CN106858041B - A kind of preparation method for the cold granulation feed that ferments - Google Patents
A kind of preparation method for the cold granulation feed that ferments Download PDFInfo
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- CN106858041B CN106858041B CN201710190454.3A CN201710190454A CN106858041B CN 106858041 B CN106858041 B CN 106858041B CN 201710190454 A CN201710190454 A CN 201710190454A CN 106858041 B CN106858041 B CN 106858041B
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Abstract
The present invention relates to feed processing manufacture technology field, discloses a kind of preparation method for the cold granulation feed that ferments, comprises the following steps:After feedstuff and microbial concentration ferment albumen are pulverized and mixed, granulation of fermenting in cold granulation device is put into;Adjustment matches the ring moulds and compression ratio of the cold granulation device, temperature while granulation of the material in the cold granulation device is increased, when temperature rises to 60 DEG C~65 DEG C, cooling, obtains the cold granulation feed that ferments.The preparation method of the cold granulation feed of present invention fermentation, using the cold granulation device that ferments, while granulation, feedstuff and microbial concentration ferment albumen are organically combined, and Rapid Fermentation enzymolysis is into predigesting feed.Heating unit is no longer needed, is pelletized without steam regulation of texture, conditioning of texture, is directly mutually rubbed fever with material by machinery, there is provided fermentation condition quickly realizes that microorganism rises in value and macromolecular complex is changed into small-molecule substance, realizes feed predigestion function.
Description
Technical field
The present invention relates to feed processing applied technical field, more particularly to a kind of preparation method for the cold granulation feed that ferments.
Background technology
Feed processing refers to the Feed Manufacturing processing activity suitable for pasture, farmer breed livestock, poultry, pet, aquatic products.
At present, either food-safety problem or animal health problem is all inseparable with feed processing technology relation, and increasingly
It is taken seriously.Ensure food security and animal health, in addition to raw material clean in itself, most critical is that feed adds
Work process realizes feed functionalization, ecology, and to improving animal welfare, it is significant to make ecological circulation agricultural.
At present, granulating process is warmed, it is necessary to use boiler etc. usually using height in the existing feed processing pelletization of industry
Heating equipment generation steam progress is quenched, can not realize feed functionalization, and the influence to feed quality is very big, it is difficult to realize
Environmentally friendly feed.
The content of the invention
In view of this, the present invention provides a kind of preparation method for the cold granulation feed that ferments, feedstuff is enable to make
The predigesting feed into small molecule is digested while grain, so as to add the function and quality of feed.
In order to realize foregoing invention purpose, the present invention provides following technical scheme:
The present invention provides a kind of preparation method for the cold granulation feed that ferments, comprise the following steps:
After feedstuff and microbial concentration ferment albumen are pulverized and mixed, granulation of fermenting in cold granulation device is put into;Adjust
The ring moulds and compression ratio of the whole matching cold granulation device, rise the temperature in granulation of the material in the cold granulation device,
When temperature rises to 60 DEG C~65 DEG C, cooling, obtains the cold granulation feed that ferments.
Preferably, the particle diameter after feedstuff and microbial concentration the ferment albumen crushes is 20~80 mesh.
Preferably, the ring moulds of the cold granulation device are aperture 1.5~4.5, compression ratio 1:5~25.
Preferably, fermentation Granulation time of the material in the cold granulation device is 3~15 minutes.
Preferably, the microbial concentration ferment albumen is to be made by Feed Material after microbial fermentation digests.
Preferably, the microbial concentration ferment albumen is prepared by method comprising the following steps:
(1) Feed Material input feed fermentation mixer is stirred, keeps the moisture of the Feed Material to exist
50~60wt%;
(2) microbial bacterial agent is added in step (1) described feed fermentation mixer, the microbial bacterial agent and the feeding
The weight ratio for expecting material is 7.5~10kg/t, and the spinner velocity for controlling the feed fermentation mixer is 25~30 revs/min;
(3) when the temperature of material in feed fermentation mixer rises to 40~50 DEG C, again add microbial bacterial agent after
Continuous stirring, the weight ratio for adding the microbial bacterial agent and the Feed Material at this time is 7.5~10kg/t;
(4) when the temperature of material in feed fermentation mixer rises to 50~60 DEG C, to the feed fermentation mixer
In add Feed Material again and continue to stir, add the Feed Material at this time with adding the weight of Feed Material in step (1)
Than for 1:1, when temperature of charge reaches 50 DEG C~60 DEG C again, outputting material, obtains microbial bacterial agent concentration ferment after cooling
Albumen.
