CN107099564A - The method for producing fucoxanthin using the smooth rhombus algae of Heterotrophic culture - Google Patents
The method for producing fucoxanthin using the smooth rhombus algae of Heterotrophic culture Download PDFInfo
- Publication number
- CN107099564A CN107099564A CN201710523735.6A CN201710523735A CN107099564A CN 107099564 A CN107099564 A CN 107099564A CN 201710523735 A CN201710523735 A CN 201710523735A CN 107099564 A CN107099564 A CN 107099564A
- Authority
- CN
- China
- Prior art keywords
- fucoxanthin
- rhombus algae
- fermentation
- smooth
- content range
- 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.)
- Pending
Links
- 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 title claims abstract description 110
- 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 title claims abstract description 110
- 241000195493 Cryptophyta Species 0.000 title claims abstract description 28
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 16
- 230000004151 fermentation Effects 0.000 claims abstract description 46
- 238000000855 fermentation Methods 0.000 claims abstract description 45
- 238000000034 method Methods 0.000 claims abstract description 21
- 238000002360 preparation method Methods 0.000 claims abstract description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 64
- 239000002609 medium Substances 0.000 claims description 41
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 claims description 33
- 229910052757 nitrogen Inorganic materials 0.000 claims description 32
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 24
- 239000008103 glucose Substances 0.000 claims description 24
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 21
- 229910052799 carbon Inorganic materials 0.000 claims description 21
- 241001104939 Nitzschia laevis Species 0.000 claims description 20
- 239000002994 raw material Substances 0.000 claims description 20
- 239000004317 sodium nitrate Substances 0.000 claims description 17
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 16
- 235000010344 sodium nitrate Nutrition 0.000 claims description 16
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 12
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims description 12
- 239000001888 Peptone Substances 0.000 claims description 11
- 108010080698 Peptones Proteins 0.000 claims description 11
- 239000001963 growth medium Substances 0.000 claims description 11
- 235000019319 peptone Nutrition 0.000 claims description 11
- 238000011218 seed culture Methods 0.000 claims description 8
- 239000004115 Sodium Silicate Substances 0.000 claims description 7
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 7
- 229940041514 candida albicans extract Drugs 0.000 claims description 7
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 7
- 239000012138 yeast extract Substances 0.000 claims description 7
- 239000007983 Tris buffer Substances 0.000 claims description 6
- 239000000284 extract Substances 0.000 claims description 6
- 235000010333 potassium nitrate Nutrition 0.000 claims description 6
- 239000004323 potassium nitrate Substances 0.000 claims description 6
- 239000011780 sodium chloride Substances 0.000 claims description 6
- LENZDBCJOHFCAS-UHFFFAOYSA-N tris Chemical compound OCC(N)(CO)CO LENZDBCJOHFCAS-UHFFFAOYSA-N 0.000 claims description 6
- 125000001477 organic nitrogen group Chemical group 0.000 claims description 5
- 229910003208 (NH4)6Mo7O24·4H2O Inorganic materials 0.000 claims description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 4
- 239000004111 Potassium silicate Substances 0.000 claims description 4
- 229930006000 Sucrose Natural products 0.000 claims description 4
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 claims description 4
- 150000001413 amino acids Chemical class 0.000 claims description 4
- 239000004202 carbamide Substances 0.000 claims description 4
- 239000002054 inoculum Substances 0.000 claims description 4
- NNHHDJVEYQHLHG-UHFFFAOYSA-N potassium silicate Chemical compound [K+].[K+].[O-][Si]([O-])=O NNHHDJVEYQHLHG-UHFFFAOYSA-N 0.000 claims description 4
- 229910052913 potassium silicate Inorganic materials 0.000 claims description 4
- 235000019353 potassium silicate Nutrition 0.000 claims description 4
- 239000005720 sucrose Substances 0.000 claims description 4
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 3
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 claims description 3
- 235000012538 ammonium bicarbonate Nutrition 0.000 claims description 3
- 239000001099 ammonium carbonate Substances 0.000 claims description 3
- 235000021433 fructose syrup Nutrition 0.000 claims description 3
- 239000003531 protein hydrolysate Substances 0.000 claims description 3
- 239000000460 chlorine Substances 0.000 claims description 2
- 239000012530 fluid Substances 0.000 claims 2
- 241000894006 Bacteria Species 0.000 claims 1
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims 1
- 229910021580 Cobalt(II) chloride Inorganic materials 0.000 claims 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims 1
- 239000007836 KH2PO4 Substances 0.000 claims 1
- 229910021380 Manganese Chloride Inorganic materials 0.000 claims 1
- GLFNIEUTAYBVOC-UHFFFAOYSA-L Manganese chloride Chemical compound Cl[Mn]Cl GLFNIEUTAYBVOC-UHFFFAOYSA-L 0.000 claims 1
- 229910004619 Na2MoO4 Inorganic materials 0.000 claims 1
- 235000003283 Pachira macrocarpa Nutrition 0.000 claims 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims 1
- 240000001085 Trapa natans Species 0.000 claims 1
- 235000014364 Trapa natans Nutrition 0.000 claims 1
- YADYSHISCDOTDA-UHFFFAOYSA-N azane;silicic acid Chemical compound N.O[Si](O)(O)O YADYSHISCDOTDA-UHFFFAOYSA-N 0.000 claims 1
- 239000001110 calcium chloride Substances 0.000 claims 1
- 229910001628 calcium chloride Inorganic materials 0.000 claims 1
- 229910052801 chlorine Inorganic materials 0.000 claims 1
- 235000017168 chlorine Nutrition 0.000 claims 1
- FDJOLVPMNUYSCM-WZHZPDAFSA-L cobalt(3+);[(2r,3s,4r,5s)-5-(5,6-dimethylbenzimidazol-1-yl)-4-hydroxy-2-(hydroxymethyl)oxolan-3-yl] [(2r)-1-[3-[(1r,2r,3r,4z,7s,9z,12s,13s,14z,17s,18s,19r)-2,13,18-tris(2-amino-2-oxoethyl)-7,12,17-tris(3-amino-3-oxopropyl)-3,5,8,8,13,15,18,19-octamethyl-2 Chemical compound [Co+3].N#[C-].N([C@@H]([C@]1(C)[N-]\C([C@H]([C@@]1(CC(N)=O)C)CCC(N)=O)=C(\C)/C1=N/C([C@H]([C@@]1(CC(N)=O)C)CCC(N)=O)=C\C1=N\C([C@H](C1(C)C)CCC(N)=O)=C/1C)[C@@H]2CC(N)=O)=C\1[C@]2(C)CCC(=O)NC[C@@H](C)OP([O-])(=O)O[C@H]1[C@@H](O)[C@@H](N2C3=CC(C)=C(C)C=C3N=C2)O[C@@H]1CO FDJOLVPMNUYSCM-WZHZPDAFSA-L 0.000 claims 1
- 229910000396 dipotassium phosphate Inorganic materials 0.000 claims 1
- 229910052564 epsomite Inorganic materials 0.000 claims 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 claims 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 claims 1
- 239000011565 manganese chloride Substances 0.000 claims 1
- 229910000402 monopotassium phosphate Inorganic materials 0.000 claims 1
- 235000009165 saligot Nutrition 0.000 claims 1
- 235000019795 sodium metasilicate Nutrition 0.000 claims 1
- 239000011684 sodium molybdate Substances 0.000 claims 1
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 claims 1
- 239000011715 vitamin B12 Substances 0.000 claims 1
- 239000011592 zinc chloride Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 12
- 239000002028 Biomass Substances 0.000 abstract description 10
- 239000000843 powder Substances 0.000 abstract description 9
- 241001474374 Blennius Species 0.000 abstract description 8
- 238000000605 extraction Methods 0.000 abstract description 3
- 244000005700 microbiome Species 0.000 abstract description 2
- 238000011109 contamination Methods 0.000 abstract 1
- 241000180701 Nitzschia <flatworm> Species 0.000 description 22
- 230000000694 effects Effects 0.000 description 11
- YBJHBAHKTGYVGT-ZKWXMUAHSA-N (+)-Biotin Chemical compound N1C(=O)N[C@@H]2[C@H](CCCCC(=O)O)SC[C@@H]21 YBJHBAHKTGYVGT-ZKWXMUAHSA-N 0.000 description 10
- 238000004458 analytical method Methods 0.000 description 9
- 210000004027 cell Anatomy 0.000 description 9
- 241000206761 Bacillariophyta Species 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 241000736262 Microbiota Species 0.000 description 6
- 229960002685 biotin Drugs 0.000 description 5
- 235000020958 biotin Nutrition 0.000 description 5
- 239000011616 biotin Substances 0.000 description 5
- FDJOLVPMNUYSCM-UVKKECPRSA-L cobalt(3+);[(2r,3s,4r,5s)-5-(5,6-dimethylbenzimidazol-1-yl)-4-hydroxy-2-(hydroxymethyl)oxolan-3-yl] [(2r)-1-[3-[(2r,3r,4z,7s,9z,12s,13s,14z,17s,18s,19r)-2,13,18-tris(2-amino-2-oxoethyl)-7,12,17-tris(3-amino-3-oxopropyl)-3,5,8,8,13,15,18,19-octamethyl-2,7, Chemical compound [Co+3].N#[C-].C1([C@H](CC(N)=O)[C@@]2(C)CCC(=O)NC[C@@H](C)OP([O-])(=O)O[C@H]3[C@H]([C@H](O[C@@H]3CO)N3C4=CC(C)=C(C)C=C4N=C3)O)[N-]\C2=C(C)/C([C@H](C\2(C)C)CCC(N)=O)=N/C/2=C\C([C@H]([C@@]/2(CC(N)=O)C)CCC(N)=O)=N\C\2=C(C)/C2=N[C@]1(C)[C@@](C)(CC(N)=O)[C@@H]2CCC(N)=O FDJOLVPMNUYSCM-UVKKECPRSA-L 0.000 description 5
