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

Feed with hydrolyzed protein and preparation method of feed Download PDF

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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
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protein
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hydrolyzed protein
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CN105961844B (en
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沈喆如
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Hangzhou Hetai Biotechnology Co ltd
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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

一种具有水解蛋白的饲料及其制备方法A feed with hydrolyzed protein and its preparation method

技术领域technical field

本发明属于饲料加工领域,尤其是涉及一种具有水解蛋白的饲料及其制备方法。The invention belongs to the field of feed processing, and in particular relates to a feed with hydrolyzed protein and a preparation method thereof.

背景技术Background technique

动物特别是幼小动物,为了达到最佳生产性能,必须需要一定数量的小肽,普通饲料蛋白必需经过在消化道降解后,才能被消化吸收,不但利用率低,还消耗了大量的生物能耗。Animals, especially young animals, in order to achieve the best production performance, must need a certain amount of small peptides. Ordinary feed protein must be degraded in the digestive tract before it can be digested and absorbed. Not only the utilization rate is low, but also a large amount of biological energy consumption is consumed .

现有技术中,是将油脂、蛋白、乳清粉三种饲料原料经过乳化和均质,再经高温喷雾干燥,成为固体粉末。或者是将油脂、蛋白、乳清粉、饲料添加剂经过乳化,经喷雾干燥成为饲料原料的的加工方法。In the prior art, the three feed materials of oil, protein and whey powder are emulsified and homogenized, and then spray-dried at high temperature to become solid powder. Or it is a processing method in which oil, protein, whey powder, and feed additives are emulsified and spray-dried to become feed raw materials.

以上工艺在提高饲料加工效率,促进动物消化吸收,提升饲料乳化性、溶解性方面具有积极的作用。但它们具有一个显著的缺点:所制备得到的饲料中的蛋白无法被动物消化道直接吸收。The above process plays a positive role in improving feed processing efficiency, promoting animal digestion and absorption, and improving feed emulsification and solubility. But they have a significant disadvantage: the protein in the prepared feed cannot be directly absorbed by the animal's digestive tract.

发明内容Contents of the invention

本发明的目的在于,针对以上存在的问题,提供一种具有水解蛋白的饲料及其制备方法。The object of the present invention is to provide a feed with hydrolyzed protein and a preparation method thereof for the above problems.

为此,本发明采用如下技术方案:For this reason, the present invention adopts following technical scheme:

一种具有水解蛋白的饲料的制备方法,所述制备方法包括:A preparation method of feed with hydrolyzed protein, the preparation method comprising:

(1)将配合好的原料加入水中,经加热和pH调节后加入乳化剂充分搅拌,然后加入酶充分搅拌;pH调节的目的在于为酶所参与的反应提供反应条件,加热的目的在于为乳化和酶所参与的反应同时提供反应条件;(1) Add the prepared raw materials into the water, add the emulsifier after heating and pH adjustment, and then add the enzyme to fully stir; the purpose of pH adjustment is to provide reaction conditions for the reaction in which the enzyme participates, and the purpose of heating is to provide emulsification. Provide reaction conditions at the same time as the reaction in which the enzyme participates;

(2)将步骤(1)中得到的混合物加入到均质机中进行均质处理;或者将步骤(1)中得到的混合物加入到乳化机中进行乳化处理;或者将步骤(1)中得到的混合物加入到均质机中进行均质处理,然后将均质处理后的混合物加入到乳化机中进行乳化处理;或者将步骤(1)中得到的混合物加入到乳化机中进行乳化处理,然后将乳化处理后的混合物加入到均质机中进行均质处理;(2) The mixture obtained in step (1) is added to a homogenizer for homogenization; or the mixture obtained in step (1) is added to an emulsifier for emulsification; or the mixture obtained in step (1) The mixture is added into a homogenizer for homogenization, and then the homogenized mixture is added to an emulsifier for emulsification; or the mixture obtained in step (1) is added to an emulsifier for emulsification, and then Add the emulsified mixture to a homogenizer for homogenization;

(3)将步骤(2)中得到的半成品进行干燥成粉末,即得到一种具有水解蛋白的饲料。(3) Drying the semi-finished product obtained in step (2) into powder to obtain a feed with hydrolyzed protein.

优选地,将质量百分比为1~60%的乳清粉、0~60%的植物蛋白、0~60%的动物蛋白、0~60%的植物油脂、0~60%的动物油脂按比例进行混合配成原料,且至少存在植物蛋白或动物蛋白中的一种。Preferably, whey powder, 0-60% vegetable protein, 0-60% animal protein, 0-60% vegetable oil, and 0-60% animal oil are carried out in proportion by mass percentage It is mixed and made into raw materials, and at least one of vegetable protein or animal protein exists.

优选地,步骤(1)中加热温度控制在30~100℃的范围内。Preferably, the heating temperature in step (1) is controlled within the range of 30-100°C.

优选地,步骤(1)中pH控制在1.5~9.5的范围内。Preferably, the pH in step (1) is controlled within the range of 1.5-9.5.

