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CN108588150A - Batch feeding-oxidation pre-treatment auxiliary enzymes hydrolyzing chitosan prepares chitosan oligosaccharide method - Google Patents

Batch feeding-oxidation pre-treatment auxiliary enzymes hydrolyzing chitosan prepares chitosan oligosaccharide method Download PDF

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CN108588150A
CN108588150A CN201810388841.2A CN201810388841A CN108588150A CN 108588150 A CN108588150 A CN 108588150A CN 201810388841 A CN201810388841 A CN 201810388841A CN 108588150 A CN108588150 A CN 108588150A
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chitosan
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刘健
李蒙
龙敏南
甘礼惠
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Xiamen University
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Abstract

Batch feeding oxidation pre-treatment auxiliary enzymes hydrolyzing chitosan prepares chitosan oligosaccharide method, is related to the preparation method of low-molecular weight chitoglycan.The batch feeding oxidative degradation of chitosan pre-processes, and obtains degradation solution;Hydrogen peroxide removes;The enzymatic hydrolysis of chitosan inhibits with side reaction;Product detaches and drying, obtains chitosan oligosaccharide.Concentration of substrate in degradation of chitosan system is improved by batch feeding mode in oxidation pre-treatment, initial hydrolysis is realized, so that chitosan is further hydrolyzed eventually by the effect of enzyme.With the highly concentrated Hydrolyze method of chitosan of early development comparatively, preprocess method has equipment simple, adaptable, it is easy to be combined with technologies such as enzyme mebrane reactor, immobilised enzymes, has larger application prospect in terms of the chitosan oligosaccharide of preparation Narrow Molecular Weight Distribution.

Description

分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法Method for preparing chitooligosaccharides by fed-batch-oxidative pretreatment-assisted enzymatic hydrolysis of chitosan

技术领域technical field

本发明涉及低分子量壳聚糖的制备方法,尤其是涉及分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖的方法。The invention relates to a preparation method of low-molecular-weight chitosan, in particular to a method for preparing chitosan oligosaccharide by fed-batch-oxidation pretreatment assisting enzyme hydrolysis of chitosan.

背景技术Background technique

壳聚糖是由氨基葡萄糖和乙酰氨基葡萄糖通过β-1,4糖苷键连接而成线性大分子,分子量从几十万到几百万不等,是自然界中唯一天然存在的带正电荷的聚糖,在中性和碱性溶液中不溶,也不能溶解在有机溶剂中,虽然在酸性水溶液中可溶,但是溶解度有限,而且粘度极高,严重影响壳聚糖的应用。低分子量壳聚糖是壳聚糖的不完全水解产物,保留有壳聚糖的吸附特性、正电荷特性、还原性以及碱性等基本特性,同时又具有溶解性好、粘度低、生物活性高等优点,尤其是壳寡糖在抗肿瘤药物和提高免疫力方面的潜在应用引起国内外研究者的广泛关注。低分子量壳聚糖作为一种功能性糖,在农业、医药、功能性食品、材料等领域均有广阔的应用前景。Chitosan is a linear macromolecule formed by connecting glucosamine and acetylglucosamine through β-1,4 glycosidic bonds. Its molecular weight ranges from hundreds of thousands to millions. It is the only naturally occurring positively charged polymer in nature. Sugar is insoluble in neutral and alkaline solutions, and cannot be dissolved in organic solvents. Although it is soluble in acidic aqueous solutions, its solubility is limited and its viscosity is extremely high, which seriously affects the application of chitosan. Low-molecular-weight chitosan is an incomplete hydrolysis product of chitosan, which retains the basic properties of chitosan such as adsorption, positive charge, reduction and alkalinity, and has good solubility, low viscosity, and high biological activity. The advantages, especially the potential application of chitosan oligosaccharides in antitumor drugs and improving immunity have attracted extensive attention of researchers at home and abroad. As a functional sugar, low molecular weight chitosan has broad application prospects in agriculture, medicine, functional food, materials and other fields.

