CN108576373A - A kind of novel biological fermentation feed production technology - Google Patents

A kind of novel biological fermentation feed production technology Download PDF

Info

Publication number
CN108576373A
CN108576373A CN201810271419.9A CN201810271419A CN108576373A CN 108576373 A CN108576373 A CN 108576373A CN 201810271419 A CN201810271419 A CN 201810271419A CN 108576373 A CN108576373 A CN 108576373A
Authority
CN
China
Prior art keywords
parts
fermentation
temperature
hours
production technology
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810271419.9A
Other languages
Chinese (zh)
Inventor
乔先良
余世发
王海
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hubei Wuerli Biological Engineering Ltd By Share Ltd
Original Assignee
Hubei Wuerli Biological Engineering Ltd By Share Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hubei Wuerli Biological Engineering Ltd By Share Ltd filed Critical Hubei Wuerli Biological Engineering Ltd By Share Ltd
Priority to CN201810271419.9A priority Critical patent/CN108576373A/en
Publication of CN108576373A publication Critical patent/CN108576373A/en
Pending legal-status Critical Current

Links

Classifications

    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K10/00Animal feeding-stuffs
    • A23K10/10Animal feeding-stuffs obtained by microbiological or biochemical processes
    • A23K10/12Animal feeding-stuffs obtained by microbiological or biochemical processes by fermentation of natural products, e.g. of vegetable material, animal waste material or biomass
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K40/00Shaping or working-up of animal feeding-stuffs
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23KFODDER
    • A23K40/00Shaping or working-up of animal feeding-stuffs
    • A23K40/30Shaping or working-up of animal feeding-stuffs by encapsulating; by coating

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Polymers & Plastics (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Food Science & Technology (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Sustainable Development (AREA)
  • Biochemistry (AREA)
  • Biomedical Technology (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Physiology (AREA)
  • Animal Husbandry (AREA)
  • Fodder In General (AREA)

Abstract

The invention discloses a kind of novel biological fermentation feed production technology, production technology is as follows:A, coarse crushing:Raw material are chosen by following ingredient and weight:10 ~ 14 parts of 15 ~ 22 parts of corn, 12 ~ 18 parts of soybean, 11 ~ 15 parts of rape cake, 12 ~ 16 parts of sesame-send cake, 13 ~ 17 parts of wheat bran and fish meal, it is 26 ~ 31 mesh that by raw material, coarse powder, which is broken to granularity, respectively;B, finely divided;C, wet method expanding treatment;D, fermenting microbe activates;E, solid fermentation;F, spray attachment protective agent;G, vacuum freeze drying;H, detection, packaging, the method have the advantages that:This production technology is by wet method bulking process and bio-fermentation process perfect adaptation, wet method expanding treatment process is the problem of solid fermentation process improves efficiency, and solid fermentation process supplements the losses such as nutriment, active biological enzyme and beneficial bacterium existing for wet method expanding treatment in the process.

