CN115074256A - Hericium erinaceus liquid fermentation medium and method for preparing triterpenes - Google Patents
Hericium erinaceus liquid fermentation medium and method for preparing triterpenes Download PDFInfo
- Publication number
- CN115074256A CN115074256A CN202210805087.4A CN202210805087A CN115074256A CN 115074256 A CN115074256 A CN 115074256A CN 202210805087 A CN202210805087 A CN 202210805087A CN 115074256 A CN115074256 A CN 115074256A
- Authority
- CN
- China
- Prior art keywords
- hericium erinaceus
- fermentation
- liquid fermentation
- water
- mycelium
- 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.)
- Granted
Links
- 238000000855 fermentation Methods 0.000 title claims abstract description 128
- 230000004151 fermentation Effects 0.000 title claims abstract description 128
- 240000000588 Hericium erinaceus Species 0.000 title claims abstract description 111
- 235000007328 Hericium erinaceus Nutrition 0.000 title claims abstract description 111
- 239000007788 liquid Substances 0.000 title claims abstract description 103
- 150000003648 triterpenes Chemical class 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims abstract description 30
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 58
- 239000001963 growth medium Substances 0.000 claims abstract description 43
- 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 abstract description 26
- 239000008103 glucose Substances 0.000 claims abstract description 26
- 229940041514 candida albicans extract Drugs 0.000 claims abstract description 23
- 229910000402 monopotassium phosphate Inorganic materials 0.000 claims abstract description 23
- 235000019796 monopotassium phosphate Nutrition 0.000 claims abstract description 23
- 239000012138 yeast extract Substances 0.000 claims abstract description 23
- 229920002472 Starch Polymers 0.000 claims abstract description 15
- WRUGWIBCXHJTDG-UHFFFAOYSA-L magnesium sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Mg+2].[O-]S([O-])(=O)=O WRUGWIBCXHJTDG-UHFFFAOYSA-L 0.000 claims abstract description 15
- 229940061634 magnesium sulfate heptahydrate Drugs 0.000 claims abstract description 15
- 235000019698 starch Nutrition 0.000 claims abstract description 15
- 239000008107 starch Substances 0.000 claims abstract description 15
- GNSKLFRGEWLPPA-UHFFFAOYSA-M potassium dihydrogen phosphate Chemical compound [K+].OP(O)([O-])=O GNSKLFRGEWLPPA-UHFFFAOYSA-M 0.000 claims abstract description 8
- LWIHDJKSTIGBAC-UHFFFAOYSA-K potassium phosphate Substances [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 claims abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 42
- 239000002609 medium Substances 0.000 claims description 35
- 230000004913 activation Effects 0.000 claims description 18
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 claims description 16
- 238000001914 filtration Methods 0.000 claims description 15
- PJNZPQUBCPKICU-UHFFFAOYSA-N phosphoric acid;potassium Chemical compound [K].OP(O)(O)=O PJNZPQUBCPKICU-UHFFFAOYSA-N 0.000 claims description 15
- 238000002137 ultrasound extraction Methods 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 11
- 229920001817 Agar Polymers 0.000 claims description 8
- 239000001888 Peptone Substances 0.000 claims description 8
- 108010080698 Peptones Proteins 0.000 claims description 8
- 230000003213 activating effect Effects 0.000 claims description 8
- 239000008272 agar Substances 0.000 claims description 8
- 229910052943 magnesium sulfate Inorganic materials 0.000 claims description 8
- 235000019341 magnesium sulphate Nutrition 0.000 claims description 8
- 235000019319 peptone Nutrition 0.000 claims description 8
- 230000001580 bacterial effect Effects 0.000 claims description 7
- 239000006228 supernatant Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 238000005119 centrifugation Methods 0.000 claims description 4
- 239000000706 filtrate Substances 0.000 claims description 3
- JZRWCGZRTZMZEH-UHFFFAOYSA-N thiamine Chemical compound CC1=C(CCO)SC=[N+]1CC1=CN=C(C)N=C1N JZRWCGZRTZMZEH-UHFFFAOYSA-N 0.000 claims description 3
- 239000000243 solution Substances 0.000 claims 3
- 239000007864 aqueous solution Substances 0.000 claims 1
- 241000894007 species Species 0.000 claims 1
- 241000233866 Fungi Species 0.000 abstract description 21
- 238000000605 extraction Methods 0.000 abstract description 6
- 235000016709 nutrition Nutrition 0.000 abstract description 5
- 229930000044 secondary metabolite Natural products 0.000 abstract description 2
- 239000008188 pellet Substances 0.000 description 39
- 239000000306 component Substances 0.000 description 22
- 230000001954 sterilising effect Effects 0.000 description 22
- 238000012258 culturing Methods 0.000 description 13
- 238000004659 sterilization and disinfection Methods 0.000 description 13
- 238000005520 cutting process Methods 0.000 description 12
- 238000001035 drying Methods 0.000 description 12
- 238000005303 weighing Methods 0.000 description 12
- 239000010410 layer Substances 0.000 description 8
- MIJYXULNPSFWEK-GTOFXWBISA-N 3beta-hydroxyolean-12-en-28-oic acid Chemical compound C1C[C@H](O)C(C)(C)[C@@H]2CC[C@@]3(C)[C@]4(C)CC[C@@]5(C(O)=O)CCC(C)(C)C[C@H]5C4=CC[C@@H]3[C@]21C MIJYXULNPSFWEK-GTOFXWBISA-N 0.000 description 7
- JKLISIRFYWXLQG-UHFFFAOYSA-N Epioleonolsaeure Natural products C1CC(O)C(C)(C)C2CCC3(C)C4(C)CCC5(C(O)=O)CCC(C)(C)CC5C4CCC3C21C JKLISIRFYWXLQG-UHFFFAOYSA-N 0.000 description 7
- YBRJHZPWOMJYKQ-UHFFFAOYSA-N Oleanolic acid Natural products CC1(C)CC2C3=CCC4C5(C)CCC(O)C(C)(C)C5CCC4(C)C3(C)CCC2(C1)C(=O)O YBRJHZPWOMJYKQ-UHFFFAOYSA-N 0.000 description 7
- MIJYXULNPSFWEK-UHFFFAOYSA-N Oleanolinsaeure Natural products C1CC(O)C(C)(C)C2CCC3(C)C4(C)CCC5(C(O)=O)CCC(C)(C)CC5C4=CCC3C21C MIJYXULNPSFWEK-UHFFFAOYSA-N 0.000 description 7
- 229910052799 carbon Inorganic materials 0.000 description 7
- 235000015097 nutrients Nutrition 0.000 description 7
- 229940100243 oleanolic acid Drugs 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 7
- HZLWUYJLOIAQFC-UHFFFAOYSA-N prosapogenin PS-A Natural products C12CC(C)(C)CCC2(C(O)=O)CCC(C2(CCC3C4(C)C)C)(C)C1=CCC2C3(C)CCC4OC1OCC(O)C(O)C1O HZLWUYJLOIAQFC-UHFFFAOYSA-N 0.000 description 7
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 239000004744 fabric Substances 0.000 description 6
- 238000005259 measurement Methods 0.000 description 6
- 239000002207 metabolite Substances 0.000 description 6
- 239000002356 single layer Substances 0.000 description 6
- 229960000583 acetic acid Drugs 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 230000008901 benefit Effects 0.000 description 5
- 239000012362 glacial acetic acid Substances 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000011782 vitamin Substances 0.000 description 5
- 235000013343 vitamin Nutrition 0.000 description 5
- 229930003231 vitamin Natural products 0.000 description 5
- 229940088594 vitamin Drugs 0.000 description 5
- 150000003722 vitamin derivatives Chemical class 0.000 description 5