壳聚糖的降解方法主要有物理法、化学法、酶法和各种联合水解法。物理法如常用的γ辐射法在降解过程容易发生壳聚糖交联和歧化副反应,影响进一步降解,而且大型辐射设备增加了生产成本。化学法是利用强酸或者氧化剂破坏β-1,4糖苷键实现水解,该法价格低廉,尤其是以双氧水为氧化剂的氧化降解工艺具有无残毒、清洁、高效等优势。但是通过化学法制备壳寡糖也存在很大的弊端。如酸水解法水解过程难以控制,产物主要是单糖和二糖等生物活性较低的产物,而且大量的酸对后期产物的纯化和废液处理不利;双氧水氧化降解壳聚糖对于制备分子量高于10000的低分子量壳聚糖较为有利,而进一步降解存在产物“过氧化”问题,即产物结构发生明显变化,因此仅仅通过化学法很难获得低聚壳聚糖。酶法是一种温和的方法,尤其是专一性的壳聚糖酶能够生产几乎不含单糖的寡糖产品。但是专一性酶制剂成本高,热稳定性差,难以大规模应用;另外,壳聚糖溶液的高粘度极大阻碍了酶分子与壳聚糖大分子的碰撞,不利于酶的有效剪切。实验证实,当壳聚糖浓度高于5%(质量体积比)时,壳聚糖溶解缓慢,难以形成均一体系,而且粘度极高,分散性极差。壳聚糖的低浓度水解导致能耗、水耗高,设备利用率低,后处理麻烦等。因此,壳聚糖降解体系的低浓度、高粘度仍然是阻碍低分子量壳聚糖高效生产的最大瓶颈。中国专利201010172203.0公开一种快速溶解壳聚糖、以高底物浓度酶法制备壳寡糖的方法,采用高速剪切分散机辅助溶解壳聚糖,通过逐步添加壳聚糖、醋酸和水解酶的方式使壳聚糖降解体系中底物终浓度达到10%~20%。但这种方法需要使用高速分散设备可能影响酶的活性,另外,降解过程持续的高粘度体系不利于酶分子构象的转换以及分子扩散,因此该工艺对酶活性和用量要求较高(20~80U/g),生产成本较高。The degradation methods of chitosan mainly include physical method, chemical method, enzymatic method and various combined hydrolysis methods. Physical methods such as the commonly used gamma radiation method are prone to chitosan cross-linking and disproportionation side reactions during the degradation process, affecting further degradation, and large-scale radiation equipment increases production costs. The chemical method is to use strong acid or oxidant to destroy the β-1,4 glycosidic bond to achieve hydrolysis. This method is cheap, especially the oxidative degradation process using hydrogen peroxide as the oxidant has the advantages of no residue, cleanliness, and high efficiency. However, the preparation of chitosan oligosaccharides by chemical methods also has great disadvantages. For example, the acid hydrolysis process is difficult to control, and the products are mainly products with low biological activity such as monosaccharides and disaccharides, and a large amount of acid is unfavorable to the purification of later products and waste liquid treatment; hydrogen peroxide oxidative degradation of chitosan is very important for the preparation of high molecular weight Chitosan with a low molecular weight of more than 10000 is more favorable, and further degradation has the problem of "peroxidation" of the product, that is, the structure of the product changes significantly, so it is difficult to obtain low-molecular-weight chitosan only by chemical methods. The enzymatic method is a mild method, especially the specific chitosanase can produce oligosaccharide products with almost no monosaccharides. However, the high cost of specific enzyme preparations and poor thermal stability make it difficult to apply on a large scale. In addition, the high viscosity of chitosan solution greatly hinders the collision between enzyme molecules and chitosan macromolecules, which is not conducive to the effective shearing of enzymes. Experiments have proved that when the concentration of chitosan is higher than 5% (mass volume ratio), chitosan dissolves slowly, it is difficult to form a uniform system, and the viscosity is extremely high, and the dispersibility is extremely poor. The low-concentration hydrolysis of chitosan leads to high energy consumption, high water consumption, low utilization rate of equipment, troublesome post-processing, etc. Therefore, the low concentration and high viscosity of the chitosan degradation system are still the biggest bottlenecks hindering the efficient production of low molecular weight chitosan. Chinese patent 201010172203.0 discloses a method for quickly dissolving chitosan and preparing chitosan oligosaccharides with high substrate concentration enzymatically, using a high-speed shearing disperser to assist in dissolving chitosan, and gradually adding chitosan, acetic acid and hydrolase The method is to make the final concentration of the substrate in the chitosan degradation system reach 10%-20%. However, this method requires the use of high-speed dispersing equipment, which may affect the activity of the enzyme. In addition, the continuous high-viscosity system during the degradation process is not conducive to the conversion of the enzyme molecular conformation and molecular diffusion, so this process requires high enzyme activity and dosage (20 ~ 80U /g), the production cost is higher.

