CN109043262A - The preparation method and its proportion of plant extract complex function drink - Google Patents
The preparation method and its proportion of plant extract complex function drink Download PDFInfo
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- CN109043262A CN109043262A CN201810958815.9A CN201810958815A CN109043262A CN 109043262 A CN109043262 A CN 109043262A CN 201810958815 A CN201810958815 A CN 201810958815A CN 109043262 A CN109043262 A CN 109043262A
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- gas
- bubble
- current divider
- heat exchanger
- dispensing containers
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- 239000000419 plant extract Substances 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- 238000002347 injection Methods 0.000 claims abstract description 48
- 239000007924 injection Substances 0.000 claims abstract description 48
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 238000000855 fermentation Methods 0.000 claims abstract description 14
- 230000004151 fermentation Effects 0.000 claims abstract description 14
- 239000006041 probiotic Substances 0.000 claims abstract description 10
- 235000018291 probiotics Nutrition 0.000 claims abstract description 10
- 238000005096 rolling process Methods 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 18
- 239000011229 interlayer Substances 0.000 claims description 14
- 238000003756 stirring Methods 0.000 claims description 14
- 238000009826 distribution Methods 0.000 claims description 13
- 239000000463 material Substances 0.000 claims description 11
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- 235000013399 edible fruits Nutrition 0.000 claims description 9
- 238000005485 electric heating Methods 0.000 claims description 9
- 239000004744 fabric Substances 0.000 claims description 9
- 229910021389 graphene Inorganic materials 0.000 claims description 8
- 235000013361 beverage Nutrition 0.000 claims description 7
- 102000004190 Enzymes Human genes 0.000 claims description 6
- 108090000790 Enzymes Proteins 0.000 claims description 6
- 241000208688 Eucommia Species 0.000 claims description 6
- YZXBAPSDXZZRGB-DOFZRALJSA-N arachidonic acid Chemical compound CCCCC\C=C/C\C=C/C\C=C/C\C=C/CCCC(O)=O YZXBAPSDXZZRGB-DOFZRALJSA-N 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 5
- 238000011049 filling Methods 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- SERLAGPUMNYUCK-DCUALPFSSA-N 1-O-alpha-D-glucopyranosyl-D-mannitol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@H](O)CO[C@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O SERLAGPUMNYUCK-DCUALPFSSA-N 0.000 claims description 3
- 241000219226 Acer truncatum Species 0.000 claims description 3
- 244000144927 Aloe barbadensis Species 0.000 claims description 3
- 235000002961 Aloe barbadensis Nutrition 0.000 claims description 3
- 241000563984 Ampelopsis Species 0.000 claims description 3
- 241000345998 Calamus manan Species 0.000 claims description 3
- 235000008671 Calycanthus floridus Nutrition 0.000 claims description 3
- 235000008670 Calycanthus occidentalis Nutrition 0.000 claims description 3
- 244000249214 Chlorella pyrenoidosa Species 0.000 claims description 3
- 235000007091 Chlorella pyrenoidosa Nutrition 0.000 claims description 3
- 241001264174 Cordyceps militaris Species 0.000 claims description 3
- 229920002307 Dextran Polymers 0.000 claims description 3
- 241000195620 Euglena Species 0.000 claims description 3
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Chemical compound OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 claims description 3
- MVORZMQFXBLMHM-QWRGUYRKSA-N Gly-His-Lys Chemical compound NCCCC[C@@H](C(O)=O)NC(=O)[C@@H](NC(=O)CN)CC1=CN=CN1 MVORZMQFXBLMHM-QWRGUYRKSA-N 0.000 claims description 3
- 241000168525 Haematococcus Species 0.000 claims description 3
- 241000253121 Inula britannica Species 0.000 claims description 3
- 229920001202 Inulin Polymers 0.000 claims description 3
- 244000148992 Lindera benzoin Species 0.000 claims description 3
- 235000004520 Lindera benzoin Nutrition 0.000 claims description 3
- 235000008262 Lindera benzoin var. benzoin Nutrition 0.000 claims description 3
- 244000131360 Morinda citrifolia Species 0.000 claims description 3
- 244000179886 Moringa oleifera Species 0.000 claims description 3
- 235000011347 Moringa oleifera Nutrition 0.000 claims description 3
- 108010038807 Oligopeptides Proteins 0.000 claims description 3
- 102000015636 Oligopeptides Human genes 0.000 claims description 3
- 244000131316 Panax pseudoginseng Species 0.000 claims description 3
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 claims description 3
- 235000003140 Panax quinquefolius Nutrition 0.000 claims description 3
- 235000009388 Parthenocissus quinquefolia Nutrition 0.000 claims description 3
- 241000219780 Pueraria Species 0.000 claims description 3
- 240000008599 Rhus glabra Species 0.000 claims description 3
- 235000013234 Rhus glabra Nutrition 0.000 claims description 3
- 240000004808 Saccharomyces cerevisiae Species 0.000 claims description 3
- 241000124033 Salix Species 0.000 claims description 3
- 244000007853 Sarothamnus scoparius Species 0.000 claims description 3
- 241001145025 Saussurea involucrata Species 0.000 claims description 3
- 244000272459 Silybum marianum Species 0.000 claims description 3
- 235000010841 Silybum marianum Nutrition 0.000 claims description 3
- 229920000377 Sinistrin Polymers 0.000 claims description 3
- 241000586290 Suaeda salsa Species 0.000 claims description 3
- 235000021307 Triticum Nutrition 0.000 claims description 3
- 235000011399 aloe vera Nutrition 0.000 claims description 3
- 229940114079 arachidonic acid Drugs 0.000 claims description 3
- 235000021342 arachidonic acid Nutrition 0.000 claims description 3
- 210000001367 artery Anatomy 0.000 claims description 3
- 238000005452 bending Methods 0.000 claims description 3
- 239000002131 composite material Substances 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 3
- HEBKCHPVOIAQTA-NGQZWQHPSA-N d-xylitol Chemical compound OC[C@H](O)C(O)[C@H](O)CO HEBKCHPVOIAQTA-NGQZWQHPSA-N 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 235000021255 galacto-oligosaccharides Nutrition 0.000 claims description 3
- 150000003271 galactooligosaccharides Chemical class 0.000 claims description 3
- 235000008434 ginseng Nutrition 0.000 claims description 3
- 108010038983 glycyl-histidyl-lysine Proteins 0.000 claims description 3
