CN109136068A - Preparation system, component proportion and its method of probiotics fermented beverage - Google Patents
Preparation system, component proportion and its method of probiotics fermented beverage Download PDFInfo
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- CN109136068A CN109136068A CN201811012679.0A CN201811012679A CN109136068A CN 109136068 A CN109136068 A CN 109136068A CN 201811012679 A CN201811012679 A CN 201811012679A CN 109136068 A CN109136068 A CN 109136068A
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- 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
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- 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
- A23L2/38—Other non-alcoholic beverages
- A23L2/382—Other non-alcoholic beverages fermented
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- 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
- C12M29/00—Means for introduction, extraction or recirculation of materials, e.g. pumps
- C12M29/06—Nozzles; Sprayers; Spargers; Diffusers
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Abstract
The invention discloses a kind of preparation system stoste of probiotics fermented beverage configuration cylinder, drinkable water storage element, aerated fermentation tank and finished product splicing containers；The water outlet of the drinkable water storage element connects the water inlet end that the stoste configures cylinder by aqueduct, is also provided with and communicated with material feeding tube on one end upside of the stoste configuration cylinder, is provided with loading hopper on the material feeding tube；The stoste discharge end of the stoste configuration cylinder connects the feed end of the aerated fermentation tank top by feed pipe；Structure of the invention is simple, and fusion mixes rapidly under the continuous agitation of flood dragon blade for drinkable water and raw material, forms fermenation raw liquid；The second electromagnetic liquid valve is opened at the same time, and starts liquid pump, and then the mixed fermenation raw liquid mixed in channel that twists of stoste is continuously pumped into aerated fermentation tank by liquid pump, the liquid for keeping the stoste entered in aerated fermentation tank substantially uniform.
Description
Technical field
The invention belongs to the preparation system of probiotics fermention field more particularly to probiotics fermented beverage, component proportion and
Its method.
Background technique
Probiotics fermented beverage has thick taste, feature easy to digest and absorb；The fermentation liquid of existing fermented beverage is sent out
It tends to generate precipitating during ferment, causes product homogeneity bad, and the aeration head in existing fermentor is often adopted
With fixed aeration head, equally there is also be aerated non-uniform situation.
Summary of the invention
Goal of the invention: in order to overcome the deficiencies in the prior art, the present invention provides a kind of aeration uniformly, prevents from precipitating
Probiotics fermented beverage preparation system, component proportion and its method.
Technical solution: to achieve the above object, a kind of preparation system of probiotics fermented beverage of the invention, including stoste
Configure cylinder, drinkable water storage element, aerated fermentation tank and finished product splicing container；
The water outlet of the drinkable water storage element connects the water inlet end that the stoste configures cylinder, the original by aqueduct
It is also provided with and communicated with material feeding tube on the upside of one end of liquid configuration cylinder, is provided with loading hopper on the material feeding tube；Institute
The stoste discharge end for stating stoste configuration cylinder connects the feed end of the aerated fermentation tank top by feed pipe；The aerated fermentation
The discharge end of pot bottom connects the feed end of the finished product splicing container by discharge duct, and the first electricity is provided on the aqueduct
Magnetic liquid valve is provided with the second electromagnetic liquid valve on the feed pipe, is additionally provided with third electromagnetic liquid valve on the discharge duct, it is described into
Liquid pump is additionally provided in expects pipe, the liquid that the liquid pump can configure stoste in cylinder is pumped into the aerated fermentation tank.
Further, tapered discharge head is arranged in the discharge end of the stoste configuration cylinder, going out in the taper discharge head
Liquid cone chamber is connected to the liquid feeding end of the feed pipe；It is concentric in the stoste configuration cylinder to be provided with agitation blades axis, the agitation
New results stoste is mixed between sharf outer wall and stoste configuration cylinder inner wall twists channel, and the mixed channel that twists of the stoste is far from described
One end of taper discharge head is connected to the material feeding tube, and the agitation blades axis is rotated far from one end of the taper discharge head
It is pierced by the stoste configuration cylinder, agitation blades axle position spirals in one section of outer wall integration in stoste configuration cylinder and is provided with strand
Imperial blade, the flood dragon blade outer rim and the stoste configure cylinder inner wall clearance fit；Agitation blades axle position is matched in the stoste
It sets and is synchronously arranged with belt pulley on one outside cylinder section of outer wall；It further include belt motor, the belt motor is driven by belt
Unit is drivingly connected the belt pulley；
Concentric inside the agitation blades axis to be provided with liquid-conveying ducts, the liquid-conveying ducts are close to the taper discharge head
It is closed at one end；The one end of the agitation blades axis far from the taper discharge head passes through the first sealing bearing and the aqueduct
Discharge end rotation socket；The liquid-conveying ducts are connected to the aqueduct discharge end far from one end of the taper discharge head；
The liquid-conveying ducts, which are located on the mixed one section of inner wall twisted in channel of stoste, waits matrixs column to be provided with several liquid injection holes, respectively
The liquid-conveying ducts and the mixed channel that twists of stoste are interconnected by the liquid injection hole；The cone chamber of liquid out and the mixed strand channel of the stoste
Between be provided with filter disc, several filter openings are provided on the filter disc.
