CN109363216A - Composite feed compounding system and preparation method - Google Patents
Composite feed compounding system and preparation method Download PDFInfo
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- CN109363216A CN109363216A CN201811500049.8A CN201811500049A CN109363216A CN 109363216 A CN109363216 A CN 109363216A CN 201811500049 A CN201811500049 A CN 201811500049A CN 109363216 A CN109363216 A CN 109363216A
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N17/00—Apparatus specially adapted for preparing animal feeding-stuffs
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23N—MACHINES OR APPARATUS FOR TREATING HARVESTED FRUIT, VEGETABLES OR FLOWER BULBS IN BULK, NOT OTHERWISE PROVIDED FOR; PEELING VEGETABLES OR FRUIT IN BULK; APPARATUS FOR PREPARING ANIMAL FEEDING- STUFFS
- A23N17/00—Apparatus specially adapted for preparing animal feeding-stuffs
- A23N17/007—Apparatus specially adapted for preparing animal feeding-stuffs for mixing feeding-stuff components
Abstract
The invention discloses composite feed compounding systems, including insoluble ingredient pulverizing unit, fermenation raw liquid configuration unit, fermentor；Insoluble ingredient feed pipe, dissolubility ingredient feed pipe and fermentation magma discharge nozzle are respectively arranged in the fermenation raw liquid configuration unit；The slurry fermentation magma discharge nozzle connects the feed end of the fermentor；The discharge end of the insoluble ingredient pulverizing unit connects the insoluble ingredient feed pipe；It is persistently emerged into fermentation chamber in the form of bubble on gas tip, also containing in bubble while providing oxygen for the yeast probiotics in fermentation chamber has heat, the slurries in fermentation chamber are heated using the temperature of bubble, which is used to maintain the temperature constant state in the fermentation chamber.
Description
Technical field
The invention belongs to agriculture field more particularly to composite feed compounding system and preparation methods.
Background technique
In composite feed fermentation magma, soluble ingredient can carry out whole stir with high fructose corn syrup in a mixing bowl
It mixes and is able to achieve dissolution, but when insoluble ingredient stirs in a mixing bowl, insoluble ingredient is difficult to be uniformly dispersed in high fructose corn
In syrup, it partially will appear precipitating or rising phenomenon, it is uneven that the feed product finally to discharge will appear insoluble ingredient dispersion
Even phenomenon, and during the fermentation all critically important to the constant temperature, gas supply and agitating procedure of fermentation liquid.
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 the compound of good mixing effect
Type feed formulation system and preparation method.
Technical solution: to achieve the above object, composite feed compounding system of the invention, including insoluble ingredient crush
Unit, fermenation raw liquid configuration unit, fermentor；
Insoluble ingredient feed pipe, dissolubility ingredient feed pipe and hair are respectively arranged in the fermenation raw liquid configuration unit
Ferment magma discharge nozzle；The slurry fermentation magma discharge nozzle connects the feed end of the fermentor；The insoluble ingredient crushes single
The discharge end of member connects the insoluble ingredient feed pipe.
Further, concentric in the fermentation chamber of the fermentor to be provided with gas injection shaft, the wall body of the gas injection shaft
Side be fixedly connected with several lodicule support rods being laterally extended, several lodicule support rods are along the gas injection shaft axis
The linear array distribution in line direction, and the end of each lodicule support rod is respectively connected with agitation lodicule；
The upper end of the gas injection shaft turns through the fermentor upper end wall body of the fermentor by the second sealing bearing；
Also concentric in the gas injection shaft to be provided with gas injection channel, the upper end in the gas injection channel is pierced by gas injection shaft top,
The lower end closed in the gas injection channel；Upper end inlet in the gas injection channel is provided with check valve, and the check valve is led
It is logical to be directed downward；
The other side of the wall body of the gas injection shaft is fixedly connected with several hard air injection pipes being laterally extended, Ruo Gansuo
Hard air injection pipe is stated along the linear array distribution in gas injection shaft axis direction, and the air flue of each hard air injection pipe root
Bypass connects the gas injection channel, and the end of each hard air injection pipe is connected with gas tip；Each hard air injection pipe
Pipe range be shorter than the lodicule support rod；The lower end of the gas injection shaft turns through the fermentation by the first sealing bearing
The fermentor lower end wall body of tank；It further include stirring spindle motor, the stirring spindle motor and the gas injection shaft are drivingly connected；
The upside of the fermentor is concentric to be provided with heating sterilization tube, concentric setting in the cylinder of the heating sterilization tube
Have every disk, the downside every disk is transition air cavity, and gas injection channel upper end is connected to the transition air cavity；It is described every the upper of disk
Side is concentric to be provided with inner tube wall, and insulated cavity layer is formed between inner tube wall and the heating sterilization tube inner wall；The inner tube wall
Inside it is also concentric be provided with transparent glass cylinder, between the transparent glass cylinder and the inner tube wall formed central column air
Heat channel；Air heating channel inside turn is provided with spiral helicine heating wire, concentric in the transparent glass cylinder to set
It is equipped with second and forms lamp chamber every the upside of disk every disk, described second, be provided with luminescence-utraviolet lamp unit in the lamp chamber；It is described
Second forms outlet chamber every the downside of disk, and the outlet chamber lower end is connected to the transition air cavity, saturating on the downside of disk positioned at second
Hollow out is provided with several air inlets on bright glass infuser wall body；The air is heated lower end and the outlet in channel by each air inlet
Chamber is interconnected；Booster fan is installed, the air outlet of the discharge pipe of the booster fan is connected to institute at the top of the fermentor
State the top in air heating channel；The water conservancy diversion vertex of a cone, the tip court of the water conservancy diversion vertex of a cone are provided at the top of the transparent glass cylinder
To the air outlet of the discharge pipe；
Further, the lower end of the heating sterilization tube is provided with sealing flange, the sealing flange and the hair
It is locked and is connected by flange plate bolt in the upper surface of fermentation tank upper end wall body；The sealing flange and fermentor upper end wall body
Upper surface between be provided with sealing ring；
The fermentation chamber upper end connects the discharge end of the slurry fermentation magma discharge nozzle, and the fermentation chamber lower end is connected with out
Expects pipe；The first open and close valve and the second open and close valve are respectively arranged on the passage and discharge nozzle, the upper end of the fermentation chamber is also
It is connected with gas outlet, overflow valve and third open and close valve have been arranged in series on the gas outlet.
