KR810000104B1 - Method for preparing pure squalan from shark-liver oil - Google Patents

Method for preparing pure squalan from shark-liver oil Download PDF

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KR810000104B1
KR810000104B1 KR7802529A KR780002529A KR810000104B1 KR 810000104 B1 KR810000104 B1 KR 810000104B1 KR 7802529 A KR7802529 A KR 7802529A KR 780002529 A KR780002529 A KR 780002529A KR 810000104 B1 KR810000104 B1 KR 810000104B1
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squalene
shark
liver oil
squalane
squaraine
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KR7802529A
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이장열
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이장열
김성준
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    • 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
    • C11C3/02Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fatty acids with glycerol

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  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
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  • Oil, Petroleum & Natural Gas (AREA)
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  • Organic Chemistry (AREA)
  • Fats And Perfumes (AREA)

Abstract

Squalane was prepared from squalene in a way as follows: squalene prepared from the liver oil of shark by deoxidation, decoloration and fractionary vacuum distillation was treated with alkali and water washing treatment to removes impurities and was put into autoclave attached on agitator with a porous rotor. Mixed catalyst(Ni and active carbon 1:1) of about 1.0% by weight of above squalene was added to it. After adding H for 5 hrs., obtained squalane was treated with metal Na and then was purified by fractionary vacuum distillation and deodorization.

Description

상어 간유에서 고순도 스쿠아란의 제조방법Method for producing high purity squalane from shark liver oil

본원의 발명은 심해 상어간유에서 응고점이 -60℃이고 윤활성이 우수하여 정밀기계의 고급윤활제로 사용할 수 있고 피부에의 삼투력이 좋고 피하조직을 자극하지 아니하면서 활성을 주어 피부미용에도 효과가 있어 화장품의 기초원료로서 좋은 효과를 가진 고순도 스쿠아란의 제법에 관한 것이다.The present invention has a coagulation point of -60 ℃ in deep sea shark liver oil and excellent lubricity, so it can be used as an advanced lubricant of precision machinery. It has good osmotic power to the skin and gives activity without irritating the subcutaneous tissue. The present invention relates to a high-purity squalane preparation having a good effect as a basic raw material for cosmetics.

심해(200-1,000m)에서 잡히는 상어간유에는 약 15-80%의 스쿠아렌이 함유되어 있는데 우리나라 근해에서 잡히는 물치상어 간유에는 약 20-30%의 스쿠아렌이 함유되어 있다.Shark liver oil caught in the deep sea (200-1,000m) contains about 15-80% of squaraine, while shark liver oil caught near Korea contains about 20-30% of squaraine.

스쿠아렌은 분자식이 C30H50으로서 그 분자내에는 6개의 이중결합을 가지고 있는 테레핀류에 속하는 화합물로서 그 옥소가가 372인데 스쿠아렌을 수소 첨가하여 그 이중결합을 없앤것이 스쿠아란인데 그 스쿠아란은 응고점이 -60℃이고 윤활성이 좋으며 그 점과 저온에서도 그다지 변화하지 아니하여 정밀기계의 윤활유로서도 극히 적합하고 또한 피부에의 삼투력이 강하며 피하조직을 자극하지 아니하면서 활성을 주어 피부미용에도 효과가 있어 화장품의 기초원료로서의 우수한 성질을 가지고 있다.Squalene is a molecular formula of C 30 H 50 , a compound belonging to terepins with six double bonds in its molecule, and its oxo number is 372. Aran has a solidification point of -60 ℃ and has good lubricity and does not change very much at low temperatures and low temperatures. It is extremely suitable as a lubricant for precision machinery. It also has an excellent effect as a basic raw material of cosmetics.

종래에도 심해간유에서 스쿠아란을 제조하는 방법이 알려져 있는데 그와같은 방법은 불순물이 상당량 함유된 스쿠아렌의 이중결합을 어느정도 수소첨가에 의하여 없앤 것으로서 상당량의 불순물과 스쿠아란 아닌 스쿠아렌 유도체도 함유되어 있어 윤활유로서는 어느정도 적합하나 기초화장품의 원료로서 사용하기 곤란한 것이였는데 그 제조방법을 기술하면 다음과 같다.Conventionally, a method of producing squaraine from deep sea liver oil is known. Such a method removes a double bond of squaraine containing a considerable amount of impurities by hydrogenation, and also contains a large amount of impurities and a non-squalane squaraine derivative. Although it is somewhat suitable as a lubricating oil, it was difficult to use as a raw material for basic cosmetics.

