WO2021132764A1 - Method for separating and purifying fucoxanthin from diatoms - Google Patents
Method for separating and purifying fucoxanthin from diatoms Download PDFInfo
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- WO2021132764A1 WO2021132764A1 PCT/KR2019/018529 KR2019018529W WO2021132764A1 WO 2021132764 A1 WO2021132764 A1 WO 2021132764A1 KR 2019018529 W KR2019018529 W KR 2019018529W WO 2021132764 A1 WO2021132764 A1 WO 2021132764A1
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- fucoxanthin
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D301/00—Preparation of oxiranes
- C07D301/32—Separation; Purification
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/33—Heterocyclic compounds
- A61K31/335—Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin
- A61K31/336—Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having three-membered rings, e.g. oxirane, fumagillin
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- 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
- A61K8/49—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds
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- 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
- A61K8/49—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds
- A61K8/4973—Cosmetics or similar toiletry preparations characterised by the composition containing organic compounds containing heterocyclic compounds with oxygen as the only hetero atom
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- 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
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D303/00—Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
- C07D303/02—Compounds containing oxirane rings
- C07D303/12—Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
- C07D303/32—Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by aldehydo- or ketonic radicals
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K2800/00—Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
- A61K2800/80—Process related aspects concerning the preparation of the cosmetic composition or the storage or application thereof
- A61K2800/805—Corresponding aspects not provided for by any of codes A61K2800/81ย -ย A61K2800/95
Definitions
- the present invention relates to a method for separating and purifying diatom-derived fucoxanthin, and more particularly, to an optimal method for separating and purifying fucoxanthin from adherent diatoms taken together with Jeju lava seawater.
- Lava seawater is seawater that penetrates the basalt layer of Jeju Island and flows underground.
- Lava seawater is found mainly in the western and eastern parts of Jeju Island and contains high concentrations of minerals.
- general seawater is exposed to unstable environments such as domestic sewage, industrial wastewater, and port pollution, it takes a lot of money to process industrial materials, whereas lava seawater undergoes natural purification and filtration by volcanic bedrock to block heavy metal adsorption and harmful substances. Therefore, it secures safety, stability, and economic feasibility, and the cost of water intake is incomparably lower than that of deep sea water taken from the deep sea.
- Adherent diatoms can be used as a valuable resource as an alternative energy source for feed in the aquaculture industry or as a basic material in various industrial fields such as medicine, environment, and life industry.
- the carotenoid market is classified into synthetic carotenoids and carotenoids derived from natural products, and is growing steadily.
- the global carotenoid market was valued at USD 1.5 billion in 2014 and is expected to increase to approximately USD 1.8 billion in 2019.
- xanthophyll-based carotenoids such as lutein, canthaxanthin, and astaxanthin is increasing, and they are mainly used as natural pigments, antioxidants, vitamin A precursors, and aquaculture feed additives.
- Fucoxanthin refers to a kind of carotenoid pigment that is mainly present in brown algae such as seaweed, kelp, motherwort, and turmeric. Brown algae are brown because their unique photosynthetic pigment called fucoxanthin is relatively higher than that of chlorophyll. It assists photosynthesis by capturing light energy and delivering about 80% of it to chlorophyll. The captured light energy absorbs light with a wavelength of 450 to 540 nm on the spectrum, and absorbs the most light with a wavelength of 510 to 525 nm, and is known to have various effects such as anti-obesity, anti-inflammatory, skin protection, and anti-aging.
- (S1) agitating the diatoms collected by mass culture in 70% alcohol; (S2) loading and filtering on a filter bed pre-coated with diatomaceous earth; (S3) fractionating and concentrating the filtered extract; (S4) separating and purifying fucoxanthin from the concentrated extract; And (S5) provides a separation and purification method of diatom-derived fucoxanthin comprising the step of storing the separated and purified fucoxanthin in a dark room.
- the diatoms may be adherent diatoms that are taken together with Jeju lava seawater.
- the adherent diatoms are Melosira nummuloides, Achnanthes brevipes var. It may be at least one species selected from the group consisting of intermedia, Achnanthes sancti-pauli, Achnanthes brevipes, or Melosira octogona.
- the diatoms may be diatoms collected from a bottom diatom culture.
- step (S1) may be characterized in that it is treated with an alcohol amount of 7 times (v/v) compared to the raw material for 1 day.
- step (S1) it may further include the step of treating plasma for 25 minutes in step (S1).
- (S4) the step of separating and purifying fucoxanthin from the concentrated extract may be characterized in that it is performed by silica gel column chromatography.
- the elution solvent used for the silica gel column chromatography may be characterized in that the ratio of N-hexane to acetone is 7:3.
- the present invention provides an optimal method for separating and purifying fucoxanthin from adherent diatoms taken from lava seawater in Jeju, Korea. Using high-purity fucoxanthin separated and purified from adherent diatoms cultured in large quantities, medical and cosmetic It can be used in various industrial fields such as fields.
- 1 is a standard solution 1 in which the raw material of diatomaceous material is stirred in alcohol, loaded on a filter bed pre-coated with diatomaceous earth and filtered, and fucoxanthin purified by silica gel column chromatography is dissolved in methanol. HPLC analysis for
- Figure 2 is HPLC for the mother liquid of standard solution 2, in which the raw material of diatomaceous material was stirred in alcohol, loaded on a filter bed pre-coated with diatomaceous earth, filtered, and stored at -20ยฐC for two days for recrystallization. analysis is shown.
- Figure 3 is HPLC for the crystallization of standard solution 2, in which the raw material of diatomaceous material is stirred in alcohol, loaded on a filter bed pre-coated with diatomaceous earth, filtered, and stored at -20ยฐC for two days for recrystallization. analysis is shown.
- Figure 4 shows the HPLC analysis of the standard solution 3 prepared in the same manner as the standard solution 1, but without the desalting reaction.
- Figure 5 shows the HPLC analysis of the standard solution 3 prepared in the same manner as the standard solution 1, but subjected to a desalting reaction.
- Figure 10 shows a schematic diagram of the fucoxanthin separation and purification process.
- Figure 11 shows the fucoxanthin separation and purification process by silica gel column chromatography (silica gel column chromatography).
- Figure 12 shows the results of TLC (Thin Layer Chromatography) of the fraction containing fucoxanthin.
- Figure 19 shows the HPLC quantitative analysis of Sample No 1 of Table 3.
- Figure 21 shows the HPLC quantitative analysis of Sample No 15 of Table 3.
- Figure 22 shows the HPLC quantitative analysis of Sample No 16 of Table 3.
- Figure 24 shows the HPLC quantitative analysis of Sample No 8 of Table 3.
- (S1) agitating the diatoms collected by mass culture in 70% alcohol; (S2) loading and filtering on a filter bed pre-coated with diatomaceous earth; (S3) fractionating and concentrating the filtered extract; (S4) separating and purifying fucoxanthin from the concentrated extract; And (S5) provides a separation and purification method of diatom-derived fucoxanthin comprising the step of storing the separated and purified fucoxanthin in a dark room.
- the diatoms may be adherent diatoms that are taken together with Jeju lava seawater.
- the adherent diatom is Melosira nummuloides, Achnanthes brevipes var. It may be at least one species selected from the group consisting of intermedia, Achnanthes sancti-pauli, Achnanthes brevipes, or Melosira octogona.
- the diatoms may be diatoms collected from a bottom diatom culture.
- step (S1) may be characterized in that it is treated with an alcohol amount of 7 times (v/v) compared to the raw material for 1 day.
- it may further include the step of treating plasma for 25 minutes in step (S1).
- the step of separating and purifying fucoxanthin from the concentrated extract may be characterized in that it is performed by silica gel column chromatography.
- the elution solvent used for the silica gel column chromatography may be characterized in that the ratio of N-hexane to acetone is 7:3.
- the separation and purification method was optimized by measuring the change in the content of fucoxanthin according to the separation and purification method. To this end, 50 g of diatoms in wet state were first put and dried in a vacuum dryer for 48 hours, and thereafter, the change in the content of fucoxanthin by various processes was measured using HPLC.
- standard solution 2 was prepared through a recrystallization process. Dissolving a solute in a solvent at a higher temperature can dissolve a larger amount of the solute than at a lower temperature. In this dissolved state, if the temperature is lowered again slowly, the solubility decreases, so the solute is precipitated again to form crystals, which is called recrystallization.
- the filtered sample for recrystallization experiment was stored at -20ยฐC for two days to prepare standard solution 2. After that, standard solution 2 was dispensed in a transparent container and the content of fucoxanthin was measured by HPLC.
- Standard solution 3 proceeded in the same manner as standard solution 1 except for adding the desalting process for raw diatoms, and the effect of the desalting process was verified.
- Standard solution 3 was dispensed in a transparent container and the content of fucoxanthin was measured by HPLC. There was no color change and fucoxanthin content was calculated based on the peak area value. The observed fucoxanthin content was lowered to a level of 21% compared to standard solution 1 when desalting was performed, and was lowered to a level of 17% when desalting was not performed ( FIGS. 4 and 5 ).
- Standard solution 4 verified the stability of fucoxanthin by changing the content of fucoxanthin when exposed to sunlight.
- Standard solution 4 was dispensed in a transparent container and the content of fucoxanthin was measured by HPLC. There was no color change and fucoxanthin content was calculated based on the peak area value.
- the content decreased by about 82%, and the purity decreased from 90% to 55% (FIG. 6).
- Silica gel chromatography is used for separation and purification of functional substances such as fucoxanthin. will be.
- silica gel chromatography was performed under various conditions to efficiently separate and purify fucoxanthin, a target material.
- the primary alcohol extract obtained by first filtering the extract extracted from 100 g of diatom powder with 70% alcohol at 10 times the volume with 5um filter paper was separated into n-Hexane: 70% alcohol (1:1), and 70% alcohol in the lower layer A fraction was obtained.
- a fraction (dark orange layer) that is expected to contain fucoxanthin was obtained and TLC (Thin Layer Chromatography) was performed (FIGS. 11 and 12), and as a result, fractions from Fraction No. 1 to No. 9 It was confirmed that fucoxanthin was separated from the , and the concentration process was performed using a high pressure vacuum concentrator (FIG. 13).
- the standard material fucoxanthin (purchased from Sigma Aldrich) was diluted by concentration to prepare an HPLC standard calibration curve (FIG. 14).
- HPLC standard calibration curve For HPLC analysis, Waters 2695 HPLC equipment was used, the column used was Kromasil 100-5-C18 (4.6x250mm, 5um), the detection wavelength was 450 nm, and the solvent was Acetonitrile / water (Table 2).
- the usefulness of recrystallization of the concentrate to improve the degree of purification and yield of fucoxanthin was studied. Specifically, the primary extract obtained by stirring 100 g of diatomaceous powder with 70% alcohol at 10 times the volume for 2 hours was loaded into a filter bed coated with 50 g of diatomaceous earth to obtain an extract filtrate. The finally obtained concentrate was dissolved in acetone, and the fucoxanthin fraction was sampled by silica gel chromatography, and it was checked by TLC (Thin Layer Chromatography) to confirm that the fucoxanthin was separated (FIG. 16).
- TLC Thin Layer Chromatography
- HPLC analysis was performed under the same conditions as in Example, and dry diatom powder (No. 1 to No. 11) was dissolved in methanol at a concentration of 50 mg/mL, sonicated for 30 minutes, filtered, and then used for analysis. This was repeated 3 times.
- the bottom diatom showed a higher fucoxanthin content than the floating diatom (Table 3, No. 1 & No. 3), and the presence or absence of desalination did not significantly affect the content change. appear.
- the diatomite sample that had the highest content of fucoxanthin was an undried diatomite sample. This result indicates that some of the fucoxanthin in the diatom was decomposed during the collection and drying (natural drying or hot air drying) process of the diatom culture ( No. 15, 16).
- the harvesting/processing step of diatom it is the most efficient process to directly harvest the raw diatom without going through the drying process and directly enter the extraction process.
- the optimal extraction conditions were determined by comparing and analyzing the extraction efficiency of fucoxanthin according to the presence or absence of plasma treatment.
- extracts were prepared from samples treated with plasma and untreated biodiatoms to compare the extraction yield of fucoxanthin. After adding 20 mL of 70% alcohol to 5 g of biological diatom, plasma was treated for 25 minutes, extracted at 40 ยฐ C for 3 days, the extract was centrifuged at 3500 rpm for 10 minutes to remove the extraction residue, and HPLC analysis was performed using the extract of the upper layer. As a control, a sample that was not subjected to plasma treatment under the same extraction conditions as above was set as a control. Since the extract was small, the extract was obtained after removing the residue by centrifugation without going through a filtration process (Table 4), and the fucoxanthin extraction efficiency according to plasma treatment was reviewed through HPLC analysis (Table 5).
- the optimal extraction conditions were determined by comparatively analyzing the extraction efficiency according to the type of solvent used, the amount of solvent, and the extraction time.