Further, the fermenation raw liquid configuration unit includes cream liquid a mixing bowl, is provided in the cream liquid a mixing bowl molten
Solution property ingredient feed pipe, the cream liquid a mixing bowl are column shape container structure；It is coaxial on the upside of the upper reservoir wall of the cream liquid a mixing bowl
The heart is connected with transmission outer cylinder, and concentric rotate is provided with hollow transmission axle in the transmission outer cylinder, under the hollow transmission axle
End seals bearing by third and can be rotated across the upper reservoir wall, and protrudes into the stir chamber of the cream liquid a mixing bowl；
Circumferentially array distribution has several teeter columns being laterally extended to hollow transmission axle outer wall in stir chamber；
It is formed between the transmission outer cylinder and the hollow transmission axle and declines transmission channel, in the decline transmission channel
It spirals in the shape of a spiral on hollow transmission axle outer wall and is provided with decline screw conveyor blade, the lower end bypass of the decline transmission channel
Connection fermentation magma discharge nozzle；The inside of the hollow transmission axle is concentric to be provided with rising transmission channel, the rising transmission
Concentric rotation is provided with solid transmission sharf in channel, and spiraling to be provided in the shape of a spiral on the solid transmission sharf mentions
Rise screw conveyor blade；If circumferentially array is evenly equipped with dry cream liquid extrusion cavities on the upper end side wall of the hollow transmission axle, several
The upper end for rising transmission channel is connected to by cream liquid extrusion cavities with the upper end of the decline transmission channel, rises transmission channel
If the cream liquid of upper end is uniformly squeezed out by dry cream liquid extrusion cavities into decline transmission channel；The lower end of the solid transmission sharf
The agitation feed inlet of the low hollow transmission axle lower end out is extended to, and the blade lower end for promoting screw conveyor blade is immersed
In the stir chamber；The promotion screw conveyor blade can continuously twist the paste liquid in stir chamber into the agitation feed inlet
In, and make paste liquid along the upward direction continuous feed for rising transmission channel；
The discharge end of the insoluble ingredient feed pipe is connected to the upper end of the decline transmission channel.
Further, the top integrated coaxial heart of the hollow transmission axle is provided with solid cylinder, the solid cylinder
Pass through the 4th sealing bearing rotation connection with the cylinder inner wall of the transmission outer cylinder；
Outer transmission shaft is provided with across hole at the axle center of the top wall body of the transmission outer cylinder, further includes outer transmission shaft, institute
State outer transmission shaft it is concentric pass through the outer transmission shaft pass through hole, and the outer transmission shaft lower end it is concentric integration connection institute
Solid cylinder is stated, the rotational energy of the outer transmission shaft drives the solid cylinder and hollow transmission axle synchronous rotary；The unofficial biography
Synchronized links have synchronizing wheel on the top axial wall of moving axis, further include synchronous translator, and the output shaft of the synchronous translator passes through
Synchronous tape cell and the synchronizing wheel are sequentially connected；
The inside of the outer transmission shaft is concentric to be provided with intermediate solid drive shaft channel up and down, the intermediate solid drive shaft channel
Lower end extends to the connection rising transmission channel；The upper end of the solid transmission sharf is concentric to pass through the intermediate solid drive shaft
The lower end inner wall in channel, the intermediate solid drive shaft channel seals bearing by third and the solid transmission sharf is rotatablely connected；
It further include the output end drive connection solid transmission sharf of solid spindle motor described in solid spindle motor；
The transmission outer cylinder upper end is additionally provided with electric machine support, and the solid spindle motor is fixedly mounted with synchronous translator
On the electric machine support.