It is further preferred that contain 1 × 10 in the microbial bacterial agent6~1 × 108The microorganism of CFU/g, micro- life
Thing is any one or two or more compositions in bacillus subtilis, bacillus coagulans and saccharomycete.It is further excellent
Choosing, in step (2), the mass ratio of the bacillus subtilis, bacillus coagulans and saccharomycete is 1:1~2:1;Step
(3) in, the mass ratio of the bacillus subtilis, bacillus coagulans and saccharomycete is 1:2~3:1.
Preferably, the feedstuff be expanded soybean, it is dregs of beans, corn, wheat-middlings, flour, fish meal, wheat skin, wheat, big
One or more of mixtures in rice, rice bran meal, rapeseed meal and cotton dregs.
Preferably, the mass ratio of the feedstuff and the microbial concentration ferment albumen is 5~10:1~3.
Processing technology of the present invention based on cold granulation of fermenting, using fermenting, cold granulation device coordinates, by a certain proportion of base
Plinth feedstuff and microbial concentration ferment albumen organically combine, and Rapid Fermentation is digested into predigesting feed.Add without boiler etc.
Hot auxiliary device, pelletizes without steam regulation of texture, conditioning of texture, directly mutually rubs fever with material by machinery, there is provided the quick reality of fermentation condition
Existing microorganism rises in value and macromolecular complex is changed into small-molecule substance, realizes feed predigestion function.Technique is simple, living easy to height
Property biological feedstuff mass production, granulation it is best in quality.The preparation method of the cold granulation feed of fermentation of the present invention, can realize
High efficiency, high-quality, the production model of low cost, bottle is popularized for the fresh-keeping of fermented feed application, keep-alive, convenience etc.
Neck.
Brief description of the drawings
Fig. 1 is the Technology Roadmap of the cold granulation feed producing method of present invention fermentation.
Embodiment
The present invention provides a kind of preparation method for the cold granulation feed that ferments, comprise the following steps:By feedstuff and micro-
After bioconcentration ferment albumen is pulverized and mixed, granulation of fermenting in cold granulation device is put into;Adjustment matches the cold granulation device
Ring moulds and compression ratio, rise the temperature in granulation of the material in the cold granulation device, when temperature rises to 60 DEG C~65 DEG C
When, cooling, obtains the cold granulation feed that ferments.
The feedstuff and microbial concentration ferment albumen that the present invention applies are to pelletize again through cold granulation device after crushed.
The present invention is not particularly limited the concrete mode of smashing, can realize that feedstuff and microbial concentration ferment albumen crush effect
All methods of fruit are all within protection scope of the present invention.In the specific embodiment of the invention, preferably using pulverizer to raising
Material raw material and microbial concentration ferment albumen are crushed.Slot size using pulverizer is 0.7~2.5, preferably 0.8~
2.2, more preferably 1.0~2.0.Preferable particle diameter is 20~80 after feedstuff and the crushing of microbial concentration ferment albumen
Mesh, more preferably 25~75 mesh, more preferably 30~70 mesh.
After feedstuff after crushing and microbial concentration ferment albumen are mixed, put into cold granulation device and ferment
Granulation.Feedstuff and microbial concentration ferment albumen after crushing can be put into mixer respectively, thrown again after mixing
Enter in cold granulation device.The mode that the present invention mixes feedstuff and microbial concentration ferment albumen does not limit.In this hair
In bright, the mass ratio of feedstuff and the mixing of microbial concentration ferment albumen is preferably 5~10:1~3, more preferably 6~9:1
~3, it is further 7~8:1~3.