- 238000001514 detection method Methods 0.000 description 5
- 230000012010 growth Effects 0.000 description 5
- 238000004128 high performance liquid chromatography Methods 0.000 description 5
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 4
- 238000011081 inoculation Methods 0.000 description 4
- 239000011734 sodium Substances 0.000 description 4
- WEVYAHXRMPXWCK-UHFFFAOYSA-N Acetonitrile Chemical group CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 3
- 241001147476 Cyclotella Species 0.000 description 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 241000289371 Ornithorhynchus anatinus Species 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 235000019270 ammonium chloride Nutrition 0.000 description 2
- 230000003698 anagen phase Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 239000013028 medium composition Substances 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 230000004580 weight loss Effects 0.000 description 2
- ZNEMGFATAVGQSF-UHFFFAOYSA-N 1-(2-amino-6,7-dihydro-4H-[1,3]thiazolo[4,5-c]pyridin-5-yl)-2-[5-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]-1,3,4-oxadiazol-2-yl]ethanone Chemical compound NC=1SC2=C(CN(CC2)C(CC=2OC(=NN=2)C=2C=NC(=NC=2)NC2CC3=CC=CC=C3C2)=O)N=1 ZNEMGFATAVGQSF-UHFFFAOYSA-N 0.000 description 1
- 241000206751 Chrysophyceae Species 0.000 description 1
- 206010061218 Inflammation Diseases 0.000 description 1
- 235000007688 Lycopersicon esculentum Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- 241000502321 Navicula Species 0.000 description 1
- 241000015177 Saccharina japonica Species 0.000 description 1
- 240000003768 Solanum lycopersicum Species 0.000 description 1
- 241001607776 Surirellales Species 0.000 description 1
- 241001261506 Undaria pinnatifida Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 210000001789 adipocyte Anatomy 0.000 description 1
- 125000003046 allene group Chemical group 0.000 description 1
- 230000003527 anti-angiogenesis Effects 0.000 description 1
- 230000001093 anti-cancer Effects 0.000 description 1
- 230000000078 anti-malarial effect Effects 0.000 description 1
- 230000003579 anti-obesity Effects 0.000 description 1
- 230000003064 anti-oxidating effect Effects 0.000 description 1
- 239000003430 antimalarial agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- 230000036983 biotransformation Effects 0.000 description 1
- 210000004204 blood vessel Anatomy 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 210000004556 brain Anatomy 0.000 description 1
- 235000021466 carotenoid Nutrition 0.000 description 1
- 150000001747 carotenoids Chemical class 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 238000012364 cultivation method Methods 0.000 description 1
- 206010012601 diabetes mellitus Diseases 0.000 description 1
- 238000009509 drug development Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 210000001508 eye Anatomy 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 230000005714 functional activity Effects 0.000 description 1
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 235000013402 health food Nutrition 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 238000009655 industrial fermentation Methods 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N nitrate group Chemical group [N+](=O)([O-])[O-] NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 238000012803 optimization experiment Methods 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 230000029553 photosynthesis Effects 0.000 description 1
- 238000010672 photosynthesis Methods 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 150000003071 polychlorinated biphenyls Chemical class 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical class O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 210000003491 skin Anatomy 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P17/00—Preparation of heterocyclic carbon compounds with only O, N, S, Se or Te as ring hetero atoms
- C12P17/02—Oxygen as only ring hetero atoms
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N1/00—Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
- C12N1/12—Unicellular algae; Culture media therefor
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Biotechnology (AREA)
- Zoology (AREA)
- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Microbiology (AREA)
- Tropical Medicine & Parasitology (AREA)
- Cell Biology (AREA)
- Medicinal Chemistry (AREA)
- Virology (AREA)
- Biomedical Technology (AREA)
- Botany (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
本发明属于微生物的培养,特别是指一种利用异养培养平滑菱形藻生产岩藻黄素的方法。包括种子液的制备、发酵培养、发酵结束后的发酵液中提取岩藻黄素等步骤,本发明解决了现有技术中存在的异养条件下平滑菱形藻的生物量浓度、岩藻黄素产率及岩藻黄素含量低等问题。具有所制备的平滑菱形藻干燥藻粉中岩藻黄素的含量高,岩藻黄素的产率高,较大型海藻来源的岩藻黄素更安全,在提高生产效率、降低生产成本的同时,大大降低了培养过程中的污染风险等优点。
The invention belongs to the cultivation of microorganisms, and in particular refers to a method for producing fucoxanthin by using heterotrophic cultivation of Nishina smoothis. Including the preparation of seed liquid, fermentation culture, extraction of fucoxanthin from the fermentation liquid after fermentation, etc., the present invention solves the problems of biomass concentration and fucoxanthin of Nitzkirella smoothis under heterotrophic conditions existing in the prior art. Problems such as low yield and fucoxanthin content. The content of fucoxanthin in the prepared dry algae powder of Nishida smoothis is high, the yield of fucoxanthin is high, and it is safer than the fucoxanthin derived from large seaweeds. It improves production efficiency and reduces production costs at the same time , greatly reducing the risk of contamination during the cultivation process and other advantages.
Description
技术领域technical field
本发明属于微生物的培养,特别是指一种利用异养培养平滑菱形藻生产岩藻黄素的方法。The invention belongs to the cultivation of microorganisms, and in particular refers to a method for producing fucoxanthin by using heterotrophic cultivation of Nishina smoothis.
背景技术Background technique
岩藻黄素(Fucoxanthin),又称岩藻黄质、褐藻素,主要来自大藻、硅藻及金藻等大型海藻和微藻,是一种天然的类胡萝卜素,参与光合作用中光系统II的反应。因其具有独特的丙二烯结构,岩藻黄素是一种具有强抗氧化性的活性分子。近年来研究发现,岩藻黄素在细胞、动物以及人体都证实具有多种功能活性,包括抗氧化、抗炎症、抗癌、抗肥胖、抗糖尿病、抗血管生成和抗疟等生理活性,且对肝脏、脑部血管、骨骼、皮肤和眼睛等器官具有保护作用。综合以上功能,岩藻黄素是一种具有广阔保健食品和药物开发前景的天然产物,岩藻黄素的市场容量500吨,10%含量的岩藻黄素浸膏价格即高达40000元/公斤,因此具有巨大的市场价值。Fucoxanthin (Fucoxanthin), also known as fucoxanthin and fucoidin, mainly comes from large algae and microalgae such as algae, diatoms, and golden algae. It is a natural carotenoid that participates in the photosystem of photosynthesis II's response. Because of its unique allene structure, fucoxanthin is an active molecule with strong antioxidant properties. In recent years, studies have found that fucoxanthin has a variety of functional activities in cells, animals and humans, including anti-oxidation, anti-inflammation, anti-cancer, anti-obesity, anti-diabetes, anti-angiogenesis and anti-malarial and other physiological activities, and It has a protective effect on organs such as liver, brain blood vessels, bones, skin and eyes. Based on the above functions, fucoxanthin is a natural product with broad prospects for health food and drug development. The market capacity of fucoxanthin is 500 tons, and the price of fucoxanthin extract with 10% content is as high as 40,000 yuan/kg , so it has a huge market value.
岩藻黄素的功效中减肥方面的显著作用使其受到越来越多的关注,它可以通过抑制脂肪细胞的生成和加速脂肪分解代谢两条途径达到减肥的效果。目前市场上岩藻黄素主要是通过裙带菜(Undariapinnatifida)、海带(Laminaria japonica)等大型海藻中提取获得。但是上述方法存在着大型海藻在细胞壁厚、多糖类物质含量高、纯化困难和海洋污染等问题,且大型海藻中岩藻黄素含量极低(仅为干重的0.01%-0.07%),综上所述,岩藻黄素的产品质量在一定程度上难以保证,并且下游分离纯化的难度加大,因其对提取分离纯化有更高的技术要求,从而导致高纯岩藻黄素价格昂贵,进一步限制了岩藻黄素的应用。Fucoxanthin's significant role in weight loss has attracted more and more attention. It can achieve the effect of weight loss by inhibiting the formation of fat cells and accelerating fat catabolism. Fucoxanthin currently on the market is mainly extracted from large seaweeds such as Undaria pinnatifida and Laminaria japonica. However, the above-mentioned method has problems such as large seaweed having a thick cell wall, high polysaccharide content, difficult purification and marine pollution, and the content of fucoxanthin in the large seaweed is extremely low (only 0.01%-0.07% of the dry weight), To sum up, the product quality of fucoxanthin is difficult to guarantee to a certain extent, and the difficulty of downstream separation and purification is increased, because it has higher technical requirements for extraction, separation and purification, resulting in expensive high-purity fucoxanthin. Further limit the application of fucoxanthin.