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Abstract
Description
๋ณธ ๋ฐ๋ช ์ ๊ท์กฐ๋ฅ ์ ๋ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ๋ฐฉ๋ฒ์ ๊ดํ ๊ฒ์ผ๋ก, ๋์ฑ ์์ธํ๊ฒ๋ ์ ์ฃผ ์ฉ์ ํด์์ ํจ๊ป ์ทจ์๋๋ ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๋ก๋ถํฐ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ํ๋ ์ต์ ์ ๋ฐฉ๋ฒ์ ๊ดํ ๊ฒ์ด๋ค.The present invention relates to a method for separating and purifying diatom-derived fucoxanthin, and more particularly, to an optimal method for separating and purifying fucoxanthin from adherent diatoms taken together with Jeju lava seawater.
์ฉ์ํด์๋ ์ ์ฃผ๋์ ํ๋ฌด์์ธต์ ๋ซ๊ณ ์ก์ง ์งํ๋ก ํ๋ฌ ๋ค์ด์จ ๋ฐ๋ท๋ฌผ์ด๋ค. ์ฉ์ํด์๋ ์ ์ฃผ๋์ ์๋ถ ์ผ๋ถ์ง์ญ๊ณผ ๋๋ถ์ง์ญ์ ์ค์ฌ์ผ๋ก ๋ฐ๊ฒฌ๋๋ฉฐ ๊ณ ๋๋์ ๋ฏธ๋ค๋์ ํจ์ ํ๊ณ ์๋ค. ๋ํ ์ผ๋ฐํด์๋ ์ํํ์, ์ฐ์ ํ์, ํญ๋ง์ค์ผ ๋ฑ์ ๋ถ์์ ํ ํ๊ฒฝ์ ๋ ธ์ถ๋์ด ์ฐ์ ํ ์์ฌ ๊ฐ๊ณต์ ๋ง์ ๋น์ฉ์ด ์์๋๋ ๋ฐ๋ฉด, ์ฉ์ํด์๋ ํ์ฐ์๋ฐ์ธต์ ์ํ ์์ฐ์ ํ์ ์ฌ๊ณผ๋ฅผ ๊ฑฐ์ณ ์ค๊ธ์ ํก์ฐฉ ๋ฐ ์ ํด๋ฌผ์ง์ ์ฐจ๋จํ๊ธฐ ๋๋ฌธ์ ์์ ์ฑ๊ณผ ์์ ์ฑ, ๊ฒฝ์ ์ฑ์ ํ๋ณดํ๊ณ ์๊ณ , ๊น์ ๋ฐ๋ค์์ ์ทจ์ํ๋ ํด์์ฌ์ธต์์ ๋นํด์ ๋น๊ตํ ์ ์์ ์ ๋๋ก ์ทจ์๋น์ฉ์ด ์ ๋ ดํ๋ค.Lava seawater is seawater that penetrates the basalt layer of Jeju Island and flows underground. Lava seawater is found mainly in the western and eastern parts of Jeju Island and contains high concentrations of minerals. In addition, while general seawater is exposed to unstable environments such as domestic sewage, industrial wastewater, and port pollution, it takes a lot of money to process industrial materials, whereas lava seawater undergoes natural purification and filtration by volcanic bedrock to block heavy metal adsorption and harmful substances. Therefore, it secures safety, stability, and economic feasibility, and the cost of water intake is incomparably lower than that of deep sea water taken from the deep sea.
๋ณธ ์ถ์์ ๋ฐ๋ช ์๋ ์ ์ฃผ ์ฉ์ํด์๋ฅผ ์ด์ฉํ์ฌ ์์์ ํ๋ ๊ณผ์ ์์ ์ฉ์ํด์์ ํจ๊ป ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๊ฐ ์ทจ์๋๋ ๊ฒ์ ํ์ธํ๊ณ , ์ด๋ค ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๋ฅผ ์ฐ์ ์์ผ ๋๋ ๋ฐฐ์ํ๋ ๋ฐฉ๋ฒ์ ํ๋ฆฝํ์๋ค. ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๋ ์์ ์ฐ์ ์ ์ฌ๋ฃ ๋์ฒด ์๋์ง์์ผ๋ก์ ๋๋ ์ํ, ํ๊ฒฝ, ์๋ช ์ฐ์ ๋ฑ ์ฌ๋ฌ ์ฐ์ ๋ถ์ผ์ ๊ธฐ์ด์ฌ๋ก์ ๊ฐ์น๊ฐ ๋์ ์์์ผ๋ก ํ์ฉ๊ฐ๋ฅํ๋ค.The inventor of the present application confirmed that adherent diatoms were taken together with lava seawater in the process of aquaculture using Jeju lava seawater, and established a method of mass-cultivating these adherent diatoms dominantly. Adherent diatoms can be used as a valuable resource as an alternative energy source for feed in the aquaculture industry or as a basic material in various industrial fields such as medicine, environment, and life industry.
ํํธ, ์นด๋กํฐ๋ ธ์ด๋ ์์ฅ์ ํฉ์ฑ ์นด๋กํฐ๋ ธ์ด๋์ ์ฒ์ฐ๋ฌผ ์ ๋ ์นด๋กํฐ๋ ธ์ด๋๋ก ๋ถ๋ฅ๋๋ฉฐ, ๊พธ์คํ ์ฑ์ฅ์ธ๋ฅผ ์ด๋ฃจ๊ณ ์๋ค. ์ ์ธ๊ณ ์นด๋กํฐ๋ ธ์ด๋ ์์ฅ์ 2014๋ 15์ต ๋ฌ๋ฌ๋ฅผ ๊ธฐ๋กํ๊ณ , 2019๋ ์๋ ์ฝ 18์ต ๋ฌ๋ฌ๋ก ์ฆ๊ฐํ ๊ฒ์ผ๋ก ์์๋๋ค. ํนํ ๋ฃจํ ์ธ, ์นธํ์ํด, ์์คํ์ํด ๋ฑ์ ํฌ์ฐํ ํ๊ณ ์นด๋กํฐ๋ ธ์ด๋์ ๊ฐ์น๊ฐ ๋์์ง๊ณ ์์ผ๋ฉฐ, ์ฃผ๋ก ์ฒ์ฐ์์, ํญ์ฐํ์ , ๋นํ๋ฏผA ์ ๊ตฌ์ฒด, ์์ ์ฌ๋ฃ ์ฒจ๊ฐ์ ๋ฑ์ผ๋ก ์ฌ์ฉ๋๊ณ ์๋ค.On the other hand, the carotenoid market is classified into synthetic carotenoids and carotenoids derived from natural products, and is growing steadily. The global carotenoid market was valued at USD 1.5 billion in 2014 and is expected to increase to approximately USD 1.8 billion in 2019. In particular, the value of xanthophyll-based carotenoids such as lutein, canthaxanthin, and astaxanthin is increasing, and they are mainly used as natural pigments, antioxidants, vitamin A precursors, and aquaculture feed additives.
ํ์ฝ์ํด์ ์ฃผ๋ก ๋ฏธ์ญ, ๋ค์๋ง, ๋ชจ์๋ฐ, ํณ ๋ฑ์ ๊ฐ์กฐ๋ฅ(brown algae)์ ์กด์ฌํ๋ ์ผ์ข ์ ์นด๋กํฐ๋ ธ์ด๋๊ณ(Carotenoid) ์์๋ฅผ ์๋ฏธํ๋ค. ๊ฐ์กฐ๋ฅ๊ฐ ๊ฐ์์ ๋ํ๋ด๋ ๊ฒ์ ํ์ฝ์ํด์ด๋ผ๋ ๊ณ ์ ํ ๊ดํฉ์ฑ ์์๊ฐ ์ฝ๋ก์์ ๋นํด ์๋์ ์ผ๋ก ๋ง๊ธฐ ๋๋ฌธ์ด๋ค. ๋น์๋์ง๋ฅผ ํฌ์ฐฉํด ์ฝ 80%๋ฅผ ์ฝ๋ก์์ ์ ๋ฌํจ์ผ๋ก์จ ๊ดํฉ์ฑ์ ๋ณด์กฐํ๋ค. ํฌ์ฐฉ๋ ๋น์๋์ง๋ ์คํํธ๋ผ ์์ 450~540nm ํ์ฅ์ ๋น์ ํก์ํ๋ฉฐ, 510~525nm ํ์ฅ์ ๋น์ ๊ฐ์ฅ ๋ง์ด ํก์ํ๋ฉฐ, ํญ๋น๋ง, ํญ์ผ์ฆ, ํผ๋ถ๋ณดํธ, ๋ ธํ์ต์ ๋ฑ ๋ค์ํ ํจ๋ฅ์ด ์๋ ๊ฒ์ผ๋ก ์๋ ค์ก๋ค.Fucoxanthin refers to a kind of carotenoid pigment that is mainly present in brown algae such as seaweed, kelp, motherwort, and turmeric. Brown algae are brown because their unique photosynthetic pigment called fucoxanthin is relatively higher than that of chlorophyll. It assists photosynthesis by capturing light energy and delivering about 80% of it to chlorophyll. The captured light energy absorbs light with a wavelength of 450 to 540 nm on the spectrum, and absorbs the most light with a wavelength of 510 to 525 nm, and is known to have various effects such as anti-obesity, anti-inflammatory, skin protection, and anti-aging.
์ฐ๋ฆฌ๋๋ผ ์ ์ฃผ ์ฉ์ํด์์์ ์ทจ์๋๋ ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๋ก๋ถํฐ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ํ๋ ์ต์ ์ ๋ฐฉ๋ฒ์ ์ ๊ณตํ๋ค.We provide an optimal method for separating and purifying fucoxanthin from adherent diatoms taken from lava seawater in Jeju, Korea.
์๊ธฐ์ ๊ฐ์ ๋ฌธ์ ๋ฅผ ํด๊ฒฐํ๊ธฐ ์ํด ๋ณธ ๋ฐ๋ช ์์๋ (S1) ๋๋ ๋ฐฐ์ํ์ฌ ์๊ฑฐ๋ ๊ท์กฐ๋ฅ๋ฅผ 70% ์ฃผ์ ์ ๊ต๋ฐํ๋ ๋จ๊ณ; (S2) ๊ท์กฐํ ๋ก ์ฌ์ ์ฝํ (precoat)๋ ์ฌ๊ณผ๋ฒ ๋(filter bed)์ loadingํ์ฌ ์ฌ๊ณผํ๋ ๋จ๊ณ; (S3) ์ฌ๊ณผ๋ ์ถ์ถ๋ฌผ์ ๋ถํ ๋ฐ ๋์ถํ๋ ๋จ๊ณ; (S4) ๋์ถ๋ ์ถ์ถ๋ฌผ์์ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ํ๋ ๋จ๊ณ; ๋ฐ (S5) ๋ถ๋ฆฌ์ ์ ๋ ํ์ฝ์ํด์ ์์ค์ ๋ณด๊ดํ๋ ๋จ๊ณ๋ก ์ด๋ฃจ์ด์ง๋ ๊ท์กฐ๋ฅ ์ ๋ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ๋ฐฉ๋ฒ์ ์ ๊ณตํ๋ค.In the present invention in order to solve the above problems, (S1) agitating the diatoms collected by mass culture in 70% alcohol; (S2) loading and filtering on a filter bed pre-coated with diatomaceous earth; (S3) fractionating and concentrating the filtered extract; (S4) separating and purifying fucoxanthin from the concentrated extract; And (S5) provides a separation and purification method of diatom-derived fucoxanthin comprising the step of storing the separated and purified fucoxanthin in a dark room.
๋ณธ ๋ฐ๋ช ์ ์์ด์, ๊ท์กฐ๋ฅ๋ ์ ์ฃผ ์ฉ์ ํด์์ ํจ๊ป ์ทจ์๋๋ ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ์ผ ์ ์๋ค.In the present invention, the diatoms may be adherent diatoms that are taken together with Jeju lava seawater.
๋ณธ ๋ฐ๋ช ์ ์์ด์, ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๋ Melosira nummuloides, Achnanthes brevipes var. intermedia, Achnanthes sancti-pauli, Achnanthes brevipes ๋๋ Melosira octogona ๋ก ์ด๋ฃจ์ด์ง ๊ตฐ ์ค ์ ํ๋ ํ ์ข ์ด์์ผ ์ ์๋ค. In the present invention, the adherent diatoms are Melosira nummuloides, Achnanthes brevipes var. It may be at least one species selected from the group consisting of intermedia, Achnanthes sancti-pauli, Achnanthes brevipes, or Melosira octogona.
๋ณธ ๋ฐ๋ช ์ ์์ด์, ์๊ธฐ ๊ท์กฐ๋ฅ๋ ๋ฐ๋ฅ๊ท์กฐ ๋ฐฐ์๋ฌผ์์ ์๊ฑฐ๋๋ ๊ท์กฐ๋ฅ์ผ ์ ์๋ค.In the present invention, the diatoms may be diatoms collected from a bottom diatom culture.
๋ณธ ๋ฐ๋ช ์ ์์ด์, (S1)๋จ๊ณ๋ ์๋ฌผ ๋๋น 7๋ฐฐ(v/v)์ ์ฃผ์ ๋์ผ๋ก 1์ผ๊ฐ ์ฒ๋ฆฌํ๋ ๊ฒ์ ํน์ง์ผ๋ก ํ ์ ์๋ค.In the present invention, step (S1) may be characterized in that it is treated with an alcohol amount of 7 times (v/v) compared to the raw material for 1 day.