- 239000010903 husk Substances 0.000 claims description 3
- JYJIGFIDKWBXDU-MNNPPOADSA-N inulin Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)OC[C@]1(OC[C@]2(OC[C@]3(OC[C@]4(OC[C@]5(OC[C@]6(OC[C@]7(OC[C@]8(OC[C@]9(OC[C@]%10(OC[C@]%11(OC[C@]%12(OC[C@]%13(OC[C@]%14(OC[C@]%15(OC[C@]%16(OC[C@]%17(OC[C@]%18(OC[C@]%19(OC[C@]%20(OC[C@]%21(OC[C@]%22(OC[C@]%23(OC[C@]%24(OC[C@]%25(OC[C@]%26(OC[C@]%27(OC[C@]%28(OC[C@]%29(OC[C@]%30(OC[C@]%31(OC[C@]%32(OC[C@]%33(OC[C@]%34(OC[C@]%35(OC[C@]%36(O[C@@H]%37[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O%37)O)[C@H]([C@H](O)[C@@H](CO)O%36)O)[C@H]([C@H](O)[C@@H](CO)O%35)O)[C@H]([C@H](O)[C@@H](CO)O%34)O)[C@H]([C@H](O)[C@@H](CO)O%33)O)[C@H]([C@H](O)[C@@H](CO)O%32)O)[C@H]([C@H](O)[C@@H](CO)O%31)O)[C@H]([C@H](O)[C@@H](CO)O%30)O)[C@H]([C@H](O)[C@@H](CO)O%29)O)[C@H]([C@H](O)[C@@H](CO)O%28)O)[C@H]([C@H](O)[C@@H](CO)O%27)O)[C@H]([C@H](O)[C@@H](CO)O%26)O)[C@H]([C@H](O)[C@@H](CO)O%25)O)[C@H]([C@H](O)[C@@H](CO)O%24)O)[C@H]([C@H](O)[C@@H](CO)O%23)O)[C@H]([C@H](O)[C@@H](CO)O%22)O)[C@H]([C@H](O)[C@@H](CO)O%21)O)[C@H]([C@H](O)[C@@H](CO)O%20)O)[C@H]([C@H](O)[C@@H](CO)O%19)O)[C@H]([C@H](O)[C@@H](CO)O%18)O)[C@H]([C@H](O)[C@@H](CO)O%17)O)[C@H]([C@H](O)[C@@H](CO)O%16)O)[C@H]([C@H](O)[C@@H](CO)O%15)O)[C@H]([C@H](O)[C@@H](CO)O%14)O)[C@H]([C@H](O)[C@@H](CO)O%13)O)[C@H]([C@H](O)[C@@H](CO)O%12)O)[C@H]([C@H](O)[C@@H](CO)O%11)O)[C@H]([C@H](O)[C@@H](CO)O%10)O)[C@H]([C@H](O)[C@@H](CO)O9)O)[C@H]([C@H](O)[C@@H](CO)O8)O)[C@H]([C@H](O)[C@@H](CO)O7)O)[C@H]([C@H](O)[C@@H](CO)O6)O)[C@H]([C@H](O)[C@@H](CO)O5)O)[C@H]([C@H](O)[C@@H](CO)O4)O)[C@H]([C@H](O)[C@@H](CO)O3)O)[C@H]([C@H](O)[C@@H](CO)O2)O)[C@@H](O)[C@H](O)[C@@H](CO)O1 JYJIGFIDKWBXDU-MNNPPOADSA-N 0.000 claims description 3
- 229940029339 inulin Drugs 0.000 claims description 3
- 239000000905 isomalt Substances 0.000 claims description 3
- 235000010439 isomalt Nutrition 0.000 claims description 3
- HPIGCVXMBGOWTF-UHFFFAOYSA-N isomaltol Natural products CC(=O)C=1OC=CC=1O HPIGCVXMBGOWTF-UHFFFAOYSA-N 0.000 claims description 3
- 235000017524 noni Nutrition 0.000 claims description 3
- 238000010943 off-gassing Methods 0.000 claims description 3
- 229940107071 plant stanol ester Drugs 0.000 claims description 3
- 239000000843 powder Substances 0.000 claims description 3
- 235000012950 rattan cane Nutrition 0.000 claims description 3
- 238000010992 reflux Methods 0.000 claims description 3
- 239000007921 spray Substances 0.000 claims description 3
- 210000003462 vein Anatomy 0.000 claims description 3
- 238000005303 weighing Methods 0.000 claims description 3
- 239000002023 wood Substances 0.000 claims description 3
- 244000098338 Triticum aestivum Species 0.000 claims 1
- 238000003491 array Methods 0.000 claims 1
- 239000002994 raw material Substances 0.000 claims 1
- 241000894006 Bacteria Species 0.000 abstract description 5
- 238000013461 design Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 244000005706 microflora Species 0.000 abstract description 2
- 230000008569 process Effects 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 79
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 229940088598 enzyme Drugs 0.000 description 4
- 241000235342 Saccharomycetes Species 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 235000014655 lactic acid Nutrition 0.000 description 3
- 239000004310 lactic acid Substances 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 206010037660 Pyrexia Diseases 0.000 description 2
- 241000209140 Triticum Species 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000003303 reheating Methods 0.000 description 2
- 108010059892 Cellulase Proteins 0.000 description 1
- 108091005804 Peptidases Proteins 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- 102100037486 Reverse transcriptase/ribonuclease H Human genes 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229940106157 cellulase Drugs 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000006911 enzymatic reaction Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000002045 lasting effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 230000002085 persistent effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Preparation or treatment thereof
- A23L2/38—Other non-alcoholic beverages
- A23L2/382—Other non-alcoholic beverages fermented
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M27/00—Means for mixing, agitating or circulating fluids in the vessel
- C12M27/02—Stirrer or mobile mixing elements
- C12M27/04—Stirrer or mobile mixing elements with introduction of gas through the stirrer or mixing element
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/12—Means for regulation, monitoring, measurement or control, e.g. flow regulation of temperature
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
- C12M41/00—Means for regulation, monitoring, measurement or control, e.g. flow regulation
- C12M41/30—Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration
- C12M41/34—Means for regulation, monitoring, measurement or control, e.g. flow regulation of concentration of gas
-
- 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
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Organic Chemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- Genetics & Genomics (AREA)
- Biomedical Technology (AREA)
- Microbiology (AREA)
- Biochemistry (AREA)
- Biotechnology (AREA)
- General Health & Medical Sciences (AREA)
- Sustainable Development (AREA)
- Analytical Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Nutrition Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Non-Alcoholic Beverages (AREA)
Abstract
The invention discloses the preparation methods and its proportion of plant extract complex function drink, the compositional liquor continued in producing process into dispensing containers injects constant temperature bubble, the compositional liquor in dispensing containers is set to be in continuous rolling agitated conditions using the impact force of injection bubble, also compositional liquor is heated using the temperature of bubble simultaneously, while containing gas needed for product design in bubble；Gas directly supplies in a liquid, can be naked quick-fried in compositional liquor sufficiently in the form of bubble in liquid, promotes compositional liquor more completely to ferment, and without detriment to probiotics integrality；And play the bigger microflora fermentation vigor after [bacterium gas fused] by design.
