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CN119614547A - Biological compound enzyme preparation and preparation method thereof - Google Patents

Biological compound enzyme preparation and preparation method thereof Download PDF

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Publication number
CN119614547A
CN119614547A CN202411749330.0A CN202411749330A CN119614547A CN 119614547 A CN119614547 A CN 119614547A CN 202411749330 A CN202411749330 A CN 202411749330A CN 119614547 A CN119614547 A CN 119614547A
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China
Prior art keywords
enzyme
parts
auxiliary agent
pellet core
composite
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Inventor
刘文龙
伏圣秘
张法玲
杜正超
陈志华
李玉
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Shandong Lonct Enzymes Co ltd
Tianjin University of Science and Technology
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Shandong Lonct Enzymes Co ltd
Tianjin University of Science and Technology
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Priority to CN202411749330.0A priority Critical patent/CN119614547A/en
Publication of CN119614547A publication Critical patent/CN119614547A/en
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Abstract

The invention belongs to the technical field of enzyme engineering, and particularly relates to a composite enzyme particle and a preparation method thereof. The enzyme granule comprises an enzyme pill core and an auxiliary agent layer, wherein the enzyme pill core is used as a core part, the auxiliary agent layer is coated on the outer layer of the enzyme pill core, and the enzyme pill core comprises an enzyme component and a stabilizer. The improved composite enzyme particles improve the storage stability of the enzyme, store under the same condition, improve the retention rate of the enzyme activity by 20-30%, improve the mixing uniformity of the enzyme by 20% after shaking with the same intensity, improve the stress resistance in the use process, store under the same condition after dissolving with high pH, prolong the half life of the enzyme by 30-50%, and in addition, can reduce the dust and labor intensity in the use process and the influence of human factors on the production, and is beneficial to promoting the automation of industrial production, thereby improving the stability of the production process and improving the product quality.

Description

Biological compound enzyme preparation and preparation method thereof
Technical field:
the invention belongs to the technical field of enzyme engineering, and particularly relates to a high-efficiency biological compound enzyme preparation granule and a preparation method thereof.
Technical background:
At present, biological enzymes are widely used in textile degumming and refining treatment, and can greatly improve the production efficiency. Compared with chemical treatment, the use of biological enzyme has unique treatment effect particularly on the degumming process of cotton, hemp and the like and the textile finishing process of jeans and the like. At present, most of industrially used enzymes are added in the form of liquid single enzyme or compound enzyme powder, and the liquid compound enzyme has poor stability and is unfavorable for storage and transportation. The components such as enzymes and fillers in the solid composite enzyme powder are not uniform in specific gravity and fineness, so that materials with different specific gravities and fineness are easy to separate and even layer in the process of carrying or transporting, and the mixing uniformity of the composite enzyme preparation is affected, so that the using effect is affected. The powder complex enzyme is easy to generate dust during the weighing and using and adding processes, and the contact or inhalation of people can cause contact allergic reaction, for example, if the contact or inhalation is excessive for a long time, the contact or inhalation can cause harm to human skin, eyes, nasal mucosa and tissues thereof, and the health is affected.
In the aspect of stress resistance and use effect of the enzyme, the stress resistance of the enzyme is improved by a genetic engineering means at present so as to improve the application effect of the enzyme, but the improvement is also achieved, but the genetic engineering aspect has high cost for enzyme modification, long research and development period, unsatisfactory effect after modification and the like, and the requirements of low cost and urgent need of the current industry cannot be met.
The technical staff in the field aim to develop a stable and efficient enzyme granule and a preparation process thereof so as to meet the requirements of high efficiency, simplicity and safety of industrial production, realize low dust or no dust in workshops, reduce the labor intensity of people and the influence of human factors on the production, promote the automation of the industrial production, and improve the stability of the production process so as to improve the product quality.