相对大型海藻而言,海洋微藻是岩藻黄素更好的替代来源。目前市场上大型海藻中提取的浓缩岩藻黄素的含量普遍低于1%,而一些海洋微藻细胞中岩藻黄素含量即高达0.6%,是大型海藻的近100倍。硅藻为分布广泛的海洋微藻,在海洋、淡水及潮湿的表面上均广泛存在,一般依靠光能合成自身所需的养分。平滑菱形藻(Nitzchia laevis)为一种单细胞藻类,属于硅藻门(Bacillariophyta)。Marine microalgae are a better alternative source of fucoxanthin than macroalgae. At present, the content of concentrated fucoxanthin extracted from macroalgae on the market is generally less than 1%, while the content of fucoxanthin in some marine microalgae cells is as high as 0.6%, which is nearly 100 times that of macroalgae. Diatoms are widely distributed marine microalgae that exist widely in oceans, fresh water and wet surfaces, and generally rely on light energy to synthesize the nutrients they need. Nitzchia laevis is a unicellular alga belonging to the division Bacillariophyta.
研究发现舟形藻属、小环藻属、筒柱藻属等硅藻可异养培养生长,本申请中的设计人发现其生物量浓度极低,较难应用于高密度异养发酵(Guo,et al.,2016)。平滑菱形藻(Nitzchia laevis)是一种单细胞藻类,属于硅藻门(Bacillariophyta),羽纹硅藻纲(Pennaeae),双菱藻目(Surirellales),菱形藻属(Nitzschia),具有异养发酵培养的潜力。利用平滑菱形藻生产岩藻黄素的研究较少。申请人经检索发现申请号为201310329269.X的专利文献中公开了一种提高硅藻中岩藻黄素产率的培养方法,该专利过优化培养基,添加番茄提取物在一定程度上促进合成了岩藻黄素,后期采用光照处理最终使得小环藻达到7.77mg/(L·d)的岩藻黄素产率,其中提出平滑菱形藻可用于光照培养生产岩藻黄素,但是该文献仅公开了利用小环藻制备岩藻黄素的方法、步骤及工艺条件。并未公布采用其他菌种可进行岩藻黄素的生产,同时其中也并未相关的培养条件、光照强度、培养基组成、生物量浓度等培养结果以及岩藻黄素含量和产率等一系列关键技术信息。本申请的设计人等利用异养手段培养平滑菱形藻,岩藻黄素含量仅为0.4%左右,岩藻黄素产率仅为0.1mg/(L·d)。然而平滑菱形藻(Nitzschia laevis)UTEX 2047在光照自养条件下生产岩藻黄素,其含量(占细胞干重)高达0.7%,但生物量浓度<0.2g/L,产率仅为0.06mg/(L·d),而此论文中并未对其进行培养条件的优化(Guo,et al.,2016)。因此有必要通过优化培养基组成及培养条件等技术手段,提高异养条件下平滑菱形藻的生物量浓度和岩藻黄素产率,同时进一步提高岩藻黄素含量。Studies have found that diatoms such as Navicula, Cyclotella, and Cylindrica can grow in heterotrophic culture. The designer in this application found that the biomass concentration is extremely low, and it is difficult to apply to high-density heterotrophic fermentation (Guo, et al., 2016). Nitzchia laevis is a single-celled alga belonging to the division Bacillariophyta, class Pennaeae, order Surirellales, genus Nitzschia, and has heterotrophic fermentation cultivated potential. There are few studies on the production of fucoxanthin by using Nitzschia smoothis. After searching, the applicant found that the patent literature with application number 201310329269.X disclosed a cultivation method for increasing the yield of fucoxanthin in diatoms. The patent optimized the medium and added tomato extract to promote the synthesis to a certain extent. Fucoxanthin was obtained, and light treatment was used in the later stage to finally make Cyclotella reach a fucoxanthin yield of 7.77mg/(L d). It was proposed that Nitzschia smoothis can be used for light culture to produce fucoxanthin, but this document Only the method, steps and process conditions for preparing fucoxanthin by using Cyclotella are disclosed. It has not been announced that other strains can be used for the production of fucoxanthin, and there are no related culture conditions, light intensity, medium composition, biomass concentration and other culture results, as well as fucoxanthin content and yield. Series key technical information. The designers of the present application used heterotrophic methods to cultivate Nitzschia smoothis, the content of fucoxanthin was only about 0.4%, and the yield of fucoxanthin was only 0.1 mg/(L·d). However, Nitzschia laevis UTEX 2047 produces fucoxanthin under photoautotrophic conditions, and its content (accounting for dry cell weight) is as high as 0.7%, but the biomass concentration is <0.2g/L, and the yield is only 0.06mg /(L·d), and this paper did not optimize the culture conditions (Guo, et al., 2016). Therefore, it is necessary to improve the biomass concentration and fucoxanthin yield of Nitzschia platypus under heterotrophic conditions by optimizing medium composition and culture conditions and other technical means, and further increase the fucoxanthin content at the same time.
发明内容Contents of the invention
本发明的目的是提供一种利用异养培养平滑菱形藻生产岩藻黄素的方法,通过优化培养条件能够实现高产制备岩藻黄素。The purpose of the present invention is to provide a method for producing fucoxanthin by using heterotrophic culture of Nitzschia plastifolia, which can realize high-yield preparation of fucoxanthin by optimizing the culture conditions.
本发明的整体技术构思是:Overall technical idea of the present invention is:
利用异养培养平滑菱形藻生产岩藻黄素的方法,包括如下步骤:The method for producing fucoxanthin by using heterotrophic cultivation of Nitzschia smoothis comprises the following steps:
A、种子液的制备A. Preparation of seed solution
将活化好的平滑菱形藻置于无菌种子培养基中异养培养3-11天制成种子液,使平滑菱形藻细胞处于对数生长期;Put the activated Nitzschia smoothii in a sterile seed medium for heterotrophic culture for 3-11 days to make a seed solution, so that the Nitzkiplankton cells are in the logarithmic growth phase;
B、发酵培养B. Fermentation culture
将步骤A中的种子液按照体积比为3%-20%的接种量转接入无菌发酵培养基中进行摇床培养制备发酵液,培养温度20℃-30℃,培养周期3-11天;The seed liquid in step A is transferred to the sterile fermentation medium according to the inoculum amount of 3%-20% by volume to carry out shaker culture to prepare the fermentation liquid, the culture temperature is 20°C-30°C, and the culture period is 3-11 days ;
所述的种子培养基及发酵培养基包括如下含量范围的原料:Described seed culture medium and fermentation medium comprise the raw material of following content scope:
NaCl 10g/L-32g/L;MgSO4·7H2O 1.09g/L-2.18g/L;CaCl2·2H2O 0.1g/L-0.27g/L;KH2PO4 0.031g/L-0.062g/L;K2HPO4 0.00375g/L-0.0075g/L;FeCl3·6H2O 0.291mg/L-0.582mg/L;MnCl2·4H2O 0.025mg/L-0.246mg/L;ZnCl2 0.031mg/L-0.311mg/L;CoCl2·6H2O0.0114mg/L-0.0228mg/L;Na2MoO4·2H2O 0.012mg/L-0.024mg/L;H3BO3 3.06g/L-30.56g/L;(NH4)6MO7O24·4H2O 0.028mg/L-0.278mg/L;Tris-buffer 0.089g/L-0.892g/L;H2SO4 1.64μg/L-16.4μg/L;vitamin B12 1.5g/L-15×10-5g/L;biotin 2.5g/L-25×10-5g/L;有机碳源2g/L-50g/L;硅酸盐20mg/L-700mg/L;氮源0.4g/L-7g/L;pH=6-9;NaCl 10g/L-32g/L; MgSO 4 7H 2 O 1.09g/L-2.18g/L; CaCl 2 2H 2 O 0.1g/L-0.27g/L; KH 2 PO 4 0.031g/L- 0.062g/L; K 2 HPO 4 0.00375g/L-0.0075g/L; FeCl 3 6H 2 O 0.291mg/L-0.582mg/L; MnCl 2 4H 2 O 0.025mg/L-0.246mg/L ; ZnCl 2 0.031mg/L-0.311mg/L; CoCl 2 6H 2 O 0.0114mg/L-0.0228mg/L; Na 2 MoO 4 2H 2 O 0.012mg/L-0.024mg/L; H 3 BO 3 3.06g/L-30.56g/L; (NH 4 ) 6 MO 7 O 24 ·4H 2 O 0.028mg/L-0.278mg/L; Tris-buffer 0.089g/L-0.892g/L; H 2 SO 4 1.64μg/L-16.4μg/L; vitamin B 12 1.5g/L-15×10 -5 g/L; biotin 2.5g/L-25×10 -5 g/L; organic carbon source 2g/L- 50g/L; Silicate 20mg/L-700mg/L; Nitrogen source 0.4g/L-7g/L; pH=6-9;
所述有机碳源包括但不限限于:葡萄糖、淀粉水解物、果葡糖浆、蔗糖或其组合;所述氮源选用有机氮源、无机氮源或其组合,其中有机氮源包括但不限于:酵母膏、蛋白胨、酵母提取物、氨基酸、尿素、蛋白水解物或其组合,无机氮源包括但不限于选用硝酸钾、硝酸钠、氯化铵、碳酸氢铵或其组合;所述硅酸盐包括但不限于硅酸钠、硅酸钾、硅酸氨或其组合。The organic carbon source includes but is not limited to: glucose, starch hydrolyzate, fructose syrup, sucrose or a combination thereof; the nitrogen source is selected from an organic nitrogen source, an inorganic nitrogen source or a combination thereof, wherein the organic nitrogen source includes but is not limited to : yeast extract, peptone, yeast extract, amino acid, urea, protein hydrolyzate or a combination thereof, inorganic nitrogen sources include but are not limited to potassium nitrate, sodium nitrate, ammonium chloride, ammonium bicarbonate or a combination thereof; the silicic acid Salts include, but are not limited to, sodium silicate, potassium silicate, ammonium silicate, or combinations thereof.