Further, start belt motor, so that agitation blades axis is in continuous agitated conditions, at the same time to loading hopper
Middle blanking is used for the raw material of fermentation reaction, and then under the agitation of flood dragon blade, and raw material leads in mixed twist of entire stoste
Play in road, opens the first electromagnetic liquid valve at the same time, and the water outlet of drinkable water storage element enters edible to drain in-passage pressure
Water, and then the drinkable water in liquid-conveying ducts is uniformly pressed into the mixed strand channel of stoste by several liquid injection holes, and then drinkable water and original
Fusion mixes material matter rapidly under the continuous agitation of flood dragon blade, forms fermenation raw liquid；The second electromagnetic liquid is opened at the same time
Valve, and start liquid pump, and then the mixed fermenation raw liquid mixed in channel that twists of stoste is continuously pumped into aerated fermentation tank by liquid pump.
It further, is cylindricality fermentation stir chamber inside the aerated fermentation tank；Also concentric setting in the stir chamber
There is columnar sink-float stirring body, sink-float stirring body integration from top to bottom includes that upper section drains cone, middle section airbag housing
Cone is drained with lower section；The cone point of the upper section drainage cone is concentric to be arranged upward, the cone of the upper section drainage cone
Shape tip is arranged downward, and the middle section airbag housing is Cylindrical housing structure；The inner cavity of the middle section airbag housing is air bag
Extrusion chamber, the intracavitary flexible pressure accumulation air bag of setting of air sac pressing, the inside of the elasticity pressure accumulation air bag is Air pressure accumulation chamber；
The wall body of the middle section airbag housing is evenly equipped with several teeter columns in divergent shape, is arranged along its length inside each teeter column
There are liquid-conveying ducts, the air sac pressing chamber and fermentation stir chamber are interconnected by each liquid-conveying ducts；
The inside of the lower section drainage cone is hollow gas coning chamber out, and the lower section drains on the conical surface of cone circumferentially
Array is evenly equipped with several bubble leadout holes, and each bubble leadout hole is connected to the outlet connected inside the lower section drainage cone
Bore chamber；
Described to go out to be provided with partition between gas coning chamber and the air sac pressing chamber, the centre of the partition is vertically arranged
There are communicating pipe, the lower end connection of the communicating pipe gas coning chamber out, the air inlet of the communicating pipe upper end is connected to the air
The lower end of pressure accumulation chamber；
It is concentric on the top wall body of the fermentation stir chamber to be provided with sliding tube guide hole；It further include sliding vertically wind-guiding
Pipe, the sliding guide duct is concentric to slide through the sliding tube guide hole, and the concentric one in the sliding guide duct lower end
Change and connect the upper section drainage cone top, the sliding guide duct upper end is synchronously arranged with electric heating booster fan, the electricity
The air outlet of hot booster fan is connected to the sliding guide duct upper end, described in the air outlet of the sliding guide duct lower end is connected to
Air pressure accumulation chamber.
Further, the fermentation stir chamber top is additionally provided with relief tube；Gas overflow is provided on the relief tube
Relief valve；A quarter of the total volume of the sink-float stirring body not less than the fermentation stir chamber total measurement (volume)；The sliding is led
Conducting direction check valve directed downwardly is additionally provided in air hose；The upper section drainage cone is solid structure；The communicating pipe
It is internally provided with excess-flow valve；The downside of the gas coning chamber out is solid pointed cone bottom；Under elastic pressure accumulation air bag swelling state, institute
Stating sink-float stirring body can float in fermentation stir chamber.
Further, the component proportion of the fermenation raw liquid in the aerated fermentation tank is according to weight percent by following component
Composition:
Sucrose: 6% -11%；
Isomalt: 1.8% -2.5%；
Arachidonic acid: 1.5% -2.8%；
Wheat oligopeptide: 0.8% -2.5%；
Ah Say fruit: 1.8% -2.5%；
Rhus glabra: 0.8% -2.2%；
Qingqian Willow leaf: 2% -2.5%；
Fructose: 4% -5%；
Surplus is water.