๋ณธ ๋ฐ๋ช ์ ์์ด์, (S1)๋จ๊ณ์์ 25๋ถ๊ฐ plasma๋ฅผ ์ฒ๋ฆฌํ๋ ๋จ๊ณ๋ฅผ ๋ ํฌํจํ ์ ์๋ค.In the present invention, it may further include the step of treating plasma for 25 minutes in step (S1).
๋ณธ ๋ฐ๋ช ์ ์์ด์, (S4) ๋์ถ๋ ์ถ์ถ๋ฌผ์์ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ํ๋ ๋จ๊ณ๋ ์ค๋ฆฌ์นด ๊ฒ ์ปฌ๋ผ ํฌ๋ก๋งํ ๊ทธ๋ํผ(silica gel column chromatography)์ ์ํ์ฌ ์ด๋ฃจ์ด์ง๋ ๊ฒ์ ํน์ง์ผ๋ก ํ ์ ์๋ค.In the present invention, (S4) the step of separating and purifying fucoxanthin from the concentrated extract may be characterized in that it is performed by silica gel column chromatography.
๋ณธ ๋ฐ๋ช ์ ์์ด์, ์๊ธฐ ์ค๋ฆฌ์นด ๊ฒ ์ปฌ๋ผ ํฌ๋ก๋งํ ๊ทธ๋ํผ์ ์ฌ์ฉ๋๋ ์ฉ์ถ์ฉ๋งค๋ N-hexane๊ณผ Acetone์ ๋น์จ์ด 7 : 3 ์ธ ๊ฒ์ ํน์ง์ผ๋ก ํ ์ ์๋ค.In the present invention, the elution solvent used for the silica gel column chromatography may be characterized in that the ratio of N-hexane to acetone is 7:3.
๋ณธ ๋ฐ๋ช ์ ์ฐ๋ฆฌ๋๋ผ ์ ์ฃผ ์ฉ์ํด์์์ ์ทจ์๋๋ ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๋ก๋ถํฐ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ํ๋ ์ต์ ์ ๋ฐฉ๋ฒ์ ์ ๊ณตํ๋ ๋ฐ, ๋๋์ผ๋ก ๋ฐฐ์๋ ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๋ก๋ถํฐ ๋ถ๋ฆฌ์ ์ ๋ ๊ณ ์๋์ ํ์ฝ์ํด์ ์ด์ฉํ์ฌ ์๋ฃ๋ถ์ผ, ๋ฏธ์ฉ๋ถ์ผ ๋ฑ ๋ค์ํ ์ฐ์ ๋ถ์ผ์์ ํ์ฉ์ด ๊ฐ๋ฅํ๋ค.The present invention provides an optimal method for separating and purifying fucoxanthin from adherent diatoms taken from lava seawater in Jeju, Korea. Using high-purity fucoxanthin separated and purified from adherent diatoms cultured in large quantities, medical and cosmetic It can be used in various industrial fields such as fields.
๋ 1์ ๊ท์กฐ๋ฃ ์๋ฌผ์ ์ฃผ์ ์ ๊ต๋ฐ ํ ๊ท์กฐํ ๋ก ์ฌ์ ์ฝํ
(precoat)๋ ์ฌ๊ณผ๋ฒ ๋(filter bed)์ loadingํ์ฌ ์ฌ๊ณผํ๊ณ , ์ค๋ฆฌ์นด ๊ฒ ์ปฌ๋ผ ํฌ๋ก๋งํ ๊ทธ๋ํผ์ ์ํ์ฌ ๋ถ๋ฆฌ์ ์ ๋ ํ์ฝ์ํด์ ๋ฉํ์ฌ์ ๋
น์ธ ํ์ค์ฉ์ก 1์ ๋ํ HPLC ๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.1 is a
๋ 2๋ ๊ท์กฐ๋ฃ ์๋ฌผ์ ์ฃผ์ ์ ๊ต๋ฐ ํ ๊ท์กฐํ ๋ก ์ฌ์ ์ฝํ
(precoat)๋ ์ฌ๊ณผ๋ฒ ๋(filter bed)์ loadingํ์ฌ ์ฌ๊ณผํ๊ณ , ์ดํ๋์ -20โ์์ ๋ณด๊ดํ์ฌ ์ฌ๊ฒฐ์ ์ ์ค์ํ ํ์ค์ฉ์ก 2์ ๋ชจ์ก์ ๋ํ HPLC ๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 2 is HPLC for the mother liquid of
๋ 3์ ๊ท์กฐ๋ฃ ์๋ฌผ์ ์ฃผ์ ์ ๊ต๋ฐ ํ ๊ท์กฐํ ๋ก ์ฌ์ ์ฝํ
(precoat)๋ ์ฌ๊ณผ๋ฒ ๋(filter bed)์ loadingํ์ฌ ์ฌ๊ณผํ๊ณ , ์ดํ๋์ -20โ์์ ๋ณด๊ดํ์ฌ ์ฌ๊ฒฐ์ ์ ์ค์ํ ํ์ค์ฉ์ก 2์ ๊ฒฐ์ ์ ๋ํ HPLC ๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 3 is HPLC for the crystallization of
๋ 4๋ ์๊ธฐ ํ์ค์ฉ์ก 1๊ณผ ๋์ผํ๊ฒ ์ ์กฐํ๋ ํ์ผ๋ฐ์์ ์งํํ์ง ์๋ํ ํ์ค์ฉ์ก 3์ ๋ํ HPLC ๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 4 shows the HPLC analysis of the
๋ 5๋ ์๊ธฐ ํ์ค์ฉ์ก 1๊ณผ ๋์ผํ๊ฒ ์ ์กฐํ๋ ํ์ผ๋ฐ์์ ์งํํ ํ์ค์ฉ์ก 3์ ๋ํ HPLC ๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 5 shows the HPLC analysis of the
๋ 6์ ์๊ธฐ ํ์ค์ฉ์ก 1๊ณผ ๋์ผํ๊ฒ ์ ์กฐํ๋ ํ๋น์ ๋
ธ์ถํ ํ์ค์ฉ์ก 4์ ๋ํ HPLC ๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.6 shows the HPLC analysis of the
๋ 7์ ํ 1์ Sample No 4์ ๋ํ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.7 shows the HPLC quantitative analysis of
๋ 8์ ํ 1์ Sample No 5์ ๋ํ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.8 shows the HPLC quantitative analysis of
๋ 9๋ ํ 1์ Sample No 6์ ๋ํ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.9 shows the HPLC quantitative analysis of
๋ 10์ ํ์ฝ์ํด ๋ถ๋ฆฌ์ ์ ๊ณต์ ์ ๊ฐ๋ต๋๋ฅผ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 10 shows a schematic diagram of the fucoxanthin separation and purification process.
๋ 11์ ์ค๋ฆฌ์นด ๊ฒ ์ปฌ๋ผ ํฌ๋ก๋งํ ๊ทธ๋ํผ(silica gel column chromatography)์ ์ํ ํ์ฝ์ํด ๋ถ๋ฆฌ์ ์ ๊ณต์ ์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 11 shows the fucoxanthin separation and purification process by silica gel column chromatography (silica gel column chromatography).
๋ 12๋ ํ์ฝ์ํด์ ํฌํจํ๋ ๋ถํ๋ฌผ์ TLC(Thin Layer Chromatography) ๊ฒฐ๊ณผ๋ฅผ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 12 shows the results of TLC (Thin Layer Chromatography) of the fraction containing fucoxanthin.
๋ 13์ ํ์ฝ์ํด์ ๋์ถ๊ณผ์ ์ ๋ํ๋ธ ๊ฒ์ด๋ค.13 shows the concentration process of fucoxanthin.
๋ 14๋ ํ์ค ํ์ฝ์ํด(Sigma Aldrich์์ ๊ตฌ์ )์ ์ด์ฉํ ํ์ค๊ฒ๋์ ์์ฑ์ ๋ํ๋ธ ๊ฒ์ด๋ค.14 shows the creation of a standard calibration curve using standard fucoxanthin (purchased from Sigma Aldrich).
๋ 15๋ ๊ท์กฐ๋ถ๋ง์ 70% ์ฃผ์ ์ถ์ถ๋ฌผ๋ก๋ถํฐ ๋ถํ/๋์ถ๊ณผ์ ์ ํตํ์ฌ ์ต์ข ์ ์ผ๋ก ์ป์ด์ง ์๋ 60% ํ์ฝ์ํด์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.15 shows HPLC quantitative analysis of 60% pure fucoxanthin finally obtained through fractionation/concentration process from 70% alcohol extract of diatom powder.
๋ 16์ ๊ท์กฐํ ์ฌ์ ์ฝํ (precoat) ์ฌ๊ณผ ๋ฐ ์ฌ๊ฒฐ์ ํ ๊ณผ์ ์ ๋ํ๋ธ ๊ฒ์ด๋ค.16 shows the diatomaceous earth precoat filtration and recrystallization process.
๋ 17์ ์ฌ๊ณผ๊ณผ์ ๋ฐ ์ฌ๊ฒฐ์ ์ ํ๋ฏธ๊ฒฝ ๊ด์ฐฐ์ฌ์ง(ร400)์ ๋ํ๋ธ ๊ฒ์ด๋ค.17 shows a microscopic observation photograph (ร400) of the filtration process and recrystallization.
๋ 18์ ์ฌ๊ฒฐ์ ์ ์ค์ํ ํ์ฝ์ํด์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.18 shows the HPLC quantitative analysis of fucoxanthin subjected to recrystallization.
๋ 19๋ ํ 3์ Sample No 1์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 19 shows the HPLC quantitative analysis of
๋ 20์ ํ 3์ Sample No 3์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.20 shows the HPLC quantitative analysis of
๋ 21์ ํ 3์ Sample No 15์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 21 shows the HPLC quantitative analysis of
๋ 22๋ ํ 3์ Sample No 16์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 22 shows the HPLC quantitative analysis of
๋ 23์ ํ์ฝ์ํด์ ๋ถ๋ง์ ํ์ ๋ํ๋ธ ๊ฒ์ด๋ค.23 shows a powder formulation of fucoxanthin.
๋ 24๋ ํ 3์ Sample No 8์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.Figure 24 shows the HPLC quantitative analysis of
๋ 25๋ ํ 3์ Sample No 9์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.25 shows the HPLC quantitative analysis of Sample No 9 of Table 3.
๋ 26์ ํ 3์ Sample No 10์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.26 shows the HPLC quantitative analysis of
๋ 27์ ํ 3์ Sample No 11์ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.27 shows the HPLC quantitative analysis of
๋ 28 ๋ด์ง ๋47์ ํ 6์ sample 1 ๋ด์ง 20์ ๋ํ HPLC ์ ๋๋ถ์์ ๋ํ๋ธ ๊ฒ์ด๋ค.28 to 47 show HPLC quantitative analysis of
๋ณธ ๋ฐ๋ช ์ ์ํ ์ผ ์ค์์๋ก์, (S1) ๋๋ ๋ฐฐ์ํ์ฌ ์๊ฑฐ๋ ๊ท์กฐ๋ฅ๋ฅผ 70% ์ฃผ์ ์ ๊ต๋ฐํ๋ ๋จ๊ณ; (S2) ๊ท์กฐํ ๋ก ์ฌ์ ์ฝํ (precoat)๋ ์ฌ๊ณผ๋ฒ ๋(filter bed)์ loadingํ์ฌ ์ฌ๊ณผํ๋ ๋จ๊ณ; (S3) ์ฌ๊ณผ๋ ์ถ์ถ๋ฌผ์ ๋ถํ ๋ฐ ๋์ถํ๋ ๋จ๊ณ; (S4) ๋์ถ๋ ์ถ์ถ๋ฌผ์์ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ํ๋ ๋จ๊ณ; ๋ฐ (S5) ๋ถ๋ฆฌ์ ์ ๋ ํ์ฝ์ํด์ ์์ค์ ๋ณด๊ดํ๋ ๋จ๊ณ๋ก ์ด๋ฃจ์ด์ง๋ ๊ท์กฐ๋ฅ ์ ๋ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ๋ฐฉ๋ฒ์ ์ ๊ณตํ๋ค.As an embodiment of the present invention, (S1) agitating the diatoms collected by mass culture in 70% alcohol; (S2) loading and filtering on a filter bed pre-coated with diatomaceous earth; (S3) fractionating and concentrating the filtered extract; (S4) separating and purifying fucoxanthin from the concentrated extract; And (S5) provides a separation and purification method of diatom-derived fucoxanthin comprising the step of storing the separated and purified fucoxanthin in a dark room.
๋ณธ ๋ฐ๋ช ์ ์ํ ๋ค๋ฅธ ์ค์์์์, ๊ท์กฐ๋ฅ๋ ์ ์ฃผ ์ฉ์ ํด์์ ํจ๊ป ์ทจ์๋๋ ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ์ผ ์ ์๋ค.In another embodiment according to the present invention, the diatoms may be adherent diatoms that are taken together with Jeju lava seawater.