Further, the preparation method of composite feed compounding system:
The configuration technique of fermenation raw liquid configuration unit includes the following steps:
Step 1 first passes through dissolubility ingredient feed pipe and injects high fructose corn syrup paste into stir chamber, then starts
Synchronous translator, and then drive hollow transmission axle to rotate in the forward direction, and then drive several teeter columns in stir chamber continuously to stirring
Intracavitary high fructose corn syrup is continuously stirred；
Step 2 maintains to infuse to by dissolubility ingredient feed pipe into stir chamber in the case where stirring in stir chamber
Enter dissolubility ingredient, until dissolubility ingredient is substantially dissolved in high fructose corn syrup in stir chamber；
Step 3, the solid spindle motor of starting after property ingredient to be dissolved is substantially dissolved in high fructose corn syrup, and then solid shafting
The solid transmission sharf rotation of motor driven, and the direction of rotation for controlling the solid transmission sharf and hollow transmission axle at this time
Direction of rotation is conversely, because the blade lower end for promoting screw conveyor blade is immersed in the stir chamber, and then is passed promoting spiral
The paste liquid in stir chamber is continuously twisted in the agitation feed inlet under the action of defeated blade, and makes paste liquid along the rising
The upward direction continuous feed of transmission channel, in paste liquid along the process of the upward direction continuous feed for rising transmission channel
In, since the direction of rotation of solid transmission sharf leads to the direction of rotation of hollow transmission axle at this time on the contrary, rising transmission in turn
The paste liquid that the agitation of screw conveyor blade forward direction is elevated in road also suffers from the reversed grinding effect of hollow transmission axle inner wall, into
And make rise transmission channel in paste liquid it is finer and smoother homogenize, if the paste liquid wait rise in transmission channel rises to dry cream
When liquid extrusion cavities position, if the cream liquid for rising the upper end of transmission channel is squeezed out by dry cream liquid extrusion cavities uniformly continuous under
It drops in transmission channel；
Step 4, if being squeezed out by dry cream liquid extrusion cavities to decline biography wait rise the paste liquid being polished in transmission channel
While defeated channel, insoluble ingredient is continuously introduced into the upper end of decline transmission channel by insoluble ingredient feed pipe, at this time
Insoluble ingredient and the cream liquid that squeezes out from cream liquid extrusion cavities persistently meet in the upper end of decline transmission channel and merge resulting mixture,
And under the action of declining screw conveyor blade, the mixture of insoluble ingredient and paste liquid along decline transmission channel continue to
Lower feeding also receives during insoluble ingredient and the mixture of paste liquid are persistently fed down along decline transmission channel
Decline the prolonged agitation of screw conveyor blade, and then the mixture for making to decline insoluble ingredient and paste liquid in transmission channel fills
Divide mixing, and then is dispersed in insoluble ingredients in paste liquid；
The mixture of step 5, the final insoluble ingredient declined in transmission channel and paste liquid passes through fermentation magma discharging
Pipe discharge；From the paste liquid that fermentation magma discharge nozzle is discharged, the high fructose corn syrup finer and smoother compared to raw material is generated, and
Dissolubility ingredients are dissolved in high fructose corn syrup, and insoluble ingredient is also dispersed in the high fructose corn syrup.
The utility model has the advantages that structure of the invention is simple, air along air heating channel flow downward during persistently by
The irradiation-sterilize of luminescence-utraviolet lamp unit, and also persistently heated by spiral helicine heater strip, it is heated and ultraviolet-sterilization
Air is persistently emerged into fermentation chamber in the form of bubble on several gas tips afterwards, is mentioned for the yeast probiotics in fermentation chamber
Also containing in bubble while oxygen has heat, is heated using the temperature of bubble to the slurries in fermentation chamber, the heat
For maintaining the temperature constant state in the fermentation chamber.
Detailed description of the invention
Attached drawing 1 is this programme overall system architecture schematic diagram；
Attached drawing 2 is fermentor cut-away diagram；
Attached drawing 3 is the partial schematic diagram at the label 60 of attached drawing 2；
Attached drawing 4 is partial schematic diagram at the top of fermentor；
Attached drawing 5 is that fermentation magma configuration unit just cuts open schematic diagram；
Attached drawing 6 is the enlarged diagram at the label 16 of attached drawing 5；
Attached drawing 7 is the enlarged diagram at the label 5 of attached drawing 5.
Specific embodiment
The present invention will be further explained with reference to the accompanying drawing.
The composite feed compounding system as shown in attached drawing 1 to 7, including insoluble ingredient pulverizing unit 09, fermenation raw liquid
Configuration unit, fermentor 96；
Insoluble ingredient feed pipe 12, dissolubility ingredient feed pipe 17 are respectively arranged in the fermenation raw liquid configuration unit
With fermentation magma discharge nozzle 10；The slurry fermentation magma discharge nozzle 10 connects the feed end of the fermentor 96；It is described insoluble
The discharge end of ingredient pulverizing unit 09 connects the insoluble ingredient feed pipe 12.
It is concentric in the fermentation chamber 73 of the fermentor 96 to be provided with gas injection shaft 87, the wall body of the gas injection shaft 87
Side is fixedly connected with several lodicule support rods 84 being laterally extended, and several lodicule support rods 84 are along the gas injection shaft
The linear array distribution of 87 axis directions, and the end of each lodicule support rod 84 is respectively connected with agitation lodicule 06；
The upper end of the gas injection shaft 87 is turned through on the fermentor of the fermentor 96 by the second sealing bearing 64
End wall body 63；Also concentric in the gas injection shaft 87 to be provided with gas injection channel 89, the upper end in the gas injection channel 89 is pierced by institute
State 87 top of gas injection shaft, the lower end closed in the gas injection channel 89；Upper end inlet in the gas injection channel 89 is provided with
Check valve 04, the conducting direction of the check valve 04 is downward；
The other side of the wall body of the gas injection shaft 87 is fixedly connected with several hard air injection pipes 03 being laterally extended, if
The hard air injection pipe 03 is done along the linear array distribution of 87 axis direction of gas injection shaft, and each hard air injection pipe 03
The air flue 01 of root bypasses the connection gas injection channel 89, and the end of each hard air injection pipe 03 is connected with gas tip
02；The pipe range of each hard air injection pipe 03 is shorter than the lodicule support rod 84；The lower end of the gas injection shaft 87 passes through the