The utility model has the advantages that structure of the invention is simple, drinkable water and raw material are rapid under the continuous agitation of flood dragon blade
Fusion mixes, and forms fermenation raw liquid；The second electromagnetic liquid valve is opened at the same time, and starts liquid pump, and then in the mixed strand channel of stoste
The fermenation raw liquid mixed is continuously pumped into aerated fermentation tank by liquid pump, makes the stoste entered in aerated fermentation tank substantially
One liquid.
Detailed description of the invention
Attached drawing 1 is overall structure of the present invention；
Attached drawing 2 is the whole cut-away diagram of the present invention；
Attached drawing 3 is that stoste configuration cylinder splits structural schematic diagram；
Attached drawing 4 is the schematic diagram that stoste configures cylinder and aqueduct junction；
Attached drawing 5 is sink-float stirring body structural schematic diagram；
Attached drawing 6 is that sink-float stirring body splits structural schematic diagram.
Specific embodiment
The present invention will be further explained with reference to the accompanying drawing.
A kind of preparation system of probiotics fermented beverage as shown in attached drawing 1 to 6, including stoste configure cylinder 70, drinkable water
Storage element 74, aerated fermentation tank 24 and finished product splicing container 93；
The water outlet of the drinkable water storage element 74 connects the water inlet end that the stoste configures cylinder 70 by aqueduct 61,
It is also provided with and communicated with material feeding tube 66 on the upside of one end of the stoste configuration cylinder 70, is provided on the material feeding tube 66
Loading hopper 72；The stoste discharge end of the stoste configuration cylinder 70 connects 24 top of aerated fermentation tank by feed pipe 26
Feed end；The discharge end of 24 bottom of aerated fermentation tank connects the charging of the finished product splicing container 93 by discharge duct 29
It holds, is provided with the first electromagnetic liquid valve 90 on the aqueduct 61, the second electromagnetic liquid valve 27 is provided on the feed pipe 26, it is described
It is additionally provided with third electromagnetic liquid valve 30 on discharge duct 29, liquid pump 71 is additionally provided on the feed pipe 26, the liquid pump 71 can incite somebody to action
Stoste configures the liquid in cylinder 70 and is pumped into the aerated fermentation tank 24.
Tapered discharge head 190 is arranged in the discharge end of the stoste configuration cylinder 70, goes out liquid in the taper discharge head 190
Cone chamber 96 is connected to the liquid feeding end of the feed pipe 26；It is concentric in the stoste configuration cylinder 70 to be provided with agitation blades axis 189, institute
It is mixed to state the mixed strand channel 68 of new results stoste, the stoste between 189 outer wall of agitation blades axis and stoste configuration 70 inner wall of cylinder
It twists channel 68 and is connected to the material feeding tube 66 far from one end of the taper discharge head 190, the agitation blades axis 189 is separate
One end rotation of the taper discharge head 190 is pierced by the stoste configuration cylinder 70, and agitation blades axis 189 is located at stoste configuration
One section of outer wall integration in cylinder 70, which is spiraled, is provided with packing auger blade 69, and 69 outer rim of flood dragon blade and the stoste configure cylinder
70 inner wall clearance fits；Agitation blades axis 189, which is located on one section of outer wall outside stoste configuration cylinder 70, is synchronously arranged with skin
Belt wheel 64；It further include belt motor 92, the belt motor 92 is drivingly connected the belt pulley 64 by belt gear unit 91；
189 inside of agitation blades axis is concentric to be provided with liquid-conveying ducts 65, and the liquid-conveying ducts 65 are close to the cone
Shape discharge head 190 it is closed at one end；The one end of the agitation blades axis 189 far from the taper discharge head 190 is close by first
It seals bearing 63 and 61 discharge end of aqueduct rotation is socketed；The liquid-conveying ducts 65 far from the taper discharge head 190 one
End is connected to 61 discharge end of aqueduct；
The liquid-conveying ducts 65, which are located on the mixed one section of inner wall twisted in channel 68 of stoste, waits matrixs column to be provided with several fluid injections
The liquid-conveying ducts 65 and the mixed channel 68 that twists of stoste are interconnected by hole 67, each liquid injection hole 67；It is described go out liquid cone chamber 96 with
The stoste mixed twist is provided with filter disc 95 between channel 68, and several filter openings 94 are provided on the filter disc 95.
