JP6546578B2 - Method for extracting fat-soluble components from algae - Google Patents
Method for extracting fat-soluble components from algae Download PDFInfo
- Publication number
- JP6546578B2 JP6546578B2 JP2016214651A JP2016214651A JP6546578B2 JP 6546578 B2 JP6546578 B2 JP 6546578B2 JP 2016214651 A JP2016214651 A JP 2016214651A JP 2016214651 A JP2016214651 A JP 2016214651A JP 6546578 B2 JP6546578 B2 JP 6546578B2
- Authority
- JP
- Japan
- Prior art keywords
- fucoxanthin
- algae
- extract
- silicofluoride
- fat
- 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.)
- Active
Links
- 241000195493 Cryptophyta Species 0.000 title claims description 47
- 238000000034 method Methods 0.000 title claims description 41
- SJWWTRQNNRNTPU-ABBNZJFMSA-N fucoxanthin Chemical compound C[C@@]1(O)C[C@@H](OC(=O)C)CC(C)(C)C1=C=C\C(C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)C(=O)C[C@]1(C(C[C@H](O)C2)(C)C)[C@]2(C)O1 SJWWTRQNNRNTPU-ABBNZJFMSA-N 0.000 claims description 51
- AQLRNQCFQNNMJA-UHFFFAOYSA-N fucoxanthin Natural products CC(=O)OC1CC(C)(C)C(=C=CC(=CC=CC(=CC=CC=C(/C)C=CC=C(/C)C(=O)CC23OC2(C)CC(O)CC3(C)C)C)CO)C(C)(O)C1 AQLRNQCFQNNMJA-UHFFFAOYSA-N 0.000 claims description 50
- 238000000889 atomisation Methods 0.000 claims description 31
- 235000013305 food Nutrition 0.000 claims description 25
- 239000000243 solution Substances 0.000 claims description 24
- 239000002537 cosmetic Substances 0.000 claims description 21
- 239000002245 particle Substances 0.000 claims description 16
- 150000004667 medium chain fatty acids Chemical class 0.000 claims description 15
- 239000000203 mixture Substances 0.000 claims description 12
- 230000008569 process Effects 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 9
- 238000009832 plasma treatment Methods 0.000 claims description 7
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- 238000007599 discharging Methods 0.000 claims description 3
- 238000010298 pulverizing process Methods 0.000 claims description 3
- 238000000605 extraction Methods 0.000 description 18
- 241001474374 Blennius Species 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 15
- 241000206761 Bacillariophyta Species 0.000 description 11
- JAZBEHYOTPTENJ-JLNKQSITSA-N all-cis-5,8,11,14,17-icosapentaenoic acid Chemical compound CC\C=C/C\C=C/C\C=C/C\C=C/C\C=C/CCCC(O)=O JAZBEHYOTPTENJ-JLNKQSITSA-N 0.000 description 11
- 210000004027 cell Anatomy 0.000 description 11
- 238000000227 grinding Methods 0.000 description 11
- JAZBEHYOTPTENJ-UHFFFAOYSA-N eicosapentaenoic acid Natural products CCC=CCC=CCC=CCC=CCC=CCCCC(O)=O JAZBEHYOTPTENJ-UHFFFAOYSA-N 0.000 description 10
- 235000020673 eicosapentaenoic acid Nutrition 0.000 description 10
- 229960005135 eicosapentaenoic acid Drugs 0.000 description 10
- 239000002904 solvent Substances 0.000 description 10
- OENHQHLEOONYIE-JLTXGRSLSA-N β-Carotene Chemical compound CC=1CCCC(C)(C)C=1\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C OENHQHLEOONYIE-JLTXGRSLSA-N 0.000 description 10
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 9
- OENHQHLEOONYIE-UKMVMLAPSA-N all-trans beta-carotene Natural products CC=1CCCC(C)(C)C=1/C=C/C(/C)=C/C=C/C(/C)=C/C=C/C=C(C)C=CC=C(C)C=CC1=C(C)CCCC1(C)C OENHQHLEOONYIE-UKMVMLAPSA-N 0.000 description 9
- TUPZEYHYWIEDIH-WAIFQNFQSA-N beta-carotene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1=C(C)CCCC1(C)C)C=CC=C(/C)C=CC2=CCCCC2(C)C TUPZEYHYWIEDIH-WAIFQNFQSA-N 0.000 description 9
- 235000013734 beta-carotene Nutrition 0.000 description 9
- 239000011648 beta-carotene Substances 0.000 description 9
- 229960002747 betacarotene Drugs 0.000 description 9
- 230000000694 effects Effects 0.000 description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 8
- 239000006185 dispersion Substances 0.000 description 7
- 239000003921 oil Substances 0.000 description 7
- 235000019198 oils Nutrition 0.000 description 7
- 239000003925 fat Substances 0.000 description 6
- 235000019197 fats Nutrition 0.000 description 6
- 239000002798 polar solvent Substances 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 239000006228 supernatant Substances 0.000 description 6
- 238000005119 centrifugation Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 239000000047 product Substances 0.000 description 5
- 238000005057 refrigeration Methods 0.000 description 5
- 206010021033 Hypomenorrhoea Diseases 0.000 description 4
- 241000206744 Phaeodactylum tricornutum Species 0.000 description 4
- 241000199919 Phaeophyceae Species 0.000 description 4
- 230000009471 action Effects 0.000 description 4
- 230000003712 anti-aging effect Effects 0.000 description 4
- 230000003078 antioxidant effect Effects 0.000 description 4
- 235000021466 carotenoid Nutrition 0.000 description 4
- 150000001747 carotenoids Chemical class 0.000 description 4
- 210000002421 cell wall Anatomy 0.000 description 4
- 235000014113 dietary fatty acids Nutrition 0.000 description 4
- 229930195729 fatty acid Natural products 0.000 description 4
- 239000000194 fatty acid Substances 0.000 description 4
- 150000004665 fatty acids Chemical class 0.000 description 4
- 229920000515 polycarbonate Polymers 0.000 description 4
- 239000004417 polycarbonate Substances 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 206010003210 Arteriosclerosis Diseases 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 3
- 108090000790 Enzymes Proteins 0.000 description 3
- 235000019482 Palm oil Nutrition 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 230000000259 anti-tumor effect Effects 0.000 description 3
- 208000011775 arteriosclerosis disease Diseases 0.000 description 3
- 239000008280 blood Substances 0.000 description 3
- 210000004369 blood Anatomy 0.000 description 3
- 235000009508 confectionery Nutrition 0.000 description 3
- 235000013365 dairy product Nutrition 0.000 description 3
- 201000010099 disease Diseases 0.000 description 3
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 3
- 235000013402 health food Nutrition 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 210000002569 neuron Anatomy 0.000 description 3
- 239000002540 palm oil Substances 0.000 description 3
- 230000001954 sterilising effect Effects 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 206010008132 Cerebral thrombosis Diseases 0.000 description 2
- 201000001429 Intracranial Thrombosis Diseases 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 2
- 235000007164 Oryza sativa Nutrition 0.000 description 2
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 description 2
- 239000003240 coconut oil Substances 0.000 description 2
- 235000019864 coconut oil Nutrition 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 235000013373 food additive Nutrition 0.000 description 2
- 239000002778 food additive Substances 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 235000015110 jellies Nutrition 0.000 description 2
- 239000008274 jelly Substances 0.000 description 2
- 150000002632 lipids Chemical class 0.000 description 2
- 239000006210 lotion Substances 0.000 description 2
- 239000004006 olive oil Substances 0.000 description 2
- 235000008390 olive oil Nutrition 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- -1 pack Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000004321 preservation Methods 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 235000009566 rice Nutrition 0.000 description 2
- 235000014214 soft drink Nutrition 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000010902 straw Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 235000015961 tonic Nutrition 0.000 description 2
- 230000001256 tonic effect Effects 0.000 description 2
- 229960000716 tonics Drugs 0.000 description 2
- FPIPGXGPPPQFEQ-UHFFFAOYSA-N 13-cis retinol Natural products OCC=C(C)C=CC=C(C)C=CC1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-UHFFFAOYSA-N 0.000 description 1
- 241000512259 Ascophyllum nodosum Species 0.000 description 1
- 241000195940 Bryophyta Species 0.000 description 1
- 208000003643 Callosities Diseases 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 241000270617 Cheloniidae Species 0.000 description 1
- 229920000855 Fucoidan Polymers 0.000 description 1
- 206010020649 Hyperkeratosis Diseases 0.000 description 1
- 244000061775 Olea africana Species 0.000 description 1
