CN104473175A - Antrodia fermented product and preparation method thereof - Google Patents
Antrodia fermented product and preparation method thereof Download PDFInfo
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- CN104473175A CN104473175A CN201510025535.9A CN201510025535A CN104473175A CN 104473175 A CN104473175 A CN 104473175A CN 201510025535 A CN201510025535 A CN 201510025535A CN 104473175 A CN104473175 A CN 104473175A
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- zymotic fluid
- fermentation
- lactobacillus
- preparation
- peptide
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- 238000002360 preparation method Methods 0.000 title claims abstract description 21
- 241000123370 Antrodia Species 0.000 title abstract 5
- 238000004519 manufacturing process Methods 0.000 title description 4
- 238000000855 fermentation Methods 0.000 claims abstract description 74
- 230000004151 fermentation Effects 0.000 claims abstract description 74
- 239000007788 liquid Substances 0.000 claims abstract description 68
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- 150000001875 compounds Chemical class 0.000 claims abstract description 23
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- 239000000306 component Substances 0.000 claims abstract description 20
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 claims abstract description 20
- 241000192130 Leuconostoc mesenteroides Species 0.000 claims abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000004310 lactic acid Substances 0.000 claims abstract description 10
- 235000014655 lactic acid Nutrition 0.000 claims abstract description 10
- 230000001954 sterilising effect Effects 0.000 claims abstract description 8
- 239000012530 fluid Substances 0.000 claims description 76
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 64
- 241001486992 Taiwanofungus camphoratus Species 0.000 claims description 56
- 239000000047 product Substances 0.000 claims description 53
- 108090000765 processed proteins & peptides Proteins 0.000 claims description 52
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 claims description 45
- 239000002002 slurry Substances 0.000 claims description 42
- 241000186660 Lactobacillus Species 0.000 claims description 20
- 229940039696 lactobacillus Drugs 0.000 claims description 20
- 241000194020 Streptococcus thermophilus Species 0.000 claims description 19
- 241000186673 Lactobacillus delbrueckii Species 0.000 claims description 18
- 238000002156 mixing Methods 0.000 claims description 14
- 239000006228 supernatant Substances 0.000 claims description 14
- 235000019990 fruit wine Nutrition 0.000 claims description 13
- 150000003839 salts Chemical class 0.000 claims description 12
- 238000012545 processing Methods 0.000 claims description 11
- 239000012533 medium component Substances 0.000 claims description 10
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- 235000013956 Lactobacillus acidophilus Nutrition 0.000 claims description 9
- 244000199866 Lactobacillus casei Species 0.000 claims description 9
- 235000013958 Lactobacillus casei Nutrition 0.000 claims description 9
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- 238000000605 extraction Methods 0.000 claims description 9
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- NWGKJDSIEKMTRX-AAZCQSIUSA-N Sorbitan monooleate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O NWGKJDSIEKMTRX-AAZCQSIUSA-N 0.000 description 3
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- CHHHXKFHOYLYRE-UHFFFAOYSA-M 2,4-Hexadienoic acid, potassium salt (1:1), (2E,4E)- Chemical compound [K+].CC=CC=CC([O-])=O CHHHXKFHOYLYRE-UHFFFAOYSA-M 0.000 description 1
- XDFNWJDGWJVGGN-UHFFFAOYSA-N 2-(2,7-dichloro-3,6-dihydroxy-9h-xanthen-9-yl)benzoic acid Chemical compound OC(=O)C1=CC=CC=C1C1C2=CC(Cl)=C(O)C=C2OC2=CC(O)=C(Cl)C=C21 XDFNWJDGWJVGGN-UHFFFAOYSA-N 0.000 description 1
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- 108010011485 Aspartame Proteins 0.000 description 1
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- 241000233866 Fungi Species 0.000 description 1
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- 239000008101 lactose Substances 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 210000004698 lymphocyte Anatomy 0.000 description 1
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- 239000001814 pectin Substances 0.000 description 1
- 229920001277 pectin Polymers 0.000 description 1
- 235000010987 pectin Nutrition 0.000 description 1
- 229940049954 penicillin Drugs 0.000 description 1
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- 235000010241 potassium sorbate Nutrition 0.000 description 1
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- IZTQOLKUZKXIRV-YRVFCXMDSA-N sincalide Chemical compound C([C@@H](C(=O)N[C@@H](CCSC)C(=O)NCC(=O)N[C@@H](CC=1C2=CC=CC=C2NC=1)C(=O)N[C@@H](CCSC)C(=O)N[C@@H](CC(O)=O)C(=O)N[C@@H](CC=1C=CC=CC=1)C(N)=O)NC(=O)[C@@H](N)CC(O)=O)C1=CC=C(OS(O)(=O)=O)C=C1 IZTQOLKUZKXIRV-YRVFCXMDSA-N 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000001632 sodium acetate Substances 0.000 description 1
- 235000010378 sodium ascorbate Nutrition 0.000 description 1
- PPASLZSBLFJQEF-RKJRWTFHSA-M sodium ascorbate Substances [Na+].OC[C@@H](O)[C@H]1OC(=O)C(O)=C1[O-] PPASLZSBLFJQEF-RKJRWTFHSA-M 0.000 description 1
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- PPASLZSBLFJQEF-RXSVEWSESA-M sodium-L-ascorbate Chemical compound [Na+].OC[C@H](O)[C@H]1OC(=O)C(O)=C1[O-] PPASLZSBLFJQEF-RXSVEWSESA-M 0.000 description 1
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Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
- A23L2/70—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter
- A23L2/84—Clarifying or fining of non-alcoholic beverages; Removing unwanted matter using microorganisms or biological material, e.g. enzymes
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Landscapes
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Molecular Biology (AREA)
- Zoology (AREA)
- Nutrition Science (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Medicines Containing Material From Animals Or Micro-Organisms (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
The invention provides an Antrodia fermented product and a preparation method thereof. The preparation method comprises the following steps that (1) Antrodia is soaked in water, extracted, crushed and subjected to mashing, and mash is obtained; (2) after culture medium components are added into the mash, leuconostoc mesenteroides are added to carry out first fermentation, and first fermentation liquor is obtained; (3) pectinase is added into fruit and vegetable liquid with the pH value being 4.5-6 to carry out enzymolysis, and zymolytic fruit and vegetable liquid is obtained; (4) after culture medium components are added into the zymolytic fruit and vegetable liquid, compound lactic acid bacteria are added to carry out second fermentation, and second fermentation liquor is obtained; (5) after culture medium components are added into the second fermentation liquor, compound microzyme is added to carry out third fermentation, and third fermentation liquor is obtained; (6) the first fermentation liquor and the third fermentation liquor are evenly mixed and then centrifuged, and the Antrodia fermented product is obtained after homogenization and sterilization are carried out on centrifuged supernate. The Antrodia fermented product is good in taste and unique in flavor, has good immune adjustment and oxidation resistance functions, and is suitable for the crowd.