The invention comprises the following steps:
the invention aims to provide stable, efficient and environment-friendly composite enzyme particles and a preparation method thereof,
The invention provides a stable and efficient composite enzyme particle, which comprises an enzyme pellet core and an auxiliary agent layer, wherein the enzyme pellet core is used as a core part, the auxiliary agent layer is coated on the outer layer of the enzyme pellet core, and the enzyme pellet core comprises an enzyme component and a stabilizer;
Further, the weight ratio of the enzyme pellet core to the auxiliary agent layer is 4:1;
further, the weight part ratio of the enzyme component and the stabilizer in the enzyme pellet core is 40-85:10-40, and preferably, the weight part ratio of the enzyme component and the stabilizer is 60-65:35-40.
Further, the enzyme component is selected from 2 or more of the following enzyme classes alkaline protease, alkaline pectinase, alkaline lipase, neutral cellulase, xylanase, laccase, amylase and mannanase;
preferably, the enzyme component comprises, by weight, 1-5 parts of alkaline protease, 10-20 parts of alkaline pectase, 6-10 parts of alkaline lipase, 30-40 parts of neutral cellulase, 20-30 parts of xylanase, 5-10 parts of laccase, 5-10 parts of amylase and 2-5 parts of mannanase;
Further, the stabilizer is selected from 2 or more of sorbitol, glucose, dextrin, trehalose, mannitol, calcium chloride, copper sulfate and zinc sulfate;
Preferably, the stabilizer comprises the following components, by weight, 30-40 parts of sorbitol, 35-40 parts of dextrin, 20-25 parts of trehalose, 4.5-6 parts of calcium chloride and 0.3-0.5 part of copper sulfate;
further, the auxiliary agent layer comprises one or more of polyethylene glycol, sodium alkyl sulfonate, alkylphenol ethoxylates, fatty alcohol ethoxylates and tween;
Preferably, the auxiliary agent layer comprises 60 parts by weight of C12-C14 fatty alcohol polyoxyethylene ether, 1000 30 parts by weight of polyethylene glycol and 10 parts by weight of alkylphenol polyoxyethylene ether.
The second technical scheme provided by the invention is a preparation method of the composite enzyme particles, which comprises the steps of enzyme immobilization treatment, enzyme pellet core preparation and addition of an auxiliary agent layer, and specifically comprises the following steps:
(1) The immobilization treatment of the enzyme is as follows:
Immobilizing all or part of the enzyme components in the enzyme pellet core, immobilizing the enzyme to be immobilized by adopting an immobilization method commonly used in the field;
further, the immobilization is to add enzyme into an immobilization reagent, stir and mix, and carry out embedding, adsorption or crosslinking immobilization treatment at a certain pH and temperature;
Further, the enzyme to be immobilized is alkaline protease, alkaline pectase, alkaline lipase, amylase and laccase;
The immobilized reagent is one or more selected from cyclodextrin, carboxymethyl starch, sodium carboxymethyl cellulose, sodium alginate, calcium chloride, silicon dioxide, polyvinyl alcohol, chitosan, montmorillonite and calcium phosphate;
still further, the immobilizing agent includes, but is not limited to, at least one of sodium alginate, calcium chloride, cyclodextrin, chitosan, CMC, montmorillonite, etc.;
Preferably, the alkaline protease is immobilized by embedding sodium alginate and calcium chloride so as to reduce the hydrolysis of the alkaline protease;
preferably, the alkaline lipase is subjected to embedding treatment by adopting beta-cyclodextrin, so that the catalytic activity and stress resistance of the alkaline lipase are improved;
preferably, the alkaline pectinase is crosslinked and fixed by chitosan so as to improve alkali resistance and heat resistance;
Preferably, the amylase or laccase is immobilized by montmorillonite adsorption to improve alkali resistance of the enzyme.