1) 일본특허공보 공고번호 소26-3275호의 고순도 스쿠아란의 제조법으로서 그 방법은 원료인 흑자상어간유를 0.1-0.5mm/Hg의 감압하에 증류하여 230-235℃의 유출물을 모아 수소 첨가한 후 상법에 의하여 가성소다를 넣어 충분히 검화한 후 수세 탈수하여 얻은것을 재증류하고 다음 농황산을 약 5% 첨가하고 약 3시간 교반하여 충분히 반응시킨 다음 방냉후 분리하고 다시 5%의 백토를 가하고 약 115℃에 가열 교반후 여과후 알미나 및 시리카겔을 충진한 여과층을 통하여 -20℃에서 감압여과하는 공정의 결합으로서 된 것을 특징으로 하는 고순도 스쿠아란의 제법이며,1) A method of preparing high-purity squaraine from Japanese Patent Publication No. 26-3275, the method comprising distilling black fish shark oil as a raw material under reduced pressure of 0.1-0.5 mm / Hg to collect effluent at 230-235 ° C. and hydrogenating it. After adding caustic soda by the conventional method, saponification sufficiently, and distilled what was obtained by washing with water and dehydrating. Then, about 5% of concentrated sulfuric acid was added and stirred for about 3 hours to fully react. After cooling, the mixture was separated and 5% of clay was added. It is a manufacturing method of high purity squalane characterized by combining the process of filtration under reduced pressure at -20 ° C through a filtration layer filled with alumina and silica gel after filtration after heating and stirring at ° C.

2) 일본특허공보 공고번호 소 26-4125호의 스쿠아렌 농주유의 제법으로서 그 방법은 흑자상어간유를 분별증류하여 얻은 스쿠아렌에 니켈촉매를 가하고 수소압력 50㎏/㎠, 온도 156℃에서 수소 첨가하여 옥소가 98.7의 생성물을 얻고 그 생성물 100부에 빙초산 30%의 과산화수소 30부를 가하고 100℃에서 약 8시간 교반하면서 가열 반응시킨다음 과인의 초산을 제거하고 탄산소다 용액과 가열후 수세하여 제품을 얻은다음 그 생성물을 냉각하여 석출물을 가급적 제거하여 만든 스쿠아렌으로 부터의 농주유의 제법에 관한 발명임을 양공보의 기재에 의하여 알 수 있다.2) A method of preparing squaraine oil of Japanese Patent Publication No. 26-4125, which is a method of producing squaraine oil obtained by fractional distillation of surplus shark oil, adding a nickel catalyst and hydrogenating at a hydrogen pressure of 50 kg / cm 2 and a temperature of 156 ° C. Oxo obtains 98.7 of the product, adds 30 parts of hydrogen peroxide of 30% glacial acetic acid to the product, heats and reacts with stirring at 100 ° C. for about 8 hours, removes acetic acid of acetic acid, washes with sodium carbonate solution, and washes with water to obtain a product. It can be seen from the description of both publications that the invention relates to a process for producing a liquor oil from squalene produced by cooling the product to remove precipitates as much as possible.

그런데 전기한 바와같은 각 스쿠아란의 제조법은 스쿠아란의 응고점이 -60℃인데 그 최종제품이 -20-30℃에서 석출물이 생긴다는 기재와 그 외의 상세한 설명기제로 보아 그와같이 만들어진 스쿠아란은 불순물이 많이 함유되어 있음을 알 수 있다.However, as described above, the manufacturing method of each squaraine has a freezing point of -60 ℃ and the final product has a precipitate at -20-30 ℃. It can be seen that many impurities are contained.

그러므로 그와같이 만들어진 스쿠아란은 정밀기계류의 윤활유로서는 어느정도 가치가 있으나 극히 추운 지방에서 사용하는 윤활유로서는 적합하지 아니하고 또한 불순물이 많이 함유되어 있어 피하에 삼투되었을때 그 부작용이 생길 수 있으므로 화장품의 기초원료로서 적합하지 못하다.Therefore, Squalane made as such has some value as a lubricating oil of precision machinery, but it is not suitable as a lubricating oil used in extremely cold fats and contains a lot of impurities, so it can cause side effects when osmotically subcutaneous. Not suitable as

본 발명자는 극한 지방에서도 정밀기계류 윤활유로 사용할 수 있고 또한 화장품의 기초원료로서 사용할 수 있는 스쿠아란을 물치상어와 같이 스쿠아렌 함량이 낮은 간유로부터 제조하기 위하여 많은 연구를 실시한 결과 본 발명을 완성하였는데 그 상세한 내용을 기술하면 다음과 같다.The inventors of the present invention have completed the present invention as a result of many studies to prepare squaraine, which can be used as a precision machinery lubricant even in extreme regions and as a basic raw material of cosmetics, from cod liver oil with a low content of squalene, such as fish shark. The details are as follows.