Description
Technical field
The present invention relates to a kind of fermented product, particularly relate to a kind of Antrodia camphorata fermented product and preparation method thereof.
Background technology
Antrodia camphorata has another name called Cinnamomum kanahirai hay mushroom, belongs to Aphyllophorales class, is the new species just delivered by biochemical boundary nineteen ninety.Its growth district is between the height above sea level 450-2000 rice mountain forest of mountain area, Taiwan, is the distinctive fungi in Taiwan, and only growth is on the distinctive Cinnamomum kanahirai hay tree in Taiwan, so very precious.The polysaccharides wherein contained, terpenoid, super oxygen disproportionation ferment and nucleic acid material can anticancer, reinforced immunological, antiallergy, anti-oxidant reducing blood lipid, there is high medical value.General instructions of taking is the infusion or with alcohol-pickled of adding water, bitter.
Though Antrodia camphorata is rich in various active composition, but due to the mushroom structure of matter fine and close, and mouthfeel is pained, therefore how to make human body at utmost absorb active component wherein, and making its mouthfeel obtain liking of eater, is the major issue carrying out required for present stage studying.At present, a small amount of relevant report Antrodia camphorata being processed into beverage is had.Such as, notification number be CN103750455A patent discloses a kind of health drink containing Antrodia camphorata, it interpolation sodium ascorbate Antrodia camphorata and water is heated to obtain extract and remaining Antrodia camphorata slag, beverage is made with HFCS, thickener/emulsifier, food acids, essence, Aspartame, potassium sorbate, drinking water, this beverage has certain effect that sterilization solution swells, stagnation resolvation is invigorated blood circulation, also compensate for the pained mouthfeel of Antrodia camphorata, but the effective ingredient that still can not thoroughly discharge in Antrodia camphorata, and additive is too much.
Publication number is the extracting process that patent discloses a kind of Antrodia camphorata active ingredient of CN103923743A, by Antrodia camphorata accelerated freeze-drying to moisture content lower than 2%, pulverize, 35 DEG C, 25Mpa time carry out supercritical carbon dioxide extracting, finally high-pressure rectification is adopted to obtain Antrodia camphorata oil again, its extraction yield improves relative to water infusion, but mouthfeel still puckery hardship, and this extract is oily simultaneously, not only take inconvenience, and composition is single, health care is limited.
Summary of the invention
The invention provides a kind of Antrodia camphorata fermented product and preparation method thereof, taking the technological deficiencies such as inconvenience, composition is single, palatability is poor, health care is limited for solving Antrodia camphorata series products of the prior art.
The invention provides a kind of preparation method of Antrodia camphorata fermented product, comprise the steps:
1) be soaked in water by Antrodia camphorata and extract, crushing and beating, gets slurries;
2), after adding medium component in described slurries, access Leuconostoc mesenteroides carries out the first fermentation, when the pH value of zymotic fluid reduces by more than 0.5, and the content of reducing sugar of zymotic fluid lower than 1.5% time terminate described first fermentation, obtained first zymotic fluid;
3) to pH value be 4.5 ~ 6 fruits and vegetables liquid in add pectase and carry out enzymolysis processing, obtained enzymolysis fruits and vegetables liquid;
4) after adding medium component in described enzymolysis fruits and vegetables liquid, access compound lactobacillus carries out the second fermentation, terminates described second fermentation, obtained second zymotic fluid when the pH value of zymotic fluid reduces by more than 0.5; Wherein, described compound lactobacillus is selected from more than four kinds in streptococcus thermophilus, Lactobacillus delbrueckii, lactobacillus acidophilus, Lactobacillus casei, Lactobacillus plantarum, lactobacillus fermenti, Lactobacillus rhamnosus, Lactobacillus pentosus, Lactococcus garvieae, Lactobacillus helveticus, Pediococcus acidilactici;
5), after adding medium component in described second zymotic fluid, access mulriple yeasts carries out the 3rd fermentation, when zymotic fluid total sugar content lower than 2% time terminate described 3rd fermentation, obtained 3rd zymotic fluid; Wherein, what described mulriple yeasts was selected from rice wine yeast, saccharomyces sake, brewer's yeast, white wine yeast and fruit wine and wine yeast is two or more;
6) by centrifugal after described first zymotic fluid and described 3rd zymotic fluid mixing, after centrifuged supernatant homogeneous, sterilizing, obtained Antrodia camphorata fermented product.
In the preparation process in accordance with the present invention, described Leuconostoc mesenteroides can select Leuconostoc mesenteroides dextran subspecies (L.mesenteroides subsp.dextranicum) or leuconostoc mesenteroides sub species cremoris (L.mesenteroides subsp.cremoris), and each bacterium of the present invention can adopt the mode of bacterium powder or bacterium liquid to use.When adopting bacterium powder, the viable count of described each lactic acid bacteria bacterium powder can be 10
9about CFU/g, the viable count of each saccharomycete bacterium powder can be 10
10about CFU/g.In addition, the inoculum concentration of described Leuconostoc mesenteroides (bacterium powder) can be 0.05 ~ 0.2%, such as 0.1%, the inoculum concentration of described compound lactobacillus (bacterium powder) can be 0.05 ~ 0.2%, such as 0.1%, the inoculum concentration of described mulriple yeasts (bacterium powder) can be 0.01 ~ 0.02%; When adopting bacterium liquid, the viable count and the inoculum concentration that can refer to above-mentioned bacterium powder are inoculated.Each bacterial strain conventionally can activate according to needs before use.