(2) The preparation method of the enzyme pill core comprises the following steps:
mixing all enzyme components and stabilizing agents in the enzyme pill core according to the weight ratio of 40-85:10-40 to obtain a mixture, adding microcrystalline cellulose disintegrating agent according to the weight ratio of 90-95:5-10 of the mixture, uniformly mixing, preparing a wet enzyme pill core by adopting a wet rotary extrusion granulating method, and then drying the wet enzyme pill core in a fluidized bed;
further, the weight ratio of the materials in the granulating process of the enzyme pill core is 1:5-2:5;
further, the temperature of the spun extruded material is <70 ℃, preferably <60 ℃, more preferably <50 ℃;
further, extruding and granulating by using a 30-40 mesh net, and controlling the diameter of the extruded strip to be 0.3-0.5mm;
Further, adding the extruded strip into a shot blasting machine, and blasting at a rotating speed of 40-120rpm for 30 seconds, wherein the granules are controlled to be nearly spherical, so as to obtain wet enzyme pellet core granules with a diameter of 0.3-0.5mm, and preferably at a rotating speed of 60-80rpm;
Further, the wet enzyme pellet core particles are placed in a fluidized bed for drying, and the air inlet temperature is 60-70 ℃ and the drying is carried out under the vacuum for 0.3-0.5 time until the moisture is <5%, preferably the moisture is <4%, more preferably the moisture is <3%;
(3) The preparation method of the additive comprises the following steps:
weighing the auxiliary agent according to the weight ratio of the enzyme pill core to the auxiliary agent of 4:1, pouring the auxiliary agent into an oil bath pot, and heating to 90-110 ℃ to melt the auxiliary agent;
Pouring the dried enzyme pellet core into a fluidized bed, controlling the air inlet temperature of the fluidized bed to be 15-25 ℃ and the air quantity to be 60m < 3 >/h-170 m < 3 >/h, and spraying the auxiliary agent after the thermal dissolution on the enzyme pellet core by a peristaltic pump under the atomization pressure of 0.3-0.4Mpa to obtain the composite enzyme particles.
Further, in order to improve the hardness of the particles, a protective layer is sprayed outside the auxiliary agent layer according to the weight ratio of the composite enzyme particles to the protective layer of 9:1, wherein the protective layer comprises the following components in parts by weight of 20 parts of CMC, 30 parts of microcrystalline cellulose, 50 parts of calcium carbonate and 400 parts of water, and the components are mixed and emulsified into suspension.
Further, the spraying method of the protective layer comprises the following steps of controlling the air inlet temperature of a fluidized bed to be 40-60 ℃, the air quantity to be 60m < 3 >/h to 170m < 3 >/h, and the atomization pressure to be 0.5-0.7Mpa until all the protective layer is sprayed on enzyme particles.
The beneficial effects are that:
The invention aims to provide stable, environment-friendly and efficient composite enzyme granules and a preparation method thereof, wherein the composite enzyme granules are prepared by mixing powder with simple enzyme, so that the storage stability of the enzyme is improved, the retention rate of enzyme activity is improved by 20-30%, the mixing uniformity of the enzyme is improved by 20% after shaking with the same strength, the stress resistance in the use process is improved, the enzyme half life is prolonged by 30-50% after dissolution with high pH, and in addition, the dust and labor intensity in the use process and the influence of human factors on production are obviously reduced, the automation of industrial production is promoted, and the stability of the production process is improved to improve the product quality.
The specific embodiment is as follows:
In order to more clearly illustrate the advantageous features and properties of the present invention, a highly efficient bio-complex enzyme preparation granule and a method for preparing the same according to the present invention will be described in detail, and the following examples are only given for illustrating the enzyme preparation granule and the method for preparing the same, but are not intended to limit the scope of the present invention.
The invention aims to provide high-efficiency biological compound enzyme preparation particles and a preparation method thereof, so that the problems of dust hazard and mixing uniformity of powder compound enzyme in the using process are solved, and the storage and use stability of the enzyme in the compound enzyme are improved. The preparation method is safe, simple, convenient and efficient. The enzyme particles comprise an enzyme pellet core and an auxiliary agent, and the auxiliary agent can improve the action efficiency of the enzyme to a certain extent.
