WO2020037866A1 - Low molecular weight chitooligosaccharide and preparation method therefor - Google Patents

Low molecular weight chitooligosaccharide and preparation method therefor Download PDF

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WO2020037866A1
WO2020037866A1 PCT/CN2018/118048 CN2018118048W WO2020037866A1 WO 2020037866 A1 WO2020037866 A1 WO 2020037866A1 CN 2018118048 W CN2018118048 W CN 2018118048W WO 2020037866 A1 WO2020037866 A1 WO 2020037866A1
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chitosan
mass
preparing
solution
low
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苏政权
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广东药科大学
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08BPOLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B37/00Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
    • C08B37/0006Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
    • C08B37/0024Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid beta-D-Glucans; (beta-1,3)-D-Glucans, e.g. paramylon, coriolan, sclerotan, pachyman, callose, scleroglucan, schizophyllan, laminaran, lentinan or curdlan; (beta-1,6)-D-Glucans, e.g. pustulan; (beta-1,4)-D-Glucans; (beta-1,3)(beta-1,4)-D-Glucans, e.g. lichenan; Derivatives thereof
    • C08B37/00272-Acetamido-2-deoxy-beta-glucans; Derivatives thereof
    • C08B37/003Chitin, i.e. 2-acetamido-2-deoxy-(beta-1,4)-D-glucan or N-acetyl-beta-1,4-D-glucosamine; Chitosan, i.e. deacetylated product of chitin or (beta-1,4)-D-glucosamine; Derivatives thereof

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  • the invention belongs to the field of oligosaccharide preparation methods, and particularly relates to a low molecular weight chitooligosaccharide and a preparation method thereof.
  • Chitosan is the only positively-charged, alkaline, water-soluble polysaccharide found in nature at present. It has superior biological activity and can be prepared from chitin and chitosan. Chito-oligosaccharides with different molecular weights have different functions. Chito-oligosaccharides with a molecular weight of about 5000 Da have the function of lowering blood lipids. Chito-oligosaccharides with a molecular weight of about 3,000-2000 Da can inhibit the growth and metastasis of tumor cells. Chitooligosaccharides below 1000 Da have unique physiological activities and functions, including enhancing humoral immunity and cellular immunity; promoting calcium absorption and bone health; antibacterial, bacteriostatic, and significant moisture-absorbing capacity.
  • chitosan is mainly produced by enzymatic degradation of chitosan.
  • the enzymatic hydrolysis method has the advantages of specificity, mild reaction conditions, easy control of the process, and less environmental pollution.
  • the commonly used enzymes can be divided into specific enzymes and non-specific enzymes.
  • Specific enzymes have good enzymatic hydrolysis, but they are expensive. Some non-specific enzymes such as papain and bromelain are less expensive.
  • the hydrolysis effect is not good.
  • Chinese Patent Publication No. CN107739418A discloses a method for preparing chitosan oligosaccharides by freeze-drying papain.
  • the method has a short enzymolysis time, the molecular weight of the product is about 3000 Da; China with publication number CN107988287A
  • the patent discloses a method for preparing chitooligosaccharides by spray drying of cellulase. The method uses cheap and easy-to-obtain enzymes, but has problems such as long enzymatic hydrolysis time.
  • Tannase also known as tanninase, is a tannin hydrolase.
  • the enzyme can be produced by molds such as Aspergillus niger and Aspergillus oryzae. At present, it is mainly used for processing tannin and protein in beer to make it clear and transparent. However, its role in enzymatic hydrolysis of chitosan is not mentioned.
  • the object of the present invention is to provide a chitooligosaccharide and a preparation method thereof.
  • the method for preparing chitosan oligosaccharides provided by the present invention has mild conditions, is simple, requires short preparation time, has a high yield of chitosan oligosaccharides with a molecular weight of about 1000 Da, does not need to add a large number of reaction reagents, has less environmental pollution, and uses figs Proteases and tannins are inexpensive and readily available.
  • the technical scheme of the present invention is: a method for preparing a low molecular weight chitooligosaccharide, comprising the following steps:
  • step S2 Add a complex enzyme to the chitosan solution obtained in step S1.
  • the mass ratio of the mass of the complex enzyme to the mass of the chitosan is 2.5 to 25%.
  • the reaction is performed at 65 ° C for 1 to 3 hours to obtain an enzymatic hydrolysis solution.