所述的平滑菱形藻选自平滑菱形藻(Nitzschia laevis)UTEX 2047(购自美国德克萨斯大学奥斯汀分校微藻保藏库,Culture Collection of Algae at The Universityof Texas at Austin,简称UTEX)、平滑菱形藻(Nitzschia laevis)CCMP559(购自美国海洋微藻和微生物保藏中心,National Center for Marine Algae and Microbiota,简称NCMA)、或平滑菱形藻(Nitzschia laevis)CCMP 1092(购自美国海洋微藻和微生物保藏中心,National Center for Marine Algae and Microbiota,简称NCMA),平滑菱形藻(Nitzschia laevis)O-7(购自米尔福德海洋微藻培养收集实验室,Milford LaboratoryMarine Microalgal Culture Collection),其中优选平滑菱形藻(Nitzschia laevis)UTEX 2047。The smooth Nitzschia laevis is selected from Nitzschia laevis UTEX 2047 (purchased from the Microalgae Collection of the University of Texas at Austin, Culture Collection of Algae at The University of Texas at Austin, referred to as UTEX), smooth Nitzschia laevis Algae (Nitzschia laevis) CCMP559 (purchased from the National Center for Marine Algae and Microbiota, NCMA for short), or Nitzschia laevis CCMP 1092 (purchased from the American Marine Microalgae and Microbiota Collection Center, National Center for Marine Algae and Microbiota (NCMA for short), Nitzschia laevis (Nitzschia laevis) O-7 (purchased from Milford Laboratory Marine Microalgal Culture Collection), wherein Nitzschia laevis is preferred (Nitzschia laevis) UTEX 2047.
C、从步骤B发酵结束后的发酵液中提取岩藻黄素。C. extracting fucoxanthin from the fermented liquid after step B fermentation is finished.
因从发酵液中分离平滑菱形藻细胞以及从平滑菱形藻细胞中提取岩藻黄素属于现有技术,申请人在此不再赘述。Since the isolation of Nitzbrae cells from the fermentation broth and the extraction of fucoxanthin from Nitzbrae cells belong to the prior art, the applicant will not repeat them here.
本发明中各步骤的具体技术方案如下:The concrete technical scheme of each step among the present invention is as follows:
为便于工业发酵过程的进行并取得较好的发酵效果,优选的技术方案是,所述的步骤B摇床培养过程中摇床转速为100-240转/分钟。In order to facilitate the industrial fermentation process and achieve a better fermentation effect, the preferred technical solution is that the rotating speed of the shaking table in the shaking bed cultivation process of step B is 100-240 rpm.
为提高岩藻黄素的产率及含量,优选的培养条是,种子培养基及发酵培养基中氮源选用如下含量范围的原料:蛋白胨1g/L;有机碳源选用如下含量范围的原料:葡萄糖5g/L。In order to improve the yield and content of fucoxanthin, the preferred culture strip is that the nitrogen source in the seed medium and the fermentation medium is selected from the following content range: peptone 1g/L; the organic carbon source is selected from the following content range: Glucose 5g/L.
更进一步优选的培养条件是,种子培养基及发酵培养基中氮源选用如下含量范围的原料:蛋白胨1g/L;有机碳源含量范围如下:5g/L<有机碳源含量≤50g/L。Further preferred culture conditions are that the nitrogen source in the seed medium and the fermentation medium is selected from raw materials with the following content range: peptone 1g/L; the organic carbon source content range is as follows: 5g/L<organic carbon source content≤50g/L.
更进一步的优选技术方案是,种子培养基及发酵培养基中氮源选用如下含量范围的原料:硝酸钾或硝酸钠0.4g/L-2g/L;有机碳源选用如下含量范围的原料:葡萄糖5g/L。A further preferred technical solution is that the nitrogen source in the seed medium and the fermentation medium is selected from the following content range of raw materials: potassium nitrate or sodium nitrate 0.4g/L-2g/L; the organic carbon source is selected from the following content range of raw materials: glucose 5g/L.
更进一步的优选技术方案是,种子培养基及发酵培养基中氮源选用如下含量范围的原料:硝酸钠1g/L;有机碳源选用如下含量范围的原料:葡萄糖5g/L。A further preferred technical solution is that the nitrogen source in the seed medium and the fermentation medium is selected from the following content range: sodium nitrate 1g/L; the organic carbon source is selected from the following content range: glucose 5g/L.
本发明中的涉及的检测方法如下:The detection method involved in the present invention is as follows:
1、平滑菱形藻细胞干重的测定1. Determination of cell dry weight of Nitzschia smoothis
接种后每隔24小时取3mL发酵液,在转速为3000转/分钟的条件下离心5分钟,ddH2O洗涤后重新离心,重复2次;将发酵液滤至预称重的滤纸上,放入80℃真空干燥箱中烘干至恒重。After inoculation, take 3 mL of fermentation broth every 24 hours, centrifuge at a speed of 3000 rpm for 5 minutes, wash with ddH 2 O and centrifuge again, repeat twice; filter the fermentation broth onto pre-weighed filter paper, put Dry in a vacuum oven at 80°C until constant weight.
2、岩藻黄素的检测2. Detection of fucoxanthin
目前申请人未发现岩藻黄素检测的国家或者企业标准,主要通过紫外可见吸光法(UV法)和高效液相色谱仪(HPLC)检测,因UV法特异性差,易受其他色素的干扰,因此HPLC法是岩藻黄素目前较好的检测手段。本申请参照Guo等人的研究,并在其基础上进行改进,具体如下:At present, the applicant has not found a national or enterprise standard for the detection of fucoxanthin. It is mainly detected by ultraviolet-visible absorption method (UV method) and high-performance liquid chromatography (HPLC). Due to the poor specificity of the UV method, it is easily interfered by other pigments. Therefore, HPLC method is currently a better detection method for fucoxanthin. This application refers to the research of Guo et al., and improves on the basis of it, as follows:
称取20mg冻干后的藻粉,低温研磨后加入5mL无水乙醇震荡提取10分钟,离心(条件为温度4℃、转速3000转/分钟、时间5分钟)收集上清,沉淀中重新加入3mL无水乙醇震荡提取,直至藻粉呈白色。收集提取液,在温度4℃、转速为12000转/分钟的条件下离心10分钟,取上清氮气吹干,再加入1mL无水乙醇溶解色素,过膜后高效液相色谱仪(HPLC)分析,整个过程避光条件下进行。Weigh 20 mg of lyophilized algae powder, grind at low temperature, add 5 mL of absolute ethanol to shake and extract for 10 minutes, centrifuge (conditions: temperature 4°C, speed 3000 rpm, time 5 minutes) to collect the supernatant, add 3 mL to the precipitate Extract by shaking with absolute ethanol until the algae powder turns white. Collect the extract, centrifuge at 4°C and 12,000 rpm for 10 minutes, take the supernatant and dry it with nitrogen, then add 1 mL of absolute ethanol to dissolve the pigment, and pass through the membrane for high-performance liquid chromatography (HPLC) analysis , the whole process was carried out under dark conditions.
3、HPLC分析方法3. HPLC analysis method
高效液相色谱仪waters2695,配置PDA检测器,检测波长450nm,选用C18反相柱(250mm×4.6mm×5mm)。流动相为:A相为纯乙酸乙酯,B相为乙腈:甲醇:水=84:2:14,C相为纯甲醇,采用梯度洗脱,流动相均采用HPLC级。The high-performance liquid chromatograph waters2695 is configured with a PDA detector, the detection wavelength is 450nm, and a C18 reversed-phase column (250mm×4.6mm×5mm) is selected. The mobile phase is: phase A is pure ethyl acetate, phase B is acetonitrile:methanol:water=84:2:14, phase C is pure methanol, gradient elution is adopted, and the mobile phases are HPLC grade.
梯度洗脱条件如下:The gradient elution conditions are as follows:
本发明所具备的实质性特点和取得的显著技术进步在于:The substantive features possessed by the present invention and the remarkable technical progress obtained are:
1、本发明首次提出利用平滑菱形藻通过规模化发酵方法生产岩藻黄素,经申请人实验证实,所制备的平滑菱形藻干燥藻粉中岩藻黄素的含量高(至少可达0.38%,最高可达1.15%,较现有技术提高187.5%),岩藻黄素的产率高(至少可达1.1mg/(L·d),最高可达3.31mg/(L·d),较现有技术提高32倍)。1. For the first time, the present invention proposes to utilize Nitzporella smoothis to produce fucoxanthin through large-scale fermentation method. It is confirmed by the applicant's experiment that the content of fucoxanthin in the dried Nitzkiplano smoothis powder prepared is high (at least up to 0.38%) , up to 1.15%, 187.5% higher than prior art), the productive rate of fucoxanthin (at least up to 1.1mg/(L d), up to 3.31mg/(L d), compared with The existing technology improves by 32 times).
