CN118285508A - Probiotic delivery method based on oxidized high amylose starch carrier - Google Patents
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Abstract
Description
技术领域Technical Field
本发明涉及一种基于氧化高直链淀粉载体的益生菌递送方法,属于生物递送与缓释技术领域。The invention relates to a probiotic delivery method based on an oxidized high-amylose starch carrier, belonging to the technical field of biological delivery and sustained release.
背景技术Background technique
随着人们健康意识的提高和生活水平的提升,安全、健康和营养的功能性产品逐步受到消费者的青睐。其中,益生菌产品的市场接受度逐年上升,已经发展为一大朝阳产业,对促进人体健康和提高人类生活质量方面具有重大意义。随着研究人员对肠道微生物菌群的逐步探究以及菌群失衡在多种疾病中的重要表现,使得我们发现补充益生菌有助于恢复肠道生态系统的平衡,提高机体免疫。As people's health awareness and living standards improve, safe, healthy and nutritious functional products are gradually favored by consumers. Among them, the market acceptance of probiotic products has increased year by year, and it has developed into a sunrise industry, which is of great significance in promoting human health and improving the quality of human life. As researchers gradually explore the intestinal microbial flora and the important manifestation of flora imbalance in various diseases, we have found that supplementing probiotics can help restore the balance of the intestinal ecosystem and improve the body's immunity.
为达到促进宿主健康的目的,益生菌在肠道中的最低浓度必须达到106~107cfu/mL。但是,在加工、贮藏以及消化过程中维持益生菌活力是目前该行业的一大挑战。因此,选用合适的材料作为载体,对益生菌进行一系列的包埋保护是至关重要的。目前,微胶囊技术是一种成熟且应用广泛的新型方法,它利用天然或合成的高分子材料,包覆生物活性物质形成半透性或密闭的囊泡结构,使其对内容物起到良好的保护作用,降低外界环境对其活性的影响。因此,利用该技术包埋益生菌被认为是经济高效的保护策略之一,也是目前的研究热点。In order to promote host health, the minimum concentration of probiotics in the intestine must reach 10 6 to 10 7 cfu/mL. However, maintaining the activity of probiotics during processing, storage and digestion is a major challenge in the industry. Therefore, it is crucial to select suitable materials as carriers and perform a series of encapsulation and protection on probiotics. At present, microencapsulation technology is a mature and widely used new method. It uses natural or synthetic polymer materials to encapsulate bioactive substances to form semi-permeable or closed vesicle structures, so that it can provide good protection for the contents and reduce the impact of the external environment on its activity. Therefore, the use of this technology to encapsulate probiotics is considered to be one of the cost-effective protection strategies and is also a current research hotspot.
天然淀粉来源广泛,是植物中含量最丰富的多糖,良好的相容性和表面可修饰性使其成为生物活性载体的理想壁材。但是,天然淀粉具有溶解性差,持水能力弱等缺点,限制了其在食品行业的应用和发展。许多研究发现,通过化学改性可以控制淀粉聚集体的结构,改善其溶解度、吸水性等性能,使其更好的为功能性食品提供保护,促进其在食品行业的发展的应用。Natural starch is widely available and is the most abundant polysaccharide in plants. Its good compatibility and surface modifiability make it an ideal wall material for bioactive carriers. However, natural starch has disadvantages such as poor solubility and weak water holding capacity, which limits its application and development in the food industry. Many studies have found that chemical modification can control the structure of starch aggregates, improve their solubility, water absorption and other properties, so that they can better protect functional foods and promote their development and application in the food industry.
包封率和存活率可以直接体现益生菌包埋的效果。包埋益生菌在胃中的存活率和肠中的释放性对益生菌在肠道中的存活和定植直接相关,另外,益生菌微胶囊在肠道中的缓慢释放也有利于益生菌在肠道中的定植。提高益生菌在肠道中的黏附和定植是非常重要的,因为这对于维持肠道健康和整体健康有着重要的作用。首先,益生菌的黏附和定植可以形成一层保护膜,阻止有害细菌和毒素对肠道黏膜的侵害,从而保护肠道健康;其次,益生菌的定植可以竞争性地抑制有害菌在肠道中的生长,维持肠道微生态平衡,减少有害菌对肠道的侵害;另外,益生菌在肠道中的定植可以促进免疫系统的发育和功能,增强肠道黏膜的屏障功能,提高机体的抵抗力;最后,黏附在肠道中的益生菌可以帮助分解食物中的营养物质,促进其吸收和利用,提高营养物质的利用率。因此,提高益生菌在肠道中的黏附和定植有助于维持肠道健康,促进整体健康。The encapsulation rate and survival rate can directly reflect the effect of probiotic encapsulation. The survival rate of encapsulated probiotics in the stomach and the release in the intestine are directly related to the survival and colonization of probiotics in the intestine. In addition, the slow release of probiotic microcapsules in the intestine is also conducive to the colonization of probiotics in the intestine. It is very important to improve the adhesion and colonization of probiotics in the intestine, because this plays an important role in maintaining intestinal health and overall health. First, the adhesion and colonization of probiotics can form a protective film to prevent harmful bacteria and toxins from invading the intestinal mucosa, thereby protecting intestinal health; secondly, the colonization of probiotics can competitively inhibit the growth of harmful bacteria in the intestine, maintain the balance of intestinal microecology, and reduce the invasion of harmful bacteria on the intestine; in addition, the colonization of probiotics in the intestine can promote the development and function of the immune system, enhance the barrier function of the intestinal mucosa, and improve the body's resistance; finally, probiotics adhering to the intestine can help decompose nutrients in food, promote their absorption and utilization, and improve the utilization rate of nutrients. Therefore, improving the adhesion and colonization of probiotics in the intestines can help maintain intestinal health and promote overall health.
由于不同益生菌菌株具有特异的性能,益生菌包裹材料与菌株的性质之间并没有统一、固定的关联,因此,对于特定的益生菌而言,包裹壁材对益生菌包埋效果的影响是不可预期的;包裹壁材是否能够同时实现益生菌微胶囊包裹后的高包封率、储藏后及置于胃液暴露后的高存活率、肠中缓释效果、高黏附和定植率也是无法预料的。同时,能够实现对多种益生菌菌株都具有良好的包埋效果,是非常困难的。Since different probiotic strains have specific properties, there is no uniform and fixed correlation between the probiotic encapsulation materials and the properties of the strains. Therefore, for specific probiotics, the effect of the encapsulation wall material on the encapsulation effect of the probiotics is unpredictable; whether the encapsulation wall material can simultaneously achieve a high encapsulation rate after encapsulation of the probiotic microcapsules, a high survival rate after storage and exposure to gastric juice, a sustained release effect in the intestine, and a high adhesion and colonization rate is also unpredictable. At the same time, it is very difficult to achieve a good encapsulation effect for multiple probiotic strains.
发明内容Summary of the invention
有鉴于此,本发明的首要目的在于克服现有技术的缺点与不足,提供一种氧化高直链淀粉-多糖复合微胶囊的制备方法。本发明的另一目的在于提供通过以上制备方法制备得到的氧化高直链淀粉-多糖复合微胶囊。本发明的再一个目的在于提供上述氧化高直链淀粉-多糖复合微胶囊的应用。In view of this, the primary purpose of the present invention is to overcome the shortcomings and deficiencies of the prior art and provide a method for preparing oxidized high-amylose starch-polysaccharide composite microcapsules. Another purpose of the present invention is to provide oxidized high-amylose starch-polysaccharide composite microcapsules prepared by the above preparation method. Another purpose of the present invention is to provide the application of the above oxidized high-amylose starch-polysaccharide composite microcapsules.
本发明将氧化高直链淀粉与多糖复配后获得的氧化淀粉-多糖复合物,能够更容易黏附在肠道表面,有利于益生菌在肠道中的定植,这些益生菌递送体系的新特性尚未见报道。The oxidized starch-polysaccharide complex obtained by compounding oxidized high-amylose starch with polysaccharides in the present invention can adhere to the intestinal surface more easily, which is beneficial to the colonization of probiotics in the intestine. These new properties of the probiotic delivery system have not been reported yet.
为实现上述目的,本发明通过下述技术方案来实现:To achieve the above object, the present invention is implemented by the following technical solutions:
本发明提供一种基于氧化高直链淀粉载体制备益生菌微胶囊的方法,包括以下步骤:The present invention provides a method for preparing probiotic microcapsules based on oxidized high-amylose starch carrier, comprising the following steps:
(1)利用氧化剂将高直链淀粉溶液氧化,得到氧化高直链淀粉;(1) oxidizing a high-amylose starch solution using an oxidant to obtain oxidized high-amylose starch;
(2)将所述氧化高直链淀粉溶液与益生菌混合得到氧化淀粉-益生菌混合溶液,每100mL的氧化高直链淀粉溶液与3×108~3×1010cfu的益生菌混合;(2) mixing the oxidized high-amylose starch solution with probiotics to obtain an oxidized starch-probiotic mixed solution, wherein 3×10 8 to 3×10 10 cfu of probiotics are mixed with every 100 mL of the oxidized high-amylose starch solution;
(3)将多糖溶解于水中,得到浓度为2~3g/100mL的多糖溶液;(3) dissolving the polysaccharide in water to obtain a polysaccharide solution with a concentration of 2 to 3 g/100 mL;
(4)将步骤(2)制得的氧化高直链淀粉-益生菌混合溶液与多糖溶液混合后,保持体系温度在40~50℃,调整体系pH在4.5~4.8,得到氧化淀粉-益生菌-多糖混合溶液(水相);(4) mixing the oxidized high-amylose starch-probiotic mixed solution obtained in step (2) with the polysaccharide solution, maintaining the system temperature at 40 to 50° C., and adjusting the system pH to 4.5 to 4.8 to obtain an oxidized starch-probiotic-polysaccharide mixed solution (aqueous phase);
(5)取上述氧化淀粉-益生菌-多糖混合溶液2~4mL,在搅拌状态下缓慢加入油相,得到混合溶液,继续搅拌10~20min后,加入固化剂,继续搅拌10~20min,多次离心、生理盐水洗涤2~3次后获得湿微胶囊;(5) Take 2-4 mL of the above-mentioned oxidized starch-probiotic-polysaccharide mixed solution, slowly add the oil phase under stirring to obtain a mixed solution, continue stirring for 10-20 minutes, add a curing agent, continue stirring for 10-20 minutes, centrifuge several times, wash with physiological saline 2-3 times, and obtain wet microcapsules;
(6)将上述湿微胶囊冷冻干燥,得到益生菌微胶囊粉末。(6) freeze-drying the wet microcapsules to obtain probiotic microcapsule powder.
在一种实施方式中,步骤(1)所述氧化高直链淀粉的氧化度为8%~12%。In one embodiment, the oxidation degree of the oxidized high-amylose starch in step (1) is 8% to 12%.
在一种实施方式中,步骤(4)所述水相中,氧化高直链淀粉的终浓度为0.66g/100mL,多糖的终浓度为0.83g/100mL,益生菌的活菌数为3×108cfu/mL。In one embodiment, in the aqueous phase of step (4), the final concentration of oxidized high-amylose starch is 0.66 g/100 mL, the final concentration of polysaccharide is 0.83 g/100 mL, and the number of viable probiotics is 3×10 8 cfu/mL.
在一种实施方式中,所述益生菌包括干酪乳杆菌、鼠李糖乳杆菌、干酪乳杆菌、保加利亚乳杆菌和嗜热链球菌中的一种或多种。In one embodiment, the probiotics include one or more of Lactobacillus casei, Lactobacillus rhamnosus, Lactobacillus casei, Lactobacillus bulgaricus and Streptococcus thermophilus.