  • Fig protease and tannin are composed in a weight ratio of 1: (0.1 to 1);
  • step S3 Add 5% NaOH solution with a mass concentration of 5% to the enzymatic hydrolysis solution obtained in step S2 with stirring, adjust the pH to 7.0 to 8.0, filter, and separate the water-insoluble chitosan.
  • the filtrate is placed in a dialysis bag and dialyzed in distilled water. 24h, get dialysate;
  • the dialysate obtained in step S3 is concentrated, concentrated to a concentrated solution having a solid content concentration of 9 to 15%, and spray-dried.
  • the complex enzyme in the step S1 is composed of fig protease and tannin in a weight ratio of 1: 0.3.
  • the pH value of the acetic acid-sodium acetate buffer solution in step S1 is 5.0, and the concentration is 0.2 mol / L.
  • the mass ratio of the mass of the complex enzyme to the mass of chitosan in step S2 is 5-10%.
  • the mass ratio of the mass of the complex enzyme to the mass of chitosan in step S2 is 7.5%.
  • step S2 the reaction is performed at 65 ° C for 2h.
  • the dialysis bag in step S3 is a regenerated cellulose dialysis bag with a molecular weight cut off of 1000 Da.
  • the solid content mass concentration of the spray-dried concentrated liquid in the step S4 is 10%.
  • step S4 the process conditions for spray drying in step S4 are: an inlet air temperature of 180 ° C., and a feed rate of 700 mL / h.
  • the invention uses fig protease and tannin to hydrolyze chitosan, which can obtain more small molecular weight chitosan oligosaccharides with a molecular weight of about 1000 Da in a short period of time, and the average yield can reach 39.47%, which significantly shortens the enzyme. Solution time and reduce costs.
  • fig protease or the tannase is used alone, the same or similar effects as those described above cannot be obtained.
  • the present invention has the following beneficial effects:
  • the method provided by the invention has mild conditions, the complex enzyme used is cheap and easy to obtain, the production cost is low, the time required for preparation is short, and more importantly, the yield of low molecular weight chitooligosaccharide is higher, and significant progress has been achieved compared with the prior art. .
  • Chitosan (batch number: 171112A, DD85%, Shandong Aokang Biotechnology Co., Ltd.); fig protease (Tixi Aihuacheng Industrial Development Co., Ltd.); tannase (Henan Xihe Chemical Co., Ltd.); Sheng Ocean Technology Co., Ltd.); regenerated cellulose dialysis bag (cut-off molecular weight 1000 Da, US MYM Biotechnology Company).
  • step S2 Add a 0.5% complex enzyme solution to the chitosan solution obtained in step S1.
  • the complex enzyme is composed of fig protease and tannin in a weight ratio of 1: 0.3. It was 7.5%, and reacted at 65 ° C for 2h to obtain an enzymatic hydrolysis solution;
  • step S3 Add 5% NaOH solution with a mass concentration of 5% to the enzymatic hydrolysis solution obtained in step S2 under stirring, adjust the pH to 7.0-8.0, filter, separate the water-insoluble chitosan, and fill the filtrate with regeneration with a molecular weight of 1000 Da.
  • dialysis was performed in distilled water for 24 hours to obtain a dialysate;
  • the dialysate obtained in step S3 is concentrated, concentrated to a concentrated solution with a solid content concentration of 10%, and spray-dried.
  • the process conditions for spray-drying are: an inlet air temperature of 180 ° C and a feed rate of 700 mL / h.
  • the complex enzyme solution is prepared from a 0.2 mol / L acetate-sodium acetate buffer solution with a pH value of 5.0.
  • Example 2 The difference between Example 2 and Example 1 is that in step S1, the mass concentration of the chitosan solution is 1.2%, and the mass ratio of the mass of the complex enzyme to the mass of chitosan in step S2 is 5%.
  • the complex enzyme is composed of fig protease and Tannase was composed by a weight ratio of 1: 0.1, and the rest was the same as in Example 1.
  • Example 3 The difference between Example 3 and Example 1 is that in step S1, the mass concentration of the chitosan solution is 1.2%, and the mass ratio of the compound enzyme to the mass of chitosan in step S2 is 7.5%.
  • the compound enzyme is composed of fig protease and Tannase was composed by a weight ratio of 1: 1, and the rest was the same as in Example 1.