One sealing bearing 92 turns through the fermentor lower end wall body 63.1 of the fermentor 96；It further include stirring spindle motor 72, it is described
It stirs spindle motor 72 and the gas injection shaft 87 is drivingly connected；
Concentric be provided in the upside of the fermentor 96 heats sterilization tube 55, coaxial in the cylinder of the heating sterilization tube 55
The heart is provided with every disk 66, and the downside every disk 66 is transition air cavity 61, and 89 upper end of gas injection channel is connected to the transitional gas
Chamber 61；The upside every disk 66 is concentric to be provided with inner tube wall 56, between inner tube wall 56 and 55 inner wall of heating sterilization tube
Form insulated cavity layer 54；The inside of the inner tube wall 56 is also concentric to be provided with transparent glass cylinder 51, the transparent glass cylinder
The air that central column is formed between 51 and the inner tube wall 56 heats channel 59；Air heating 59 inside turn of channel is provided with
Spiral helicine heating wire 69, concentric in the transparent glass cylinder 51 to be provided with second every disk 68, described second every the upper of disk 68
Side forms lamp chamber 80, is provided with luminescence-utraviolet lamp unit 57 in the lamp chamber 80；Described second forms out every the downside of disk 68
Air cavity 94,94 lower end of outlet chamber are connected to the transition air cavity 61, positioned at the second 51 wall of transparent glass cylinder on the downside of disk 68
Hollow out is provided with several air inlets 58 on body；The air is heated lower end and the outlet chamber 94 in channel 59 by each air inlet 58
It is interconnected；The top of the fermentor 96 is equipped with booster fan 81, the air outlet of the discharge pipe 52 of the booster fan 81
It is connected to the top in air heating channel 59；The top of the transparent glass cylinder 51 is provided with the water conservancy diversion vertex of a cone 53, the water conservancy diversion
Air outlet of the tip of the vertex of a cone 53 towards the discharge pipe 52；
The lower end of the heating sterilization tube 55 is provided with sealing flange 62, the sealing flange 62 and the fermentor
It is locked and is connected by flange plate bolt in the upper surface of upper end wall body 63；The sealing flange 62 and fermentor upper end wall body
Sealing ring 67 is provided between 63 upper surface；
73 upper end of fermentation chamber connects the discharge end of the slurry fermentation magma discharge nozzle 10, and 73 lower end of fermentation chamber connects
It is connected to discharge nozzle 91；The first open and close valve 86 and the second open and close valve 74, institute are respectively arranged on the passage 10 and discharge nozzle 91
The upper end for stating fermentation chamber 73 is also connected with gas outlet 82, has been arranged in series overflow valve and third open and close valve 83 on the gas outlet 82.
The fermenation raw liquid configuration unit includes cream liquid a mixing bowl 18, is provided with dissolubility in the cream liquid a mixing bowl 18 and matches
Expect that feed pipe 17, the cream liquid a mixing bowl 18 are column shape container structure；18.1 upside of upper reservoir wall of the cream liquid a mixing bowl 18
Concentric to be connected with transmission outer cylinder 8, concentric rotation is provided with hollow transmission axle 14, the hollow biography in the transmission outer cylinder 8
The lower end of defeated axis 14 seals bearing 21 by third and can be rotated across the upper reservoir wall 18.1, and protrudes into the cream liquid a mixing bowl
In 18 stir chamber 19；
Circumferentially array distribution has several teeter columns being laterally extended to 14 outer wall of hollow transmission axle in stir chamber 19
20；
Decline transmission channel 7, the decline transmission channel are formed between the transmission outer cylinder 8 and the hollow transmission axle 14
It spirals in the shape of a spiral on 14 outer wall of hollow transmission axle in 7 and is provided with decline screw conveyor blade 9, the decline transmission channel 7
Lower end bypass connection fermentation magma discharge nozzle 10；The inside of the hollow transmission axle 14 is concentric to be provided with rising transmission channel
15, concentric rotation is provided with solid transmission sharf 13, the solid transmission sharf 13 in the rising transmission channel 15
On spiral in the shape of a spiral be provided with promoted screw conveyor blade 6；Circumferentially array on the upper end side wall of the hollow transmission axle 14
If being evenly equipped with dry cream liquid extrusion cavities 24, if dry cream liquid extrusion cavities 24 pass the upper end for rising transmission channel 15 and the decline
The upper end in defeated channel 7 is connected to, if the cream liquid for rising the upper end of transmission channel 15 is uniformly squeezed out under by dry cream liquid extrusion cavities 24
It drops in transmission channel 7；The lower end of the solid transmission sharf 13 extends to the agitation of low hollow 14 lower end of transmission axle out
Feed inlet 22, and the blade lower end for promoting screw conveyor blade 6 is immersed in the stir chamber 19；The promotion screw conveyor
Blade 6 can continuously twist the paste liquid in stir chamber 19 in the agitation feed inlet 22, and pass paste liquid along the rising
The upward direction continuous feed in defeated channel 15；
The discharge end of the insoluble ingredient feed pipe 12 is connected to the upper end of the decline transmission channel 7.
The top integrated coaxial heart of the hollow transmission axle 14 is provided with solid cylinder 26, the solid cylinder 26 and institute
The cylinder inner wall for stating transmission outer cylinder 8 is rotatablely connected by the 4th sealing bearing 23；
Outer transmission shaft is provided with across hole 29 at the axle center of the top wall body 28 of the transmission outer cylinder 8, further includes outer transmission
Axis 27, the outer transmission shaft 27 is concentric to pass through the outer transmission shaft across hole 29, and the lower end of the outer transmission shaft 27 is coaxial
Heart integration connects the solid cylinder 26, and the rotational energy of the outer transmission shaft 27 drives the solid cylinder 26 and hollow transmission
14 synchronous rotary of axis；Synchronized links have synchronizing wheel 20 on the top axial wall of the outer transmission shaft 27, further include synchronous translator 2,
The output shaft of the synchronous translator 2 passes through synchronous tape cell 4 and is sequentially connected with the synchronizing wheel 20；
The inside of the outer transmission shaft 27 is concentric to be provided with intermediate solid drive shaft channel 13.1, the intermediate solid drive shaft up and down
The lower end in channel 13.1 extends to the connection rising transmission channel 15；The upper end of the solid transmission sharf 13 is concentric to wear
Cross the intermediate solid drive shaft channel 13.1, the lower end inner wall in the intermediate solid drive shaft channel 13.1 by third seal bearing 25 with it is described
Solid transmission sharf 13 is rotatablely connected；It further include described in the output end drive connection of solid spindle motor 3 described in solid spindle motor 3
Solid transmission sharf 13；
8 upper end of transmission outer cylinder is additionally provided with electric machine support 1, and the solid spindle motor 3 is fixed with synchronous translator 2
It is mounted on the electric machine support 1.