- 238000002835 absorbance Methods 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- VLTRZXGMWDSKGL-UHFFFAOYSA-N perchloric acid Chemical compound OCl(=O)(=O)=O VLTRZXGMWDSKGL-UHFFFAOYSA-N 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000003153 chemical reaction reagent Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000006911 enzymatic reaction Methods 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 239000012533 medium component Substances 0.000 description 3
- 230000002503 metabolic effect Effects 0.000 description 3
- 230000004060 metabolic process Effects 0.000 description 3
- 230000012666 negative regulation of transcription by glucose Effects 0.000 description 3
- 229910052757 nitrogen Inorganic materials 0.000 description 3
- 230000035764 nutrition Effects 0.000 description 3
- 238000004506 ultrasonic cleaning Methods 0.000 description 3
- 241000282693 Cercopithecidae Species 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 206010028980 Neoplasm Diseases 0.000 description 2
- 241000700605 Viruses Species 0.000 description 2
- 239000013543 active substance Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 210000004027 cell Anatomy 0.000 description 2
- 210000000170 cell membrane Anatomy 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
- 238000001816 cooling Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 150000004676 glycans Chemical class 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920001184 polypeptide Polymers 0.000 description 2
- 229920001282 polysaccharide Polymers 0.000 description 2
- 239000005017 polysaccharide Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 102000004196 processed proteins & peptides Human genes 0.000 description 2
- 108090000765 processed proteins & peptides Proteins 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 230000029058 respiratory gaseous exchange Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000011573 trace mineral Substances 0.000 description 2
- 235000013619 trace mineral Nutrition 0.000 description 2
- 238000000870 ultraviolet spectroscopy Methods 0.000 description 2
- 206010000060 Abdominal distension Diseases 0.000 description 1
- 241000251730 Chondrichthyes Species 0.000 description 1
- 208000007882 Gastritis Diseases 0.000 description 1
- 241000123222 Hericium Species 0.000 description 1
- 241000251511 Holothuroidea Species 0.000 description 1
- 206010061218 Inflammation Diseases 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 208000007107 Stomach Ulcer Diseases 0.000 description 1
- 241001052560 Thallis Species 0.000 description 1
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 230000006696 biosynthetic metabolic pathway Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000015895 biscuits Nutrition 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 235000012000 cholesterol Nutrition 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000012043 crude product Substances 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 208000000718 duodenal ulcer Diseases 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 239000003797 essential amino acid Substances 0.000 description 1
- 235000020776 essential amino acid Nutrition 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 230000006870 function Effects 0.000 description 1
- 201000005917 gastric ulcer Diseases 0.000 description 1
- 210000001035 gastrointestinal tract Anatomy 0.000 description 1
- 229930182470 glycoside Natural products 0.000 description 1
- 150000002338 glycosides Chemical class 0.000 description 1
- 230000002779 inactivation Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000004054 inflammatory process Effects 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000010977 jade Substances 0.000 description 1
- 238000009630 liquid culture Methods 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 108020004707 nucleic acids Proteins 0.000 description 1
- 102000039446 nucleic acids Human genes 0.000 description 1
- 150000007523 nucleic acids Chemical class 0.000 description 1
- 239000002773 nucleotide Substances 0.000 description 1
- 125000003729 nucleotide group Chemical group 0.000 description 1
- 235000021049 nutrient content Nutrition 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000001766 physiological effect Effects 0.000 description 1
- 230000035479 physiological effects, processes and functions Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000000241 respiratory effect Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 235000014102 seafood Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- -1 terpenoid compound Chemical class 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
- MWOOGOJBHIARFG-UHFFFAOYSA-N vanillin Chemical compound COC1=CC(C=O)=CC=C1O MWOOGOJBHIARFG-UHFFFAOYSA-N 0.000 description 1
- FGQOOHJZONJGDT-UHFFFAOYSA-N vanillin Natural products COC1=CC(O)=CC(C=O)=C1 FGQOOHJZONJGDT-UHFFFAOYSA-N 0.000 description 1
- 235000012141 vanillin Nutrition 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
- 210000001835 viscera Anatomy 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Images
Classifications
-
- 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
- C12N1/14—Fungi; Culture media therefor
-
- 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
- C12P33/00—Preparation of steroids
- C12P33/20—Preparation of steroids containing heterocyclic rings
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12R—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES C12C - C12Q, RELATING TO MICROORGANISMS
- C12R2001/00—Microorganisms ; Processes using microorganisms
- C12R2001/645—Fungi ; Processes using fungi
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Biotechnology (AREA)
- Genetics & Genomics (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Microbiology (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- General Engineering & Computer Science (AREA)
- Mycology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Botany (AREA)
- General Chemical & Material Sciences (AREA)
- Medicinal Chemistry (AREA)
- Tropical Medicine & Parasitology (AREA)
- Virology (AREA)
- Biomedical Technology (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
The invention provides a hericium erinaceus liquid fermentation culture medium and a method for preparing triterpenes, wherein the hericium erinaceus liquid fermentation culture medium comprises the following components in percentage by mass: 2 to 4 percent of glucose, 1 to 3 percent of soluble starch, 0.5 to 1.5 percent of yeast extract, 0.05 to 0.15 percent of monopotassium phosphate, 0.04 to 0.1 percent of magnesium sulfate heptahydrate and the balance of water. According to the invention, the fermentation conditions for the hericium erinaceus to grow at the fastest speed are found by optimizing the fermentation conditions of the edible fungus liquid. The invention also optimizes the triterpene extraction conditions, increases the content of secondary metabolite triterpene of the hericium erinaceus, and increases the nutritional value and economic value of the hericium erinaceus.
Description
Technical Field
The invention relates to the technical field of bioengineering, in particular to a hericium erinaceus liquid fermentation medium and a method for preparing triterpenes.