Description

A kind of novel biological fermentation feed production technology
Technical field
The present invention relates to the technical fields of feed production technology, more particularly to the skill of fermented feed production technology Art field.
Background technology
Expanded pellet diet is feedstuff in the environment of high temperature, high pressure, high shear force and high-moisture, pass through it is quenched, rise Temperature, supercharging, the bulk porous particle feed for squeezing out die hole and being formed after being depressured suddenly.After expanding treatment, fragrance increases feed Add, palatability improves, and can stimulate animal appetite, while the backbone of the organic matters such as protein, fat can be promoted to become short chain Structure is easy to digest.However, expanded pellet diet has the following disadvantages:1, vitamin is lost, the high temperature generated in expanded pellet diet production High pressure can make vitamin A, vitamin D and folic acid loss 11% or so, the loss late of vitamin B1 be 17% or so, vitamin C and The loss late of vitamin K is 50% or so.2, enzyme preparation is lost, and the optimum temperature of enzyme is 35 ~ 40 DEG C, not more than 50 DEG C, swollen The activity of high temperature, high pressure, high humidity effect during change, most of enzyme preparations will all lose totally.3, microorganism loses, feed In more microorganism formulation mainly have Lactococcus, saccharomycete, streptococcus, bacillus etc., puffing process that can lead to these Viable bacteria in microorganism formulation largely loses.4, protein and amino acid loss, a part of reduced sugar and free in puffing process Amino acid generates Maillard reaction, reduces the utilization rate of protein, and lead to the amino acid such as lysine, arginine and histidine Loss.5, puffing technique can reduce its digestive utilization ratio to dregs of beans, fish meal etc..
Biological fermentation feed refers to the feed obtained after being fermented to feedstuff using microbial bacterial agent, biofermentation Feed has many advantages, such as to improve efficiency of feed utilization, improvement feed quality.Biological feedstuff fermentation be broadly divided into aerobic solid fermentation and Anaerobic solids ferment, however, that there are labor intensity is big for aerobic solid fermentation, the shortcomings of easily causing living contaminants;Anaerobic solids Fermentation the shortcomings of there are the microorganism speed of growth is slower, and fermentation period is long.
Invention content
The purpose of the present invention is exactly to provide one kind in order to solve above-mentioned deficiency and feed digestion absorptivity can be improved, and is reduced The loss of nutriment, active biological enzyme and beneficial bacterium etc., and living contaminants can be reduced, shorten fermentation time, improves production effect The novel biological fermentation feed production technology of rate.
In order to solve the above-mentioned technical problem technical solution that the present invention uses is as follows:
A kind of novel biological fermentation feed production technology, production technology are as follows:
A, coarse crushing:Raw material are chosen by following ingredient and weight:15 ~ 22 parts of corn, 12 ~ 18 parts of soybean, rape cake 10 ~ 14 parts of 11 ~ 15 parts, 12 ~ 16 parts of sesame-send cake, 13 ~ 17 parts of wheat bran and fish meal, by raw material respectively coarse powder be broken to granularity be 26 ~ 31 mesh;
B, finely divided:Raw material after step a coarse crushings are sufficiently mixed uniformly, mixed raw material fine powder is broken to grain Degree is 40 ~ 50 mesh, and mixed material is made;
C, wet method expanding treatment:Mixed material is sent into the quality-adjusting device of wet-process puffing machine and carries out modifier treatment, in quenched process Middle that steam is passed through into quality-adjusting device, 41% ~ 47%, moisture control exists for the curing degree control of the mixed material after modifier treatment 25% ~ 32%, temperature is controlled at 85 ~ 92 DEG C, then, the mixed material after modifier treatment is discharged into the puffing of wet-process puffing machine Intracavitary carries out extrusion, is made expanded material, and the unit weight control of expanded material is 360 ~ 400g/L, curing degree control for 91% ~ 94%;
D, fermenting microbe activates:3 ~ 5 parts of fermenting microbe, 16 ~ 20 parts of wheat bran, 2 ~ 3 parts of sucrose and water 18 ~ 22 are taken by weight ratio Part, and be sufficiently mixed uniformly, standing 4 ~ 5 hours at a temperature of 34 ~ 38 DEG C is made fermenting agent, and the fermenting microbe is by weight Than for(9~11):(8~10):(10~12):(2~5)Lactobacillus plantarum, bacillus subtilis, saccharomycete and enterococcus faecalis structure At;