After putting into feedstuff and microbial concentration ferment albumen in cold granulation device, adjustment matches cold granulation device
Ring moulds and compression ratio, the heat source produced with material friction that run at high speed using ring moulds in granulator are created conditions for fermentation.At this
In invention, the ring moulds pore size control of the cold granulation device is preferably 1.5~4.5, is further 1.5~4.3, is further
1.5~4.0.The compression ratio of the cold granulation device ring moulds is preferably 1:5~25, more preferably 1:6~22, more preferably
1:7~20.In the present invention, the ring moulds of cold granulation device and compression ratio are adjusted according to the difference of feed product.Such as, feeding is worked as
When material product is pig's feed, the ring moulds aperture of cold granulation device is 3.0~4.0, compression ratio 1:7~10;Work as feed product
For poultry fodder when, the ring moulds aperture of cold granulation device is 2.0~3.5, compression ratio 1:6~12;When feed product is used for fish
During feed, the ring moulds aperture of cold granulation device is 1.5~3.0, compression ratio 1:15~20.It is cold with the progress of fermentation granulation
Temperature of charge in granulation device is gradually increasing.When the temperature of charge in cold granulation device rises to 60 DEG C~65 DEG C, more preferably
For 62 DEG C~64 DEG C when, terminate fermentation.Fermentation Granulation time of the material of the present invention in the cold granulation device is preferred
For 3~15 minutes, more preferably 5~11 minutes, more preferably 8~10 minutes.
The present invention stops fermentation process by carrying out fast cooling to the material in cold granulation device.It is of the invention preferred
Room temperature is quickly reduced to using fermentation is completed pellet feeding cooling system, other can realize the mode of cooling in this hair
Within bright protection domain, the present invention is not particularly limited this.
Granule materials after cooling are the predigesting feed after the completion of fermenting.
In the present invention, it is not particularly limited, can be used in the prior art to putting into the feedstuff in cold granulation device
Routine or unconventional feed, preferably include grain raw grain, soybean, dregs of beans, corn, fish meal, miscellaneous dregs of rice, whey powder, grease,
Grain byproducts etc..Can be with mixed fodder premix material additive in the feedstuff of the present invention.The feed pre-mixing material addition
Agent can be single premix or compound premix, such as micro-element premix, amino acid premix, trace quantity mineral substance element premix
Deng.
Microbial concentration ferment albumen is employed herein fermentation enzymolysis is carried out to feedstuff.The microbial concentration
Ferment albumen is to be made by Feed Material after microbial bacterial agent fermentation enzymolysis.In the present invention, Feed Material is dregs of beans, rapeseed meal
With one or more of mixtures in cotton dregs, but the present invention is not limited thereto, can also include other kinds of Feed Material.
The present invention is not particularly limited the mode of fermentation enzymolysis, can use conventional fermentation mode of action, can also be sent out in feed
Rapid Fermentation is carried out to Feed Material in ferment mixer and prepares microbial concentration ferment albumen.Make in the specific embodiment of the invention
Microbial concentration ferment albumen is prepared in feed fermentation mixer, specifically includes following steps:
(1) Feed Material input feed fermentation mixer is stirred, keeps the moisture of the Feed Material to exist
50~60wt%;
(2) microbial bacterial agent is added in step (1) described feed fermentation mixer and carries out fermentation enzymolysis, the microorganism
The weight ratio of microbial inoculum and the Feed Material is 7.5~10kg/t, controls the feed fermentation to mix in the fermentation enzymolysis process
The spinner velocity of conjunction machine is 25~30 revs/min;
(3) when the temperature of material in feed fermentation mixer rises to 40~50 DEG C, again add microbial bacterial agent after
Continuous stirring, the weight ratio for adding the microbial bacterial agent and the Feed Material at this time is 7.5~10kg/t;
(4) when the temperature of material in feed fermentation mixer rises to 50~60 DEG C, to the feed fermentation mixer
In add Feed Material again and continue to stir, add the Feed Material at this time with adding the weight of Feed Material in step (1)
Than for 1:1, when temperature of charge reaches 50 DEG C~60 DEG C again, material is cooled down, obtains microbial concentration ferment albumen.
Feed Material is put into feed fermentation mixer first and is stirred, is uniformly mixed Feed Material.According to institute
State in Feed Material containing moisture difference, moderately adjust its moisture.Heretofore described Feed Material is adjusted to its moisture
Content is preferably 52%~58% 50%~60%, and more preferably 53%~56%, meet needed for microbial fermentation
Water content.The present invention is not particularly limited the mode for adjusting the Feed Material water content, can put into and raise in Feed Material
Its moisture is adjusted before material fermentation mixer, water can also be added into feed fermentation mixer at the initial stage of mixing
Point.It is preferred that the moisture of Feed Material is adjusted before fermentation.
