CN105961844A - Feed with hydrolyzed protein and preparation method of feed - Google Patents

Feed with hydrolyzed protein and preparation method of feed Download PDF

Info

Publication number
CN105961844A
CN105961844A CN201610292782.XA CN201610292782A CN105961844A CN 105961844 A CN105961844 A CN 105961844A CN 201610292782 A CN201610292782 A CN 201610292782A CN 105961844 A CN105961844 A CN 105961844A
Authority
CN
China
Prior art keywords
feedstuff
mixture
emulsifying
protein
homogenizing
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.)
Granted
Application number
CN201610292782.XA
Other languages
Chinese (zh)
Other versions
CN105961844B (en
Inventor
沈喆如
Original Assignee
沈喆如
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 沈喆如 filed Critical 沈喆如
Priority to CN201610292782.XA priority Critical patent/CN105961844B/en
Publication of CN105961844A publication Critical patent/CN105961844A/en
Application granted granted Critical
Publication of CN105961844B publication Critical patent/CN105961844B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention belongs to the field of feed processing, and particularly relates to a feed with hydrolyzed protein and a preparation method of the feed. The preparation method provided by the invention comprises the following steps of adding prepared raw materials to water, performing heating, adjusting a pH value, adding an emulsifying agent, performing sufficient stirring, adding enzymes, and performing sufficient stirring; adding the obtained mixture to a homogenizing machine for homogenizing treatment; or adding the obtained mixture to an emulsifying machine for emulsifying treatment; or adding the obtained mixture to the homogenizing machine for homogenizing treatment, and then adding the homogenized mixture to the emulsifying machine for the emulsifying treatment; or adding the obtained mixture to the emulsifying machine for the emulsifying treatment, and then adding the emulsified mixture to the homogenizing machine for homogenizing treatment; and then drying obtained semi-finished products to obtain powder, so that the feed with hydrolyzed protein is obtained.