E, solid fermentation:Expanded material layering tiling is placed in closed environment, the uniformly sprinkling fermentation in every layer of expanded material Suitable water is added into expanded material for microbial inoculum, by the control of the moisture of expanded material 40% ~ 45%, to expanded material into Row anaerobic fermentation, fermentation temperature are controlled at 31 ~ 36 DEG C, and fermentation terminates for 3 ~ 5 days, and fermentation materials are made;
F, spray attachment protective agent:10 ~ 12 parts of animal fat, 9 ~ 11 parts of molasses, defatted milk are chosen by following ingredient and weight 60 ~ 64 parts of 8 ~ 12 parts of powder and water, and be sufficiently mixed and protective agent uniformly is made, by the uniform spray attachment of protective agent fermentation materials table Coating fermentation materials are made in face;
G, vacuum freeze drying:Coating fermentation materials are evenly laid out on pallet, and be sent into -40 ~ -38 DEG C of household freezer into Row is anxious to be frozen, and the central temperature of coating fermentation materials is made to be down to -30 ~ -26 DEG C, and the anxious coating fermentation materials frozen are sent into vacuum and are done It in the drying box of drying system, is thermally dried under the vacuum environment of 10 ~ 40pa, when heat drying does vacuum drying system Initial temperature control in dry case is 25 ~ 28 DEG C, and constant temperature 5.5 ~ 5.8 hours;Then it utilizes 0.6 ~ 1 hour, it will be in drying box Temperature rise to 30 ~ 33 DEG C, and constant temperature 8.6 ~ 9 hours;Followed by 1.2 ~ 1.5 hours, the temperature in drying box is risen to 38 ~ 40 DEG C, and constant temperature 3.2 ~ 3.7 hours;It recycles 1.3 ~ 1.5 hours, the temperature in drying box is down to 34 ~ 36 DEG C, and constant temperature 7.5 ~ 8 hours;It recycles 1.4 ~ 1.8 hours, the temperature in drying box is risen to 38 ~ 41 DEG C, and constant temperature 2.6 ~ 2.8 hours;Most It utilizes 1 ~ 1.2 hour afterwards, the temperature in drying box is down to 32 ~ 35 DEG C, and constant temperature is until the moisture of coating fermentation materials is contained Amount is dry to 4% ~ 8%, and biological fermentation feed is made;
H, detection, packaging:Biological fermentation feed is crossed metal detector to be detected, vacuum then is carried out to biological fermentation feed Packaging.
Coarse crushing is carried out to raw material using beater disintegrating machine during the coarse crushing, in the finely divided process It is middle finely divided to the progress of mixed raw material using micronizer.
The wet-process puffing machine is single screw squeezing expansion machine.
The animal fat is fish oil.
The lactobacillus plantarum is the lactobacillus plantarum bacterium powder that Changzhou beneficial bacteria adds bio tech ltd to produce, described withered Careless bacillus is the bacillus subtilis powder of Jiangsu Lv Ke Bioisystech Co., Ltd production, and the saccharomycete is Cangzhou City The saccharomycete bacterium powder of the bio tech ltd Zhong Xin production, the enterococcus faecalis, which is Luoyang Ou Kebaike biotechnology shares, to be had The enterococcus faecalis bacterium powder of limit company production.
The present invention is using the attainable advantageous effect of above-mentioned technical solution institute:This production technology is by the puffing work of wet method Skill and bio-fermentation process perfect adaptation, wet method expanding treatment process are that solid fermentation process improves efficiency, solid fermentation mistake Journey supplements the problem of losses such as nutriment, active biological enzyme and beneficial bacterium existing for wet method expanding treatment in the process.Wet method High temperature, high pressure during expanding treatment and mechanism make the basic nutritions such as starch and the protein in raw material at distribution Biochemical and physical change forms scheduled state.Microstructure detaches in starch, forms that gap is big and irregular stereoscopic graticule Shape structure, and par-tial polysaccharide substance is converted into the monosaccharide more easily utilized or oligosaccharides form.Protein is moderately denaturalized, extraneous Protease be more easy to enter protein interior.Cellulose components dietary fiber amount after extruding increases, health-care effect enhancing.By After wet method expanding treatment, raw material have passed through one of sterilisation program using high temperature action, various nutriment packets in raw material The substances such as carbohydrate, protein are included to be easier to be absorbed by microorganism conversion after pretreatment.Solid fermentation process inoculation is a large amount of Beneficial bacterium includes lactobacillus plantarum, bacillus subtilis, saccharomycete and enterococcus faecalis, and beneficial bacterium is after wet method expanding treatment Advantageous nutritional condition under reproduction speed can accelerate, reduce the probability of pollution microbes, shorten