2、本发明提供的方法具有应用于工业化生产岩藻黄素的潜力。一是优化培养条件后平滑菱形藻的岩藻黄素含量大大提高;二是岩藻黄素产率远高于目前报道的所有硅藻和其他藻类。2. The method provided by the present invention has the potential to be applied to industrial production of fucoxanthin. One is that the fucoxanthin content of Nitzschia smoothis is greatly increased after optimizing the culture conditions; the other is that the yield of fucoxanthin is much higher than that of all diatoms and other algae reported so far.
3、本发明所获得的平滑菱形藻粉,在不受外界条件限制下可以稳定实现连续工业化生产的基础上,能够从培养基的源头控制重金属、多氯联苯等海洋常见污染物,较大型海藻来源的岩藻黄素更安全。3. The smooth diamond-shaped algal powder obtained by the present invention can stably realize continuous industrial production without being restricted by external conditions, and can control common marine pollutants such as heavy metals and polychlorinated biphenyls from the source of the culture medium. Seaweed-derived fucoxanthin is safer.
4、相对其他微藻培养生产岩藻黄素,生产周期大大缩短,最短可3天结束发酵,在提高生产效率、降低生产成本的同时,大大降低了培养过程中的污染风险。4. Compared with other microalgae cultures to produce fucoxanthin, the production cycle is greatly shortened, and the fermentation can be completed in as little as 3 days. While improving production efficiency and reducing production costs, it also greatly reduces the risk of pollution during the cultivation process.
附图说明Description of drawings
图1是平滑菱形藻在异养条件下的生长曲线。Figure 1 is the growth curve of Nitzschia smoothis under heterotrophic conditions.
从图中可见,5天培养后最高生物量为1.1g/L,岩藻黄素浓度为0.5%,最大产率为1.1mg/(L·d),较现有技术中异养培养的平滑菱形藻最高岩藻黄素含量和最高岩藻黄素产率分别提高25%和10倍。As can be seen from the figure, the highest biomass after 5 days of cultivation is 1.1g/L, the concentration of fucoxanthin is 0.5%, and the maximum yield is 1.1mg/(L d), which is smoother than that of heterotrophic culture in the prior art. The highest content of fucoxanthin and the highest yield of fucoxanthin in Nitzschia are increased by 25% and 10 times respectively.
图2是平滑菱形藻在不同葡萄糖初始浓度下的生长曲线。Fig. 2 is the growth curve of Nitzschia plaza under different initial concentrations of glucose.
其中H-5、H-10、H-20、H-40分别代表培养基中添加葡萄糖的初始浓度为5g/L、10g/L、20g/L、40g/L,从图中可见,当葡萄糖浓度为5g/L时比生长速率最高。Among them, H-5, H-10, H-20, and H-40 respectively represent that the initial concentration of glucose added in the culture medium is 5g/L, 10g/L, 20g/L, 40g/L, as can be seen from the figure, when glucose The specific growth rate was the highest when the concentration was 5g/L.
图3是不同葡萄糖初始浓度的培养条件下所获得的藻粉中岩藻黄素的含量(即岩藻黄素/冻干藻粉的质量比)及产率的比较。Fig. 3 is a comparison of the content of fucoxanthin (ie, the mass ratio of fucoxanthin/freeze-dried algal powder) and yield in algal powder obtained under different initial concentrations of glucose.
其中H-5、H-10、H-20、H-40分别代表异养条件下初始葡萄糖浓度为5g/L、10g/L、20g/L、40g/L,由图中可见,葡萄糖浓度为10g/L时,岩藻黄素含量达最高0.72%,岩藻黄素产率达到最高为3.26mg/(L·d),较现有技术异养培养的平滑菱形藻最高岩藻黄素含量和最高岩藻黄素产率分别提高80%和31.6倍。Among them, H-5, H-10, H-20, and H-40 respectively represent that the initial glucose concentration under heterotrophic conditions is 5g/L, 10g/L, 20g/L, and 40g/L. As can be seen from the figure, the glucose concentration is At 10g/L, the fucoxanthin content reaches the highest 0.72%, and the fucoxanthin yield reaches the highest 3.26mg/(L·d), which is the highest fucoxanthin content compared with the heterotrophic cultured Nitzschia smoothis in the prior art and the highest fucoxanthin yield were increased by 80% and 31.6 times.
图4是不同氮元素种类对平滑菱形藻细胞中岩藻黄素含量和产率的影响。Fig. 4 is the effect of different types of nitrogen elements on the content and yield of fucoxanthin in Nitzschia smoothis cells.
由图中可见,氮源为硝酸盐时岩藻黄素含量显著提高,氮源为硝酸钠时最高达0.91%,较现有技术异养培养的平滑菱形藻中最高岩藻黄素含量提高127.5%。It can be seen from the figure that when the nitrogen source is nitrate, the content of fucoxanthin is significantly increased, and when the nitrogen source is sodium nitrate, the content of fucoxanthin is as high as 0.91%, which is 127.5% higher than that in the prior art heterotrophically cultured Nishiki. %.
图5是不同硝酸钠初始浓度的培养条件下所获得的藻粉中岩藻黄素的含量及产率的比较。Fig. 5 is a comparison of the content and yield of fucoxanthin in the algae powder obtained under the culture conditions of different initial concentrations of sodium nitrate.
由图中可见,硝酸钠浓度为0.25g/L时,岩藻黄素含量低于0.2%,产率低于0.5mg/(L·d),而当硝酸钠浓度为提高为0.5g/L时,岩藻黄素的产率和产率均有大幅提高,分别大于0.4%和1.1mg/(L·d)。而当硝酸钠浓度为1g/L时,岩藻黄素含量较高(1.06%),较现有技术异养培养的平滑菱形藻中最高岩藻黄素含量提高165%。As can be seen from the figure, when the sodium nitrate concentration was 0.25g/L, the fucoxanthin content was lower than 0.2%, and the productive rate was lower than 0.5mg/(L·d), and when the sodium nitrate concentration was increased to 0.5g/L , the yield and yield of fucoxanthin were greatly improved, which were greater than 0.4% and 1.1mg/(L·d) respectively. And when the concentration of sodium nitrate is 1g/L, the content of fucoxanthin is higher (1.06%), which is 165% higher than the highest content of fucoxanthin in the heterotrophically cultured Nishiki in the prior art.
图6是不同硅酸盐初始浓度的培养条件下所获得的藻粉中岩藻黄素的含量及产率的比较。Fig. 6 is a comparison of the content and yield of fucoxanthin in algae flour obtained under the culture conditions of different initial silicate concentrations.
由图中可见,硅酸盐浓度对岩藻黄素的产量和产率均有明显影响。当不添加硅酸钠时,岩藻黄素含量仅为0.41%,而产率则低于0.5mg/(L·d),而当硅酸钠浓度为30mg/L时,岩藻黄素含量和产率显著提高,而当硅酸盐浓度为120mg/L时,岩藻黄素含量高达1.15%,岩藻黄素产率达3.31mg/(L·d),较现有技术异养培养的平滑菱形藻最高岩藻黄素含量和最高岩藻黄素产率分别提高187.5%和32.1倍。It can be seen from the figure that the silicate concentration has a significant impact on the yield and yield of fucoxanthin. When no sodium silicate was added, the fucoxanthin content was only 0.41%, while the yield was lower than 0.5mg/(L·d), and when the sodium silicate concentration was 30mg/L, the fucoxanthin content and productive rate are significantly improved, and when silicate concentration is 120mg/L, fucoxanthin content is as high as 1.15%, and fucoxanthin productive rate reaches 3.31mg/(L·d), compared with prior art heterotrophic culture The highest fucoxanthin content and the highest fucoxanthin yield of Nitzschia smoothis increased by 187.5% and 32.1 times, respectively.
具体实施方式detailed description
以下结合附图对本发明的实施例作进一步描述,但不作为对本发明的限定,本发明的保护范围以权利要求记载的内容为准,任何依据说明书做出的等效技术手段替换,均不脱离本发明的保护范围。The embodiments of the present invention will be further described below in conjunction with the accompanying drawings, but this is not a limitation of the present invention. The scope of protection of the present invention is subject to the content recorded in the claims, and any equivalent technical means replacement made according to the specification will not depart from protection scope of the present invention.
实施例1Example 1
平滑菱形藻异养培养Heterotrophic culture of Nitzschia smoothis
本实施例中的生产菌种选用平滑菱形藻(Nitzschia laevis)UTEX 2047(购自美国德克萨斯大学奥斯汀分校微藻保藏库,Culture Collection of Algae at TheUniversity of Texas at Austin,简称UTEX)。Nitzschia laevis UTEX 2047 (purchased from the Microalgae Collection of the University of Texas at Austin, Culture Collection of Algae at The University of Texas at Austin, UTEX for short) was selected as the production strain in this example.