일반적으로 유기화합물의 이중결합부에 수소첨가를 할때는 촉매로서 니켈촉매를 사용하고 고압하에서 수소첨가를 하는 방법이 사용되는데 앞에 기재한 바와같이 스쿠아렌에 니켈촉매를 가하고 수소압력을 50기압의 높은 압력에서 150℃로 가열하여 수소첨가하여도 그 생성물의 옥소가가 98.7인 것으로 보아 전기한 생성물중에는 다른 불순물도 많음을 알 수 있는데 출원인은 니켈촉매에 같은 량의 활성탄소 미분말을 혼합하면 그 촉매의 활성도가 극히 제고되고 또한 스쿠아렌을 고압 수소하에서 수소 첨가시킴에 있어서 교반기의 회전익에 다수의 구멍이 설하면 그 수소 첨가반응이 잘 진행됨을 발견하여 본 발명을 완성하였는데 그 제조방법을 기술하면 다음과 같다.In general, when hydrogenating a double bond of an organic compound, a nickel catalyst is used as a catalyst and hydrogenation is performed under high pressure. As described above, a nickel catalyst is added to squalene and a hydrogen pressure is applied at a high pressure of 50 atm. When the product is heated to 150 ° C and hydrogenated at, the product has an oxo number of 98.7, which indicates that the above-mentioned product contains many other impurities. Applicants can mix the same amount of fine powder of activated carbon with a nickel catalyst to activate the catalyst. In the hydrogen addition of squalene under high pressure hydrogen, the hydrogenation reaction was found to proceed well when a large number of holes were installed in the rotor blades of the stirrer, and the present invention was described. .

[실시예]EXAMPLE

[제1공정][Step 1]

원료 간유를 공지의 방법에 의하여 탈산 탈색처리후 분별 증류관에 넣고 공지의 방법으로 진공 증류하되 진공도 2mm/Hg에서 50-200℃에서 유출되는 초류분(주로 프리스탄 및 고급알콜류)을 따로 포집하고 200-250℃류분의 조제 스쿠아렌을 얻고 다음 전기조제 스쿠아렌을 공지의 알카리처리 및 수세를 하여 유리지방산등의 불순물을 제거한다. 류출잔유물은 주로 중성유 및 납류이다.After deoxidation and decolorization of the raw liver oil by a known method, it is put in a fractional distillation tube and vacuum distilled by a known method, and supernatants (mainly pristane and higher alcohols) flowing out at 50-200 ° C. at a vacuum degree of 2 mm / Hg are separately collected. Prepared squalene for 200-250 ° C. flow is obtained, and the following electrically prepared squalene is subjected to a known alkali treatment and washed with water to remove impurities such as free fatty acids. The resids are mainly neutral oils and lead streams.

[제2공정][Step 2]

전기조제 스쿠아렌을 회전익이 달린 교반기가 부설된 특수 오토크레브에 넣고 조제스쿠아렌의 약 1%중량의 활성탄소와 니켈촉매를 동량혼합 특수촉매를 가한다음 가열하여 온도 180-220℃에서 수소압력 30-40㎏/㎠에서 5시간 수소 첨가후 촉매를 분리하여 스쿠아란을 얻는다.Put the electric preparation squalene in a special autoclave equipped with a rotor blade and add a similar amount of activated carbon and nickel catalyst of about 1% of crude squalene to the hydrogen pressure at 180-220 ℃. After hydrogenation at 30-40 kg / cm 2 for 5 hours, the catalyst is separated to obtain squaran.

[제3공정][Step 3]

전기스쿠아란을 교반기가 부설된 반응조에 넣고 약 1%중량의 금속나트륨을 가한다음 140-150℃에서 약 3시간 가열 교반하여 반응을 진행시킨다(이때 스쿠아란에 함유된 소량의 고급알콜과 지방산이 금속나트륨과 결합하여 알코라드 및 지방산소다가 형성된다).The electrosquarane is placed in a reactor equipped with a stirrer, and about 1% by weight of sodium metal is added, followed by heating and stirring at 140-150 ° C. for about 3 hours (at this time, a small amount of higher alcohol and fatty acid Combined with sodium metal to form alkalade and fatty acid soda).