The present invention does not make considered critical to described Antrodia camphorata, and it can be fresh Antrodia camphorata, also can be dry Antrodia camphorata.In concrete scheme of the present invention, fresh Antrodia camphorata can be adopted as raw material, its moisture content is 50 ~ 60%.Further, the quality proportioning controlling described Antrodia camphorata and described water is 1:15 ~ 25, and described extraction temperature is 85 ~ 95 DEG C, and the time of described extraction is 20 ~ 60min, and described Antrodia camphorata is crushed to 40 ~ 80 orders.The pH of the slurries obtained by described Antrodia camphorata crushing and beating is 4.5 ~ 6.Extraction process can make the active component in Antrodia camphorata raw material discharge more effectively, thus further increases raw material availability.
In the present invention, described medium component can comprise carbon source, nitrogenous source, inorganic salts, trace element etc., and those skilled in the art can select according to the concrete bacterial strain cultivated or compound bacteria the medium component that is suitable for.In concrete scheme of the present invention, described medium component comprise in sugar, peptide, inorganic salts and surfactant one or more, in wherein said peptide, mean molecule quantity is less than gross mass content >=80% of the component of 1000Da.
Namely, the present invention additionally provides a kind of fluid nutrient medium for Leuconostoc mesenteroides fermentation on the other hand, it comprises Antrodia camphorata slurries, sugar, peptide, inorganic salts and surfactant, wherein the mass content of sugar in described slurries can be 5 ~ 10%, the mass content of peptide in described slurries can be 0.3 ~ 0.8%, the mass content of inorganic salts in described slurries can be 0.1 ~ 0.3%, and the mass content of surfactant in described slurries can be 0.01 ~ 0.1%; These Antrodia camphorata slurries are obtained by Antrodia camphorata and water being extracted, after crushing and beating.
Again on the one hand, present invention also offers a kind of fluid nutrient medium fermented for compound lactobacillus and/or mulriple yeasts, it comprises enzymolysis fruits and vegetables liquid, sugar, peptide, inorganic salts and surfactant, wherein the mass content of sugar in described enzymolysis fruits and vegetables liquid can be 5 ~ 10%, the mass content of peptide in described enzymolysis fruits and vegetables liquid can be 0.3 ~ 0.8%, the mass content of inorganic salts in described enzymolysis fruits and vegetables liquid can be 0.1 ~ 0.3%, and the mass content of surfactant in described enzymolysis fruits and vegetables liquid can be 0.01 ~ 0.1%; This enzymolysis fruits and vegetables liquid by pH value be 4.5 ~ 6 fruits and vegetables liquid in add pectinase enzymatic hydrolysis obtain.
Further, described sugar can be selected from glucose, sucrose, lactose and maltose one or more, such as sucrose; Described inorganic salts can be selected from sodium salt, calcium salt, manganese salt, sylvite and magnesium salts one or more, such as calcium carbonate; Described surfactant can be selected from the smooth and polysorbate of fatty glyceride, aliphatic acid sorb one or more, such as Arlacel-80 etc.Particularly, the component of peptide described in the present invention is not particularly limited, as long as wherein mean molecule quantity is less than gross mass content >=80% of the component of 1000Da, further >=90%, adopts described peptide significantly can promote the growth of Leuconostoc mesenteroides and compound lactobacillus and mulriple yeasts as nitrogenous source.
The step 2 of concrete scheme of the present invention) in, sugar, peptide and inorganic salts are added to described slurries kind, the mass content of described sugar in described slurries is made to be 5 ~ 10%, the mass content of described peptide in described slurries is 0.3 ~ 0.8%, the mass content of described inorganic salts in described slurries is 0.1 ~ 0.3%, and the temperature controlling described first fermentation is 22 ~ 28 DEG C, and rotating speed is 80 ~ 120r/min.Under this condition Leuconostoc mesenteroides is fermented, the mouthfeel of product can be improved and promote the performance of product health care.In addition, the pH value controlling this zymotic fluid reduces by more than 0.5 (pH value of such as zymotic fluid is 4.5 ~ 5), and the content of reducing sugar of zymotic fluid is lower than 1.5%, not only be conducive to avoiding product tart flavour overweight and affecting palatability, and low content of reducing sugar can make product have applicability more widely, particularly can drink by diabetic.
In the present invention, described fruits and vegetables liquid is the slurries, juice etc. made through fruit and/or fruits and vegetables, such as, can adopt commercial Juice etc., particularly preferably not containing the fruit and vegetable juice of the additives such as any anticorrisive agent.Further, after fruit and vegetable materials can also be chosen, be crushed to 40 ~ 80 orders, such as 60 orders, obtained described fruits and vegetables liquid; This particle size range both can improve the speed of fermentation, also helped the mouthfeel ensureing fermented product.In addition, the present invention does not do strict restriction to the kind of fruit and vegetable materials, particularly can choose locality and abound with and/or be convenient to the fruits and vegetables of processing as raw material, such as banana, mango, pawpaw, mangosteen, dragon fruit, carrot, cucumber, tomato etc.; And, when choosing fruit and vegetable materials, can carry out reasonably combined for the characteristic of raw material itself (such as pH value), and make the fruits and vegetables liquid pH value made in the scope of 4.5 ~ 6, thus without the need to add other pH adjusting agent to regulate the pH value of fruits and vegetables liquid, to ensure the genuineness of product.
Pectase of the present invention can by common commercial acquisition.In described fruits and vegetables liquid, add pectase be mainly used in decompose pectin etc., thus make the nutritional labeling of fruit and vegetable materials discharge more thorough, to improve raw material availability.Further, the consumption of described pectase is every gram of fruits and vegetables liquid 2 ~ 3 unit, and the temperature controlling described enzymolysis processing is 40 ~ 50 DEG C, and the time is 2 ~ 3h.
Step 4 of the present invention) in, in described enzymolysis fruits and vegetables liquid, add sugar and peptide, make the mass content of described sugar in described enzymolysis fruits and vegetables liquid be 3 ~ 5%, the mass content of described peptide in described enzymolysis fruits and vegetables liquid is 0.3 ~ 0.8%; Described compound lactobacillus at least comprises streptococcus thermophilus and Lactobacillus delbrueckii, the weight proportion of described streptococcus thermophilus, Lactobacillus delbrueckii and all the other lactic acid bacterias is 3:2:(2 ~ 5), and the temperature controlling described second fermentation is 18 ~ 23 DEG C, and rotating speed is 80 ~ 120r/min.