Background
Hericium erinaceus is a large-scale edible fungus of the Hericium genus. The fruit body is large in meat quality and looks like the head of a monkey, so the monkey is called as a hericium erinaceus. The hericium erinaceus is one of eight Chinese "mountain delicacies", the mountain delicacies hericium erinaceus and the seafood cubilose are listed as four famous vegetables together with the bear paw, the sea cucumber and the shark fin, and are tender in meat, delicious, tasty, rich in nutrition, superior in color, fragrance and taste. In addition, the hericium erinaceus is also a traditional precious Chinese medicinal material in China, and has the functions of nourishing, building body, promoting digestion and benefiting five internal organs. Modern researches show that the traditional Chinese medicine composition contains active ingredients such as polypeptide, polysaccharide, fat, protein and the like, and has certain curative effects on digestive tract tumors, gastric ulcer, duodenal ulcer, gastritis, abdominal distension and the like. The economic value of the hericium erinaceus is high, such as hericium erinaceus health-care beverage, hericium erinaceus biscuits, hericium erinaceus rice and the like.
The liquid fermentation technology is one of the modern biotechnology, and is a process of dissolving some trace elements such as carbon source, nitrogen source, inorganic salt and the like and other nutrient substances necessary for edible and medicinal fungi in the growth process in pure water to be used as a culture medium, inoculating the strains after sterilization, introducing sterile air and stirring to provide oxygen required by respiratory metabolism of edible fungi, controlling proper external conditions, and carrying out mass culture and propagation of hyphae. The industrialized large-scale fermentation culture is fermentation production, also called submerged culture or submerged culture. The obtained fermentation liquid contains thallus, nutrient components decomposed and not decomposed by thallus, and metabolite produced by thallus. Compared with solid plate culture of edible fungi, liquid fermentation has many advantages, such as rapid growth of mycelium, and uniform distribution of nutrients in liquid culture medium, and is beneficial to full contact and absorption of fungi nutrients. Hypha cells can grow in a culture medium under the conditions of optimal temperature, pH, oxygen and carbon-nitrogen ratio, and metabolic waste gas generated by respiration can be discharged in time, so that metabolism is vigorous, hypha grows and splits quickly, and a large amount of mycelium, polysaccharide, polypeptide and other metabolites with physiological activity can be accumulated in a short time; the production cycle is short, the time for obtaining a large amount of mycelium and physiologically active substances through liquid fermentation culture of edible and medicinal fungi is only about 10 days generally, and the solid culture time is 20-30 days.
The carbon source is a carbon source for the growth of the hericium erinaceus and is also an energy source for the metabolic activity of the hericium erinaceus, and is a raw material for generating various metabolic substances. Glucose is the most predominant carbon source and is also the most commonly used carbon source. However, the addition of too much glucose is disadvantageous in the growth of hyphae due to the glucose effect. The nitrogen source is an important nutrient component of the hericium erinaceus mycelium and is also an indispensable raw material for synthesizing protein and nucleic acid by the hericium erinaceus. The potassium dihydrogen phosphate and magnesium sulfate heptahydrate are used as inorganic salts to maintain the osmotic pressure of the culture solution and the cell morphology.
The temperature has great influence on the fermentation of the hericium erinaceus liquid and is complicated. Firstly, the temperature influences the growth speed of hericium erinaceus mycelium pellets, and with the temperature rise, the growth and the propagation speed of the hericium erinaceus are accelerated because enzymes participate in the growth metabolism and the propagation of the hericium erinaceus. According to the kinetics of the enzymatic reaction, the temperature is increased, the enzymatic reaction is enhanced, and the respiration intensity is increased, so that the growth speed of the hericium erinaceus is increased. But with the rise of temperature, the speed of enzyme inactivation is accelerated, the fermentation period is shortened, and thalli die; secondly, temperature affects the yield of hericium erinaceus metabolites; finally, the temperature influences the physical properties of the liquid fermentation broth, indirectly influences the biosynthesis of the hericium erinaceus by changing the physical properties of the fermentation broth, and also influences the absorption of the hericium erinaceus on nutrient substances in the fermentation broth.
The pH has great influence on the liquid fermentation of the hericium erinaceus, firstly, the pH also influences the enzymatic reaction of the hericium erinaceus, strong acid and strong alkali easily inactivate the hericium erinaceus and reduce the growth speed of the hericium erinaceus; secondly, the pH influences the charge state of the hericium erinaceus cell membrane, causes the permeability change of the cell membrane, further influences the absorption of the hericium erinaceus on nutrient substances, influences the growth speed of the hericium erinaceus, and influences the generation of metabolites; in addition, pH also affects the morphology of hericium erinaceus; finally, pH has a significant impact on certain biosynthetic pathways of hericium erinaceus. Experiments prove that the hericium erinaceus can absorb organic components in the fermentation liquor only in a medium-acidity environment.
The shaking table rotational speed can change dissolved oxygen volume, and dissolved oxygen influences the growth of mycelium through participating in the physiology and biochemistry and the in-process of hericium erinaceus liquid fermentation, and the rotational speed undersize can influence dissolved oxygen and then influence the growth of hypha, and the rotational speed is too big then can force the hypha to become the piece, thereby the agglomeration suppresses the hypha and grows.
The triterpene component is a terpenoid compound with a basic parent nucleus composed of 30 carbon atoms, exists in a free form or a form combined with sugar into glycoside or ester, and has various biochemical activities. Triterpenes are also important active substances in hericium erinaceus, can be used for resisting cancers, bacteria and viruses, resisting inflammation and viruses and reducing cholesterol, and are beneficial to human bodies.
Therefore, the hericium erinaceus is required to be developed rapidly, industrial production is realized, a liquid fermentation culture medium suitable for the hericium erinaceus is researched, the most suitable fermentation condition is found, and growth of hericium erinaceus hyphae can be accelerated. An optimal triterpene extraction method is found, the yield of triterpene products can be increased, and the economic benefit of the hericium erinaceus is improved.
Disclosure of Invention
The purpose of the invention is as follows: the invention aims to solve the technical problem of the prior art and provides a hericium erinaceus liquid fermentation culture medium to effectively accelerate the growth of bacteria and the generation of bacteria metabolites.
The invention also aims to solve the technical problem of providing a method for producing mycelium spheres by fermenting hericium erinaceus.
The invention also aims to solve the technical problem of providing a method for preparing the hericium erinaceus triterpene.
In order to solve the first technical problem, the invention discloses a hericium erinaceus liquid fermentation culture medium which comprises the following components in percentage by mass: 2 to 4 percent of glucose, 1 to 3 percent of soluble starch, 0.5 to 1.5 percent of yeast extract, 0.05 to 0.15 percent of monopotassium phosphate, 0.04 to 0.1 percent of magnesium sulfate heptahydrate and the balance of water. In some embodiments, the hericium erinaceus liquid fermentation medium comprises the following components in percentage by mass: 3% of glucose, 2% of soluble starch, 1% of yeast extract, 0.1% of monopotassium phosphate, 0.06% of magnesium sulfate heptahydrate and the balance of water.
The hericium erinaceus liquid fermentation culture medium is suitable for all hericium erinaceus in the prior art, and comprises but is not limited to hericium erinaceus first-level test tube strains (in the research of Wuhanzhou jade unicorn edible fungi) ((https://m.tb.cn/h.ft114lesm= b79355tk=Xvjk29O0vbZ)。
In some embodiments, the hericium erinaceus liquid fermentation culture medium is sterilized in a sterilization pot, and incubated at 115 ℃ for 20 min.