The application method of stoste configuration cylinder: starting belt motor 92 makes agitation blades axis 189 be in continuous agitated conditions,
Raw material of the blanking for fermentation reaction into loading hopper 72 at the same time, the raw material of the present embodiment are Suaeda salsa
The plant extracts such as seed, U.S. rattan fruit, rhus glabra, Euglena；Fermenting carbon source is glucose sugar and saccharomycete, and then in flood dragon leaf
Under the agitation of piece 69, raw material play in the mixed strand channel 68 of entire stoste is opened the first electromagnetic liquid valve 90 at the same time, is eaten
Enter drinkable water to 65 internal pressure of liquid-conveying ducts with the water outlet of water storage element 74, and if then drinkable water in liquid-conveying ducts 65 by
Uniformly indentation stoste is mixed twists in channel 68 for dry liquid injection hole 67, and then drinkable water and raw material are in the continuous agitation of flood dragon blade 69
Lower fusion rapidly mixes, and forms fermenation raw liquid；The second electromagnetic liquid valve 27 is opened at the same time, and starts liquid pump 71, and then stoste
The mixed fermenation raw liquid mixed in channel 68 that twists continuously is pumped into aerated fermentation tank 24 by liquid pump 71.
It is cylindricality fermentation stir chamber 19 inside the aerated fermentation tank 24；It is also concentric in the stir chamber 19 to be provided with column
The sink-float stirring body 18 of shape, the sink-float stirring body 18 integration from top to bottom include that upper section drains cone 1, middle section airbag housing
14 and lower section drain cone 10；The cone point of the upper section drainage cone 1 is concentric to be arranged upward, and upper section drains 1 He of cone
Lower section drainage cone 10 can reduce the running resistance that sink-float stirring body 18 floats and sinks, the cone of the upper section drainage cone 1
Shape tip is arranged downward, and the middle section airbag housing 14 is Cylindrical housing structure；The inner cavity of the middle section airbag housing 14 is
Air sac pressing chamber 2, the interior flexible pressure accumulation air bag 3 of setting of the air sac pressing chamber 2, the inside of the elasticity pressure accumulation air bag 3 is sky
Gas pressure accumulation chamber 4；The wall body of the middle section airbag housing 14 is evenly equipped with several teeter columns 13 in divergent shape, in each teeter column 13
Portion is provided with liquid-conveying ducts 12 along its length, and each liquid-conveying ducts 12 are by the air sac pressing chamber 2 and fermentation stir chamber 19
It is interconnected；
The inside of the lower section drainage cone 10 is hollow gas coning chamber 6 out, and the lower section drains on the conical surface of cone 10
Circumferentially array is evenly equipped with several bubble leadout holes 7, and each bubble leadout hole 7 is connected to the connection lower section drainage cone 10
Internal goes out gas coning chamber 6；
Described to go out to be provided with partition 11 between gas coning chamber 6 and the air sac pressing chamber 2, the centre of the partition 11 is perpendicular
To communicating pipe 8, the lower end connection of the communicating pipe 8 gas coning chamber 6 out is provided with, the air inlet 5 of 8 upper end of communicating pipe connects
Lead to the lower end of the Air pressure accumulation chamber 4；
It is concentric on the top wall body 19.1 of the fermentation stir chamber 19 to be provided with sliding tube guide hole 22；It further include vertical cunning
Dynamic guide duct 16, the sliding guide duct 16 is concentric to slide through the sliding tube guide hole 22, and the sliding guide duct 16
The concentric integration in lower end connects 1 top of upper section drainage cone, and 16 upper end of sliding guide duct is synchronously arranged with electric heating
The air outlet of booster fan 25, the electric heating booster fan 25 is connected to 16 upper end of sliding guide duct, and the sliding is led
The air outlet 15 of 16 lower end of air hose is connected to the Air pressure accumulation chamber 4.
19 top of fermentation stir chamber is additionally provided with relief tube 32；Gas overflow pressure release is provided on the relief tube 32
Valve 31；A quarter of the total volume of the sink-float stirring body 18 not less than fermentation 19 total measurement (volume) of stir chamber；The sliding
Conducting direction check valve 21 directed downwardly is additionally provided in guide duct 16；The upper section drainage cone 1 is solid structure；The company
Siphunculus 8 is internally provided with excess-flow valve；The downside of the gas coning chamber 6 out is solid pointed cone bottom 9；Elastic pressure accumulation air bag 3 is swollen
Under swollen state, the sink-float stirring body 18 can float in fermentation stir chamber 19.