Further, all the other lactic acid bacterias described can be one or more in following first to fourth component:
First component: comprise lactobacillus acidophilus and Lactobacillus rhamnosus, and the weight proportion of lactobacillus acidophilus and Lactobacillus rhamnosus is (0.5 ~ 1.5): (0.5 ~ 1.5);
Second component: comprise Pediococcus acidilactici, lactobacillus fermenti and Lactobacillus pentosus, and the weight proportion of Pediococcus acidilactici, lactobacillus fermenti and Lactobacillus pentosus is (0.5 ~ 1.5): (0.5 ~ 1.5): (0.5 ~ 1);
Three components: comprise Lactobacillus casei and Lactobacillus plantarum, and the weight proportion of Lactobacillus casei and Lactobacillus plantarum is (0.5 ~ 1): (0.5 ~ 1);
Four composition: comprise Lactococcus garvieae and Lactobacillus helveticus, and the weight proportion between Lactococcus garvieae and Lactobacillus helveticus is (0.5 ~ 1): (0.5 ~ 1).
Step 5 of the present invention) in, in described second zymotic fluid, add sugar and peptide, make the mass content of described sugar in described second zymotic fluid be 4 ~ 8%, the mass content of described peptide in described second zymotic fluid is 0.3 ~ 0.8%; And the weight proportion controlled between two primary yeasts in described mulriple yeasts is 1:(0.8 ~ 1.2), the temperature of described 3rd fermentation is 16 ~ 20 DEG C, and rotating speed is 40 ~ 60r/min.Particularly, each saccharomycete in mulriple yeasts all adopts bacterium powder, when in composite yeast, each yeast weight is identical, the local flavor of fermented product is splendid.
Further, described mulriple yeasts can be selected from any one in following first to fourth component:
First component: comprise rice wine yeast and fruit wine and wine yeast, and rice wine yeast, weight proportion between fruit wine and wine yeast are 1:(0.8 ~ 1.2);
Second component: comprise saccharomyces sake and fruit wine and wine yeast, and saccharomyces sake, weight proportion between fruit wine and wine yeast are 1:(0.8 ~ 1.2);
Three components: comprise rice wine yeast, brewer's yeast and white wine yeast, and rice wine yeast, weight proportion between brewer's yeast and white wine yeast are 1:(0.8 ~ 1.2): (0.8 ~ 1.2);
Four composition: comprise brewer's yeast, white wine yeast and fruit wine and wine yeast, and brewer's yeast, white wine yeast and the weight proportion between fruit wine and wine yeast are 1:(0.8 ~ 1.2): (0.8 ~ 1.2).
Step 6 of the present invention) in, the weight proportion of described first zymotic fluid and described 3rd zymotic fluid is (4 ~ 6): (4 ~ 6).And, before described homogeneous, can optionally allocate centrifuged supernatant, such as can add appropriate sugar, peptide etc. to improve the mouthfeel of product, improve the health care etc. of product, the mass content of wherein said sugar in centrifuged supernatant can be 8 ~ 16%, and the mass content of described peptide in centrifuged supernatant can be 0.5 ~ 2%.
Further, described sugar can comprise white sugar and brown sugar, and described white sugar and the brown sugar quality proportioning in described sugar can be 1:0.5 ~ 2.In addition, described peptide can be collagen peptide, and in the former peptide of this peptide, mean molecule quantity is less than gross mass content >=80% of the component of 1000Da, further >=90%.
The present invention also provides a kind of Antrodia camphorata fermented product, obtains according to above-mentioned arbitrary described preparation method.
The enforcement of the present invention program, at least has following advantage:
1, the present invention adopts Leuconostoc mesenteroides to ferment to Antrodia camphorata slurries, not only more effectively releases activity and the nutritional labeling of Antrodia camphorata, improves the utilization rate of Antrodia camphorata, add the health care of zymotic fluid in addition; Meanwhile, the present invention adopts compound lactobacillus and mulriple yeasts to ferment to fruits and vegetables liquid successively, not only ensure that the comprehensive and balanced of the nutritional labeling in fermented product, improves the mouthfeel of fermented product in addition and improves the local flavor of fermented product.
2, the condition of the present invention to zymotechnique is optimized, and not only increases fermenting speed, shortens fermentation time, and the mouthfeel of fermented product, local flavor and immunological regulation and the function such as anti-oxidant are significantly improved in addition.
3, the Antrodia camphorata fermented product mouthfeel prepared of the present invention good, unique flavor, nutritional labeling general equilibrium, instant, this fermented product not containing any additive, green health; In addition, it also has good immunological regulation and the function such as anti-oxidant, is suitable for crowd in extensive range.
Accompanying drawing explanation
Fig. 1 is that the fermented product of the embodiment of the present invention and reference examples is to the evaluation result of the mouse T lymphocyte multiplication capacity that ConA induces;
Fig. 2 is that the fermented product of the embodiment of the present invention and reference examples is to the evaluation result of the mouse T lymphocyte multiplication capacity that LPS induces;
Fig. 3 is the anti-oxidation function evaluation result of the fermented product of the embodiment of the present invention and reference examples.
Detailed description of the invention
For making the object, technical solutions and advantages of the present invention clearly, below in conjunction with embodiments of the invention, the technical scheme in the embodiment of the present invention is clearly and completely described, obviously, described embodiment is the present invention's part embodiment, instead of whole embodiments.Based on the embodiment in the present invention, those of ordinary skill in the art, not making the every other embodiment obtained under creative work prerequisite, belong to the scope of protection of the invention.
Each lactic acid bacteria that various embodiments of the present invention adopt is all from Research for Industrial Microbial Germ preservation administrative center (CICC), each lactic acid bacteria is respectively: leuconostoc mesenteroides subsp mesenteroides (CICC 22181), streptococcus thermophilus (CICC 6220), Lactobacillus delbrueckii subsp. lactis (CICC 6077), lactobacillus acidophilus (CICC 6085), Lactobacillus casei (CICC 6114), Lactobacillus plantarum (CICC 22135), lactobacillus fermenti (CICC 22555), Lactobacillus rhamnosus (CICC 6155), Lactobacillus pentosus (CICC21810), Lactococcus garvieae (CICC 20393), Lactobacillus helveticus (CICC 22171), Pediococcus acidilactici (CICC 10346), the viable count of each lactic acid bacteria is about 10
9cFU/g,
Each saccharomycete is all from Angel Yeast Co., Ltd, and each saccharomycetic viable count is all about 10
10cFU/g;
Black-bone chicken peptide and collagen peptide, purchased from Beijing Zhongshi Haishi Biotechnology Co., Ltd., in two kinds of peptides, mean molecule quantity is less than the gross mass content of the component of 1000Da all >=80%;
Pectase: purchased from Pangbo Bioengineering Co Ltd, Nanning.