After the Feed Material stirs 2~3min in feed fermentation mixer, microbial bacterial agent is added into the feeding
Continuously it is mixed in material fermentation mixer.
Contain 1 × 10 in the microbial bacterial agent of the present invention6~1 × 108The microorganism of CFU/g, is preferably 1 × 107CFU/g
Microorganism.The microorganism is any one in bacillus subtilis, bacillus coagulans and saccharomycete or two or more
Composition.The present invention is not particularly limited the source of mentioned microorganism, can use the purchase strain of in the market, can also
Using the strain for gathering or taming from nature.When using two or more strains, the present invention is to above two or a variety of
The mixed proportion of strain does not have special limitation, bacillus subtilis, bacillus coagulans and the ferment mixed using arbitrary proportion
Female bacterium is all within protection scope of the present invention.In the microbial bacterial agent, bacillus subtilis, bacillus coagulans and yeast
The weight percent amount that bacterium accounts for the microbial bacterial agent is preferably 1:2~3:1, it is further 1:2.2~2.8:1, be further
1:2.5:1。
In order to improve the fermentation efficiency that microorganism utilizes fermented material, shorten fermentation period, the present invention is in feed fermentation
Required bacillus subtilis, bacillus coagulans and saccharomycete carries out scientific matching, different in the different phase of fermentation, addition
The microbial inoculum of ratio microorganism.In the microbial bacterial agent just added, the bacillus subtilis, bacillus coagulans and saccharomycete
Weight ratio be preferably 1:1~2:1, more preferably 1:1~1.5:1, it is further 1:1:1.
In the present invention, the mentioned microorganism microbial inoculum of addition and the weight ratio of the Feed Material are 7.5~10kg/t, excellent
Elect 8.0~9.5kg/t as, more preferably 8.5~9.0kg/t.
In the present invention, after adding the microorganism, the control of the spinner velocity of the feed fermentation mixer 25~30 turns/
Minute, so that the fermentation temperature in feed fermentation mixer is controlled in certain climbing speed, make microorganism in fermentation time
It is interior to keep required oxygen of fermenting.The spinner velocity of preferably feed fermentation mixer of the invention is 26~29 revs/min, into
One step is 27~28 revs/min.At this time, the frequency converter frequency of mixer of fermenting is 45~55HZ, is preferably 48~52HZ, into one
Walk as 50HZ.With the continuation of fermentation process, frictional heat mixes feed fermentation together with the metabolism heat that microbial fermentation is released
The temperature of material rises in conjunction machine, until the temperature of charge in feed fermentation mixer is 40~50 DEG C.In this stage, feed
When the time that fermentation mixer continuously stirs fermentation is 1.0~1.5 small, when being preferably 1.2~1.4 small.
When temperature of charge rises to certain temperature, added again in the feed fermentation mixer microbial bacterial agent after
Continuous stirring fermentation.In the present invention, the temperature of the material is 40 DEG C~50 DEG C when adding microbial bacterial agent again, is preferably 43
DEG C~48 DEG C, more preferably 44 DEG C~46 DEG C.The amount of the microbial bacterial agent added again, is calculated, often by Feed Material
Ton Feed Material adds 7.5~10kg of microbial bacterial agent, is preferably 7.8~9.5kg, more preferably 8.0~8.5kg.This
Containing two or more in bacillus subtilis, bacillus coagulans and saccharomycete in the microbial bacterial agent of secondary addition, not
Need strictly limitation identical with the amount or ratio added first.It is preferably described if fermenting containing two or more microorganisms
The mixed proportion of bacillus subtilis, bacillus coagulans and saccharomycete is 1:2~3:1, more preferably 1:2.2~2.8:
1, more preferably 1:2.5:1.
Feed fermentation mixer continues to stir after microbial bacterial agent is added again, and mixing speed is still maintained at 25~30
Rev/min, it is preferably 26~29 revs/min, is further 27~28 revs/min.At this time, ferment the frequency converter frequency of mixer
For 45~55HZ, it is preferably 48~52HZ, is further 50HZ.After keeping above-mentioned mixing speed for a period of time, temperature of charge is held
It is continuous to rise, treat that temperature of charge rises to 50~60 DEG C, Feed Material is added again when being preferably 52~57 DEG C.This stage, again
Microbial bacterial agent to temperature is added when rising to 50~60 DEG C, the time that feed fermentation mixer continuously stirs is preferably 0.5~
1.5 it is small when, more preferably 0.7~1.2 it is small when.