- 235000002852 Olea africana Nutrition 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- 235000019485 Safflower oil Nutrition 0.000 description 1
- 241000195473 Sargassum fulvellum Species 0.000 description 1
- 241001260874 Sargassum horneri Species 0.000 description 1
- 201000010001 Silicosis Diseases 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 208000006011 Stroke Diseases 0.000 description 1
- 235000019486 Sunflower oil Nutrition 0.000 description 1
- 241000276707 Tilapia Species 0.000 description 1
- 241001261506 Undaria pinnatifida Species 0.000 description 1
- FPIPGXGPPPQFEQ-BOOMUCAASA-N Vitamin A Natural products OC/C=C(/C)\C=C\C=C(\C)/C=C/C1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-BOOMUCAASA-N 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 235000013334 alcoholic beverage Nutrition 0.000 description 1
- FPIPGXGPPPQFEQ-OVSJKPMPSA-N all-trans-retinol Chemical compound OC\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C FPIPGXGPPPQFEQ-OVSJKPMPSA-N 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 235000015895 biscuits Nutrition 0.000 description 1
- 235000008429 bread Nutrition 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 206010008118 cerebral infarction Diseases 0.000 description 1
- 208000026106 cerebrovascular disease Diseases 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000020235 chia seed Nutrition 0.000 description 1
- 210000003763 chloroplast Anatomy 0.000 description 1
- 235000019219 chocolate Nutrition 0.000 description 1
- 235000012000 cholesterol Nutrition 0.000 description 1
- 238000004440 column chromatography Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 235000012343 cottonseed oil Nutrition 0.000 description 1
- 239000002385 cottonseed oil Substances 0.000 description 1
- 239000006071 cream Substances 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 235000013325 dietary fiber Nutrition 0.000 description 1
- 235000015872 dietary supplement Nutrition 0.000 description 1
- 235000015071 dressings Nutrition 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 238000002481 ethanol extraction Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 235000012041 food component Nutrition 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 239000000499 gel Substances 0.000 description 1
- 239000008169 grapeseed oil Substances 0.000 description 1
- 238000004128 high performance liquid chromatography Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 150000004668 long chain fatty acids Chemical class 0.000 description 1
- KBPHJBAIARWVSC-RGZFRNHPSA-N lutein Chemical compound C([C@H](O)CC=1C)C(C)(C)C=1\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\[C@H]1C(C)=C[C@H](O)CC1(C)C KBPHJBAIARWVSC-RGZFRNHPSA-N 0.000 description 1
- 229960005375 lutein Drugs 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000020124 milk-based beverage Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 235000011929 mousse Nutrition 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 235000012149 noodles Nutrition 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000002674 ointment Substances 0.000 description 1
- 235000015927 pasta Nutrition 0.000 description 1
- 230000000243 photosynthetic effect Effects 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 235000005713 safflower oil Nutrition 0.000 description 1
- 239000003813 safflower oil Substances 0.000 description 1
- 150000004671 saturated fatty acids Chemical class 0.000 description 1
- 235000003441 saturated fatty acids Nutrition 0.000 description 1
- 210000004761 scalp Anatomy 0.000 description 1
- 239000008159 sesame oil Substances 0.000 description 1
- 235000011803 sesame oil Nutrition 0.000 description 1
- 239000002453 shampoo Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 235000014347 soups Nutrition 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000013112 stability test Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000002600 sunflower oil Substances 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 235000013616 tea Nutrition 0.000 description 1
- KBPHJBAIARWVSC-XQIHNALSSA-N trans-lutein Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1=C(C)CC(O)CC1(C)C)C=CC=C(/C)C=CC2C(=CC(O)CC2(C)C)C KBPHJBAIARWVSC-XQIHNALSSA-N 0.000 description 1
- 238000002525 ultrasonication Methods 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 229940088594 vitamin Drugs 0.000 description 1
- 229930003231 vitamin Natural products 0.000 description 1
- 235000013343 vitamin Nutrition 0.000 description 1
- 239000011782 vitamin Substances 0.000 description 1
- 235000019155 vitamin A Nutrition 0.000 description 1
- 239000011719 vitamin A Substances 0.000 description 1
- 229940045997 vitamin a Drugs 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
- FJHBOVDFOQMZRV-XQIHNALSSA-N xanthophyll Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1=C(C)CC(O)CC1(C)C)C=CC=C(/C)C=CC2C=C(C)C(O)CC2(C)C FJHBOVDFOQMZRV-XQIHNALSSA-N 0.000 description 1
- 235000008210 xanthophylls Nutrition 0.000 description 1
- 235000013618 yogurt Nutrition 0.000 description 1
Landscapes
- Coloring Foods And Improving Nutritive Qualities (AREA)
- Edible Seaweed (AREA)
- Cosmetics (AREA)
- Fats And Perfumes (AREA)
Description
本発明は、藻類に含まれるフコキサンチンやエイコサペンタエン酸(EPA)、β−カロテンなどの脂溶性成分を高濃度で簡便に抽出する方法、およびその抽出物を配合した食品および化粧品組成物に関する。 The present invention relates to a method of easily extracting fat-soluble components such as fucoxanthin, eicosapentaenoic acid (EPA), β-carotene and the like contained in algae at a high concentration, and food and cosmetic compositions containing the extract.
藻類はミネラル、ビタミン、食物繊維(フコイダン等)などの有用な栄養成分を含有しており、健康食品として近年注目されている。 Alga contains useful nutrients such as minerals, vitamins and dietary fibers (fucoidan etc.), and has recently been attracting attention as a health food.
藻類にはβ−カロテンやEPA等の脂溶性成分が含まれており、これらの脂溶性成分は栄養成分として、あるいは化粧品の素材として有用である。
具体的には、β−カロテンは強力な抗酸化作用を有するため、化粧品に加えると美肌効果、アンチエイジング効果が期待でき、食品として摂取すれば動脈硬化や生活習慣病の予防につながる。
β−カロテンを体内に取り込めば必要量に応じてビタミンAに変換されて使用される。
The algae contains fat-soluble components such as β-carotene and EPA, and these fat-soluble components are useful as nutritional components or as materials for cosmetics.
Specifically, since β-carotene has a strong antioxidative effect, it can be expected to be effective in skin care and anti-aging when added to cosmetics and leads to prevention of arteriosclerosis and lifestyle-related diseases if it is taken as a food.
If beta-carotene is taken into the body, it is converted to vitamin A and used according to the required amount.
EPAは血中の中性脂肪やコレステロールを低下させる働きを有するため、食品として摂取すると脳血栓や脳梗塞などのリスクを軽減できる。β−カロテンと同様に強力な抗酸化作用を有するため、化粧品に加えると美肌効果、アンチエイジング効果が期待できる。 Since EPA has the function of reducing neutral fat and cholesterol in the blood, taking it as a food can reduce the risk of cerebral thrombosis and cerebral infarction. As it has a strong antioxidant action like β-carotene, it can be expected to be effective in skin care and anti-aging when added to cosmetics.
藻類由来の脂溶性成分の中でも、近年注目を集めているのはフコキサンチンである。フコキサンチンは褐藻類に含まれるカロテノイド(キサントフィル)の一種であり、ワカメ、モズク、コンブ、ヒジキなど日常的に食される海藻類に含まれている成分である。近年、フコキサンチンには抗酸化作用、抗腫瘍作用、神経細胞保護作用、血糖値上昇抑制などの保健機能的作用効果が報告されており、健康食品や化粧品等において利用することが期待されている。 Among algae-derived fat-soluble components, fucoxanthin has recently attracted attention. Fucoxanthin is a kind of carotenoid (xanthophyll) contained in brown algae, and is a component contained in seaweeds such as wakame, mozuku, kelp and hijiki which are eaten on a daily basis. In recent years, fucoxanthin has been reported to have health functional effects such as antioxidative action, antitumor action, nerve cell protective action, and suppression of blood sugar level elevation, and is expected to be used in health food and cosmetics etc. .
一方、藻類の脂溶性成分を抽出する方法としては、その抽出溶媒としてエタノールなど水に相溶性を有する有機溶媒を用いて抽出する方法が行われている。
しかし、一般に、カロテノイドやEPA等の脂溶性成分を産生する細胞であっても、細胞中に含まれる脂溶性成分の含量は低く、例えば、一般に食用に供される海藻中に含まれるフコキサンチンは、湿重量あたり0.2mg/g以下と極めて微量である。
よって、有効な機能性を発揮する量の脂溶性成分を得るためには、エタノールなど水に相溶性を有する有機溶媒を用いた後、様々な方法を用いて濃縮し、油脂に可溶化する必要があり、大量の原料を必要とするうえ手間がかかるという問題点があった。
このため、藻類から脂溶性成分を効率よく、簡便に抽出できる方法の開発が求められている。
さらに、フコキサンチンは時間の経過とともに分解しやすい物質である。このため、フコキサンチンを長期間安定して保存できる抽出方法が求められている。
On the other hand, as a method of extracting a lipid-soluble component of algae, a method of extracting using an organic solvent having compatibility with water, such as ethanol, as the extraction solvent is performed.