发明内容Contents of the invention

本发明的目的在于可克服现有壳寡糖生产技术中存在粘度高、底物浓度低、生产效率低等不足,提供分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖的方法。The purpose of the present invention is to overcome the deficiencies such as high viscosity, low substrate concentration and low production efficiency in the existing chitosan oligosaccharide production technology, and provide fed-batch-oxidative pretreatment auxiliary enzyme hydrolysis chitosan to prepare chitosan oligosaccharide method.

本发明包括以下步骤:The present invention comprises the following steps:

1)壳聚糖的分批补料-氧化降解预处理,得降解液;1) Fed-batch-oxidative degradation pretreatment of chitosan to obtain a degradation solution;

在步骤1)中,所述壳聚糖的分批补料-氧化降解预处理的方法可为:将壳聚糖粉末分散于水中,加入酸溶解,再加入双氧水反应,分批补加酸和壳聚糖,直到壳聚糖浓度达到6%~30%;所述将壳聚糖粉末分散于水中,按质量体积比将壳聚糖粉末分散于25~50倍水中,其中壳聚糖粉末按质量计算,水按体积计算;所述加入酸溶解可按照0.25~0.35mL酸/g壳聚糖;所述双氧水可加入质量终浓度可为0.5%~10%;所述反应的温度可为40~70℃;所述预处理的时间可为10~60min;所述酸可采用醋酸;所述分批补加酸和壳聚糖,可每次补加的壳聚糖量不超过壳聚糖的初始加入量,每次补料时间间隔为5~10min,使壳聚糖最终浓度达到6%~30%;氧化降解结束后,利用过氧化氢酶脱除体系中的双氧水直至淀粉-碘化钾试纸不变蓝,过氧化氢酶用量为0.0015~0.003g/mL。In step 1), the method of fed-batch-oxidative degradation pretreatment of described chitosan can be: chitosan powder is dispersed in water, add acid to dissolve, then add hydrogen peroxide reaction, add acid and batchwise Chitosan until the chitosan concentration reaches 6% to 30%; the chitosan powder is dispersed in water, and the chitosan powder is dispersed in 25 to 50 times the water according to the mass volume ratio, wherein the chitosan powder is Calculated by mass, water is calculated by volume; the addition of acid can be dissolved according to 0.25~0.35mL acid/g chitosan; the mass final concentration of the hydrogen peroxide can be added and can be 0.5%~10%; the temperature of the reaction can be 40 ~70°C; the time of the pretreatment can be 10 ~ 60min; the acid can be acetic acid; the addition of acid and chitosan in batches, the amount of chitosan that can be added each time does not exceed the amount of chitosan The initial addition amount is 5-10 minutes each time, so that the final concentration of chitosan reaches 6%-30%. No blue, the amount of catalase is 0.0015 ~ 0.003g/mL.

2)双氧水脱除;2) hydrogen peroxide removal;

在步骤2)中,所述双氧水脱除的方法可为:在步骤1)所得降解液中添加过氧化氢酶脱除残余双氧水,用量为0.0015~0.003g/mL预处理液,直至液体不能使KI-淀粉试纸变蓝。In step 2), the method for removing hydrogen peroxide can be: add catalase to the degradation solution obtained in step 1) to remove residual hydrogen peroxide, and the dosage is 0.0015-0.003g/mL pretreatment solution until the liquid cannot be used KI-starch test paper turns blue.