๋ณธ ๋ฐ๋ช ์ ์ํ ๋ ๋ค๋ฅธ ์ค์์์์, ๋ถ์ฐฉ์ฑ ๊ท์กฐ๋ฅ๋ Melosira nummuloides, Achnanthes brevipes var. intermedia, Achnanthes sancti-pauli, Achnanthes brevipes ๋๋ Melosira octogona ๋ก ์ด๋ฃจ์ด์ง ๊ตฐ ์ค ์ ํ๋ ํ ์ข ์ด์์ผ ์ ์๋ค. In another embodiment according to the present invention, the adherent diatom is Melosira nummuloides, Achnanthes brevipes var. It may be at least one species selected from the group consisting of intermedia, Achnanthes sancti-pauli, Achnanthes brevipes, or Melosira octogona.
๋ณธ ๋ฐ๋ช ์ ์ํ ๋ ๋ค๋ฅธ ์ค์์์์, ์๊ธฐ ๊ท์กฐ๋ฅ๋ ๋ฐ๋ฅ๊ท์กฐ ๋ฐฐ์๋ฌผ์์ ์๊ฑฐ๋๋ ๊ท์กฐ๋ฅ์ผ ์ ์๋ค.In another embodiment according to the present invention, the diatoms may be diatoms collected from a bottom diatom culture.
๋ณธ ๋ฐ๋ช ์ ์ํ ๋ ๋ค๋ฅธ ์ค์์์์, (S1)๋จ๊ณ๋ ์๋ฌผ ๋๋น 7๋ฐฐ(v/v)์ ์ฃผ์ ๋์ผ๋ก 1์ผ๊ฐ ์ฒ๋ฆฌํ๋ ๊ฒ์ ํน์ง์ผ๋ก ํ ์ ์๋ค.In another embodiment according to the present invention, step (S1) may be characterized in that it is treated with an alcohol amount of 7 times (v/v) compared to the raw material for 1 day.
๋ณธ ๋ฐ๋ช ์ ์ํ ๋ ๋ค๋ฅธ ์ค์์์์, (S1)๋จ๊ณ์์ 25๋ถ๊ฐ plasma๋ฅผ ์ฒ๋ฆฌํ๋ ๋จ๊ณ๋ฅผ ๋ ํฌํจํ ์ ์๋ค.In another embodiment according to the present invention, it may further include the step of treating plasma for 25 minutes in step (S1).
๋ณธ ๋ฐ๋ช ์ ์ํ ๋ ๋ค๋ฅธ ์ค์์์์, (S4) ๋์ถ๋ ์ถ์ถ๋ฌผ์์ ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์ ํ๋ ๋จ๊ณ๋ ์ค๋ฆฌ์นด ๊ฒ ์ปฌ๋ผ ํฌ๋ก๋งํ ๊ทธ๋ํผ(silica gel column chromatography)์ ์ํ์ฌ ์ด๋ฃจ์ด์ง๋ ๊ฒ์ ํน์ง์ผ๋ก ํ ์ ์๋ค.In another embodiment according to the present invention, (S4) the step of separating and purifying fucoxanthin from the concentrated extract may be characterized in that it is performed by silica gel column chromatography.
๋ณธ ๋ฐ๋ช ์ ์ํ ๋ ๋ค๋ฅธ ์ค์์์์, ์๊ธฐ ์ค๋ฆฌ์นด ๊ฒ ์ปฌ๋ผ ํฌ๋ก๋งํ ๊ทธ๋ํผ์ ์ฌ์ฉ๋๋ ์ฉ์ถ์ฉ๋งค๋ N-hexane๊ณผ Acetone์ ๋น์จ์ด 7 : 3 ์ธ ๊ฒ์ ํน์ง์ผ๋ก ํ ์ ์๋ค.In another embodiment of the present invention, the elution solvent used for the silica gel column chromatography may be characterized in that the ratio of N-hexane to acetone is 7:3.
์ดํ, ๊ตฌ์ฒด์ ์ธ ์ค์์๋ฅผ ํตํ์ฌ ๋ณธ ๋ฐ๋ช ์ ๋ณด๋ค ์์ธํ ์ค๋ช ํ๊ณ ์ ํ๋ค. ์ด๋ค ์ค์์๋ ์ค๋ก์ง ๋ณธ ๋ฐ๋ช ์ ๋ณด๋ค ๊ตฌ์ฒด์ ์ผ๋ก ์ค๋ช ํ๊ธฐ ์ํ ๊ฒ์ผ๋ก, ๋ณธ ๋ฐ๋ช ์ ์์ง์ ๋ฐ๋ผ ๋ณธ ๋ฐ๋ช ์ ๋ฒ์๊ฐ ์ด๋ค ์ค์์์ ์ํด ์ ํ๋์ง ์๋๋ค๋ ๊ฒ์ ๋น์ ๊ณ์์ ํต์์ ์ง์์ ๊ฐ์ง ์์๊ฒ ์์ด์ ์๋ช ํ ๊ฒ์ด๋ค.Hereinafter, the present invention will be described in more detail through specific examples. These examples are only for illustrating the present invention in more detail, and it will be apparent to those of ordinary skill in the art that the scope of the present invention is not limited by these examples according to the gist of the present invention. .
์ค์์ 1. ํ์ฝ์ํด ๋ถ๋ฆฌ์ ์ ๋ฐฉ๋ฒ์ ์ต์ ํExample 1. Optimization of fucoxanthin separation and purification method
๋ถ๋ฆฌ์ ์ ๋ฐฉ๋ฒ์ ๋ฐ๋ฅธ ํ์ฝ์ํด์ ํจ๋๋ณํ๋ฅผ ์ธก์ ํ์ฌ ๋ถ๋ฆฌ์ ์ ๋ฐฉ๋ฒ์ ์ต์ ํํ์๋ค. ์ด๋ฅผ ์ํ์ฌ ๋จผ์ wet ์ํ์ ๊ท์กฐ๋ฅ๋ฅผ 50g์ฉ ๋ด์ ์ง๊ณต๊ฑด์กฐ๊ธฐ์์ 48์๊ฐ ๊ฑด์กฐ๋ฅผ ํ์๊ณ , ์ดํ ๋ค์ํ ๊ณต์ ์ ์ํ ํ์ฝ์ํด์ ํจ๋๋ณํ๋ฅผ HPLC๋ฅผ ์ด์ฉํ์ฌ ์ธก์ ํ์๋ค.The separation and purification method was optimized by measuring the change in the content of fucoxanthin according to the separation and purification method. To this end, 50 g of diatoms in wet state were first put and dried in a vacuum dryer for 48 hours, and thereafter, the change in the content of fucoxanthin by various processes was measured using HPLC.
๋จผ์ , ํ์ค์ฉ์ก 1์ ๊ท์กฐ๋ฅ ์๋ฌผ์ 70% ์ฃผ์ ์ 2์๊ฐ ๋์ ๊ต๋ฐ ํ ๊ท์กฐํ ๋ก ์ฌ์ ์ฝํ
(precoat)๋ ์ฌ๊ณผ๋ฒ ๋(filter bed)์ loadingํ์ฌ ์ฌ๊ณผ ํ ๊ฐ์๋์ถ์ ์ค์ํ์๋ค. ์ด์ ๋ฐ๋ฅธ sample 1.2g์ ์ ์์ ์ธ๋ก ์นญ๋ํ์ฌ ์ค๋ฆฌ์นด ๊ฒ ์ปฌ๋ผ ํฌ๋ก๋งํ ๊ทธ๋ํผ(silica gel column chromatography, ฮฆ 3.5 cm x 15 cm)๋ฅผ ์ค์ํ์๊ณ , ์ฉ์ถ์ฉ๋งค๋ก๋ N-Hexane : Acetone = 70 : 30 ์ผ๋ก ํ๋ ค์ฃผ์๋ค. ๋ถ๋ฆฌ์ ์ ๋ ํ์ฝ์ํด์ methanol์ ๋
น์ฌ์ ๋๋ 0.1% ์ธ ํ์ค์ฉ์ก 1์ ์ ์กฐํ์๋ค. ์ด ํ, ํ์ค์ฉ์ก 1์ ํฌ๋ช
์ฉ๊ธฐ์ ๋ถ์ฃผํ๊ณ ํ์ฝ์ํด ํจ๋์ HPLC ๋ฐฉ๋ฒ์ผ๋ก ์ธก์ ํ์๋ค. ์๋ณํ๋ ๋ํ๋์ง ์์์ผ๋ฉฐ ํ์ฝ์ํด ํจ๋์ peak area ๊ฐ์ ๊ธฐ์ค์ผ๋ก ์ฐ์ถํ์๋ค. ํ๊ธฐ ํ์ค์ฉ์ก 2์ ๋น๊ตํ์์ ๋ ํ์ฝ์ํด ํจ๋์ด ๋์ ๊ฒ์ผ๋ก ๋ํ๋ฌ๊ณ , ๋ค๋ฅธ ์ฑ๋ถ๋ค์ ์ ๊ฑฐ๋์ด ์๋๊ฐ 90%๋ก ๋ํ๋ฌ๋ค(๋ 1).First,
๋ค์์ผ๋ก, ํ์ค์ฉ์ก 2๋ ์ฌ๊ฒฐ์ ๊ณต์ ์ ํตํ์ฌ ์ ์กฐํ์๋ค. ์จ๋๊ฐ ๋์ ์ฉ๋งค์ ์ฉ์ง์ ๋
น์ด๋ฉด ๋ฎ์ ์จ๋์์๋ณด๋ค ๋ ๋ง์ ์์ ์ฉ์ง์ ์ฉํด์ํฌ ์ ์๋ค. ์ด๋ ๊ฒ ์ฉํด๋์ด ์๋ ์ํ์์, ์จ๋๋ฅผ ๋ค์ ์ฒ์ฒํ ๋ด๋ฆฌ๋ฉด ์ฉํด๋๊ฐ ์์์ง๊ธฐ ๋๋ฌธ์ ์ฉ์ง์ ๋ค์ ์์ถ๋๋ฉด์ ๊ฒฐ์ ์ ์ด๋ฃจ๊ฒ ๋๋๋ฐ, ์ด๋ฅผ ์ฌ๊ฒฐ์ ์ด๋ผ ํ๋ค. ๋ณธ ๋ฐ๋ช
์์๋ 70% ์ฃผ์ ์ ๊ท์กฐ๋ฅ ์๋ฌผ 5g์ 2์๊ฐ ๋์ ๊ต๋ฐํ์ฌ ์ฌ๊ณผํ ํ, ์ฌ๊ฒฐ์ ์คํ์ ์ํด ์ฌ๊ณผ๋ sample์ ์ดํ๋์ -20โ๋ณด๊ดํ์ฌ ํ์ค์ฉ์ก 2๋ฅผ ์ ์กฐํ์๋ค. ์ด ํ ํ์ค์ฉ์ก 2๋ฅผ ํฌ๋ช
์ฉ๊ธฐ์ ๋ถ์ฃผํ๊ณ ํ์ฝ์ํด ํจ๋์ HPLC ๋ฐฉ๋ฒ์ผ๋ก ์ธก์ ํ์๋ค. ์๋ณํ๋ ๋ํ๋์ง ์์์ผ๋ฉฐ ํ์ฝ์ํด ํจ๋์ peak area ๊ฐ์ ๊ธฐ์ค์ผ๋ก ์ฐ์ถํ์๋ค. ํ์ค์ฉ์ก 1๊ณผ ๋น๊ตํ์ฌ, Chlorophyll ์ฑ๋ถ์ด ์ ๊ฑฐ๋์ง ์๋ํ์ฌ ๊ฒฐ์ sample ์ ์๋๊ฐ 75%, ๋ชจ์ก sample์ ์๋๊ฐ 61%๋ก ๋ํ๋ฌ๋ค(๋ 2, ๋ 3).Next,
ํ์ค์ฉ์ก 3์ ๊ท์กฐ๋ฅ ์๋ฌผ์ ๋ํ ํ์ผ๊ณต์ ์ ์ถ๊ฐํ ๊ฒ ์ด์ธ์๋ ํ์ค์ฉ์ก 1๊ณผ ๋์ผํ๊ฒ ์งํํ์ฌ ํ์ผ๊ณต์ ์ ํจ๊ณผ๋ฅผ ๊ฒ์ฆํ์๋ค. ํ์ค์ฉ์ก 3์ ํฌ๋ช
์ฉ๊ธฐ์ ๋ถ์ฃผํ๊ณ ํ์ฝ์ํด ํจ๋์ HPLC ๋ฐฉ๋ฒ์ผ๋ก ์ธก์ ํ์๋ค. ์๋ณํ๋ ๋ํ๋์ง ์์์ผ๋ฉฐ ํ์ฝ์ํด ํจ๋์ peak area ๊ฐ์ ๊ธฐ์ค์ผ๋ก ์ฐ์ถํ์๋ค. ๊ด์ฐฐ๋ ํ์ฝ์ํด ํจ๋์ ํ์ผ์ ์งํํ ๊ฒฝ์ฐ ํ์ค์ฉ์ก 1๊ณผ ๋น๊ตํ์ฌ 21% ์์ค์ผ๋ก ๋ฎ์์ก๊ณ , ํ์ผ์ ์งํํ์ง ์์ ๊ฒฝ์ฐ 17% ์์ค์ผ๋ก ๋ฎ์์ก๋ค(๋ 4, ๋ 5).