The fermentation aeration system process of the preparation system of the probiotics fermented beverage of this programme and technological progress arrange as follows:
Preparation stage: drink to be fermented is continuously introduced into fermentation stir chamber 19 by feed pipe 26 and configures liquid and corresponding
Get well the probiotics of fermenting that itches, wait the liquid level in stir chamber 19 of fermenting be more than container 3/4ths when start the second electromagnetic liquid valve 27,
Stop feeding to fermentation stir chamber 19；At this time since electric heating booster fan 25 is in inactive state, in fermentation stir chamber 19
Under interior liquid pressure effect, the fermentation liquid in stir chamber 19 of fermenting is imported by the liquid-conveying ducts 12 in each teeter column 13
In air sac pressing chamber 2, and elastic pressure accumulation air bag 3 is inwardly squeezed, and then gradually taper up elastic pressure accumulation air bag 3, gradually tapered up
Elastic pressure accumulation air bag 3, which passes through the air in its Air pressure accumulation chamber 4, is squeezed into out gas coning chamber 6 communicating pipe 8, and by each several
Bubble leadout hole 7 is expelled in fermentation stir chamber 19 in the form of bubble, is become smaller since elastic pressure accumulation air bag 3 gradually tapers up, into
And gradually decrease down buoyancy suffered by sink-float stirring body 18 lower than own wt, and then the stirring body 18 that rises and falls sinks down into fermentation stirring
The bottom of chamber of chamber 19；
Cycle stage: air is pressed into elastic pressure accumulation air bag 3 rapidly by starting electric heating booster fan 25, booster fan 25
Air pressure accumulation chamber 4 in, make the expansion rapidly of elastic pressure accumulation air bag 3, elastic pressure accumulation air bag 3 extruding gasbag extrusion chamber 2 rapidly outward,
And then the fermentation liquid in air sac pressing chamber 2 is logical by the drain passed through in each teeter column 13 after the extruding of elastic pressure accumulation air bag 3
Road 12 is exported in fermentation stir chamber 19；The pause when elastic pressure accumulation air bag 3 is expanded into full of middle section 14 inner cavity of airbag housing
Booster fan 25；At this time due to the expansion of elastic pressure accumulation air bag 3, it is promoted to buoyancy suffered by sink-float stirring body 18 rapidly and is greater than certainly
Body gravity；And then the stirring body 18 that rises and falls starts gradually to do upward floating movement；
At the same time, the gas pressure intensity of the 3 inner air pressure accumulation chamber 4 of elastic pressure accumulation air bag under swelling state is greater than fermentation and stirs
Mix the pressure in chamber 19, thus the pressure accumulation air in Air pressure accumulation chamber 4 is by being continuously expressed into out in gas coning chamber 6 communicating pipe 8, and
And out the air in gas coning chamber 6 each several continuous uniforms in the form of bubble of bubble leadout hole 7 diffuse to fermentation stirring
In chamber 19, and then the oxygen continuous uniform in bubble is dissolved in and promotes to ferment in fermentation liquid, due to the storage in Air pressure accumulation chamber 4
Pressure air is gradually discharged, and then elastic pressure accumulation air bag 3 starts to gradually taper up and becomes smaller in 18 floating-upward process of stirring body that makes to rise and fall；With
Elastic pressure accumulation air bag 3 gradually taper up and become smaller, and then the buoyancy suffered by stirring body 18 that rises and falls gradually becomes smaller, and sink-float stirring body 18 floats
The fermentation liquid to ferment in stir chamber 19 in the process imported into air sac pressing by the liquid-conveying ducts 12 in each teeter column 13 again
In chamber 2, as buoyancy suffered by sink-float stirring body 18 is gradually decreased down lower than own wt, the stirring body 18 that rises and falls starts by floating shape
State is changed into slow sinking state, and gradually sinks down into the bottom of chamber of fermentation stir chamber 19 again；Stirring body 18 to be risen and fallen sinks
To fermentation stir chamber 19 bottom of chamber when restart electric heating booster fan 25, booster fan 25 rapidly by air be pressed into elasticity store