Description
Technical field
The preparation method in field more particularly to plant extract complex function drink is produced the invention belongs to beverage and its is matched
Than.
Background technique
Existing complex function drink often uses simple milled mixture, then carry out sterilization processing after carry out it is filling,
However there are moieties to be difficult to be directly absorbed by the body in plant extracts, thus it be easy to cause dyspeptic consequence；Therefore
If the drink in plant extracts carries out fermenting in advance in producing process and biological enzymatic reaction, then the drink after Chunhua is not
Only thick taste is more preferably absorbed, and often fermentation process is bad is precisely controlled for existing Zymolysis Equipment.
Summary of the invention
Goal of the invention: in order to overcome the deficiencies in the prior art, the present invention provides one kind and produces high-efficient, is conducive to people
The preparation method and its proportion for the plant extract complex function drink that body absorbs.
Technical solution: to achieve the above object, a kind of plant extract complex function drink preparation method of the invention:
Composite beverage produce the following steps are included:
Step 1: weighing and stirs and evenly mixs plant extracts, and the plant extracts mixed is launched and is matched into anhydrous
It sets in container；
Step 2: filling the water and be stirred into the dispensing containers that step 1 is stirred, and makes to form mixing in dispensing containers
Complete compositional liquor, and 30 DEG C ± 0.5 DEG C in dispensing containers of temperature constant state is maintained, and the temperature constant state is maintained to step
Five；
Step 3: the compositional liquor into the dispensing containers of step 2 continues to launch carbon source and probiotics, and maintenance 7 × 24 is small
When the probiotics fermention time；
Step 4: biological enzyme, and pneumatic stirring are launched into the step 3 dispensing containers of fermented completion；
Step 5: the constant temperature Chunhua in dispensing containers by fermentation liquid and biological enzyme；
Step 6: by the good compound beverage discharging of Chunhua in dispensing containers；
During step 2 to step 5, the compositional liquor continued into dispensing containers injects constant temperature bubble, utilizes injection
The impact force of bubble makes the compositional liquor in dispensing containers be in continuous rolling agitated conditions, while also using the temperature of bubble to multiple
It is heated with liquid, while containing the gas containing preparation needed for product in bubble, sufficiently fused in compositional liquor, promote fermentation；
And 30 DEG C ± 0.5 DEG C of liquid in dispensing containers is controlled by temperature, speed and the gas percentage of control injection bubble
Temperature constant state, stirring intensity reach control fermenting speed.
Further, the producing equipment of plant extract complex function drink, the dispensing containers include that lateral cylindricality is close
Tank body is closed, is lateral columnar configuration chamber in the cylindricality vapor tight tank body, the upside of the tank body is connected with feed pipe, institute
The downside for stating tank body is connected with discharge nozzle；The first shut-off valve and second is separately installed on the feed pipe and discharge nozzle to close
Disconnected valve；It is also provided with and communicated with exhaust pipe on the upside of the closed tank body, relief valve is provided on the exhaust pipe, the exhaust pipe goes out
Mouth is provided with gaseous sphere spray head；
It further include barotropic gas supply pipe, pneumatic filter, gas thermostatic heater, level-one current divider box；The positive pressure gas
The outlet side connection of body supply pipe connects the inlet end of the pneumatic filter, described in the outlet side connection of the pneumatic filter
The inlet end of gas thermostatic heater, the outlet side of the gas thermostatic heater are connected to the inlet end of the level-one current divider box；
It further include second level current divider box, the two second level current divider boxes are symmetrically disposed on the vapor tight tank body both sides external, and two
The second level current divider box passes through two gas-guide tubes respectively and is connected to the level-one current divider box；
The bubble injection pipe of several hard is respectively connected on each second level current divider box, it is several on single second level current divider box
The bubble injection pipe of hard is along the equidistant array distribution of vapor tight tank body axis direction；And the bubble injection pipe of each hard
Outlet port protrudes into that the configuration is intracavitary, and bubble injection pipe protrudes into the circle that the intracavitary part of the configuration is affixed on the configuration chamber
The distribution of arc inner wall；Several bubble injection pipes of configuration cavity wall are affixed at spiral bending curvature；
The two second level current divider boxes are respectively the first current divider box and the second current divider box, and first current divider box and second shunt
Each bubble injection pipe connected on case is respectively first bubble injection pipe array and the second bubble injection pipe array；First gas
The bubble each gas outlet of injection pipe array is in replace cross-distribution to match in described with each gas outlet of the second bubble injection pipe array
Set bottom of chamber portion.
Further, observation window is also set up on the upside of the closed tank body of the cylindricality；It is provided on each bubble injection pipe
The check valve of liquid reflux is prevented, further includes temperature indicator in tank on the closed tank body, also shunts and set on the discharge nozzle
It is equipped with product control isocon.