Description

A kind of feedstuff with hydrolyzed protein and preparation method thereof
Technical field
The invention belongs to field of feed processing, especially relate to a kind of feedstuff with hydrolyzed protein and preparation method thereof.
Background technology
Animal particularly brood, in order to reach optimal production performance, it is necessary to needs a number of little peptide, normal diet egg Must pass through in vain after digestive tract is degraded, the digested absorption of ability, not only utilization rate is low, is also consumed by substantial amounts of biological energy consumption.
In prior art, it is through Over emulsfication and homogenizing by oils and fats, albumen, whey powder Three feed raw material, then does through high-temperature spray Dry, become pressed powder.Or by oils and fats, albumen, whey powder, feed additive through Over emulsfication, spray-dried become Feedstuff processing method.
Process above is improving feed manufacturing efficiency, promotes that animal digestion absorbs, and lifting feedstuff emulsibility, dissolubility aspect have Positive effect.But they have a significant shortcoming: the albumen in preparation-obtained feedstuff cannot be straight by animal alimentary canal Connect absorption.
Summary of the invention
It is an object of the invention to, for present on problem, it is provided that a kind of feedstuff with hydrolyzed protein and preparation method thereof.
To this end, the present invention adopts the following technical scheme that
A kind of preparation method of the feedstuff with hydrolyzed protein, described preparation method includes:
(1) raw material worked good is added to the water, adds emulsifying agent after heated and pH regulator and be sufficiently stirred for, be subsequently adding enzyme It is sufficiently stirred for;The purpose of pH regulator is that the reaction participated in by enzyme provides reaction condition, and the purpose of heating is as emulsifying and enzyme The reaction participated in provides reaction condition simultaneously;
(2) mixture obtained in step (1) is joined homogenizer carries out homogenizing process;Or will step (1) obtain To mixture join mulser carry out emulsifying;Or the mixture obtained in step (1) is joined in homogenizer Carrying out homogenizing process, the mixture after then being processed by homogenizing joins and carries out emulsifying in mulser;Or by step (1) In the mixture that obtains join mulser carry out emulsifying, then the mixture after emulsifying is joined in homogenizer Carry out homogenizing process;
(3) semi-finished product obtained in step (2) are dried into powder, i.e. obtain a kind of feedstuff with hydrolyzed protein.
Preferably, it is 1~the animal proteinum of the vegetable protein of the whey powder of 60%, 0~60%, 0~60%, 0~60% by mass percent The animal oil of Vegetable oil lipoprotein, 0~60% carry out mixing in proportion and be made into raw material, and at least there is vegetable protein or animal proteinum In one.
Preferably, in step (1) heating and temperature control in the range of 30~100 DEG C.
Preferably, in step (1), pH controls in the range of 1.5~9.5.
Preferably, described enzyme includes protease and carbohydrase, lipase, food flavor enzyme, cellulase, lactobacillus, double qi bar One or more in bacterium, bacillus subtilis, redox enzymes, isomerase, enzyme inhibitor, zymoexciter.That is to say at least Including protease.Protease is the general name of the class of enzymes of aminosal peptide chain.The effect of carbohydrase is to be tied by monosaccharide in cracking polysaccharide The chemical bond being combined, makes polysaccharide be degraded into less molecule.Lipase is under the jurisdiction of carboxylic ester hydrolase class, it is possible to progressively Triglyceride hydrolysis is become glycerol and fatty acid.Redox enzymes is the enzyme of a class catalytic oxidation-reduction reaction, can be divided into oxidation Enzyme and reductase two class.Lactobacillus genus lactic acid Bacteriaceae, names because sugar fermentation produces a large amount of lactic acid.It exists extensively, addicted to Acidity, existence optimum pH is 5.5~6.0, certainly, still can survive in the environment that pH is 3.0~4.5, and it is without brood cell Bacillus is acid-resistant strength is the strongest.Bifidus bacillus is the Gram-positive of isolated a kind of anaerobism from the intestinal of breast milk nutrition youngster Bacillus, bacillus subtilis, is the one of Bacillus.Isomerase is also known as allomerase, is the enzyme of catalysis generation isomerization reaction General name.Enzyme inhibitor is that a class can be with desmoenzyme the molecule reducing its activity.Owing to the activity of suppression certain enzyme can be killed Pathogen or correct metabolic imbalance, many related drugs are exactly enzyme inhibitor.It is inactive that zymoexciter is that one can make Enzyme can become the material of active enzyme.
The present invention also provides for that a kind of basis preparation method above described in any one is preparation-obtained has raising of hydrolyzed protein Material.