In Air pressure accumulation chamber 4 in pressuring gasbag 3, make the elastic expansion rapidly of pressure accumulation air bag 3, elastic pressure accumulation air bag 3 squeezes rapidly gas outward
Capsule extrusion chamber 2, so the fermentation liquid in air sac pressing chamber 2 by after the extruding of elastic pressure accumulation air bag 3 pass through each teeter column 13
Interior liquid-conveying ducts 12 are exported to again in fermentation stir chamber 19；So far sink-float stirring body 18 complete floating, sink one
A period；Gas extra in fermentation stir chamber 19 is continuously discharged in gas overflow relief valve 31 in the above process, and then lets out immediately
Air pressure in hair loss ferment stir chamber 19, the period stirring movement for maintaining sink-float stirring body 18 to float, sink；According to this rule, sink
Floating stirring body 18 does the stirring periodically floated and sunk repeatedly and aeration movement in fermentation stir chamber 19, and then makes to ferment
Liquid in stir chamber 19 is in lasting play up and down and effectively prevent precipitating, the sink-float stirring body 18 moved repeatedly up and down
Aeration in fermentation stir chamber 19 is more uniform, and then it is more uniform to be dissolved in the oxygen in fermentation liquid；In sink-float stirring body
The liquid-conveying ducts 12 that fermentation liquid during 18 floatings and sinking in air sac pressing chamber 2 is iterated through in each teeter column 13
Indentation and extrusion further promote the fermentation liquid in fermentation stir chamber 19 to homogenize, keep fermentation process more uniform；
Discharging phase: when needing discharging, start electric heating booster fan 25, and maintain the operation of electric heating booster fan 25
State, and then elastic pressure accumulation air bag 3 is made to be in constant expanded state, and then make during elastic pressure accumulation air bag 3 is expanded into and is persistently full of
The inner cavity of section airbag housing 14, and then make the fermentation liquid in air sac pressing chamber 2 is complete to be expelled in fermentation stir chamber 19；Then it opens
Third electromagnetic liquid valve 30, and then the fermentation liquid of fermented completion is discharged from discharge duct 29 in stir chamber 19 of fermenting.
The probiotics of the present embodiment is using saccharomycete；The group of fermenation raw liquid in the aerated fermentation tank (24) is distributed
Than being made of according to weight percent following component:
Sucrose: 6% -11%；
Isomalt: 1.8% -2.5%；
Arachidonic acid: 1.5% -2.8%；
Wheat oligopeptide: 0.8% -2.5%；
Ah Say fruit: 1.8% -2.5%；
Rhus glabra: 0.8% -2.2%；
Qingqian Willow leaf: 2% -2.5%；
Fructose: 4% -5%；
Surplus is water.
32 DEG C ± 0.5 DEG C of temperature constant state in the predetermined fermentation stir chamber of the present embodiment, when 7 × 24 hours probiotics fermentions
Between；
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 (6)
1. a kind of preparation system of probiotics fermented beverage, it is characterised in that: single including stoste configuration cylinder (70), drinkable water storage
First (74), aerated fermentation tank (24) and finished product splicing container (93)；
The water outlet of the drinkable water storage element (74) connects the water inlet of stoste configuration cylinder (70) by aqueduct (61)
End, the stoste configure on the upside of the one end of cylinder (70) and are also provided with and communicated with material feeding tube (66), the material feeding tube
(66) loading hopper (72) are provided on；The stoste discharge end of stoste configuration cylinder (70) passes through described in feed pipe (26) connection
Feed end at the top of aerated fermentation tank (24)；The discharge end of aerated fermentation tank (24) bottom connects institute by discharge duct (29)
The feed end of finished product splicing container (93) is stated, the first electromagnetic liquid valve (90), the feed pipe are provided on the aqueduct (61)
(26) be provided with the second electromagnetic liquid valve (27) on, be additionally provided with third electromagnetic liquid valve (30) on the discharge duct (29), it is described into
It is additionally provided in expects pipe (26) liquid pump (71), the liquid that the liquid pump (71) can configure stoste in cylinder (70) is pumped into the aeration
In fermentor (24).