In order to solve the second technical problem, the invention discloses a method for producing mycelium spheres by hericium erinaceus fermentation, which comprises the step of inoculating a strain obtained by activating hericium erinaceus into the liquid fermentation culture medium for fermentation to obtain the hericium erinaceus mycelium spheres.
In some embodiments, the activation medium in the activating comprises the following components in weight percent: 2% of glucose, 10% of bran water, 0.4% of peptone, 0.3% of yeast extract, 2% of agar, 0.1% of potassium dihydrogen phosphate, 0.05% of magnesium sulfate and vitamin B 1 0.001% and the balance of water. In some embodiments, the bran water is prepared as follows: adding the crude bran into water with the dosage of 80-120g/500mL, boiling, preserving the heat for 10-50min, and filtering by using one-seven layers of gauze to obtain filtrate, namely bran water. In some embodiments, the bran water is prepared as follows: crude product is treatedAdding 100g/500mL bran into water, boiling, keeping the temperature for 30min, and filtering with four layers of gauze to obtain filtrate, namely bran water.
In some embodiments, the activation is performed by inoculating a piece of hericium erinaceus cut 0.5cm by 0.5cm in a sterile environment into an activation medium, and culturing the piece of hericium erinaceus in an incubator at 26 ℃ for 12 to 14 days to obtain an activated strain.
In some embodiments, the seed is inoculated into the liquid fermentation medium at an amount of 1-5 pieces per 100 mL; in some embodiments, the seed is at 0.5 x 0.5cm 3 Piece 3 pieces/100 mL of the amount inoculated into the liquid fermentation medium.
In some embodiments, the initial pH of the fermentation is 5.0-6.0, the fermentation temperature is 25-29 ℃, and the rotation speed of the shaker during the fermentation is 150-210 r/min. In some embodiments, the initial pH of the fermentation is 5.5, the temperature of the fermentation is 27 ℃, and the rotation speed of the shaker during the fermentation is 180 r/min.
In some embodiments, the fermentation time is 8-12 days; in some embodiments, the fermentation time is 10 days.
In order to solve the third technical problem, the invention discloses a method for preparing hericium erinaceus triterpene, which comprises the steps of dissolving mycelium spheres prepared by the method in an ethanol water solution, carrying out ultrasonic extraction and centrifuging, and obtaining supernate, namely the extracting solution containing the hericium erinaceus triterpene.
In some embodiments, the ethanol solution has a concentration of 40% to 80% by volume ethanol; in some embodiments, the ethanol solution has a concentration of 80% ethanol by volume.
In some embodiments, the feed-to-liquid ratio of the mycelium spheres to the aqueous ethanol solution is 1g:15-30 mL; in some embodiments, the feed-to-liquid ratio of the mycelium spheres to the aqueous ethanol solution is 1g to 30 mL.
In some embodiments, the temperature of the ultrasonic extraction is 40-80 ℃; in some embodiments, the temperature of the ultrasonic extraction is 80 ℃.
In some embodiments, the time of the ultrasonic extraction is 10-50 min; in some embodiments, the time of the ultrasound extraction is 30 min.
In some embodiments, the frequency of the ultrasonic extraction is 30-50 khz; in some embodiments, the frequency of the ultrasonic extraction is 40 khz.
In some embodiments, the rotational speed of the centrifugation is 3000-; in some embodiments, the rotation speed of the centrifuge is 4000 r/min.
In some embodiments, the time of centrifugation is 5-15 min; in some embodiments, the time of centrifugation is 10 min.
In some embodiments, the triterpene content is determined by uv spectrophotometry, which comprises the following steps: firstly, preparing a triterpene standard oleanolic acid into an oleanolic acid solution with the concentration of 0.2mg/ml, respectively sucking 0,0.1,0.2,0.3,0.4,0.5ml and 25ml colorimetric tubes, evaporating a solvent in a boiling water bath, adding 0.5ml of vanillin-glacial acetic acid solution with the concentration of 50g/L and 1ml of perchloric acid solution, mixing, carrying out water bath at 60 ℃ for 20min, cooling with cold water for 15min, and then adding 3ml of glacial acetic acid. Reacting at room temperature for 10min, and measuring absorbance at 547nm, and making standard curve with oleanolic acid quality as abscissa and absorbance as ordinate. Adding the triterpene extractive solution into corresponding reagent according to the above method, measuring under the same conditions, and fitting into standard curve to obtain triterpene content.
Has the advantages that: compared with the prior art, the invention has the following advantages:
the invention provides a culture medium for liquid fermentation of hericium erinaceus, and the fermentation conditions which enable the growth speed of the hericium erinaceus to be fastest are found by optimizing the fermentation conditions of edible fungus liquid.
According to the invention, the triterpene extraction conditions are optimized, so that the content of the secondary metabolite triterpene of the hericium erinaceus is increased, and the nutritional value and the economic value of the hericium erinaceus are increased.
Drawings
The foregoing and/or other advantages of the invention will become more apparent from the following detailed description of the invention when taken in conjunction with the accompanying drawings.
FIG. 1 shows the growth of Hericium erinaceum on an activated medium.
FIG. 2 shows the growth of Hericium erinaceus in a fermentation medium.
FIG. 3 shows oven-dried Hericium erinaceus mycelia.
FIG. 4 shows the milling of Hericium erinaceum mycelia.
FIG. 5 shows the triterpene extract from Hericium erinaceum.
Detailed Description
The experimental methods described in the following examples are all conventional methods unless otherwise specified; the reagents and materials are commercially available, unless otherwise specified.
The hericium erinaceus slant strain (hericium erinaceus) is a hericium erinaceus first-grade test tube strain (https:// m.tb.cn/h.ft114lesm ═ b79355tk ═ Xvjk29O0vbZ) purchased from the study of edible fungi of the pericarp of wuhan zhou.
In examples 1 to 3, the external fermentation conditions were the same in each example, the initial pH was 5.5, and the mixture was cultured on a shaker at 27 ℃ and 180r/min for 10 days
Example 1: preparation of mycelium ball by liquid fermentation of hericium erinaceus
(1) Activation of mother strain: cutting Hericium Erinaceus slant strain in refrigerator under aseptic environment to obtain 0.5cm × 0.5cm block, inoculating on activation culture medium, and culturing in constant temperature box at 26 deg.C for 12-14 days to obtain first-stage strain (FIG. 1). The mass contents of the components in the activation medium are as follows: 2% of glucose, 10% of bran water, 0.4% of peptone, 0.3% of yeast extract, 2% of agar, 0.1% of potassium dihydrogen phosphate, 0.05% of magnesium sulfate and vitamin B 1 0.001%, and water in balance, wherein the bran water is prepared by adding 100g crude bran into about 500ml pure water, boiling, keeping the temperature for 30min, and filtering on four layers of gauze.