다음 냉각후 전기한 스쿠아란을 진공분별 증류관에 넣고 진공도 2mm/Hg에서 류출온도 200-240℃의 류분을 포집하여 정제스쿠아란을 얻는다. 이때 각 류출온도의 류출분 및 잔류분의 량은 대략 다음과 같다.Next, after cooling, the above-mentioned squalane is put in a vacuum fractional distillation tube, and the purified fraction of squalene is collected by collecting a stream having a flow rate of 200-240 ° C. at a vacuum degree of 2 mm / Hg. At this time, the flow rate and the residual amount of each flow temperature is as follows.

초류분 200℃이하 10-15%Initial flow rate 200 ℃ or less 10-15%

다음 류출분 200-240℃ 70-80%(정제 스쿠아란)Next flow rate 200-240 ° C 70-80% (purified squalane)

잔류분 10-15%Residue 10-15%

다음 상기 정제스쿠아란을 탈취관에 넣고 진공도 약 2mm/Hg 온도 150-170℃로 가열하면서 1-2시간 수증기를 통하는 공지의 탈취조작을 실시하여 본 발명의 고순도 스쿠아란을 제조하는데 그 제품의 옥소가는 불과 1이하이다.Next, the purified squaraine is put in a deodorization tube and subjected to a known deodorization operation through steam for 1-2 hours while heating at a vacuum degree of about 2 mm / Hg temperature of 150-170 ° C. to produce high purity squalane of the present invention. It is less than 1 to go.

상기 제1공정에서 얻어진 조제스쿠아렌은 그 주성분이 스쿠아렌이고 소량의 지방산 고급알콜류 프리스탄이 함유되어 있고 미량의 중성유 및 유취물이 함유되어 있으나 그 다음의 공정에서 별로 지장을 주지 아니한다.The crude squalene obtained in the first step is mainly composed of squalene, a small amount of fatty acid higher alcohol pristane, and a small amount of neutral oils and odorants, but it does not interfere in the subsequent step.

제3공정, 제2공정에서 얻어진 스쿠아란을 금속 처리하는 것은 그 스쿠아란중에 소량으로 함유된 유리지방산 및 미량의 중성유를 지방산염으로 하고 또한 소량의 알콜을 알코라드로 하여 다음의 진공 분별중시에 이를 완전 제거시키기 위함이다.Metal treatment of squalene obtained in the third and second steps is carried out by vacuum fractionation with the use of a small amount of free fatty acid and trace neutral oil contained in the squalane as fatty acid salt and a small amount of alcohol as alcorad. This is to completely remove it.

본원의 발명은 이상에 기술한 바와같이 종래의 스쿠아란 제법보다 그 수소첨가 압력이 낮으면서 수소첨가율을 높일 수 있어 그 제조방법이 용이하면서 종래에 알려진 스쿠아란의 제조방법보다 순도가 높은 스쿠아란을 제조할 수 있어 그 제품은 극히 추운지방(-60℃되어야 응고되므로)에서도 정밀기계류의 윤활유로 사용할 수 있고 또한 화장품 기초원료로서 안심하고 사용할 수 있는 스쿠아란의 제법에 관한 것이다.As described above, the present invention can increase the hydrogenation rate while the hydrogenation pressure is lower than that of the conventional squaraine production method, and thus the production method is easy and the purity of the squaraine obtained is higher than that of the conventionally known squaraine production method. It can be manufactured, and the product relates to the manufacturing method of Squalane, which can be used as a lubricant for precision machinery even in extremely cold fats (because it should be solidified at -60 ℃) and can be used with confidence as a cosmetic raw material.

Claims (1)

본문에 상술한 바와같이 물치상어 간유를 탈산, 탈색처리와 분별 진공증류를 실시하여 얻는 조제스쿠아렌을 알카리, 수세 처리하는 공지의 공정과 다공 회전익이 달린 교반기가 부설된 오토그레브에 스쿠아렌에 약 1.0%의 니켈촉매와 활성탄소 동량혼합 촉매를 가하고 통상의 방법에 의하여 약 5시간 수소첨가하여 얻은 스쿠아란을 금속나트륨 처리하고 공지의 진공 분별증류의 탈취처리하는 공정의 결합을 특징으로 하는 스쿠아란의 제법.As described above, the known process of alkali-washing and washing the crude squalene obtained by deoxidizing, decolorizing, and fractional vacuum distillation of the molten shark liver oil is carried out on the square on an autogreb equipped with a stirrer with a porous rotor blade. Squeeze characterized by combining the process of adding sodium catalyst with about 1.0% of nickel and a catalyst for the same amount of activated carbon, and hydrogenating the squalane obtained by hydrogenation by a conventional method for about 5 hours, followed by deodorization of a known vacuum fractional distillation. Aran's recipe.
KR7802529A 1978-08-19 1978-08-19 Method for preparing pure squalan from shark-liver oil KR810000104B1 (en)

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