However, in general, even in cells producing lipid-soluble components such as carotenoids and EPA, the content of fat-soluble components contained in the cells is low. For example, fucoxanthin contained in seaweed generally used for food is , 0.2 mg / g or less per wet weight extremely small amount.
Therefore, in order to obtain a fat-soluble component in an amount that exhibits effective functionality, it is necessary to use an organic solvent compatible with water, such as ethanol, and then concentrate using various methods to solubilize it in fats and oils. There is a problem in that it requires a large amount of raw materials and takes time and effort.
For this reason, development of a method capable of extracting lipid-soluble components from algae efficiently and simply is required.
Furthermore, fucoxanthin is a substance that is easily decomposed with the passage of time. Therefore, there is a need for an extraction method that can stably store fucoxanthin for a long period of time.
藻類から効率的に脂溶性成分を抽出するために、様々な方法が開発されている。
その中には、物理的に細胞を破砕して細胞に含まれる脂溶性成分を取り出す方法がある。
例えば、特許文献1には微細藻類を含む分散液に二酸化炭素を溶解させ、高圧分散装置により剪断力を加えることで微細藻類を破砕して脂質を抽出する方法が記載されている。しかし、特許文献1記載の方法では分散液に含まれる溶媒として水を用いており、脂質を分離するためにはその後溶媒抽出、遠心分離、静置処理、及び/又はカラムクロマトグラフィー等を行う必要があり、時間と手間を要するという問題点を有する。
Various methods have been developed to efficiently extract fat-soluble components from algae.
Among them, there is a method of physically disrupting cells and removing the fat-soluble component contained in the cells.
For example, Patent Document 1 describes a method of dissolving carbon dioxide in a dispersion containing microalga and applying shear force with a high-pressure dispersing device to break up the microalga and extract lipids. However, in the method described in Patent Document 1, water is used as a solvent contained in the dispersion, and it is necessary to subsequently perform solvent extraction, centrifugation, stationary treatment, and / or column chromatography, etc. in order to separate lipids. And it takes time and effort.
特許文献2には、脂溶性成分からなる生理活性物質を含む海藻由来製品素材の製造方法であって、海藻を微細化し、微細化した海藻を、海藻細胞壁分解酵素を含む酵素水溶液中でインキュベートした後、液体成分を固体成分から分離し、固体成分を乾燥させて海藻由来製品素材を得る、製造方法が記載されている。
特許文献2記載の方法では酵素水溶液中で脂溶性成分を抽出しているため、その後水溶液から脂溶性成分を分離する必要があり、分離に手間と時間がかかるという問題点を有する。
Patent Document 2 describes a method for producing a seaweed-derived product material containing a physiologically active substance consisting of a fat-soluble component, wherein the seaweed is refined and the refined seaweed is incubated in an aqueous enzyme solution containing a seaweed cell wall degrading enzyme Thereafter, a manufacturing method is described in which the liquid component is separated from the solid component and the solid component is dried to obtain a seaweed-derived product material.
In the method described in Patent Document 2, since the fat-soluble component is extracted in the aqueous enzyme solution, it is necessary to separate the fat-soluble component from the aqueous solution thereafter, and it takes time and effort to separate.
特許文献3には、海藻類の細片または粉末にオリーブ油などの油脂、ロウ類または炭化水素を加えて撹拌し、その後常温で摩砕することで脂溶性成分を油脂等に抽出する方法が記載されている。
特許文献3では、抽出した油脂等をそのまま化粧品に用いた実施例が記載されているものの、食品として用いるにはその後滅菌操作等を行う必要があるため、抽出後の処理に時間と手間を要するという問題点を有する。さらに、特許文献3記載の方法では油脂中に抽出された脂溶性成分は均一に分散していないため、その後食品や化粧品に加える際に正確な濃度で加えることが難しいという問題点を有する。
Patent Document 3 describes a method of extracting fat-soluble components into fats and oils, etc. by adding fats and oils such as olive oil, waxes or hydrocarbons to pieces or powder of seaweed, stirring and then grinding at normal temperature. It is done.
Although the example which used extracted fats and oils etc. for cosmetics as it is described in patent document 3, since it is necessary to perform sterilization operation after that in order to use as foodstuffs, processing after extraction requires time and effort. It has the problem of Furthermore, in the method described in Patent Document 3, since the fat-soluble component extracted in the fat and oil is not uniformly dispersed, it has a problem that it is difficult to add it at an accurate concentration when added to food and cosmetics thereafter.
本発明は、藻類に含まれるフコキサンチンやEPA、β−カロテンなどの脂溶性成分を高濃度で簡便に抽出する方法、およびその抽出物を配合した食品および化粧品組成物を提供するものである。 The present invention provides a method of easily extracting fat-soluble components such as fucoxanthin, EPA, β-carotene and the like contained in algae at a high concentration, and a food and cosmetic composition containing the extract.
請求項1に係る発明は、珪藻類からフコキサンチンを1.5mg/g以上の濃度で抽出する方法であって、(1)珪藻類を粉砕する工程、(2)粉砕した珪藻類に中鎖脂肪酸を添加してなる溶液を作製する工程、及び(3)該溶液を湿式微粒化処理して抽出物を得る工程を含み、湿式微粒化処理が、(a)該溶液を高圧ノズルから高圧噴射し微粒化処理する工程、(b)微粒化処理した溶液にエアを供給する工程、(c)エアを供給することによって形成された気泡中で放電させ、液中プラズマ処理し、フコキサンチンを含む抽出物を得る工程、を含むことを特徴とする、方法に関する。
Invention, fucoxanthin from silicofluoride algae A method for extracting at a concentration of at least 1.5 mg / g, (1) a step of pulverizing the silicofluoride algae, chain medium to silicofluoride algae were ground (2) according to claim 1 And (3) wet atomizing treatment of the solution to obtain an extract, wherein the wet atomization treatment comprises (a) high pressure spraying the solution from a high pressure nozzle. Atomization process, (b) supplying air to the atomized solution, (c) discharging in air bubbles formed by supplying air, performing in-liquid plasma treatment, containing fucoxanthin to obtain an extract, characterized by a-law including the relates to a method.
請求項2に係る発明は、湿式微粒化処理によって形成された粒子の5%以上が粒径1μm−100μmの範囲内であることを特徴とする、請求項1に記載の方法に関する。
The invention according to claim 2, characterized in that more than 5% of the particles formed by wet atomization process is in the range of particle size 1 [mu] m-100 [mu] m, to a method as claimed in claim 1.
請求項3に係る発明は、珪藻類と中鎖脂肪酸のみからなり、珪藻類由来のフコキサンチンの濃度が1.5mg/g以上であり、2か月保存してもフコキサンチンの保存率が78%以上であることを特徴とする、請求項1または2に記載の方法により製造された、フコキサンチン含有抽出物に関する。
The invention according to claim 3, consisting solely silicofluoride algae and medium-chain fatty acids, the concentration of fucoxanthin from silicofluoride algae is not less 1.5 mg / g or more, even after storage 2 months fucoxanthin storage rate 78 It relates to a fucoxanthin- containing extract produced by the method according to claim 1 or 2 , characterized in that it is% or more.
請求項4に係る発明は、請求項3に記載のフコキサンチン含有抽出物を含む食品又は化粧品組成物に関する。
The invention according to claim 4 relates to a food or cosmetic composition comprising the fucoxanthin- containing extract according to claim 3 .
請求項1に係る発明によれば、珪藻類のフコキサンチンを中鎖脂肪酸中で抽出することで、溶媒を蒸発させてフコキサンチンを濃縮、精製することなく、直接食品や化粧品組成物に添加することができる。
微粒化処理することで珪藻類の細胞壁を破壊し、効率よくフコキサンチンを抽出することができる。
According to the invention of claim 1, by extracting the fucoxanthin of silicofluoride algae in a medium-chain fatty acid, concentrated fucoxanthin the solvent was evaporated, without purification, is added directly to the food and cosmetic compositions be able to.
To disrupt the cell walls of silicofluoride algae by treating atomization can be extracted efficiently fucoxanthin.