(2) Sterilization of liquid fermentation medium: preparing a liquid fermentation culture medium, wherein the components of the liquid fermentation culture medium comprise, by weight, 2% of glucose, 1% of soluble starch, 0.5% of yeast extract, 0.05% of monopotassium phosphate, 0.04% of magnesium sulfate heptahydrate and the balance of pure water, and the pH value is 5.5. Putting the liquid fermentation medium into a 250mL triangular flask according to the amount of 100mL, putting the triangular flask into a sterilizing pot, sterilizing at 115 ℃ for 20min, and drying in a 65 ℃ oven after sterilization.
(3) Liquid fermentation of hericium erinaceus: and (2) cutting off 0.5cm x 0.5cm of the primary strain obtained in the step (1), inoculating 3 fungus blocks into the liquid fermentation medium obtained in the step (2) under an aseptic condition, and culturing on a shaking table at 27 ℃ and 180r/min for 10 days (figure 2) to form mycelium spheres, thereby obtaining a fermentation liquid containing the mycelium spheres.
Dry weight measurement by hypha dry weight method: and (3) filtering the mycelium pellets obtained in the step (3) by using single-layer filter cloth, weighing a clean flat plate, flatly paving the filtered mycelium pellets on the flat plate, drying the mycelium pellets in a 65-DEG C oven (shown in figure 3), weighing again, wherein the weight of the flat plate subtracted from the total weight is the dry weight of the mycelium, and storing the filtered bacterial liquid in a refrigerator for later use.
Example 2: preparation of mycelium ball by liquid fermentation of hericium erinaceus
(1) Activation of mother strain: cutting Hericium Erinaceus slant strain in refrigerator under aseptic environment to obtain 0.5cm × 0.5cm block, inoculating on activating culture medium, and culturing in constant temperature box at 26 deg.C for 12-14 days to obtain first-stage strain. The mass contents of the components in the activation medium are as follows: glucose 2%, bran water 10%, peptone 0.4%, yeast extract 0.3%, agar 2%, potassium dihydrogen phosphate 0.1%, magnesium sulfate 0.05%, vitamin B10.001%, and water in balance, wherein the bran water is prepared by adding about 500ml pure water into 100g of crude bran, boiling, keeping the temperature for 30min, and filtering on four layers of gauze.
(2) And (3) sterilizing a liquid fermentation medium: preparing a liquid fermentation culture medium, wherein the components of the liquid fermentation culture medium comprise, by weight, 3% of glucose, 2% of soluble starch, 1% of yeast extract, 0.1% of potassium dihydrogen phosphate, 0.06% of magnesium sulfate heptahydrate and the balance of pure water, and the pH value is 5.5. Placing the liquid fermentation culture medium into a 250mL triangular flask according to the amount of 100mL, placing the triangular flask into a sterilizing pot at 115 ℃, preserving the temperature for 20min for sterilization, and placing the sterilized liquid fermentation culture medium into a 65 ℃ oven for drying.
(3) Liquid fermentation of edible fungi: and (3) cutting off the primary strain obtained in the step (1) by 0.5cm x 0.5cm, inoculating the cut primary strain into the liquid fermentation medium obtained in the step (2), inoculating 3 fungus blocks into each bottle under an aseptic condition, and culturing on a shaking table at the temperature of 27 ℃ and the speed of 180r/min for 10 days to form mycelium spheres, thereby obtaining the fermentation liquid containing the mycelium spheres.
Dry weight measurement by hypha dry weight method: and (4) filtering the mycelium pellets obtained in the step (3) by using single-layer filter cloth, weighing a clean flat plate, flatly paving the filtered mycelium pellets on the flat plate, drying the mycelium pellets in a 65-DEG C oven, weighing again, and storing the filtered bacterial liquid in a refrigerator for later use, wherein the weight of the filtered mycelium pellets is subtracted from the total weight of the mycelium pellets to obtain the dry weight of the mycelium.
Example 3: mycelium sphere prepared by hericium erinaceus liquid fermentation
(1) Activation of mother strain: cutting Hericium Erinaceus slant strain in refrigerator under aseptic environment to obtain 0.5cm × 0.5cm block, inoculating on activating culture medium, and culturing in constant temperature box at 26 deg.C for 12-14 days to obtain first-stage strain. The mass contents of the components in the activation medium are as follows: glucose 2%, bran water 10%, peptone 0.4%, yeast extract 0.3%, agar 2%, potassium dihydrogen phosphate 0.1%, magnesium sulfate 0.05%, vitamin B10.001%, and water in balance, wherein the bran water is prepared by adding about 500ml pure water into 100g of crude bran, boiling, keeping the temperature for 30min, and filtering on four layers of gauze.
(2) And (3) sterilizing a liquid fermentation medium: preparing a liquid fermentation culture medium, wherein the components of the liquid fermentation culture medium comprise, by weight, 4% of glucose, 3% of soluble starch, 1.5% of yeast extract, 0.15% of monopotassium phosphate, 0.1% of magnesium sulfate heptahydrate and the balance of pure water, and the pH value is 5.5. Placing the liquid fermentation culture medium into a 250mL triangular flask according to the amount of 100mL, placing the triangular flask into a sterilizing pot at 115 ℃, preserving the temperature for 20min for sterilization, and placing the sterilized liquid fermentation culture medium into a 65 ℃ oven for drying.
(3) Liquid fermentation of edible fungi: and (3) cutting off the primary strain obtained in the step (1) by 0.5cm x 0.5cm, inoculating the cut primary strain into the liquid fermentation medium obtained in the step (2), inoculating 3 fungus blocks into each bottle under an aseptic condition, and culturing on a shaking table at the temperature of 27 ℃ and the speed of 180r/min for 10 days to form mycelium spheres, thereby obtaining the fermentation liquid containing the mycelium spheres.
Dry weight measurement by hypha dry weight method: and (4) filtering the mycelium pellets obtained in the step (3) by using single-layer filter cloth, weighing a clean flat plate, flatly paving the filtered mycelium pellets on the flat plate, drying the mycelium pellets in a 65-DEG C oven, weighing again, and storing the filtered bacterial liquid in a refrigerator for later use, wherein the weight of the filtered mycelium pellets is subtracted from the total weight of the mycelium pellets to obtain the dry weight of the mycelium.
In examples 4 to 6, the fermentation medium components were identical in each example, and the medium components were glucose 3%, soluble starch 2%, yeast extract 1%, potassium dihydrogen phosphate 0.1%, magnesium sulfate heptahydrate 0.06%, and pure water in balance
Example 4: preparation of mycelium ball by liquid fermentation of hericium erinaceus
(1) Activation of mother strain: cutting Hericium Erinaceus slant strain in refrigerator under aseptic environment to obtain 0.5cm × 0.5cm block, inoculating on activating culture medium, and culturing in constant temperature box at 26 deg.C for 12-14 days to obtain first-stage strain. The mass contents of the components in the activation medium are as follows: glucose 2%, bran water 10%, peptone 0.4%, yeast extract 0.3%, agar 2%, potassium dihydrogen phosphate 0.1%, magnesium sulfate 0.05%, vitamin B10.001%, and water in balance, wherein the bran water is prepared by adding about 500ml pure water into 100g of crude bran, boiling, keeping the temperature for 30min, and filtering on four layers of gauze.