  • Example 1 Compared with Example 1, this comparative example is different in that the enzyme used is fig protease, and the rest are the same as in Example 1.
  • Example 1 Compared with Example 1, this comparative example is different in that the enzyme used is tannin, and the rest are the same as in Example 1.
  • Example 1 Compared with Example 1, this comparative example is different in that Tannase is replaced with cellulase, and the rest are the same as in Example 1.
  • Test example one product performance measurement
  • Example 1 5.02 62.71 1.38 39.47%
  • Example 2 5.15 61.03 1.41 37.36%
  • Example 3 5.29 64.69 1.35 38.54%
  • Comparative Example 1 5.18 43.74 1.42 20.06%
  • Comparative Example 2 5.00 30.65 1.43 11.57%
  • Comparative Example 3 5.23 56.53 1.40 25.36% 1000Da Chitosan API 4.96 57.66 1.42 -

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Abstract

A low molecular weight chitooligosaccharide and a preparation method therefor, comprising the steps of dissolving chitosan in an acetate-sodium acetate buffer solution, preparing a chitosan solution, adding a compound enzyme solution into the chitosan solution for enzymatic digestion, dialyzing a filtrate by using dialysis after the completion of enzymatic digestion, concentrating an obtained dialysate and then spray-drying, and so on. The described preparation method has the advantages of the yield of low molecular weight chitooligosaccharide being high, conditions being simple, time required for preparation being short, the enzymes used being cheap and easy to obtain, and production costs being low, thus being suitable for wide-scale promotion and application.

Description

一种低分子量壳寡糖及其制备方法Low molecular weight chitooligosaccharide and preparation method thereof 技术领域Technical field
本发明属于低聚糖制备方法领域,具体涉及一种低分子量壳寡糖及其制备方法。The invention belongs to the field of oligosaccharide preparation methods, and particularly relates to a low molecular weight chitooligosaccharide and a preparation method thereof.
背景技术Background technique
壳寡糖是目前发现的自然界中唯一的带正电荷、呈碱性、水溶性的多糖,具有优越的生物活性,可由甲壳素、壳聚糖制备。不同分子量的壳寡糖具有不同的功能,分子量5000Da左右的壳寡糖具有降血脂的功能,分子量3000-2000Da左右的壳寡糖具有抑制肿瘤细胞的生长和转移的作用;值得注意的是分子量在1000Da以下的壳寡糖具有独特的生理活性和功能,包括增强体液免疫和细胞免疫;促进钙的吸收和骨骼健康;抗菌、抑菌和显著的保湿吸湿能力等。Chitosan is the only positively-charged, alkaline, water-soluble polysaccharide found in nature at present. It has superior biological activity and can be prepared from chitin and chitosan. Chito-oligosaccharides with different molecular weights have different functions. Chito-oligosaccharides with a molecular weight of about 5000 Da have the function of lowering blood lipids. Chito-oligosaccharides with a molecular weight of about 3,000-2000 Da can inhibit the growth and metastasis of tumor cells. Chitooligosaccharides below 1000 Da have unique physiological activities and functions, including enhancing humoral immunity and cellular immunity; promoting calcium absorption and bone health; antibacterial, bacteriostatic, and significant moisture-absorbing capacity.
目前主要通过酶解法降解壳聚糖来制备壳寡糖,酶解法具有专一性强、反应条件温和、过程易控制和环境污染少等优点。而目前常用的酶可分专一性酶和非专一性酶,专一性酶酶解效果好,但价格昂贵,部分非专一性酶如木瓜蛋白酶和菠萝蛋白酶等价格较低,但酶解效果不佳,如公开号CN107739418A的中国专利公开了一种采用木瓜蛋白酶冷冻干燥制备壳寡糖的方法,该方法虽然酶解时间较短,但产物分子量多在3000Da左右;公开号CN107988287A的中国专利公开了一种采用纤维素酶喷雾干燥制备壳寡糖的方法,该方法所用酶廉价易得,但是存在酶解时间长等问题。At present, chitosan is mainly produced by enzymatic degradation of chitosan. The enzymatic hydrolysis method has the advantages of specificity, mild reaction conditions, easy control of the process, and less environmental pollution. At present, the commonly used enzymes can be divided into specific enzymes and non-specific enzymes. Specific enzymes have good enzymatic hydrolysis, but they are expensive. Some non-specific enzymes such as papain and bromelain are less expensive. The hydrolysis effect is not good. For example, Chinese Patent Publication No. CN107739418A discloses a method for preparing chitosan oligosaccharides by freeze-drying papain. Although the method has a short enzymolysis time, the molecular weight of the product is about 3000 Da; China with publication number CN107988287A The patent discloses a method for preparing chitooligosaccharides by spray drying of cellulase. The method uses cheap and easy-to-obtain enzymes, but has problems such as long enzymatic hydrolysis time.