The method of this programme, process and technological progress arrange as follows:
Zymotechnique includes the following steps:
Step 1: fermentation magma configuration unit exports configured fermentation virgin pulp liquid by slurry fermentation magma discharge nozzle 10
Into the fermentation chamber 73 of the inside of fermentor 96, and yeast probiotics is added in fermentation chamber 73；
Step 2: starting stirring spindle motor 72 rotates gas injection shaft 87 persistently, and then in the gas injection shaft 87
Several agitation lodicules 06 drive the slurries in fermentation chamber 73 to continue slowly to stir, which maintains to step 4；
Step 3: starting centrifugation booster fan 81, and then it is empty to import discharge pipe 52 persistently into air heating channel 59
Gas, and then air is killed along the irradiation that air heats during channel 59 flows downward persistently by luminescence-utraviolet lamp unit 57
Bacterium, and also persistently heated by spiral helicine heater strip, the air for being then heated and sterilizing in air heating channel 59 is logical
It crosses several air inlets 58 to import in outlet chamber 94, then the gas in outlet chamber 94 imports in transition air cavity 61, then transitional gas
Gas in chamber 61 is persistently pressed into gas injection channel 89, and then the gas in gas injection channel 89 is imported by several air flues 01
To several gas tips 02, finally it is heated and is continued in the form of bubble on several gas tips 02 with air after ultraviolet-sterilization
It emerges into fermentation chamber 73, and then provides oxygen for the yeast probiotics in fermentation chamber 73, and pass through several gas tips 02
On the bubble emerged also contain and have heat, the slurries in fermentation chamber 73 are heated using the temperature of bubble, which is used for
The temperature constant state in the fermentation chamber 73 is maintained, and is controlled 30 in fermentation chamber 73 by the heating power of control electric heating heater strip 69
DEG C ± 0.5 DEG C of temperature constant state, the excessive gas in fermentation chamber 73 is persistently arranged by the overflow valve on gas outlet 82 at the same time
Out, and then the air pressure in fermentation chamber 73 is made to form dynamic equilibrium；
Step 4: standing, and maintains step 3 72 hours yeast probiotics fermention time；
Step 5: preparing discharging after fermentation process, slurries after fermentation are in sticky slurries, directly opens the
Blanking velocity is inadequate in the case of two open and close valves 74, and the first open and close valve 86 and third open and close valve 83 are closed in control at this time, beats simultaneously
The second open and close valve 74 is opened, then starting centrifugation booster fan 81 increases its export wind pressure, and then keeps the air pressure in fermentation chamber 73 big
In external atmosphere pressure, and then the cream liquid of fermented completion in fermentation chamber 73 is promoted persistently to be extruded by discharge nozzle 91, improved
Blanking velocity；
The configuration technique of fermenation raw liquid configuration unit includes the following steps:
Step 1 first passes through dissolubility ingredient feed pipe 17 and injects high fructose corn syrup 19 paste into stir chamber 19, so
Start synchronous translator 2 afterwards, and then hollow transmission axle 14 is driven to rotate in the forward direction, and then drives several teeter columns in stir chamber 19
20 continuously continuously stir the high fructose corn syrup 19 in stir chamber 19；
Step 2, maintain in stir chamber 19 in the case where stirring to by dissolubility ingredient feed pipe 17 to stir chamber
Dissolubility ingredient is injected in 19, until dissolubility ingredient is substantially dissolved in high fructose corn syrup 19 in stir chamber 19；
Step 3, the solid spindle motor 3 of starting after property ingredient to be dissolved is substantially dissolved in high fructose corn syrup 19, so that it is solid
Spindle motor 3 drives solid transmission sharf 13 to rotate, and control direction of rotation of the solid transmission sharf 13 with it is hollow at this time
The direction of rotation of transmission axle 14 is conversely, because the blade lower end for promoting screw conveyor blade 6 is immersed in the stir chamber 19, in turn
The paste liquid in stir chamber 19 is continuously twisted in the agitation feed inlet 22 under the action of promoting screw conveyor blade 6, and
Make paste liquid along the upward direction continuous feed for rising transmission channel 15, in paste liquid along the rising transmission channel 15
Direction of rotation and the rotation of hollow transmission axle 14 at this time during upward direction continuous feed, due to solid transmission sharf 13
Turn contrary, and then the paste liquid that the positive agitation of screw conveyor blade 6 is elevated in rising transmission channel 15 also suffers from sky
The reversed grinding effect of 14 inner wall of heart transmission axle, and then make the paste liquid in rising transmission channel 15 is finer and smoother to homogenize, to
If the paste liquid in rising transmission channel 15 rises to dry cream liquid 24 position of extrusion cavities, rise the upper end of transmission channel 15
If cream liquid by 24 uniformly continuous of dry cream liquid extrusion cavities squeeze out to decline transmission channel 7 in；
Step 4, if the paste liquid being polished in transmission channel to be risen 15 is squeezed out by dry cream liquid extrusion cavities 24 under
While dropping transmission channel 7, insoluble match is continuously introduced into the upper end of decline transmission channel 7 by insoluble ingredient feed pipe 12
Material, insoluble ingredient is persistently met and is melted in the upper end of decline transmission channel 7 with the cream liquid squeezed out from cream liquid extrusion cavities 24 at this time
Synthetic mixture, and under the action of declining screw conveyor blade 9, the mixture of insoluble ingredient and paste liquid is passed along decline
Defeated channel 7 is persistently fed down, and is persistently fed down in the mixture of insoluble ingredient and paste liquid along decline transmission channel 7
Also receive in the process decline screw conveyor blade 9 prolonged agitation, and then make decline transmission channel 7 in insoluble ingredient with
The mixture of paste liquid is sufficiently mixed, and then is dispersed in insoluble ingredients in paste liquid；
The mixture of step 5, the final insoluble ingredient declined in transmission channel 7 and paste liquid is gone out by magma of fermenting
Expects pipe 10 is discharged；From the paste liquid that fermentation magma discharge nozzle 10 is discharged, the high fructose corn sugar finer and smoother compared to raw material is generated
Slurry, and dissolubility ingredients are dissolved in high fructose corn syrup, and insoluble ingredient is also dispersed in the high fructose corn syrup
In.