In the present invention, the Feed Material and the mass ratio of the Feed Material of previous addition that add again are 1:3~3:1, into
One step is preferably 1:2~2:1, more preferably 1:1.After adding Feed Material again, the temperature of charge in feed fermentation mixer
Reduce.When temperature of charge is down to 40 DEG C~50 DEG C, the frequency converter frequency of adjustment feed fermentation mixer is 40~42HZ, preferably
For 41HZ, continue to keep spinner velocity more preferably to continuously stir fermentation for 26~28 revs/min at 25~30 revs/min,
The metabolic heat and physical friction heat produced during the fermentation by microorganism heats up temperature of charge, keeps microbial fermentation institute
The temperature needed.Terminate to ferment when temperature of charge rises to 50~60 DEG C again, is preferably 53~57 DEG C.At this time, add again
When the time of Feed Material fermentation is preferably 0.5~1.5 small, when being more preferably 0.8~1.3 small.
Material is reduced to room temperature, Batch fermentation process while output through transport system outputting material by material after fermentation
Terminate, obtain microbial concentration ferment albumen.
The quick fermentation technology of microbial concentration ferment albumen of the present invention, is fermented using dynamic type, using microorganism to raising
Material material ferments, and promotes the simultaneous oxygen Rapid Fermentation of Feed Material, accelerates the biodegradation of organic matter in Feed Material, shortens
Fermentation period, improves the vigor of microbial concentration ferment albumen.Every batch of fermentation period most can reach soon 3 it is small when, it is effectively save
Time, improves production efficiency, meets industrial production demand.
In order to ensure the activity of microorganism in microbial bacterial agent, in the microbial bacterial agent of the present invention, except including withered grass
Bacillus, bacillus coagulans, outside saccharomycete, also added other auxiliary materials.A certain proportion of skin of beancurd is added in the present invention
Powder, certain nutrition supply is provided for microorganism.In the microbial bacterial agent of the present invention, microbial bacterial agent is formed with auxiliary material weight
Gross weight.Wherein, skin of beancurd powder addition weight percentage is 10~15%, is preferably 11~14%, more preferably 12~
13%.In the present invention, the auxiliary material further includes diatomite 85~90%, is preferably 87~89%, and the addition as microorganism carries
Body.
Mentioned microorganism microbial inoculum can use the preparation method of this area routine to be prepared.The microorganism that the present invention uses
Microbial inoculum preferably using by containing bacillus subtilis, bacillus coagulans, saccharomycete bacterium solution in proportionally add skin of beancurd powder,
Diatomite, carries out low temperature drying and obtains microbial bacterial agent.The temperature of low temperature drying is 30~40 DEG C, is preferably 31~37 DEG C, into
One step is preferably 32~35 DEG C;The time of low temperature drying is 40~60min, is preferably 42~55min, more preferably 44~
50min。
Microbe concentration ferment albumen of the present invention carries out predigestion to feedstuff.The digestion ferment of microorganism secretion
Element, such as amylase, lipase, cellulase and protease, by macromolecular nutritional ingredient (starch, fat, fiber in feedstuff
And protein etc.) small molecule, such as monosaccharide and disaccharide, aliphatic acid, amino acid and polypeptide are resolved into, help poultry to digest and assimilate.Together
When beneficial microbe raw enteron aisle after can inhibit harmful bacteria growth, produce antibacterial material, improve enterobacteriaceae phase, reduce harmful bacteria production
Raw noxious material or gases affect poultry body health;Intestinal flora has adjusting immune function, reduces the use of antibiotic.Predigestion
Beneficial microbe in feed can inhibit the spoilage organisms growth for producing odor, therefore can improve excrement quality, reduces odor and has
Evil gas, while reduce the discharge of ammonia nitrogen.Generation changes the material of livestock and poultry body fat acid metabolic, reduces muscle fibre density, and
The total amount of amino acid can be improved, therefore it is delicious fresh and tender to produce meat.
With reference to embodiment, the present invention will be described in detail, but they cannot be interpreted as protecting the present invention
The restriction of scope.