单宁酶又称鞣酸酶,是一种单宁酰基水解酶。该酶可由霉菌,如黑曲霉、米曲霉生产,目前主要用于处理啤酒中单宁、蛋白质,使其澄清透明。但是并未涉及其在酶解壳聚糖方面的作用。Tannase, also known as tanninase, is a tannin hydrolase. The enzyme can be produced by molds such as Aspergillus niger and Aspergillus oryzae. At present, it is mainly used for processing tannin and protein in beer to make it clear and transparent. However, its role in enzymatic hydrolysis of chitosan is not mentioned.
目前尚未出现利用无花果蛋白酶和单宁酶作为复合酶酶解壳聚糖生产壳寡糖的报道。So far, there have been no reports on the use of fig protease and tannase as complex enzymes to hydrolyze chitosan to produce chitooligosaccharides.
发明内容Summary of the Invention
针对现有技术的不足,本发明的目的在于提供一种壳寡糖及其制备方法。本发明提供的一种壳寡糖制备方法条件温和,简便、制备所需时间短,分子量1000Da左右的壳寡糖产量较高,且不需要加入大量的反应试剂,对环境污染较少,所用无花果蛋白酶及单宁酶价廉易得。In view of the shortcomings of the prior art, the object of the present invention is to provide a chitooligosaccharide and a preparation method thereof. The method for preparing chitosan oligosaccharides provided by the present invention has mild conditions, is simple, requires short preparation time, has a high yield of chitosan oligosaccharides with a molecular weight of about 1000 Da, does not need to add a large number of reaction reagents, has less environmental pollution, and uses figs Proteases and tannins are inexpensive and readily available.
本发明的技术方案是:一种低分子量壳寡糖制备方法,包括以下步骤:The technical scheme of the present invention is: a method for preparing a low molecular weight chitooligosaccharide, comprising the following steps:
S1、将壳聚糖溶解于醋酸-醋酸钠缓冲溶液中,配制成质量浓度为0.5~1.5%的壳聚糖溶液;S1. Dissolving chitosan in an acetate-sodium acetate buffer solution to prepare a chitosan solution with a mass concentration of 0.5 to 1.5%;
S2、向步骤S1所得壳聚糖溶液中加入复合酶,复合酶的质量与壳聚糖的质量比为2.5~25%,于65℃下反应1~3h,得酶解液,其中复合酶由无花果蛋白酶及单宁酶按1∶(0.1~1)的重量比组成;S2. Add a complex enzyme to the chitosan solution obtained in step S1. The mass ratio of the mass of the complex enzyme to the mass of the chitosan is 2.5 to 25%. The reaction is performed at 65 ° C for 1 to 3 hours to obtain an enzymatic hydrolysis solution. Fig protease and tannin are composed in a weight ratio of 1: (0.1 to 1);
S3、搅拌下往步骤S2所得酶解液中滴加质量浓度为5%的NaOH溶液,调节pH为7.0~8.0,过滤,分离水不溶性壳聚糖,滤液装入透析袋中,在蒸馏水中透析24h,得透析液;S3. Add 5% NaOH solution with a mass concentration of 5% to the enzymatic hydrolysis solution obtained in step S2 with stirring, adjust the pH to 7.0 to 8.0, filter, and separate the water-insoluble chitosan. The filtrate is placed in a dialysis bag and dialyzed in distilled water. 24h, get dialysate;
S4、将步骤S3所得透析液进行浓缩,浓缩至固形物质量浓度为9~15%的浓缩液,进行喷雾干燥。S4. The dialysate obtained in step S3 is concentrated, concentrated to a concentrated solution having a solid content concentration of 9 to 15%, and spray-dried.