๋ค์ ํ์ค์ฉ์ก 4๋ ํ์ฝ์ํด์ด ํ๋น์ ๋
ธ์ถ๋ ๊ฒฝ์ฐ์ ํจ๋๋ณํ๋ฅผ ํตํ์ฌ ํ์ฝ์ํด์ ์์ ์ฑ์ ๊ฒ์ฆํ์๋ค. ํ์ค์ฉ์ก 4๋ฅผ ํฌ๋ช
์ฉ๊ธฐ์ ๋ถ์ฃผํ๊ณ ํ์ฝ์ํด ํจ๋์ HPLC ๋ฐฉ๋ฒ์ผ๋ก ์ธก์ ํ์๋ค. ์๋ณํ๋ ๋ํ๋์ง ์์์ผ๋ฉฐ ํ์ฝ์ํด ํจ๋์ peak area ๊ฐ์ ๊ธฐ์ค์ผ๋ก ์ฐ์ถํ์๋ค. ์ผ์ฃผ์ผ ๋์ ํ๋น์ ๋ฐฉ์น ํ ํ์ฝ์ํด์ ํจ๋๊ณผ ์๋๋ฅผ ๊ด์ฐฐํ ๊ฒฐ๊ณผ ํจ๋์ ์ฝ 82% ๊ฐ์ํ์๊ณ , ์๋๋ 90%์์ 55%๋ก ๊ฐ์ํ์๋ค(๋ 6).The following
๊ฒฐ๋ก ์ ์ผ๋ก ํ์ฝ์ํด ์กฐ์ ๋ฌผ์ 0.1% ๋๋๋ก ๋ฉํ์ฌ์ ์ฉํดํ ๊ฒ์ HPLC ๋ถ์ํ ๊ฒฐ๊ณผ ํ์ค์ฉ์ก 1์ด ํจ๋๊ณผ ์๋๋ฉด์์ ์ฐ์ํ ๊ฒ์ผ๋ก ๋ํ๋ฌ์ผ๋ฉฐ, ์ค๋ฆฌ์นด ๊ฒ ์ปฌ๋ผ ํฌ๋ก๋งํ ๊ทธ๋ํผ๋ฅผ ์ค์ํ์ง ์์์ ๋์๋ ๋ถ๋ฆฌ์ ์ ๊ฐ ์ ๋๋ก ๋์ง ์๋ํ์ฌ ํ์ฝ์ํด์ ํจ๋ ๋ฐ ์๋๊ฐ ๋ฎ์์ง๋ ๊ฒ์ผ๋ก ๋ํ๋ฌ๋ค. ๋ํ ํ์ผ๊ณต์ ์ ํ์ฝ์ํด ํจ๋๊ณผ ์๋์ ํฌ๊ฒ ์ํฅ์ ๋ฏธ์น์ง ์๋ ๊ฒ์ผ๋ก ํ์ธ๋์๊ณ , ๋ํ ์ฌ๊ฒฐ์ ๊ณต์ ๋ ํ์ค์ฉ์ก 1๊ณผ ๋น๊ตํ์ฌ ํ์ฝ์ํด์ ์๋ ๋ฐ ํจ๋์ด ๋ค์ ๋ฎ์์ง๋ ๊ฒฐ๊ณผ๋ฅผ ํ์ธํ ์ ์์๋ค. ๋์๊ฐ ํ์ฝ์ํด์ ํ๋น ๋
ธ์ถ์ ๋ฏผ๊ฐํ๊ฒ ์์ฉํ๋ ๊ฒ์ ํ์ค์ฉ์ก 4์์ ํ์ธํ ์ ์์๋ค. In conclusion, as a result of HPLC analysis of a fucoxanthin preparation dissolved in methanol at a concentration of 0.1%,
์ค์์ 2. ํ์ฝ์ํด ์ถ์ถ์ ์์ด์ ์ ์ ์ฉ๋งค์ ๊ฒฐ์ Example 2. Determination of a suitable solvent for fucoxanthin extraction
ํ์ฝ์ํด์ ๋ถ๋ฆฌ์ ์์ด์ ๋์ข ์ ๋ฏธ์ธ์กฐ๋ฅ ๋ถ๋ง์ ์ฉ๋งค์ถ์ถ์ ์ฃผ์ ์ ์ฌ์ฉํ์์ ๊ฒฝ์ฐ ๊ฐ์ฅ ์ถ์ถ์์จ์ด ๋์๋ค๋ ๊ฒฐ๊ณผ์, ์ฉ๋งค๋ฅผ ์ฃผ์ ๋ก ํ์์ ๊ฒฝ์ฐ ๊ธฐํ ์ถ์ถ๋ฐฉ๋ฒ(Sohxlet๋ฒ, ์ด์ํ์ถ์ถ๋ฒ, ์์๊ณ ์ถ์ถ๋ฒ ๋ฑ)์ ์ฌ์ฉํ ๊ฒ๊ณผ ํฌ๊ฒ ๋ค๋ฅด์ง ์์๋ค๋ ๊ฒฐ๊ณผ ๋ฐ ์ํ์ ํ์ฉํ ์ ์๋ค๋ ์ ๋ฑ์ ๊ณ ๋ คํ์ฌ, 70% ์ฃผ์ ์ ์ถ์ถ์ฉ๋งค๋ก ํ์๋ค. In the separation of fucoxanthin, the solvent extraction of the same type of microalgal powder showed the highest extraction yield when alcohol was used, and other extraction methods (Sohxlet method, ultrasonic extraction method, subcritical extraction method, etc.) 70% alcohol was used as the extraction solvent in consideration of the result that it was not significantly different from the use of alcohol and the fact that it can be used in food.
๋ค๋ง, ์ถ์ถ์ฉ๋งค์ ์ฌ์ฉ๋์ ํฅํ ์ฐ์
ํ ๊ณผ์ ์์ ์์ฐ๋จ๊ฐ ๊ฒฐ์ ์ ์ค์ํ ์์๊ฐ ๋๋ฏ๋ก ์ฐ์ ๊ท์กฐ๋ฅ ์๋ฌผ ๋๋น ์ ์ ์ฉ๋งค๋น์จ์ ์คํํ์๋ค. ๊ท์กฐ๋ฅ ๋ถ๋ง 100g(sample No 1, 2, 3)์ 10๋ฐฐ์ 70% ์ฃผ์ ์ ๊ต๋ฐํ๊ณ , 50g(No. 4, 5, 6)์ ๊ฐ๊ฐ 10๋ฐฐ, 20๋ฐฐ, 30๋ฐฐ์ 70% ์ฃผ์ ์ ๊ต๋ฐํ์ฌ ์ถ์ถํจ์จ์ ๋น๊ตํ์ฌ ๋ํ๋ด์๋ค(ํ 1, ๋ 7 ๋ด์ง ๋ 9)However, since the amount of extraction solvent used is an important factor in determining the production cost in the future industrialization process, an appropriate solvent ratio compared to the raw material for diatoms was first tested. 10
(โป No.1-3; 70% ์ฃผ์ 10x ์ฌ์ก, No.4; 70% ์ฃผ์ 10x ์ฌ์ก, No.5; 70% ์ฃผ์ 20x ์ฌ์ก, No.6; 70% ์ฃผ์ 30x ์ฌ์ก)(โป No.1-3; 70% alcohol 10x filtrate, No.4; 70% alcohol 10x filtrate, No.5; 70% alcohol 20x filtrate, No.6; 70% alcohol 30x filtrate)
10๋ฐฐ ์ฉ๋์ ์ฃผ์ ๋ก ์ถ์ถํ ๊ตฌ๊ฐ์์๋ ์ด 250mg, 20๋ฐฐ ์ฉ๋์์๋ 274mg, 30๋ฐฐ ์ฉ๋์์๋ 260mg์ ํ์ฝ์ํด์ด ์ถ์ถ๋์ด ์ฃผ์ ์์ด ๋์ด๋จ์ ๋ฐ๋ผ ์ถ์ถํจ์จ์ด ์ํญ ์ฆ๊ฐํ์์ง๋ง ๊ทธ ์ฐจ์ด๋ 10% ๋ด์ธ์ด๋ฏ๋ก ์ ์ ์ถ์ถ ์ฉ๋งค๋์ 10๋ฐฐ์ 70% ์ฃผ์ ์ ๊ธฐ์ค์ผ๋ก ์งํํ์๋ค. ๋ค๋ง, ๋์ฑ ์ ํํ ์ฉ๋งค์กฐ๊ฑด์ ๊ฒฐ์ ํ๊ธฐ ์ํ์ฌ ์ถ๊ฐ์คํ์ ์งํํ์๊ณ , ๊ทธ ๊ฒฐ๊ณผ๋ ํ๊ธฐ ์ค์์ 9์ ๋ํ๋ด์๋ค. In the section extracted with 10 times the volume of alcohol, a total of 250 mg, at 20 times, 274 mg, and at 30 times, 260 mg of fucoxanthin were extracted. The extraction efficiency slightly increased as the amount of alcohol increased, but the difference was around 10%, so proper extraction The amount of solvent was carried out on the basis of 10
์ค์์ 3. ํ์ฝ์ํด ๋ถ๋ฆฌ์ ์ Example 3. Separation and purification of fucoxanthin
ํ์ฝ์ํด ๋ฑ์ ๊ธฐ๋ฅ์ฑ ๋ฌผ์ง์ ๋ถ๋ฆฌ์ ์ ์๋ ์ค๋ฆฌ์นด ๊ฒ ํฌ๋ก๋งํ ๊ทธ๋ํผ(silica gel chromatography)๊ฐ ์ด์ฉ๋๊ณ ์๋๋ฐ, ์ฌ๋ฌ ๊ฐ์ง ํํฉ๋ฌผ๋ค์ ๋ฌผ๋ฆฌ ํํ์ ํน์ฑ์ ์ํ silica gel ์ปฌ๋ผ ๋ด์์์ ์ด๋๋์ ์ฐจ์ด์ ๋ฐ๋ผ ๋ถ๋ฆฌ๋๋ ์ฑ์ง์ ์ด์ฉํ ๊ฒ์ด๋ค. ๋ณธ ๋ฐ๋ช ์์๋ ๋ชฉํ๋ฌผ์ง์ธ ํ์ฝ์ํด์ ํจ์จ์ ์ผ๋ก ๋ถ๋ฆฌ์ ์ ํ๊ธฐ ์ํ์ฌ ๋ค์ํ ์กฐ๊ฑด์์์ ์ค๋ฆฌ์นด ๊ฒ ํฌ๋ก๋งํ ๊ทธ๋ํผ๋ฅผ ์ํํ์๋ค.Silica gel chromatography is used for separation and purification of functional substances such as fucoxanthin. will be. In the present invention, silica gel chromatography was performed under various conditions to efficiently separate and purify fucoxanthin, a target material.
์ ์ฒด๊ณผ์ ์ ๋ 10์ ๋ฐ๋ผ ๊ท์กฐ๋ฅ ๋ถ๋ง์ 10๋ฐฐ ์ฉ๋์ 70% ์ฃผ์ ์ ๋ฃ๊ณ 2์๊ฐ ๊ต๋ฐ ํ ์ฌ๊ณผํ์ฌ ๊ฐ๊ฐ์ ์ถ์ถ๋ฌผ์ ์ป๊ณ ๋ถํ๊ณผ์ , ๋์ถ๊ณผ์ ์ ๊ฑฐ์น ํ ์ค๋ฆฌ์นด ๊ฒ ํฌ๋ก๋งํ ๊ทธ๋ํผ๋ก ๋ถ๋ฆฌํ์๋ค.As for the whole process, according to FIG. 10, 70% alcohol in a 10-fold volume was added to the diatom powder, stirred for 2 hours, filtered to obtain each extract, and fractionation process and concentration process were performed, and then separated by silica gel chromatography.