It is understood that within the scope of the present invention, the above-described technical features of the present invention and technical features specifically described in the following (embodiments) may be combined with each other to constitute a new or preferred technical combination scheme. Is limited to space and will not be described again.
Example 1A biological Complex enzyme preparation granule and method for preparing the same
The stable and efficient composite enzyme particle comprises an enzyme pellet core and an auxiliary agent layer, wherein the enzyme pellet core is used as a core part, the auxiliary agent layer is coated on the outer layer of the enzyme pellet core, and the enzyme pellet core comprises an enzyme component and a stabilizer;
The weight ratio of the enzyme pellet core to the auxiliary agent layer is 4:1;
The weight part ratio of the enzyme component to the stabilizer in the enzyme pill core is 8:2;
The enzyme component comprises, by weight, 3 parts of alkaline protease, 15 parts of alkaline pectase, 8 parts of alkaline lipase, 35 parts of neutral cellulase, 25 parts of xylanase, 5 parts of laccase, 6 parts of amylase and 3 parts of mannanase;
The stabilizer comprises the following components in parts by weight of 35 parts of sorbitol, 38 parts of dextrin, 21 parts of trehalose, 5.6 parts of calcium chloride and 0.4 part of copper sulfate;
The auxiliary agent layer comprises the following components in parts by weight of 60 parts of C12-C14 fatty alcohol polyoxyethylene ether, 1000 30 parts of polyethylene glycol and 10 parts of alkylphenol polyoxyethylene ether.
According to the composition and the dosage, the preparation method is as follows:
(1) Immobilization treatment of partial enzymes:
Embedding and immobilizing alkaline protease by sodium alginate and calcium chloride to improve stress resistance of the enzyme;
Dissolving alkaline protease in 2% sodium alginate solution, atomizing under 0.5Mpa, adding into 3% calcium chloride solution containing 0.2% glutaraldehyde, fixing for 0.5 hr, filtering, washing with distilled water for 3 times, and drying at low temperature.
The alkaline lipase is embedded with beta cyclodextrin to improve the catalytic activity and stress resistance;
And respectively weighing 10 times of the weight of the lipase, mixing and stirring uniformly, adding into a lipase phosphate buffer solution with the pH of 7-8, stirring, reacting for 1h, pouring the product into a beaker after the reaction is finished, washing with 65% ethanol solution, centrifuging, and drying the product at 45-50 ℃ to obtain the immobilized lipase.
Crosslinking and fixing alkaline pectinase by chitosan to improve alkali resistance and heat resistance;
Weighing alkaline pectase, adding into chitosan suspension, adding glutaraldehyde solution with concentration of 0.2% -0.3%, immobilizing for 4 hours at 25-30 ℃, filtering, washing, recovering precipitate, and drying at 45-50 ℃.