Vegetable protein described in the preparation method of the present invention includes: Semen Pisi sativi protein, wheat protein, barley protein, avenin, Soybean protein concentrate, rice protein, soybean protein isolate, textured soybean protein, bean cake, Semen arachidis hypogaeae protein, Semen sojae atricolor powder, Semen Pisi sativi One or more in the vegetable proteins such as powder, Semen Viciae fabae powder, black sesame powder, peanut powder;Described animal proteinum includes: fish flour, blood One or more in the slurry animal proteinum such as albumen, hyperglobulinemia;Described Vegetable oil lipoprotein includes: soybean oil, soybean phospholipid, The plants such as Oleum Cocois, olive oil, Testa oryzae oil, Oleum sesami, sunflower oil, safflower oil, Petiolus Trachycarpi oil, vegetable oil, Oleum Arachidis hypogaeae semen, cotton oil One or more in oils and fats;Described animal oil includes one or more in Adeps Sus domestica, chicken oil, duck oil, Adeps Bovis seu Bubali, butter; Described emulsifying agent includes: acetic acid and fatty glyceride, lactic acid and fatty glyceride, cholic acid, lecithin, polyglycereol castor Oleum Sesami alcohol ester, polyethylene ricinoleyl alcohol acid esters, sodium caseinate, polysorbate (sorbitan fatty acid fat), tween etc. There are one or more in the food and feed additive of emulsification function;Described enzyme include protease and carbohydrase, lipase, Food flavor enzyme, cellulase, lactobacillus, bifidus bacillus, bacillus subtilis, redox enzymes, isomerase etc. have biology and urge One or more in the material of change effect, enzyme inhibitor and zymoexciter.Heretofore described homogenizer includes all having all The machinery of matter function, described mulser includes all machinery with emulsification function.
The preparation method of the feedstuff with hydrolyzed protein provided by the present invention has the advantage that
(1) cost of investment needed for the preparation method of the feedstuff with hydrolyzed protein provided by the present invention is less, and production technology is more For brief and practical, floor space is little, and i.e. sends out during homogenizer carries out homogenizing process and/or mulser carries out emulsifying Raw hydrolysis, so that be greatly shortened process time, therefore, it can energy efficient, country advocate reduce atmospheric pollution, Forbid, under the background of fire coal, especially there is realistic meaning;
Emulsifying after homogenizing, first homogenizing after (2) preparation method of the feedstuff with hydrolyzed protein provided by the present invention uses first emulsifying, Omnidistance emulsifying, four kinds of production technologies of omnidistance homogenizing, owing to homogenizer can diminish material material uniformly, so that enzyme Reaction, or available mulser high speed rotating can be fully contacted with unclassified stores, shear, dispersion, clash into, between strength imparting material With interpenetrating of enzyme, thus strengthen hydrolysis effect;
(3) preparation method of the feedstuff with hydrolyzed protein provided by the present invention is passed through in homogenizer and/or mulser at enzyme Effect issue raw hydrolysis, promoting the Proteolytic enzyme in material is little peptide, and little peptide directly can be digested and assimilated by animal, this A little the most meaningful in high-grade aquatic feeds, because the digestive tract of many high-grade Aquatic products is comparatively short, albumen is digested and assimilated Incomplete, easily cause the waste of albumen in feedstuff, and the feedstuff obtained by preparation method provided by the present invention is deposited after hydrolyzing Little peptide, can be by the accessible absorption of aquatic animal;Feedstuff obtained by preparation method provided by the present invention is more suitable for young stock, Owing to young stock gut development is not complete, protease and lipase hyposecretion, feed general proteins and be easily caused dyspepsia, gastrointestinal Road chorion epithelioma cellular atrophy, thus cause the series of problems such as diarrhoea, growth retardation, even death, this weans young stock Stage is the most prominent, is that row insider is presently required the difficult problem captured, and raising obtained by preparation method provided by the present invention The little peptide formed in material directly can be absorbed by young stock, thus solves the wean problem of young stock;
(4) the little peptide contained in the feedstuff obtained by the preparation method of the feedstuff with hydrolyzed protein provided by the present invention can be The aminoacid that in intestinal, protection is the most destroyed.Simple aminoacid can reformulate peptide and protein in vivo as required, And little peptide and amino acid whose mixture can carry out protected amino acid by little peptide, thus save the amino that a part needs to reconfigure Acid, thus also make the biological assessment of the feedstuff that preparation method provided by the present invention obtains higher, simultaneously can in feed manufacturing To reduce the consumption of protein raw materials, this is even more important in high-grade Aquatic product material and young stock feedstuff, because high-grade Aquatic product material and young stock are raised Protein raw materials used by material, as fish flour, milk powder, lactalbumin, blood plasma egg price all at more than 10000 yuan per ton.
(5) preparation method of the feedstuff with hydrolyzed protein provided by the present invention can also be by adding the enzyme group containing lipase Close, thus improve Animal fat and the hydrolysis of Vegetable oil lipoprotein, thus strengthen animal to Animal fat and the digestible energy of Vegetable oil lipoprotein Power, strengthens the resistance of animal, promotes growth.
The preparation-obtained feedstuff of preparation method of the feedstuff with hydrolyzed protein that the present invention provides has the advantage that
(1) substitute oils and fats, albumen, lactose and good palatability, improve animal feed intake;
(2) improve albumen and the utilization rate of oils and fats in feedstuff, reduce albumen feedstuff and the waste of energy feed;
(3) feedstuff Small Peptides content is high, is suitable for the raising of high-grade Aquatic product and solves the wean problem of young stock;
(4) anti-stress, particularly in hot season, it is possible to decrease " heat increment ", effectively alleviates heat stress;Increase in cold season Add Energy intaking, increase growth needs nutrition, improve production performance;
(5) improve milk yield of sow and butterfat percnetage, thus improve piglet survival ratio and weight of weaning litter;
(6) improve piglets palatability, digestibility, significantly improve the speed of growth, feedstuff-meat ratio can be reduced, improve feedstuff effective utilization;