๊ตฌ์ฒด์ ์ผ๋ก, ๋จผ์ ๊ท์กฐ๋ฅ ๋ถ๋ง 100g์์ 10๋ฐฐ ์ฉ๋์ 70% ์ฃผ์ ์ผ๋ก ์ถ์ถํ ์ถ์ถ์ก์ 5um ์ฌ๊ณผ์ง๋ก ํํฐ๋งํ์ฌ ์ป์ 1์ฐจ ์ฃผ์ ์ถ์ถ๋ฌผ์ n-Hexane : 70% ์ฃผ์ (1:1)๋ก ๋ถ๋ฆฌํ์ฌ ์๋์ธต์ 70% ์ฃผ์ ๋ถํ๋ฌผ์ ์ป์๋ค. ์๊ธฐ ๋ถํ๋ฌผ์์ ํ์ฝ์ํด์ ๋ถ๋ฆฌํ๊ธฐ ์ํ์ฌ, ์ปฌ๋ผ์ silica๋ฅผ ์ถฉ์งํ์ฌ ์ํ์ loadingํ๊ณ , gradient (Hexane:Acetone=7:3โ6:4โ5:5โAcetone) ๋ถ๋ฆฌ๊ณผ์ ์ ์ํํ์ฌ ์ต์ข ๋ถํ๋ฌผ๋ค์ ์ป์๋ค. ์ด ํ, ํ์ฝ์ํด์ ํฌํจํ๊ณ ์๋ค๊ณ ์์๋์ด์ง๋ ๋ถํ๋ฌผ(์งํ ์ฃผํฉ์์ธต)์ ํ๋ณดํ์ฌ TLC(Thin Layer Chromatography)๋ฅผ ์ํํ์๊ณ (๋ 11, 12), ๊ทธ ๊ฒฐ๊ณผ Fraction No.1์์ No.9๊น์ง์ ๋ถํ๋ฌผ์์ ํ์ฝ์ํด์ด ๋ถ๋ฆฌ๋์์์ ํ์ธํ๊ณ ๊ณ ์์ง๊ณต๋์ถ๊ธฐ๋ฅผ ์ด์ฉํ์ฌ ๋์ถ๊ณผ์ ์ ์งํํ์๋ค(๋ 13).Specifically, the primary alcohol extract obtained by first filtering the extract extracted from 100 g of diatom powder with 70% alcohol at 10 times the volume with 5um filter paper was separated into n-Hexane: 70% alcohol (1:1), and 70% alcohol in the lower layer A fraction was obtained. In order to separate fucoxanthin from the fraction, silica was filled in a column to load a sample, and a gradient (Hexane:Acetone=7:3โ6:4โ5:5โAcetone) separation process was performed to obtain final fractions. . After that, a fraction (dark orange layer) that is expected to contain fucoxanthin was obtained and TLC (Thin Layer Chromatography) was performed (FIGS. 11 and 12), and as a result, fractions from Fraction No. 1 to No. 9 It was confirmed that fucoxanthin was separated from the , and the concentration process was performed using a high pressure vacuum concentrator (FIG. 13).
์ค์์ 4. HPLC๋ฅผ ์ด์ฉํ ํ์ฝ์ํด ์ ๋๋ถ์Example 4. Quantitative analysis of fucoxanthin using HPLC
๋จผ์ , ํ์ค๋ฌผ์ง ํ์ฝ์ํด(Sigma Aldrich๋ก ๋ถํฐ ๊ตฌ์ )์ ์ด์ฉํ์ฌ ๋๋๋ณ๋ก ํฌ์ํ์ฌ HPLC ํ์ค๊ฒ๋์ ์ ์์ฑํ์๋ค(๋ 14). HPLC ๋ถ์์, Waters 2695 HPLC ์ฅ๋น๋ฅผ ์ฌ์ฉํ์๊ณ , ์ฌ์ฉ์นผ๋ผ์ Kromasil 100-5-C18 (4.6x250mm, 5um), ๊ฒ์ถํ์ฅ์ 450nm, ์ฉ๋งค๋ Acetonitrile / water๋ฅผ ์ฌ์ฉํ์๋ค(ํ 2).First, the standard material fucoxanthin (purchased from Sigma Aldrich) was diluted by concentration to prepare an HPLC standard calibration curve (FIG. 14). For HPLC analysis, Waters 2695 HPLC equipment was used, the column used was Kromasil 100-5-C18 (4.6x250mm, 5um), the detection wavelength was 450 nm, and the solvent was Acetonitrile / water (Table 2).
HPLC ์ ๋๋ถ์๊ฒฐ๊ณผ, 100g์ ๊ท์กฐ๋ถ๋ง์ 70% ์ฃผ์ ์ถ์ถ๋ฌผ๋ก๋ถํฐ ๋ถํ/๋์ถ๊ณผ์ ์ ํตํ์ฌ ์ต์ข ์ ์ผ๋ก ์๋ 60%์ ํ์ฝ์ํด 8.7g์ ์ป์์ผ๋ฉฐ ๊ฒฐ๊ณผ์ ์ผ๋ก 5.22%์ ์์จ์ ๋ํ๋ด์๋ค(๋ 15).As a result of quantitative HPLC analysis, 8.7 g of fucoxanthin having a purity of 60% was finally obtained through a fractionation/concentration process from a 70% alcohol extract of 100 g of diatom powder, and as a result, a yield of 5.22% was obtained (FIG. 15).
์ค์์ 5. ์ฌ๊ฒฐ์ ํ ๋ฐฉ๋ฒ์ ์ ์ฉ์ฑ ์คํExample 5. Utility test of recrystallization method
ํ์ฝ์ํด์ ์ ์ ๋ ๋ฐ ์์จ์ ํฅ์์ํค๊ธฐ ์ํ์ฌ ๋์ถ๋ฌผ์ ์ฌ๊ฒฐ์ ํ์ ์ ์ฉ์ฑ์ ๊ฒํ ํ์๋ค. ๊ตฌ์ฒด์ ์ผ๋ก, ๊ท์กฐ ๋ถ๋ง 100g์ 10๋ฐฐ ์ฉ๋์ 70% ์ฃผ์ ๋ก 2์๊ฐ ๊ต๋ฐํ์ฌ ์ป์ 1์ฐจ์ถ์ถ๋ฌผ์, 50g์ ๊ท์กฐํ ๋ก ์ฝํ ํ ์ฌ๊ณผ๋ฒ ๋์ loadingํ์ฌ ์ถ์ถ๋ฌผ ์ฌ์ก์ ์ป์๋ค. ์ต์ข ์ ์ผ๋ก ์ป์ ๋์ถ๋ฌผ์ acetone์ผ๋ก ์ฉํด์์ผ ์ค๋ฆฌ์นด ๊ฒ ํฌ๋ก๋งํ ๊ทธ๋ํผ๋ก ํ์ฝ์ํด ๋ถํ๋ฌผ์ ์ํ๋งํ๊ณ , TLC(Thin Layer Chromatography)๋ก ์ฒดํฌํ์ฌ ํ์ฝ์ํด์ด ๋ถ๋ฆฌ๋์์์ ํ์ธํ์๋ค(๋ 16). The usefulness of recrystallization of the concentrate to improve the degree of purification and yield of fucoxanthin was studied. Specifically, the primary extract obtained by stirring 100 g of diatomaceous powder with 70% alcohol at 10 times the volume for 2 hours was loaded into a filter bed coated with 50 g of diatomaceous earth to obtain an extract filtrate. The finally obtained concentrate was dissolved in acetone, and the fucoxanthin fraction was sampled by silica gel chromatography, and it was checked by TLC (Thin Layer Chromatography) to confirm that the fucoxanthin was separated (FIG. 16).
์๊ธฐ ํ์ฝ์ํด ๋ถํ๋ฌผ๋ก๋ถํฐ ์ฌ๊ฒฐ์ ํ๋ฅผ ์๋ํ์๋๋ฐ, ์ฌ๊ฒฐ์ ํ ๊ณผ์ ์ ๋ค์๊ณผ ๊ฐ๋ค. ์๋ฃ์ ๋๋์ 50โ์ ๋ฌผ์ ์๊ณ 40โ์์ 2์๊ฐ ๊ต๋ฐํ ํ, -20โ์์ overnight ๋ณด๊ดํ๊ณ , ์ฌ๊ณผ๋ฅผ ํตํด ์ฌ๊ฒฐ์ ํ๋ฅผ ์งํํ์๋ค. ํ์ฝ์ํด์ ๊ฒฐ์ ์ ํ๋ฏธ๊ฒฝ ๊ด์ฐฐ(400๋ฐฐ์จ)์ ํตํด ํ์ธํ์์ผ๋ฉฐ(๋ 17), ์๊ธฐ ์กฐ๊ฑด์ผ๋ก HPLC ์ ๋๋ถ์์ ์ํํ์๋ค(๋ 18). ๊ทธ ๊ฒฐ๊ณผ, ์ฌ๊ฒฐ์ ํ๋ฅผ ํตํด ํ์ฝ์ํด ๋์ถ์ด ๊ฐ๋ฅํ๊ฒ ๋์์ง๋ง, ๋ชฉ์ ํ๋ ๊ณ ์๋์ ํ์ฝ์ํด์ ๋ถ๋ฆฌํ๋๋ฐ๋ ์ ์ฉ์ฑ์ด ํฌ์ง ์๋ค๋ ๊ฒ์ ํ์ธํ ์ ์์๋ค.Recrystallization was attempted from the fucoxanthin fraction, and the recrystallization process is as follows. The sample was mixed with the same amount of water at 50ยฐC, stirred at 40ยฐC for 2 hours, stored at -20ยฐC overnight, and recrystallized through filtration. The crystals of fucoxanthin were confirmed through microscopic observation (400 magnification) (FIG. 17), and HPLC quantitative analysis was performed under the above conditions (FIG. 18). As a result, although it was possible to concentrate fucoxanthin through recrystallization, it was confirmed that the usefulness was not great for isolating the desired high-purity fucoxanthin.
์ค์์ 6. ๋ค์ํ ๋ฐฐ์/ํ๊ฒฝ ์กฐ๊ฑด์์์ ํ์ฝ์ํด ํจ๋๋น๊ตExample 6. Comparison of fucoxanthin content in various culture/environmental conditions
๊ท์กฐ ๋ฐฐ์ํ๊ฒฝ, ํด์์ผ ์ ๊ฑฐ์ ๋ฌด, ๊ฑด์กฐํํ, ๊ฑด์กฐ์จ๋ ๋ฑ์ ๋ฐ๋ฅธ ๊ท์กฐ์์์ ํ์ฝ์ํด ํจ๋๋ณํ๋ฅผ ๋น๊ต๋ถ์ ํ์๋ค(๋ 19 ๋ด์ง 22, ํ 3).Changes in fucoxanthin content in diatoms according to the diatom culture environment, sea salt removal, drying type, drying temperature, etc. were comparatively analyzed ( FIGS. 19 to 22 , Table 3).
(โป No.1; ๋ฐ๋ฅ๊ท์กฐ/ํ์ผX/์์ฐ๊ฑด์กฐ, No.2; ๋ฐ๋ฅ๊ท์กฐ/ํ์ผ/60โ๊ฑด์กฐ, No.3; ๋ถ์๊ท์กฐ/ํ์ผX/๋ํด๋/์์ฐ๊ฑด์กฐ, No.4; ๋ถ์๊ท์กฐ/ํ์ผ/60โ๊ฑด์กฐ, No.5; ๋ฐ๋ฅ๊ท์กฐ/ํ์ผ2/์์ฐ๊ฑด์กฐ, No.7 ๋ถ์๊ท์กฐ/40โ์ดํ๊ฑด์กฐ, No.8-11; ๋ฒ ํ์ฌ์ดํด๋ก๋ฑ์คํธ๋ฆฐ ์ ํ๋ถ๋ง, No.12-14; ๊ฑด์กฐ๋ถ๋ง/1,3BG์ถ์ถ/10x,7x,10x, No.15; Fresh Diatom/1,3BG์ถ์ถ 10x, No.16; Fresh Diatom/์ฃผ์ ์ถ์ถ 10x)(โป No.1; Bottom diatom/Desalted X/Naturally dry, No.2; Bottom Diatom/Demineralized/60โ drying, No.3; Floating diatom/Demineralized X/Cold thaw/Naturally dry, No.4; Floating diatom /Desalting / 60โ drying, No.5; Bottom diatom /
HPLC๋ถ์์ ์๊ธฐ ์ค์์์ ๋์ผํ ์กฐ๊ฑด์ผ๋ก ๋ถ์ํ์์ผ๋ฉฐ, ๊ท์กฐ๋ฅ ๊ฑด์กฐ๋ถ๋ง(No.1 ๋ด์ง No.11)์ 50mg/mL์ ๋๋๋ก methanol์ ์ฉํด, 30๋ถ๊ฐ ์ด์ํ ์ฒ๋ฆฌ, filteringํ ๋ถ์์ ์ด์ฉํ์์ผ๋ฉฐ, ๋ถ์์ 3ํ ๋ฐ๋ณต ์ํํ์๋ค. ๊ทธ ๊ฒฐ๊ณผ, ๊ท์กฐ ์์กํ๊ฒฝ์ ์์ด์, ๋ฐ๋ฅ๊ท์กฐ๊ฐ ๋ถ์๊ท์กฐ๋ณด๋ค ํ์ฝ์ํด ํจ๋์ด ๋์ ๊ฒ์ผ๋ก ๋ํ๋ฌ์ผ๋ฉฐ (ํ 3, No.1 & No.3), ํ์ผ์ ์ ๋ฌด๋ ํจ๋๋ณํ์ ํฌ๊ฒ ์ํฅ์ ๋ฏธ์น์ง ์๋ ๊ฒ์ผ๋ก ๋ํ๋ฌ๋ค.HPLC analysis was performed under the same conditions as in Example, and dry diatom powder (No. 1 to No. 11) was dissolved in methanol at a concentration of 50 mg/mL, sonicated for 30 minutes, filtered, and then used for analysis. This was repeated 3 times. As a result, in the diatom growth environment, the bottom diatom showed a higher fucoxanthin content than the floating diatom (Table 3, No. 1 & No. 3), and the presence or absence of desalination did not significantly affect the content change. appear.