3)壳聚糖的酶法水解与副反应抑制;3) enzymatic hydrolysis and side reaction inhibition of chitosan;

在步骤3)中,所述壳聚糖的酶法水解与副反应抑制的方法可为:用氨水、氢氧化钠或氢氧化钾溶液中的一种调整步骤2)所得液体pH值4~6,按照壳聚糖质量的1%~20%添加壳聚糖水解酶,酶解过程通过添加亚硫酸氢钠、亚硫酸钠、焦亚硫酸钠等中的一种抑制褐变反应,抑制剂的用量为0.05~0.15g/g壳聚糖,反应温度40~60℃,反应时间4~24h,直至所需分子量;所述氨水、氢氧化钠或氢氧化钾溶液可采用质量浓度为5~10M;所述酶包括壳聚糖酶、纤维素酶、半纤维素酶等中的一种。In step 3), the enzymatic hydrolysis of chitosan and side reaction inhibition can be: use one of ammonia water, sodium hydroxide or potassium hydroxide solution to adjust the pH value of the liquid obtained in step 2) to 4-6 , adding chitosan hydrolase according to 1% to 20% of the mass of chitosan, and adding one of sodium bisulfite, sodium sulfite, sodium pyrosulfite, etc. during the enzymolysis process to inhibit the browning reaction, and the dosage of the inhibitor is 0.05- 0.15g/g chitosan, the reaction temperature is 40-60°C, the reaction time is 4-24h, until the required molecular weight; the ammonia water, sodium hydroxide or potassium hydroxide solution can be used with a mass concentration of 5-10M; the enzyme Including one of chitosanase, cellulase, hemicellulase and the like.

4)产物分离与干燥,得壳寡糖。4) The product is separated and dried to obtain chitosan oligosaccharide.

在步骤4)中,所述产物分离与干燥的方法可为:用氨水、氢氧化钠或氢氧化钾溶液中的一种调整步骤3)所得液体pH值至7,利用10~20kDa超滤膜脱除酶,干燥后获得壳寡糖,所述壳寡糖为浅黄色壳寡糖产品,壳聚糖脱乙酰度为80%~100%;所述干燥可采用喷雾干燥、冷冻干燥、真空干燥等中的一种。In step 4), the method for separating and drying the product can be: adjust the pH value of the liquid obtained in step 3) to 7 with one of ammonia water, sodium hydroxide or potassium hydroxide solution, and use a 10-20kDa ultrafiltration membrane Remove the enzyme, and obtain chitosan oligosaccharide after drying, the chitosan oligosaccharide is a light yellow chitosan product, and the deacetylation degree of chitosan is 80% to 100%; the drying can be spray drying, freeze drying, vacuum drying One of a kind.

本发明在氧化预处理过程中通过分批补料方式提高壳聚糖降解体系中底物浓度,实现初步水解,最终通过酶的作用使壳聚糖进一步水解。与前期开发的壳聚糖高浓水解法比较而言,本发明涉及到的预处理方法具有设备简单、适应性强,易于与酶膜反应器、固定化酶等技术相结合,在制备窄分子量分布的壳寡糖方面有较大的应用前景。本发明内容对壳寡糖的高效、绿色生产具有重要意义。The present invention increases the substrate concentration in the chitosan degradation system by feeding batches in the oxidation pretreatment process, realizes preliminary hydrolysis, and finally further hydrolyzes the chitosan through the action of enzymes. Compared with the high-concentration chitosan hydrolysis method developed in the early stage, the pretreatment method involved in the present invention has simple equipment, strong adaptability, and is easy to combine with technologies such as enzyme membrane reactors and immobilized enzymes. The distribution of chitosan oligosaccharides has great application prospects. The content of the present invention is of great significance to the high-efficiency and green production of chitosan oligosaccharides.

本发明具有以下优点:The present invention has the following advantages:

1)分批补料氧化预处理法降粘、增浓效果好,方法适应性强,易于与酶膜反应器、酶的固定化技术进行耦合,在制备窄分子量分布的壳寡糖方面有较大的应用前景;1) The fed-batch oxidation pretreatment method has a good effect of reducing viscosity and increasing concentration, and the method has strong adaptability, and is easy to be coupled with enzyme membrane reactor and enzyme immobilization technology. Great application prospects;

2)该方法使用的化学试剂少,污染少,产物安全性高,符合绿色化学生产理念;2) The method uses less chemical reagents, less pollution, high product safety, and conforms to the concept of green chemical production;

3)整个降解体系反应条件温和,反应设备简单,易于扩大生产。3) The reaction conditions of the entire degradation system are mild, the reaction equipment is simple, and it is easy to expand production.