さらに、請求項1に係る発明によれば、粉砕した珪藻類に中鎖脂肪酸を添加した溶液を高圧ノズルから高圧噴射することで珪藻類の細胞壁を破壊し、マイクロサイズにまで微粒化することで細胞中のほとんどのフコキサンチンを中鎖脂肪酸中に放出することができ、結果として珪藻類から最大量のフコキサンチンを抽出することができる。
微粒化処理した溶液を液中プラズマ処理することで、静電反発の作用によって再凝集が防止されるとともにフコキサンチンの中鎖脂肪酸中での分散安定性が向上する。また、プラズマ中の荷電粒子の衝突による細菌の破壊や滅菌の効果もある。
さらに、液中プラズマ処理をする前に微粒化処理した溶液にエアを供給することで放電しやすい環境を作り、静電反発の作用を溶液中の微粒子に行き渡らせることが容易になる。
中鎖脂肪酸、つまり食用油を使用することで、最終的に得られた抽出物をそのまま食品や化粧品組成物に添加することができる。
Furthermore, according to the invention of claim 1, a solution prepared by adding medium-chain fatty acids silicofluoride algae were ground to destroy the cell walls of silicofluoride algae by high-pressure injection from the high-pressure nozzles, by atomization to a micro-sized can be released into the medium-chain fatty acid most fucoxanthin in the cell, the result can be extracted fucoxanthin maximum amount from silicofluoride algae as.
By subjecting the atomized solution to in-liquid plasma treatment, reaggregation is prevented by the action of electrostatic repulsion, and the dispersion stability of fucoxanthin in medium-chain fatty acids is improved. There is also an effect of destruction or sterilization of bacteria due to collision of charged particles in plasma.
Furthermore, by supplying air to the atomized solution prior to the in-liquid plasma treatment, it becomes easy to create an environment susceptible to discharge and spread the action of electrostatic repulsion to the particles in the solution.
By using a medium-chain fatty acid , that is, an edible oil, the finally obtained extract can be added as it is to a food or cosmetic composition.
また、請求項1に係る発明によれば、フコキサンチンを含む抽出物が珪藻類から得られる。
Further, the invention according to claim 1, including extract extract is obtained from silicofluoride algae Fukokisanchi down.
加えて、請求項1に係る発明によれば、従来の抽出方法で得られた抽出物と比較して高濃度のフコキサンチンを含む抽出物が珪藻類から得られる。
In addition, the invention according to claim 1, extract containing a high concentration of fucoxanthin compared to the extract obtained in the conventional extraction method is obtained from silicofluoride algae.
請求項2に係る発明によれば、微粒化処理によって形成された粒子の5%以上が粒径1μm−100μmの範囲内にある、つまりマイクロサイズに微細化することで珪藻類の細胞に含まれるフコキサンチンをより効率よく抽出することができるという効果を奏する。
According to the invention according to claim 2, contained in the cell of silicofluoride algae by more than 5% of the particles formed by the atomization process is within the range of particle size 1 [mu] m-100 [mu] m, to refine the words micro-sized The effect is that fucoxanthin can be extracted more efficiently.
請求項3に係る発明によれば、珪藻類由来のフコキサンチンの濃度が1.5mg/g以上であり、2か月保存してもフコキサンチンの保存率が78%以上であることを特徴とする、フコキサンチン含有抽出物を提供することができる。
According to the invention of claim 3 state, and are the concentration of fucoxanthin 1.5 mg / g or more from silicosis algae, the Der Rukoto saving rate is 78% or more fucoxanthin be stored for 2 months A fucoxanthin- containing extract can be provided, which is characterized.
請求項4に係る発明によれば、請求項3に記載のフコキサンチン含有抽出物を含む食品又は化粧品組成物とすることで、食品として摂取すれば動脈硬化や生活習慣病の予防につながり、脳血栓や脳梗塞などのリスクを軽減し、抗酸化作用、抗腫瘍作用、神経細胞保護作用、血糖値上昇抑制効果を奏する。化粧品組成物として使用すれば美肌効果、アンチエイジング効果を奏する。
According to the invention as set forth in claim 4 , the food or cosmetic composition containing the fucoxanthin- containing extract as set forth in claim 3 leads to prevention of arteriosclerosis and lifestyle-related diseases if it is ingested as a food, and cerebral thrombosis And reduce the risk of stroke, etc., and exert antioxidative action, antitumor action, nerve cell protective action, and blood sugar level elevation suppressive effect. When used as a cosmetic composition, it produces a skin-beautifying effect and an anti-aging effect.
<脂溶性成分>
以下、本発明に係る脂溶性成分について説明する。
Fat-soluble component
Hereinafter, the fat-soluble component according to the present invention will be described.
本発明の抽出方法によって得られる脂溶性成分は、フコキサンチンやβ−カロテン等のカロテノイド、及びEPAのような脂肪酸を含む。 The fat-soluble components obtained by the extraction method of the present invention include carotenoids such as fucoxanthin and β-carotene, and fatty acids such as EPA.
フコキサンチンは、CAS番号3351−86−8であって、下式(化1)に示す構造を有している。 Fucoxanthin is CAS number 3351-86-8 and has a structure shown in the following formula (Formula 1).
β−カロテンは、CAS番号7235−40−7であって、下式(化2)に示す構造を有している。 (beta) -carotene is CAS number 7235-40-7, and has a structure shown to the following Formula (chemical formula 2).
EPAは、CAS番号10417−94−4であって、下式(化3)に示す構造を有している。 EPA is CAS No. 10417-94-4 and has a structure shown in the following formula (Chemical formula 3).
本発明において、フコキサンチン、EPA、β−カロテンを含む抽出物は藻類等からの抽出物を用いることができる。 In the present invention, the extract containing fucoxanthin, EPA, β-carotene can be an extract from algae or the like.
<藻類>
本発明で用いる藻類は、フコキサンチンを含有するものであれば特に制限されないが、フコキサンチンは褐藻やその他の不等毛藻に存在して茶色−オリーブ色を呈するとともに、葉緑体において光合成の補助色素として機能している。特に、褐藻類や珪藻類中のカロテノイドの大部分がフコキサンチンである。そこで、フコキサンチンを比較的多く含む褐藻綱に属する海藻および珪藻綱に属する珪藻類が好ましい。
<Algae>
The algae used in the present invention is not particularly limited as long as it contains fucoxanthin, but fucoxanthin is present in brown algae and other unequal hair algae to exhibit a brown-olive color and is photosynthetic in chloroplasts. It functions as an auxiliary dye. In particular, most of the carotenoids in brown algae and diatoms are fucoxanthins. Thus, seaweeds belonging to brown algae and diatoms belonging to diatoms, which contain relatively high amounts of fucoxanthin, are preferred.
その中でも、資源量及び市場流通性の観点から、ホンダワラ(Sargassum fulvellum)やアカモク(Sargassum horneri)などのホンダワラ類、ヒジキ類、ワカメ類、コンブ類、モズク類がより好ましい。フコキサンチンの含有量が豊富であれば、微細藻類等であってもよい。
ホンダワラは褐藻綱ホンダワラ科ホンダワラ属の海藻の1種であり、本州、四国、九州、朝鮮半島等に分布している。1年生で、1−2mの長さになる。柔軟質で、葉は披針形をしており切れ込みがある。楕円や倒卵形の気泡を有することで浮力を得て流れ藻となる。古くから食用や肥料、飾り物として用いられていた。
アカモクは褐藻綱ホンダワラ科ホンダワラ属に属する海藻である。北海道(東部を除く)から日本全土の漸深帯(浅海)に分布し、朝鮮半島、中国及びベトナム北部にまで分布する。1年生で、秋から冬に生長し、4−7mの長さに達する。雌雄異株である(まれに雌雄同株の個体がある)。
Among them, from the viewpoint of resource amount and market circulation, Honda straws such as Honda straw (Sargassum fulvellum) and Akamoku (Sargassum horneri), tilapia, sea turtles, seaweeds, corns and mozuku are more preferable. As long as the content of fucoxanthin is abundant, microalgae and the like may be used.
Honda Walla is a kind of seaweed of the brown alga Hondalaaceae, and is distributed in Honshu, Shikoku, Kyushu, Korean Peninsula, etc. In the first grade, it will be 1-2 m in length. It has a soft texture, leaves are lancet shaped and there are cuts. It becomes buoyant and becomes a flowing algae by having an oval or ovate-shaped air bubble. It has been used for a long time as food, fertilizer and ornaments.
Akamoku is a seaweed that belongs to the brown alga Hondawara ssp. It is distributed in Hokkaido (except the eastern part) and in a deep-sea zone (shallow sea) of the whole of Japan, and also in the Korean peninsula, China and northern Vietnam. It is a first grader and grows from autumn to winter, reaching 4 to 7 m in length. It is a dimorphism (rarely there are individuals of the dimorphism).
これら藻類は、天然または養殖の何れであっても良く、一種で用いても二種以上の混合で用いても良い。また、前記海藻類は、海より採取したままの海藻類、冷凍された海藻類、塩蔵された海藻類、乾燥された海藻類、水洗処理、熱水処理、酸性水洗浄、アルカリ水洗浄、細断処理などの加工処理された状態の何れでも使用できる。 These algae may be either natural or aquaculture, and may be used singly or in combination of two or more. In addition, the seaweed may be seaweed as collected from the sea, frozen seaweed, salted seaweed, dried seaweed, water washing treatment, hot water treatment, acid water washing, alkaline water washing, Any of the processed state such as disconnection processing can be used.
<低極性溶媒>
本発明において、低極性溶媒は特に限定されないが、中鎖脂肪酸、大豆油、菜種油、紅花油、コーン油、綿実油、ごま油、オリーブオイル、ヤシ油、パーム油、チアシードオイル、ひまわり油、米油及びグレープシードオイルが含まれる。使用目的に応じて上記より選択し用いることができる。
脂肪酸とは、長鎖炭化水素の1価のカルボン酸であり、一般的に、炭素数5−12個のものを中鎖脂肪酸と呼ぶ。中鎖脂肪酸は、乳製品やパーム油、ココナッツ油などに多く含まれている。不飽和脂肪酸に比べて飽和脂肪酸は酸化臭が少なく、濁りも少ないことから、本発明において好適に利用できる。中鎖脂肪酸は、長鎖脂肪酸と比較して水溶性が高いため体内に吸収されやすく、酸化臭が少ないことから、本発明において好適に利用できる。
<Low polar solvent>
In the present invention, the low polarity solvent is not particularly limited, but medium chain fatty acid, soybean oil, rapeseed oil, safflower oil, corn oil, cottonseed oil, sesame oil, olive oil, coconut oil, palm oil, palm oil, chia seed oil, sunflower oil, rice oil and Contains grape seed oil. It can be selected from the above according to the purpose of use.
A fatty acid is a long chain hydrocarbon monovalent carboxylic acid, and in general, one having 5 to 12 carbon atoms is called a medium chain fatty acid. Medium-chain fatty acids are abundant in dairy products, palm oil and coconut oil. Saturated fatty acids have less oxidizing odor and less turbidity than unsaturated fatty acids, and thus can be suitably used in the present invention. Medium-chain fatty acids are easily absorbed in the body because they have high water solubility compared to long-chain fatty acids, and they are suitable for use in the present invention because they have low oxidative odor.
<藻類からの脂溶性成分の抽出>
本発明において、藻類から脂溶性成分を抽出する方法は、(1)藻類を粉砕する工程、(2)粉砕した藻類に低極性溶媒を添加してなる溶液を作製する工程、(3)該溶液を湿式微粒化処理して抽出物を得る工程、を含む。
<Extraction of fat-soluble components from algae>
In the present invention, the method of extracting a lipid-soluble component from algae comprises (1) a step of grinding algae, (2) a step of preparing a solution obtained by adding a low polarity solvent to the crushed algae, (3) the solution Wet atomization to obtain an extract.
本発明の藻類から脂溶性成分を抽出する方法は、粉砕した藻類に低極性溶媒を添加し、その後湿式微粒化処理している。藻類を粉砕した後、さらに微粒化処理することで藻類の細胞壁を破壊し、藻類の細胞中に含まれる成分のほとんどを低極性溶媒中に放出する。これにより、従来のように微粒化せずに単に溶媒中に藻類を加えるよりも多くの脂溶性成分を抽出することができる。特に、フコキサンチンやEPA、β−カロテンのような細胞中の含量が小さい(細胞中の含量が湿重量あたり0.2mg/g以下)成分を抽出する方法として適している。
低極性溶媒中で微粒化処理する「湿式微粒化処理」を行うことで、溶媒を水等の極性溶媒を使用した場合のように極性溶媒から脂溶性成分を分離する必要がなく、脂溶性成分が低極性溶媒に溶解するため、抽出処理後の抽出物をそのまま食品や化粧品組成物に使用することができる。微粒化処理したことで抽出物中の脂溶性成分の濃度が高い(1.5mg/g程度)ため、濃縮工程を経ることなく、そのまま食品や化粧品組成物に使用することができる。
また、さらに高濃度(例えば5−10mg/g)でフコキサンチン等の脂溶性成分を抽出したい場合、一度湿式微粒化処理をした結果得られた抽出物に、さらに藻類を加えて再び湿式微粒化処理をする、という工程を繰り返すことで、さらに高濃度(例えば5−10mg/g)で脂溶性成分を含む抽出物を得ることができる。
In the method of extracting a lipid-soluble component from algae of the present invention, a low polarity solvent is added to crushed algae, and then wet atomization treatment is performed. After crushing the algae, further atomization treatment destroys the algal cell wall and releases most of the components contained in the algal cells into the low polarity solvent. This makes it possible to extract more fat-soluble components than adding algae in the solvent without atomization as in the prior art. In particular, it is suitable as a method for extracting a component having a small content in the cell (content in the cell is 0.2 mg / g or less per wet weight) such as fucoxanthin, EPA and β-carotene.
There is no need to separate the fat-soluble component from the polar solvent as in the case of using a polar solvent such as water by performing "wet-pulverizing treatment" in which the fine particle processing is performed in the low polar solvent, and the fat-soluble component Since it is dissolved in a low polarity solvent, the extract after extraction can be used as it is in food and cosmetic compositions. Since the concentration of the fat-soluble component in the extract is high (approximately 1.5 mg / g) by the atomization treatment, it can be used as it is in food and cosmetic compositions without undergoing a concentration step.
In addition, when it is desired to extract a fat-soluble component such as fucoxanthin at a higher concentration (for example, 5-10 mg / g), algae are further added to the extract obtained as a result of the wet atomization treatment once to obtain wet atomization again. By repeating the process of treating, it is possible to obtain an extract containing a fat-soluble component at a higher concentration (for example, 5 to 10 mg / g).
(藻類を粉砕する工程)
湿式微粒化処理の前処理として、藻類を粗く粉砕することが望ましい。予め粗く粉砕することで湿式微粒化処理にかける時間を短縮でき、湿式微粒化処理を行う装置にかける負担を軽減できる。
粉砕するための装置は特に限定されず、ミルを使用して粉砕しても、圧力を利用して粉砕しても良く、粉砕刃による衝撃粉砕であっても良い。粉砕機構としてボールミル、ロッドミル、SAGミル、自生粉砕ミル、高圧粉砕ロール、縦軸インパクタミル、ジェットミル等が挙げられる。
粉砕した後の藻類の粒径は1mm以下が望ましい。
(Step of crushing algae)
It is desirable to crush the algae roughly as a pretreatment for wet atomization. By crushing roughly in advance, the time required for the wet atomization process can be shortened, and the load imposed on the apparatus for performing the wet atomization process can be reduced.
The apparatus for grinding is not particularly limited, and grinding may be performed using a mill, or may be performed using pressure, or may be impact grinding with a grinding blade. As a grinding mechanism, a ball mill, a rod mill, a SAG mill, an autogenous grinding mill, a high pressure grinding roll, a vertical axis impactor mill, a jet mill and the like can be mentioned.
The particle size of the algae after crushing is preferably 1 mm or less.
(湿式微粒化処理)
低極性溶媒を入れた状態で微粒化処理することで、藻類の細胞中の脂溶性成分が低極性溶媒中に放出される。
湿式微粒化処理として湿式ジェットミル、超音波振動による分散、ビーズミル等の粉砕用媒体を使用した湿式の機械的接触式粉砕等が挙げられる。この発明においては湿式ジェットミルがより好ましく採用できる。
(Wet atomization process)
By carrying out atomization treatment in a state of containing a low polar solvent, fat-soluble components in algal cells are released into the low polar solvent.
Examples of the wet atomization treatment include a wet jet mill, dispersion by ultrasonic vibration, and wet mechanical contact grinding using a grinding medium such as a bead mill. In the present invention, a wet jet mill can be more preferably employed.
湿式ジェットミルはウォータージェット技術を用いた方法であり、原料溶液を高圧ノズルから高圧噴射することで粒子自体を壊さずコンタミの混入がない微粒化工法として開発されたものである。本発明においては低極性溶媒を添加した、前処理で予め粗く粉砕した藻類を高圧ノズルから高圧噴射する。
高圧ノズルからの圧力は特に限定されないが、15から500MPaの間で調整し、必要に応じて高圧ノズルから溶液を所定の圧力で高圧噴射する作業を複数回繰り返しても良い。このように使用することで、藻類を所望のメジアン径の粒子とすることが容易にできる。
The wet jet mill is a method using a water jet technology, and is developed as an atomization method without causing contamination of particles without breaking the particles themselves by injecting a raw material solution under high pressure from a high pressure nozzle. In the present invention, algae pre-treated and coarsely crushed in advance, to which a low polarity solvent has been added, is high-pressure jetted from a high-pressure nozzle.
The pressure from the high pressure nozzle is not particularly limited, but may be adjusted between 15 and 500 MPa, and the operation of high-pressure injection of the solution from the high pressure nozzle at a predetermined pressure may be repeated multiple times if necessary. By using it in this manner, it is possible to easily make the algae into particles of a desired median diameter.
湿式微粒化処理は、上記の工程に加えて、微粒化処理した溶液にエアを供給する工程、及びエアを供給することによって形成された気泡中で放電させ、液中プラズマ処理し、脂溶性成分を含む抽出物を得る工程を含み得る。
つまり、高圧噴射処理装置の物理的作用による分散と液中プラズマ処理による改質作用が連続的に行われる構成となり、これらの相乗効果によって再凝集が防止されるとともに分散安定性が向上する。また、プラズマ中の荷電粒子の衝突による細菌の破壊や滅菌の効果もある。
液中プラズマ処理の前にエアを供給することが好ましい。エアを供給することにより、気泡中で放電されるため、プラズマ処理の効果が溶液中に均一に行き渡る。
In the wet atomization treatment, in addition to the above steps, a step of supplying air to the atomized solution, and discharging in air bubbles formed by supplying air, plasma treatment in liquid, a fat-soluble component And B. obtaining an extract containing
That is, the dispersion by physical action of the high-pressure injection processing apparatus and the reforming action by the in-liquid plasma process are continuously performed, and the synergetic effect of these elements prevents reaggregation and improves the dispersion stability. There is also an effect of destruction or sterilization of bacteria due to collision of charged particles in plasma.
Preferably, air is supplied prior to the in-liquid plasma treatment. By supplying air, the effect of plasma treatment is uniformly spread in the solution because it is discharged in the air bubbles.
湿式微粒化処理のための装置は、プラズマ処理した抽出物を還流させるポンプを備えていても良い。ポンプを備えていることにより、高圧噴射し、液中プラズマ処理する作業が複数回繰り返される。
繰り返す回数は1−30回であることが好ましい。30回を超えても、それ以上脂溶性成分の抽出効率は向上しないためである。
The apparatus for the wet atomization process may include a pump for refluxing the plasma-treated extract. By providing the pump, the operation of performing high-pressure injection and in-liquid plasma processing is repeated multiple times.
The number of repetitions is preferably 1 to 30 times. Even if it exceeds 30 times, the extraction efficiency of the fat-soluble component is not further improved.
上記の微粒化処理によって形成された粒子の5%以上が粒径1μm−100μmの範囲内である。微粒化処理によってマイクロサイズの粒子を形成することで、藻類の細胞に含まれる脂溶性成分をより効率よく抽出することができる。
さらに、抽出物中には高濃度の脂溶性成分が含まれている。例えば、上記方法であればフコキサンチンの濃度が1.5mg/g以上となる。
At least 5% of the particles formed by the above-mentioned atomization treatment are in the range of 1 μm to 100 μm in particle diameter. By forming micro-sized particles by atomization treatment, fat-soluble components contained in algal cells can be extracted more efficiently.
Furthermore, the extract contains a high concentration of fat-soluble components. For example, if it is the said method, the density | concentration of fucoxanthin will be 1.5 mg / g or more.
上記方法によって得られた脂溶性成分を有効成分として含有する本発明の脂溶性成分高濃度含有抽出物は、各種用途に使用することができる。 The extract with high concentration of a fat-soluble component of the present invention containing the fat-soluble component obtained by the above method as an active ingredient can be used for various uses.
本発明の脂溶性成分高濃度含有抽出物は、食品添加剤として、例えば清涼飲料水、乳製品(加工乳、ヨーグルト)、菓子類(ゼリー、チョコレート、ビスケット、ガム、錠菓)又はサプリメント等の各種飲食品に配合することもできる。 The extract with high fat-soluble ingredient concentration of the present invention is a food additive such as soft drink, dairy product (processed milk, yogurt), confectionery product (jelly, chocolate, biscuit, gum, tablets) or supplement etc. It can also be blended in various food and drink products.
食品添加剤として使用する場合、その添加量については、特に限定されず、食品の種類に応じて適宜決定すればよい。一例としては、上記した抽出物の乾燥重量として、含有量が1〜50mg/g程度の範囲となるように添加すればよい。 When used as a food additive, the addition amount thereof is not particularly limited, and may be appropriately determined according to the type of food. As an example, the dry weight of the above-mentioned extract may be added so that the content is in the range of about 1 to 50 mg / g.
上記食品用途としては、例えば、パン類、菓子類、麺類、米飯類、餅類、パスタ類、ドレッシング類、ムース、ゼリーおよびスープなどを挙げることができる。 Examples of the above-mentioned food use include breads, confectionery, noodles, cooked rice, potatoes, pasta, dressings, mousse, jelly and soup.
食品の形態としては、特に限定はないが、例えばバータイプ食品、ブロックタイプ食品あるいはチアーバックタイプ食品などの場合、経口摂取が容易となる。また、飲料用途としては、例えばジュース類、乳飲料、アルコール飲料、茶飲料などを挙げることができる。また、特定保健用食品や栄養補助剤、栄養剤、いわゆる健康食品としての利用も挙げられる。 The form of the food is not particularly limited, but in the case of, for example, a bar-type food, a block-type food or a tearback-type food, oral intake is facilitated. Moreover, as beverages, for example, juices, milk beverages, alcoholic beverages, tea beverages and the like can be mentioned. In addition, food for specified health use, nutritional supplement, nutritional agent, and so-called health food may be used.
化粧品用途としては、肌のくすみ防止、肌荒れ防止、しみ防止、しわの改善、皮膚の若返りを目的として、乳液、クリーム、化粧水、美容液、パック、洗浄料、ファンデーション、頬紅、口紅等のメーキャップ化粧料、養毛料、ヘアトニック、シャンプー、リンス等の頭皮化粧料、分散液、軟膏、液剤、エアゾール、貼付剤での用途が挙げられる。 For cosmetic use, it is intended to prevent skin dullness, rough skin, prevent stains, improve wrinkles, rejuvenate skin, make up of milky lotion, cream, lotion, essence, pack, cleansing agent, foundation, blush, lipstick etc. Applications include scalp cosmetics such as cosmetics, hair tonics, hair tonics, shampoos, and rinses, dispersions, ointments, solutions, aerosols, and patches.
以下、本発明の実施例を説明することにより、本発明の効果をより明確なものとする。但し、本発明は以下の実施例には限定されない。 Hereinafter, the effects of the present invention will be made clearer by describing examples of the present invention. However, the present invention is not limited to the following examples.
脂溶性成分高濃度含有抽出物の製造
(実施例1)
原料に用いる珪藻類(Phaeodactylum tricornutum)はf/2培地を用いて培養した。培養は、22℃の恒温室内で500Lの水槽(ポリカーボネート製)を用い100μmol m−2 S−1(明期24時間)にて10日間培養した。
得られた培養液は遠心分離(3,000rpm、10分間)に供し、上清を除去し沈殿物として珪藻を回収した。回収した珪藻は中鎖脂肪酸(パナセート810、日油株式会社製)と重量比1:1となるように混ぜ合わせた。
その後この混合物を、高圧ノズルの圧力を250MPaとした湿式ジェットミルに4回供し、抽出物を得た。
得られた抽出物を遠心分離(3000rpm、10分間等)して、脂溶性成分を含む上清を脂肪酸が溶解する抽出液として回収した。
抽出液約1gをメタノールに溶解後、超音波装置にて5分間処理し、その後100mLに定容した。これを実施例1とした。
Production of an extract containing a high concentration of a fat-soluble component (Example 1)
The diatom (Phaeodactylum tricornutum) used as a raw material was cultured using f / 2 medium. The culture was performed for 10 days in 100 μmol m −2 S −1 (light period 24 hours) using a 500 L water tank (made of polycarbonate) in a constant temperature room at 22 ° C.
The obtained culture solution was subjected to centrifugation (3,000 rpm, 10 minutes), the supernatant was removed, and diatoms were collected as a precipitate. The recovered diatoms were mixed with medium-chain fatty acids (Panacet 810, manufactured by NOF Corporation) at a weight ratio of 1: 1.
The mixture was then subjected to a wet jet mill at a high pressure nozzle pressure of 250 MPa four times to obtain an extract.
The obtained extract was centrifuged (3000 rpm, 10 minutes, etc.) to recover the supernatant containing the fat-soluble component as an extract in which fatty acids are dissolved.
About 1 g of the extract was dissolved in methanol, treated with an ultrasonic device for 5 minutes, and then adjusted to 100 mL. This is referred to as Example 1.
(比較例1)
原料に用いる珪藻類(Phaeodactylum tricornutum)はf/2培地を用いて培養した。培養は、22℃の恒温室内で500Lの水槽(ポリカーボネート製)を用い100μmol m−2 S−1(明期24時間)にて10日間培養した。
得られた培養液は遠心分離(3,000rpm、10分間)に供し、上清を除去し沈殿物として珪藻を回収した。
回収したサンプル13.80gを同重量のエタノールで10分間超音波処理した。得られた混合物を遠心分離(3000rpm、10分間)して、脂溶性成分を含む上清を脂肪酸が溶解する抽出液として回収した。抽出液約1gをメタノールに溶解後、超音波装置にて5分間処理し、その後100mLに定容した。これを比較例1とした。
(Comparative example 1)
The diatom (Phaeodactylum tricornutum) used as a raw material was cultured using f / 2 medium. The culture was performed for 10 days in 100 μmol m −2 S −1 (light period 24 hours) using a 500 L water tank (made of polycarbonate) in a constant temperature room at 22 ° C.
The obtained culture solution was subjected to centrifugation (3,000 rpm, 10 minutes), the supernatant was removed, and diatoms were collected as a precipitate.
13.80 g of the recovered sample was sonicated with an equal weight of ethanol for 10 minutes. The resulting mixture was centrifuged (3000 rpm, 10 minutes) to recover the supernatant containing the fat-soluble component as an extract in which fatty acids are dissolved. About 1 g of the extract was dissolved in methanol, treated with an ultrasonic device for 5 minutes, and then adjusted to 100 mL. This is Comparative Example 1.
2.抽出効率の比較
実施例1及び比較例1のフコキサンチンの抽出効率を測定するために、HPLCカラムを用いた液体クロマトグラフィー分析を行った。分析の条件は以下の通りである。
・装置 LC−20AT、及び紫外可視吸光光度計 SPD−20A
(株式会社島津製作所製)
・カラム Tosoh TSK−Gel ODS−80TM
Φ4.6mm×250mm(東ソー株式会社製)
・移動相 メタノール:水=90:10
・流量 1.0ml/分
・カラム温度 40℃
・SPD−20A解析波長 450nm
2. In order to measure the extraction efficiency of fucoxanthin of Comparative Example 1 and Comparative Example 1 of extraction efficiency, liquid chromatography analysis using an HPLC column was performed. The conditions of analysis are as follows.
・ Apparatus LC-20AT, and UV-visible spectrophotometer SPD-20A
(Made by Shimadzu Corporation)
・ Column Tosoh TSK-Gel ODS-80TM
4.6 4.6 mm × 250 mm (made by Tosoh Corporation)
Mobile phase methanol: water = 90: 10
・ Flow rate 1.0 ml / min ・ Column temperature 40 ° C
・ SPD-20A analysis wavelength 450nm
その後、同じ条件及び装置にてフコキサンチンの標準品、実施例1及び比較例1を分析し、フコキサンチンの濃度を測定した。結果を以下の表1に示す。 Thereafter, standard fucoxanthin, Example 1 and Comparative Example 1 were analyzed under the same conditions and apparatus to measure the concentration of fucoxanthin. The results are shown in Table 1 below.
上記の表1記載の結果は、本発明の抽出方法で得られた実施例1におけるフコキサンチン濃度、従来の方法(エタノール中における超音波処理による抽出、比較例1)と比較して高いことを示した。
つまり、本発明の抽出方法は、従来のエタノールによる抽出よりもフコキサンチンの抽出効率が高いことがわかった。
The results described in Table 1 above indicate that the fucoxanthin concentration in Example 1 obtained by the extraction method of the present invention is higher than that in the conventional method (extraction by ultrasonication in ethanol, Comparative Example 1). Indicated.
That is, it was found that the extraction method of the present invention has a higher fucoxanthin extraction efficiency than conventional ethanol extraction.
3.湿式微粒化処理回数と抽出効率の関係
(比較例2、及び実施例2−4)
原料に用いる珪藻類(Phaeodactylum tricornutum)はf/2培地を用いて培養した。培養は、22℃の恒温室内で500Lの水槽(ポリカーボネート製)を用い100μmol m−2 S−1(明期24時間)にて10日間培養した。
得られた培養液は遠心分離(3,000rpm、10分間等)に供し、上清を除去し沈殿物として珪藻を回収した。
回収した珪藻2,400gを400gの中鎖脂肪酸(パナセート810、日油株式会社製)と混ぜ合わせ、その後0回、1回、3回、4回湿式微粒化処理した。これらをそれぞれ比較例2、実施例2、3、4とした。この時のフコキサンチンの濃度を以下の表2に示す。
3. Relationship between the number of wet atomization processes and the extraction efficiency (Comparative Example 2 and Example 2-4)
The diatom (Phaeodactylum tricornutum) used as a raw material was cultured using f / 2 medium. The culture was performed for 10 days in 100 μmol m −2 S −1 (light period 24 hours) using a 500 L water tank (made of polycarbonate) in a constant temperature room at 22 ° C.
The obtained culture solution was subjected to centrifugation (3,000 rpm, 10 minutes, etc.), the supernatant was removed, and diatoms were collected as a precipitate.
2,400 g of the recovered diatoms were mixed with 400 g of medium-chain fatty acid (Panacet 810, manufactured by NOF Corporation), and then subjected to wet atomization treatment zero times, once, three times, and four times. These were designated as Comparative Example 2 and Examples 2, 3 and 4, respectively. The concentration of fucoxanthin at this time is shown in Table 2 below.
上記抽出方法における湿式微粒化処理を珪藻類追加で複数回繰り返すことで、脂溶性成分の抽出効率が上がることを示した。 It was shown that the extraction efficiency of the fat-soluble component is improved by repeating the wet atomization treatment in the above extraction method a plurality of times by adding diatoms.
簡易加速試験(フコキサンチンの保存安定性試験)
本発明を冷凍(−20℃)、冷蔵(4℃)、常温(25℃)暗所下で保管し、1か月後のフコキサンチン濃度を測定した。
Simple accelerated test (storage stability test of fucoxanthin)
The present invention was stored under refrigeration (-20.degree. C.), refrigeration (4.degree. C.), normal temperature (25.degree. C.) and dark place, and the fucoxanthin concentration after 1 month was measured.
(実施例5)
原料に用いる珪藻類(Phaeodactylum tricornutum)はf/2培地を用いて培養した。培養は、22℃の恒温室内で500Lの水槽(ポリカーボネート製)を用い100μmol m−2 S−1(明期24時間)にて10日間培養した。
得られた培養液は遠心分離(3,000rpm、10分間等)に供し、上清を除去し沈殿物として珪藻を回収した。
回収した珪藻約1kgに同重量の中鎖脂肪酸を添加し、高圧ノズルの圧力を250MPaとした湿式ジェットミルによる処理を4回繰り返した。これを実施例5とした。
(Example 5)
The diatom (Phaeodactylum tricornutum) used as a raw material was cultured using f / 2 medium. The culture was performed for 10 days in 100 μmol m −2 S −1 (light period 24 hours) using a 500 L water tank (made of polycarbonate) in a constant temperature room at 22 ° C.
The obtained culture solution was subjected to centrifugation (3,000 rpm, 10 minutes, etc.), the supernatant was removed, and diatoms were collected as a precipitate.
The same weight of medium-chain fatty acid was added to about 1 kg of the collected diatoms, and treatment with a wet jet mill was repeated four times with the pressure of the high pressure nozzle set to 250 MPa. This is taken as Example 5.
実施例5の加速試験開始時のフコキサンチン濃度は2.86mg/gであった。これをそれぞれ冷凍(−20℃)、冷蔵(4℃)、常温(25℃)暗所下で保管した。
1か月保管後、実施例5のフコキサンチン濃度は冷凍保管で2.35mg/g、冷蔵保管で2.25mg/g、常温保管で2.30mg/gであった。同じく2か月保管後の実施例5のフコキサンチン濃度は冷凍保管で2.42mg/g、冷蔵保管で2.34mg/g、常温保管で2.30mg/gであった。
つまり保存率は2か月間経過しても冷凍で82%以上、冷蔵で78%以上、常温で80%であった。
いずれの保存方法でも、8割程度のフコキサンチンが保存されることがわかった。
The fucoxanthin concentration at the start of the accelerated test of Example 5 was 2.86 mg / g. They were stored under refrigeration (−20 ° C.), refrigeration (4 ° C.) and normal temperature (25 ° C.) in the dark, respectively.
After storage for one month, the fucoxanthin concentration in Example 5 was 2.35 mg / g in frozen storage, 2.25 mg / g in refrigerated storage, and 2.30 mg / g in normal temperature storage. Similarly, the fucoxanthin concentration of Example 5 after storage for 2 months was 2.42 mg / g in frozen storage, 2.34 mg / g in refrigerated storage, and 2.30 mg / g in normal temperature storage.
That is, even after 2 months, the preservation rate was 82% or more for freezing, 78% or more for refrigeration, and 80% for normal temperature.
About 80% of fucoxanthin was found to be preserved by any preservation method.
この保存率の高さは、湿式微粒化処理による物理的作用に起因すると考えられる。
つまり、本発明の抽出方法でフコキサンチンを抽出すると、フコキサンチンの保存率が高い脂溶性成分高濃度含有抽出物を得ることができる。
The high storage rate is considered to be due to the physical action of the wet atomization treatment.
That is, when fucoxanthin is extracted by the extraction method of the present invention, it is possible to obtain an extract containing a high concentration of a fat-soluble component having a high storage rate of fucoxanthin.
本発明は、化粧品として使用すれば美肌効果やアンチエイジング効果が期待でき、食品として摂取すれば動脈硬化や生活習慣病の予防、抗腫瘍作用、神経細胞保護作用が期待でき、乳液や化粧水などの化粧品、清涼飲料水、乳製品、菓子類又はサプリメント等の各種飲食品の添加剤に好適に使用することができる。 The present invention can be expected to be a skin-care effect and an anti-aging effect when used as a cosmetic, and can be expected to prevent arteriosclerosis and lifestyle-related diseases, to have an antitumor effect and a nerve cell protection action when taken as a food. It can be suitably used as an additive for various food and drink such as cosmetics, soft drinks, dairy products, confectionery products or supplements.
Claims (4)
(1)珪藻類を粉砕する工程、
(2)粉砕した珪藻類に中鎖脂肪酸を添加してなる溶液を作製する工程、及び
(3)該溶液を湿式微粒化処理して抽出物を得る工程
を含み、
湿式微粒化処理が、
(a)該溶液を高圧ノズルから高圧噴射し微粒化処理する工程、
(b)微粒化処理した溶液にエアを供給する工程、
(c)エアを供給することによって形成された気泡中で放電させ、液中プラズマ処理し、フコキサンチンを含む抽出物を得る工程、
を含むことを特徴とする、方法。 Fucoxanthin from silicofluoride algae A method for extracting at a concentration of at least 1.5 mg / g,
(1) a step of pulverizing the silicofluoride algae,
(2) a step to prepare a solution prepared by adding a medium chain fatty acid into crashed silicofluoride algae, and (3) obtaining an extract with the solution was treated wet atomization,
Wet atomization process,
(A) a step of subjecting the solution to high pressure injection from a high pressure nozzle and atomizing treatment;
(B) supplying air to the atomized solution,
(C) discharging in air bubbles formed by supplying air, performing in-liquid plasma treatment to obtain an extract containing fucoxanthin ,
The features and-law including, method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2016214651A JP6546578B2 (en) | 2016-11-01 | 2016-11-01 | Method for extracting fat-soluble components from algae |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2016214651A JP6546578B2 (en) | 2016-11-01 | 2016-11-01 | Method for extracting fat-soluble components from algae |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2018068245A JP2018068245A (en) | 2018-05-10 |
JP6546578B2 true JP6546578B2 (en) | 2019-07-17 |
Family
ID=62112312
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2016214651A Active JP6546578B2 (en) | 2016-11-01 | 2016-11-01 | Method for extracting fat-soluble components from algae |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP6546578B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2020029492A (en) * | 2018-08-21 | 2020-02-27 | 国立大学法人北海道大学 | Method for efficiently extracting lipophilic functional component by edible oil |
KR102345998B1 (en) * | 2018-10-24 | 2022-01-04 | 가천대학교 산학협력단 | Method and system for reducing harmful generated-substances including benzopyrene of argricultural processed goods using cold plasma |
JP7237689B2 (en) | 2019-03-28 | 2023-03-13 | 株式会社ナリス化粧品 | Screening method for agent for improving skin barrier function caused by stress |
CN111205179B (en) * | 2020-01-09 | 2022-07-19 | 青岛科海生物有限公司 | Method for comprehensively extracting EPA and fucoxanthin from Phaeodactylum tricornutum |
KR20240003888A (en) * | 2022-07-04 | 2024-01-11 | 주식회사 피글 | High efficient extraction method for extracting active ingredient of vegetability solide material and apparatus for the same |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2923919B2 (en) * | 1993-06-25 | 1999-07-26 | 美穂 田中 | Edible oil suspension containing ground alga and its production method |
JP2004089158A (en) * | 2002-07-10 | 2004-03-25 | Shirako:Kk | Method for extracting oil-soluble component of seaweed and use of extract |
JP2010006783A (en) * | 2008-06-30 | 2010-01-14 | Kagawa Industry Support Foundation | Method and apparatus for extracting fucoxanthin from seaweed |
JP4870787B2 (en) * | 2009-01-20 | 2012-02-08 | 株式会社サウスプロダクト | Process for producing fucoxanthin and / or fucosterol |
JP2015231975A (en) * | 2014-06-10 | 2015-12-24 | 株式会社日本触媒 | Fucoxanthin extracted from microalga |
JP6392652B2 (en) * | 2014-12-05 | 2018-09-19 | 株式会社スギノマシン | Wet atomization method and wet atomization apparatus |
JP6348056B2 (en) * | 2014-12-05 | 2018-06-27 | 株式会社スギノマシン | Wet atomization method and wet atomization apparatus |
-
2016
- 2016-11-01 JP JP2016214651A patent/JP6546578B2/en active Active
Also Published As
Publication number | Publication date |
---|---|
JP2018068245A (en) | 2018-05-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6546578B2 (en) | Method for extracting fat-soluble components from algae | |
US9138452B2 (en) | Plant derived seed extract rich in essential fatty acids derived from Perilla seed: composition of matter, manufacturing process and use | |
TWI679029B (en) | Emulsified composition | |
US9096508B2 (en) | Method for producing carotenoid composition | |
CN102100260B (en) | Yeast grease and preparation method and application thereof | |
Coelho et al. | Integral valorisation of tomato by-products towards bioactive compounds recovery: Human health benefits | |
Rodríguez-Sifuentes et al. | Importance of downstream processing of natural astaxanthin for pharmaceutical application | |
Vernès et al. | Biorefinery concept as a key for sustainable future to green chemistry—the case of microalgae | |
JP2013202005A (en) | Curcumin-containing oil and fat, and method for producing the same | |
Satheesh | REVIEW ON PRODUCTION AND POTENTIAL APPLICATIONS OF VIRGIN COCONUT OIL. | |
JP4074652B1 (en) | Method for producing catechin derivative | |
JP2007124917A (en) | Method for producing rice oil richly containing oryzanol, and usage of the rice oil | |
Yang et al. | Technological readiness of commercial microalgae species for foods | |
EP2802335B1 (en) | Use of avocado kernel to obtain avocado oil enriched in alkyl polyols and/or their acetylated derivatives | |
Stolp et al. | Naturally occurring high-oleic oils: Avocado, macadamia, and olive oils | |
JPH0799932A (en) | Health food containing phaffia coloring matter oil | |
US9414620B2 (en) | Perilla seed composition | |
JP2008297214A (en) | Composition having skin-beautifying effect | |
Laurora et al. | Application of ultrasound to obtain food additives and nutraceuticals | |
EP2802336B1 (en) | Use of avocado skin to obtain unsaponifiable matter enriched with saturated aliphatic hydrocarbons and with sterols | |
KR102072111B1 (en) | Antioxidant composition comprising defatted perilla extract as effective component and manufacturing method thereof | |
CN110087491A (en) | Food or beverage based on marine microalgae | |
Thao et al. | 11 Extraction of Fatty Acids | |
JP2008274106A (en) | Method of manufacturing sphingolipid-containing composition | |
JP5499352B2 (en) | Antioxidants, food and drink, cosmetics, quasi drugs, and whitening agents |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20180622 |
|
A871 | Explanation of circumstances concerning accelerated examination |
Free format text: JAPANESE INTERMEDIATE CODE: A871 Effective date: 20180622 |
|
A975 | Report on accelerated examination |
Free format text: JAPANESE INTERMEDIATE CODE: A971005 Effective date: 20180712 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20180725 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20180911 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20181203 |
|
A601 | Written request for extension of time |
Free format text: JAPANESE INTERMEDIATE CODE: A601 Effective date: 20190122 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20190327 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20190529 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20190621 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 6546578 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |
|
R250 | Receipt of annual fees |
Free format text: JAPANESE INTERMEDIATE CODE: R250 |