Above-mentioned high fructose corn syrup 19, insoluble ingredient, the weight proportion between dissolubility ingredient three are as follows: high fructose corn syrup
19 account for 68-75%, and insoluble ingredient accounts for 14-18%, and dissolubility ingredient accounts for 10-12%；
The Ingredients Weight of above-mentioned insoluble ingredient matches are as follows: corn flour 40-50%, dehulled soybeans powder 20-30%, wheat are gone
Miscellaneous powder 25-35%；
The Ingredients Weight of above-mentioned dissolubility ingredient matches are as follows: whey powder 45-56%, plasma protein 14-17%, fatty powder
13-18%, calcium formate 6-8%, amino acid 7-12%, citric acid 7-9%.
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. composite feed compounding system, it is characterised in that: single including insoluble ingredient pulverizing unit (09), fermenation raw liquid configuration
Member, fermentor (96)；
Insoluble ingredient feed pipe (12), dissolubility ingredient feed pipe (17) are respectively arranged in the fermenation raw liquid configuration unit
With fermentation magma discharge nozzle (10)；Slurry fermentation magma discharge nozzle (10) connects the feed end of the fermentor (96)；It is described
The discharge end of insoluble ingredient pulverizing unit (09) connects the insoluble ingredient feed pipe (12).
2. composite feed compounding system according to claim 1, it is characterised in that: the fermentation chamber of the fermentor (96)
(73) concentric in be provided with gas injection shaft (87), the side of the wall body of the gas injection shaft (87) is fixedly connected with several cross
To the lodicule support rod (84) of extension, several lodicule support rods (84) are linear along gas injection shaft (87) axis direction
Array distribution, and the end of each lodicule support rod (84) is respectively connected with agitation lodicule (06)；
The upper end of the gas injection shaft (87) turns through the fermentor of the fermentor (96) by the second sealing bearing (64)
Upper end wall body (63)；It is also concentric in the gas injection shaft (87) to be provided with gas injection channel (89), the gas injection channel (89)
Upper end is pierced by gas injection shaft (87) top, the lower end closed of the gas injection channel (89)；In the gas injection channel (89)
Upper end inlet is provided with check valve (04), and the conducting direction of the check valve (04) is downward；
The other side of the wall body of the gas injection shaft (87) is fixedly connected with several hard air injection pipes (03) being laterally extended, if
The hard air injection pipe (03) is done along the linear array distribution of gas injection shaft (87) axis direction, and each hard gas injection
The air flue (01) of pipe (03) root bypasses the connection gas injection channel (89), the end connection of each hard air injection pipe (03)
There is gas tip (02)；The pipe range of each hard air injection pipe (03) is shorter than the lodicule support rod (84)；The gas injection turns
The lower end of axis (87) turns through the fermentor lower end wall body (63.1) of the fermentor (96) by the first sealing bearing (92)；
It further include stirring spindle motor (72), the stirring spindle motor (72) and the gas injection shaft (87) are drivingly connected；
Concentric be provided in the upside of the fermentor (96) heats sterilization tube (55), same in the cylinder of heating sterilization tube (55)
Axle center is provided with every disk (66), and the downside every disk (66) is transition air cavity (61), gas injection channel (89) the upper end connection
The transition air cavity (61)；The upside every disk (66) is concentric to be provided with inner tube wall (56), and inner tube wall (56) adds with described
Insulated cavity layer (54) are formed between thermal sterilization cylinder (55) inner wall；The inside of the inner tube wall (56) also it is concentric be provided with it is transparent
Glass infuser (51), the air that central column is formed between the transparent glass cylinder (51) and the inner tube wall (56) heat channel
(59)；Described air heating channel (59) inside turn is provided with spiral helicine heating wire (69), in the transparent glass cylinder (51)
Concentric to be provided with second every disk (68), described second every the upside of disk (68) formation lamp chamber (80), and the lamp chamber (80) is interior to be set
It is equipped with luminescence-utraviolet lamp unit (57)；Described second forms outlet chamber (94) every the downside of disk (68), the outlet chamber (94)
Lower end is connected to the transition air cavity (61), is located at hollow out on second transparent glass cylinder (51) wall body on the downside of disk (68) and is provided with
Several air inlets (58)；Each air inlet (58) mutually interconnects the lower end of air heating channel (59) with outlet chamber (94)
It is logical；It is equipped with booster fan (81) at the top of the fermentor (96), the outlet air of the discharge pipe (52) of the booster fan (81)
Mouth is connected to the top of air heating channel (59)；The water conservancy diversion vertex of a cone (53) are provided at the top of the transparent glass cylinder (51),
Air outlet of the tip of the water conservancy diversion vertex of a cone (53) towards the discharge pipe (52).