the time of solid fermentation, improve Production efficiency.Contain a large amount of active biological enzyme in fermentation materials after fermentation, macromolecular substances in feed can be decomposed For small molecule organic compound, contains a large amount of beneficial microbe and its metabolite simultaneously, the reparation of enteron aisle villus can be promoted, carried The absorptivity of high feed.Organic acid in this biological fermentation feed can reduce intestinal pH, while also contain antibacterial substance(Peroxide Change hydrogen), the proliferation of pathogen can be effectively inhibited, ensures intestinal microecology balance, promotes to absorb, reduces total feces volume.Feed In microorganism when being discharged with excrement, can further decompose excrement in vitro, reduce the pernicious gases such as colony house ammonia, hydrogen sulfide Concentration improves breeding environment.Expanded material is dried it after solid fermentation, using vacuum freeze-drying method, and And the vacuum freeze drying temperature curve of this production technology is according to the well-designed optimum temperature change curve of fermentation materials, together When, the spray attachment protective agent on fermentation materials surface plays very the microorganisms such as beneficial bacterium in fermentation materials in drying process Good protective effect, is then vacuum-packed, to effectively increase the beneficial bacterium viable bacteria content in this biological fermentation feed, The time-to-live for extending beneficial bacterium avoids conventional drying processes and is lost to the beneficial bacterium in fermentation materials.Due to puff For material after solid fermentation, the bulked structure of itself reduces expanded level due to water suction, is made by vacuum freeze drying Obtaining the expanded material after solid fermentation becomes loose porous, restores its original puffing state again, to play very Good attractant effect, improves the palatability of feed.
Specific implementation mode
Embodiment 1:A kind of novel biological fermentation feed production technology, production technology are as follows:
A, coarse crushing:Raw material are chosen by following ingredient and weight proportion:15 kilograms of corn, 12 kilograms of soybean, rape cake 11,000 Gram, 12 kilograms of sesame-send cake, 13 kilograms of wheat bran and 10 kilograms of fish meal, it is 26 mesh that by raw material, coarse powder, which is broken to granularity, respectively;
B, finely divided:Raw material after step a coarse crushings are sufficiently mixed uniformly, mixed raw material fine powder is broken to grain Degree is 40 mesh, and mixed material is made;
C, wet method expanding treatment:Mixed material is sent into the quality-adjusting device of wet-process puffing machine and carries out modifier treatment, in quenched process It is middle that steam is passed through into quality-adjusting device, the control of the curing degree of the mixed material after modifier treatment 41%, moisture control 25%, Temperature is controlled at 85 DEG C, then, the mixed material after modifier treatment is discharged into the Builking cavity of wet-process puffing machine and is squeezed It presses puffing, is made expanded material, the unit weight control of expanded material is 400g/L, and curing degree control is 91%;
D, fermenting microbe activates:18 kilograms of 3 kilograms of fermenting microbe, 16 kilograms of wheat bran, 2 kilograms of sucrose and water are taken by weight ratio, And be sufficiently mixed uniformly, it stands 4 hours at a temperature of 34 DEG C and fermenting agent is made, the fermenting microbe is 9 by weight ratio:8: 10:2 lactobacillus plantarum, bacillus subtilis, saccharomycete and enterococcus faecalis is constituted;
E, solid fermentation:Expanded material layering tiling is placed in closed environment, the uniformly sprinkling fermentation in every layer of expanded material Suitable water is added into expanded material for microbial inoculum, and the moisture of expanded material is controlled 40%, is detested expanded material Aerobe fermentation, fermentation temperature are controlled at 31 DEG C, and fermentation terminates for 3 days, and fermentation materials are made;
F, spray attachment protective agent:10 kilograms of animal fat, 9 kilograms of molasses, skimmed milk power 8,000 are chosen by following ingredient and weight proportion Gram and 60 kilograms of water, and be sufficiently mixed and protective agent uniformly be made, by the uniform spray attachment of protective agent on the surface of fermentation materials, packet is made Film fermentation material;