Embodiment 1
Bacillus subtilis and bacillus coagulans are pressed 1:1 ratio expands numerous culture.Added in cultured liquid bacteria
Skin of beancurd powder, diatomite, low temperature drying 50min, is prepared into microbial bacterial agent at 35 DEG C.In the microbial bacterial agent by weight
Meter, containing 10% skin of beancurd powder, 90% diatomite, wherein the bacillus subtilis contained and the content of bacillus coagulans are respectively
1×108CFU/g。
Feed Material is fermented in feed fermentation mixer using microbial bacterial agent, prepares microbial concentration ferment
Albumen.Detailed process is as follows:
The feed fermentation mixer that 1000kg dregs of beans input is had been turned on, added drainage 700kg and stirred 3 minutes, and made feeding
Feed Material moisture is 50% in material fermentation mixer;7.5kg microbial bacterial agents are added into above-mentioned feed fermentation mixer
In, frequency converter frequency 50HZ, spinner velocity control at 25 revs/min, continuously stir 1.5 it is small when, treat that temperature of charge rises to
After 45 DEG C, addition 10kg microbial bacterial agents to feed fermentation mixer, keep identical frequency converter frequency and spinner velocity again,
Continuously stir 1 it is small when after, temperature of charge rises to 55 DEG C.1000kg cotton dregs are added into feed fermentation mixer, adjust frequency conversion
Device frequency is 40HZ, and it is 26 revs/min to control spinner velocity, is continuously stirred for after sixty minutes, temperature of charge rises to 60 DEG C.Beat
Feed fermentation mixer discharge port is opened, material enters transport system, and material is reduced to room temperature by conveying at the same time, and Batch fermentation process is whole
Only.By material coating-dividing sealing, specification is 25 kilograms/bag for weighing, packaging system.
Feedstuff and microbial concentration ferment albumen are put into cold granulation device, prepare cold granulation particle feed.Tool
Body process is as follows:
A certain proportion of 1000 kilograms of basal feed raw material is put into sieve aperture ф for 0 kilogram with microbial concentration ferment protein 10
2.0 pulverizers crush, and the particle diameter after crushing is 30 mesh.Feedstuff after crushing and microbial concentration ferment albumen are sent into
Start mixer to stir 120 seconds, after material is uniform.Start cold granulation device, uniformly mixed material is put into cold granulation device
In, the ring moulds ф for controlling cold granulation device is 4.5, compression ratio 1:9, ring moulds run at high speed in granulator and material friction produces
Heat source create conditions for fermentation.When temperature of charge reaches 63 DEG C, pellet feeding cooling system is completed into fermentation and is reduced to
Room temperature.By material coating-dividing sealing, specification is 50 kilograms/bag for weighing, packaging system.
Embodiment 2
Bacillus subtilis, bacillus coagulans and saccharomycete are pressed 1:1:1 ratio expands numerous culture.In cultured liquid
Skin of beancurd powder, diatomite are added in bacterium, the low temperature drying 45min at 37 DEG C, is prepared into the first microbial bacterial agent.First micro- life
In thing microbial inoculum by weight, containing 15% skin of beancurd powder, 85% diatomite, wherein the bacillus subtilis contained, condensation gemma
The total content of bacillus and saccharomycete is 1 × 109CFU/g。
Bacillus subtilis and bacillus coagulans are pressed 1:3:1 ratio expands numerous culture.Add in cultured liquid bacteria
Enter skin of beancurd powder, diatomite the low temperature drying 45min at 37 DEG C, be prepared into the second microbial bacterial agent.Second microbial bacterial agent
In by weight, containing 15% skin of beancurd powder, 85% diatomite, wherein the bacillus subtilis contained, bacillus coagulans and
The total content of saccharomycete is 1 × 109CFU/g。
Feed Material is fermented in feed fermentation mixer using microbial bacterial agent, prepares microbial concentration ferment
Albumen.Detailed process is as follows:
The feed fermentation mixer that 500kg dregs of beans and 500kg cotton dregs input are had been turned on, added drainage 750kg stirrings 2
Minute, it is 60% to make Feed Material moisture in feed fermentation mixer;The first microbial bacterial agents of 10kg are added into above-mentioned feeding
In material fermentation mixer, it is 47HZ control frequency converter frequency, spinner velocity control at 30 revs/min, continuously stir 1 it is small when, treat
After temperature of charge rises to 40 DEG C, the second microbial bacterial agents of 10kg are added again to feed fermentation mixer, control frequency converter frequency
Rate is 51HZ, and spinner velocity is controlled at 29 revs/min, continuously stir 1 it is small when after, temperature of charge rises to 50 DEG C.Sent out to feed
1000kg rapeseed meals are added in ferment mixer, adjusting frequency converter frequency is 41HZ, and it is 27 revs/min to control spinner velocity, continuously again
After sixty minutes, temperature of charge rises to 60 DEG C for stirring.Feed fermentation mixer discharge port is opened, material enters transport system, defeated
Send while material is reduced to room temperature, Batch fermentation process terminates.Weighing, packaging system are public for 25 by material coating-dividing sealing, specification
Jin/bag.