进一步地,所述步骤S1中所述复合酶由无花果蛋白酶及单宁酶按1∶0.3的重量比组成。Further, the complex enzyme in the step S1 is composed of fig protease and tannin in a weight ratio of 1: 0.3.
进一步地,所述步骤S1中所述醋酸-醋酸钠缓冲溶液的pH值为5.0,浓度为0.2mol/L。Further, the pH value of the acetic acid-sodium acetate buffer solution in step S1 is 5.0, and the concentration is 0.2 mol / L.
进一步地,所述步骤S2中所述复合酶的质量与壳聚糖的质量比为5~10%。Further, the mass ratio of the mass of the complex enzyme to the mass of chitosan in step S2 is 5-10%.
进一步地,所述步骤S2中所述复合酶的质量与壳聚糖的质量比为7.5%。Further, the mass ratio of the mass of the complex enzyme to the mass of chitosan in step S2 is 7.5%.
进一步地,所述步骤S2中于65℃反应2h。Further, in step S2, the reaction is performed at 65 ° C for 2h.
进一步地,所述步骤S3所述透析袋为再生纤维素透析袋,截留分子量1000Da。Further, the dialysis bag in step S3 is a regenerated cellulose dialysis bag with a molecular weight cut off of 1000 Da.
进一步地,所述步骤S4所述喷雾干燥的浓缩液的固形物质量浓度为10%。Further, the solid content mass concentration of the spray-dried concentrated liquid in the step S4 is 10%.
进一步地,所述步骤S4所述喷雾干燥的工艺条件为:进风温度180℃,进料速度为700mL/h。Further, the process conditions for spray drying in step S4 are: an inlet air temperature of 180 ° C., and a feed rate of 700 mL / h.
本发明采用无花果蛋白酶和单宁酶酶解壳聚糖能够在较短的时间内,酶解得到较多分子量在1000Da左右的小分子量壳寡糖,平均产率可达到39.47%,显著缩短了酶解时间,降低了成本。而当单独采用无花果蛋白酶抑或是单宁酶时均无法取得与上述相同或类似的效果。The invention uses fig protease and tannin to hydrolyze chitosan, which can obtain more small molecular weight chitosan oligosaccharides with a molecular weight of about 1000 Da in a short period of time, and the average yield can reach 39.47%, which significantly shortens the enzyme. Solution time and reduce costs. However, when the fig protease or the tannase is used alone, the same or similar effects as those described above cannot be obtained.
与现有技术相比,本发明具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
本发明提供的方法条件温和,所用复合酶价廉易得,生产成本低,制备所需时间短,更重要的是低分子量壳寡糖产量较高,与现有技术相比取得了显著的进步。The method provided by the invention has mild conditions, the complex enzyme used is cheap and easy to obtain, the production cost is low, the time required for preparation is short, and more importantly, the yield of low molecular weight chitooligosaccharide is higher, and significant progress has been achieved compared with the prior art. .
具体实施方式detailed description
以下通过具体实施方式的描述对本发明作进一步说明,但这并非是对本发明的限制,本领域技术人员根据本发明的基本思想,可以做出各种修改或改进,但是只要不脱离本发明的基本思想,均在本发明的范围之内。The following further describes the present invention through the description of specific embodiments, but this is not a limitation on the present invention. Those skilled in the art can make various modifications or improvements based on the basic idea of the present invention, but as long as it does not depart from the basics of the present invention The ideas are all within the scope of the present invention.
壳聚糖(批号:171112A,DD85%,山东奥康生物科技有限公司);无花果蛋白酶(梯希爱化成工业发展有限公司);单宁酶(河南希禾化工有限公司);壳寡糖(青岛祥昇海洋科技有限公司);再生纤维素透析袋(截留分子量1000Da,美国MYM生物技术公司)。Chitosan (batch number: 171112A, DD85%, Shandong Aokang Biotechnology Co., Ltd.); fig protease (Tixi Aihuacheng Industrial Development Co., Ltd.); tannase (Henan Xihe Chemical Co., Ltd.); Sheng Ocean Technology Co., Ltd.); regenerated cellulose dialysis bag (cut-off molecular weight 1000 Da, US MYM Biotechnology Company).