附图说明Description of drawings

图1为本发明实施例所得壳聚糖经过氧化-酶法降解后产物分子量分布情况。在图1中,(a)为6%壳聚糖;(b)为9%壳聚糖。Fig. 1 is the product molecular weight distribution situation of chitosan obtained in the embodiment of the present invention after oxidation-enzymatic degradation. In Figure 1, (a) is 6% chitosan; (b) is 9% chitosan.

具体实施方式Detailed ways

以下实施例将结合附图对本发明的具体实施方式进行详细说明。The following embodiments will describe the specific implementation manners of the present invention in detail in conjunction with the accompanying drawings.

实施例1Example 1

3g壳聚糖均匀分散在96mL水中,加入1mL冰醋酸,室温下搅拌溶解,再添加4mL30%双氧水,于60℃下搅拌反应5min,迅速补加1mL冰醋酸和3g壳聚糖,控制预处理总时间1h,添加0.2g过氧化氢酶脱除双氧水,用浓氨水调节pH值,加入5g纤维素酶,于55℃摇床反应12h,获得的降解液用氨水调节pH值为7,利用10kDa超滤膜脱除酶,滤液通过真空冷冻干燥获得浅黄色壳寡糖产品,其中能够溶解于75%乙醇的壳寡糖得率达到90%。对产品进行薄层层析鉴定,见图1(a),S为标准品,1~4分别为同样的样品重复4次。标准品由上至下7个点分别为GlcN:氨基葡萄糖;(GlcN)2:壳二糖;(GlcN)3:壳三糖;(GlcN)4:壳四糖;(GlcN)5:壳五糖;(GlcN)6:壳六糖;(GlcN)7:壳七糖。3g of chitosan was uniformly dispersed in 96mL of water, 1mL of glacial acetic acid was added, stirred and dissolved at room temperature, then 4mL of 30% hydrogen peroxide was added, stirred and reacted at 60°C for 5min, and 1mL of glacial acetic acid and 3g of chitosan were added quickly to control the total amount of pretreatment. For 1 hour, add 0.2 g of catalase to remove hydrogen peroxide, adjust the pH value with concentrated ammonia water, add 5 g of cellulase, and react in a shaking table at 55 °C for 12 hours, adjust the pH value of the obtained degradation solution to 7 with ammonia water, and use a 10 kDa super The filter membrane removes the enzyme, and the filtrate is vacuum freeze-dried to obtain light yellow chitosan oligosaccharide products, wherein the yield of chitosan oligosaccharides that can be dissolved in 75% ethanol reaches 90%. The product was identified by TLC, as shown in Figure 1(a), S is the standard product, and 1-4 are the same samples repeated 4 times. The seven points of the standard from top to bottom are GlcN: glucosamine; (GlcN) 2 : chitobiose; (GlcN) 3 : chitotriose; (GlcN) 4 : chitotetraose; (GlcN) 5 : chitopentose sugar; (GlcN) 6 : Chitohexaose; (GlcN) 7 : Chitoheptaose.