Feedstuff and microbial concentration ferment albumen are put into cold granulation device, prepare cold granulation particle feed.Tool
Body process is as follows:
A certain proportion of 1000 kilograms of basal feed raw material is put into sieve aperture ф for 0 kilogram with microbial concentration ferment protein 20
2.0 pulverizers crush, and the particle diameter after crushing is 40 mesh.Feedstuff after crushing and microbial concentration ferment albumen are sent into
Start mixer to stir 120 seconds, material is uniform.Start cold granulation device, uniformly mixed material put into cold granulation device,
The ring moulds ф for controlling cold granulation device is 3.0, compression ratio 1:10, ring moulds run at high speed in granulator and material friction produces
Heat source creates conditions for fermentation.When temperature of charge reaches 66 DEG C, pellet feeding cooling system is completed into fermentation and is reduced to often
Temperature.By material coating-dividing sealing, specification is 50 kilograms/bag for weighing, packaging system.
Embodiment 3
Skin of beancurd powder, diatomite low temperature drying 50min at 40 DEG C are added in the bacterium solution containing bacillus subtilis, is prepared
Into the first microbial bacterial agent.In first microbial bacterial agent by weight, containing 10% skin of beancurd powder, 90% diatomite, its
In the total content containing bacillus subtilis be 1 × 108CFU/g。
Skin of beancurd powder, diatomite low temperature drying 50min at 40 DEG C are added in the bacterium solution containing bacillus coagulans, is prepared
Into the second microbial bacterial agent.In second microbial bacterial agent by weight, containing 10% skin of beancurd powder, 90% diatomite, its
In the total content of bacillus coagulans that contains be 1 × 108CFU/g。
Feed Material is fermented in feed fermentation mixer using microbial bacterial agent, prepares fermented feed.Specifically
Process is as follows:
The feed fermentation mixer that 500kg rapeseed meals and 500kg cotton dregs input are had been turned on, added drainage 650kg stirrings 2
Minute, it is 52% to make Feed Material moisture in feed fermentation mixer;The first microbial bacterial agents of 8kg are added into above-mentioned feed
Ferment in mixer, it is 52HZ control frequency converter frequency, spinner velocity control at 27 revs/min, continuously stir 1 it is small when, treat thing
After material temperature degree rises to 42 DEG C, the second microbial bacterial agents of 8kg are added again to feed fermentation mixer, control the frequency converter frequency to be
50HZ, spinner velocity control at 28 revs/min, continuously stir 1 it is small when after, temperature of charge rises to 60 DEG C.Mixed to feed fermentation
1000kg rapeseed meals are added in conjunction machine, adjusting frequency converter frequency is 42HZ, and it is 30 revs/min to control spinner velocity, is continuously stirred for
After sixty minutes, temperature of charge rises to 60 DEG C again.Feed fermentation mixer discharge port is opened, material enters transport system, defeated
Send while material is reduced to room temperature, Batch fermentation process terminates.Weighing, packaging system are public for 25 by material coating-dividing sealing, specification
Jin/bag.
Feedstuff and microbial concentration ferment albumen are put into cold granulation device, prepare cold granulation particle feed.Tool
Body process is as follows:
A certain proportion of 1000 kilograms of basal feed raw material is put into sieve respectively with 300 kilograms of microbial concentration ferment albumen
ф 1.0 pulverizers in hole crush, and the particle diameter after crushing is 70 mesh.Feedstuff after crushing and microbial concentration ferment albumen are sent
Enter to have been turned on mixer to stir 120 seconds, material is uniform.Start cold granulation device, the uniformly mixed cold granulation of material input is filled
In putting, the ring moulds ф for controlling cold granulation device is 1.5, compression ratio 1:20, ring moulds run at high speed and material friction in granulator
The heat source of generation creates conditions for fermentation.When temperature of charge reaches 70 DEG C, fermentation will be completed pellet and be sent into cooling system
System is reduced to room temperature.By material coating-dividing sealing, specification is 50 kilograms/bag for weighing, packaging system.