The alkali resistance of the amylase and laccase is improved by the montmorillonite adsorption immobilization treatment. The optimal immobilization condition is that montmorillonite with 5 times weight of enzyme is weighed and added into enzyme solution with pH of 6.5-8.0, the temperature is 15-20 ℃, and the adsorption immobilization time is 0.5-2 hours. Filtering or centrifuging the immobilized enzyme, recovering immobilized enzyme, oven drying at low temperature, pulverizing, and sieving;
(2) Preparing an enzyme pill core:
mixing all enzyme components and a stabilizer in the enzyme pellet core according to the weight ratio of 8:2, adding a microcrystalline cellulose disintegrating agent according to the weight ratio of 95:5 into the mixture according to the mixture, uniformly mixing, preparing a wet enzyme pellet core by adopting a wet rotary extrusion granulating method, and then drying the wet enzyme pellet core in a fluidized bed;
In the wet rotary extrusion granulating process, the proportion of water to materials (enzyme component, stabilizer and microcrystalline cellulose disintegrating agent) is controlled at 1.5:5, the temperature of the rotary extrusion materials is less than 50 ℃, a 30-mesh hole net is selected for extrusion granulating, the diameter of an extrusion strip is controlled to be 0.3-0.5mm, the extrusion strip is added into a shot blasting machine, the rotating speed is 80rpm, the shot blasting is carried out for 30 seconds, and the particles are controlled to be nearly spherical, so that wet enzyme pellet core particles with the diameter of 0.3-0.5mm are obtained;
drying the wet enzyme pellet core particles in a fluidized bed at 60-70 ℃ and 0.3-0.5 vacuum until the moisture is less than 3%;
(3) Spraying an auxiliary agent layer:
Weighing the auxiliary agent according to the weight ratio of the enzyme pill core to the auxiliary agent of 4:1, pouring the auxiliary agent into an oil bath pot, heating to 90-110 ℃, melting and spraying the mixture onto the surface of the enzyme pill core;
pouring the dried enzyme pellet core particles into a fluidized bed, controlling the air inlet temperature of the fluidized bed to be 15-25 ℃ and the air quantity to be 80
M3/h, spraying the auxiliary agent after the thermal dissolution on the enzyme pill core by a peristaltic pump under the atomization pressure of 0.3-0.4 Mpa.
(4) And (3) spraying a protective layer:
In order to improve the hardness of the granules, a protective layer is sprayed outside the auxiliary agent layer according to the weight ratio of enzyme granules to the protective layer of 9:1, and the protective layer comprises the following components in parts by weight of 20 parts of CMC, 30 parts of microcrystalline cellulose, 50 parts of calcium carbonate and 400 parts of water, and the components are mixed and emulsified into suspension.
The spraying method of the protective layer comprises the following steps of controlling the air inlet temperature of a fluidized bed to be 50 ℃, the air quantity to be 80m < 3 >/h and the atomization pressure to be 0.5Mpa until all the protective layer is sprayed on enzyme particles.
The particles prepared as described above are designated particle 1.
Example 2 Complex enzyme preparation particle and method for preparing the same
The composition and preparation method of the compound enzyme granule are the same as those of the enzyme of the example 1, except that no stabilizer is added. A complex enzyme pellet was prepared as described above and designated pellet 2.
Example 3 Complex enzyme preparation particle and method for preparing the same
The composition and preparation method of the compound enzyme granule are the same as those of the enzyme of the example 1, except that all enzymes are not immobilized. A complex enzyme pellet was prepared as described above and designated pellet 3.
Example 4 Complex enzyme preparation particle and method for preparing the same
The composition and preparation method of the compound enzyme granule are the same as those of the enzyme of the example 1, except that no auxiliary agent is sprayed. A complex enzyme pellet was prepared as described above and designated pellet 4.
Example 5A Complex enzyme preparation and method for preparing the same
Alkaline protease, alkaline pectase, alkaline lipase, neutral cellulase, xylanase, laccase, amylase and mannanase are weighed according to the composite granular enzyme components in the embodiment 1, and are uniformly mixed. And taking 5 enzyme powders at different positions, detecting enzyme activities, ensuring that the difference of detection values of the same enzyme activity at different positions is less than 2.0%, regarding the enzyme powders as uniform mixing, and ending uniform mixing operation.
Example 6 comparison of different Complex enzymes
The enzyme complex of examples 1 to 5 was stored in an incubator at 40℃and 30 to 40% humidity for 1 month, and the activity was measured, and the enzyme activity retention rate was calculated with the enzyme activity in the non-stored product being 100%.
Example 7 comparison of different Complex enzymes
The complex enzymes of examples 1-5 were weighed, placed in self-sealing bags of the same type, put in a shaker, shaken for 1 hour at 100 rpm, taken out, and the complex enzymes of the same mass were weighed from the same place to measure the activity, and the enzyme mixing uniformity was calculated with the enzyme activity in the product without shaking being 100%.