(7) improve egg fowl egg laying performance, extend egg-laying peak, the poultry speed of growth and meat can be improved;
(8) extending the holding time of feedstuff, convenient transport, refinement degree is uniformly obviously improved, and improves and comprehensively uses economic benefit;
(9) fluid oil can be converted solid powdery, easily add, can use after mixing homogeneously with other feedstuffs, processing Convenient.
Detailed description of the invention
In conjunction with specific embodiments the present invention is described in further detail.
Protein is prone to absorb than free amino acid in human body by hydrolysis, the product being hydrolyzed to dipeptides or tripeptides, and ratio does not has The protein of hydrolysis more easily absorbs, therefore, when being hydrolyzed protein with different proteases, it is necessary to carry out water Xie Du measures.
The definition of degree of hydrolysis: the degree of hydrolysis DH of protein represents protein in hydrolytic process, the degree or hundred that peptide bond is cleaved Proportion by subtraction.
Its detection method is as follows: take Hydrolyzed protein liquid 5.00ml in small beaker, adds 60ml distilled water, then magnetic agitation And measure its pH value with Accurate pH meter, then it is titrated to pH=8.2 by 0.05mol/l NaOH solution, is subsequently adding and neutralizes Good formalin 10ml, is then titrated to pH=9.2, record by its pH value from 8.2 titration 9.2 time post consumption 0.05mol/l The volume of NaOH solution, does reagent blank titration experiments (distilled water) simultaneously, then calculates its degree of hydrolysis.Degree of hydrolysis DH Computing formula as follows:
D H = C · ( V 1 - V 2 ) · V / 5 M · P · 8 × 100 %
C is NaOH concentration, and unit is mol/l;
V1And V2Being respectively sample and the volume of the blank NaOH consumed, be the volume dropping to 9.2 from PH8.2, unit is ml;
V is the volume of protein enzymatic hydrolyzate, and unit is ml;
M is sample quality, and unit is g;
P is the mass percent of albumen in raw material, and unit is %;
MM number mmol/g of 8 peptide bonds contained by every gram of protein (with reference to the value of soybean protein, if other albumen are different, Can do and slightly adjust).
Embodiment 1
150kg whey powder, 500kg soybean protein, 250kg Adeps Sus domestica, 150kg soybean oil are added 2000kg water, temperature control System is between 50-60 DEG C, and pH value is about 7.0, adds 5kg emulsifying agent, stirring, adds neutral protease 1.5kg, Fructus Chaenomelis Protease 1.5kg, lipase 1.0kg, stirring, by homogenizer homogeneous micronization, pressure about 29-35MPa, subsequently into Mulser processes, and mulser rotor speed is about 1200r/min, quiet abrasive disc, dynamic abrasive disc, propeller blade three it Between the narrowest gap in formed strong, reciprocal aquashear, rub, the comprehensive effect such as centrifugal extruding, liquid stream collision After, last about 90 minutes, spray-dried for material semi-finished product tower is spray-dried, become powder, dried product, Sieve, metering, packaging.Its degree of hydrolysis is 13.7%.
Embodiment 2
By 50kg whey powder, 160kg Oleum Cocois, 290kg Petiolus Trachycarpi oil, 500kg bean cake inserts 2000kg, pH value is 6.5-7.5 Aqueous solution in, temperature controls at about 60 DEG C, add 10kg emulsifying agent, stirring, add bacillus subtilis 1.5kg, Fructus Chaenomelis egg White enzyme 1.5kg, bromelain 1.0kg, stirring, by homogenizer homogeneous micronization, pressure is at about 40-45MPa, then Entering mulser to process, mulser rotor speed is about 18000r/min, in quiet abrasive disc, dynamic abrasive disc conjunction between the two Manage and narrow gap is formed strong, reciprocal aquashear, rub, after the comprehensive effect such as centrifugal extruding, liquid stream collision, lead to Cross circulation pipe to be moved in circles in a reservoir by material above work process, last about 300 minutes, by material semi-finished product through spraying Drying tower is spray-dried, and becomes powder, dried product, sieves, metering, packaging.Its degree of hydrolysis is 8.7%.
Embodiment 3
By 150kg whey powder, 195kg Oleum Cocois, 200kg Petiolus Trachycarpi oil, 440kg wheat protein inserts 2000kg, pH value exists In aqueous solution between 1.5-3.0, temperature controls at about 40-50 DEG C, adds 15kg emulsifying agent, stirring, adds pepsin 5kg, stirring, process subsequently into mulser, mulser rotor speed is about 2900r/min, stator, rotor, The narrowest gap between propeller blade three is formed strong, reciprocal aquashear, rub, centrifugal extruding, liquid stream After the comprehensive effects such as collision, lasting about 120 minutes, subsequently into high pressure homogenizer homogenizing, pressure, will at about 20MPa Material refines, and the spray-dried tower of semi-finished product is spray-dried.Become powder, dried product, sieve, metering, Packaging.Its degree of hydrolysis is 18.6%.
Embodiment 4
By 50kg whey powder, 350kg Petiolus Trachycarpi oil, 100kg Oleum Cocois, 500kg rice protein inserts 2000kg, pH value is In the aqueous solution of 5.5-6.5, temperature controls at about 45-60 DEG C., add 20kg emulsifying agent, stirring, add bromelain 4kg, cellulase 1.5kg, stirring, process subsequently into mulser, mulser rotor speed is 8000r/min, The narrowest gap between stator, rotor, propeller blade three is formed strong, reciprocal aquashear, friction, from After the comprehensive effects such as heart extruding, liquid stream collision, lasting about 120 minutes, subsequently into high pressure homogenizer homogenizing, pressure exists About 280MPa, refines material, and the spray-dried tower of semi-finished product is spray-dried.Become powder, dried product Product, sieve, metering, packaging.Its degree of hydrolysis is 13.7%.
Embodiment 5