实施例2Example 2

按照实施例1,在预处理第5和15min分别补加1mL冰醋酸和3g壳聚糖,控制预处理总时间0.5h,添加0.2g过氧化氢酶脱除双氧水,用浓氨水调节pH值,加入5g纤维素酶,于55℃摇床反应6h,产物在pH7~14条件下均可以溶解,继续反应至12h,获得的降解液用氨水调节pH值为7,利用10kDa超滤膜脱除酶,滤液通过真空冷冻干燥获得浅黄色壳寡糖产品,其中能够溶解于75%乙醇的壳寡糖得率达到70%。对产品进行薄层层析鉴定,见图1(b)。S为标准品;5~8分别为同样的样品重复4次。标准品由上至下7个点分别为GlcN:氨基葡萄糖;(GlcN)2:壳二糖;(GlcN)3:壳三糖;(GlcN)4:壳四糖;(GlcN)5:壳五糖;(GlcN)6:壳六糖;(GlcN)7:壳七糖。According to embodiment 1, add 1mL glacial acetic acid and 3g chitosan respectively at the 5th and 15min of pretreatment, control pretreatment total time 0.5h, add 0.2g catalase to remove hydrogen peroxide, adjust pH value with concentrated ammonia water, Add 5g of cellulase and react on a shaker at 55°C for 6 hours. The product can be dissolved under the condition of pH 7-14. Continue to react for 12 hours. Use ammonia water to adjust the pH value of the obtained degradation solution to 7, and use a 10kDa ultrafiltration membrane to remove the enzyme. , the filtrate was vacuum freeze-dried to obtain light yellow chitosan oligosaccharide products, wherein the yield of chitosan oligosaccharides that could be dissolved in 75% ethanol reached 70%. The product was identified by thin-layer chromatography, as shown in Figure 1(b). S is the standard; 5-8 are the same samples repeated 4 times. The seven points of the standard from top to bottom are GlcN: glucosamine; (GlcN) 2 : chitobiose; (GlcN) 3 : chitotriose; (GlcN) 4 : chitotetraose; (GlcN) 5 : chitopentose sugar; (GlcN) 6 : Chitohexaose; (GlcN) 7 : Chitoheptaose.

实施例3Example 3

按照实施例2,酶解时加入1.2g NaHSO3,酶解12h,得到几乎纯白色的壳寡糖,其中能够溶解于75%乙醇的壳寡糖得率达到48%。According to Example 2, 1.2 g of NaHSO 3 was added during enzymatic hydrolysis for 12 hours to obtain almost pure white chitosan oligosaccharides, wherein the yield of chitosan oligosaccharides soluble in 75% ethanol reached 48%.

Claims (10)

