CN105724778A - Processing technology of distiller's grain feed - Google Patents

Processing technology of distiller's grain feed Download PDF

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Publication number
CN105724778A
CN105724778A CN201610100261.XA CN201610100261A CN105724778A CN 105724778 A CN105724778 A CN 105724778A CN 201610100261 A CN201610100261 A CN 201610100261A CN 105724778 A CN105724778 A CN 105724778A
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CN
China
Prior art keywords
enzymolysis
distiller
compound
grains
bulked
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Pending
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CN201610100261.XA
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Chinese (zh)
Inventor
齐芳
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Individual
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Individual
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Priority to CN201610100261.XA priority Critical patent/CN105724778A/en
Publication of CN105724778A publication Critical patent/CN105724778A/en
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/87Re-use of by-products of food processing for fodder production

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Abstract

The invention relates to a processing technology of distiller's grain feed. The processing technology comprises the steps that ethanol dehydrogenase is added into distiller's grains, after enzymolysis is performed for 2-3 hours, acetaldehyde dehydrogenase is added for enzymolysis, enzymolysis materials are dried until the water content is lower than 10%, and a dried mixed material is obtained; the dried mixed material is put into a bulking machine to be bulked, a bulked mixed material is obtained, the bulked mixed material is smashed to be 40-50 mesh, and then the distiller's grain feed is obtained. According to the processing technology, after the distiller's grains are treated through ethanol dehydrogenase and acetaldehyde dehydrogenase, the protein content in the distiller's grains can be significantly increased, cellulose pectin substances in the distiller's grains can be effectively degraded into monosaccharide and oligosaccharide, multiple organic acids and vitamins are generated, and the nutritional value and aroma of the distiller's grains are improved; the rice hull fiber tissue treated through a bulking technology is in a fluffy state and is easy to digest and absorb, the dissolution rate of the nutrients in rice hulls can be increased, and the bulked distiller's grains are good in solubility and palatability and can be easily digested by livestock.

Description

A kind of processing technique of lees feeds
Technical field
The present invention relates to the production method of a kind of feedstuff, be specifically related to the processing technique of a kind of lees feeds.
Background technology
Distiller grains are the direct leftover bits and pieces during wine brewing, it does not contain only a certain proportion of grain can save the concentrate feeding cattle, it is possibly together with abundant crude protein, about exceed 23 times of Semen Maydis content, simultaneously possibly together with various trace elements, vitamin, yeast etc., the content of lysine, methionine and tryptophan is the highest, this is that agricultural crop straw is not provided that, distiller grains are excellent protein resources, but owing to hindering material-rice husk containing more nutrition, it is impossible to be directly used as feedstuff, make waste disposal more, not only cause the wasting of resources, and pollute environment.
Summary of the invention
For making full use of abandoned vinasse of the prior art, it is an object of the invention to provide the processing technique of a kind of lees feeds.
The technical solution used in the present invention is, the processing technique of a kind of lees feeds, and it comprises the steps of
nullThe weight ratio pressing 10:0.1 in distiller grains adds ethanol dehydrogenase,It is 100-120mpa at pressure、Temperature be 35-38 DEG C in the environment of enzymolysis 2-3 hour,Compound is stirred by enzymolysis simultaneously,Stir speed (S.S.) is 120 revs/min,Obtain the first enzymolysis compound,The weight ratio pressing 10:0.15 in the first enzymolysis blended stock adds aldehyde dehydrogenase,It is 130-150mpa at pressure、Temperature be 32-34 DEG C in the environment of enzymolysis 40-50 minute,First enzymolysis blended stock is stirred by enzymolysis simultaneously,Stir speed (S.S.) is 160 revs/min,Obtain the second enzymolysis compound,Second enzymolysis compound is dried at a temperature of the drying of 60-65 DEG C to water content less than 10%,Obtain drying compound,Drying compound is put into bulking machine,It is 85-90 DEG C in temperature,Pressure is 270-280kg/cm2Under conditions of expanded, obtain expanded compound, expanded compound be crushed to 40-50 mesh, obtain lees feeds of the present invention.
Distiller grains enough increase substantially the protein content in distiller grains after ethanol dehydrogenase and acetaldehyde-dehydrogenase ferment treatment, effectively the cellulose pectic substance in distiller grains can be degraded to monosaccharide and oligosaccharide, and generate multiple organic acid, vitamin, improve nutritive value and the fragrance of distiller grains, rice hull cellulose tissue after bulking process processes is fluffy state, it is easy to digested absorption, can improve the dissolution rate of nutrient in rice husk, the distiller grains dissolubility of after the swelling and palatability more carefully, are easily digested by domestic animal.
Detailed description of the invention
Embodiment 1:
The weight ratio pressing 10:0.1 in distiller grains adds ethanol dehydrogenase, it is 100mpa at pressure, temperature be 35 DEG C in the environment of enzymolysis 2 hours, compound is stirred by enzymolysis simultaneously, stir speed (S.S.) is 120 revs/min, obtain the first enzymolysis compound, the weight ratio pressing 10:0.15 in the first enzymolysis blended stock adds aldehyde dehydrogenase, it is 130-mpa at pressure, temperature be 32 DEG C in the environment of enzymolysis 40 minutes, first enzymolysis blended stock is stirred by enzymolysis simultaneously, stir speed (S.S.) is 160 revs/min, obtain the second enzymolysis compound, second enzymolysis compound is dried at a temperature of the drying of 60 DEG C to water content less than 10%, obtain drying compound, drying compound is put into bulking machine, it it is 85 DEG C in temperature, pressure is 270kg/cm2Under conditions of expanded, obtain expanded compound, expanded compound be crushed to 40 mesh, obtain lees feeds of the present invention.
Embodiment 2:
The weight ratio pressing 10:0.1 in distiller grains adds ethanol dehydrogenase, it is 120mpa at pressure, temperature be 38 DEG C in the environment of enzymolysis 3 hours, compound is stirred by enzymolysis simultaneously, stir speed (S.S.) is 120 revs/min, obtain the first enzymolysis compound, the weight ratio pressing 10:0.15 in the first enzymolysis blended stock adds aldehyde dehydrogenase, it is 150mpa at pressure, temperature be 34 DEG C in the environment of enzymolysis 50 minutes, first enzymolysis blended stock is stirred by enzymolysis simultaneously, stir speed (S.S.) is 160 revs/min, obtain the second enzymolysis compound, second enzymolysis compound is dried at a temperature of the drying of 65 DEG C to water content less than 10%, obtain drying compound, drying compound is put into bulking machine, it it is 90 DEG C in temperature, pressure is 280kg/cm2Under conditions of expanded, obtain expanded compound, expanded compound be crushed to 50 mesh, obtain lees feeds of the present invention.

Claims (1)

1. the processing technique of a lees feeds, it is characterised in that it comprises the steps of
nullThe weight ratio pressing 10:0.1 in distiller grains adds ethanol dehydrogenase,It is 100-120mpa at pressure、Temperature be 35-38 DEG C in the environment of enzymolysis 2-3 hour,Compound is stirred by enzymolysis simultaneously,Stir speed (S.S.) is 120 revs/min,Obtain the first enzymolysis compound,The weight ratio pressing 10:0.15 in the first enzymolysis blended stock adds aldehyde dehydrogenase,It is 130-150mpa at pressure、Temperature be 32-34 DEG C in the environment of enzymolysis 40-50 minute,First enzymolysis blended stock is stirred by enzymolysis simultaneously,Stir speed (S.S.) is 160 revs/min,Obtain the second enzymolysis compound,Second enzymolysis compound is dried at a temperature of the drying of 60-65 DEG C to water content less than 10%,Obtain drying compound,Drying compound is put into bulking machine,It is 85-90 DEG C in temperature,Pressure is 270-280kg/cm2Under conditions of expanded, obtain expanded compound, expanded compound be crushed to 40-50 mesh, obtain lees feeds of the present invention.
CN201610100261.XA 2016-02-24 2016-02-24 Processing technology of distiller's grain feed Pending CN105724778A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610100261.XA CN105724778A (en) 2016-02-24 2016-02-24 Processing technology of distiller's grain feed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610100261.XA CN105724778A (en) 2016-02-24 2016-02-24 Processing technology of distiller's grain feed

Publications (1)

Publication Number Publication Date
CN105724778A true CN105724778A (en) 2016-07-06

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610100261.XA Pending CN105724778A (en) 2016-02-24 2016-02-24 Processing technology of distiller's grain feed

Country Status (1)

Country Link
CN (1) CN105724778A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109744368A (en) * 2019-03-22 2019-05-14 东莞市澹一生物科技有限公司 Utilize the method and feedstuff of wheat vinasse production feedstuff
CN109744367A (en) * 2019-03-22 2019-05-14 东莞市澹一生物科技有限公司 The method and feedstuff of resource utilization wheat vinasse production feedstuff
CN110089636A (en) * 2019-03-15 2019-08-06 河南贾湖生物科技有限公司 A kind of stoving process of fresh grain stillage feed
CN111493226A (en) * 2020-04-27 2020-08-07 安徽省金裕皖酒业有限公司 Inductive vinasse bait
CN114886133A (en) * 2022-03-26 2022-08-12 刘文治 Complete equipment for producing feed raw materials by utilizing fermented grains containing a large amount of rice husks

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110089636A (en) * 2019-03-15 2019-08-06 河南贾湖生物科技有限公司 A kind of stoving process of fresh grain stillage feed
CN109744368A (en) * 2019-03-22 2019-05-14 东莞市澹一生物科技有限公司 Utilize the method and feedstuff of wheat vinasse production feedstuff
CN109744367A (en) * 2019-03-22 2019-05-14 东莞市澹一生物科技有限公司 The method and feedstuff of resource utilization wheat vinasse production feedstuff
CN111493226A (en) * 2020-04-27 2020-08-07 安徽省金裕皖酒业有限公司 Inductive vinasse bait
CN114886133A (en) * 2022-03-26 2022-08-12 刘文治 Complete equipment for producing feed raw materials by utilizing fermented grains containing a large amount of rice husks
CN114886133B (en) * 2022-03-26 2023-10-17 刘文治 Complete set of equipment for producing feed raw material by using fermentation tank containing large quantity of rice husk

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Application publication date: 20160706