Further, the gas thermostatic heater includes columned outer cylinder, the cylindrical wall of the columned outer cylinder
Uniformly distributed hollow out has several first gas ports on face, and one end of the columned outer cylinder is inlet end, the other end is outlet side；Institute
The concentric circle that is provided in the inside by near outgassing end of outer cylinder is stated every disk, the circle is coaxial close to the side of inlet end every disk
The heart is provided with outer heat exchanger tube, and air inlet heat exchanger channels, the air inlet are formed between the outer heat exchange drum outer wall and the outer tube inner wall
The end of heat exchanger channels is connected to the inlet end, and the outer heat exchanger tube is set far from round one end integrated coaxial heart every disk
It is equipped with coniform drainage cone, the tip direction of the drainage cone is opposite with the airintake direction of the inlet end；
It is also concentric in the outer heat exchanger tube to be provided with interior heat exchanger tube, uniformly distributed hollow out on the cylinder wall surface of the interior heat exchanger tube
There are several second gas ports, forms heating wire between the interior heat exchanger tube and the outer heat exchanger tube and spiral interlayer；It further include graphite
The heater of alkene electric heating cloth material, spiral spiral of the heater of the graphene electric heating cloth material are set to the heating wire
It spirals in interlayer；Gas is formed in the cylinder of the interior heat exchanger tube and disturbs column chamber, and the intracavitary concentric rotation of gas disturbance column is set
It is equipped with disturbance shaft, array distribution there are several disturbance rotating vanes in the axial direction in the disturbance shaft；The gas disturbance
Column is intracavitary to be also fixedly installed with rotating shaft electric motor, and the rotating shaft electric motor and the disturbance shaft are drivingly connected；The circle is every disk
Disk is additionally provided with several ventholes, and the outlet side and gas disturbance column chamber are interconnected by each venthole；It is described go out
Gas is additionally provided with temperature sensor at end.
Further, plant extract complex function drink preparation proportion: the material combination substance of the drink is configured according to weight
Amount percentage is made of following component:
Carbon source: 8% -15%；
Plant extracts: 10% -20%；
Surplus is water.
Further, the carbon source is glucose.
Further, the plant extracts is made of according to weight percent following component:
Xylo-oligosaccharide: 2% -3%；
Sessileflower Acanthopanax Bark: 2% -3%；
Aloe barbadensis Miller: 2% -3%；
Galactooligosaccharide: 2% -3%；
Isomalt: 2% -3%；
Plant stanol ester: 2% -3%；
Pearl Gly-His-Lys: 2% -3%；
Inulin: 5.5% -6.5%；
Polyfructosan: 2% -3%；
Seed of bark of eucommia: 2% -3%；
Phytosterol: 2% -3%；
Arachidonic acid: 2% -3%；
Aobvious arteries and veins Inula britannica chinensis: 2% -3%；
Noni puree: 2% -3%；
Yeast beta-dextran: 2% -3%；
Saussurea involucrata culture: 2% -3%；
Haematococcus: 2% -3%；
Samara: 2% -3%；
Acer truncatum: 2% -3%；
Pueraria root powder: 2% -3%；
Wheat oligopeptide: 2.5% -3.5%；
Ginseng: 2% -3%；
Chlorella pyrenoidosa: 2% -3%；
Combined spicebush leaf: 2% -3%；
Suaeda salsa seed: 2% -3%；
U.S. rattan fruit: 2% -3%；
Rhus glabra: 2% -3%；
Cordyceps militaris sporocarp: 2% -3%；
Ah Say fruit: 2% -3%；
Euglena: 2% -3%；
Smooth bark Lai wood fruit: 2% -3%；
Qingqian Willow leaf: 2% -3%；
Ampelopsis grossdentata leaf: 2% -3%；
Silybum marianum seed: 2% -3%；
Eucommia Bark male flower: 2% -3%；
Odd Asia seed: 2% -3%；
Circle bud isapgol husk: 2% -3%；
Line leaf broom top: 2% -3%；
Leaf of Moringa: 2% -3%.
The utility model has the advantages that the nutritive value of complex function drink of the invention is high, it is easy to be absorbed by the body, while dispensing containers
Interior compositional liquor injects constant temperature bubble, so that the compositional liquor in dispensing containers is in continuous rolling using the impact force of injection bubble and stirs
Dynamic state, while also compositional liquor is heated using the temperature of bubble, while being filled in bubble containing gas needed for product design
Divide fused required gas in compositional liquor, promotes fermentation；And pass through the temperature of control injection bubble, speed and required gas
Percentage controls the temperature constant state of liquid, stirring intensity and fermenting speed in dispensing containers；The first bubble of cross-distribution is infused
The bubble for entering each gas outlet ejection of pipe array and the second bubble injection pipe array makes to configure intracavitary compositional liquor in axis side
It is in upwardsThe rolling of shape promotes the mixing of configuration intracavity liquid；Gas directly supplies in a liquid, can be sufficiently in liquid
The form of bubble is naked quick-fried in compositional liquor, promotes compositional liquor more completely to ferment, and without detriment to probiotics integrality.
Detailed description of the invention
Attached drawing 1 is whole first schematic diagram of equipment of this programme；
Attached drawing 2 is whole second schematic diagram of equipment of this programme；
Attached drawing 3 is closed tank body solid cut-away diagram；
Attached drawing 4 is that closed tank body is bowed cross-sectional view；
Attached drawing 5 is gas thermostatic heater schematic diagram；
Attached drawing 6 is that gas thermostatic heater splits structural schematic diagram.
Specific embodiment
The present invention will be further explained with reference to the accompanying drawing.
The preparation of the plant extract complex function drink as shown in attached drawing 1 to 6 configures the original of the drink with when preparation method
Material compatibility substance is made of according to weight percent following component:
Carbon source: 8% -15%；
Plant extracts: 10% -20%；
Surplus is water.
The carbon source of the present embodiment is glucose.
The plant extracts of the present embodiment is made of according to weight percent following component:
Xylo-oligosaccharide: 2% -3%；
Sessileflower Acanthopanax Bark: 2% -3%；
Aloe barbadensis Miller: 2% -3%；
Galactooligosaccharide: 2% -3%；
Isomalt: 2% -3%；
Plant stanol ester: 2% -3%；
Pearl Gly-His-Lys: 2% -3%；
Inulin: 5.5% -6.5%；
Polyfructosan: 2% -3%；
Seed of bark of eucommia: 2% -3%；
Phytosterol: 2% -3%；
Arachidonic acid: 2% -3%；
Aobvious arteries and veins Inula britannica chinensis: 2% -3%；
Noni puree: 2% -3%；
Yeast beta-dextran: 2% -3%；
Saussurea involucrata culture: 2% -3%；
Haematococcus: 2% -3%；
Samara: 2% -3%；
Acer truncatum: 2% -3%；
Pueraria root powder: 2% -3%；
Wheat oligopeptide: 2.5% -3.5%；
Ginseng: 2% -3%；
Chlorella pyrenoidosa: 2% -3%；
Combined spicebush leaf: 2% -3%；
Suaeda salsa seed: 2% -3%；
U.S. rattan fruit: 2% -3%；
Rhus glabra: 2% -3%；
Cordyceps militaris sporocarp: 2% -3%；
Ah Say fruit: 2% -3%；
Euglena: 2% -3%；
Smooth bark Lai wood fruit: 2% -3%；
Qingqian Willow leaf: 2% -3%；
Ampelopsis grossdentata leaf: 2% -3%；
Silybum marianum seed: 2% -3%；
Eucommia Bark male flower: 2% -3%；
Odd Asia seed: 2% -3%；
Circle bud isapgol husk: 2% -3%；
Line leaf broom top: 2% -3%；
Leaf of Moringa: 2% -3%.