Embodiment 1
1, the first fermentation
By moisture content be 52% Antrodia camphorata be soaked in (namely solid-liquid ratio is 1:20) in water according to weight proportion 1:20,90 DEG C extraction about 30min after, crushing and beating to 60 order, obtained pH value is about the slurries of 5.5.
Sucrose is added in above-mentioned slurries, black-bone chicken peptide and calcium carbonate, the mass content of sucrose in slurries is made to be about 8%, the mass content of black-bone chicken peptide in slurries is about 0.5%, the mass content of calcium carbonate in slurries is about 0.18%, after stirring and evenly mixing, inoculum concentration according to about 0.1% accesses Leuconostoc mesenteroides and carries out the first fermentation in slurries, the temperature controlling the first fermentation is about 25 DEG C, speed of agitator is about 100r/min, when the pH value of zymotic fluid reduces by more than 0.5, and the content of reducing sugar of zymotic fluid lower than 1.5% time terminate the first fermentation, obtained first zymotic fluid (pH value is 4.7 ~ 5).
Adopt the cell concentration of spectrophotometry first zymotic fluid, the results are shown in Table 1.
2, enzymolysis processing
After fresh mango and carrot are 2:1 mixing according to weight proportion, be crushed to 60 orders, obtained pH value is about the fruits and vegetables liquid of 5.5;
In above-mentioned fruits and vegetables liquid, add pectase carry out enzymolysis processing, wherein the consumption of pectase is about every gram of fruits and vegetables liquid 2.5 unit, and the temperature of controlled enzymatic hydrolysis process is about 45 DEG C, and the time is about 3h, obtained enzymolysis fruits and vegetables liquid.
3, the second fermentation
Glucose and black-bone chicken peptide is added in described enzymolysis fruits and vegetables liquid, the mass content of glucose in enzymolysis fruits and vegetables liquid is made to be about 4%, the mass content of black-bone chicken peptide in enzymolysis fruits and vegetables liquid is about 0.5%, after stirring and evenly mixing, inoculum concentration according to about 0.1% accesses compound lactobacillus and carries out the second fermentation in enzymolysis fruits and vegetables liquid, compound lactobacillus is by streptococcus thermophilus, Lactobacillus delbrueckii, lactobacillus acidophilus and Lactobacillus rhamnosus composition, wherein streptococcus thermophilus, Lactobacillus delbrueckii, weight proportion between lactobacillus acidophilus and Lactobacillus rhamnosus is 3:2:1.5:1.5, and the temperature controlling the second fermentation is about 20 DEG C, speed of agitator is about 100r/min, the second fermentation is terminated when the pH value of zymotic fluid reduces by more than 0.5, obtained second zymotic fluid (pH value is 4.6 ~ 5).
4, the 3rd fermentation
Glucose and black-bone chicken peptide is added in above-mentioned second zymotic fluid, the mass content of glucose in the second zymotic fluid is made to be about 6%, the mass content of black-bone chicken peptide in the second zymotic fluid is about 0.5%, after stirring and evenly mixing, the 3rd fermentation is carried out according to the inoculum concentration access mulriple yeasts of about 0.01%, described mulriple yeasts is made up of rice wine yeast and fruit wine and wine yeast, wherein rice wine yeast and the weight proportion between fruit wine and wine yeast are 1:0.8, and the temperature controlling the 3rd fermentation is about 18 DEG C, speed of agitator is about 50r/min, when zymotic fluid total sugar content lower than 2% time terminate the 3rd fermentation, obtained 3rd zymotic fluid.
5, Antrodia camphorata fermented product is prepared
After above-mentioned first zymotic fluid and the 3rd zymotic fluid being mixed according to weight proportion 1:1, centrifugal about 15min under 4000r/min, carries out homogeneous, sterilizing to centrifuged supernatant, obtained Antrodia camphorata fermented product (pH value is 4.7 ~ 5).
50 experimenters making age level be distributed in 20 years old ~ 80 years old eat the Antrodia camphorata fermented product of above-mentioned preparation, and carry out mouthfeel and local flavor marking to this Antrodia camphorata fermented product respectively according to following standard:
Mouthfeel scoring criterion: full marks 10 points, wherein sweet taste and persistence length total score meter 3.5 points, tart flavour and persistence length total score meter 3.5 points, smooth degree total score meter 1.5 points, lingering taste total score meter 1.5 points in mouth;
Local flavor scoring criterion: full marks 10 points, its Raw peculiar fragrance total score meter 3 points, ferment peculiar fragrance total score meter 3 points, fragrance mixability total score meter 3 points, other assorted taste total score meters 1 point;
1 be the results are shown in Table to the average score of Antrodia camphorata fermented product.
Embodiment 2
1, the first fermentation
By moisture content be 50% Antrodia camphorata be soaked in (namely solid-liquid ratio is 1:15) in water according to weight proportion 1:15,85 DEG C extraction about 50min after, crushing and beating to 50 order, obtained pH value is about the slurries of 5.
Sucrose is added in above-mentioned slurries, black-bone chicken peptide and magnesium sulfate, the mass content of sucrose in slurries is made to be about 10%, the mass content of black-bone chicken peptide in slurries is about 0.3%, the mass content of magnesium sulfate in slurries is about 0.15%, after stirring and evenly mixing, inoculum concentration according to about 0.05% accesses Leuconostoc mesenteroides and carries out the first fermentation in slurries, the temperature controlling the first fermentation is about 22 DEG C, speed of agitator is about 90r/min, when the pH value of zymotic fluid reduces by more than 0.5, and the content of reducing sugar of zymotic fluid lower than 1.5% time terminate the first fermentation, obtained first zymotic fluid (pH value is 4.2 ~ 4.5), the cell concentration of the first zymotic fluid is in table 1.
2, enzymolysis processing
After fresh dragon fruit and mangosteen are 1:1 mixing according to weight proportion, be crushed to 40 orders, obtained pH value is about the fruits and vegetables liquid of 4.5;
In above-mentioned fruits and vegetables liquid, add pectase carry out enzymolysis processing, wherein the consumption of pectase is about every gram of fruits and vegetables liquid 2 unit, and the temperature of controlled enzymatic hydrolysis process is about 45 DEG C, and the time is about 2h, obtained enzymolysis fruits and vegetables liquid.