By 150kg whey powder, 250kg soybean protein, 250kg rice protein, 100kg Oleum Cocois, 250kg Petiolus Trachycarpi oil, put Entering in the 2000kg aqueous solution that pH value is 6.5-7.5, temperature controls at about 45 DEG C, adds 15kg emulsifying agent, stirring, adds Enter food flavor enzyme 1kg, bacillus subtilis 1.5kg, bromelain 2.5kg, process subsequently into mulser, mulser rotor Rotating speed is 4800r/min, is formed strong, reciprocal in the narrowest gap between stator, rotor, propeller blade three Aquashear, rub, the comprehensive effect such as centrifugal extruding, liquid stream collision, after lasting about 120 minutes, semi-finished product are through spraying Drying tower is spray-dried.Become powder, dried product, sieve, metering, packaging.Its degree of hydrolysis is 10.7%.
Embodiment 6
By 100kg whey powder, 150kg Oleum Cocois, 250kg Petiolus Trachycarpi oil, 250kg wheat protein, 200kg soybean protein, put Entering in the 2000kg aqueous solution that pH value is 6.5-7.5, temperature controls at about 35-40 DEG C, adds 20kg emulsifying agent, stirs, Adding bacillus subtilis 1.5kg, bromelain 2.5kg, process subsequently into mulser, mulser rotor speed is About 2000-2900r/min, is formed strong, past in the narrowest gap between stator, rotor, propeller blade three Multiple aquashear, rubbing, after the comprehensive effect such as centrifugal extruding, liquid stream collision, last about 200 minutes, semi-finished product are through spraying Mist drying tower is spray-dried.Become powder, dried product, sieve, metering, packaging.Its degree of hydrolysis is 15.5%.
Embodiment 7
By 500kg whey powder, 250kg soybean protein, 250kg rice protein, inserting in 1000kg aqueous solution, pH value is 8.0-9.5, temperature controls at about 50 DEG C, add 25kg emulsifying agent, add trypsin 2.0kg, alkaline protease 2.5kg, Momordica grosvenori proteolytic 1.5kg, subsequently into high pressure homogenizer homogenizing, pressure freely can adjust in 400MPa, by circulation Material is moved in circles above work process by pipe in a reservoir, reaches the purpose of refinement, is then stirred for 300 minutes, semi-finished product Drying machine is dried, and dried product is pulverized, sieved, metering, packaging.Its degree of hydrolysis is 9.7%.
Embodiment 8
150kg whey powder, 100kg Oleum Cocois, 150kg Petiolus Trachycarpi oil, 200kg soybean protein, 175kg rice protein are inserted In 700kg water, pH value is 6.3-7.5, and temperature controls at about 50-60 DEG C, adds 25kg emulsifying agent, stirring, adds 1.5kg Bacillus subtilis, 1.5kg papain, subsequently into high pressure homogenizer homogenizing, pressure freely can adjust in 400MPa, Material moved in circles in a reservoir above work process by circulation pipe, reaches the purpose of refinement, be then stirred for 360 minutes, Semi-finished product drying machine is dried, and dried product is pulverized, sieved, metering, packaging.Its degree of hydrolysis is 13.7%.
Embodiment 9
50kg whey powder, 500kg rice protein, 250kg Petiolus Trachycarpi oil, 150kg soybean oil are added 2000kg water, temperature control System is between 50-60 DEG C, and pH value is about 7.0, adds 5kg emulsifying agent, stirring, adds neutral protease 1.5kg, Fructus Chaenomelis Protease 1.5kg, stirring, by homogenizer homogeneous micronization, pressure, at about 15-25MPa, adds subsequently into mulser Processing, mulser rotor speed is about 2900r/min, in quiet abrasive disc, dynamic conjunction between abrasive disc, propeller blade three Manage and narrow gap is formed strong, reciprocal aquashear, rub, after the comprehensive effect such as centrifugal extruding, liquid stream collision, lead to Cross circulation pipe to be moved in circles in a reservoir by material above work process, last about 90 minutes, by material semi-finished product through spray dried Dry tower is spray-dried, and becomes powder, dried product, sieves, metering, packaging.Its degree of hydrolysis is 11.3%.
Embodiment 10
670kg Semen sojae atricolor powder, 330kg Petiolus Trachycarpi oil being added in 2000kg water, pH is 5.5-7, and temperature controls at about 35-40 DEG C, Add 10kg emulsifying agent, stirring, add lactobacillus 3kg, bacillus bifidus 1.5kg, process subsequently into mulser, Rotating speed is about 11000r/min, is formed in quiet abrasive disc, dynamic the narrowest gap between abrasive disc, propeller blade three Strongly, reciprocal aquashear, rub, after the comprehensive effect such as centrifugal extruding, liquid stream collision, after lasting 150 minutes, half one-tenth The spray-dried tower of product is spray-dried.Become powder, dried product, sieve, metering, packaging.Its degree of hydrolysis exists 9.8%.
Embodiment 11
By 50kg whey powder, 160kg Oleum Cocois, 290kg Petiolus Trachycarpi oil, 500kg wheat protein inserts 2000kg, pH value is In the aqueous solution of 6.5-7.5, temperature controls at about 60 DEG C, adds 10kg emulsifying agent, stirs, addition bacillus subtilis 1.5kg, Papain 1.5kg, bromelain 1.0kg, stirring, by homogenizer homogeneous micronization, pressure is at about 80MPa, so Rear entrance mulser processes, and mulser rotor speed is 2900r/min, left and right, at quiet abrasive disc, dynamic abrasive disc, propeller The narrowest gap between leaf three is formed strong, reciprocal aquashear, rub, centrifugal extruding, liquid stream collision etc. After comprehensive effect, material moved in circles in a reservoir above work process by circulation pipe, last about 300 minutes, by thing The material spray-dried tower of semi-finished product is spray-dried, and becomes powder, dried product, sieves, metering, packaging.Its water Xie Du is 15.2%.
Above-mentioned detailed description of the invention is used for illustrating the present invention, only the preferred embodiments of the present invention rather than to this Bright limiting, in the protection domain of spirit and claims of the present invention, any amendment, the equivalent of making the present invention are replaced Change, improvement etc., both fall within protection scope of the present invention.