ํํธ, ๊ฑด์กฐ์จ๋์ ๋ฐ๋ฅธ ํ์ฝ์ํด ํจ๋๋ณํ๋ฅผ ๋ถ์ํ ๊ฒฐ๊ณผ, ์์ฐ๊ฑด์กฐ์ ๋นํด ๊ฑด์กฐ์จ๋๊ฐ 50โ ์ด์์ ์กฐ๊ฑด์์๋ ํ์ฝ์ํด ํจ๋์ด ํฌ๊ฒ ๊ฐ์ํ๋ ๊ฒ์ผ๋ก ๋ํ๋ฌ๋ค (ํ 3, No.1 ๋ด์ง No.5). ์ด ๊ฒฐ๊ณผ๋ ํ์ฝ์ํด์ด ์ด ์์ ์ฑ์ด ๋ฎ๋ค๋ ๊ธฐ์กด ์ฐ๊ตฌ๊ฒฐ๊ณผ๋ค๊ณผ ์ผ์นํ๋ฉฐ, ํ์ฝ์ํด์ ์ฐ์ ์ ์ผ๋ก ์์ฐํ ๊ฒฝ์ฐ 50โ์ดํ์ ํ๊ฒฝ ๋ฐ ์ถ์ถ์กฐ๊ฑด์ ์ค์ ํ๋ ๊ฒ์ด ์ค์ํ๋ค๋ ๊ฒ์ ์์ฌํ๋ค. On the other hand, as a result of analyzing the change in the fucoxanthin content according to the drying temperature, it was found that the fucoxanthin content was significantly reduced in the condition of the drying temperature of 50ยฐ C. or higher compared to natural drying (Table 3, No. 1 to No. 5). This result is consistent with the existing research results that fucoxanthin has low thermal stability, and suggests that it is important to set the environment and extraction conditions below 50ยฐC for industrial production of fucoxanthin.
๋ถ์ํ ์๋ฃ ์ค ํ์ฝ์ํด ํจ๋์ด ๊ฐ์ฅ ๋์ ๊ฒ์ ๊ฑด์กฐ์ํค์ง ์์ ๊ท์กฐ์๋ฌผ ์๋ฃ๋ก์จ, ์ด ๊ฒฐ๊ณผ๋ ๊ท์กฐ๋ฐฐ์๋ฌผ์ ์๊ฑฐ, ๊ฑด์กฐ(์์ฐ๊ฑด์กฐ ๋๋ ์ดํ๊ฑด์กฐ)๊ณผ์ ์์ ๊ท์กฐ๋ด์ ํ์ฝ์ํด์ด ์ผ๋ถ ๋ถํด๋์๋ค๋ ๊ฒ์ ๋ํ๋ธ๋ค (No. 15, 16). ๊ฒฐ๋ก ์ ์ผ๋ก, ํ์ฝ์ํด์ ๋๋ ์ถ์ถ๊ณต์ ํ๋ฆฝ์ ์์ด์ ์ต์ด๋จ๊ณ์ธ ๊ท์กฐ์ ์ํ/๊ฐ๊ณต๋จ๊ณ๋, ๊ฑด์กฐ๊ณต์ ์ ๊ฑฐ์น์ง ์๊ณ ๊ท์กฐ ์๋ฌผ ์์ฒด๋ฅผ ๊ทธ๋๋ก ์ํํ์ฌ ๊ณง๋ฐ๋ก ์ถ์ถ๊ณต์ ์ผ๋ก ์ง์ ํ๋ ๊ฒ์ด ๊ฐ์ฅ ํจ์จ์ ์ธ ๊ณต์ ์ด๋ค.Among the analyzed samples, the diatomite sample that had the highest content of fucoxanthin was an undried diatomite sample. This result indicates that some of the fucoxanthin in the diatom was decomposed during the collection and drying (natural drying or hot air drying) process of the diatom culture ( No. 15, 16). In conclusion, in the first step in establishing the mass extraction process for fucoxanthin, the harvesting/processing step of diatom, it is the most efficient process to directly harvest the raw diatom without going through the drying process and directly enter the extraction process.
์ค์์ 7. ํ์ฝ์ํด์ ์ ํํExample 7. Formulation of fucoxanthin
1์ฐจ ์ฃผ์ ์ถ์ถ๋ฌผ์ ์ ์กฐํ์ฌ ์ฌ๊ณผ ํ ๋์ถ๊ณผ์ ์ ๊ฑฐ์ณ ์ป์ด์ง ๋์ถ๋ฌผ์, ๋ฒ ํ์ฌ์ดํด๋ก ๋ฑ์คํธ๋ฆฐ์ ๋๋ ๋ฐ 30%์ฉ ์ฆ๊ฐ์ํจ ์์ ์ฒจ๊ฐํ์ฌ ๋ฐ์ฃฝ์ ๋ง๋ ํ 72์๊ฐ ๋๊ฒฐ๊ฑด์กฐ๋ฅผ ์งํํ์๋ค. ๋๊ฒฐ๊ฑด์กฐ๋ ์๋ฃ๋ฅผ ๋ถ์ํ์ฌ ๋ถ๋ง์ ํ์ ์ ์กฐํ๊ณ , ๊ฐ ์๋ฃ์์์ ํ์ฝ์ํด ํจ๋์ ๋ถ์ํ์๋ค (๋ 23 ๋ด์ง 27, ํ 3 No.8 ๋ด์ง 11). ๋ถ์๊ฒฐ๊ณผ, ๋ฑ์คํธ๋ฆฐ ์ฒจ๊ฐ๋์ ๋ณํ์ ๋ฐ๋ฅธ ํ์ฝ์ํด ํจ๋์๋ ํฐ ์ฐจ์ด๋ฅผ ๋ณด์ด์ง ์์์ผ๋ฉฐ, ํ ์๋ฃ๋ณด๋ค 5๋ฐฐ ๋์ถํ ๋์ถ์ก์ ๋๋์ ๋ฑ์คํธ๋ฆฐ์ ์ฒจ๊ฐํ ์๋ฃ(No.8)์์๋ ๊ฐ์ฅ ๋์ 316ppm (0.6%)์ ๋ํ๋ด์์ง๋ง ๋ค๋ฅธ ์๋ฃ์ ๋นํด ์์ ๋ฐ ํฅ์ ์์ด์ ๋ฌธ์ ์ ์ ๋ํ๋๋ค. ๊ฒฐ๋ก ์ ์ผ๋ก, ์ํ์ผ๋ก์ ์ ํ์ ๋ถํ์ ์ธ ๋ฒ ํ์ฌ์ดํด๋ก ๋ฑ์คํธ๋ฆฐ์ ์ต์๋ก ์ฒจ๊ฐํ๋ ์กฐ๊ฑด ์ฆ, ์ถ์ถ๋ฌผ ๋์ถ์ก๊ณผ ๋๋(1:1)์ ๋ฑ์คํธ๋ฆฐ์ ์ฒจ๊ฐํ์ฌ ์ ์กฐํ๋ ๊ฒ์ด ๊ฐ์ฅ ํจ์จ์ ์ธ ๋ฐฉ๋ฒ์์ ํ์ธํ ์ ์๋ค.To the concentrate obtained by preparing the primary alcohol extract, filtering and concentrating, the same amount of beta-cyclodextrin and 30% increments were added to make a dough, followed by freeze-drying for 72 hours. A powder formulation was prepared by pulverizing the freeze-dried sample, and the content of fucoxanthin in each sample was analyzed (FIGS. 23 to 27, Table 3 No. 8 to 11). As a result of the analysis, there was no significant difference in fucoxanthin content according to the change in the amount of dextrin added, and the highest 316ppm (0.6%) was obtained in the sample (No.8) in which the same amount of dextrin was added to the
์ค์์ 8. ํ๋ผ์ฆ๋ง ์ฒ๋ฆฌ์ ๋ฐ๋ฅธ ํ์ฝ์ํด ์ถ์ถํจ์จ ๋ถ์Example 8. Analysis of fucoxanthin extraction efficiency according to plasma treatment
์๋ฌผ ๊ท์กฐ(Fresh Diatom)์์ ํ์ฝ์ํด์ ์ถ์ถํ๋๋ฐ ์์ด์, ํ๋ผ์ฆ๋ง ์ฒ๋ฆฌ ์ ๋ฌด์ ๋ฐ๋ฅธ ํ์ฝ์ํด์ ์ถ์ถํจ์จ์ ๋น๊ต ๋ถ์ํจ์ผ๋ก์จ ์ต์ ์ ์ถ์ถ์กฐ๊ฑด์ ๊ฒฐ์ ํ์๋ค.In extracting fucoxanthin from fresh diatom, the optimal extraction conditions were determined by comparing and analyzing the extraction efficiency of fucoxanthin according to the presence or absence of plasma treatment.
๋จผ์ , ์๋ฌผ๊ท์กฐ์ ํ๋ผ์ฆ๋ง๋ฅผ ์ฒ๋ฆฌํ ๊ฒ๊ณผ ์ฒ๋ฆฌํ์ง ์์ ์๋ฃ๋ก ๋ถํฐ ์ถ์ถ๋ฌผ์ ์กฐ์ ํ์ฌ ํ์ฝ์ํด ์ถ์ถ์์จ์ ๋น๊ตํ์๋ค. ์๋ฌผ๊ท์กฐ 5g์ 20mL์ 70%์ฃผ์ ์ ์ฒจ๊ฐํ์ฌ 25๋ถ๊ฐ plasma๋ฅผ ์ฒ๋ฆฌํ ํ 40โ์์ 3์ผ๊ฐ ์ถ์ถํ๊ณ , ์ถ์ถ์ก์ 3500rpm์์ 10๋ถ๊ฐ ์์ฌ๋ถ๋ฆฌ ํ์ฌ ์ถ์ถ์์ฌ๋ฅผ ์ ๊ฑฐ, ์์ธต์ ์ถ์ถ์ก์ ์ด์ฉํ์ฌ HPLC ๋ถ์์ ์ํํ์๊ณ , ๋์กฐ๊ตฐ์ผ๋ก์จ, ์๊ธฐ์ ๋์ผํ ์ถ์ถ์กฐ๊ฑด์์, ํ๋ผ์ฆ๋ง ์ฒ๋ฆฌ๋ฅผ ํ์ง ์์ ์๋ฃ๋ฅผ ๋์กฐ๊ตฐ์ผ๋ก ์ค์ ํ์๋ค. ์ถ์ถ์ก์ด ์๋์ธ ๊ด๊ณ๋ก ์ฌ๊ณผ๊ณผ์ ์ ๊ฑฐ์น์ง ์๊ณ ์์ฌ๋ถ๋ฆฌ๋ฅผ ์ด์ฉํ์ฌ ์์ฌ๋ฅผ์ ๊ฑฐ ํ ํ ์ถ์ถ์ก์ ์ป์๊ณ (ํ 4), ํ๋ผ์ฆ๋ง ์ฒ๋ฆฌ์ ๋ฐ๋ฅธ ํ์ฝ์ํด ์ถ์ถํจ์จ์ HPLC ๋ถ์์ ํตํ์ฌ ๊ฒํ ํ์๋ค(ํ 5).First, extracts were prepared from samples treated with plasma and untreated biodiatoms to compare the extraction yield of fucoxanthin. After adding 20 mL of 70% alcohol to 5 g of biological diatom, plasma was treated for 25 minutes, extracted at 40 ยฐ C for 3 days, the extract was centrifuged at 3500 rpm for 10 minutes to remove the extraction residue, and HPLC analysis was performed using the extract of the upper layer. As a control, a sample that was not subjected to plasma treatment under the same extraction conditions as above was set as a control. Since the extract was small, the extract was obtained after removing the residue by centrifugation without going through a filtration process (Table 4), and the fucoxanthin extraction efficiency according to plasma treatment was reviewed through HPLC analysis (Table 5).
* NP:ํ๋ผ์ฆ๋ง ๋ฌด์ฒ๋ฆฌ, Pla:ํ๋ผ์ฆ๋ง ์ฒ๋ฆฌ * NP: no plasma treatment, Pla: plasma treatment
์๊ธฐ ํ์ ๋ฐ๋ฅด๋ฉด, ํ๋ผ์ฆ๋ง๋ฅผ ์ฒ๋ฆฌํ์ง ์์ ์๋ฃ์์๋ 1.08mg์ด ์ถ์ถ๋ ๋ฐ๋ฉด, ํ๋ผ์ฆ๋ง๋ฅผ ์ฒ๋ฆฌํ ์๋ฃ์์๋ 1.22mg์ด ์ถ์ถ๋์ด, ํ๋ผ์ฆ๋ง ์ฒ๋ฆฌ์ ์ํด ์ฝ 13%์ ์ถ์ถํจ์จ์ด ์ฆ๊ฐ๋์์์ ํ์ธํ์๋ค. ์ด๋ ์๋ฃ์ ํ๋ผ์ฆ๋ง ์ฒ๋ฆฌ๋ฅผ ํจ์ผ๋ก์จ ๊ท์กฐ ์ธํฌ๋ฒฝ ์ฑ๋ถ์ ๋ฌผ์ฑ๋ณํ๋ฅผ ์ด๋ํ์ฌ ์ธํฌ๋ด ๊ตฌ์ฑ์ฑ๋ถ์ด ์ฉ์ดํ๊ฒ ์ฉ์ถ ๋์์์ ์์ฌํ๋ค.According to the table, 1.08 mg was extracted from the sample not treated with plasma, whereas 1.22 mg was extracted from the sample treated with plasma, confirming that the extraction efficiency was increased by about 13% by plasma treatment. This suggests that the plasma treatment of the sample caused a change in the physical properties of the diatom cell wall components, and that the intracellular components were easily eluted.