G, vacuum freeze drying:Coating fermentation materials are evenly laid out on pallet, and be sent into -40 DEG C of household freezer and carry out suddenly Freeze, the central temperature of coating fermentation materials is made to be down to -30 DEG C, the anxious coating fermentation materials frozen are sent into vacuum drying system In drying box, be thermally dried under the vacuum environment of 10pa, will be in vacuum drying system drying box when heat drying just The control of beginning temperature is 25 DEG C, and constant temperature 5.5 hours;Then it utilizes 0.6 hour, the temperature in drying box is risen to 30 DEG C, and permanent Temperature 8.6 hours;Followed by 1.2 hours, the temperature in drying box is risen to 38 DEG C, and constant temperature 3.2 hours;It recycles 1.3 small When, the temperature in drying box is down to 34 DEG C, and constant temperature 7.5 hours;It recycles 1.4 hours, the temperature in drying box is risen to 38 DEG C, and constant temperature 2.6 hours;It finally utilizes 1 hour, the temperature in drying box is down to 32 DEG C, and constant temperature is until coating is sent out The moisture of ferment material is dried to 4%, and biological fermentation feed is made;
H, detection, packaging:Biological fermentation feed is crossed metal detector to be detected, vacuum then is carried out to biological fermentation feed Packaging.
Embodiment 2:A kind of novel biological fermentation feed production technology, production technology are as follows:
A, coarse crushing:Raw material are chosen by following ingredient and weight proportion:18 kilograms of corn, 15 kilograms of soybean, rape cake 13,000 Gram, 14 kilograms of sesame-send cake, 15 kilograms of wheat bran and 12 kilograms of fish meal, it is 28 mesh that by raw material, coarse powder, which is broken to granularity, respectively;
B, finely divided:Raw material after step a coarse crushings are sufficiently mixed uniformly, mixed raw material fine powder is broken to grain Degree is 45 mesh, and mixed material is made;
C, wet method expanding treatment:Mixed material is sent into the quality-adjusting device of wet-process puffing machine and carries out modifier treatment, in quenched process It is middle that steam is passed through into quality-adjusting device, the control of the curing degree of the mixed material after modifier treatment 44%, moisture control 28%, Temperature is controlled at 89 DEG C, then, the mixed material after modifier treatment is discharged into the Builking cavity of wet-process puffing machine and is squeezed It presses puffing, is made expanded material, the unit weight control of expanded material is 380g/L, and curing degree control is 92%;
D, fermenting microbe activates:20 kilograms of 4 kilograms of fermenting microbe, 18 kilograms of wheat bran, 2 kilograms of sucrose and water are taken by weight ratio, And be sufficiently mixed uniformly, it stands 4 hours at a temperature of 36 DEG C and fermenting agent is made, the fermenting microbe is 10 by weight ratio: 9:11:3 lactobacillus plantarum, bacillus subtilis, saccharomycete and enterococcus faecalis is constituted;
E, solid fermentation:Expanded material layering tiling is placed in closed environment, the uniformly sprinkling fermentation in every layer of expanded material Suitable water is added into expanded material for microbial inoculum, and the moisture of expanded material is controlled 42%, is detested expanded material Aerobe fermentation, fermentation temperature are controlled at 33 DEG C, and fermentation terminates for 4 days, and fermentation materials are made;
F, spray attachment protective agent:11 kilograms of animal fat, 10 kilograms of molasses, skimmed milk power 10 are chosen by following ingredient and weight proportion Kilogram and 62 kilograms of water, and be sufficiently mixed and protective agent uniformly be made, by the uniform spray attachment of protective agent on the surface of fermentation materials, be made Coating fermentation materials;
G, vacuum freeze drying:Coating fermentation materials are evenly laid out on pallet, and be sent into -39 DEG C of household freezer and carry out suddenly Freeze, the central temperature of coating fermentation materials is made to be down to -28 DEG C, the anxious coating fermentation materials frozen are sent into vacuum drying system In drying box, be thermally dried under the vacuum environment of 25pa, will be in vacuum drying system drying box when heat drying just The control of beginning temperature is 27 DEG C, and constant temperature 5.7 hours;Then it utilizes 0.8 hour, the temperature in drying box is risen to 31 DEG C, and permanent Temperature 8.8 hours;Followed by 1.3 hours, the temperature in drying box is risen to 39 DEG C, and constant temperature 3.5 hours;It recycles 1.4 small When, the temperature in drying box is down to 35 DEG C, and constant temperature 7.8 hours;It recycles 1.6 hours, the temperature in drying box is risen to 39 DEG C, and constant temperature 2.7 hours;It finally utilizes 1.1 hours, the temperature in drying box is down to 33 DEG C, and constant temperature is until by coating The moisture of fermentation materials is dried to 6%, and biological fermentation feed is made;