(2) Sterilization of liquid fermentation medium: preparing a liquid fermentation culture medium, wherein the components of the liquid fermentation culture medium comprise, by weight, 3% of glucose, 2% of soluble starch, 1% of yeast extract, 0.1% of potassium dihydrogen phosphate, 0.06% of magnesium sulfate heptahydrate and the balance of pure water, and the pH value is 5.0. Placing the liquid fermentation culture medium into a 250mL triangular flask according to the amount of 100mL, placing the triangular flask into a sterilizing pot at 115 ℃, preserving the temperature for 20min for sterilization, and placing the sterilized liquid fermentation culture medium into a 65 ℃ oven for drying.
(3) Liquid fermentation of edible fungi: and (3) cutting off the primary strain obtained in the step (1) by 0.5cm x 0.5cm, inoculating the cut primary strain into the liquid fermentation medium obtained in the step (2), inoculating 3 fungus blocks into each bottle under aseptic conditions, and culturing for 10 days on a shaking bed at the temperature of 25 ℃ and at the speed of 150r/min to form mycelium spheres, thereby obtaining the fermentation liquid containing the mycelium spheres.
Dry weight measurement by hypha dry weight method: and (4) filtering the mycelium pellets obtained in the step (3) by using single-layer filter cloth, weighing a clean flat plate, flatly paving the filtered mycelium pellets on the flat plate, drying the mycelium pellets in a 65-DEG C oven, weighing again, and storing the filtered bacterial liquid in a refrigerator for later use, wherein the weight of the filtered mycelium pellets is subtracted from the total weight of the mycelium pellets to obtain the dry weight of the mycelium.
Example 5: preparation of mycelium ball by liquid fermentation of hericium erinaceus
(1) Activation of mother strain: cutting Hericium Erinaceus slant strain in refrigerator under aseptic environment to obtain 0.5cm × 0.5cm block, inoculating on activating culture medium, and culturing in constant temperature box at 26 deg.C for 12-14 days to obtain first-stage strain. The mass contents of the components in the activation medium are as follows: glucose 2%, bran water 10%, peptone 0.4%, yeast extract 0.3%, agar 2%, potassium dihydrogen phosphate 0.1%, magnesium sulfate 0.05%, vitamin B10.001%, and water in balance, wherein the bran water is prepared by adding about 500ml pure water into 100g of crude bran, boiling, keeping the temperature for 30min, and filtering on four layers of gauze.
(2) Sterilization of liquid fermentation medium: preparing a liquid fermentation culture medium, wherein the components of the liquid fermentation culture medium comprise, by weight, 3% of glucose, 2% of soluble starch, 1% of yeast extract, 0.1% of potassium dihydrogen phosphate, 0.06% of magnesium sulfate heptahydrate and the balance of pure water, and the pH value is 5.5. Putting the liquid fermentation medium into a 250mL triangular flask according to the amount of 100mL, putting the triangular flask into a sterilization pot, sterilizing at 115 ℃ for 20min, and putting the triangular flask into a 65 ℃ oven for drying after sterilization.
(3) Liquid fermentation of edible fungi: and (3) cutting off the primary strain obtained in the step (1) by 0.5cm x 0.5cm, inoculating the cut primary strain into the liquid fermentation medium obtained in the step (2), inoculating 3 fungus blocks into each bottle under an aseptic condition, and culturing on a shaking table at the temperature of 27 ℃ and the speed of 180r/min for 10 days to form mycelium spheres, thereby obtaining the fermentation liquid containing the mycelium spheres.
Dry weight measurement by hypha dry weight method: and (4) filtering the mycelium pellets obtained in the step (3) by using single-layer filter cloth, weighing a clean flat plate, flatly paving the filtered mycelium pellets on the flat plate, drying the mycelium pellets in a 65-DEG C oven, weighing again, and storing the filtered bacterial liquid in a refrigerator for later use, wherein the weight of the filtered mycelium pellets is subtracted from the total weight of the mycelium pellets to obtain the dry weight of the mycelium.
Example 6: preparation of mycelium ball by liquid fermentation of hericium erinaceus
(1) Activation of mother strain: cutting Hericium Erinaceus slant strain in refrigerator under aseptic environment to obtain 0.5cm × 0.5cm block, inoculating on activating culture medium, and culturing in constant temperature box at 26 deg.C for 12-14 days to obtain first-stage strain. The mass contents of the components in the activation medium are as follows: glucose 2%, bran water 10%, peptone 0.4%, yeast extract 0.3%, agar 2%, potassium dihydrogen phosphate 0.1%, magnesium sulfate 0.05%, vitamin B10.001%, and water in balance, wherein the bran water is prepared by adding about 500ml pure water into 100g of crude bran, boiling, keeping the temperature for 30min, and filtering on four layers of gauze.
(2) Sterilization of liquid fermentation medium: preparing a liquid fermentation culture medium, wherein the components of the liquid fermentation culture medium comprise, by weight, 3% of glucose, 2% of soluble starch, 1% of yeast extract, 0.1% of monopotassium phosphate, 0.06% of magnesium sulfate heptahydrate and the balance of pure water, and the pH value of the liquid fermentation culture medium is 5.5. Placing the liquid fermentation culture medium into a 250mL triangular flask according to the amount of 100mL, placing the triangular flask into a sterilizing pot at 115 ℃, preserving the temperature for 20min for sterilization, and placing the sterilized liquid fermentation culture medium into a 65 ℃ oven for drying.
(3) Liquid fermentation of edible fungi: and (3) cutting off the primary strain obtained in the step (1) by 0.5cm x 0.5cm, inoculating the cut primary strain into the liquid fermentation medium obtained in the step (2), inoculating 3 fungus blocks into each bottle under an aseptic condition, and culturing on a shaking table at 29 ℃ for 10 days at 210r/min to form mycelium spheres, thereby obtaining the fermentation liquid containing the mycelium spheres.
Dry weight measurement by hypha dry weight method: and (4) filtering the mycelium pellets obtained in the step (3) by using single-layer filter cloth, weighing a clean flat plate, flatly paving the filtered mycelium pellets on the flat plate, drying the mycelium pellets in a 65-DEG C oven, weighing again, and storing the filtered bacterial liquid in a refrigerator for later use, wherein the weight of the filtered mycelium pellets is subtracted from the total weight of the mycelium pellets to obtain the dry weight of the mycelium.