Example 8 comparison of different Complex enzymes
Weighing the compound enzyme of examples 1-5, adding into 9 times of buffer with pH of 9.0, detecting enzyme activity after dissolution, taking the enzyme activity as initial enzyme activity, incubating at 40 ℃, detecting solution activity during incubation, and calculating the time for enzyme activity to remain 50%.
Example 9 calculation
The enzyme activity detection criteria in this example are referred to as alkaline protease detection criteria GB/T23527.1, alkaline lipase activity detection criteria GB/T2583, neutral cellulase detection criteria QB/T2583, pectinase detection criteria QB/T4482, and in this example, a portion of the enzymes are selected as the evaluation subjects for the activity detection.
Enzyme activity retention = remaining enzyme activity after treatment ≡initial enzyme activity before treatment × 100%
Enzyme component mixing uniformity= (1- | enzyme activity after shaking-enzyme activity before shaking|/enzyme activity before shaking) ×100%
EXAMPLE 6 enzyme Activity survival
EXAMPLE 7 uniformity of mixing of enzyme Components
Example 8 half-life of enzyme component
In summary, compared with powder, the composite enzyme granule prepared by the invention has the advantages that the retention rate of enzyme activity is improved by 20-30%, the mixing uniformity of enzyme components is improved, the mixing uniformity of the enzyme components is improved and is unchanged after the enzyme components are shaken outside, the mixing uniformity of the composite enzyme powder is reduced by 20%, the stress resistance of the composite enzyme granule in the use process is improved, the composite enzyme granule is preserved under the same test condition, the half-life period of the enzyme is prolonged by 30-50%, and in addition, obviously, the dust and labor intensity in the use process and the influence of human factors on production are reduced, the automation of industrial production is promoted, and the stability of the production process is improved to improve the product quality.

Claims (8)

1.一种复合酶颗粒,其特征在于,所述酶颗粒包括酶丸芯和助剂层,所述酶丸芯作为芯部,助剂层涂覆在酶丸芯的外层,所述酶丸芯包含酶组分和稳定剂;1. A composite enzyme granule, characterized in that the enzyme granule comprises an enzyme pellet core and an auxiliary agent layer, wherein the enzyme pellet core serves as a core, the auxiliary agent layer is coated on an outer layer of the enzyme pellet core, and the enzyme pellet core comprises an enzyme component and a stabilizer; 所述酶丸芯和助剂层的重量份数比为4:1;The weight ratio of the enzyme pellet core to the auxiliary agent layer is 4:1; 所述酶丸芯中酶组分和稳定剂的重量份数比为40-85:10-40。The weight ratio of the enzyme component to the stabilizer in the enzyme pellet core is 40-85:10-40. 2.如权利要求1所述的一种复合酶颗粒,其特征在于,所述酶组分选自以下酶种类中的2种或多种:碱性蛋白酶、碱性果胶酶、碱性脂肪酶、中性纤维素酶、木聚糖酶、漆酶、淀粉酶和甘露聚糖酶;2. A composite enzyme granule according to claim 1, characterized in that the enzyme component is selected from two or more of the following enzyme types: alkaline protease, alkaline pectinase, alkaline lipase, neutral cellulase, xylanase, laccase, amylase and mannanase; 所述稳定剂选自如下组份中的2种或多种:山梨醇、葡萄糖、糊精、海藻糖、甘露醇、氯化钙、硫酸铜,硫酸锌;The stabilizer is selected from two or more of the following components: sorbitol, glucose, dextrin, trehalose, mannitol, calcium chloride, copper sulfate, zinc sulfate; 所述助剂层包含以下组分中的一种或多种:聚乙二醇、烷基磺酸钠、烷基酚聚氧乙烯醚、脂肪醇聚氧乙烯醚、吐温。