A、种子液的制备A. Preparation of seed solution
将活化好的平滑菱形藻置于无菌种子培养基中异养培养3-11天制成种子液,使平滑菱形藻细胞处于对数生长期;Put the activated Nitzschia smoothii in a sterile seed medium for heterotrophic culture for 3-11 days to make a seed solution, so that the Nitzkiplankton cells are in the logarithmic growth phase;
B、发酵培养B. Fermentation culture
将步骤A中的种子液按照体积比为10%的接种量转接入无菌发酵培养基中进行摇床培养制备发酵液,在培养温度为23℃、转速为150转/分钟的条件下培养5天;Transfer the seed liquid in step A into a sterile fermentation medium according to the volume ratio of 10% inoculum to prepare a fermentation liquid on a shaker, and cultivate it under the conditions of a culture temperature of 23°C and a rotation speed of 150 rpm 5 days;
所述的种子培养基及发酵培养基包括如下含量范围的原料:Described seed culture medium and fermentation medium comprise the raw material of following content scope:
NaCl 10g/L;MgSO4·7H2O 2.18g/L;CaCl2·2H2O 0.27g/L;KH2PO4 0.062g/L;K2HPO4 0.0075g/L;FeCl3·6H2O 0.582mg/L;MnCl2·4H2O 0.246mg/L;ZnCl2 0.311mg/L;CoCl2·6H2O 0.0228mg/L;Na2MoO4·2H2O 0.024mg/L;H3BO3 30.56g/L;(NH4)6MO7O24·4H2O0.278mg/L;Tris-buffer 0.892g/L;H2SO4 16.4μg/L;vitamin B12 15×10-5g/L;biotin 25×10-5g/L;有机碳源5g/L;氮源1g/L;硅酸盐0mg/L-700mg/L;pH=8.5;NaCl 10g/L; MgSO 4 7H 2 O 2.18g/L; CaCl 2 2H 2 O 0.27g/L; KH 2 PO 4 0.062g/L; K 2 HPO 4 0.0075g/L; FeCl 3 6H 2 O 0.582mg/L; MnCl 2 4H 2 O 0.246mg/L; ZnCl 2 0.311mg/L; CoCl 2 6H 2 O 0.0228mg/L; Na 2 MoO 4 2H 2 O 0.024mg/L; H 3 BO 3 30.56g/L; (NH 4 ) 6 MO 7 O 24 ·4H 2 O 0.278mg/L; Tris-buffer 0.892g/L; H 2 SO 4 16.4μg/L; vitamin B 12 15×10 -5 g/L; biotin 25×10 -5 g/L; organic carbon source 5g/L; nitrogen source 1g/L; silicate 0mg/L-700mg/L; pH=8.5;
所述有机碳源选用葡萄糖;所述氮源选用蛋白胨;所述硅酸盐包括但不限于硅酸钠、硅酸钾、硅酸氨或其组合。The organic carbon source is glucose; the nitrogen source is peptone; the silicate includes but not limited to sodium silicate, potassium silicate, ammonium silicate or a combination thereof.
C、从步骤B发酵结束后的发酵液中提取岩藻黄素。C. extracting fucoxanthin from the fermented liquid after step B fermentation is finished.
实施例1的效果分析:The effect analysis of embodiment 1:
平滑菱形藻(UTEX 2047)在异养条件下生长状态较佳,生物量最高达1.1g/L,岩藻黄素含量为0.5%。计算得异养条件下岩藻黄素产率为1.1mg/(L·d)。此产率是目前报道的平滑菱形藻最高的岩藻黄素产率。Nitzschia plastifolia (UTEX 2047) grows better under heterotrophic conditions, with a biomass of up to 1.1g/L and a fucoxanthin content of 0.5%. The yield of fucoxanthin was calculated to be 1.1 mg/(L·d) under heterotrophic conditions. This yield is the highest fucoxanthin yield of Nitzschia platypus reported so far.
实施例2:平滑菱形藻的异养培养Embodiment 2: Heterotrophic cultivation of Nitzschia smoothis
以250mL锥形瓶为培养容器,转入发酵培养基100mL,按体积比为10%的接种量接入发酵培养基中进行摇床培养。培养条件如下:摇床转速为150转/分钟,温度为23℃,培养时间为5天。With a 250mL Erlenmeyer flask as a culture vessel, 100mL of fermentation medium was transferred, and the inoculation amount of 10% by volume was inserted into the fermentation medium for shaker culture. The culture conditions are as follows: the rotation speed of the shaker is 150 rpm, the temperature is 23° C., and the culture time is 5 days.
发酵培养基及种子培养基中还包括如下含量的原料:NaNO3 1g/L,其余内容同实施例1。The fermentation medium and seed medium also include raw materials with the following content: NaNO 3 1g/L, and the rest are the same as in Example 1.
实施例3-5与实施例2的区别在于:实施例3-5中的初始葡萄糖浓度分别为10g/L,20g/L和40g/L,培养时间分别延长至7、9、11天。The difference between Example 3-5 and Example 2 is that the initial glucose concentration in Example 3-5 is 10g/L, 20g/L and 40g/L respectively, and the culture time is extended to 7, 9, 11 days respectively.
实施例2-5的效果分析:The effect analysis of embodiment 2-5:
参见图2和图3,不同葡萄糖初始浓度对平滑菱形藻的生长和岩藻黄素含量均有较大影响。初始葡萄糖浓度为40g/L时,获得生物量浓度最大(5.33g/L),而葡萄糖浓度为5g/L时,生物量最高浓度为1.84g/L。葡萄糖浓度为10g/L时岩藻黄素含量最高(0.72%),此时的岩藻黄素产率也最高(3.26mg/(L·d)),然而,葡萄糖浓度为5g/L时,生长周期仅为5天,且葡萄糖的生物转化率最高(1.84g生物量/5g葡萄糖)。因此后期优化实验选用初始葡萄糖浓度5g/L。Referring to Fig. 2 and Fig. 3, different initial concentrations of glucose have a great influence on the growth and fucoxanthin content of Nitzschia smoothis. The maximum biomass concentration (5.33g/L) was obtained when the initial glucose concentration was 40g/L, and the highest biomass concentration was 1.84g/L when the glucose concentration was 5g/L. When the glucose concentration is 10g/L, the content of fucoxanthin is the highest (0.72%), and the yield of fucoxanthin at this time is also the highest (3.26mg/(L·d)), however, when the glucose concentration is 5g/L, The growth cycle was only 5 days, and the biotransformation rate of glucose was the highest (1.84g biomass/5g glucose). Therefore, the initial glucose concentration of 5 g/L was selected in the later optimization experiment.
实施例6-11Example 6-11
实施例6-11与实施例1的区别在于:实施例6-11中的氮源依次分别为2g/L的NaNO3、KNO3、NH4Cl、尿素、蛋白胨和酵母提取物。其余内容同实施例1。The difference between Examples 6-11 and Example 1 is that the nitrogen sources in Examples 6-11 are respectively 2g/L NaNO 3 , KNO 3 , NH 4 Cl, urea, peptone and yeast extract. All the other contents are the same as in Example 1.
实施例6-11的效果分析:The effect analysis of embodiment 6-11:
参见图4,仅采用2g/L的硝酸钠是检测冻干藻粉中的岩藻黄素含量可高达0.91%,岩藻黄素含量大大提高。氮源仅使用无机氮源—硝酸钠或硝酸钾可得到较高含量的岩藻黄素,而仅用有机氮源蛋白胨和酵母膏时所得岩藻黄素含量低于用仅用无机氮源时岩藻黄素含量。Referring to Fig. 4, only 2 g/L of sodium nitrate is used to detect that the content of fucoxanthin in the freeze-dried algal powder can be as high as 0.91%, and the content of fucoxanthin is greatly increased. Nitrogen sources Only use inorganic nitrogen sources—sodium nitrate or potassium nitrate can get higher content of fucoxanthin, while the content of fucoxanthin obtained when only organic nitrogen sources peptone and yeast extract are used is lower than when only inorganic nitrogen sources are used Fucoxanthin content.
实施例12-16Examples 12-16
实施例12-16与实施例1的区别在于:实施例12-16中的氮源选用硝酸钠,且浓度依次分别为0.4g/L,0.5g/L,1.0g/L,1.5g/L和2g/L。其余内容同实施例1。The difference between Examples 12-16 and Example 1 is that the nitrogen source in Examples 12-16 is sodium nitrate, and the concentrations are respectively 0.4g/L, 0.5g/L, 1.0g/L, and 1.5g/L and 2g/L. All the other contents are the same as in Example 1.
实施例12-16的效果分析:The effect analysis of embodiment 12-16:
参见图5,硝酸钠初始浓度为1.0g/L时岩藻黄素含量最高(1.06%),岩藻黄素产率为3.18mg/(L·d)。Referring to Fig. 5, when the initial concentration of sodium nitrate is 1.0g/L, the content of fucoxanthin is the highest (1.06%), and the yield of fucoxanthin is 3.18 mg/(L·d).
实施例17-20Examples 17-20
实施例17-20与实施例1的区别在于:实施例17-20中的氮源选用1g/L的硝酸钠,硅酸盐选用硅酸钠,浓度依次分别为:0mg/L,30mg/L,60mg/L和120mg/L。The difference between Example 17-20 and Example 1 is that the nitrogen source in Example 17-20 is 1g/L sodium nitrate, the silicate is sodium silicate, and the concentrations are respectively: 0mg/L, 30mg/L , 60mg/L and 120mg/L.
实施例17-20效果分析:Embodiment 17-20 effect analysis:
参见图6,硅酸盐初始浓度为120mg/L时岩藻黄素含量最高(1.15%),岩藻黄素产率为3.31mg/(L·d)。Referring to Fig. 6, the fucoxanthin content was the highest (1.15%) when the initial silicate concentration was 120 mg/L, and the fucoxanthin yield was 3.31 mg/(L·d).
实施例21Example 21
实施例21与实施例1的区别在于:生产菌种选用平滑菱形藻(Nitzschia laevis)CCMP1092(购自美国海洋微藻和微生物保藏中心,National Center for Marine Algaeand Microbiota,简称NCMA),种子液按照体积比为3%的接种量转接入无菌发酵培养基中,发酵培养基装量为20%,培养温度25℃,培养周期9天;所述的种子培养基及发酵培养基包括如下含量范围的原料:碳源采用浓度为25g/L的蔗糖;NaCl 32g/L;MgSO4·7H2O 2.18g/L;CaCl2·2H2O 0.1g/L;KH2PO4 0.031g/L;K2HPO4 0.0055g/L;FeCl3·6H2O 0.291mg/L;MnCl2·4H2O 0.025mg/L;ZnCl2 0.031mg/L;CoCl2·6H2O 0.0180mg/L;Na2MoO4·2H2O0.012mg/L;H3BO3 16.1g/L;(NH4)6MO7O24·4H2O 0.278mg/L;Tris-buffer 0.089g/L;H2SO49.4μg/L;vitamin B12 15×10-5g/L;biotin 0.21g/L;氮源3.5g/L;pH=6,所述氮源由如下质量份数的原料组成:酵母膏:碳酸氢铵:蛋白胨:尿素=1:2:1:2,硅酸盐选用硅酸钾,浓度为350mg/L。其余内容与实施例4相同。The difference between Example 21 and Example 1 is that the production strain is Nitzschia laevis (Nitzschia laevis) CCMP1092 (purchased from the American Marine Microalgae and Microbiota Collection Center, National Center for Marine Algae and Microbiota, referred to as NCMA), and the seed liquid is Transfer an inoculation amount of 3% into a sterile fermentation medium, the loading of the fermentation medium is 20%, the culture temperature is 25°C, and the culture period is 9 days; the seed medium and fermentation medium include the following content ranges Raw materials: sucrose with a concentration of 25g/L as carbon source; NaCl 32g/L; MgSO 4 7H 2 O 2.18g/L; CaCl 2 2H 2 O 0.1g/L; KH 2 PO 4 0.031g/L; K 2 HPO 4 0.0055g/L; FeCl 3 6H 2 O 0.291mg/L; MnCl 2 4H 2 O 0.025mg/L; ZnCl 2 0.031mg/L; CoCl 2 6H 2 O 0.0180mg/L; 2 MoO 4 2H 2 O 0.012mg/L; H 3 BO 3 16.1g/L; (NH 4 ) 6 MO 7 O 24 4H 2 O 0.278mg/L; Tris-buffer 0.089g/L; H 2 SO 4 9.4μg/L; vitamin B 12 15×10 -5 g/L; biotin 0.21g/L; nitrogen source 3.5g/L; pH=6, the nitrogen source is composed of the following raw materials in parts by mass: yeast extract : Ammonium bicarbonate: Peptone: Urea = 1:2:1:2, the silicate is potassium silicate, the concentration is 350mg/L. All the other contents are the same as in Example 4.
实施例21效果分析:Embodiment 21 effect analysis:
岩藻黄素含量为1.08%,岩藻黄素产量为3.1mg/(L·d)。The content of fucoxanthin is 1.08%, and the yield of fucoxanthin is 3.1 mg/(L·d).
实施例22Example 22
实施例22与实施例1的区别在于:生产菌种选用平滑菱形藻(Nitzschia laevis)CCMP559(购自美国海洋微藻和微生物保藏中心,National Center for Marine Algae andMicrobiota,简称NCMA),种子培养基与发酵培养基中有机碳源浓度为2g/L,有机碳源选用淀粉水解物,种子液按照体积比为20%的接种量转接入无菌发酵培养基中,发酵培养基装量为80%,培养温度30℃,培养周期3天;所述的种子培养基及发酵培养基包括如下含量范围的原料:NaCl 10g/L;MgSO4·7H2O 1.09g/L;CaCl2·2H2O 0.16g/L;KH2PO4 0.062g/L;K2HPO4 0.00375g/L;FeCl3·6H2O 0.582mg/L;MnCl2·4H2O 0.112mg/L;ZnCl2 0.311mg/L;CoCl2·6H2O 0.0228mg/L;Na2MoO4·2H2O 0.024mg/L;H3BO3 3.06g/L;(NH4)6MO7O24·4H2O0.140mg/L;Tris-buffer 0.892g/L;H2SO4 16.4μg/L;vitamin B12 1.5g/L;biotin 25×10-5g/L;氮源7g/L;pH=6-9,所述氮源选用如下质量份数的原料组成:蛋白胨:酵母提取物:氨基酸:硝酸钾=1:1:1:2;硅酸盐选用硅酸氨,浓度为700mg/L。其余内容同实施例1。The difference between Example 22 and Example 1 is that: Nitzschia laevis (Nitzschia laevis) CCMP559 (purchased from the National Center for Marine Algae and Microbiota, NCMA for short) was selected as the production strain, and the seed medium was mixed with The organic carbon source concentration in the fermentation medium is 2g/L, the organic carbon source is selected from starch hydrolyzate, the seed liquid is transferred into the sterile fermentation medium according to the inoculation amount of 20% by volume, and the fermentation medium load is 80% , the culture temperature is 30°C, and the culture period is 3 days; the seed medium and fermentation medium include raw materials in the following content ranges: NaCl 10g/L; MgSO 4 ·7H 2 O 1.09g/L; CaCl 2 ·2H 2 O 0.16g/L; KH 2 PO 4 0.062g/L; K 2 HPO 4 0.00375g/L; FeCl 3 6H 2 O 0.582mg/L; MnCl 2 4H 2 O 0.112mg/L; ZnCl 2 0.311mg/L L; CoCl 2 6H 2 O 0.0228mg/L; Na 2 MoO 4 2H 2 O 0.024mg/L; H 3 BO 3 3.06g/L; (NH 4 ) 6 MO 7 O 24 4H 2 O 0.140mg /L; Tris-buffer 0.892g/L; H 2 SO 4 16.4μg/L; vitamin B 12 1.5g/L; biotin 25×10 -5 g/L; nitrogen source 7g/L; pH=6-9, The nitrogen source is composed of the following raw materials in parts by mass: peptone: yeast extract: amino acid: potassium nitrate = 1:1:1:2; the silicate is ammonium silicate with a concentration of 700 mg/L. All the other contents are the same as in Example 1.
实施例22效果分析:Embodiment 22 effect analysis:
岩藻黄素含量为1.11%,岩藻黄素产量为3.12mg/(L·d)。The content of fucoxanthin is 1.11%, and the yield of fucoxanthin is 3.12 mg/(L·d).
实施例23Example 23
实施例23与实施例1的区别在于:选用平滑菱形藻(Nitzschia laevis)O-7(购自米尔福德海洋微藻培养收集实验室,Milford Laboratory Marine Microalgal CultureCollection),种子培养基与发酵培养基中碳源浓度为50g/L,碳源为蔗糖和果葡糖浆按照体积为1:1混配后的混合物,种子液按照体积比为14%的接种量转接入无菌发酵培养基中,培养基装量为40%,培养温度20℃,培养周期6天;所述的种子培养基及发酵培养基包括如下含量范围的原料:NaCl 22g/L;MgSO4·7H2O 1.66g/L;CaCl2·2H2O 0.27g/L;KH2PO40.045g/L;K2HPO4 0.0075g/L;FeCl3·6H2O 0.431mg/L;MnCl2·4H2O 0.246mg/L;ZnCl20.151mg/L;CoCl2·6H2O 0.0114mg/L;Na2MoO4·2H2O 0.018mg/L;H3BO3 30.56g/L;(NH4)6MO7O24·4H2O 0.028mg/L;Tris-buffer 0.451g/L;H2SO4 1.64μg/L;vitamin B12 0.1g/L;biotin 2.5g/L;氮源0.4g/L;pH=6-9,所述氮源选用如下质量份数的原料组成:氨基酸:蛋白水解物:硝酸钠:氯化铵=2:2:1:2;硅酸盐选用硅酸钠,浓度为20mg/L。The difference between Example 23 and Example 1 is that Nitzschia laevis O-7 (purchased from Milford Laboratory Marine Microalgal Culture Collection), seed medium and fermentation medium were selected. The medium carbon source concentration is 50g/L, the carbon source is a mixture of sucrose and fructose syrup according to the volume of 1:1, and the seed liquid is transferred into the sterile fermentation medium according to the volume ratio of 14% inoculum. The content of the medium is 40%, the culture temperature is 20°C, and the culture period is 6 days; the seed medium and fermentation medium include raw materials in the following content range: NaCl 22g/L; MgSO 4 ·7H 2 O 1.66g/L ; CaCl 2 ·2H 2 O 0.27g/L; KH 2 PO 4 0.045g/L; K 2 HPO 4 0.0075g/L; FeCl 3 ·6H 2 O 0.431mg/L; MnCl 2 ·4H 2 O 0.246mg/L L; ZnCl 2 0.151mg/L; CoCl 2 6H 2 O 0.0114mg/L; Na 2 MoO 4 2H 2 O 0.018mg/L; H 3 BO 3 30.56g/L; (NH 4 ) 6 MO 7 O 24 ·4H 2 O 0.028mg/L; Tris-buffer 0.451g/L; H 2 SO 4 1.64μg/L; vitamin B 12 0.1g/L; biotin 2.5g/L; nitrogen source 0.4g/L; pH= 6-9, the nitrogen source is composed of the following raw materials in parts by mass: amino acid: protein hydrolyzate: sodium nitrate: ammonium chloride = 2:2:1:2; the silicate is sodium silicate with a concentration of 20 mg/ L.