Examples 7 to 9 are the preparation of triterpene from Hericium erinaceum, and the mycelium pellet used was the mycelium pellet prepared in example 2
In the following examples, the triterpene content was determined by uv spectrophotometry, specifically: firstly, preparing a triterpene standard oleanolic acid into an oleanolic acid solution with the concentration of 0.2mg/ml (0.2mg oleanolic acid is dissolved in 1ml methanol solution), respectively sucking 0,0.1,0.2,0.3,0.4,0.5ml and 25ml colorimetric tubes, evaporating a solvent in boiling water bath, adding 0.5ml vanillin-glacial acetic acid solution with the concentration of 50g/L (50g vanillin is dissolved in 1L glacial acetic acid solution) and 1ml perchloric acid solution, mixing, carrying out water bath at 60 ℃ for 20min, cooling with cold water for 15min, and then adding 3ml glacial acetic acid. Reacting at room temperature for 10min, and measuring absorbance at 547nm, and making standard curve with oleanolic acid quality as abscissa and absorbance as ordinate. And adding corresponding reagents into the triterpene extracting solution extracted in each embodiment according to the method, measuring under the same condition, substituting into a standard curve, and calculating the content of the hericium erinaceus triterpene.
Example 7: ultrasonic-assisted extraction of triterpenes from ethanol
Grinding the dried mycelium pellet (figure 4), dissolving with 40% ethanol, and extracting the dissolved solution in an ultrasonic cleaning instrument at 40khz under the condition of ultrasonic frequency of 40khz and temperature of 40 deg.C, wherein the ratio of mycelium pellet to ethanol is 1g:10 ml. Then centrifuging the extractive solution at 4000r/min for 10min, and collecting supernatant, which is triterpene extractive solution (FIG. 5).
Example 8: ultrasonic-assisted extraction of triterpenes from ethanol
Grinding the dried mycelium pellet, dissolving with 60% ethanol, and extracting the dissolved solution in an ultrasonic cleaning instrument at ultrasonic frequency of 40khz and temperature of 60 deg.C for 30min, wherein the ratio of mycelium pellet to ethanol is 1g:15 ml. And then centrifuging the extracting solution on a centrifuge at the rotating speed of 4000r/min for 10min, and collecting supernatant, wherein the supernatant is the triterpene extracting solution.
Example 9: ultrasonic-assisted extraction of triterpenes from ethanol
Grinding the dried mycelium pellets, dissolving the mycelium pellets in 80% ethanol, and extracting the dissolved solution on an ultrasonic cleaning instrument for 30min at the ultrasonic frequency of 40khz and the temperature of 80 ℃ with the ratio of the mycelium pellets to the ethanol being 1g to 30 ml. And then centrifuging the extracting solution on a centrifuge at the rotating speed of 4000r/min for 10min, and collecting supernatant, wherein the supernatant is the triterpene extracting solution.
The results of the above examples are shown in tables 1 to 3.
Table 1: hericium erinaceus liquid fermentation result (external fermentation conditions are consistent)
Table 2: hericium erinaceus liquid fermentation result (culture medium with consistent content of components)
Table 3: preparation of triterpene as metabolite of Hericium erinaceus
Triterpene yield (mg/L fermentation liquor) | Triterpene yield (%) | |
Example 7 | 21.27 | 0.19 |
Example 8 | 31.36 | 0.28 |
Example 9 | 33.57 | 0.30 |
As can be seen from Table 1, when the medium components were glucose 3%, soluble starch 2%, yeast extract 1%, potassium dihydrogen phosphate 0.1%, magnesium sulfate heptahydrate 0.06%, and pure water in balance (example 2), the growth rate of Hericium erinaceus was the fastest; when the nutrient content was further increased (example 3), the effect on the growth of Hericium erinaceum was not large, probably because the glucose effect was produced due to the excessively high glucose content.
As can be seen from Table 2, the fermentation conditions were that the pH of the fermentation medium was 5.5, the temperature of shake cultivation was 27 ℃ and the rotation speed was 180r/min (example 5), the liquid fermentation of Hericium erinaceus was the best, the mycelia grew the fastest, the dry weight of mycelia was also the greatest, and the change in external conditions had a great influence on the growth of Hericium erinaceus.
Therefore, it can be concluded that the liquid fermentation medium comprises, by weight, 3% of glucose, 2% of soluble starch, 1% of yeast extract, 0.1% of potassium dihydrogen phosphate, 0.06% of magnesium sulfate heptahydrate, and the balance of pure water, wherein the fermentation conditions are that the initial pH is 5.5, the fermentation temperature is 27 ℃, the rotation speed of a shaking table is 180r/min, the liquid fermentation is most suitable for the liquid fermentation of hericium erinaceus, and the dry weight of mycelia is maximum.
As can be seen from Table 3, the yield of triterpene varied from triterpene extraction condition to triterpene extraction condition. When the ethanol concentration is 80%, the feed-liquid ratio of the hericium erinaceus mycelium pellets to the ethanol is 1:30g/ml, and the extraction temperature is 80 ℃ (example 9), the triterpene yield is highest and the yield is also highest.
In conclusion, the invention utilizes glucose and soluble starch as composite carbon sources, thus eliminating the glucose effect, increasing the nutrition of the liquid fermentation liquor and increasing the growth speed of the hericium erinaceus; the yeast extract is used as a nitrogen source, is rich in nutrition, is rich in essential amino acids, nucleotides, trace elements and the like required by the growth of the hericium erinaceus, and can greatly accelerate the growth of the hericium erinaceus. In addition, the content of each component of the culture medium is optimized, and the condition most suitable for liquid fermentation of the hericium erinaceus is found; experiments prove that for liquid fermentation of hericium erinaceus, the temperature is controlled to be 25-29 ℃, and the growth speed of mycelia is high; experiments prove that for liquid fermentation of hericium erinaceus, the pH is controlled to be 5.0-6.0, and the growth speed of mycelia is high; according to the experimental verification, the rotation speed of the shaking table is 150-210r/min, and the mycelium grows fastest.
The present invention provides a method and a medium for liquid fermentation of hericium erinaceus and a method for preparing triterpenes, and a method and a means for implementing the method and the means are numerous, and the above description is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, many modifications and embellishments can be made without departing from the principle of the present invention, and these modifications and embellishments should be regarded as the protection scope of the present invention. All the components not specified in the present embodiment can be realized by the prior art.
Claims (10)
1. The hericium erinaceus liquid fermentation culture medium is characterized by comprising the following components in percentage by mass: 2 to 4 percent of glucose, 1 to 3 percent of soluble starch, 0.5 to 1.5 percent of yeast extract, 0.05 to 0.15 percent of monopotassium phosphate, 0.04 to 0.1 percent of magnesium sulfate heptahydrate and the balance of water.
2. The hericium erinaceus liquid fermentation culture medium according to claim 1, characterized by comprising the following components in percentage by mass: 3% of glucose, 2% of soluble starch, 1% of yeast extract, 0.1% of monopotassium phosphate, 0.06% of magnesium sulfate heptahydrate and the balance of water.