H, detection, packaging:Biological fermentation feed is crossed metal detector to be detected, vacuum then is carried out to biological fermentation feed Packaging.
Embodiment 3:A kind of novel biological fermentation feed production technology, production technology are as follows:
A, coarse crushing:Raw material are chosen by following ingredient and weight proportion:22 kilograms of corn, 18 kilograms of soybean, rape cake 15,000 Gram, 16 kilograms of sesame-send cake, 17 kilograms of wheat bran and 14 kilograms of fish meal, it is 31 mesh that by raw material, coarse powder, which is broken to granularity, respectively;
B, finely divided:Raw material after step a coarse crushings are sufficiently mixed uniformly, mixed raw material fine powder is broken to grain Degree is 50 mesh, and mixed material is made;
C, wet method expanding treatment:Mixed material is sent into the quality-adjusting device of wet-process puffing machine and carries out modifier treatment, in quenched process It is middle that steam is passed through into quality-adjusting device, the control of the curing degree of the mixed material after modifier treatment 47%, moisture control 32%, Temperature is controlled at 92 DEG C, then, the mixed material after modifier treatment is discharged into the Builking cavity of wet-process puffing machine and is squeezed It presses puffing, is made expanded material, the unit weight control of expanded material is 360g/L, and curing degree control is 94%;
D, fermenting microbe activates:22 kilograms of 5 kilograms of fermenting microbe, 20 kilograms of wheat bran, 3 kilograms of sucrose and water are taken by weight ratio, And be sufficiently mixed uniformly, it stands 5 hours at a temperature of 38 DEG C and fermenting agent is made, the fermenting microbe is 11 by weight ratio: 10:12:5 lactobacillus plantarum, bacillus subtilis, saccharomycete and enterococcus faecalis is constituted;
E, solid fermentation:Expanded material layering tiling is placed in closed environment, the uniformly sprinkling fermentation in every layer of expanded material Suitable water is added into expanded material for microbial inoculum, and the moisture of expanded material is controlled 45%, is detested expanded material Aerobe fermentation, fermentation temperature are controlled at 36 DEG C, and fermentation terminates for 5 days, and fermentation materials are made;
F, spray attachment protective agent:12 kilograms of animal fat, 11 kilograms of molasses, skimmed milk power 12 are chosen by following ingredient and weight proportion Kilogram and 64 kilograms of water, and be sufficiently mixed and protective agent uniformly be made, by the uniform spray attachment of protective agent on the surface of fermentation materials, be made Coating fermentation materials;
G, vacuum freeze drying:Coating fermentation materials are evenly laid out on pallet, and be sent into -38 DEG C of household freezer and carry out suddenly Freeze, the central temperature of coating fermentation materials is made to be down to -26 DEG C, the anxious coating fermentation materials frozen are sent into vacuum drying system In drying box, be thermally dried under the vacuum environment of 40pa, will be in vacuum drying system drying box when heat drying just The control of beginning temperature is 28 DEG C, and constant temperature 5.8 hours;Then it utilizes 1 hour, the temperature in drying box is risen into 33 DEG C, and constant temperature 9 Hour;Followed by 1.5 hours, the temperature in drying box is risen to 40 DEG C, and constant temperature 3.7 hours;It recycles 1.5 hours, it will Temperature in drying box is down to 36 DEG C, and constant temperature 8 hours;It recycles 1.8 hours, the temperature in drying box is risen to 41 DEG C, and Constant temperature 2.8 hours;It finally utilizes 1.2 hours, the temperature in drying box is down to 35 DEG C, and constant temperature is until by coating fermentation materials Moisture dry to 8%, biological fermentation feed is made;
H, detection, packaging:Biological fermentation feed is crossed metal detector to be detected, vacuum then is carried out to biological fermentation feed Packaging.
In above-mentioned all embodiments, coarse powder is carried out to raw material using beater disintegrating machine during the coarse crushing It is broken, described finely divided finely divided to the progress of mixed raw material using micronizer in the process;The wet-process puffing machine For single screw squeezing expansion machine;The animal fat is fish oil;The lactobacillus plantarum is that Changzhou beneficial bacteria adds biotechnology limited The lactobacillus plantarum bacterium powder of company's production, the bacillus subtilis are the withered grass of Jiangsu Lv Ke Bioisystech Co., Ltd production Bacillus bacterium powder, the saccharomycete are the saccharomycete bacterium powder of Cangzhou Zhongxin Biological Technology Co., Ltd.'s production, the excrement intestines Coccus is the enterococcus faecalis bacterium powder of Luoyang OKBK Biotechnology Co., Ltd.'s production.

Claims (5)

1. a kind of novel biological fermentation feed production technology, it is characterised in that its production technology is as follows:
A, coarse crushing:Raw material are chosen by following ingredient and weight:15 ~ 22 parts of corn, 12 ~ 18 parts of soybean, rape cake 10 ~ 14 parts of 11 ~ 15 parts, 12 ~ 16 parts of sesame-send cake, 13 ~ 17 parts of wheat bran and fish meal, by raw material respectively coarse powder be broken to granularity be 26 ~ 31 mesh;
B, finely divided:Raw material after step a coarse crushings are sufficiently mixed uniformly, mixed raw material fine powder is broken to grain Degree is 40 ~ 50 mesh, and mixed material is made;
C, wet method expanding treatment:Mixed material is sent into the quality-adjusting device of wet-process puffing machine and carries out modifier treatment, in quenched process Middle that steam is passed through into quality-adjusting device, 41% ~ 47%, moisture control exists for the curing degree control of the mixed material after modifier treatment 25% ~ 32%, temperature is controlled at 85 ~ 92 DEG C, then, the mixed material after modifier treatment is discharged into the puffing of wet-process puffing machine Intracavitary carries out extrusion, is made expanded material, and the unit weight control of expanded material is 360 ~ 400g/L, curing degree control for 91% ~ 94%;
D, fermenting microbe activates:3 ~ 5 parts of fermenting microbe, 16 ~ 20 parts of wheat bran, 2 ~ 3 parts of sucrose and water 18 ~ 22 are taken by weight ratio Part, and be sufficiently mixed uniformly, standing 4 ~ 5 hours at a temperature of 34 ~ 38 DEG C is made fermenting agent, and the fermenting microbe is by weight Than for(9~11):(8~10):(10~12):(2~5)Lactobacillus plantarum, bacillus subtilis, saccharomycete and enterococcus faecalis structure At;
E, solid fermentation:Expanded material layering tiling is placed in closed environment, the uniformly sprinkling fermentation in every layer of expanded material Suitable water is added into expanded material for microbial inoculum, by the control of the moisture of expanded material 40% ~ 45%, to expanded material into Row anaerobic fermentation, fermentation temperature are controlled at 31 ~ 36 DEG C, and fermentation terminates for 3 ~ 5 days, and fermentation materials are made;
F, spray attachment protective agent:10 ~ 12 parts of animal fat, 9 ~ 11 parts of molasses, defatted milk are chosen by following ingredient and weight 60 ~ 64 parts of 8 ~ 12 parts of powder and water, and be sufficiently mixed and protective agent uniformly is made, by the uniform spray attachment of protective agent fermentation materials table Coating fermentation materials are made in face;
G, vacuum freeze drying:Coating fermentation materials are evenly laid out on pallet, and be sent into -40 ~ -38 DEG C of household freezer into Row is anxious to be frozen, and the central temperature of coating fermentation materials is made to be down to -30 ~ -26 DEG C, and the anxious coating fermentation materials frozen are sent into vacuum and are done It in the drying box of drying system, is thermally dried under the vacuum environment of 10 ~ 40pa, when heat drying does vacuum drying system Initial temperature control in dry case is 25 ~ 28 DEG C, and constant temperature 5.5 ~ 5.8 hours;Then it utilizes 0.6 ~ 1 hour, it will be in drying box Temperature rise to 30 ~ 33 DEG C, and constant temperature 8.6 ~ 9 hours;Followed by 1.2 ~ 1.5 hours, the temperature in drying box is risen to 38 ~ 40 DEG C, and constant temperature 3.2 ~ 3.7 hours;It recycles 1.3 ~ 1.5 hours, the temperature in drying box is down to 34 ~ 36 DEG C, and constant temperature 7.5 ~ 8 hours;It recycles 1.4 ~ 1.8 hours, the temperature in drying box is risen to 38 ~ 41 DEG C, and constant temperature 2.6 ~ 2.8 hours;Most It utilizes 1 ~ 1.2 hour afterwards, the temperature in drying box is down to 32 ~ 35 DEG C, and constant temperature is until the moisture of coating fermentation materials is contained Amount is dry to 4% ~ 8%, and biological fermentation feed is made;
H, detection, packaging:Biological fermentation feed is crossed metal detector to be detected, vacuum then is carried out to biological fermentation feed Packaging.
2. a kind of novel biological fermentation feed production technology according to claim 1, it is characterised in that:In the coarse powder Coarse crushing is carried out to raw material using beater disintegrating machine during broken, described finely divided in the process using micronizer pair Mixed raw material carry out finely divided.
3. a kind of novel biological fermentation feed production technology according to claim 1 or 2, it is characterised in that:It is described wet Method bulking machine is single screw squeezing expansion machine.
4. a kind of novel biological fermentation feed production technology according to claim 1 or 2, it is characterised in that:It is described dynamic Object grease is fish oil.
5. a kind of novel biological fermentation feed production technology according to claim 1 or 2, it is characterised in that:The plant Object lactobacillus is the lactobacillus plantarum bacterium powder that Changzhou beneficial bacteria adds bio tech ltd to produce, and the bacillus subtilis is river The bacillus subtilis powder of Bioisystech Co., Ltd of Su Lv sections production, the saccharomycete are there is letter biotechnology in Cangzhou City The saccharomycete bacterium powder of limit company production, the enterococcus faecalis are the excrement of Luoyang OKBK Biotechnology Co., Ltd.'s production Enterococcus bacterium powder.
CN201810271419.9A 2018-03-29 2018-03-29 A kind of novel biological fermentation feed production technology Pending CN108576373A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810271419.9A CN108576373A (en) 2018-03-29 2018-03-29 A kind of novel biological fermentation feed production technology