1.分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于包括以下步骤:1. Fed-batch-oxidative pretreatment assisted enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that comprising the following steps: 1)壳聚糖的分批补料-氧化降解预处理,得降解液;1) Fed-batch-oxidative degradation pretreatment of chitosan to obtain a degradation solution; 2)双氧水脱除;2) hydrogen peroxide removal; 3)壳聚糖的酶法水解与副反应抑制;3) enzymatic hydrolysis and side reaction inhibition of chitosan; 4)产物分离与干燥,得壳寡糖。4) The product is separated and dried to obtain chitosan oligosaccharide. 2.如权利要求1所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于在步骤1)中,所述壳聚糖的分批补料-氧化降解预处理的方法为:将壳聚糖粉末分散于水中,加入酸溶解,再加入双氧水反应,分批补加酸和壳聚糖,直到壳聚糖浓度达到6%~30%。2. fed-batch-oxidative pretreatment auxiliary enzyme hydrolysis chitosan as claimed in claim 1 prepares chitosan oligosaccharide method, it is characterized in that in step 1) in, the fed-batch-oxidative degradation of described chitosan The pretreatment method is as follows: disperse chitosan powder in water, add acid to dissolve, then add hydrogen peroxide to react, add acid and chitosan in batches until the concentration of chitosan reaches 6%-30%. 3.如权利要求2所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于所述将壳聚糖粉末分散于水中,按质量体积比将壳聚糖粉末分散于25~50倍水中,其中壳聚糖粉末按质量计算,水按体积计算。3. fed batches as claimed in claim 2-oxidative pretreatment auxiliary enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that described chitosan powder is dispersed in water, by mass volume ratio chitosan The powder is dispersed in 25-50 times of water, wherein the chitosan powder is calculated by mass, and the water is calculated by volume. 4.如权利要求2所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于所述加入酸溶解是按照0.25~0.35mL酸/g壳聚糖;所述双氧水是加入质量终浓度为0.5%~10%;所述反应的温度为40~70℃;所述预处理的时间为10~60min。4. fed batches as claimed in claim 2-oxidative pretreatment auxiliary enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that described adding acid dissolution is according to 0.25~0.35mL acid/g chitosan; The hydrogen peroxide is added with a final mass concentration of 0.5%-10%; the reaction temperature is 40-70° C.; the pretreatment time is 10-60 minutes. 5.如权利要求2所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于所述酸采用醋酸;所述分批补加酸和壳聚糖,是每次补加的壳聚糖量不超过壳聚糖的初始加入量,每次补料时间间隔为5~10min,使壳聚糖最终浓度达到6%~30%;氧化降解结束后,利用过氧化氢酶脱除体系中的双氧水直至淀粉-碘化钾试纸不变蓝,过氧化氢酶用量为0.0015~0.003g/mL。5. fed batches as claimed in claim 2-oxidative pretreatment auxiliary enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that described acid adopts acetic acid; Described adding acid and chitosan in batches, is The amount of chitosan added each time does not exceed the initial amount of chitosan added, and the time interval between each feeding is 5 to 10 minutes, so that the final concentration of chitosan reaches 6% to 30%; Remove the hydrogen peroxide in the system with catalase until the starch-potassium iodide test paper does not turn blue, and the dosage of catalase is 0.0015-0.003g/mL. 6.如权利要求1所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于在步骤2)中,所述双氧水脱除的方法为:在步骤1)所得降解液中添加过氧化氢酶脱除残余双氧水,用量为0.0015~0.003g/mL预处理液,直至液体不能使KI-淀粉试纸变蓝。6. fed batches as claimed in claim 1-oxidative pretreatment auxiliary enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that in step 2) in, the method that described hydrogen peroxide removes is: in step 1) Add catalase to the obtained degradation liquid to remove residual hydrogen peroxide, and the dosage is 0.0015-0.003 g/mL pretreatment liquid until the liquid cannot turn KI-starch test paper blue. 7.如权利要求1所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于在步骤3)中,所述壳聚糖的酶法水解与副反应抑制的方法为:用氨水、氢氧化钠或氢氧化钾溶液中的一种调整步骤2)所得液体pH值4~6,按照壳聚糖质量的1%~20%添加壳聚糖水解酶,酶解过程通过添加亚硫酸氢钠、亚硫酸钠、焦亚硫酸钠中的一种抑制褐变反应,抑制剂的用量为0.05~0.15g/g壳聚糖,反应温度40~60℃,反应时间4~24h,直至所需分子量。7. fed batches as claimed in claim 1-oxidative pretreatment auxiliary enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that in step 3) in, the enzymatic hydrolysis of described chitosan and side reaction inhibition The method is: use one of ammonia water, sodium hydroxide or potassium hydroxide solution to adjust the pH value of the liquid obtained in step 2) to 4 to 6, add chitosan hydrolase according to 1% to 20% of the mass of chitosan, and the enzyme The solution process suppresses the browning reaction by adding one of sodium bisulfite, sodium sulfite and sodium metabisulfite. The dosage of the inhibitor is 0.05~0.15g/g chitosan, the reaction temperature is 40~60°C, and the reaction time is 4~24h. to the desired molecular weight. 8.如权利要求7所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于所述氨水、氢氧化钠或氢氧化钾溶液采用质量浓度为5~10M;所述酶包括壳聚糖酶、纤维素酶、半纤维素酶中的一种。8. fed batches as claimed in claim 7-oxidative pretreatment auxiliary enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that described ammoniacal liquor, sodium hydroxide or potassium hydroxide solution adopt mass concentration to be 5~10M ; The enzyme comprises one of chitosanase, cellulase and hemicellulase. 9.如权利要求1所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于在步骤4)中,所述产物分离与干燥的方法为:用氨水、氢氧化钠或氢氧化钾溶液中的一种调整步骤3)所得液体pH值至7,利用10~20kDa超滤膜脱除酶,干燥后获得壳寡糖。9. fed batches as claimed in claim 1-oxidative pretreatment auxiliary enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that in step 4) in, the method for described product separation and drying is: use ammoniacal liquor, One of sodium hydroxide or potassium hydroxide solution is used to adjust the pH value of the liquid obtained in step 3) to 7, and the enzyme is removed by using a 10-20 kDa ultrafiltration membrane, and the chitosan oligosaccharide is obtained after drying. 10.如权利要求9所述分批补料-氧化预处理辅助酶水解壳聚糖制备壳寡糖方法,其特征在于所述干燥采用喷雾干燥、冷冻干燥、真空干燥中的一种。10. fed batches as claimed in claim 9-oxidative pretreatment auxiliary enzyme hydrolysis chitosan prepares chitosan oligosaccharide method, it is characterized in that described drying adopts the one in spray drying, freeze drying, vacuum drying.
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