characteristics at 50±2℃.
Each is shown in the table.

【表】【table】

【表】 この第2−1表より明らかな如く、選択的水素
添加処理のみによるオレンジラフイーオイルは短
期間に悪化することが判明した。 この実施例1及び2で得られたオレンジラフイ
ー処理油50gを、それぞれ2検体(実施例1;
a,c、実施例2;b,d)調製し、次のカラム
クロマトグラフ的精製処理した。 すなわち、非極性有機溶剤としてN−ヘキサン
150mlに溶解させ、吸着剤100gを充填したカラム
に通液しさらにN−ヘキサン200mlを通液し、こ
の溶出液を数回通液して精製油を溶出したのちN
−ヘキサンを蒸発留去し精製油とした。 この試験に使用した吸着剤、収率及び得られた
精製不飽和油脂の性状を第3表、第4表に示す。 また、50±2℃の保存特性を第4−1表に示
す。
[Table] As is clear from this Table 2-1, it was found that orange roughy oil treated only with selective hydrogenation deteriorated in a short period of time. Two samples each of 50 g of orange roughy treated oil obtained in Examples 1 and 2 (Example 1;
a, c, Example 2; b, d) were prepared and subjected to the following column chromatographic purification treatment. That is, N-hexane is used as a nonpolar organic solvent.
The solution was dissolved in 150 ml and passed through a column packed with 100 g of adsorbent, and then 200 ml of N-hexane was passed through the column. This eluate was passed several times to elute the refined oil, and then N-hexane was passed through the column.
- Hexane was distilled off to obtain a refined oil. The adsorbent used in this test, the yield, and the properties of the purified unsaturated oil and fat obtained are shown in Tables 3 and 4. Furthermore, the storage characteristics at 50±2°C are shown in Table 4-1.

【表】【table】

【表】【table】

【表】 このように選択的水素添加処理後、カラムクロ
マトグラフ的精製処理をしたこの発明に係る不飽
和脂肪類は50℃で30日経過しても、過酸化物価は
20以下であつた。 上記精製法で得られた選択的水素添加処理後の
不飽和油脂50gを各3検体(実施例1;e,g,
i、実施例2;f,h,j)調製しバツチ式のカ
ラムクロマトグラフ的精製処理を行つた。 その吸着剤の種類及び収率を第5表に、更にそ
の性状を第6表にそれぞれ示す。
[Table] Even after 30 days at 50°C, the unsaturated fats according to the present invention, which have been subjected to column chromatographic purification after selective hydrogenation, have a low peroxide value.
It was below 20. Three samples each (Example 1; e, g,
i, Example 2; f, h, j) were prepared and subjected to batch column chromatographic purification. Table 5 shows the type and yield of the adsorbent, and Table 6 shows its properties.

【表】【table】

【表】 以上の結果より、この発明に係るカラムクロマ
トグラフ的精製法(複数回通液)はこの発明法に
係るカラムクロマトグラフ的バチ精製法(1回通
液)に較べて優れていることが判る。 実施例 3及び4 不飽和油脂として黄褐色で強い特異臭を持つ、
主として不飽和ワツクス型エステル油である抹香
鯨油を使用した。その性状は第8表に示し、保存
特性を第8−1表に示す。 この抹香鯨油を第7表に示す条件で選択的水素
添加を行つた。
[Table] From the above results, the column chromatographic purification method (multiple passes) according to the present invention is superior to the column chromatographic purification method (single pass) according to the present invention. I understand. Examples 3 and 4 Unsaturated oils and fats are yellowish brown in color and have a strong characteristic odor.
Matcha whale oil, which is an unsaturated wax-type ester oil, was mainly used. Its properties are shown in Table 8, and its storage characteristics are shown in Table 8-1. Selective hydrogenation of this Macaron whale oil was carried out under the conditions shown in Table 7.

【表】【table】

【表】【table】

【表】【table】

【表】 第8−1表のように、選択的水素添加処理のみ
の抹香鯨油は、過酸化物価は短時間の内に上昇
し、油が劣化することが判明した。 上記実施例3及び4で得られた選択的水素添加
処理後の抹香鯨油50gをそれぞれ2検体調製し
た。(実施例3;a,c、実施例4;b,d) この検体を非極性有機溶剤として、N−ヘキサ
ン150mlに溶解し、吸着剤100gを充填したカラム
に通液しさらにN−ヘキサン200ml通液し、この
溶出液を循環通液し、精製油を溶出する。 さらにN−ヘキサンを蒸発留去し、精製油とし
た。 吸着剤、収率及び結果を第9表及び第10表に示
す。 保存特性を第10−1表に示す。
[Table] As shown in Table 8-1, it was found that the peroxide value of Macaroma whale oil treated only with selective hydrogenation increased within a short period of time, and the oil deteriorated. Two samples of 50 g of the selectively hydrogenated whale oil obtained in Examples 3 and 4 were each prepared. (Example 3: a, c, Example 4: b, d) This sample was dissolved in 150 ml of N-hexane as a non-polar organic solvent, passed through a column packed with 100 g of adsorbent, and further 200 ml of N-hexane. This eluate is circulated and purified oil is eluted. Furthermore, N-hexane was distilled off to obtain a refined oil. Adsorbents, yields and results are shown in Tables 9 and 10. The storage characteristics are shown in Table 10-1.

【表】【table】

【表】【table】

【表】 第10−1表このように選択的水素添加処理後、
カラムクロマトグラフ的精製処理すれば、処理後
50℃で保存し30日経過しても過酸化物価は20を越
さない。 実施例 5 淡黄色の性状で油臭を持ち酸化0.2、ケン化価
187.5、ヨウ素価81.3の不飽和トリグリセライド
油であるオリーブ油を用いて、このオリーブ油50
gを非極性有機溶剤N−ヘキサン150mlに溶解し、
吸着剤100g(実施例5;活性白土)を充填した
カラムに通液し、更にN−ヘキサンを通液、この
溶出液を循環通液した後、N−ヘキサンを蒸発留
去して精製油とした。 この精製油の性状を第11表に、保存特性を第11
−1表にそれぞれ示す。
[Table] Table 10-1 After selective hydrogenation treatment as described above,
After column chromatographic purification,
Even after 30 days of storage at 50℃, the peroxide value does not exceed 20. Example 5 Pale yellow color with oily odor, oxidation value of 0.2, saponification value
187.5, this olive oil is an unsaturated triglyceride oil with an iodine value of 81.3.
Dissolve g in 150 ml of non-polar organic solvent N-hexane,
The liquid was passed through a column packed with 100 g of adsorbent (Example 5; activated clay), and then N-hexane was passed through it. After circulating the eluate, the N-hexane was evaporated to form a purified oil. did. The properties of this refined oil are shown in Table 11, and the storage characteristics are shown in Table 11.
-1 Table shows each.

【表】【table】

【表】 第11−1表のように、カラムクロマトグラフ的
精製処理だけでは、短時間の間に過酸化物価が増
大し油が劣化する。 この精製油を第12表の条件で選択的水素添加処
理をした。
[Table] As shown in Table 11-1, column chromatographic purification alone increases the peroxide value and deteriorates the oil in a short period of time. This refined oil was subjected to selective hydrogenation treatment under the conditions shown in Table 12.

【表】 得られた精製油の性状を第13表に保存性を第13
−1にそれぞれ記す。
[Table] The properties of the obtained refined oil are shown in Table 13.
-1 respectively.

【表】【table】

【表】【table】

【表】 後、
このように、カラムクロマトグラフ的精製処理
後、選択的水素添加処理すると、過酸化物価は50
℃30日経過しても、僅かの劣化にとどめることが
できる。 <経時的酸化性> 実施例1,3,5で得られた精製不飽和油脂
(検体A,B,C)と比較例として実施例1,3
で得られた中間精製不飽和油脂(選択的水素添加
処理のみした不飽和油脂)(検体D,E)および
実施例5で得られた中間精製不飽和油脂(カラム
クロマトグラフ的循環精製処理のみした不飽和油
脂)(検体F)50gを100mlのガラスビーカーにと
り50±2℃の恒温器内に放置し、一定時間ごとに
POV値及び臭いについて試験を行つた。 この試験方法は、前記保存特性試験と同一であ
る。 このPOV値の測定は、日本油化学協会基準油
脂分析試験法2・4・12−1の規格に基づいて行
つた。 臭いについては、30日後の結果をまとめて第14
表に示す。 又POVの経日的変化は第1図にまとめて示す。
[Table] After,
In this way, when selective hydrogenation treatment is performed after column chromatographic purification treatment, the peroxide value is 50.
Even after 30 days at ℃, there is only slight deterioration. <Oxidability over time> Purified unsaturated fats and oils obtained in Examples 1, 3, and 5 (specimens A, B, C) and Examples 1 and 3 as comparative examples
Intermediately purified unsaturated fats and oils obtained in Example 5 (unsaturated fats and oils subjected to selective hydrogenation treatment) (Samples D and E) and intermediately purified unsaturated fats and oils obtained in Example 5 (unsaturated fats and oils subjected to only column chromatographic circulation purification treatment) Put 50g of unsaturated fats and oils (sample F) into a 100ml glass beaker and leave it in a thermostat at 50±2°C, and
Tests were conducted for POV value and odor. This test method is the same as the storage property test described above. The POV value was measured based on the Japan Oil Chemists' Association Standard Oil and Fat Analysis Test Method 2.4.12-1. Regarding odor, we summarized the results after 30 days and
Shown in the table. The daily changes in POV are summarized in Figure 1.

【表】 以上実施例1乃至5更には経日的酸化性試験の
結果から判るように、この発明に係る化粧料用不
飽和油脂類は精製50℃で30日後でも酸化防止剤の
添加なしに経日的な酸化安定性に特にすぐれ、所
謂臭い戻り現象がなく化粧料原料として極めて有
用であることが分る。
[Table] As can be seen from Examples 1 to 5 and the results of the daily oxidation test, the unsaturated oils and fats for cosmetics according to the present invention can be purified without adding antioxidants even after 30 days at 50°C. It is found that it has particularly excellent oxidation stability over time, and is extremely useful as a cosmetic raw material because there is no so-called odor return phenomenon.

【図面の簡単な説明】[Brief explanation of drawings]

第1図はこの発明の実施例及び比較例で得られ
た油脂の経日的酸化特性曲線を示す図である。 A……実施例1、B……実施例2、C……実施
例3、D……選択的水素添加処理のみをしたオレ
ンジラフイー油、E……選択的水素添加処理のみ
をした抹香鯨油、F……カラムクロマトグラフ的
循環精製処理のみしたオリーブ油。
FIG. 1 is a diagram showing oxidation characteristic curves over time of oils and fats obtained in Examples and Comparative Examples of the present invention. A...Example 1, B...Example 2, C...Example 3, D...Orange roughy oil subjected to only selective hydrogenation treatment, E... Macro whale oil only subjected to selective hydrogenation treatment , F...Olive oil that has only been subjected to column chromatographic circulation purification.

Claims (1)

【特許請求の範囲】[Claims] 1 高級アルコールと高級脂肪酸との不飽和エス
テル油であつて、前記高級アルコールと高級脂防
酸のうちどちらか一方又は両方の炭化水素部分に
は二重結合が2ケ以上含有されてなるとともに多
少の過酸化物をも含有されてなる不飽和エステル
油を原料油脂類とし、この原料油脂類を選択的水
素添加工程とカラムクロマトグラフ的精製工程と
の組合せで精製することにより得られ、精製直後
は勿論少なくとも精製後50±2℃で30日経過後も
過酸化物価を20以下に維持する化粧料用不飽和油
脂類であつてかつ不飽和結合2ケ以上のポリエン
脂肪酸又は/及びポリエン脂肪族アルコールの炭
化水素部分が選択的にモノエン体に変性され、か
つ多少含まれている過酸化物が還元されてなるこ
とを特徴とする化粧用不飽和油脂類。
1. An unsaturated ester oil of a higher alcohol and a higher fatty acid, which contains two or more double bonds in the hydrocarbon portion of either or both of the higher alcohol and the higher fatty acid-protecting acid, and has some It is obtained by using an unsaturated ester oil that also contains peroxides as a raw material oil and refining this raw material oil and fat by a combination of a selective hydrogenation step and a column chromatographic refining step, and immediately after purification. Of course, polyene fatty acids and/or polyene aliphatic alcohols are unsaturated oils and fats for cosmetics that maintain a peroxide value of 20 or less even after 30 days at 50±2°C after purification, and have two or more unsaturated bonds. 1. An unsaturated oil and fat for cosmetic use, characterized in that the hydrocarbon moiety of is selectively modified into a monoene form, and a certain amount of peroxide contained therein is reduced.
JP19401582A 1982-11-04 1982-11-04 Purification of oil and fat Granted JPS5984992A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP19401582A JPS5984992A (en) 1982-11-04 1982-11-04 Purification of oil and fat
EP83306586A EP0108571A3 (en) 1982-11-04 1983-10-28 Process for purification of unsaturated fatty oils