3. A method for producing mycelium spheres by fermentation of hericium erinaceus is characterized in that a strain obtained by activating the hericium erinaceus is inoculated into the liquid fermentation medium according to claim 1 or 2 and fermented to obtain the hericium erinaceus mycelium spheres.
4. The method according to claim 3, wherein the activation medium in the activation comprises the following components in percentage by weight: 2% of glucose, 10% of bran water, 0.4% of peptone, 0.3% of yeast extract, 2% of agar, 0.1% of potassium dihydrogen phosphate, 0.05% of magnesium sulfate and vitamin B 1 0.001% and the balance of water.
5. The method as claimed in claim 4, wherein said bran water is prepared as follows: adding the crude bran into water with the dosage of 80-120g/500mL, boiling, preserving the heat for 10-50min, and filtering by using one-seven layers of gauze to obtain filtrate, namely bran water.
6. The method of claim 3, wherein the bacterial species is selected from the group consisting of 0.2-0.8 x 0.2-0.8 3 And/piece 1-5 pieces/100 mL, inoculating into liquid fermentation medium.
7. The method as claimed in claim 3, wherein the initial pH of the fermentation is 5.0-6.0, the fermentation temperature is 25-29 ℃, and the rotation speed of the rocking platform during the fermentation is 150-210 r/min.
8. The method of claim 3, wherein the initial pH of the fermentation is 5.5, the temperature of the fermentation is 27 ℃, and the rotation speed of the rocking platform during the fermentation is 180 r/min.
9. A method for preparing triterpene from Hericium erinaceus is characterized in that mycelium spheres prepared by the method of any one of claims 3 to 6 are dissolved in ethanol solution, ultrasonic extraction and centrifugation are carried out, and the obtained supernatant is an extracting solution containing triterpene from Hericium erinaceus.
10. The method according to claim 9, wherein the volume concentration of ethanol in the ethanol solution is 40-80%; the feed-liquid ratio of the mycelium spheres to the ethanol aqueous solution is 1g:15-30 mL; the temperature of ultrasonic extraction is 40-80 ℃.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210805087.4A CN115074256B (en) | 2022-07-08 | 2022-07-08 | Hericium erinaceus liquid fermentation medium and method for preparing triterpenes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210805087.4A CN115074256B (en) | 2022-07-08 | 2022-07-08 | Hericium erinaceus liquid fermentation medium and method for preparing triterpenes |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115074256A true CN115074256A (en) | 2022-09-20 |
CN115074256B CN115074256B (en) | 2024-06-18 |
Family
ID=83258522
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210805087.4A Active CN115074256B (en) | 2022-07-08 | 2022-07-08 | Hericium erinaceus liquid fermentation medium and method for preparing triterpenes |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115074256B (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101971762A (en) * | 2010-02-09 | 2011-02-16 | 中国农业科学院农业资源与农业区划研究所 | Liquid submerged fermentation culture method for hericium erinaceus |
CN104082037A (en) * | 2014-07-10 | 2014-10-08 | 乳山市华隆生物科技有限公司 | Method for postprocessing of hericium erinaceus fermentation mycelium solution and preparing mycelium powder through biological enzyme |
WO2015024190A1 (en) * | 2013-08-20 | 2015-02-26 | 深圳市仁泰生物科技有限公司 | Antrodia camphorata strain with high yield of triterpenoid and application thereof |
-
2022
- 2022-07-08 CN CN202210805087.4A patent/CN115074256B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101971762A (en) * | 2010-02-09 | 2011-02-16 | 中国农业科学院农业资源与农业区划研究所 | Liquid submerged fermentation culture method for hericium erinaceus |
WO2015024190A1 (en) * | 2013-08-20 | 2015-02-26 | 深圳市仁泰生物科技有限公司 | Antrodia camphorata strain with high yield of triterpenoid and application thereof |
CN104082037A (en) * | 2014-07-10 | 2014-10-08 | 乳山市华隆生物科技有限公司 | Method for postprocessing of hericium erinaceus fermentation mycelium solution and preparing mycelium powder through biological enzyme |
Non-Patent Citations (1)
Title |
---|
李英迪等: "猴头菇三萜提取工艺优化及其抗氧化活性分析", 食品工业科技 * |
Also Published As
Publication number | Publication date |
---|---|
CN115074256B (en) | 2024-06-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101671615B (en) | Preparation method of compound Daqu | |
CN1033358C (en) | Prodn of nutriment from "Xianggu mushroom | |
CN107022493B (en) | Aspergillus oryzae strain for high-yield feeding compound enzyme and application thereof | |
CN107319535B (en) | Health food rich in spirulina kinase and preparation method thereof | |
CN106916861B (en) | Method for simultaneously producing auricularia auricula polysaccharide and melanin | |
CN102816806B (en) | Production method of grifolan selenium compound | |
CN107156638B (en) | Preparation method of lipid-lowering red yeast powder | |
CN106520584A (en) | Culture medium for saccharomycetes and lactic acid bacteria co-culture and preparation method of culture medium | |
CN108934785B (en) | Liquid strain culture method and cultivation method of boletus nigricans | |
CN113498834A (en) | Integrated fermentation method of edible and medicinal fungus fermented beverage | |
CN110916177A (en) | Method for preparing kelp enzyme by enzyme fermentation coupling technology | |
CN109295146A (en) | Enzyme process abalone enzymatic extract and preparation method thereof | |
CN102268467A (en) | Polysaccharide extract of Lactarius deliciosus hypha and application thereof | |
CN105559068B (en) | It is a kind of to utilize composition for eating the acquisition of medicine fungi fermentation radix tetrastigme and preparation method thereof | |
CN115029251A (en) | Liquid culture medium for preparing tricholoma matsutake stock seeds in high-altitude areas and stock seed preparation method | |
CN103864504A (en) | Solid fermentation matrix for culturing edible and medicinal fungus, and preparation method and application thereof | |
CN101731101B (en) | Method for culturing common phellinus fungus by using high yield selenium rich hybrid red rice fermentation dregs | |
WO2020134688A1 (en) | Method for preparing high-purity hericium erinaceus polysaccharide by fermenting hericium erinaceus, and fermentation medium thereof | |
CN115074256B (en) | Hericium erinaceus liquid fermentation medium and method for preparing triterpenes | |
CN115385980A (en) | Porphyra haitanensis pancreatic lipase inhibitory peptide and preparation method and application thereof | |
CN105535035B (en) | A kind of Inonotus obliquus fermented and cultured composition and preparation method thereof | |
CN109076881B (en) | Culture method and application of selenium-rich hericium erinaceus mycelium | |
CN115039633A (en) | Artificial culture method for sporocarp of Isaria japonica | |
CN110592161A (en) | Preparation method of polysaccharide, health-care oral liquid and preparation method | |
CN101134940B (en) | Fermentation production method for Chinese caterpillar fungus fungus-bat moth hirsutella sinensis |
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 | ||
GR01 | Patent grant |