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810271419.9A CN108576373A (en) 2018-03-29 2018-03-29 A kind of novel biological fermentation feed production technology

Publications (1)

Publication Number Publication Date
CN108576373A true CN108576373A (en) 2018-09-28

Family

ID=63623830

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810271419.9A Pending CN108576373A (en) 2018-03-29 2018-03-29 A kind of novel biological fermentation feed production technology

Country Status (1)

Country Link
CN (1) CN108576373A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109997993A (en) * 2019-05-16 2019-07-12 周玉华 A kind of manufacture craft of extruding fermentation aquatic product feed stuff
CN111406830A (en) * 2020-04-07 2020-07-14 湖北希普生物科技有限公司 Preparation method of compound microbial fermentation puffed feed
CN112438347A (en) * 2019-09-03 2021-03-05 宿迁市大江饲料有限公司 Aquatic product fermented feed and preparation method thereof
CN113907196A (en) * 2021-10-11 2022-01-11 安徽五粮泰生物工程股份有限公司 Preparation method of feeding milky instant fat powder
CN114831211A (en) * 2022-05-17 2022-08-02 广西富鹏农牧有限公司 Leaven for soybean meal feed

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102283316A (en) * 2011-09-26 2011-12-21 江苏牧羊集团有限公司 soybean meal fermentation process
CN104996722A (en) * 2015-08-13 2015-10-28 江南大学 Method of two-step united multi-strain fermented feed
CN105941828A (en) * 2016-05-16 2016-09-21 内蒙古工业大学 Method for producing compound feed from mixed strains through united fermentation
CN107173557A (en) * 2017-05-31 2017-09-19 固原博泰农业科技有限公司 A kind of biology corn feedstuff and its production technology

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102283316A (en) * 2011-09-26 2011-12-21 江苏牧羊集团有限公司 soybean meal fermentation process
CN104996722A (en) * 2015-08-13 2015-10-28 江南大学 Method of two-step united multi-strain fermented feed
CN105941828A (en) * 2016-05-16 2016-09-21 内蒙古工业大学 Method for producing compound feed from mixed strains through united fermentation
CN107173557A (en) * 2017-05-31 2017-09-19 固原博泰农业科技有限公司 A kind of biology corn feedstuff and its production technology

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109997993A (en) * 2019-05-16 2019-07-12 周玉华 A kind of manufacture craft of extruding fermentation aquatic product feed stuff
CN112438347A (en) * 2019-09-03 2021-03-05 宿迁市大江饲料有限公司 Aquatic product fermented feed and preparation method thereof
CN111406830A (en) * 2020-04-07 2020-07-14 湖北希普生物科技有限公司 Preparation method of compound microbial fermentation puffed feed
CN113907196A (en) * 2021-10-11 2022-01-11 安徽五粮泰生物工程股份有限公司 Preparation method of feeding milky instant fat powder
CN114831211A (en) * 2022-05-17 2022-08-02 广西富鹏农牧有限公司 Leaven for soybean meal feed

Similar Documents

Publication Publication Date Title
CN108576373A (en) A kind of novel biological fermentation feed production technology
CN111363698B (en) Microbial inoculum for reducing mildew and mycotoxin harm of fermented feed and application
CN108208335B (en) Process for improving feeding nutritive value of cottonseed meal by microbial fermentation method
CN101263862B (en) Food and rink castoff feed processing method and culture medium and confecting method thereby
CN104041717A (en) Special feed, prepared from distiller's grains, for laying hen during egg producing period and preparation method of feed
CN110226671A (en) A kind of piglet full price fermented feed and its production method
US5622859A (en) Biologically pure strain of Enterococcus falcium FERM BP-4504
CN104472887A (en) Probiotic feed additive
CN107801837B (en) Biological fermentation process for forage-based utilization of chicken manure
CN105567740A (en) High-density solid fermentation method for agricultural bacillus
CN104855686A (en) A protein feed produced by fermenting sweet potato residues and a method to prolong shelf life thereof
CN104004675A (en) Method for production of lactic acid bacteria by utilizing ethanol industrial yellow water
CN110179015A (en) A kind of high-survival rate fermented shrimp material and preparation method thereof
CN108835393A (en) Mixed fermentation type Folium et Ramulus Mori microbiological fermented feed and preparation method thereof
CN110384178B (en) Lactic acid bacteria culture prepared based on vinasse and application of lactic acid bacteria culture in animal feed
CN108200998A (en) A kind of new bio greenfeed production technology
CN108934929A (en) A kind of high-survival rate hickory nut field planting preparation method of matrix
CN116898040A (en) Whole-plant sweet potato biological fermentation feed for pigs and preparation method thereof
CN110452850A (en) A kind of bacillus amyloliquefaciens culture, preparation method and applications
CN110870511A (en) Dry-wet mixed concentrated feed and preparation method thereof
CN108522796A (en) A kind of new bio feed prilling
CN109007373A (en) A kind of preparation method of novel fermentation gold flaxseed meal
CN107981046A (en) A kind of method of comprehensive utilization of pineapple peel
CN112586729A (en) Preparation method of plant probiotic enzyme powder
CN111436525A (en) Method for processing feed by integrating fermentation and enzymolysis

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20180928

WD01 Invention patent application deemed withdrawn after publication