Claims (6)

1. the preparation method of a feedstuff with hydrolyzed protein, it is characterised in that described preparation method includes:
(1) raw material worked good is added to the water, adds emulsifying agent after heated and pH regulator and be sufficiently stirred for, be subsequently adding enzyme and be sufficiently stirred for;
(2) mixture obtained in step (1) is joined homogenizer carries out homogenizing process;Or the mixture obtained in step (1) is joined mulser carries out emulsifying;Or being joined by the mixture obtained in step (1) and carry out homogenizing process in homogenizer, the mixture after then being processed by homogenizing joins and carries out emulsifying in mulser;Or the mixture obtained in step (1) is joined mulser carries out emulsifying, then the mixture after emulsifying is joined and homogenizer carries out homogenizing process;
(3) semi-finished product obtained in step (2) are dried into powder, i.e. obtain a kind of feedstuff with hydrolyzed protein.
2. according to the preparation method of a kind of feedstuff with hydrolyzed protein described in claim 1, it is characterized in that, whey powder that mass percent is 1 ~ 60%, the vegetable protein of 0 ~ 80%, the animal proteinum of 0 ~ 80%, the Vegetable oil lipoprotein of 0 ~ 80%, the animal oil of 0 ~ 80% are carried out mixing in proportion and is made into raw material, and at least there is the one in vegetable protein or animal proteinum.
3. according to the preparation method of a kind of feedstuff with hydrolyzed protein described in claim 1, it is characterised in that in step (1), heating and temperature control is in the range of 30 ~ 100 DEG C.
4. according to the preparation method of a kind of feedstuff with hydrolyzed protein described in claim 1, it is characterised in that in step (1), pH controls in the range of 1.5 ~ 9.5.
5. according to the preparation method of a kind of feedstuff with hydrolyzed protein described in claim 1, it is characterized in that, described enzyme includes one or more in protease and carbohydrase, lipase, food flavor enzyme, cellulase, lactobacillus, bifidus bacillus, bacillus subtilis, redox enzymes, isomerase, enzyme inhibitor, zymoexciter.
6. the basis above preparation-obtained feedstuff with hydrolyzed protein of preparation method described in any one claim.
CN201610292782.XA 2016-05-04 2016-05-04 Feed with hydrolyzed protein and preparation method thereof Active CN105961844B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610292782.XA CN105961844B (en) 2016-05-04 2016-05-04 Feed with hydrolyzed protein and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610292782.XA CN105961844B (en) 2016-05-04 2016-05-04 Feed with hydrolyzed protein and preparation method thereof