实施例1、低分子量壳寡糖的制备Example 1. Preparation of low molecular weight chitooligosaccharides
S1、将壳聚糖溶解于pH值5.0的0.2mol/L醋酸-醋酸钠缓冲溶液中,配制成质量浓度为1.0%的壳聚糖溶液;S1. Dissolve chitosan in a 0.2 mol / L acetic acid-sodium acetate buffer solution with a pH value of 5.0 to prepare a chitosan solution with a mass concentration of 1.0%;
S2、向步骤S1所得壳聚糖溶液中加入质量浓度为0.5%的复合酶液,复合酶由无花果蛋白酶及单宁酶按1∶0.3的重量比组成,复合酶质量与壳聚糖的质量比为7.5%,于65℃下反应2h,得酶解液;S2. Add a 0.5% complex enzyme solution to the chitosan solution obtained in step S1. The complex enzyme is composed of fig protease and tannin in a weight ratio of 1: 0.3. It was 7.5%, and reacted at 65 ° C for 2h to obtain an enzymatic hydrolysis solution;
S3、搅拌下向步骤S2所得酶解液中滴加质量浓度为5%的NaOH溶液,调节pH为7.0~8.0,过滤,分离水不溶性壳聚糖,将滤液分别装入截留分子量为1000Da的再生纤维素透析袋中,在蒸馏水中透析24h,得透析液;S3. Add 5% NaOH solution with a mass concentration of 5% to the enzymatic hydrolysis solution obtained in step S2 under stirring, adjust the pH to 7.0-8.0, filter, separate the water-insoluble chitosan, and fill the filtrate with regeneration with a molecular weight of 1000 Da. In a cellulose dialysis bag, dialysis was performed in distilled water for 24 hours to obtain a dialysate;
S4、将步骤S3所得透析液进行浓缩,浓缩至固形物质量浓度为10%的浓缩液,进行喷雾干燥,喷雾干燥的工艺条件为:进风温度180℃,进料速度700mL/h。S4. The dialysate obtained in step S3 is concentrated, concentrated to a concentrated solution with a solid content concentration of 10%, and spray-dried. The process conditions for spray-drying are: an inlet air temperature of 180 ° C and a feed rate of 700 mL / h.
所述复合酶液由pH值5.0的0.2mol/L的醋酸-醋酸钠缓冲溶液配制而成。The complex enzyme solution is prepared from a 0.2 mol / L acetate-sodium acetate buffer solution with a pH value of 5.0.
实施例2、低分子量壳寡糖的制备Example 2. Preparation of low molecular weight chitooligosaccharides
实施例2与实施例1的区别在于,步骤S1中,壳聚糖溶液的质量浓度为1.2%,S2步骤中复合酶的质量与壳聚糖的质量比为5%,复合酶由无花果蛋白酶及单宁酶按1∶0.1的重量比组成,其余同实施例1。The difference between Example 2 and Example 1 is that in step S1, the mass concentration of the chitosan solution is 1.2%, and the mass ratio of the mass of the complex enzyme to the mass of chitosan in step S2 is 5%. The complex enzyme is composed of fig protease and Tannase was composed by a weight ratio of 1: 0.1, and the rest was the same as in Example 1.
实施例3、低分子量壳寡糖的制备Example 3 Preparation of low molecular weight chitooligosaccharides
实施例3与实施例1的区别在于,步骤S1中,壳聚糖溶液的质量浓度为1.2%,S2步骤中复合酶的质量与壳聚糖的质量比为7.5%,复合酶由无花果蛋白酶及单宁酶按1∶1的重量比组成,其余同实施例1。The difference between Example 3 and Example 1 is that in step S1, the mass concentration of the chitosan solution is 1.2%, and the mass ratio of the compound enzyme to the mass of chitosan in step S2 is 7.5%. The compound enzyme is composed of fig protease and Tannase was composed by a weight ratio of 1: 1, and the rest was the same as in Example 1.
对比例1、低分子量壳寡糖的制备Comparative Example 1. Preparation of low molecular weight chitooligosaccharide
与实施例1相比本对比例区别在于:所用酶为无花果蛋白酶,其余同实施例 1。Compared with Example 1, this comparative example is different in that the enzyme used is fig protease, and the rest are the same as in Example 1.
对比例2、低分子量壳寡糖的制备Comparative Example 2: Preparation of low molecular weight chitooligosaccharides
与实施例1相比本对比例区别在于:所用酶为单宁酶,其余同实施例1。Compared with Example 1, this comparative example is different in that the enzyme used is tannin, and the rest are the same as in Example 1.
对比例3、低分子量壳寡糖的制备Comparative Example 3, Preparation of low molecular weight chitooligosaccharides
与实施例1相比本对比例区别在于:用纤维素酶替换单宁酶,其余同实施例1。Compared with Example 1, this comparative example is different in that Tannase is replaced with cellulase, and the rest are the same as in Example 1.
试验例一、产品性能测定Test example one, product performance measurement
对实施例1~3以及对比例1~3制备得到的壳寡糖样品的水分含量、还原糖含量、5%水溶液粘度以及1000Da壳寡糖的得率进行检测,并以相应的壳寡糖原料药作为对照组,检测结果如下表1所示。The moisture content, reducing sugar content, 5% aqueous solution viscosity, and 1000 Da chitooligosaccharide yield of the chitosan samples prepared in Examples 1 to 3 and Comparative Examples 1 to 3 were tested, and the corresponding chitosan raw materials were used. As a control group, the test results are shown in Table 1 below.
表1检测结果Table 1 test results
组别Group 水分(%)Moisture (%) 还原糖含量(%)Reducing sugar content (%) 5%水溶液粘度5% aqueous solution viscosity 得率(%)Yield (%)
实施例1Example 1 5.025.02 62.7162.71 1.381.38 39.47%39.47%
实施例2Example 2 5.155.15 61.0361.03 1.411.41 37.36%37.36%
实施例3Example 3 5.295.29 64.6964.69 1.351.35 38.54%38.54%
对比例1Comparative Example 1 5.185.18 43.7443.74 1.421.42 20.06%20.06%
对比例2Comparative Example 2 5.005.00 30.6530.65 1.431.43 11.57%11.57%
对比例3Comparative Example 3 5.235.23 56.5356.53 1.401.40 25.36%25.36%
1000Da壳寡糖原料药1000Da Chitosan API 4.964.96 57.6657.66 1.421.42 --
由表1可知,对比例1和对比例2与实施例1相比,其区别仅在于将复合降解酶替换为二者的单一酶,但1000Da壳寡糖的得率却远低于实施例1中复合降解酶的产量,尤其是采用单宁酶酶解,得率仅为11.57%;此外,对比例3和实施 例1相比,虽然两者都使用复合酶酶解壳聚糖,但对比例3所用无花果酶和纤维素酶复合酶的酶解性能不如实施例1~3所述无花果蛋白酶及单宁酶复合酶,综上说明本发明取得了意想不到的效果。It can be known from Table 1 that the difference between Comparative Example 1 and Comparative Example 2 and Example 1 is only that the composite degrading enzyme is replaced by a single enzyme of the two, but the yield of 1000 Da chitooligosaccharide is much lower than that of Example 1. The yield of complex degrading enzymes, especially the tannin digestion, was only 11.57%. In addition, compared with Example 3, although both use the complex enzymatic hydrolysis of chitosan, The enzymatic hydrolysis performance of the fig enzyme and the cellulase complex enzyme used in the ratio 3 is not as good as the fig protease and tannin complex enzymes described in Examples 1 to 3. In summary, the present invention has achieved unexpected effects.
以上所揭露的仅为本发明的优选实施例而已,当然不能以此来限定本发明之权利范围,因此依本发明申请专利范围所作的等同变化,仍属本发明所涵盖的范围。What has been disclosed above are only preferred embodiments of the present invention, and of course, the scope of rights of the present invention cannot be limited by this. Therefore, equivalent changes made in accordance with the scope of patent application of the present invention still fall within the scope of the present invention.

Claims (10)

  1. 一种低分子量壳寡糖的制备方法,其特征在于,包括以下步骤:A method for preparing low molecular weight chitooligosaccharides, which comprises the following steps:
    S1、将壳聚糖溶解于醋酸-醋酸钠缓冲溶液中,配制成质量浓度为0.5~1.5%的壳聚糖溶液;S1. Dissolving chitosan in an acetate-sodium acetate buffer solution to prepare a chitosan solution with a mass concentration of 0.5 to 1.5%;
    S2、向步骤S1所得壳聚糖溶液中加入复合酶,复合酶的质量与壳聚糖的质量比为2.5~25%,于65℃下反应1~3h,得酶解液,其中复合酶由无花果蛋白酶及单宁酶按1∶(0.1~1)的重量比组成;S2. Add a complex enzyme to the chitosan solution obtained in step S1. The mass ratio of the mass of the complex enzyme to the mass of the chitosan is 2.5 to 25%. The reaction is performed at 65 ° C for 1 to 3 hours to obtain an enzymatic hydrolysis solution. Fig protease and tannin are composed in a weight ratio of 1: (0.1 to 1);
    S3、在搅拌的条件下往步骤S2所得酶解液中滴加质量浓度为5%的NaOH溶液,调节pH为7.0~8.0,过滤,分离水不溶性壳聚糖,滤液装入透析袋中,在蒸馏水中透析24h,得透析液;S3. Add 5% NaOH solution with a mass concentration of 5% to the enzymolysis solution obtained in step S2 under stirring conditions, adjust the pH to 7.0-8.0, filter, separate the water-insoluble chitosan, and place the filtrate in a dialysis bag. Dialyzed for 24 hours in distilled water to obtain dialysate;
    S4、将步骤S3所得透析液进行浓缩,浓缩至固形物质量浓度为9~15%的浓缩液,进行喷雾干燥。S4. The dialysate obtained in step S3 is concentrated, concentrated to a concentrated solution having a solid content concentration of 9 to 15%, and spray-dried.
  2. 如权利要求1所述的低分子量壳寡糖制备方法,其特征在于,所述步骤S1中所述复合酶由无花果蛋白酶及单宁酶按1∶0.3的重量比组成。The method for preparing a low-molecular-weight chitooligosaccharide according to claim 1, wherein in step S1, the complex enzyme is composed of fig protease and tannin in a weight ratio of 1: 0.3.
  3. 如权利要求1所述的低分子量壳寡糖制备方法,其特征在于,所述步骤S1中所述醋酸-醋酸钠缓冲溶液的pH值为5.0,浓度为0.2mol/L。The method for preparing a low-molecular-weight chitooligosaccharide according to claim 1, wherein in the step S1, the pH value of the acetate-sodium acetate buffer solution is 5.0 and the concentration is 0.2 mol / L.
  4. 如权利要求1所述的低分子量壳寡糖制备方法,其特征在于,所述步骤S2中所述复合酶的质量与壳聚糖的质量比为5~10%。The method for preparing a low molecular weight chitooligosaccharide according to claim 1, wherein the mass ratio of the mass of the complex enzyme to the mass of chitosan in the step S2 is 5-10%.
  5. 如权利要求4所述的低分子量壳寡糖制备方法,其特征在于,所述复合酶的质量与壳聚糖的质量比为7.5%。The method for preparing a low-molecular-weight chitooligosaccharide according to claim 4, wherein the mass ratio of the complex enzyme to the mass of chitosan is 7.5%.
  6. 如权利要求1所述的低分子量壳寡糖制备方法,其特征在于,所述步骤 S2中于65℃反应2h。The method for preparing a low-molecular-weight chitooligosaccharide according to claim 1, wherein in step S2, the reaction is carried out at 65 ° C for 2 hours.
  7. 如权利要求1所述的低分子量壳寡糖制备方法,其特征在于,所述步骤S3中所述透析袋为再生纤维素透析袋,截留分子量1000Da。The method for preparing a low molecular weight chitooligosaccharide according to claim 1, wherein the dialysis bag in the step S3 is a regenerated cellulose dialysis bag with a molecular weight cut-off of 1000 Da.
  8. 如权利要求1所述的低分子量壳寡糖制备方法,其特征在于,所述步骤S4浓缩至固形物质量浓度为10%的浓缩液。The method for preparing a low-molecular-weight chitooligosaccharide according to claim 1, wherein the step S4 is concentrated to a concentrated solution having a solid content concentration of 10%.
  9. 如权利要求1所述的低分子量壳寡糖制备方法,其特征在于,所述步骤S4中所述喷雾干燥的工艺条件为:进风温度180℃,进料速度700mL/h。The method for preparing a low-molecular-weight chitooligosaccharide according to claim 1, wherein the spray drying process conditions in the step S4 are: an inlet air temperature of 180 ° C, and a feed rate of 700 mL / h.
  10. 一种如权利要求1~9任一所述的方法制备得到的壳寡糖。A chitooligosaccharide prepared by the method according to any one of claims 1 to 9.
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