3, the second fermentation
Glucose and black-bone chicken peptide is added in described enzymolysis fruits and vegetables liquid, the mass content of glucose in enzymolysis fruits and vegetables liquid is made to be about 3%, the mass content of black-bone chicken peptide in enzymolysis fruits and vegetables liquid is about 0.4%, after stirring and evenly mixing, inoculum concentration according to about 0.15% accesses compound lactobacillus and carries out the second fermentation in enzymolysis fruits and vegetables liquid, compound lactobacillus is by streptococcus thermophilus, Lactobacillus delbrueckii, Pediococcus acidilactici, lactobacillus fermenti and Lactobacillus pentosus composition, wherein streptococcus thermophilus, Lactobacillus delbrueckii, Pediococcus acidilactici, weight proportion between lactobacillus fermenti and Lactobacillus pentosus is 3:2:0.5:0.5:1, and the temperature controlling the second fermentation is about 18 DEG C, speed of agitator is about 80r/min, the second fermentation is terminated when the pH value of zymotic fluid reduces by more than 0.5, obtained second zymotic fluid (pH value is 3.8 ~ 4).
4, the 3rd fermentation
Glucose and black-bone chicken peptide is added in above-mentioned second zymotic fluid, the mass content of glucose in the second zymotic fluid is made to be about 4%, the mass content of black-bone chicken peptide in the second zymotic fluid is about 0.8%, after stirring and evenly mixing, inoculum concentration according to about 0.02% carries out the 3rd fermentation to access mulriple yeasts, described mulriple yeasts is made up of saccharomyces sake and fruit wine and wine yeast, wherein female and between fruit wine and wine yeast the weight proportion of pure mellow wine is 1:0.9, and the temperature controlling the 3rd fermentation is about 20 DEG C, speed of agitator is about 40r/min, when zymotic fluid total sugar content lower than 2% time terminate the 3rd fermentation, obtained 3rd zymotic fluid.
5, Antrodia camphorata fermented product is prepared
It is centrifugal after above-mentioned first zymotic fluid and the 3rd zymotic fluid are mixed according to weight proportion 2:3, white sugar, brown sugar and collagen peptide is added in centrifuged supernatant, white sugar and the brown sugar mass content in centrifuged supernatant is made to be about 6%, the mass content of collagen peptide in centrifuged supernatant is about 1%, carry out homogeneous, sterilizing subsequently, obtained Antrodia camphorata fermented product (pH value is 3.8 ~ 4.3); The mouthfeel of this Antrodia camphorata fermented product and local flavor marking the results are shown in Table 1.
Embodiment 3
1, the first fermentation
By moisture content be 55% Antrodia camphorata be soaked in (namely solid-liquid ratio is 1:25) in water according to weight proportion 1:25,95 DEG C extraction about 20min after, crushing and beating to 80 order, obtained pH value is about the slurries of 5.5.
Sucrose is added in above-mentioned slurries, black-bone chicken peptide, potassium chloride and Arlacel-80, the mass content of sucrose in slurries is made to be about 5%, the mass content of black-bone chicken peptide in slurries is about 0.6%, the mass content of potassium chloride in slurries is about 0.3%, the mass content of Arlacel-80 in slurries is about 0.05%, after stirring and evenly mixing, inoculum concentration according to about 0.2% accesses Leuconostoc mesenteroides and carries out the first fermentation in slurries, the temperature controlling the first fermentation is about 25 DEG C, speed of agitator is about 110r/min, when the pH value of zymotic fluid reduces by more than 0.5, and the content of reducing sugar of zymotic fluid lower than 1.5% time terminate the first fermentation, obtained first zymotic fluid (pH value is 4.6 ~ 5), the cell concentration of the first zymotic fluid is in table 1.
2, enzymolysis processing
By fresh mango, pawpaw, cucumber according to weight proportion be 1:1:2 mixing after, be crushed to 70 orders, obtained pH value is about the fruits and vegetables liquid of 6;
In above-mentioned fruits and vegetables liquid, add pectase carry out enzymolysis processing, wherein the consumption of pectase is about every gram of fruits and vegetables liquid 3 unit, and the temperature of controlled enzymatic hydrolysis process is about 40 DEG C, and the time is about 3h, obtained enzymolysis fruits and vegetables liquid.
3, the second fermentation
Glucose and black-bone chicken peptide is added in described enzymolysis fruits and vegetables liquid, the mass content of glucose in enzymolysis fruits and vegetables liquid is made to be about 4%, the mass content of black-bone chicken peptide in enzymolysis fruits and vegetables liquid is about 0.8%, after stirring and evenly mixing, inoculum concentration according to about 0.18% accesses compound lactobacillus and carries out the second fermentation in enzymolysis fruits and vegetables liquid, compound lactobacillus is by streptococcus thermophilus, Lactobacillus delbrueckii, Lactobacillus casei and Lactobacillus plantarum composition, wherein streptococcus thermophilus, Lactobacillus delbrueckii, weight proportion between Lactobacillus casei and Lactobacillus plantarum is 3:2:0.5:0.5, and the temperature controlling the second fermentation is about 23 DEG C, speed of agitator is about 100r/min, the second fermentation is terminated when the pH value of zymotic fluid reduces by more than 0.5, obtained second zymotic fluid (pH value is 5.2 ~ 5.5).
4, the 3rd fermentation
Glucose and black-bone chicken peptide is added in above-mentioned second zymotic fluid, the mass content of glucose in the second zymotic fluid is made to be about 7%, the mass content of black-bone chicken peptide in the second zymotic fluid is about 0.7%, after stirring and evenly mixing, inoculum concentration according to about 0.01% carries out the 3rd fermentation to access mulriple yeasts, described mulriple yeasts is by rice wine yeast, brewer's yeast and white wine yeast composition, wherein rice wine yeast, weight proportion between brewer's yeast and white wine yeast is 1:1:1, and the temperature controlling the 3rd fermentation is about 16 DEG C, speed of agitator is about 60r/min, when zymotic fluid total sugar content lower than 2% time terminate the 3rd fermentation, obtained 3rd zymotic fluid.