2. a kind of preparation system of probiotics fermented beverage according to claim 1, it is characterised in that: the stoste configuration
Tapered discharge head (190) is arranged in the discharge end of cylinder (70), and liquid cone chamber (96) that goes out in the taper discharge head (190) is connected to institute
State the liquid feeding end of feed pipe (26)；It is concentric in stoste configuration cylinder (70) to be provided with agitation blades axis (189), the agitation
New results stoste is mixed between sharf (189) outer wall and stoste configuration cylinder (70) inner wall twists channel (68), and the stoste is mixed
It twists channel (68) and is connected to the material feeding tube (66), the agitation blades axis far from one end of the taper discharge head (190)
(189) one end rotation far from the taper discharge head (190) is pierced by stoste configuration cylinder (70), agitation blades axis (189)
One section of outer wall integration in stoste configuration cylinder (70), which is spiraled, to be provided with packing auger blade (69), the flood dragon blade
(69) outer rim and the stoste configure cylinder (70) inner wall clearance fit；Agitation blades axis (189) is located at stoste configuration cylinder
(70) belt pulley (64) are synchronously arranged on one section of external outer wall；It further include belt motor (92), the belt motor (92)
The belt pulley (64) is drivingly connected by belt gear unit (91)；
Agitation blades axis (189) inside is concentric to be provided with liquid-conveying ducts (65), and the liquid-conveying ducts (65) are close to described
Taper discharge head (190) it is closed at one end；The one end of the agitation blades axis (189) far from the taper discharge head (190) is logical
It crosses the first sealing bearing (63) and the rotation of the aqueduct (61) discharge end is socketed；The liquid-conveying ducts (65) are far from the taper
One end of discharge head (190) is connected to aqueduct (61) discharge end；
The liquid-conveying ducts (65), which are located on the mixed one section of inner wall twisted in channel (68) of stoste, waits matrixs column to be provided with several fluid injections
Mixed twist channel (68) in the liquid-conveying ducts (65) and stoste are interconnected by hole (67), each liquid injection hole (67)；The liquid out
Cone chamber (96) and the stoste mixed twist are provided with filter disc (95) between channel (68), are provided with several filter openings on the filter disc (95)
(94)。
3. the application method of stoste configuration cylinder according to claim 2, it is characterised in that: starting belt motor (92) makes
Agitation blades axis (189) is in continuous agitated conditions, at the same time original of the blanking for fermentation reaction in loading hopper (72)
Material matter, and then under the agitation of flood dragon blade (69), raw material play in mixed strand channel (68) of entire stoste is same with this
When open the first electromagnetic liquid valve (90), the water outlet of drinkable water storage element (74) enters drinkable water to liquid-conveying ducts (65) internal pressure,
And then the drinkable water in liquid-conveying ducts (65) by several liquid injection holes (67), uniformly mix in strand channel (68) by indentation stoste, and then eats
With water and raw material, fusion is mixed rapidly under the continuous agitation of flood dragon blade (69), forms fermenation raw liquid；It beats at the same time
The fermenation raw liquid quilt opened the second electromagnetic liquid valve (27), and start liquid pump (71), and then mixed in mixed strand channel (68) of stoste
Liquid pump (71) is continuously pumped into aerated fermentation tank (24).
4. a kind of preparation system of probiotics fermented beverage according to claim 1, it is characterised in that: the aerated fermentation
It is that cylindricality ferments stir chamber (19) inside tank (24)；It is also concentric in the stir chamber (19) to be provided with columnar sink-float stirring body
(18), the sink-float stirring body (18) from top to bottom integration include upper section drainage cone (1), middle section airbag housing (14) and under
Duan Yinliu cone (10)；The cone point of upper section drainage cone (1) is concentric to be arranged upward, and the upper section drains cone
(1) cone point is arranged downward, and the middle section airbag housing (14) is Cylindrical housing structure；The middle section airbag housing
(14) inner cavity is air sac pressing chamber (2), and the flexible pressure accumulation air bag (3) of setting in the air sac pressing chamber (2), the elasticity stores
The inside of pressuring gasbag (3) is Air pressure accumulation chamber (4)；The wall body of the middle section airbag housing (14) is evenly equipped with several stir in divergent shape
It mixes column (13), is provided with along its length liquid-conveying ducts (12) inside each teeter column (13), each liquid-conveying ducts (12)
The air sac pressing chamber (2) and fermentation stir chamber (19) are interconnected；
The inside of lower section drainage cone (10) goes out gas coning chamber (6) for hollow, the conical surface of lower section drainage cone (10)
On circumferentially array be evenly equipped with several bubble leadout holes (7), each bubble leadout hole (7) is connected to the connection lower section drainage
Cone (10) inside goes out gas coning chamber (6)；
It is described to go out to be provided between gas coning chamber (6) and the air sac pressing chamber (2) partition (11), the central part of the partition (11)
Position is vertically provided with communicating pipe (8), and the lower end connection of the communicating pipe (8) is described out gas coning chamber (6), on the communicating pipe (8)
The air inlet (5) at end is connected to the lower end of the Air pressure accumulation chamber (4)；
It is concentric on the top wall body (19.1) of fermentation stir chamber (19) to be provided with sliding tube guide hole (22)；It further include vertical
It slides guide duct (16), the sliding guide duct (16) is concentric to slide through the sliding tube guide hole (22), and the sliding
The concentric integration in guide duct (16) lower end connects at the top of upper section drainage cone (1), sliding guide duct (16) upper end
It is synchronously arranged with electric heating booster fan (25), the air outlet of the electric heating booster fan (25) is connected to the sliding guide duct
(16) air outlet (15) of upper end, described sliding guide duct (16) lower end is connected to the Air pressure accumulation chamber (4).
5. a kind of preparation system of probiotics fermented beverage according to claim 4, it is characterised in that: the fermentation stirring
Chamber (19) top is additionally provided with relief tube (32)；Gas overflow relief valve (31) are provided on the relief tube (32)；It is described heavy
A quarter of the total volume of floating stirring body (18) not less than described fermentation stir chamber (19) total measurement (volume)；The sliding guide duct
(16) conducting direction check valve directed downwardly (21) is additionally provided in；Upper section drainage cone (1) is solid structure；The company
Siphunculus (8) is internally provided with excess-flow valve；The downside of gas coning chamber (6) out is solid pointed cone bottom (9)；Elastic pressure accumulation gas
Under capsule (3) swelling state, the sink-float stirring body (18) can be floated in fermentation stir chamber (19).
6. a kind of component proportion of probiotics fermented beverage according to claim 1, it is characterised in that: the aerated fermentation
The component proportion of fermenation raw liquid in tank (24) is made of according to weight percent following component:
Sucrose: 6% -11%；
Isomalt: 1.8% -2.5%；
Arachidonic acid: 1.5% -2.8%；
Wheat oligopeptide: 0.8% -2.5%；
Ah Say fruit: 1.8% -2.5%；
Rhus glabra: 0.8% -2.2%；
Qingqian Willow leaf: 2% -2.5%；
Fructose: 4% -5%；
Surplus is water.
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI921611A (en) * | 1991-04-12 | 1992-10-13 | Forschungszentrum Juelich Gmbh | FREQUENCY FRAME FOR ALCOHOLIC FREQUENCY OR OIL FORWARDING |
| CN201923875U (en) * | 2010-12-17 | 2011-08-10 | 浙江泰来环保科技有限公司 | Aeration machine |
| CN102839121A (en) * | 2012-09-21 | 2012-12-26 | 中国环境科学研究院 | Small-size biological hydrogen-producing device for rural family |
| CN104918689A (en) * | 2012-11-15 | 2015-09-16 | 水处理及矿业有限公司 | Systems and methods for diffusing gas into a liquid |
| RU172189U1 (en) * | 2015-12-02 | 2017-06-30 | Федеральное государственное учреждение "Федеральный исследовательский центр "Фундаментальные основы биотехнологии" Российской академии наук" (ФИЦ Биотехнологии РАН) | Anaerobic acidogenic bioreactor for preparing organic solid waste fraction together with activated sludge of aeration tanks of a sewage treatment plant for fermentation to produce biogas |
| CN108383065A (en) * | 2018-03-23 | 2018-08-10 | 南通劲凌智能科技有限公司 | A kind of jam food filling apparatus and its method |
-
2018
- 2018-08-31 CN CN201811012679.0A patent/CN109136068B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI921611A (en) * | 1991-04-12 | 1992-10-13 | Forschungszentrum Juelich Gmbh | FREQUENCY FRAME FOR ALCOHOLIC FREQUENCY OR OIL FORWARDING |
| CN201923875U (en) * | 2010-12-17 | 2011-08-10 | 浙江泰来环保科技有限公司 | Aeration machine |
| CN102839121A (en) * | 2012-09-21 | 2012-12-26 | 中国环境科学研究院 | Small-size biological hydrogen-producing device for rural family |
| CN104918689A (en) * | 2012-11-15 | 2015-09-16 | 水处理及矿业有限公司 | Systems and methods for diffusing gas into a liquid |
| RU172189U1 (en) * | 2015-12-02 | 2017-06-30 | Федеральное государственное учреждение "Федеральный исследовательский центр "Фундаментальные основы биотехнологии" Российской академии наук" (ФИЦ Биотехнологии РАН) | Anaerobic acidogenic bioreactor for preparing organic solid waste fraction together with activated sludge of aeration tanks of a sewage treatment plant for fermentation to produce biogas |
| CN108383065A (en) * | 2018-03-23 | 2018-08-10 | 南通劲凌智能科技有限公司 | A kind of jam food filling apparatus and its method |
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