Composite beverage produce the following steps are included:
Step 1: weighing and stirs and evenly mixs plant extracts, and the plant extracts mixed is launched and is matched into anhydrous
It sets in container；It had both been injected into the present embodiment in the configuration chamber 14 in closed tank body 12；
Step 2: filling the water and be stirred into the dispensing containers that step 1 is stirred, and makes to form mixing in dispensing containers
Complete compositional liquor, and 30 DEG C ± 0.5 DEG C in dispensing containers of temperature constant state is maintained, and the temperature constant state is maintained to step
Five；
Step 3: the compositional liquor into the dispensing containers of step 2 continues to launch carbon source and probiotics, and maintenance 7 × 24 is small
When the probiotics fermention time；The probiotics of the present embodiment are as follows: 1. saccharomycete；Or 2. lactic acid bacteria.
Step 4: biological enzyme, and pneumatic stirring, the present embodiment are launched into the step 3 dispensing containers of fermented completion
Biological enzyme be pectase, protease and cellulase etc., substance not easily digested in its compositional liquor is subjected to promotion body
Outer decomposition promotes to absorb.
Step 5: by dispensing containers constant temperature Chunhua；
Step 6: by the good compound beverage discharging of Chunhua in dispensing containers；
During step 2 to step 5, the compositional liquor continued into dispensing containers injects constant temperature bubble, the present embodiment
The gas heated by constent temperature heater 3 is injected by configuration chamber 14 of the bubble injection pipe 5 of several hard into closed tank body 12
Body, and then it is formed with the bubble of impact；The present embodiment is made at the compositional liquor in dispensing containers using the impact force of injection bubble
In continuously rolling agitated conditions, while also compositional liquor is heated using the temperature of bubble, while containing fermentation institute in bubble
The gas needed, sufficiently fuses in compositional liquor, promotes fermentation；And pass through temperature, speed and the gas hundred of control injection bubble
30 DEG C ± 0.5 DEG C of temperature constant state, stirring intensity and fermenting speed for dividing ratio to control liquid in dispensing containers, the present embodiment hair
1. saccharomycete of gas needed for ferment is oxygen；2. lactic acid bacteria is nitrogen.Control saccharomycete [fermentation oxygen dissolving value] can be passed through；Lactic acid
Bacterium [fermentation without oxygen value] controls the fermentation quality and speed of flora and compositional liquor in the present embodiment.
As shown in Figures 1 to 6, the producing equipment of the plant extract complex function drink preparation proportion of the present embodiment, including cross
To the closed tank body 12 of cylindricality, the closed tank body 12 of the present embodiment is the dispensing containers, is in the closed tank body 12 of cylindricality
Laterally columnar configuration chamber 14, the upside of the tank body 12 are connected with feed pipe 6, and the downside of the tank body 12 is connected to connection
There is discharge nozzle 11；The first shut-off valve 7 and the second shut-off valve 10 are separately installed on the feed pipe 6 and discharge nozzle 11；It is described close
It closes 12 upside of tank body and is also provided with and communicated with exhaust pipe 9, relief valve, the outlet of exhaust pipe 9 setting are provided on the exhaust pipe 9
There is gaseous sphere spray head 9.1；
It further include barotropic gas supply pipe 1, pneumatic filter 2, gas thermostatic heater 3, level-one current divider box 38；Positive pressure gas
The inlet end of body supply pipe 1 is connected with positive pressure air supply plant, and the outlet side connection of the barotropic gas supply pipe 1 connects the gas
The inlet end of body filter 2, the outlet side of the pneumatic filter 2 is connected to the inlet end of the gas thermostatic heater 3, described
The outlet side of gas thermostatic heater 3 is connected to the inlet end of the level-one current divider box 38；It further include second level current divider box 4, described in two
Second level current divider box 4 is symmetrically disposed on 12 both sides external of closed tank body, and the two second level current divider boxes 4 pass through two air guides respectively
Pipe 37 is connected to the level-one current divider box 38；Gas in level-one current divider box 38 branches to two two fractions by two gas-guide tubes 37
It flows in case 4, and then forms the isobaric constant temperature gas being heated, and then two two fractions in the two second level current divider boxes 4
Constant temperature gas in stream case 4 is injected into configuration chamber 14 by several bubble injection pipes 5；
The bubble injection pipe 5 of several hard is respectively connected on each second level current divider box 4, on single second level current divider box 4
The bubble injection pipe 5 of several hard is along the equidistant array distribution of closed 12 axis direction of tank body；And the bubble of each hard
15 end of gas outlet of injection pipe 5 is protruded into the configuration chamber 14, and bubble injection pipe 5 protrudes into the part patch in the configuration chamber 14
In the circular arc inner wall distribution of the configuration chamber 14；Adherent setting makes full use of the space in configuration chamber 14, avoids in configuration chamber 14
Form agitation resistance；
Several bubble injection pipes 5 of configuration 14 inner wall of chamber are affixed at spiral bending curvature, and then make each gas outlet 15
The bubble jet flow ejected is soaring along the arc inner wall of configuration chamber 14 in constant slope, this is at spiral radian bubble injection pipe 5
The bubble jet flow resistance of the ejection of gas outlet 15 is reduced, and then increases the rolling intensity in configuration chamber 14；
The two second level current divider boxes 4 are respectively the first current divider box 4.1 and the second current divider box 4.2, first current divider box 4.1
It is respectively first bubble injection pipe array 5 and the second bubble injection pipe with each bubble injection pipe 5 connected on the second current divider box 4.2
Array 5.2；Each outlet of each gas outlet 15 of the first bubble injection pipe array 5 and the second bubble injection pipe array 5.2
Mouth 15 is in be interspersed in 14 bottom of configuration chamber；The first bubble injection pipe array 5 of the cross-distribution and the second gas
The ejection of each gas outlet 15 of bubble injection pipe array 5.2 makes the compositional liquor in configuration chamber 14 exist along the bubble jet flow of axisymmetrical
It is on axis viewThe rolling of shape promotes the mixing of liquid in configuration chamber 14；Bubble is utilized at the same time while also
Temperature heats compositional liquor, while containing gas needed for fermenting in bubble, gas needed for sufficiently fusing promotees in compositional liquor
It sets out ferment；And liquid in dispensing containers is controlled by the percentage of the temperature of control injection bubble, speed and required gas
30 DEG C ± 0.5 DEG C of temperature constant state, stirring intensity and fermenting speed, the bubble type stirring make bacterium gas fuse effect it is stronger, tool
There is bigger microflora fermentation vigor.