The preparation method of the cold granulation feed of present invention fermentation, it is while granulation, feed is former using the cold granulation device that ferments
Material and microbial concentration ferment albumen organically combine, and Rapid Fermentation is digested into predigesting feed.Utilize the stronger enzymolysis of microorganism
Ability, partially or mostly resolves into feedstuff the small-molecule substance that animal directly absorbs, is more easy to after animal edible
Digestion and absorption;In addition the anti-nutritional factors to feedstuff and anaphylactogen degraded are obvious.No longer need to heat in preparation process
Device, without steam regulation of texture, conditioning of texture, directly mutually rubs fever, there is provided fermentation condition quickly realizes microorganism increasing by machinery and material
Value and macromolecular complex is changed into small-molecule substance, realizes feed predigestion function.Technique is simple, easy to high-activity biological feed
Mass production, granulation it is best in quality.
The above is only the preferred embodiment of the present invention, it is noted 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 also should
It is considered as protection scope of the present invention.
Claims (4)
1. a kind of preparation method for the cold granulation feed that ferments, it is characterised in that comprise the following steps:
After feedstuff and microbial concentration ferment albumen are pulverized and mixed, granulation of fermenting in cold granulation device is put into;Adjustment
Ring moulds and compression ratio with the cold granulation device, rise the temperature in granulation of the material in the cold granulation device, work as temperature
When degree rises to 60 DEG C~65 DEG C, cooling, obtains the cold granulation feed that ferments;
The ring moulds aperture of the cold granulation device is 1.5~4.5, compression ratio 1:5~25;
Fermentation Granulation time of the material in the cold granulation device is 3~15 minutes;
The microbial concentration ferment albumen is to be made by Feed Material after microbial fermentation digests;The microbial concentration ferment
Fibroin is prepared by method comprising the following steps:
(1) Feed Material input feed fermentation mixer is stirred, keep the moisture of the Feed Material 50~
60wt%;
(2) microbial bacterial agent is added in step (1) described feed fermentation mixer and carries out fermentation enzymolysis, the microbial bacterial agent
Weight ratio with the Feed Material is 7.5~10kg/t, and the feed fermentation mixer is controlled in the fermentation enzymolysis process
Spinner velocity be 25~30 revs/min;
(3) when the temperature of material in feed fermentation mixer rises to 40~50 DEG C, microbial bacterial agent is added again and continues to stir
Mix, the weight ratio for adding the microbial bacterial agent and the Feed Material at this time is 7.5~10kg/t;
(4) when the temperature of material in feed fermentation mixer rises to 50~60 DEG C, into the feed fermentation mixer again
Secondary addition Feed Material continues to stir, and add the Feed Material at this time is with the weight ratio that Feed Material is added in step (1)
1:1, when temperature of charge reaches 50 DEG C~60 DEG C again, material is cooled down, obtains microbial concentration ferment albumen;
Contain 1 × 10 in the microbial bacterial agent6~1 × 108The microorganism of CFU/g, the microorganism for bacillus subtilis,
Any one in bacillus coagulans and saccharomycete or two or more compositions;The feedstuff and the microorganism are dense
The mass ratio of contracting ferment albumen is 5~10:1~3.
2. preparation method according to claim 1, it is characterised in that feedstuff and microbial concentration the ferment albumen
Particle diameter after crushing is 20~80 mesh.
3. preparation method according to claim 1, it is characterised in that in step (2), the bacillus subtilis, condensation
The mass ratio of bacillus and saccharomycete is 1:1~2:1;In step (3), the bacillus subtilis, bacillus coagulans and
The mass ratio of saccharomycete is 1:2~3:1.
4. preparation method according to claim 1, it is characterised in that the feedstuff is expanded soybean, dregs of beans, jade
One or more of mixtures in rice, wheat-middlings, flour, fish meal, wheat skin, wheat, rice, rice bran meal, rapeseed meal and cotton dregs.
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