The auxiliary agent layer comprises one or more of the following components: polyethylene glycol, sodium alkyl sulfonate, alkylphenol polyoxyethylene ether, fatty alcohol polyoxyethylene ether, and Tween. 3.如权利要求2所述的一种复合酶颗粒,其特征在于,所述酶组分含如下重量份数的组分:碱性蛋白酶1-5份、碱性果胶酶10-20份、碱性脂肪酶6-10份、中性纤维素酶30-40份、木聚糖酶20-30份、漆酶5-10份、淀粉酶5-10份、甘露聚糖酶2-5份;3. A composite enzyme granule as claimed in claim 2, characterized in that the enzyme component contains the following components in parts by weight: 1-5 parts of alkaline protease, 10-20 parts of alkaline pectinase, 6-10 parts of alkaline lipase, 30-40 parts of neutral cellulase, 20-30 parts of xylanase, 5-10 parts of laccase, 5-10 parts of amylase, and 2-5 parts of mannanase; 所述稳定剂包含如下重量份数的组分:山梨醇30-40份,糊精35-40份,海藻糖20-25份,氯化钙4.5-6份、硫酸铜0.3-0.5份;The stabilizer comprises the following components in parts by weight: 30-40 parts of sorbitol, 35-40 parts of dextrin, 20-25 parts of trehalose, 4.5-6 parts of calcium chloride, and 0.3-0.5 parts of copper sulfate; 所述助剂层包含如下重量份数的组分:C12-C14脂肪醇聚氧乙烯醚 60份、聚乙二醇1000 30份,烷基酚聚氧乙烯醚 10份。The auxiliary agent layer comprises the following components in parts by weight: 60 parts of C12-C14 fatty alcohol polyoxyethylene ether, 30 parts of polyethylene glycol 1000, and 10 parts of alkylphenol polyoxyethylene ether. 4.权利要求1所述复合酶颗粒的制备方法,其特征在于,所述制备方法包括酶的固定化处理、酶丸芯的制备和助剂层的添加;具体包含如下步骤:4. The method for preparing the composite enzyme granules according to claim 1, characterized in that the method comprises enzyme immobilization treatment, enzyme pellet core preparation and additive layer addition; specifically comprises the following steps: (1)酶的固定化处理:取酶丸芯的酶组分中的全部或部分进行固定化;(1) Enzyme immobilization treatment: all or part of the enzyme components in the enzyme pellet core are immobilized; (2)酶丸芯制备:(2) Preparation of enzyme pellet core: 将酶丸芯中所有酶组分和稳定剂按照40-85:10-40重量比例混合得混合物,再根据混合物:微晶纤维素崩解剂重量比例90-95:5-10加入微晶纤维素崩解剂并混合均匀后,采用湿法旋转挤出制粒方法制备湿的酶丸芯,之后将湿的酶丸芯置于流化床内干燥;All enzyme components and stabilizers in the enzyme pellet core are mixed in a weight ratio of 40-85:10-40 to obtain a mixture, and then microcrystalline cellulose disintegrant is added in a weight ratio of 90-95:5-10 of the mixture: microcrystalline cellulose disintegrant and mixed evenly, and wet enzyme pellet cores are prepared by a wet rotary extrusion granulation method, and then the wet enzyme pellet cores are placed in a fluidized bed for drying; (3)助剂层的添加:(3) Addition of auxiliary agent layer: 按酶丸芯和助剂重量比4:1比例称取助剂,倒入油浴锅,加热至90-110℃使其熔化;Weigh the additives in a ratio of 4:1 between the enzyme pellets and the additives, pour into an oil bath, and heat to 90-110°C to melt; 将干燥的酶颗粒芯倒入流化床,将上述热溶解后的助剂用蠕动泵全部喷涂到酶丸芯上,即得复合酶颗粒。