์ค์์ 9. ํ์ฝ์ํด ์ถ์ถํจ์จ์ ์ต์ ํExample 9. Optimization of fucoxanthin extraction efficiency
์๋ฌผ ๊ท์กฐ(Fresh Diatom)์์ ํ์ฝ์ํด์ ์ถ์ถํ๋๋ฐ ์์ด์, ์ฌ์ฉํ๋ ์ฉ๋งค์ ์ข ๋ฅ, ์ฉ๋งค๋ ๋ฐ ์ถ์ถ์๊ฐ์ ๋ฐ๋ฅธ ์ถ์ถํจ์จ์ ๋น๊ต ๋ถ์ํจ์ผ๋ก์จ ์ต์ ์ ์ถ์ถ์กฐ๊ฑด์ ๊ฒฐ์ ํ์๋ค. In extracting fucoxanthin from fresh diatom, the optimal extraction conditions were determined by comparatively analyzing the extraction efficiency according to the type of solvent used, the amount of solvent, and the extraction time.
๋จผ์ , ์ถ์ถ ์ฉ๋งค์ ์, ์๊ฐ์ ๋ฐ๋ฅธ ์กฐ๊ฑด์ ๊ฒฐ์ ํ๊ธฐ ์ํ์ฌ, ์๋ฃ๋์ ์๋ฌผ๊ท์กฐ 50g(No.1โผ18), ์ถ์ถ์ฉ๋งค๋ 70%์ฃผ์ ๋๋ 1,3BG(Butylene Glycol)๋ฅผ ์ฌ์ฉํ๊ณ 40โ์กฐ๊ฑด์์, ์๋ฃ๋ (v/v)์ 3๋ฐฐ, 5๋ฐฐ, 7๋ฐฐ์ ์ฉ๋งค๋์ ๊ฐ๊ฐ ์ค์ ํ์ฌ ์ถ์ถ (์๋ฃ๋ช = ์ฃผ์ ์ฉ๋งค: A3, A5, A7. BG์ฉ๋งค: B3, B5, B7)๋ก ํ์๊ณ , ์ฌ๊ธฐ์ ์ถ์ถ์๊ฐ์ ๊ฐ๊ฐ 1์ผ, 3์ผ, 5์ผ๋ก ์ค์ ํ์ฌ ์ถ์ถ(์๋ฃ๋ช = 1์ผ: 1d, 3์ผ: 3d, 5์ผ: 5d)ํ์๋ค. First, in order to determine the amount of extraction solvent and the conditions according to time, the sample amount is 50 g of biological diatom (No. 1~18), and the extraction solvent is 70% alcohol or 1,3BG (Butylene Glycol), and , 3 times, 5 times, and 7 times the amount of the sample (v/v) was set for extraction (Sample name = Alcoholic solvent: A3, A5, A7. BG solvent: B3, B5, B7), and here The extraction time was set to 1 day, 3 days, and 5 days, respectively, and extraction was performed (sample name = 1 day: 1d, 3 days: 3d, 5 days: 5d).
์ฌ๊ณผ ๋ฐ ์์ฌ๋ถ๋ฆฌ ๊ณผ์ ์ ๋ค์๊ณผ ๊ฐ๋ค. ๊ฐ๊ฐ์ ์ถ์ถ์๋ฃ๋, ์ฌ๊ณผ์ง (Hyundai No.21: 8โผ12um, 90mm)์ ์ง๊ณตํํ๋ก ์ฌ๊ณผํ์ฌ ์์ฌ๋ฅผ ๊ฑธ๋ฌ๋ธ ํ ๋ถ์์ ์ฌ์ฉํ์๋ค(ํ 6, ๋ 28 ๋ด์ง 47). ๋ค๋ง, BG ์ถ์ถ๋ฌผ์ ์ ๋๊ฐ ๋งค์ฐ ๋์ ์ฌ๊ณผ์ 24์๊ฐ ์ด์ ๊ฑธ๋ฆฌ๊ฒ ๋์ด ์ถ์ถ์๊ฐ ์กฐ๊ฑด์ ๋ณ๋์ด ๋ฐ์ํ๊ฒ ๋๋ฏ๋ก, 3์ผ๊ณผ 5์ผ๊ฐ ์ถ์ถํ ์๋ฃ๋ 3500rpm์ผ๋ก 10๋ถ๊ฐ ์์ฌ๋ถ๋ฆฌํ ํ ์ถ์ถ์ก์ ์ป์๋ค (No.10โผ12, No.16โผ18).Filtration and centrifugation procedures were as follows. Each extraction sample was filtered with filter paper (Hyundai No. 21: 8-12um, 90mm) and a vacuum pump to filter out residues, and then used for analysis (Table 6, FIGS. 28 to 47). However, since the BG extract has a very high viscosity, filtration takes more than 24 hours, causing variations in the extraction time conditions. Therefore, the samples extracted for 3 and 5 days were centrifuged at 3500 rpm for 10 minutes to obtain an extract (No. 10 to 12). , No. 16-18).
(* A: 70%์ฃผ์ , B: 1,3BG, 3/5/7: 3x,5x,7x, d: day, NP:ํ๋ผ์ฆ๋ง ๋ฌด์ฒ๋ฆฌ, Pla:ํ๋ผ์ฆ๋ง ์ฒ๋ฆฌ)(* A: 70% alcohol, B: 1,3BG, 3/5/7: 3x,5x,7x, d: day, NP: no plasma treatment, Pla: plasma treatment)
(๋จ์ : mg) (Unit: mg)
๋จผ์ , 70% ์ฃผ์ ์ ์ฉ๋งค๋ก ์ถ์ถ์๊ฐ์ ๋ฐ๋ฅธ Fx ์ถ์ถํจ์จ์ ๋ถ์ํ ๊ฒฐ๊ณผ, 70% ์ฃผ์ 3๋ฐฐ๋(150mL) ์ถ์ถ์ 1์ผ 13mg, 3์ผ 9mg, 5์ผ 8mg, 5๋ฐฐ๋(250mL) ์ถ์ถ์ 1์ผ 29mg, 3์ผ 23mg, 5์ผ 19mg, 7๋ฐฐ๋(350mL) ์ถ์ถ์ 1์ผ 13mg, 3์ผ 9mg, 5์ผ 8mg์ผ๋ก ์๊ฐ์ด ๊ฒฝ๊ณผํจ์ ๋ฐ๋ผ Fx์ถ์ถํจ์จ์ด ๋ฎ์์ง๋ ๊ฒ์ผ๋ก ๋ํ๋ฌ๋ค(ํ 7). ์ด๋ก ๋ถํฐ 70% ์ฃผ์ ์ถ์ถ์กฐ๊ฑด์์๋ ์๋ฌผ ๋๋น 7๋ฐฐ(v/v)์ ์ฃผ์ ๋์ผ๋ก 1์ผ๊ฐ ์ถ์ถํ๋ ๊ฒ์ด ๊ฐ์ฅ ํจ๊ณผ์ ์ด๋ผ๋ ๊ฒ์์ ์ ์ ์๋ค.First, as a result of analyzing the Fx extraction efficiency according to extraction time using 70% alcohol as a solvent, when extracting 3
(๋จ์ : mg) (Unit: mg)
๋ค์, 1,3BG๋ฅผ ์ฉ๋งค๋ก ์ถ์ถ์๊ฐ์ ๋ฐ๋ฅธ Fx ์ถ์ถํจ์จ์ ๋ถ์ํ ๊ฒฐ๊ณผ, 1,3BG 3๋ฐฐ๋(150mL) ์ถ์ถ์ 1์ผ 18mg, 3์ผ 24mg, 5์ผ 28mg, 5๋ฐฐ๋(250mL) ์ถ์ถ์ 1์ผ 32mg, 3์ผ 38mg, 5์ผ 38mg, 7๋ฐฐ๋(350mL) ์ถ์ถ์ 1์ผ 43mg, 3์ผ 45mg, 5์ผ 45mg์ผ๋ก ์๊ฐ์ด ๊ฒฝ๊ณผํจ์ ๋ฐ๋ผ Fx์ถ์ถํจ์จ์ด ๋์์ง๊ฑฐ๋ ๋๋ฑํ ๊ฒ์ผ๋ก ๋ํ๋ฌ๋ค(ํ 8). ์ด ๊ฒฐ๊ณผ๋ก ๋ถํฐ 1,3BG ์ถ์ถ์กฐ๊ฑด์์๋ ์๋ฌผ ๋๋น 7๋ฐฐ(v/v)์ 1,3BG๋์ผ๋ก 3์ผ ๋๋ 5์ผ๊ฐ ์ถ์ถํ๋ ๊ฒ์ด ํจ๊ณผ์ ์ด๋ผ๋ ๊ฒ์์ ์ ์ ์๋ค. ๊ทธ๋ฌ๋, 7๋ฐฐ๋์์ 1์ผ๊ณผ 3์ผ, 5์ผ๊ฐ์ ์ฐจ์ด๊ฐ 43mg๊ณผ 45mg์ผ๋ก ํฌ์ง ์์ผ๋ฏ๋ก ์๊ฐ์ ํจ์จ์ ๊ณ ๋ คํ ๋ ์๋ฌผ๋๋น 7๋ฐฐ(v/v)์ 1,3BG๋์์ 1์ผ๊ฐ ์ถ์ถํ๋ ๊ฒ์ด ํจ์จ์ ์ด๋ผ๊ณ ํ ์ ์๋ค. Next, as a result of analyzing the Fx extraction efficiency according to the extraction time with 1,3BG as a solvent, when extracting 3 times (150 mL) 1,3BG, 18 mg per day, 24 mg for 3 days, 28 mg for 5 days, 1 for 5 times (250 mL) extraction 32mg per day,
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| JP2010120939A (en) * | 2008-11-17 | 2010-06-03 | Beijing Ginko Group Biological Technology Co Ltd | Method for producing fucoxanthin-containing extract |
| KR100964018B1 (en) * | 2008-03-07 | 2010-06-15 | ์ฃผ์ํ์ฌ ์ฝ์จ๋๋ฐ์ด์คํ | Fermentation fucoxanthin production method and cosmetic composition containing the same |
| KR101818736B1 (en) * | 2016-10-28 | 2018-01-15 | ํ๊ตญ๊ณผํ๊ธฐ์ ์ฐ๊ตฌ์ | Composition for preventing or treating dihydrotestosterone-induced diseases comprising fucoxanthin |
| KR20180008024A (en) * | 2016-07-15 | 2018-01-24 | ์ด์ ํ์ฌ๋ฒ์ธ ์ฃผ์ํ์ฌ ์ ์ด์ค์จ | Method for massive culture of adhesive microalgae |
| KR102056506B1 (en) * | 2012-04-27 | 2019-12-16 | ๊ฐ๋ถ์ํค๊ฐ์ด์ค ๊ฐ๋ค์นด | Method for producing composition containing fucoxanthin |
-
2019
- 2019-12-26 WO PCT/KR2019/018529 patent/WO2021132764A1/en not_active Ceased
- 2019-12-26 KR KR1020190175340A patent/KR102389503B1/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100964018B1 (en) * | 2008-03-07 | 2010-06-15 | ์ฃผ์ํ์ฌ ์ฝ์จ๋๋ฐ์ด์คํ | Fermentation fucoxanthin production method and cosmetic composition containing the same |
| JP2010120939A (en) * | 2008-11-17 | 2010-06-03 | Beijing Ginko Group Biological Technology Co Ltd | Method for producing fucoxanthin-containing extract |
| KR102056506B1 (en) * | 2012-04-27 | 2019-12-16 | ๊ฐ๋ถ์ํค๊ฐ์ด์ค ๊ฐ๋ค์นด | Method for producing composition containing fucoxanthin |
| KR20180008024A (en) * | 2016-07-15 | 2018-01-24 | ์ด์ ํ์ฌ๋ฒ์ธ ์ฃผ์ํ์ฌ ์ ์ด์ค์จ | Method for massive culture of adhesive microalgae |
| KR101818736B1 (en) * | 2016-10-28 | 2018-01-15 | ํ๊ตญ๊ณผํ๊ธฐ์ ์ฐ๊ตฌ์ | Composition for preventing or treating dihydrotestosterone-induced diseases comprising fucoxanthin |
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| Publication number | Publication date |
|---|---|
| KR102389503B1 (en) | 2022-04-25 |
| KR20210082902A (en) | 2021-07-06 |
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