优选地,所述酶包括蛋白酶以及糖酶、脂肪酶、风味酶、纤维素酶、乳酸杆菌、双岐杆菌、枯草杆菌、氧化还原酶类、异构酶、酶抑制剂、酶激活剂中的一种或多种。也即是至少包括蛋白酶。蛋白酶是水解蛋白质肽链的一类酶的总称。糖酶的作用是裂解多糖中将单糖结合在一起的化学键,使多糖降解成较小的分子。脂肪酶隶属于羧基酯水解酶类,能够逐步的将甘油三酯水解成甘油和脂肪酸。氧化还原酶类是一类催化氧化还原反应的酶,可分为氧化酶和还原酶两类。乳酸杆菌属乳酸杆菌科,因发酵糖产生大量乳酸而命名。其存在广泛,嗜酸性,生存最适pH为5.5~6.0,当然,在pH为3.0~4.5的环境中仍然能生存,它在无芽胞杆菌中是耐酸力最强的。双岐杆菌是从母乳营养儿的肠道中分离出的一种厌氧的革兰氏阳性杆菌,枯草杆菌,是芽胞杆菌属的一种。异构酶亦称异构化酶,是催化生成异构体反应的酶之总称。酶抑制剂是一类可以结合酶并降低其活性的分子。由于抑制特定酶的活性可以杀死病原体或校正新陈代谢的不平衡,许多相关药物就是酶抑制剂。酶激活剂是一种能使无活性的酶能变成有活性酶的物质。Preferably, the enzymes include protease and carbohydrase, lipase, flavor enzyme, cellulase, lactobacillus, bifidobacterium, subtilis, redox enzymes, isomerase, enzyme inhibitor, enzyme activator one or more. That is, at least protease is included. Protease is a general term for a class of enzymes that hydrolyze protein peptide chains. Carbohydrases work by cleaving the chemical bonds that hold the monosaccharides together in polysaccharides, degrading the polysaccharides into smaller molecules. Lipase belongs to the carboxyl ester hydrolase class, which can gradually hydrolyze triglycerides into glycerol and fatty acids. Oxidoreductases are a class of enzymes that catalyze redox reactions and can be divided into two categories: oxidases and reductases. Lactobacillus is a genus of Lactobacillus family, named for the large amount of lactic acid produced by fermenting sugar. It exists widely and is acidophilic. The optimal pH for survival is 5.5-6.0. Of course, it can still survive in an environment with a pH of 3.0-4.5. It has the strongest acid resistance among non-bacillus bacteria. Bifidobacterium is an anaerobic Gram-positive bacillus, Bacillus subtilis, a species of Bacillus isolated from the intestinal tract of breastfed infants. Isomerase, also known as isomerase, is a general term for enzymes that catalyze the reaction of isomers. Enzyme inhibitors are a class of molecules that bind to enzymes and reduce their activity. Since inhibiting the activity of specific enzymes can kill pathogens or correct metabolic imbalances, many related drugs are enzyme inhibitors. An enzyme activator is a substance that turns an inactive enzyme into an active enzyme.

本发明还提供一种根据前面任意一项中所述的制备方法所制备得到的具有水解蛋白的饲料。The present invention also provides a feed with hydrolyzed protein prepared according to any one of the preparation methods described above.

本发明的制备方法中所述的植物蛋白包括:豌豆蛋白、小麦蛋白、大麦蛋白、燕麦蛋白、大豆浓缩蛋白、大米蛋白、大豆分离蛋白、大豆组织蛋白、豆粕、花生蛋白、大豆粉、豌豆粉、蚕豆粉、芝麻粉、花生粉等植物蛋白中的一种或多种;所述的动物蛋白包括:鱼粉、血浆蛋白、血球蛋白等动物蛋白中的一种或多种;所述的植物油脂包括:大豆油、大豆磷脂、椰子油、橄榄油、米糠油、芝麻油、葵花油、红花油、棕榈油、菜油、花生油、棉油等植物油脂中的一种或多种;所述的动物油脂包括猪油、鸡油、鸭油、牛油、奶油中的一种或多种;所述的乳化剂包括:醋酸和脂肪酸甘油酯、乳酸和脂肪酸甘油酯、胆酸、卵磷酯、聚甘油蓖麻油醇酯、聚乙烯蓖麻油醇酸酯、酪蛋白酸钠、聚山梨酸酯(山梨醇酐脂肪酸脂)、吐温等具有乳化功能的食品及饲料添加剂中一种或多种;所述的酶包括蛋白酶以及糖酶、脂肪酶、风味酶、纤维素酶、乳酸杆菌、双岐杆菌、枯草杆菌、氧化还原酶类、异构酶等具有生物催化作用的物质、酶抑制剂和酶激活剂中的一种或多种。本发明中所述均质机包括所有具有均质功能的机械,所述乳化机包括所有具有乳化功能的机械。The vegetable protein described in the preparation method of the present invention includes: pea protein, wheat protein, barley protein, oat protein, soybean protein concentrate, rice protein, soybean protein isolate, soybean texture protein, soybean meal, peanut protein, soybean flour, pea flour One or more of plant proteins such as broad bean powder, sesame powder, peanut powder; the animal protein includes: one or more of animal protein such as fish meal, plasma protein, hemoglobulin; Oils and fats include: one or more of vegetable oils such as soybean oil, soybean lecithin, coconut oil, olive oil, rice bran oil, sesame oil, sunflower oil, safflower oil, palm oil, rapeseed oil, peanut oil, cotton oil; Animal fat includes one or more of lard, chicken fat, duck fat, butter, butter; the emulsifier includes: acetic acid and fatty acid glycerides, lactic acid and fatty acid glycerides, cholic acid, lecithin, One or more of polyglycerol ricinoleate, polyethylene ricinoleate, sodium caseinate, polysorbate (sorbitan fatty acid ester), Tween and other food and feed additives with emulsifying function; The enzymes include protease, carbohydrase, lipase, flavor enzyme, cellulase, lactobacillus, bifidobacterium, bacillus subtilis, redox enzymes, isomerase and other substances with biocatalysis, enzyme inhibitors and One or more of enzyme activators. The homogenizer in the present invention includes all machines with homogenization function, and the emulsification machine includes all machines with emulsification function.