Observation window 13 is also set up on the upside of the closed tank body 12 of cylindricality；The vent pressure of the relief valve is 0.2kg；Having
Stable positive pressure environment is maintained during body running in closed tank body 12, effectively avoids ambient atmos into polluting in tank in tank
Compositional liquor；The check valve for preventing liquid reflux is provided on each bubble injection pipe 5；Further include on the closed tank body 12
Temperature indicator 51 in tank also shunt on the discharge nozzle 11 and are provided with product control isocon 52.
The gas thermostatic heater 3 includes columned outer cylinder 28, on the cylinder wall surface of the columned outer cylinder 28
Uniformly distributed hollow out has several first gas ports 26, and one end of the columned outer cylinder 28 is inlet end 36, the other end is outlet side
29；The inside by near outgassing end 29 of the outer cylinder 28 is concentric be provided with it is round every disk 20, it is described it is round every disk 20 close into
The side at gas end 36 is concentric to be provided with outer heat exchanger tube 32, is formed between 28 inner wall of outer 32 outer wall of heat exchanger tube and the outer cylinder
The end of air inlet heat exchanger channels 33, the air inlet heat exchanger channels 33 is connected to the inlet end 36, and the outer heat exchanger tube 32 is far from institute
State round one end integrated coaxial heart every disk 20 and be provided with coniform drainage cone 27, the tip of the drainage cone 27 towards with
The airintake direction of the inlet end 36 is opposite；It is also concentric in the outer heat exchanger tube 32 to be provided with interior heat exchanger tube 31, it is described interior to change
Uniformly distributed hollow out has several second gas ports 34 on the cylinder wall surface of hot cylinder 31, the interior heat exchanger tube 31 and the outer heat exchanger tube 32 it
Between form heating wire and spiral interlayer 21；It further include the heater 23 of graphene electric heating cloth material, the graphene electric heating cloth material
Spiral spiral of heater 23 be set to the heating wire and spiral in interlayer 21；Gas is formed in the cylinder of the interior heat exchanger tube 31
Body disturbs column chamber 25, and concentric rotation, which is provided with, in the gas disturbance column chamber 25 disturbs shaft 22, in the disturbance shaft 22
Array distribution has several disturbance rotating vanes in the axial direction；Rotating shaft electric motor is also fixedly installed in the gas disturbance column chamber 25
35, the rotating shaft electric motor 35 is drivingly connected with the disturbance shaft 22；It is done if the round disk every disk 20 is additionally provided with
The outlet side 29 and gas disturbance column chamber 25 are interconnected by stomata 30, each venthole 30；At the outlet side 29 also
It is provided with temperature sensor；
The working principle of the gas thermostatic heater 3 is explained: during the work time, in advance by graphene electric heating cloth material
Heater 23 is powered, and then the heater 23 of spiral graphene electric heating cloth material releases heat, and then graphene electric heating
The heat that the heater 23 of cloth material is released is transmitted to immediately on the outer heat exchanger tube 32 and interior heat exchanger tube 31 being close to therewith, simultaneously
Also the chamber portion for making heating wire spiral in interlayer 21 forms fever gas-bearing formation；Cold air passes through under the positive pressure for equipment of supplying gas
Inlet end 36 enters in outer cylinder 28, and then uniformly flows into air inlet heat exchanger channels 33 in divergent shape, in air inlet heat exchanger channels 33
Gas by outer 32 outer wall of heat exchanger tube the first gas for preheating, and then being preheated in air inlet heat exchanger channels 33 again by changing outside
On hot cylinder 32 uniformly distributed several first gas ports 26 uniformly introduce in the chamber portion that heating wire spirals in interlayer 21 and by
Second reheating, so in the chamber portion that spirals in interlayer 21 of heating wire heated gas pass through it is uniformly distributed on interior heat exchanger tube 31
Several second gas ports 34 imported into gas disturbance column chamber 25 in, gas disturb column chamber 25 in gas by interior heat exchanger tube 31
The third reheating of inner wall fever, final gas disturb the gas in column chamber 25 under the gas pressure of air supply plant by several
Venthole 30 is expelled to outlet side 29, and then realizes the heating to gas and the effect of constant temperature, and the temperature at outlet side 29 passes
Sensor detects the temperature that gas is discharged from outlet side 29 immediately, and then the heating wire of adjustment heating in real time can be needed according to heating
Heating temperature；
Shaft 22 is disturbed at the same time, is in rotation status always, and then is in the gas in gas disturbance column chamber 25
Lasting disturbance eddy flow state, and then the gas that continuously disturbs in column chamber 25 is disturbed by outer heat exchanger tube 32 uniformly distributed several the
The chamber portion that one gas port 26 continuously affects heating wire to spiral in interlayer 21 is in persistent disturbances state, and then effectively prevent electricity
Stable laminar flow phenomenon occurs for the heated filament chamber portion in interlayer 21 that spirals, the chamber portion for promoting heating wire to spiral in interlayer 21
The gas of interior heating spread rapidly, make heating wire spiral 21 inner cavity portion of interlayer temperature it is more uniform, and and its gas
The eddy flow that body disturbance column chamber 25 stirs promotes the heat exchange that air in disturbance column chamber 25 and heating wire spiral between interlayer 21；
Outer heat exchanger tube 32 and interior heat exchanger tube 31 in the present embodiment are the heat-conducting of insulation.
Facilities and equipments use environment temperature of the present invention are as follows: 22-26 DEG C.
The above is only a preferred embodiment of the present invention, it should be pointed out that: for the ordinary skill people of the art
For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered
It is considered as protection scope of the present invention.
Claims (8)
1. a kind of plant extract complex function drink preparation method, it is characterised in that:
Composite beverage produce the following steps are included:
Step 1: weighing and stirs and evenly mixs plant extracts, and the plant extracts mixed is launched and is held into anhydrous configuration
In device；
Step 2: filling the water and be stirred into the dispensing containers that step 1 is stirred, and makes to be formed mixing in dispensing containers completely
Compositional liquor, and maintain temperature constant state in dispensing containers, and the temperature constant state is maintained to step 5；
Step 3: the compositional liquor into the dispensing containers of step 2 continues to launch carbon source and probiotics, and maintains one section of probiotics
Fermentation time；
Step 4: biological enzyme, and pneumatic stirring are launched into the step 3 dispensing containers of fermented completion；
Step 5: the constant temperature Chunhua in dispensing containers by fermentation liquid and biological enzyme；
Step 6: by the good compound beverage discharging of Chunhua in dispensing containers；
During step 2 to step 5, the compositional liquor continued into dispensing containers injects constant temperature bubble, utilizes injection bubble
Impact force so that the compositional liquor in dispensing containers is in continuous rolling agitated conditions, while also using the temperature of bubble to compositional liquor
It is heated, while containing the gas containing preparation needed for product in bubble, sufficiently fused in compositional liquor, promote fermentation；And
The temperature constant state of liquid in dispensing containers, stirring are controlled by force by temperature, speed and the gas percentage of control injection bubble
Degree reaches control fermenting speed.
2. a kind of plant extract complex function drink preparation method according to claim 1, it is characterised in that: step 2
In, maintain 30 DEG C ± 0.5 DEG C in dispensing containers of temperature constant state；In step 3, when maintaining 7 × 24 hours probiotics fermentions
Between.
3. a kind of plant extract complex function drink preparation method according to claim 1, it is characterised in that: the configuration
Container includes the closed tank body of lateral cylindricality (12), is laterally columnar configuration chamber (14) in the closed tank body of cylindricality (12),
The upside of the tank body (12) is connected with feed pipe (6), and the downside of the tank body (12) is connected with discharge nozzle (11)；
The first shut-off valve (7) and the second shut-off valve (10) are separately installed on the feed pipe (6) and discharge nozzle (11)；The vapor tight tank
It is also provided with and communicated with exhaust pipe (9) on the upside of body (12), relief valve, exhaust pipe (9) outlet is provided on the exhaust pipe (9)
It is provided with gaseous sphere spray head (9.1)；
It further include barotropic gas supply pipe (1), pneumatic filter (2), gas thermostatic heater (3), level-one current divider box (38)；Institute
The outlet side connection for stating barotropic gas supply pipe (1) connects the inlet end of the pneumatic filter (2), the pneumatic filter
(2) outlet side is connected to the inlet end of the gas thermostatic heater (3), and the outlet side of the gas thermostatic heater (3) connects
Lead to the inlet end of the level-one current divider box (38)；
It further include second level current divider box (4), the two second level current divider boxes (4) are symmetrically disposed on the closed tank body (12) external two
Side, and the two second level current divider boxes (4) are connected to the level-one current divider box (38) by two gas-guide tubes (37) respectively；
The bubble injection pipe (5) of several hard is respectively connected on each second level current divider box (4), on single second level current divider box (4)
Several hard bubble injection pipe (5) along the equidistant array distribution of closed tank body (12) axis direction；And each hard
Gas outlet (15) end of bubble injection pipe (5) protrude into that the configuration chamber (14) is interior, and bubble injection pipe (5) protrudes into the configuration
Part in chamber (14) is affixed on the circular arc inner wall distribution of configuration chamber (14)；It is affixed on several bubbles note of configuration chamber (14) inner wall
Enter pipe (5) at spiral bending curvature；
The two second level current divider boxes (4) are respectively the first current divider box (4.1) and the second current divider box (4.2), first current divider box
(4.1) and on the second current divider box (4.2) each bubble injection pipe (5) connected is respectively first bubble injection pipe array (5) and
Two bubble injection pipe arrays (5.2)；The each gas outlet of the first bubble injection pipe array (5) (15) and the second bubble injection pipe
Each gas outlet (15) of array (5.2) is in alternately cross-distribution in configuration chamber (14) bottom.
4. a kind of plant extract complex function drink preparation method according to claim 3, it is characterised in that: the cylindricality
Observation window (13) are also set up on the upside of closed tank body (12)；Being provided on each bubble injection pipe (5) prevents liquid reflux
Check valve further includes temperature indicator in tank (51) on the closed tank body (12), and setting is also shunted on the discharge nozzle (11)
There is product control isocon (52).
5. a kind of plant extract complex function drink preparation method according to claim 4, it is characterised in that: the gas
Constent temperature heater (3) includes columned outer cylinder (28), there is uniformly distributed hollow out on the cylinder wall surface of the columned outer cylinder (28)
Several first gas ports (26), one end of the columned outer cylinder (28) is inlet end (36), the other end is outlet side (29)；
The concentric circle that is provided in the inside by near outgassing end (29) of the outer cylinder (28) every disk (20), lean on every disk (20) by the circle
The side of nearly inlet end (36) is concentric to be provided with outer heat exchanger tube (32), outer heat exchanger tube (32) outer wall and the outer cylinder (28)
Air inlet heat exchanger channels (33) are formed between inner wall, the end of the air inlet heat exchanger channels (33) is connected to the inlet end (36), institute
It states outer heat exchanger tube (32) and round one end integrated coaxial heart every disk (20) is provided with coniform drainage cone (27),
The tip direction of the drainage cone (27) is opposite with the airintake direction of the inlet end (36)；
It is also concentric in the outer heat exchanger tube (32) to be provided with interior heat exchanger tube (31), on the cylinder wall surface of the interior heat exchanger tube (31)
Uniformly distributed hollow out has several second gas ports (34), forms heating wire between the interior heat exchanger tube (31) and the outer heat exchanger tube (32)
It spirals interlayer (21)；It further include the heater (23) of graphene electric heating cloth material, the heater of the graphene electric heating cloth material
(23) spiral spiral is set to the heating wire and spirals in interlayer (21)；Gas is formed in the cylinder of the interior heat exchanger tube (31)
It disturbs column chamber (25), concentric rotation is provided with disturbance shaft (22), the disturbance shaft in gas disturbance column chamber (25)
(22) array distribution has several disturbance rotating vanes in the axial direction on；It is also fixedly installed in gas disturbance column chamber (25)
Rotating shaft electric motor (35), the rotating shaft electric motor (35) and the disturbance shaft (22) are drivingly connected；The round disk every disk (20)
Face is additionally provided with several ventholes (30), and the outlet side (29) and gas are disturbed column chamber (25) phase by each venthole (30)
It is intercommunicated；Temperature sensor is additionally provided at the outlet side (29).
6. plant extract complex function drink preparation proportion according to claim 1, it is characterised in that: configure the drink
Raw material proportioning substance is made of according to weight percent following component:
Carbon source: 8% -15%；
Plant extracts: 10% -20%；
Surplus is water.
7. plant extract complex function drink preparation proportion according to claim 6, it is characterised in that: the carbon source is Portugal
Grape sugar.
8. plant extract complex function drink preparation proportion according to claim 6, it is characterised in that: the plant extract
Object is made of according to weight percent following component:
Xylo-oligosaccharide: 2% -3%；
Sessileflower Acanthopanax Bark: 2% -3%；
Aloe barbadensis Miller: 2% -3%；
Galactooligosaccharide: 2% -3%；
Isomalt: 2% -3%；
Plant stanol ester: 2% -3%；
Pearl Gly-His-Lys: 2% -3%；
Inulin: 5.5% -6.5%；
Polyfructosan: 2% -3%；
Seed of bark of eucommia: 2% -3%；
Phytosterol: 2% -3%；
Arachidonic acid: 2% -3%；
Aobvious arteries and veins Inula britannica chinensis: 2% -3%；
Noni puree: 2% -3%；
Yeast beta-dextran: 2% -3%；
Saussurea involucrata culture: 2% -3%；
Haematococcus: 2% -3%；
Samara: 2% -3%；
Acer truncatum: 2% -3%；
Pueraria root powder: 2% -3%；
Wheat oligopeptide: 2.5% -3.5%；
Ginseng: 2% -3%；
Chlorella pyrenoidosa: 2% -3%；
Combined spicebush leaf: 2% -3%；
Suaeda salsa seed: 2% -3%；
U.S. rattan fruit: 2% -3%；
Rhus glabra: 2% -3%；
Cordyceps militaris sporocarp: 2% -3%；
Ah Say fruit: 2% -3%；
Euglena: 2% -3%；
Smooth bark Lai wood fruit: 2% -3%；
Qingqian Willow leaf: 2% -3%；
Ampelopsis grossdentata leaf: 2% -3%；
Silybum marianum seed: 2% -3%；
Eucommia Bark male flower: 2% -3%；
Odd Asia seed: 2% -3%；
Circle bud isapgol husk: 2% -3%；
Line leaf broom top: 2% -3%；
Leaf of Moringa: 2% -3%.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116616391A (en) * | 2023-05-29 | 2023-08-22 | 海南丰席树诺丽产业有限责任公司 | A kind of preparation technology of high-efficiency Noni fruit fermented beverage |
| CN118044577A (en) * | 2024-03-14 | 2024-05-17 | 保利国氏生态农业开发河北有限公司 | Beverage and its processing method and application as health beverage |
| CN118356689A (en) * | 2024-05-20 | 2024-07-19 | 江苏元易邦生物科技有限公司 | A lysine production device with a defoaming structure |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202124625U (en) * | 2011-07-01 | 2012-01-25 | 南京润泽生物工程设备有限公司 | Multifunctional biological solid fermentation tank |
| CN102985524A (en) * | 2010-06-21 | 2013-03-20 | L.A.S.I.有限公司 | Fermentation device |
| CN203159595U (en) * | 2013-04-02 | 2013-08-28 | 广西中盟世纪环保咨询有限责任公司 | Zymocyte culture apparatus for household garbage pretreatment |
| CN103876155A (en) * | 2014-04-01 | 2014-06-25 | 田雷 | Composite plant enzyme containing probiotics and application of composite plant enzyme |
| CN105077464A (en) * | 2014-05-19 | 2015-11-25 | 金英旭 | Preparation method for vegetable lactic drinks process by using lactic acid fermented solution |
| CN105360864A (en) * | 2015-12-01 | 2016-03-02 | 中食月太(北京)健康科技有限公司 | Preparation method of enzyme beverage |
| CN206447884U (en) * | 2016-12-29 | 2017-08-29 | 交通运输部天津水运工程科学研究所 | It is mixed device |
| CN108175091A (en) * | 2017-12-29 | 2018-06-19 | 黄冈师范学院 | A kind of preparation method of the composite enzyme with antioxidant activity |
-
2018
- 2018-08-22 CN CN201810958815.9A patent/CN109043262A/en not_active Withdrawn
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102985524A (en) * | 2010-06-21 | 2013-03-20 | L.A.S.I.有限公司 | Fermentation device |
| CN202124625U (en) * | 2011-07-01 | 2012-01-25 | 南京润泽生物工程设备有限公司 | Multifunctional biological solid fermentation tank |
| CN203159595U (en) * | 2013-04-02 | 2013-08-28 | 广西中盟世纪环保咨询有限责任公司 | Zymocyte culture apparatus for household garbage pretreatment |
| CN103876155A (en) * | 2014-04-01 | 2014-06-25 | 田雷 | Composite plant enzyme containing probiotics and application of composite plant enzyme |
| CN105077464A (en) * | 2014-05-19 | 2015-11-25 | 金英旭 | Preparation method for vegetable lactic drinks process by using lactic acid fermented solution |
| CN105360864A (en) * | 2015-12-01 | 2016-03-02 | 中食月太(北京)健康科技有限公司 | Preparation method of enzyme beverage |
| CN206447884U (en) * | 2016-12-29 | 2017-08-29 | 交通运输部天津水运工程科学研究所 | It is mixed device |
| CN108175091A (en) * | 2017-12-29 | 2018-06-19 | 黄冈师范学院 | A kind of preparation method of the composite enzyme with antioxidant activity |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116616391A (en) * | 2023-05-29 | 2023-08-22 | 海南丰席树诺丽产业有限责任公司 | A kind of preparation technology of high-efficiency Noni fruit fermented beverage |
| CN118044577A (en) * | 2024-03-14 | 2024-05-17 | 保利国氏生态农业开发河北有限公司 | Beverage and its processing method and application as health beverage |
| CN118356689A (en) * | 2024-05-20 | 2024-07-19 | 江苏元易邦生物科技有限公司 | A lysine production device with a defoaming structure |
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