The dried enzyme granule cores are poured into a fluidized bed, and the heat-dissolved additives are sprayed onto the enzyme granule cores using a peristaltic pump to obtain composite enzyme granules. 5.如权利要求4所述的复合酶颗粒的制备方法,其特征在于,按复合酶颗粒与保护层重量比9:1,在助剂层外喷涂一层保护层,所述保护层包含以下重量份数的组分:20份CMC、30份微晶纤维素和50份碳酸钙、400份水。5. The method for preparing the composite enzyme granules as claimed in claim 4, characterized in that a protective layer is sprayed on the outside of the auxiliary agent layer at a weight ratio of the composite enzyme granules to the protective layer of 9:1, and the protective layer comprises the following components in parts by weight: 20 parts of CMC, 30 parts of microcrystalline cellulose, 50 parts of calcium carbonate, and 400 parts of water. 6.如权利要求4所述的复合酶颗粒的制备方法,其特征在于,酶丸芯制备过程中,水分和其他物料重量比为1:5-2:5;6. The method for preparing the composite enzyme granules according to claim 4, characterized in that, during the preparation of the enzyme pellet core, the weight ratio of water to other materials is 1:5-2:5; 旋转挤的出物料温度<70℃;The temperature of the material extruded by rotary extrusion is less than 70℃; 选用30目-40目孔网挤出制粒,控制所述挤出条的直径为0.3-0.5mm;Use 30-40 mesh mesh for extrusion granulation, and control the diameter of the extruded strip to be 0.3-0.5 mm; 将所述挤出条加入抛丸机,转速40-120rpm,抛丸30秒,控制颗粒为近球形,获得湿的酶丸芯颗粒,直径0.3-0.5mm;The extruded strip is added into a shot blasting machine at a rotation speed of 40-120 rpm, and the shot blasting is performed for 30 seconds to control the particles to be nearly spherical, and wet enzyme pellet core particles are obtained with a diameter of 0.3-0.5 mm; 将所述湿的酶丸芯颗粒置于流化床内进行干燥,进风温度60-70℃,0.3-0.5个真空下干燥至水分<5%。The wet enzyme pellet core particles are placed in a fluidized bed for drying at an inlet air temperature of 60-70° C. and 0.3-0.5 vacuum until the moisture content is less than 5%. 7.如权利要求4所述的复合酶颗粒的制备方法,其特征在于,助剂层的添加过程中,将干燥的酶丸芯倒入流化床,控制流化床进风温度15℃-25℃,风量60 m³/h-170m³/h,将热溶解后的助剂用蠕动泵,雾化压力0.3-0.4Mpa,全部喷涂到酶丸芯上,即得复合酶颗粒。7. The method for preparing the composite enzyme granules as claimed in claim 4 is characterized in that, during the process of adding the auxiliary agent layer, the dried enzyme pellet cores are poured into the fluidized bed, the air inlet temperature of the fluidized bed is controlled at 15°C-25°C, and the air volume is 60 m³/h-170 m³/h, and the heat-dissolved auxiliary agent is sprayed onto the enzyme pellet core using a peristaltic pump with an atomization pressure of 0.3-0.4 MPa to obtain the composite enzyme granules. 8.如权利要求5所述的复合酶颗粒的制备方法,其特征在于,所述保护层喷涂方法如下:控制流化床进风温度40-60℃,风量60m³/h-170m³/h,雾化压力0.5-0.7Mpa,直至保护层全部喷涂到酶颗粒上。8. The method for preparing the composite enzyme granules according to claim 5, characterized in that the protective layer spraying method is as follows: controlling the fluidized bed air inlet temperature at 40-60°C, the air volume at 60m³/h-170m³/h, and the atomization pressure at 0.5-0.7Mpa until the protective layer is completely sprayed onto the enzyme granules.
CN202411749330.0A 2024-12-02 2024-12-02 Biological compound enzyme preparation and preparation method thereof Pending CN119614547A (en)

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