实施例23效果分析:Embodiment 23 effect analysis:
岩藻黄素含量为1.10%,岩藻黄素产量为3.08mg/(L·d)。The content of fucoxanthin is 1.10%, and the yield of fucoxanthin is 3.08 mg/(L·d).
Claims (6)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710523735.6A CN107099564A (en) | 2017-06-30 | 2017-06-30 | The method for producing fucoxanthin using the smooth rhombus algae of Heterotrophic culture |
PCT/CN2018/093490 WO2019001548A1 (en) | 2017-06-30 | 2018-06-29 | Method for preparing fucoxanthin by fermental cultivation of nitzschia laevis |
US16/310,367 US11572577B2 (en) | 2017-06-30 | 2018-06-29 | Fermentation method for production of fucoxanthin by Nitzschia laevis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710523735.6A CN107099564A (en) | 2017-06-30 | 2017-06-30 | The method for producing fucoxanthin using the smooth rhombus algae of Heterotrophic culture |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107099564A true CN107099564A (en) | 2017-08-29 |
Family
ID=59663402
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710523735.6A Pending CN107099564A (en) | 2017-06-30 | 2017-06-30 | The method for producing fucoxanthin using the smooth rhombus algae of Heterotrophic culture |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107099564A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108624646A (en) * | 2018-06-15 | 2018-10-09 | 北京大学 | The method that fucoxanthin zymotic fluid is prepared using stream plus ventilation culture |
CN108841887A (en) * | 2018-06-15 | 2018-11-20 | 北京大学 | The method for improving fucoxanthin content in the smooth diamond shape algae fermentation liquid of Heterotrophic culture using illumination |
WO2019001548A1 (en) * | 2017-06-30 | 2019-01-03 | 北京大学 | Method for preparing fucoxanthin by fermental cultivation of nitzschia laevis |
CN112094798A (en) * | 2020-09-22 | 2020-12-18 | 深圳大学 | Culture medium for improving fucoxanthin yield in rhombohedral alga and application thereof |
CN112359075A (en) * | 2020-10-15 | 2021-02-12 | 云南维他源生物科技有限公司 | Large-scale production method of fucoxanthin |
CN114214203A (en) * | 2021-12-27 | 2022-03-22 | 威海迪普森生物科技有限公司 | Method for increasing fucoxanthin yield through polyculture production of nitzschia closterium |
CN116286379A (en) * | 2023-04-03 | 2023-06-23 | 广东海洋大学 | Method for promoting microalgae to accumulate fucoxanthin and synthesizing lipid |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20130030979A1 (en) * | 2009-10-02 | 2013-01-31 | Trade Capture, Otc Corp. | Method and apparatus for displaying market depth and other information on a mobile phone, handheld device, or computer system |
CN103396979A (en) * | 2013-07-31 | 2013-11-20 | 华南理工大学 | Culture method for increasing yield of fucoxanthin contained in diatom |
CN103965143A (en) * | 2013-01-30 | 2014-08-06 | 中国科学院海洋研究所 | Method for extracting and separating fucoxanthin from marine unicellular diatom |
-
2017
- 2017-06-30 CN CN201710523735.6A patent/CN107099564A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20130030979A1 (en) * | 2009-10-02 | 2013-01-31 | Trade Capture, Otc Corp. | Method and apparatus for displaying market depth and other information on a mobile phone, handheld device, or computer system |
CN103965143A (en) * | 2013-01-30 | 2014-08-06 | 中国科学院海洋研究所 | Method for extracting and separating fucoxanthin from marine unicellular diatom |
CN103396979A (en) * | 2013-07-31 | 2013-11-20 | 华南理工大学 | Culture method for increasing yield of fucoxanthin contained in diatom |
Non-Patent Citations (5)
Title |
---|
BINGBING GUO等: "Screening of Diatom Strains and Characterization of Cyclotella cryptica as A Potential Fucoxanthin Producer", 《MARINE DRUGS》 * |
RICHARD C.STARR: "The Culture Collection of Algae at the University of TEXAS at Austin", 《JOURNAL OF PHYCOLOGY》 * |
ZHIYOU WEN等: "Application of statistically-based experimental designs for the optimization of eicosapentaenoic acid production by the diatom Nitzschia laevis", 《BIOTECHNOLOGY AND BIOENGINEERING》 * |
ZHIYOU WEN等: "High cell density culture of the diatom Nitzschia laevis for eicosapentaenoic acid production:fed-batch development", 《PROCESS BIOCHEMISTRY》 * |
耿玉凤: "硅藻中多不饱和脂肪酸抗肿瘤作用研究", 《中国优秀硕士学位论文全文数据库(电子期刊)医药卫生科技辑》 * |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2019001548A1 (en) * | 2017-06-30 | 2019-01-03 | 北京大学 | Method for preparing fucoxanthin by fermental cultivation of nitzschia laevis |
CN108624646A (en) * | 2018-06-15 | 2018-10-09 | 北京大学 | The method that fucoxanthin zymotic fluid is prepared using stream plus ventilation culture |
CN108841887A (en) * | 2018-06-15 | 2018-11-20 | 北京大学 | The method for improving fucoxanthin content in the smooth diamond shape algae fermentation liquid of Heterotrophic culture using illumination |
CN108841887B (en) * | 2018-06-15 | 2022-02-08 | 北京大学 | Method for increasing the content of fucoxanthin in fermentation broth of Heterotrophic Rhizobium platysma by utilizing light |
CN112094798A (en) * | 2020-09-22 | 2020-12-18 | 深圳大学 | Culture medium for improving fucoxanthin yield in rhombohedral alga and application thereof |
CN112359075A (en) * | 2020-10-15 | 2021-02-12 | 云南维他源生物科技有限公司 | Large-scale production method of fucoxanthin |
CN114214203A (en) * | 2021-12-27 | 2022-03-22 | 威海迪普森生物科技有限公司 | Method for increasing fucoxanthin yield through polyculture production of nitzschia closterium |
CN114214203B (en) * | 2021-12-27 | 2023-12-15 | 威海迪普森生物科技有限公司 | Method for improving fucoxanthin yield by mixing and preserving of nitenpyram |
CN116286379A (en) * | 2023-04-03 | 2023-06-23 | 广东海洋大学 | Method for promoting microalgae to accumulate fucoxanthin and synthesizing lipid |
CN116286379B (en) * | 2023-04-03 | 2024-02-23 | 广东海洋大学 | Method for promoting microalgae to accumulate fucoxanthin and synthesizing lipid |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN107119099B (en) | Method for producing fucoxanthin by culturing rhombohedral algae with light | |
CN107099564A (en) | The method for producing fucoxanthin using the smooth rhombus algae of Heterotrophic culture | |
CN108841887B (en) | Method for increasing the content of fucoxanthin in fermentation broth of Heterotrophic Rhizobium platysma by utilizing light | |
CN110250210B (en) | Optimal DSE strain for promoting corn seed soaking and rooting | |
CN101845395B (en) | A two-stage high-efficiency method for producing Nostocella cells and their exopolysaccharides | |
CN105647825B (en) | Method that is a kind of while improving spiral algal biomass and polysaccharide yield | |
CN114317277B (en) | Cell pre-culture method for improving heterotrophic production of astaxanthin by green alga Zuofu | |
Chen et al. | Optimized astaxanthin production in Chlorella zofingiensis under dark condition by response surface methodology | |
US11572577B2 (en) | Fermentation method for production of fucoxanthin by Nitzschia laevis | |
CN101445815A (en) | Microbial synthesis method of gamma-linolenic acid oil | |
CN105316246B (en) | Beta carotene high-yield strains and its application | |
CN103525871B (en) | Method for producing lycopene through fermentation | |
Yu | Effect of mixed carbon substrate on exopolysaccharide production of cyanobacterium Nostoc flagelliforme in mixotrophic cultures | |
CN105400842A (en) | Method for increasing yield of paclitaxel in endophytic fungus fermentation product | |
Pang et al. | A review of fucoxanthin biomanufacturing from Phaeodactylum tricornutum | |
CN112143669B (en) | A strain of cyanobacteria and its cultivation method and application | |
CN104673849A (en) | A kind of production process based on Flavobacterium producing vitamin K2 | |
CN112094798A (en) | Culture medium for improving fucoxanthin yield in rhombohedral alga and application thereof | |
CN108588143B (en) | Method for efficiently producing extracellular polysaccharide of long thread moss | |
CN102618468B (en) | Temperature-resistant alcaligenes and application thereof in welan gum production | |
CN113430126A (en) | Aureobasidium pullulans and method for preparing melanin polysaccharide by using same | |
CN102475033A (en) | Method for producing ganoderma lucidum mycelium rich in selenium | |
Prathumpai et al. | Effects of different carbon and nitrogen sources on naphthoquinone production of Cordyceps unilateralis BCC 1869 | |
CN1187438C (en) | Fungus strain for high yield chitinase and use thereof | |
CN115820423B (en) | A kind of Persian cladophora and its cultivation method and application |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170829 |