本发明所提供的具有水解蛋白的饲料的制备方法具有以下优点:The preparation method of feed with hydrolyzed protein provided by the present invention has the following advantages:

(1)本发明所提供的具有水解蛋白的饲料的制备方法所需的投资成本更小,生产工艺更为简洁实用,占地面积小,且在均质机进行均质处理和/或乳化机进行乳化处理的过程中即发生水解反应,从而使得加工时间大大缩短,因此,可以节约能耗,在国家提倡减少大气污染、禁止燃煤的背景下,尤其具有现实意义;(1) The investment cost required for the preparation method of feed with hydrolyzed protein provided by the present invention is smaller, the production process is more concise and practical, and the floor space is small, and the homogenization treatment and/or emulsification machine are carried out in the homogenizer The hydrolysis reaction occurs during the emulsification treatment, which greatly shortens the processing time. Therefore, energy consumption can be saved, which is especially practical in the context of the country's promotion of reducing air pollution and prohibiting coal burning;

(2)本发明所提供的具有水解蛋白的饲料的制备方法采用先乳化后均质、先均质后乳化、全程乳化、全程均质的四种生产工艺,由于均质机可以把物料颗料变小变均匀,从而使得酶和其他物料能够充分接触反应,或可利用乳化机高速旋转,剪切,分散,撞击,加强物料间和酶的相互渗透,从而加强水解的效果;(2) The preparation method of the feed with hydrolyzed protein provided by the present invention adopts four kinds of production techniques of first emulsifying and then homogenizing, first homogenizing and then emulsifying, full-process emulsifying, and full-process homogenizing. Smaller and more uniform, so that the enzyme and other materials can fully contact and react, or the emulsifier can be used to rotate at high speed, shear, disperse, impact, and strengthen the mutual penetration between materials and enzymes, thereby enhancing the effect of hydrolysis;

(3)本发明所提供的具有水解蛋白的饲料的制备方法通过在均质机和/或乳化机中在酶的作用下发生水解反应,促使物料中的蛋白水解为小肽,小肽可以被动物直接消化吸收,这一点在高档水产饲料中特别有意义,因为许多高档水产的消化道比较短,对蛋白的消化吸收不全,容易造成饲料中蛋白的浪费,而本发明所提供的制备方法所得到的饲料中存在水解后的小肽,可被水产动物无障碍吸收;本发明所提供的制备方法所得到的饲料更适用于幼畜,由于幼畜消化道发育不全,蛋白酶和脂肪酶分泌不足,饲喂普通蛋白易导致消化不良、胃肠道绒毛膜上皮细胞萎缩,从而引起腹泻、生长停滞、甚至死亡等一系列问题,这在幼畜断奶阶段尤其突出,是行业内人士目前需要攻克的难题,而本发明所提供的制备方法所得到的饲料中形成的小肽可以被幼畜直接吸收,从而解决幼畜的断奶问题;(3) The preparation method of the feed with hydrolyzed protein provided by the present invention promotes the hydrolysis of the protein in the material into small peptides through the hydrolysis reaction under the action of enzymes in the homogenizer and/or emulsifier, and the small peptides can be Animals directly digest and absorb, which is particularly meaningful in high-grade aquatic feed, because the digestive tract of many high-grade aquatic products is relatively short, the digestion and absorption of protein is incomplete, and it is easy to cause waste of protein in the feed, and the preparation method provided by the present invention There are hydrolyzed small peptides in the obtained feed, which can be absorbed by aquatic animals without hindrance; the feed obtained by the preparation method provided by the present invention is more suitable for young animals, because the digestive tract of young animals is underdeveloped, and the secretion of protease and lipase is insufficient , Feeding ordinary protein can easily lead to indigestion, atrophy of the chorionic epithelial cells of the gastrointestinal tract, and a series of problems such as diarrhea, growth stagnation, and even death. However, the small peptides formed in the feed obtained by the preparation method provided by the present invention can be directly absorbed by young animals, thereby solving the weaning problem of young animals;