Publications (2)

Publication Number Publication Date
CN105961844A true CN105961844A (en) 2016-09-28
CN105961844B CN105961844B (en) 2020-11-10

Family

ID=56991195

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610292782.XA Active CN105961844B (en) 2016-05-04 2016-05-04 Feed with hydrolyzed protein and preparation method thereof

Country Status (1)

Country Link
CN (1) CN105961844B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107318889A (en) * 2017-06-27 2017-11-07 徐州农丰生物化工有限公司 A kind of disinfectant for vegetables

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1493204A (en) * 2003-08-20 2004-05-05 孟庆峰 Manufacturing method of polypeptide calf milk powder substitute
CN101147530A (en) * 2007-10-30 2008-03-26 陈忆凤 Preparation technology of feed additive biologically active small peptide
CN101390564A (en) * 2007-09-18 2009-03-25 中国食品发酵工业研究院 Production method of corn separation protein
CN101627793A (en) * 2009-07-31 2010-01-20 郑州新威营养技术有限公司 Industrial production method of hydrolyzed wheat protein for feeding
CN103160559A (en) * 2013-01-23 2013-06-19 重庆大学 Preparation method of modified zein peptide
CN103250871A (en) * 2013-05-22 2013-08-21 江苏联海生物科技有限公司 Hydrolysis process of rice protein
CN103380945A (en) * 2013-07-19 2013-11-06 杭州香保饲料有限公司 Preparation method of powdered oil feed with whey powder
CN103416592A (en) * 2013-08-27 2013-12-04 江苏康科食品工程技术有限公司 Industrial production method of rice protein hydrolysate for feed
CN103766609A (en) * 2014-02-13 2014-05-07 哈尔滨伟平科技开发有限公司 Preparation method of polypeptide feed additive
CN104605137A (en) * 2015-02-15 2015-05-13 江苏康科食品工程技术有限公司 Preparation method of wheat protolysate
CN104686790A (en) * 2013-12-10 2015-06-10 安徽五粮泰生物工程股份有限公司 Preparation method of peptidoglycolipid for feed
CN104769128A (en) * 2011-11-07 2015-07-08 马斯公司 Food protein ingredient and methods for producing