3. composite feed compounding system according to claim 2, it is characterised in that: under the heating sterilization tube (55)
End is provided with sealing flange (62), and the sealing flange (62) and the upper surface of fermentor upper end wall body (63) pass through
Flange plate bolt locking connection；It is arranged between the sealing flange (62) and the upper surface of fermentor upper end wall body (63)
There are sealing ring (67)；
The discharge end of fermentation chamber (73) upper end connection slurry fermentation magma discharge nozzle (10), fermentation chamber (73) lower end
It is connected with discharge nozzle (91)；The first open and close valve (86) and second is respectively arranged on the passage (10) and discharge nozzle (91) to open
The upper end of valve closing (74), the fermentation chamber (73) is also connected with gas outlet (82), has been arranged in series overflow on the gas outlet (82)
Valve and third open and close valve (83).
4. composite feed compounding system according to claim 3, it is characterised in that: the fermenation raw liquid configuration unit packet
Cream liquid a mixing bowl (18) is included, dissolubility ingredient feed pipe (17), the cream liquid stirring are provided in the cream liquid a mixing bowl (18)
Cylinder (18) is column shape container structure；It is concentric on the upside of the upper reservoir wall (18.1) of the cream liquid a mixing bowl (18) to be connected with outside transmission
Cylinder (8), concentric rotate is provided with hollow transmission axle (14) in the transmission outer cylinder (8), under the hollow transmission axle (14)
End can be rotated by third sealing bearing (21) across the upper reservoir wall (18.1), and protrude into the cream liquid a mixing bowl (18)
In stir chamber (19)；
Circumferentially array distribution has several teeter columns being laterally extended to hollow transmission axle (14) outer wall in stir chamber (19)
(20)；
Decline transmission channel (7) is formed between the transmission outer cylinder (8) and the hollow transmission axle (14), the decline transmission is logical
It spirals in the shape of a spiral on hollow transmission axle (14) outer wall in road (7) and is provided with decline screw conveyor blade (9), the decline passes
Lower end bypass connection fermentation magma discharge nozzle (10) of defeated channel (7)；The concentric setting in inside of the hollow transmission axle (14)
Having rising transmission channel (15), concentric rotation is provided with solid transmission sharf (13) in the rising transmission channel (15),
It spirals to be provided in the shape of a spiral on the solid transmission sharf (13) and promotes screw conveyor blade (6)；The hollow transmission axle
(14) if upper end side wall on circumferentially array be evenly equipped with dry cream liquid extrusion cavities (24), if dry cream liquid extrusion cavities (24) will be described on
The upper end for rising transmission channel (15) is connected to the upper end of decline transmission channel (7), rises the upper end of transmission channel (15)
If cream liquid is uniformly squeezed out into decline transmission channel (7) by dry cream liquid extrusion cavities (24)；The solid transmission sharf (13)
Lower end extend to it is low go out hollow transmission axle (14) lower end agitation feed inlet (22), and the promotion screw conveyor blade
(6) blade lower end is immersed in the stir chamber (19)；Promotion screw conveyor blade (6) can be by the cream in stir chamber (19)
Shape liquid continuously twists in the agitation feed inlet (22), and connects paste liquid along the upward direction for rising transmission channel (15)
Continuous feeding；
The upper end of discharge end connection decline transmission channel (7) of the insoluble ingredient feed pipe (12).
5. composite feed compounding system according to claim 4, it is characterised in that: the top of the hollow transmission axle (14)
Integrally is concentric to be provided with solid cylinder (26), and the cylinder inner wall of the solid cylinder (26) and transmission outer cylinder (8) is logical
Cross the 4th sealing bearing (23) rotation connection；
It is provided with outer transmission shaft at the axle center of the top wall body (28) of transmission outer cylinder (8) across hole (29), further includes unofficial biography
Moving axis (27), the outer transmission shaft (27) is concentric to pass through hole (29) across the outer transmission shaft, and the outer transmission shaft (27)
The concentric integration in lower end connect the solid cylinder (26), the rotational energy of the outer transmission shaft (27) drives the solid post
Body (26) and hollow transmission axle (14) synchronous rotary；Synchronized links have synchronizing wheel on the top axial wall of the outer transmission shaft (27)
(20), further include synchronous translator (2), the output shaft of the synchronous translator (2) pass through synchronous tape cell (4) with it is described synchronous
Take turns (20) transmission connection；
The inside of the outer transmission shaft (27) is concentric to be provided with intermediate solid drive shaft channel (13.1), the intermediate solid drive shaft up and down
The lower end in channel (13.1) extends to the connection rising transmission channel (15)；The upper end of solid transmission sharf (13) is same
Axle center passes through the intermediate solid drive shaft channel (13.1), and the lower end inner wall of the intermediate solid drive shaft channel (13.1) seals axis by third
It holds (25) and the solid transmission sharf (13) is rotatablely connected；It further include solid spindle motor (3) the solid spindle motor (3)
Output end is drivingly connected the solid transmission sharf (13)；
Transmission outer cylinder (8) upper end is additionally provided with electric machine support (1), and the solid spindle motor (3) is equal with synchronous translator (2)
It is fixedly mounted on the electric machine support (1).
6. the preparation method of composite feed compounding system according to claim 5, it is characterised in that:
The configuration technique of fermenation raw liquid configuration unit includes the following steps:
Step 1 first passes through dissolubility ingredient feed pipe (17) injection high fructose corn syrup (19) paste into stir chamber (19),
Then start synchronous translator (2), and then hollow transmission axle (14) driven to rotate in the forward direction, so drive stir chamber (19) if in
Dry teeter column (20) continuously continuously stirs the high fructose corn syrup (19) in stir chamber (19)；
Step 2, maintain in the case where stir chamber (19) interior stirring to by dissolubility ingredient feed pipe (17) to stir chamber
(19) dissolubility ingredient is injected in, until dissolubility ingredient is substantially dissolved in high fructose corn syrup (19) in stir chamber (19)；
Step 3, the solid spindle motor (3) of starting after property ingredient to be dissolved is substantially dissolved in high fructose corn syrup (19), so that it is solid
Spindle motor (3) drives solid transmission sharf (13) rotation, and controls the solid direction of rotation for transmitting sharf (13) and this
When hollow transmission axle (14) direction of rotation conversely, because the stirring is immersed in the blade lower end for promoting screw conveyor blade (6)
In chamber (19), and then the paste liquid in stir chamber (19) is continuously twisted into described under the action of promoting screw conveyor blade (6)
It stirs in feed inlet (22), and makes paste liquid along the upward direction continuous feed for rising transmission channel (15), in paste liquid
During the upward direction continuous feed for rising transmission channel (15), due to the rotation of solid transmission sharf (13)
Direction and the direction of rotation of hollow transmission axle (14) at this time are elevated screw conveyor leaf on the contrary, rising in transmission channel (15) in turn
The paste liquid of the positive agitation of piece (6) also suffers from the reversed grinding effect of hollow transmission axle (14) inner wall, and then makes to rise and transmit
Paste liquid in channel (15) is finer and smoother to homogenize, transmission channel (15) to be risen if in paste liquid rise to dry cream liquid and squeeze
Portal (24) position when, rise transmission channel (15) if upper end cream liquid pass through dry cream liquid extrusion cavities (24) uniformly continuous
It squeezes out into decline transmission channel (7)；
Step 4, transmission channel (15) to be risen if in the paste liquid that is polished squeezed out by dry cream liquid extrusion cavities (24) under
While dropping transmission channel (7), it is continuously introduced into not by insoluble ingredient feed pipe (12) to the upper end of decline transmission channel (7)
Dissolubility ingredient, insoluble ingredient supports in decline transmission channel (7) with from the cream liquid that cream liquid extrusion cavities (24) squeeze out at this time
It is continuous to meet and merge resulting mixture, and under the action of declining screw conveyor blade (9), insoluble ingredient is mixed with paste liquid
It closes object persistently to feed down along decline transmission channel (7), in the mixture of insoluble ingredient and paste liquid along decline transmission channel
(7) prolonged agitation of decline screw conveyor blade (9) is also received during persistently feeding down, and then keeps decline transmission logical
The mixture of insoluble ingredient and paste liquid in road (7) is sufficiently mixed, and then insoluble ingredients is made to be dispersed in paste liquid
In；
Step 5, the mixture for finally declining the insoluble ingredient and paste liquid in transmission channel (7) pass through fermentation magma discharging
Manage (10) discharge；From the paste liquid that fermentation magma discharge nozzle (10) is discharged, the high fructose corn finer and smoother compared to raw material is generated
Syrup, and dissolubility ingredients are dissolved in high fructose corn syrup, and insoluble ingredient is also dispersed in high fructose corn sugar
In slurry.
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| CN201811500049.8A CN109363216B (en) | 2018-12-10 | 2018-12-10 | Compound feed preparation system and preparation method |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109845867A (en) * | 2019-02-26 | 2019-06-07 | 顾健健 | Cereals deep processing of farm products stretch system and its concrete technology method |
| CN113355234A (en) * | 2021-07-20 | 2021-09-07 | 山东亿源环境工程有限公司 | Reation kettle is used in preparation of quality of water enzyme-based modifier |
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| CN206866601U (en) * | 2017-05-17 | 2018-01-12 | 白可可 | A kind of comminuting dasher for preparing paste feed |
| CN107927873A (en) * | 2017-12-22 | 2018-04-20 | 江西液好液态料养猪设备有限公司 | A kind of liquid-state feed preparation system |
| CN108652056A (en) * | 2018-04-22 | 2018-10-16 | 严涛 | A kind of livestock-raising feed making device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102805270A (en) * | 2012-08-24 | 2012-12-05 | 安徽五粮泰生物工程股份有限公司 | Preparation method of piglet paste feed |
| CN205040636U (en) * | 2015-09-02 | 2016-02-24 | 广州快大饲料有限公司 | Lactating sows mixed feed fermenting installation |
| CN206866601U (en) * | 2017-05-17 | 2018-01-12 | 白可可 | A kind of comminuting dasher for preparing paste feed |
| CN107927873A (en) * | 2017-12-22 | 2018-04-20 | 江西液好液态料养猪设备有限公司 | A kind of liquid-state feed preparation system |
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| CN109845867B (en) * | 2019-02-26 | 2022-07-22 | 吉林北显生态农业集团有限公司 | Grain agricultural product deep processing extension system and specific process method thereof |
| CN113355234A (en) * | 2021-07-20 | 2021-09-07 | 山东亿源环境工程有限公司 | Reation kettle is used in preparation of quality of water enzyme-based modifier |
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