(4)本发明所提供的具有水解蛋白的饲料的制备方法所得到的饲料中含有的小肽可以在肠道内保护易被破坏的氨基酸。单纯的氨基酸在生物体内会根据需要重新组成肽和蛋白质,而小肽和氨基酸的混合物可以通过小肽来保护氨基酸,从而省去一部分需要重新组合的氨基酸,从而也使得本发明所提供的制备方法得到的饲料的生物评价更高,同时在饲料加工中可以减少蛋白原料的用量,这在高档水产料和幼畜饲料中尤其重要,因为高档水产料和幼畜饲料所用的蛋白原料,如鱼粉、乳粉、乳清蛋白、血浆蛋的价格都在每吨10000元以上。(4) The small peptide contained in the feed obtained by the preparation method of the feed with hydrolyzed protein provided by the present invention can protect easily destroyed amino acids in the intestinal tract. Simple amino acids will recombine peptides and proteins in vivo according to needs, and the mixture of small peptides and amino acids can protect amino acids through small peptides, thereby saving part of the amino acids that need to be recombined, thus making the preparation method provided by the present invention The biological evaluation of the obtained feed is higher, and at the same time, the amount of protein raw materials can be reduced in feed processing, which is especially important in high-grade aquatic feed and young animal feed, because the protein raw materials used in high-grade aquatic feed and young animal feed, such as fish meal, The prices of milk powder, whey protein, and plasma eggs are all above 10,000 yuan per ton.

(5)本发明所提供的具有水解蛋白的饲料的制备方法还可以通过添加含有脂肪酶的酶组合,从而提高对动物脂肪和植物油脂的水解,从而增强动物对动物脂肪和植物油脂的消化能力,增强动物的抵抗力,促进生长。(5) The preparation method of feed with hydrolyzed protein provided by the present invention can also increase the hydrolysis of animal fat and vegetable oil by adding an enzyme combination containing lipase, thereby enhancing the animal's ability to digest animal fat and vegetable oil , enhance the resistance of animals, and promote growth.

本发明提供的具有水解蛋白的饲料的制备方法所制备得到的饲料具有以下优点:The feed prepared by the preparation method of the feed with hydrolyzed protein provided by the invention has the following advantages:

(1)替代油脂、蛋白、乳糖、且适口性好,提高动物采食量;(1) It replaces fat, protein, lactose, and has good palatability, and improves animal feed intake;

(2)提高饲料中蛋白和油脂的利用率,减少蛋白饲料和能量饲料的浪费;(2) Improve the utilization rate of protein and oil in the feed, reduce the waste of protein feed and energy feed;

(3)饲料中小肽含量高,适合于高档水产的饲养和解决幼畜的断奶问题;(3) The content of small peptides in the feed is high, which is suitable for raising high-grade aquatic products and solving the weaning problem of young animals;

(4)抗应激,特别是在炎热季节,可降低“体增热”,有效缓解热应激;在寒冷季节增加能量摄入,增加生长需要营养,提高生产性能;(4) Anti-stress, especially in hot seasons, can reduce "body heat gain" and effectively relieve heat stress; increase energy intake in cold seasons, increase nutrition needed for growth, and improve production performance;

(5)提高母猪泌乳量和乳脂率,从而提高仔猪成活率及断奶窝重;(5) Increase the lactation volume and milk fat rate of sows, thereby increasing the survival rate of piglets and the weight of weaned litters;

(6)提高乳猪适口性、消化率,显著提高生长速度,能降低料肉比,提高饲料使用效能;(6) Improve the palatability and digestibility of suckling pigs, significantly increase the growth rate, reduce the ratio of feed to meat, and improve the efficiency of feed use;

(7)提高蛋禽产蛋性能,延长产蛋高峰期,能提高肉禽生长速度和肉质;(7) Improve the egg production performance of laying poultry, prolong the peak period of egg production, and improve the growth rate and meat quality of meat poultry;

(8)延长饲料的保存时间、方便运输,细化度均匀显著提升,提高综合使用经济效益;(8) Prolong the storage time of feed, facilitate transportation, and significantly improve the uniformity of refinement, and improve the economic benefits of comprehensive use;

(9)能把液态油转化固体粉末状,易添加,与其他饲料原料混合均匀后即可使用,加工方便。(9) It can convert liquid oil into solid powder, easy to add, and can be used after being evenly mixed with other feed materials, which is convenient for processing.

具体实施方式detailed description

结合具体实施例对本发明进一步详细地描述。The present invention is further described in detail in conjunction with specific embodiments.

蛋白质通过水解,水解为二肽或三肽的产物在人体内要比自由氨基酸易于吸收,比没有水解的蛋白质更易于吸收,因此,在用不同的蛋白质酶对蛋白质进行水解时,必须要进行水解度测定。Through hydrolysis of protein, the product of hydrolysis into dipeptide or tripeptide is easier to absorb in the human body than free amino acid, and easier to absorb than protein without hydrolysis. Therefore, when using different protein enzymes to hydrolyze protein, it must be hydrolyzed degree measurement.

水解度的定义:蛋白质的水解度DH代表蛋白质在水解过程中,肽键被裂解的程度或百分比。Definition of degree of hydrolysis: The degree of hydrolysis DH of protein represents the degree or percentage of peptide bonds being cleaved during protein hydrolysis.

其检测方法如下:取水解蛋白液5.00ml于小烧杯中,加入60ml蒸馏水,然后磁力搅拌并用精密pH计测定其pH值,接着用0.05mol/l NaOH溶液滴定至pH=8.2,然后加入已中和好的甲醛溶液10ml,接着滴定至pH=9.2,记录将其pH值从8.2滴定9.2时后消耗的0.05mol/lNaOH溶液的体积,同时做试剂空白滴定实验(蒸馏水),然后计算其水解度。水解度DH的计算公式如下:The detection method is as follows: take 5.00ml of hydrolyzed protein solution in a small beaker, add 60ml of distilled water, then magnetically stir and measure the pH value with a precision pH meter, then titrate to pH=8.2 with 0.05mol/l NaOH solution, and then add Reconcile 10ml of formaldehyde solution, then titrate to pH=9.2, record the volume of 0.05mol/l NaOH solution consumed after its pH value is titrated from 8.2 to 9.2, and do reagent blank titration experiment (distilled water) at the same time, then calculate its degree of hydrolysis . The formula for calculating the degree of hydrolysis DH is as follows:

DD. Hh == CC ·· (( VV 11 -- VV 22 )) ·· VV // 55 Mm ·&Center Dot; PP ·· 88 ×× 100100 %%

C为NaOH浓度,单位为mol/l;C is NaOH concentration, the unit is mol/l;

V1和V2分别为样品和空白消耗的NaOH的体积,均为从PH8.2滴至9.2的体积,单位为ml;V 1 and V 2 are the volumes of NaOH consumed by the sample and the blank respectively, both of which are dropped from pH 8.2 to 9.2, and the unit is ml;

V为蛋白酶解液的体积,单位为ml;V is the volume of proteolysis solution, in ml;

M为样品质量,单位为g;M is the mass of the sample, in g;

P为原料中蛋白的质量百分数,单位为%;P is the mass percentage of protein in the raw material, in %;

8为每克蛋白质所含的肽键的毫摩尔数mmol/g(参考大豆蛋白的值,如果其他蛋白不同,可做略微调整)。8 is the number of millimoles of peptide bonds per gram of protein mmol/g (refer to the value of soybean protein, if other proteins are different, a slight adjustment can be made).

实施例1Example 1

将150kg乳清粉、500kg大豆蛋白、250kg猪油、150kg大豆油加入2000kg水,温度控制在50-60℃之间,pH值为7.0左右,加入5kg乳化剂,搅拌,加入中性蛋白酶1.5kg、木瓜蛋白酶1.5kg、脂肪酶1.0kg,搅拌,通过均质机均质细化,压力29-35MPa左右,然后进入乳化机进行处理,乳化机转子转速为1200r/min左右,在静磨片、动磨片、螺旋桨叶三者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应后,历时90分钟左右,将物料半成品经喷雾干燥塔进行喷雾干燥,成为粉末,干燥后的产品,过筛,计量,包装。其水解度为13.7%。Add 150kg of whey powder, 500kg of soybean protein, 250kg of lard, and 150kg of soybean oil into 2000kg of water. The temperature is controlled between 50-60°C and the pH value is about 7.0. Add 5kg of emulsifier, stir, and add 1.5kg of neutral protease , papain 1.5kg, lipase 1.0kg, stir, homogeneous refinement by homogenizer, pressure about 29-35MPa, then enter emulsifier for processing, emulsifier rotor speed is about 1200r/min, in static grinding, After strong and reciprocating hydraulic shearing, friction, centrifugal extrusion, liquid flow collision and other comprehensive effects are formed in the reasonably narrow gap between the movable grinding plate and the propeller blade, it takes about 90 minutes to spray the semi-finished material The drying tower is spray-dried to become powder, and the dried product is sieved, measured, and packaged. Its degree of hydrolysis is 13.7%.

实施例2Example 2

将50kg乳清粉、160kg椰子油、290kg棕榈油、500kg豆粕置入2000kg、pH值为6.5-7.5的水溶液中,温度控制在60℃左右,加入10kg乳化剂,搅拌,加入枯草杆菌1.5kg,木瓜蛋白酶1.5kg、菠萝蛋白酶1.0kg,搅拌,通过均质机均质细化,压力在40-45MPa左右,然后进入乳化机进行处理,乳化机转子转速为18000r/min左右,在静磨片、动磨片两者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应后,通过循环管将物料在容器中循环往复以上工作过程,历时300分钟左右,将物料半成品经喷雾干燥塔进行喷雾干燥,成为粉末,干燥后的产品,过筛,计量,包装。其水解度为8.7%。Put 50kg of whey powder, 160kg of coconut oil, 290kg of palm oil, and 500kg of soybean meal into a 2000kg aqueous solution with a pH value of 6.5-7.5. The temperature is controlled at about 60°C. Add 10kg of emulsifier, stir, and add 1.5kg of Bacillus subtilis. Papain 1.5kg, bromelain 1.0kg, stirred, homogenized and refined by a homogenizer, the pressure is about 40-45MPa, and then enters the emulsifier for processing. The rotor speed of the emulsifier is about 18000r/min. After the combined effect of strong and reciprocating hydraulic shearing, friction, centrifugal extrusion, and liquid flow collision is formed in the reasonably narrow gap between the moving grinding discs, the material is circulated in the container through the circulation tube. , which lasted about 300 minutes, the semi-finished material was spray-dried through a spray drying tower to become a powder, and the dried product was sieved, measured, and packaged. Its degree of hydrolysis is 8.7%.

实施例3Example 3

将150kg乳清粉、195kg椰子油、200kg棕榈油、440kg小麦蛋白置入2000kg、pH值在1.5-3.0之间的水溶液中,温度控制在40-50℃左右,加入15kg乳化剂,搅拌,加入胃蛋白酶5kg,搅拌,然后进入乳化机进行处理,乳化机转子转速为2900r/min左右,在定子、转子、螺旋桨叶三者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应后,历时120分钟左右,然后进入高压均质机均质,压力在20MPa左右,将物料进行细化,半成品经喷雾干燥塔进行喷雾干燥。成为粉末,干燥后的产品,过筛,计量,包装。其水解度为18.6%。Put 150kg of whey powder, 195kg of coconut oil, 200kg of palm oil, and 440kg of wheat protein into 2000kg of aqueous solution with a pH value between 1.5-3.0. Pepsin 5kg, stirred, and then enter the emulsification machine for processing, the rotor speed of the emulsification machine is about 2900r/min, forming strong, reciprocating hydraulic shearing, After the comprehensive effects of friction, centrifugal extrusion, liquid flow collision, etc., it takes about 120 minutes, and then enters the high-pressure homogenizer for homogenization, the pressure is about 20MPa, the material is refined, and the semi-finished product is spray-dried through the spray drying tower. Become a powder, dry the product, sieve, measure, and pack. Its degree of hydrolysis is 18.6%.

实施例4Example 4

将50kg乳清粉、350kg棕榈油、100kg椰子油、500kg大米蛋白置入2000kg、pH值为5.5-6.5的水溶液中,温度控制在45-60℃左右.,加入20kg乳化剂,搅拌,加入菠萝蛋白酶4kg、纤维素酶1.5kg,搅拌,然后进入乳化机进行处理,乳化机转子转速为8000r/min,在定子、转子、螺旋桨叶三者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应后,历时120分钟左右,然后进入高压均质机均质,压力在280MPa左右,将物料进行细化,半成品经喷雾干燥塔进行喷雾干燥。成为粉末,干燥后的产品,过筛,计量,包装。其水解度为13.7%。Put 50kg of whey powder, 350kg of palm oil, 100kg of coconut oil, and 500kg of rice protein into 2000kg of aqueous solution with a pH value of 5.5-6.5. The temperature is controlled at about 45-60°C. Add 20kg of emulsifier, stir, and add pineapple Protease 4kg, cellulase 1.5kg, stir, and then enter the emulsifier for processing. The rotor speed of the emulsifier is 8000r/min, and a strong, reciprocating liquid is formed in a reasonably narrow gap between the stator, rotor, and propeller blades. After the comprehensive effects of force shearing, friction, centrifugal extrusion, liquid flow collision, etc., it takes about 120 minutes, and then enters the high-pressure homogenizer for homogenization, the pressure is about 280MPa, the material is refined, and the semi-finished product is sprayed through the spray drying tower dry. Become a powder, dry the product, sieve, measure, and pack. Its degree of hydrolysis is 13.7%.

实施例5Example 5

将150kg乳清粉、250kg大豆蛋白、250kg大米蛋白、100kg椰子油、250kg棕榈油、置入pH值为6.5-7.5的2000kg水溶液中,温度控制在45℃左右,加入15kg乳化剂,搅拌,加入风味酶1kg、枯草杆菌1.5kg、菠萝蛋白酶2.5kg,然后进入乳化机进行处理,乳化机转子转速为4800r/min,在定子、转子、螺旋桨叶三者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应,历时120分钟左右后,半成品经喷雾干燥塔进行喷雾干燥。成为粉末,干燥后的产品,过筛,计量,包装。其水解度为10.7%。Put 150kg of whey powder, 250kg of soybean protein, 250kg of rice protein, 100kg of coconut oil, and 250kg of palm oil into 2000kg of aqueous solution with a pH value of 6.5-7.5. The temperature is controlled at about 45°C. Add 15kg of emulsifier, stir, and add Flavor enzyme 1kg, Bacillus subtilis 1.5kg, Bromelain 2.5kg, then enter the emulsification machine for processing, the rotor speed of the emulsification machine is 4800r/min, forming a strong, The comprehensive effects of reciprocating hydraulic shearing, friction, centrifugal extrusion, liquid flow collision, etc., lasted about 120 minutes, and the semi-finished product was spray-dried through the spray drying tower. Become a powder, dry the product, sieve, measure, and pack. Its degree of hydrolysis is 10.7%.

实施例6Example 6

将100kg乳清粉、150kg椰子油、250kg棕榈油、250kg小麦蛋白、200kg大豆蛋白,置入pH值为6.5-7.5的2000kg水溶液中,温度控制在35-40℃左右,加入20kg乳化剂,搅拌,加入枯草杆菌1.5kg、菠萝蛋白酶2.5kg,然后进入乳化机进行处理,乳化机转子转速为2000-2900r/min左右,在定子、转子、螺旋桨叶三者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应后,历时200分钟左右,半成品经喷雾干燥塔进行喷雾干燥。成为粉末,干燥后的产品,过筛,计量,包装。其水解度为15.5%。Put 100kg of whey powder, 150kg of coconut oil, 250kg of palm oil, 250kg of wheat protein, and 200kg of soybean protein into 2000kg of aqueous solution with a pH value of 6.5-7.5. The temperature is controlled at about 35-40°C. Add 20kg of emulsifier and stir. , add 1.5kg of Bacillus subtilis and 2.5kg of bromelain, and then enter the emulsification machine for processing. The rotor speed of the emulsification machine is about 2000-2900r/min, forming a strong , reciprocating hydraulic shearing, friction, centrifugal extrusion, liquid flow collision and other comprehensive effects, it takes about 200 minutes, and the semi-finished product is spray-dried through the spray drying tower. Become a powder, dry the product, sieve, measure, and pack. Its degree of hydrolysis is 15.5%.

实施例7Example 7

将500kg乳清粉、250kg大豆蛋白、250kg大米蛋白,置入1000kg水溶液中,pH值为8.0-9.5,温度控制在50℃左右,加入25kg乳化剂,加入胰蛋白酶2.0kg、碱性蛋白酶2.5kg、罗汉果蛋白酶1.5kg,然后进入高压均质机均质,压力可以在400MPa内自由调整,通过循环管将物料在容器中循环往复以上工作过程,达到细化的目的,然后再搅拌300分钟,半成品经烘干机烘干,干燥后的产品,粉碎、过筛,计量,包装。其水解度为9.7%。Put 500kg of whey powder, 250kg of soybean protein, and 250kg of rice protein into 1000kg of aqueous solution, the pH value is 8.0-9.5, and the temperature is controlled at about 50°C. Add 25kg of emulsifier, 2.0kg of trypsin, and 2.5kg of alkaline protease 1.5kg of Luo Han Guo protease, and then enter the high-pressure homogenizer for homogenization, the pressure can be adjusted freely within 400MPa, and the material is circulated in the container through the circulation tube to achieve the purpose of refinement, and then stirred for 300 minutes, the semi-finished product After being dried by a dryer, the dried product is crushed, sieved, measured, and packaged. Its degree of hydrolysis is 9.7%.

实施例8Example 8

将150kg乳清粉、100kg椰子油、150kg棕榈油、200kg大豆蛋白、175kg大米蛋白置入700kg水中,pH值为6.3-7.5,温度控制在50-60℃左右,加入25kg乳化剂,搅拌,加入1.5kg枯草杆菌、1.5kg木瓜蛋白酶,然后进入高压均质机均质,压力可以在400MPa内自由调整,通过循环管将物料在容器中循环往复以上工作过程,达到细化的目的,然后再搅拌360分钟,半成品经烘干机烘干,干燥后的产品,粉碎、过筛,计量,包装。其水解度为13.7%。Put 150kg of whey powder, 100kg of coconut oil, 150kg of palm oil, 200kg of soybean protein, and 175kg of rice protein into 700kg of water, the pH value is 6.3-7.5, the temperature is controlled at about 50-60°C, add 25kg of emulsifier, stir, add 1.5kg of Bacillus subtilis, 1.5kg of papain, and then enter the high-pressure homogenizer for homogenization, the pressure can be adjusted freely within 400MPa, and the materials are circulated in the container through the circulation pipe to achieve the purpose of refinement, and then stir again 360 minutes, the semi-finished product is dried by the dryer, and the dried product is crushed, sieved, measured, and packaged. Its degree of hydrolysis is 13.7%.

实施例9Example 9

将50kg乳清粉、500kg大米蛋白、250kg棕榈油、150kg大豆油加入2000kg水,温度控制在50-60℃之间,pH值为7.0左右,加入5kg乳化剂,搅拌,加入中性蛋白酶1.5kg、木瓜蛋白酶1.5kg,搅拌,通过均质机均质细化,压力在15-25MPa左右,再加入然后进入乳化机进行处理,乳化机转子转速为2900r/min左右,在静磨片、动磨片、螺旋桨叶三者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应后,通过循环管将物料在容器中循环往复以上工作过程,历时90分钟左右,将物料半成品经喷雾干燥塔进行喷雾干燥,成为粉末,干燥后的产品,过筛,计量,包装。其水解度为11.3%。Add 50kg of whey powder, 500kg of rice protein, 250kg of palm oil, and 150kg of soybean oil into 2000kg of water, keep the temperature between 50-60°C and the pH value at about 7.0, add 5kg of emulsifier, stir, and add 1.5kg of neutral protease 1.5kg of papain, stirred, homogenized and refined by a homogenizer, the pressure is about 15-25MPa, then added and then entered into an emulsifier for processing. The rotor speed of the emulsifier is about 2900r/min. After forming strong and reciprocating hydraulic shearing, friction, centrifugal extrusion, liquid flow collision and other comprehensive effects in the reasonably narrow gap between the blades and propeller blades, the materials are circulated and reciprocated in the container through the circulation pipe. The process lasts about 90 minutes, and the semi-finished material is spray-dried through a spray drying tower to become a powder. The dried product is sieved, measured, and packaged. Its degree of hydrolysis is 11.3%.

实施例10Example 10

将670kg大豆粉、330kg棕榈油加入2000kg水中,pH为5.5-7,温度控制在35-40℃左右,加入10kg乳化剂,搅拌,加入乳酸杆菌3kg,双歧杆菌1.5kg,然后进入乳化机进行处理,转速为11000r/min左右,在静磨片、动磨片、螺旋桨叶三者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应后,历时150分钟后,半成品经喷雾干燥塔进行喷雾干燥。成为粉末,干燥后的产品,过筛,计量,包装。其水解度在9.8%。Add 670kg of soybean flour and 330kg of palm oil into 2000kg of water, the pH is 5.5-7, the temperature is controlled at about 35-40°C, add 10kg of emulsifier, stir, add 3kg of Lactobacillus and 1.5kg of Bifidobacterium, and then enter the emulsification machine for further processing Processing, the rotating speed is about 11000r/min, forming strong and reciprocating hydraulic shearing, friction, centrifugal extrusion, liquid flow collision, etc. After the comprehensive effect, after 150 minutes, the semi-finished product is spray-dried through the spray drying tower. Become a powder, dry the product, sieve, measure, and pack. Its degree of hydrolysis is 9.8%.

实施例11Example 11

将50kg乳清粉、160kg椰子油、290kg棕榈油、500kg小麦蛋白置入2000kg、pH值为6.5-7.5的水溶液中,温度控制在60℃左右,加入10kg乳化剂,搅拌,加入枯草杆菌1.5kg、木瓜蛋白酶1.5kg、菠萝蛋白酶1.0kg,搅拌,通过均质机均质细化,压力在80MPa左右,然后进入乳化机进行处理,乳化机转子转速为2900r/min,左右,在静磨片、动磨片、螺旋桨叶三者之间的合理狭窄的间隙中形成强烈、往复的液力剪切、摩擦、离心挤压、液流碰撞等综合效应后,通过循环管将物料在容器中循环往复以上工作过程,历时300分钟左右,将物料半成品经喷雾干燥塔进行喷雾干燥,成为粉末,干燥后的产品,过筛,计量,包装。其水解度为15.2%。Put 50kg of whey powder, 160kg of coconut oil, 290kg of palm oil, and 500kg of wheat protein into 2000kg of aqueous solution with a pH value of 6.5-7.5. The temperature is controlled at about 60°C. Add 10kg of emulsifier, stir, and add 1.5kg of Bacillus subtilis , papain 1.5kg, bromelain 1.0kg, stirring, homogeneous refinement by homogenizer, pressure is about 80MPa, then enters emulsification machine for processing, emulsification machine rotor speed is 2900r/min, about, in static grinding, In the reasonably narrow gap between the movable grinding plate and the propeller blade, strong and reciprocating hydraulic shearing, friction, centrifugal extrusion, liquid flow collision and other comprehensive effects are formed, and the material is circulated in the container through the circulation pipe. The above working process lasted about 300 minutes, and the semi-finished material was spray-dried through the spray drying tower to become powder, and the dried product was sieved, measured, and packaged. Its degree of hydrolysis is 15.2%.

上述具体实施方式用来解释说明本发明,仅为本发明的优选实施例而已,而不是对本发明进行限制,在本发明的精神和权利要求的保护范围内,对本发明作出的任何修改、等同替换、改进等,都落入本发明的保护范围。The specific implementation above is used to explain the present invention, and it is only a preferred embodiment of the present invention, rather than restricting the present invention. Within the spirit of the present invention and the protection scope of the claims, any modification and equivalent replacement made to the present invention , improvements, etc., all fall within the 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.
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Cited By (3)

* 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
CN110089634A (en) * 2018-01-31 2019-08-06 沈喆如 It is a kind of with enzymatic hydrolysis small peptide-additive complex compound feed and preparation method thereof
CN116754711A (en) * 2023-08-17 2023-09-15 蓝星安迪苏南京有限公司 Emulsifying capacity evaluation method of emulsifier for feed

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 A kind of production method of corn protein isolate
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 A kind of production method of corn protein isolate
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 (4)

* 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
CN110089634A (en) * 2018-01-31 2019-08-06 沈喆如 It is a kind of with enzymatic hydrolysis small peptide-additive complex compound feed and preparation method thereof
CN116754711A (en) * 2023-08-17 2023-09-15 蓝星安迪苏南京有限公司 Emulsifying capacity evaluation method of emulsifier for feed
CN116754711B (en) * 2023-08-17 2023-11-07 蓝星安迪苏南京有限公司 Emulsifying capacity evaluation method of emulsifier for feed

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