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1493204A (en) * 2003-08-20 2004-05-05 孟庆峰 Manufacturing method of polypeptide calf milk powder substitute
CN101390564A (en) * 2007-09-18 2009-03-25 中国食品发酵工业研究院 Production method of corn separation protein
CN101147530A (en) * 2007-10-30 2008-03-26 陈忆凤 Preparation technology of feed additive biologically active small peptide
CN101627793A (en) * 2009-07-31 2010-01-20 郑州新威营养技术有限公司 Industrial production method of hydrolyzed wheat protein for feeding
CN104769128A (en) * 2011-11-07 2015-07-08 马斯公司 Food protein ingredient and methods for producing
CN103160559A (en) * 2013-01-23 2013-06-19 重庆大学 Preparation method of modified zein peptide
CN103250871A (en) * 2013-05-22 2013-08-21 江苏联海生物科技有限公司 Hydrolysis process of rice protein
CN103380945A (en) * 2013-07-19 2013-11-06 杭州香保饲料有限公司 Preparation method of powdered oil feed with whey powder
CN103416592A (en) * 2013-08-27 2013-12-04 江苏康科食品工程技术有限公司 Industrial production method of rice protein hydrolysate for feed
CN104686790A (en) * 2013-12-10 2015-06-10 安徽五粮泰生物工程股份有限公司 Preparation method of peptidoglycolipid for feed
CN103766609A (en) * 2014-02-13 2014-05-07 哈尔滨伟平科技开发有限公司 Preparation method of polypeptide feed additive
CN104605137A (en) * 2015-02-15 2015-05-13 江苏康科食品工程技术有限公司 Preparation method of wheat protolysate

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107318889A (en) * 2017-06-27 2017-11-07 徐州农丰生物化工有限公司 A kind of disinfectant for vegetables

Also Published As

Publication number Publication date
CN105961844B (en) 2020-11-10

Similar Documents

Publication Publication Date Title
CN102845645B (en) Preparation method of soluble easily-digested feed for young livestock and poultry
CN101627793B (en) Industrial production method of hydrolyzed wheat protein for feeding
CN102488085B (en) Method of making fodder for young livestock
CN101190005A (en) Method for manufacturing concentrated feed for porket and its product
CN105053552A (en) Fermented soybean meal with high biological activity and preparation method and application thereof
AU2005269462B2 (en) Stabilized pancreas product
CN101822347B (en) Piglet protein feed and production method thereof
Tapingkae et al. Influence of crude xylanase from Aspergillus niger FAS128 on the in vitro digestibility and production performance of piglets
CN102524535B (en) Oligopeptide additive for feed and preparation method thereof
CN102919529A (en) Preparation method of glycolysis and emulsification feed for young livestock and poultry
CN103704465A (en) Antibiotic-free microbial fermented feed and preparation method thereof
FR3016768A1 (en) Use of an enzyma composition in the feeding of ruminants
CN103380945B (en) Preparation method of powdered oil feed with whey powder
CN105961844A (en) Feed with hydrolyzed protein and preparation method of feed
RU2552084C1 (en) Method of processing soy oil meal into feed product with improved properties
CN106359980A (en) Feed capable of reducing disease rate of necrotic enteritis and transmissible gastroenteritis of weaned pigs
CA2406112C (en) Dephytinization of plant based products in mixtures with high moisture animal, plant or microbial by-products
CN110089634A (en) It is a kind of with enzymatic hydrolysis small peptide-additive complex compound feed and preparation method thereof
RU2601808C1 (en) Method for producing biological complex of fodders
TW202023393A (en) Method of preparing hydrolysate of soy protein concentrate, hydrolysate of soy protein concentrate and feed composition
CN108935931A (en) A kind of pannage and preparation method thereof based on cat beans and rye grass
CN110326804A (en) A kind of predigestion high-performance bio soft pellet diet Preparation equipment
KR900000926B1 (en) Process making of fodder for a ruminant
CN110037173A (en) A kind of pomace and dreg fodder and preparation method thereof
CN109601736A (en) A kind of bacterium enzyme collaboration solid state fermentation pannage and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant