JPS5931485B2 - Synthetic oil composition for cosmetics - Google Patents
Synthetic oil composition for cosmeticsInfo
- Publication number
- JPS5931485B2 JPS5931485B2 JP50067764A JP6776475A JPS5931485B2 JP S5931485 B2 JPS5931485 B2 JP S5931485B2 JP 50067764 A JP50067764 A JP 50067764A JP 6776475 A JP6776475 A JP 6776475A JP S5931485 B2 JPS5931485 B2 JP S5931485B2
- Authority
- JP
- Japan
- Prior art keywords
- molecular weight
- synthetic oil
- compound
- squalane
- hydrogenated
- 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
Links
Classifications
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q19/00—Preparations for care of the skin
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/30—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds
- A61K8/31—Hydrocarbons
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
- A61K8/81—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
- A61K8/8105—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- A61K8/8111—Homopolymers or copolymers of aliphatic olefines, e.g. polyethylene, polyisobutene; Compositions of derivatives of such polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08C—TREATMENT OR CHEMICAL MODIFICATION OF RUBBERS
- C08C19/00—Chemical modification of rubber
- C08C19/02—Hydrogenation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M107/00—Lubricating compositions characterised by the base-material being a macromolecular compound
- C10M107/02—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation
- C10M107/14—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation containing conjugated diene
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q1/00—Make-up preparations; Body powders; Preparations for removing make-up
- A61Q1/02—Preparations containing skin colorants, e.g. pigments
- A61Q1/04—Preparations containing skin colorants, e.g. pigments for lips
- A61Q1/06—Lipsticks
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/06—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing conjugated dienes
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/08—Resistance to extreme temperature
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/06—Instruments or other precision apparatus, e.g. damping fluids
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/12—Gas-turbines
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/12—Gas-turbines
- C10N2040/13—Aircraft turbines
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/16—Dielectric; Insulating oil or insulators
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/17—Electric or magnetic purposes for electric contacts
Landscapes
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Veterinary Medicine (AREA)
- Public Health (AREA)
- General Health & Medical Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- Organic Chemistry (AREA)
- Epidemiology (AREA)
- Birds (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Dermatology (AREA)
- Cosmetics (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Description
【発明の詳細な説明】
本発明は、有機金属化合物とニッケル化合物を主とする
触媒によりイソプレンを重合して得られる低分子量重合
体で、数平均分子量が150から3000までの鎖状重
合体を水素添加することにより得られる合成油を配合し
た化粧品用組成物である。Detailed Description of the Invention The present invention is a low molecular weight polymer obtained by polymerizing isoprene with a catalyst mainly consisting of an organometallic compound and a nickel compound, and is a chain polymer having a number average molecular weight of 150 to 3000. This is a cosmetic composition containing synthetic oil obtained by hydrogenation.
従来、化粧品に用いられてきた合成油としては、流動パ
ラフィン、グリセリン、ポリエチレングリコールなど多
くの種類が知られているが、鮫から得られるサメ油を精
製して得られるスクアレンは、人体の皮ふへの浸透吸収
性が合成品よりもすぐれており、またスクアレンが鮫か
ら得られるという点から、人体に対しても無害であるば
かりでなく、有益な化合物として知られている。There are many types of synthetic oils that have traditionally been used in cosmetics, including liquid paraffin, glycerin, and polyethylene glycol, but squalene, which is obtained by refining shark oil obtained from sharks, has been found to be useful for human skin. Because squalene has better permeability and absorption than synthetic products, and because squalene is obtained from sharks, it is known to be not only harmless to the human body but also a beneficial compound.
この化合物はイソプレン骨格を有しており、イソプレン
を1・4型重合して6量体となつており、2重結合も全
トランス構造であることが知られている。ところがスク
アレンのように2重結合が多く残つている油は、酸敗す
なわち空気による酸化が激しく、悪臭を発生したり、人
体に有害な物質にも変化する場合もあることが明らかと
なつてきた。そこで、スクアレンを水素添加して、完全
に不飽和度をゼロとしたスクアランが耐候性、皮ふへの
浸透性、無毒性ということでもすぐれていることが明ら
かとなつた。ところがスクアレンはサメから抽出するの
であるから、サメの魚獲量が減少してくると必然的に貴
重品となり、高価になつてきた。日本では魚獲量を制限
されており、これに代わる合成油を合成しようという試
みがなされてきた。これらのうち、日本特許公報昭49
−35984、公開特許公報昭49−85243、公開
特許公報昭49−117413、公開特許公報昭49−
−133302などに新しい合成法が記載されている。
ところがこれらの方法は次のような欠点があることが明
らかとなつた。特許公報昭49−35984の方法は、
イソプレンを固体酸触媒で加熱重合するために、イソプ
レンは1・4型重合をしないで、環化重合したり、3・
4型結合をしたり、1・2型結合をしたりするために、
側鎖にイソプロペニル基や、ビニル基や6員環基が結合
した構造をとるために、天然の直鎖状のテルペン類(ス
クアレン)を水素添加して得られる油よりも、同一分子
量では極めて粘度が高くなること、分子構造が異なつて
いるために、人体に対する皮ふ浸透性が不足しているこ
とが明らかとなつた。また、公開特許公報昭49−85
243は、イソブチレン、ブタジエン、ブテンー1など
を重合して得られた低重合体にさらに水素添加して合成
油を作るものであるが、この方法は炭素数4個のオレフ
イン、ジオレフインを重合したものであるために、分子
量が小さくても粘度が高くなり、流動特性がスクアラン
のそれにくらべて充分でなく、また分子構造、立体構造
が異なるために、人間の皮ふへの浸透性が不充分であつ
た。また公開特許公報昭49−11743、公開特許公
報昭49−133302には、ゲラニルアセトン、ヘキ
サヒドロプソイドイヨノンをカツプリングさせてさらに
脱水反応を行い、さらに水素添加することにより、スク
アランを合成する方法が記載されている。It is known that this compound has an isoprene skeleton, is formed into a hexamer by polymerizing isoprene in the 1-4 type, and the double bond is also an all-trans structure. However, it has become clear that oils like squalene, which have many residual double bonds, can become rancid, meaning they can be severely oxidized by air, producing a foul odor or turning into substances harmful to the human body. Therefore, it has become clear that squalane, which is made by hydrogenating squalene and has completely zero unsaturation, has excellent weather resistance, permeability into the skin, and non-toxicity. However, since squalene is extracted from sharks, as the amount of shark fish caught has decreased, it has inevitably become a valuable and expensive item. In Japan, the amount of fish caught is limited, and attempts have been made to synthesize synthetic oil to replace it. Among these, Japanese Patent Publication 1973
-35984, Published Patent Publication 1986-85243, Published Patent Publication 1974-117413, Published Patent Publication 1977-
-133302, etc., a new synthesis method is described.
However, it has become clear that these methods have the following drawbacks. The method of patent publication No. 49-35984 is as follows:
In order to heat-polymerize isoprene with a solid acid catalyst, isoprene is not subjected to 1.4-type polymerization, but instead undergoes cyclization polymerization or 3-type polymerization.
In order to make a type 4 bond or a type 1/2 bond,
Because it has a structure in which isopropenyl groups, vinyl groups, and 6-membered ring groups are bonded to the side chain, it is much more powerful than oil obtained by hydrogenating natural linear terpenes (squalene) at the same molecular weight. It became clear that skin permeability to the human body was insufficient due to the increased viscosity and different molecular structure. Also, published patent publication 1985-85
243 is a method in which synthetic oil is produced by further hydrogenating a low polymer obtained by polymerizing isobutylene, butadiene, butene-1, etc.; Therefore, even though its molecular weight is small, its viscosity is high, its fluidity is not as good as that of squalane, and its molecular structure and three-dimensional structure are different, so its permeability into human skin is insufficient. Ta. Furthermore, published patent publications 11743/1982 and 133302/1987 disclose a method for synthesizing squalane by coupling geranyl acetone and hexahydropseudoid ionone, further dehydration reaction, and further hydrogenation. is listed.
ところがこの方法はほぼ天然物から得られたスクアレン
を水素添加して得られるスクアランに近い流動特性を示
すが、出発原料であるゲラニルアセトンやヘキサヒドロ
プソイドイヨノンはそれ自体が高価であるために、これ
らをさらに2量化してカツプリングし、その上脱水反応
を行い、さらに水素添加しなければならないので、工程
が多く、各工程の収率が90%以下となるため価格が高
くなることが欠点であつた。ところが本発明方法による
と、イソプレンの単独重合で、しかも1・4型重合をす
るために、スクアレンと酷似の構造をとり、さらにこれ
を水素添加した後、減圧蒸留により分留することにより
、スクワランとほとんど同一構造の化合物を合成できる
。したがつて粘度特性、皮ふへの浸透性、無毒性、無刺
戟性も同一である。本発明に用いられるイソプレンの低
重合体で数平均分子量150〜3000の低重合体を得
る方法としては、例えば公開特許公報昭49一1151
89の方法があげられる。However, although this method exhibits flow characteristics similar to squalane obtained by hydrogenating squalene obtained from natural products, the starting materials geranylacetone and hexahydropsoidionone are themselves expensive. , these must be further dimerized and coupled, then subjected to dehydration reaction, and then hydrogenated, so there are many steps, and the yield in each step is less than 90%, resulting in a high price. It was hot. However, according to the method of the present invention, in order to homopolymerize isoprene and perform 1.4-type polymerization, it has a structure very similar to squalene, which is further hydrogenated, and then fractionated by vacuum distillation to produce squalane. Compounds with almost the same structure as can be synthesized. Therefore, the viscosity characteristics, skin permeability, non-toxicity, and non-irritating properties are also the same. As a method for obtaining a low polymer of isoprene used in the present invention with a number average molecular weight of 150 to 3000, for example, published patent publication No. 49-11151
There are 89 methods.
この方法は、α−オレフインの存在下に有機金属化合物
とニツケル化合物系触媒あるいは前記の触媒系にさらに
電子供与化合物を加えた触媒で、イソプレンを重合させ
ることにより得られる。分子量の調節は、d−オレフイ
ンの量、有機金属化合物、ニツケル化合物、電子供与化
合物の量を調節することにより容易に制御できる。次に
このようにして得られた重合体は、重合触媒をメタノー
ル、エタノール、プロパノール、n−アミルアルコール
、水などで失活させ、触媒を塩酸、硫酸、硝酸などの酸
性水溶液あるいは蟻酸、酢酸、蓚酸などの有機酸の水溶
液と混合して除去する。さらにアルカリ水溶液ノで中和
して、水洗後重合に用いた溶液を減圧除去して液状重合
体を得る。In this method, isoprene is polymerized in the presence of an .alpha.-olefin using an organometallic compound and a nickel compound catalyst, or a catalyst prepared by adding an electron donating compound to the above catalyst system. The molecular weight can be easily controlled by adjusting the amount of d-olefin, organometallic compound, nickel compound, and electron donating compound. Next, the polymer thus obtained is prepared by deactivating the polymerization catalyst with methanol, ethanol, propanol, n-amyl alcohol, water, etc., and removing the catalyst with an acidic aqueous solution such as hydrochloric acid, sulfuric acid, or nitric acid, or with formic acid, acetic acid, or the like. Remove by mixing with an aqueous solution of an organic acid such as oxalic acid. Further, the polymer is neutralized with an alkaline aqueous solution, washed with water, and the solution used for polymerization is removed under reduced pressure to obtain a liquid polymer.
このようにして得られた液状重合体を水素添加するには
、通常メタノール、エタノールなどのアルコール類、ア
セトン、メチルエチルケトンなどのケトン類、ヘプタン
、ヘキサン、ペンタン、シクロヘキサンなどの脂肪族炭
化水素溶媒などの溶媒あるいは混合溶媒に溶解させるか
あるいは無溶媒でも行いうる。To hydrogenate the liquid polymer obtained in this way, alcohols such as methanol and ethanol, ketones such as acetone and methyl ethyl ketone, and aliphatic hydrocarbon solvents such as heptane, hexane, pentane, and cyclohexane are usually used. It can be carried out by dissolving it in a solvent or a mixed solvent, or without a solvent.
水素添加を行うための触媒としては、ラネーニツケル、
け(・そう土ニツケル、うるし原ニツケルなどのニツケ
ル触媒あるいはパラジウム、白金などの通常用いられる
触媒である。水素圧力は5〜300k9/(−1i、温
度50〜350゜C、1〜100時間混合しながら水素
添加反応を行う。反応終了後、常法により反応液から触
媒と溶媒を除去する。次に水素添加された液状重合体を
分子蒸留法により減圧蒸留する。このようにして粘度の
低い初留分、粘度の適当な中留分、粘度の高い残留分が
得られるが、これらは各留分に応じて乳液、クリーム、
チツク、ポマードなどの化粧品に用いられる。前述の特
公昭49−35984号公報および特開昭49−852
43号公報に記載された方法で得られる液状ポリマーを
水素添加し合成飽和油としたものを原料に用い、後述の
実施例1に記載された配合処方でコールドクリームを調
製し、本発明品と比べると、クリームののび、こし、ハ
ダざわりなどのいわゆる官能特性が劣る。また、特開昭
49−117413号公報および特開昭49−1333
02号公報によつて得られる合成油は、天然のスクアレ
ンを水素添加して得られるアクアランに近い構造を有す
るため、そのクリーム配合物も天然からのスクアラン配
合クリームと同等の性能を示す。後述の実施例1に示す
ように、これは本発明品の性能と同等である。本発明の
意義は、単純、安価な原料および工程を経て得られる合
成油を使つて、上記公知例の複雑で高価な原料および工
程を経て得られる合成油と同等の性能を有する配合物を
提供できたことにある。次に本発明の具体的な実施例を
示すが、以下の具体例に限定されるものではない。実施
例 1
撹拌棒の装着してある1.5.eのステンレス製オート
クレーブ(耐圧20k9/0d)を窒素置換し、窒素気
流下で無水のトルエン300m11脱水して蒸留した無
水のイソプレン1367を加え、一5『Cに冷却し、0
.1m01/lのナフテン酸ニツケルのトルエン溶液4
m111m01/lのエチルアルミニウムセスキクロラ
イドのトルエン溶液4m1、0.02m01/lのトリ
フエニルホスフインのトルエン溶液4m11プロピレン
647を加え、60′Cで6時間重合する。Catalysts for hydrogenation include Raney nickel,
A nickel catalyst such as nickel on soil or nickel on lacquer, or a commonly used catalyst such as palladium or platinum. After the reaction, the catalyst and solvent are removed from the reaction solution using a conventional method.Then, the hydrogenated liquid polymer is distilled under reduced pressure using the molecular distillation method. A distillate, a middle distillate with an appropriate viscosity, and a residual fraction with a high viscosity can be obtained, and these can be used as emulsions, creams, etc. depending on each fraction.
Used in cosmetics such as ticks and pomades. The aforementioned Japanese Patent Publication No. 49-35984 and Japanese Patent Application Laid-Open No. 49-852
Using the liquid polymer obtained by the method described in Publication No. 43 as a synthetic saturated oil by hydrogenating it as a raw material, a cold cream was prepared according to the formulation described in Example 1 below, and the product of the present invention and the product of the present invention were prepared. In comparison, the so-called sensory characteristics such as the cream's spreadability, texture, and texture are inferior. Also, JP-A-49-117413 and JP-A-49-1333
Since the synthetic oil obtained in Publication No. 02 has a structure similar to that of aqualane obtained by hydrogenating natural squalene, its cream formulation also exhibits the same performance as a cream containing natural squalane. As shown in Example 1 below, this is equivalent to the performance of the product of the present invention. The significance of the present invention is to provide a compound that uses synthetic oil obtained through simple and inexpensive raw materials and processes and has the same performance as the synthetic oil obtained through complex and expensive raw materials and processes as described above. It's because I was able to do it. Next, specific examples of the present invention will be shown, but the present invention is not limited to the following specific examples. Example 1 1.5. equipped with a stirring bar. A stainless steel autoclave (withstand pressure 20k9/0d) was purged with nitrogen, and 300ml of anhydrous toluene was added with 11 dehydrated and distilled anhydrous isoprene 1367 under a nitrogen stream, cooled to -5°C, and heated to 0.
.. 1m01/l toluene solution of nickel naphthenate 4
4 ml of a toluene solution of ethylaluminum sesquichloride (m111 m01/l), 4 ml of a toluene solution of triphenylphosphine (0.02 m01/l), and 4 ml of propylene 647 are added and polymerized at 60'C for 6 hours.
重合停止はイソプロピルアルコールのトルエン溶液(1
0%溶液)を加圧で10m1加え10分間かくはんし、
その後ドラフト内で未反応プロピレン、ブタジエンをパ
ージする。次にPHl.6の塩酸水溶液800m1と上
記の重合液を21のガラスフラスコ中で、5時間洗浄し
、静置後水層を分離し、PH−12のカセイソーダ水溶
液800m1と油層とを1時間混合し、静置後水層を分
離し、油層をさらにイオン交換処理した水800m1と
1時間光分混合した後、静置して水層を分離する。油層
をロータリーエバポレーターで減圧濃縮する。このよう
にして無色透明な低粘度の液体103yを得た。To terminate the polymerization, use a toluene solution of isopropyl alcohol (1
Add 10ml of 0% solution) under pressure and stir for 10 minutes.
After that, unreacted propylene and butadiene are purged in the fume hood. Next, PHL. 800 ml of hydrochloric acid aqueous solution of PH-12 and the above polymerization solution were washed in a glass flask of No. 21 for 5 hours, and after standing still, the aqueous layer was separated, and 800 ml of caustic soda aqueous solution of PH-12 and the oil layer were mixed for 1 hour, and left standing. After separating the aqueous layer, the oil layer was optically mixed with 800 ml of ion-exchanged water for 1 hour, and then left to stand to separate the aqueous layer. The oil layer is concentrated under reduced pressure using a rotary evaporator. In this way, a colorless and transparent low viscosity liquid 103y was obtained.
粘度は30℃で24センチポイズであつた。蒸気圧滲透
計で分子量を測定したところ、数平均分子量が410で
あつた。この液状ポリイソプレンの水素添加を次のよう
に行つた。The viscosity was 24 centipoise at 30°C. When the molecular weight was measured using a vapor pressure permeability meter, the number average molecular weight was 410. This liquid polyisoprene was hydrogenated as follows.
日興理化学産業(株)製のラネーニツケルR−200の
活性化物を脱気、脱水して窒素中に保存して、シユレン
ク管にいれる。An activated product of Raney Nickel R-200 manufactured by Nikko Rikagaku Sangyo Co., Ltd. is degassed, dehydrated, stored in nitrogen, and placed in a Schlenk tube.
このうちラネーニツケルR−20057と上記の液状ポ
リイソプレン75m11シクロヘキサン75m1を20
0m1のステンレス製オートクレーブ中に加え、水素ボ
ンベから水素を導入して、25kg/C7?Lのゲージ
圧になるまで加える。オイルバスを用いて150℃まで
加熱して混合する。圧力25k9/?に保持して、15
0′C、30時間混合を続けて、水素添加を終了し冷却
後、常圧にしてから遠心分離器で触媒を除去して、無色
透明な液体を得た。溶媒除去をするためにロータリーエ
バポレーターで減圧濃縮して無色透明な液体74m1を
得た。粘度は30℃で35センチポイズであつた。この
ようにして水素添加した液状ポリイソプレンは、N阪赤
外スベクトルともに、スクワランとほとんど同一のチヤ
ートを示した。狸チヤートを比較するとスクワランのメ
チル基のプロトンのシグナルの面積/全プロトンのシグ
ナルの面積−0.39であるが、本発明方法による液状
ポリイソプレンの水素添加物のメチル基のプロトン/全
プロトン=0.40となり、本発明方法により得られる
液状ポリイソプレンが1・4結合型であるために、水素
添加物もスクワランとほとんど同一の構造をもつている
ことが明らかとなつた。さらにこの水素添加物を分子蒸
留装置を用いて分留した。Of these, 20 ml of Raney Nickel R-20057, 75 ml of the above liquid polyisoprene, and 75 ml of cyclohexane were added.
Add it to a 0ml stainless steel autoclave and introduce hydrogen from a hydrogen cylinder to 25kg/C7? Add until gauge pressure of L is reached. Mix by heating to 150°C using an oil bath. Pressure 25k9/? hold at 15
Mixing was continued at 0'C for 30 hours to complete hydrogenation and after cooling, the mixture was brought to normal pressure and the catalyst was removed using a centrifugal separator to obtain a colorless and transparent liquid. To remove the solvent, the mixture was concentrated under reduced pressure using a rotary evaporator to obtain 74 ml of a colorless and transparent liquid. The viscosity was 35 centipoise at 30°C. The liquid polyisoprene hydrogenated in this manner showed almost the same chart as squalane in both the Nosaka infrared spectrum. When compared with Raccoon Chart, the signal area of the proton of the methyl group of squalane/the area of the signal of the total proton - 0.39, but the proton of the methyl group of the hydrogenated liquid polyisoprene by the method of the present invention/total proton = 0.40, and it became clear that since the liquid polyisoprene obtained by the method of the present invention is of the 1,4-bond type, the hydrogenated material also has almost the same structure as squalane. Furthermore, this hydrogenated product was fractionally distilled using a molecular distillation apparatus.
107のサンプルを分留したところ、1mmHgで12
0℃以下の沸点の第1留分は3.57であり、1mmH
gの減圧度で140℃から0.2m77!Hgl25O
℃の沸点の第2留分は3.27であり、残りは3.37
であつた。When 107 samples were fractionated, 12
The first fraction with a boiling point below 0°C is 3.57 and 1 mmH
0.2m77 from 140℃ at a vacuum degree of g! Hgl25O
The second fraction of boiling point in °C is 3.27 and the remainder is 3.37
It was hot.
第2留分についての物性をスクワランと比較して表1に
示す。The physical properties of the second fraction are shown in Table 1 in comparison with squalane.
表1に記載された本発明に用いられるポリイソプレンの
水素添加物を次のように配合してコールドクリームを調
製した。A cold cream was prepared by blending the hydrogenated polyisoprene used in the present invention shown in Table 1 as follows.
この配合組成のうち、本発明ポリイソプレン水素添加物
をスクアランにおきかえたものと同一の色、臭い、長期
安定性、無刺戟性、のび、こし、ハダざわりを示した。Of this composition, it exhibited the same color, odor, long-term stability, non-irritability, spreadability, stiffness, and texture as the one in which the polyisoprene hydrogenated product of the present invention was replaced with squalane.
実施例 2
実施例1と同一の本発明ポリイソプレンの水素添加物を
配合して口紅を試作した。Example 2 A lipstick was prepared as a prototype by blending the same hydrogenated polyisoprene of the present invention as in Example 1.
この配合のうち、本発明のポリイソプレンの水素添加物
をスクアランに置き換えた口紅と同等のつやのある、の
びのよい口紅が得られた。Of this formulation, a lipstick with a gloss and good spreadability was obtained, which was equivalent to the lipstick of the present invention in which the hydrogenated polyisoprene was replaced with squalane.
実施例 3
実施例1のポリイソプレンの水素添加物を次のように配
合してハイジエニツククリームを試作した。Example 3 The hydrogenated polyisoprene obtained in Example 1 was blended as follows to prepare a Hygiene cream.
この配合のうち、ポリイソプレンの水素添加物をスクア
ランに置き換えた場合と同一ののび、なめらかさを持つ
ていた。This formulation had the same spreadability and smoothness as when the hydrogenated polyisoprene was replaced with squalane.
Claims (1)
ル化合物、有機アルミニウム化合物および電子供与化合
物からなる触媒により、イソプレンを重合して得られる
低分子量重合体で、数平均分子量が150から3000
までの鎖状重合体を水素添加することにより得られる完
全飽和合成油を配合した化粧品用組成物。1 A low molecular weight polymer obtained by polymerizing isoprene with a catalyst consisting of a nickel compound, an organoaluminium compound, and an electron donating compound, using an α-olefin as a molecular weight regulator, and having a number average molecular weight of 150 to 3000.
A cosmetic composition containing fully saturated synthetic oil obtained by hydrogenating chain polymers.
Priority Applications (8)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50067764A JPS5931485B2 (en) | 1975-06-04 | 1975-06-04 | Synthetic oil composition for cosmetics |
| CA253,053A CA1051464A (en) | 1975-05-26 | 1976-05-21 | Synthetic saturated oils, and their production and use |
| GB21341/76A GB1535849A (en) | 1975-05-26 | 1976-05-24 | Synthetic saturated oils and their production and use |
| IT68286/76A IT1062235B (en) | 1975-05-26 | 1976-05-25 | SATURATED SYNTHETIC OILS..PARTICULARLY USEFUL AS LUBRICANTS AND FOR COSMETIC PRODUCTS AND PROCEDURE FOR THEIR PREPARATION |
| US05/689,689 US4060492A (en) | 1975-05-26 | 1976-05-25 | Synthetic saturated oils, and their production and use |
| FR7615799A FR2312556A1 (en) | 1975-05-26 | 1976-05-25 | PROCESS FOR THE PRODUCTION OF SYNTHETIC SATURATED OILS BY HYDROGENATION OF POLYISOPRENE AT LOW MOLECULAR WEIGHT AND NEW PRODUCTS THUS OBTAINED |
| DE2623718A DE2623718C3 (en) | 1975-05-26 | 1976-05-26 | Hydrogenated low molecular weight polyisoprene oils, processes for their production and their use |
| US05/841,669 US4122023A (en) | 1975-05-26 | 1977-10-13 | Synthetic saturated oils, and their production and use |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50067764A JPS5931485B2 (en) | 1975-06-04 | 1975-06-04 | Synthetic oil composition for cosmetics |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS51144740A JPS51144740A (en) | 1976-12-13 |
| JPS5931485B2 true JPS5931485B2 (en) | 1984-08-02 |
Family
ID=13354318
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50067764A Expired JPS5931485B2 (en) | 1975-05-26 | 1975-06-04 | Synthetic oil composition for cosmetics |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5931485B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02107386A (en) * | 1988-10-17 | 1990-04-19 | Shin Nippon Bifuu Kk | Gas-discharging duct and its scavenger |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2715306B1 (en) * | 1994-01-25 | 1996-03-15 | Oreal | Cosmetic or dermopharmaceutical composition in the form of a flexible paste and process for the preparation of said composition. |
| JP3020882U (en) * | 1995-07-24 | 1996-02-06 | 東興産業株式会社 | Ground drilling equipment |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4935984A (en) * | 1972-08-08 | 1974-04-03 |
-
1975
- 1975-06-04 JP JP50067764A patent/JPS5931485B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02107386A (en) * | 1988-10-17 | 1990-04-19 | Shin Nippon Bifuu Kk | Gas-discharging duct and its scavenger |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS51144740A (en) | 1976-12-13 |
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