5, Antrodia camphorata fermented product is prepared
Above-mentioned first zymotic fluid and the 3rd zymotic fluid are mixed centrifugal according to weight proportion 2:3, homogeneous, sterilizing are carried out to centrifuged supernatant, obtained Antrodia camphorata fermented product (pH value is 4.8 ~ 5.3); The mouthfeel of this Antrodia camphorata fermented product and local flavor marking the results are shown in Table 1.
Embodiment 4
Except in second step, compound lactobacillus is made up of streptococcus thermophilus, Lactobacillus delbrueckii, Lactobacillus casei, Lactobacillus plantarum, Lactococcus garvieae and Lactobacillus helveticus, and wherein streptococcus thermophilus, Lactobacillus delbrueckii, Lactobacillus casei, Lactobacillus plantarum, weight proportion between Lactococcus garvieae and Lactobacillus helveticus are 3:2:1:1:1:1; In 3rd fermentation step, mulriple yeasts by weight proportion be the brewer's yeast of 1:1:1, outside white wine yeast and fruit wine and wine yeast form, all the other are identical with embodiment 1, and each measurement result is in table 1.
Embodiment 5
Except in the second fermentation step, compound lactobacillus is made up of streptococcus thermophilus, Lactobacillus delbrueckii, lactobacillus acidophilus, Lactobacillus rhamnosus, lactobacillus fermenti, Lactobacillus pentosus and lactic acid sheet bacterium bacterium, wherein streptococcus thermophilus, Lactobacillus delbrueckii, lactobacillus acidophilus, Lactobacillus rhamnosus, lactobacillus fermenti, weight proportion between Lactobacillus pentosus and Pediococcus acidilactici is outside 3:2:1:1:1:0.5:0.5, all the other are identical with embodiment 2, and each measurement result is in table 1.
Reference examples 1
Except in the first fermentation step, access Leuconostoc mesenteroides add MRS medium component in above-mentioned slurries after and carry out the first fermentation, all the other are identical with embodiment 1, and each measurement result is in table 1.
Reference examples 2
This reference examples only implements the first fermentation of embodiment 1, and adopting by weight proportion is that the slurries of compound lactobacillus to embodiment 1 that the streptococcus thermophilus of 1:1 and Lactobacillus delbrueckii form ferment, fermentation parameter ferments identical with first of embodiment 1, zymotic fluid after fermentation is under 4000r/min after centrifugal about 15min, homogeneous, sterilizing are carried out to centrifuged supernatant, obtained fermented product, each measurement result is in table 1.
Table 1 Fermentation Process of Parameter measures and fermented product marking result
Remarks: "-" expression does not detect.
As seen from the results in Table 1:
Relative to the MRS culture medium of routine, adopt black-bone chicken peptide significantly can promote the growth of Leuconostoc mesenteroides as nitrogenous source; In addition, only have employing to comprise streptococcus thermophilus, the compound lactobacillus of Lactobacillus delbrueckii and other two or more lactic acid bacteria and the mulriple yeasts that simultaneously comprises two or more yeast to ferment to fruit and vegetable materials successively simultaneously, fermented product can be made simultaneously to have preferably mouthfeel and local flavor.
The evaluation of test example 1 immunoloregulation function
1, the preparation of mouse boosting cell suspension
Draw neck to put to death Balb/c mouse, soak 5min disinfection in 75% ethanol, the complete spleen of aseptic separation, washes away floating blood with PBS, divests connective tissue and fat constituent.Adopt syringe to draw about 5mLPBS, insert blowout cell in spleen gently, repeat transparent to spleen adventitia for several times, residue spleen tissue is cut into size 1mm
3fritter, shred on the 200 order stainless steel filtering nets that are placed on small beaker, grind with syringe nook closing member, PBS liquid washs, collect flushing liquor to centrifuge tube, the centrifugal 5min of 1200rpm, abandon supernatant, add 3mL erythrocyte cracked liquid, leave standstill 2min, add 10mL PBS cessation reaction, the centrifugal 5min of 1200rpm, abandon supernatant, twice is washed with PBS liquid, the centrifugal 5min of 1200rpm, wash once with the incomplete culture medium of RPMI-1640, the centrifugal 5min of 1200rpm, abandon supernatant, add appropriate RPMI-1640 complete medium (containing 10% hyclone, 100U/mL penicillin, 100 μ g/mL streptomysins and 10mM Hepes), adjustment cell concentration to 2 × 10
6individual cell/mL, Trypan Blue detects cell survival rate and is greater than 95%.
2, each fermented product is on lymphopoietic impact
Fermented product pure water prepared by embodiment 1 ~ 5, reference examples 1 and reference examples 2 is carried out gradient dilution respectively, obtained respective gradient dilution liquid.
Above-mentioned splenocyte suspension is joined in 96 well culture plates by 100 μ L/ holes, add the gradient dilution liquid of 10 μ LConA (5 μ g/mL) or 10 μ L LPS (5 μ g/mL) and the above-mentioned each fermented product of 10 μ L more respectively, each gradient does 6 repetitions, culture plate is placed in 37 DEG C, 5%CO
2incubator in cultivate 72h; Blank (namely adding 10 μ L pure water) is set simultaneously.
Adopt each fermented product of CCK-8 kit measurement on the impact (representing with SI (SI)) of spleen lymphocyte proliferation ability, result as depicted in figs. 1 and 2.From Fig. 1 and Fig. 2: relative to the fermented product of reference examples 1 and reference examples 2, Antrodia camphorata fermented product prepared by the embodiment of the present invention can significantly increase mouse T lymphocyte activity, has more excellent immunoloregulation function.
The evaluation of test example 2 anti-oxidation function
The fermented product of embodiment 1 ~ 5, reference examples 1 and reference examples 2 is carried out gradient dilution with the DMEM culture medium of serum-free respectively, obtained gradient dilution liquid;
By HepG2 cell with cell density 2 × 10
5be seeded to Tissue Culture Plate, every hole 2ml, be placed in 37 DEG C, 5%CO
2cultivate 24h in cell culture incubator, carefully siphon away the cell conditioned medium liquid in hole subsequently, clean once with HBSS, add the gradient dilution liquid 2ml of above-mentioned each fermented product respectively, in 37 DEG C, 5%CO
23.5h is cultivated in cell culture incubator, then fluorescent dye 2 ' is added, 7'-dihydro dichlorofluorescein sodium Diacetate (2 ', 7 '-dichlorofluorescin diacetate, DCFH-DA, final concentration is 10 μMs), carefully clean three times with HBSS, finally add antioxygen damage agent 600 μMs of AAPH; Blank (namely adding the DMEM culture medium of 2ml serum-free) is set simultaneously.
ROS content in flow cytomery cell is adopted (to use EC
50value represents), result is as shown in Figure 3.As shown in Figure 3: relative to the fermented product of reference examples 1 and reference examples 2, Antrodia camphorata fermented product prepared by the present invention has more excellent anti-oxidation function.
Last it is noted that above each embodiment is only in order to illustrate technical scheme of the present invention, be not intended to limit; Although with reference to foregoing embodiments to invention has been detailed description, those of ordinary skill in the art is to be understood that: it still can be modified to the technical scheme described in foregoing embodiments, or carries out equivalent replacement to wherein some or all of technical characteristic; And these amendments or replacement, do not make the essence of appropriate technical solution depart from the scope of various embodiments of the present invention technical scheme.
Claims (10)
1. a preparation method for Antrodia camphorata fermented product, is characterized in that, comprises the steps:
1) be soaked in water by Antrodia camphorata and extract, crushing and beating, gets slurries;
2), after adding medium component in described slurries, access Leuconostoc mesenteroides carries out the first fermentation, when the pH value of zymotic fluid reduces by more than 0.5, and the content of reducing sugar of zymotic fluid lower than 1.5% time terminate described first fermentation, obtained first zymotic fluid;
3) to pH value be 4.5 ~ 6 fruits and vegetables liquid in add pectase and carry out enzymolysis processing, obtained enzymolysis fruits and vegetables liquid;
4) after adding medium component in described enzymolysis fruits and vegetables liquid, access compound lactobacillus carries out the second fermentation, terminates described second fermentation, obtained second zymotic fluid when the pH value of zymotic fluid reduces by more than 0.5; Wherein, described compound lactobacillus is selected from more than four kinds in streptococcus thermophilus, Lactobacillus delbrueckii, lactobacillus acidophilus, Lactobacillus casei, Lactobacillus plantarum, lactobacillus fermenti, Lactobacillus rhamnosus, Lactobacillus pentosus, Lactococcus garvieae, Lactobacillus helveticus, Pediococcus acidilactici;
5), after adding medium component in described second zymotic fluid, access mulriple yeasts carries out the 3rd fermentation, when zymotic fluid total sugar content lower than 2% time terminate described 3rd fermentation, obtained 3rd zymotic fluid; Wherein, what described mulriple yeasts was selected from rice wine yeast, saccharomyces sake, brewer's yeast, white wine yeast and fruit wine and wine yeast is two or more;
6) by centrifugal after described first zymotic fluid and described 3rd zymotic fluid mixing, after centrifuged supernatant homogeneous, sterilizing, obtained Antrodia camphorata fermented product.
2. preparation method according to claim 1, it is characterized in that, the quality proportioning controlling described Antrodia camphorata and described water is 1:15 ~ 25, and described extraction temperature is 85 ~ 95 DEG C, the time of described extraction is 20 ~ 60min, and described Antrodia camphorata is crushed to 40 ~ 80 orders.
3. preparation method according to claim 1, it is characterized in that, described medium component comprise in sugar, peptide, inorganic salts and surfactant one or more, and in described peptide, mean molecule quantity is less than gross mass content >=80% of the component of 1000Da.
4. preparation method according to claim 3, it is characterized in that, step 2) in, sugar, peptide and inorganic salts are added in described slurries, make the mass content of described sugar in described slurries be 5 ~ 10%, the mass content of described peptide in described slurries is 0.3 ~ 0.8%, and the mass content of described inorganic salts in described slurries is 0.1 ~ 0.3%, and the temperature controlling described first fermentation is 22 ~ 28 DEG C, and rotating speed is 80 ~ 120r/min.
5. preparation method according to claim 1, it is characterized in that, be crushed to 40 ~ 80 orders by after the two or more fruit and vegetable materials be selected from banana, mango, pawpaw, mangosteen, dragon fruit, carrot, cucumber and tomato, obtained pH value is the described fruits and vegetables liquid of 4.5 ~ 6.
6. preparation method according to claim 1, is characterized in that, the consumption of described pectase is every gram of fruits and vegetables liquid 2 ~ 3 unit, and the temperature controlling described enzymolysis processing is 40 ~ 50 DEG C, and the time is 2 ~ 3h.
7. preparation method according to claim 3, it is characterized in that, step 4) in, in described enzymolysis fruits and vegetables liquid, add sugar and peptide, make the mass content of described sugar in described enzymolysis fruits and vegetables liquid be 3 ~ 5%, the mass content of described peptide in described enzymolysis fruits and vegetables liquid is 0.3 ~ 0.8%; Described compound lactobacillus at least comprises streptococcus thermophilus and Lactobacillus delbrueckii, the weight proportion of described streptococcus thermophilus, Lactobacillus delbrueckii and all the other lactic acid bacterias is 3:2:(2 ~ 5), and the temperature controlling described second fermentation is 18 ~ 23 DEG C, and rotating speed is 80 ~ 120r/min.
8. preparation method according to claim 3, it is characterized in that, step 5) in, in described second zymotic fluid, add sugar and peptide, make the mass content of described sugar in described second zymotic fluid be 4 ~ 8%, the mass content of described peptide in described second zymotic fluid is 0.3 ~ 0.8%; And the weight proportion controlled between two primary yeasts in described mulriple yeasts is 1:(0.8 ~ 1.2), the temperature of described 3rd fermentation is 16 ~ 20 DEG C, and rotating speed is 40 ~ 60r/min.
9. preparation method according to claim 1, is characterized in that, step 6) in, the weight proportion of described first zymotic fluid and described 3rd zymotic fluid is (4 ~ 6): (4 ~ 6).
10. an Antrodia camphorata fermented product, is characterized in that, according to claim 1 to 9, arbitrary described preparation method obtains.
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Address after: 100015 Beijing, Jiuxianqiao Middle Road, building 24, No., building 6 Patentee after: China Food Fermentation Industry Research Institute Co., Ltd. Address before: 100015 Beijing, Jiuxianqiao Middle Road, building 24, No., building 6 Patentee before: China National Academy of Food & Fermentation Industries |