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19401582A JPS5984992A (en) 1982-11-04 1982-11-04 Purification of oil and fat

Publications (2)

Publication Number Publication Date
JPS5984992A JPS5984992A (en) 1984-05-16
JPH0420037B2 true JPH0420037B2 (en) 1992-03-31

Family

ID=16317529

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19401582A Granted JPS5984992A (en) 1982-11-04 1982-11-04 Purification of oil and fat

Country Status (2)

Country Link
EP (1) EP0108571A3 (en)
JP (1) JPS5984992A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4629588A (en) * 1984-12-07 1986-12-16 W. R. Grace & Co. Method for refining glyceride oils using amorphous silica
US4880574A (en) * 1984-12-07 1989-11-14 W. R. Grace & Co.-Conn. Method for refining glyceride oils using partially dried amorphous silica hydrogels
JPH0733350B2 (en) * 1985-12-07 1995-04-12 日清製油株式会社 Method for producing modified medium chain fatty acid triglyceride
GB8711431D0 (en) * 1987-05-14 1987-06-17 Unilever Plc Edible fats
JPH02196738A (en) * 1989-01-25 1990-08-03 Nobuhisa Shimizu Preparation of higher alcohol
US5053169A (en) * 1989-08-08 1991-10-01 W. R. Grace & Co.-Conn. Method for refining wax esters using amorphous silica
TR24766A (en) * 1989-10-16 1992-05-01 Procter & Gamble POLIOL POLYESTER SYNTHESIS.
CA2027418C (en) * 1989-10-16 1997-12-09 Robert Houston Polyol polyester synthesis
YU46273B (en) * 1989-11-20 1993-05-28 Do Helios Kemična Industrija Domžale OIL HYDROGENATION PROCEDURE
DE69225578T2 (en) * 1992-02-19 1998-09-10 Nestle Sa Process for decoloring fatty acid esters and food or cosmetic preparation containing them
US6280659B1 (en) * 1996-03-01 2001-08-28 David W. Sundin Vegetable seed oil insulating fluid
CN102936536B (en) 2002-04-29 2014-01-29 陶氏环球技术有限责任公司 Intergrated chemical processe for industrial utilization of seed oils
DE10302299A1 (en) * 2003-01-22 2004-07-29 Cognis Deutschland Gmbh & Co. Kg Deodorization of oils comprises treatment with a polymeric adsorbent in addition to distillation with steam or a carrier gas
JP5350265B2 (en) * 2007-10-12 2013-11-27 日本水産株式会社 Method for producing highly refined pearl millet oil
CA2715328A1 (en) * 2008-02-21 2009-08-27 Dow Global Technologies Inc. Separation of natural oil-derived aldehydes or hydroxy methyl esters using process chromatography
EP4302316A1 (en) * 2021-03-02 2024-01-10 Cargill, Incorporated Method for making bio-sourced oil dielectric fluids

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2589097A (en) * 1947-06-19 1952-03-11 Procter And Gamblc Company Retardation of development of reversion flavor in hydrogenated fats and oils

Also Published As

Publication number Publication date
EP0108571A3 (en) 1985-03-06
JPS5984992A (en) 1984-05-16
EP0108571A2 (en) 1984-05-16

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