在一种实施方式中,所述多糖为植物多糖、动物多糖或微生物来源的多糖;所述植物、动物或微生物来源的多糖包括壳聚糖、卡拉胶、阿拉伯胶和海藻酸钠中的一种或者多种。In one embodiment, the polysaccharide is a plant polysaccharide, an animal polysaccharide or a polysaccharide of microbial origin; the polysaccharide of plant, animal or microbial origin includes one or more of chitosan, carrageenan, gum arabic and sodium alginate.
在一种实施方式中,所述益生菌是通过将益生菌培养物在4℃下离心,去除上清,使用生理盐水溶液洗涤菌泥,然后离心去除上清,重复2~3次,获得的益生菌菌泥或菌悬液。In one embodiment, the probiotics are obtained by centrifuging the probiotic culture at 4°C, removing the supernatant, washing the slurry with a physiological saline solution, and then centrifuging to remove the supernatant, repeating 2 to 3 times to obtain a probiotic slurry or suspension.
在一种实施方式中,步骤(1)中所述的高直链淀粉溶液的浓度为1g/100mL~2g/100mL。In one embodiment, the concentration of the high amylose starch solution in step (1) is 1 g/100 mL to 2 g/100 mL.
优选的,步骤(1)中所述的高直链淀粉溶液的质量浓度为1.6g/100mL。Preferably, the mass concentration of the high amylose starch solution in step (1) is 1.6 g/100 mL.
在一种实施方式中,步骤(1)中所述的氧化剂为2,2,6,6-四甲基-1-哌啶基氧基(TEMPO)和NaBr,所述氧化物的添加量分别为高直链淀粉含量的0.8~0.9%和35~40%,所述氧化的pH条件为9.5~10,所述氧化的温度为4~5℃,所述搅拌的转速为500~700rpm,搅拌时间为20~30min;In one embodiment, the oxidant in step (1) is 2,2,6,6-tetramethyl-1-piperidinyloxy (TEMPO) and NaBr, the addition amount of the oxide is 0.8-0.9% and 35-40% of the high amylose content, respectively, the pH condition of the oxidation is 9.5-10, the temperature of the oxidation is 4-5°C, the stirring speed is 500-700rpm, and the stirring time is 20-30min;
优选的,所述步骤(1)中2,2,6,6-四甲基-1-哌啶基氧基(TEMPO)和NaBr,所述氧化物的添加量分别为高直链淀粉含量的0.85%和35%,所述氧化的pH条件为10,所述氧化的温度为4℃,所述搅拌的转速为600rpm,所述搅拌时间为20min;Preferably, in step (1), the addition amounts of 2,2,6,6-tetramethyl-1-piperidinyloxy (TEMPO) and NaBr are 0.85% and 35% of the high amylose content, respectively, the oxidation pH is 10, the oxidation temperature is 4° C., the stirring speed is 600 rpm, and the stirring time is 20 min;
在一种实施方式中,步骤(3)中所述多糖为植物多糖、动物多糖或微生物来源的多糖;所述植物、动物或微生物来源的多糖包括壳聚糖、卡拉胶、阿拉伯胶和海藻酸钠中的一种或者多种。In one embodiment, the polysaccharide in step (3) is a plant polysaccharide, an animal polysaccharide or a polysaccharide of microbial origin; the polysaccharide of plant, animal or microbial origin includes one or more of chitosan, carrageenan, gum arabic and sodium alginate.
优选的,所述步骤(3)中的多糖为海藻酸钠,海藻酸钠浓度为2%。Preferably, the polysaccharide in step (3) is sodium alginate, and the concentration of sodium alginate is 2%.
在一种实施方式中,步骤(5)中所述的固化剂为0.5~0.6M CaCl2溶液,所述CaCl2溶液的添加量为整体混合溶液的40~50%,所述CaCl2溶液应在氧化淀粉-益生菌-多糖混合溶液加入大豆油中继续搅拌10~20min后加入。In one embodiment, the curing agent described in step (5) is a 0.5-0.6M CaCl2 solution, and the addition amount of the CaCl2 solution is 40-50% of the entire mixed solution. The CaCl2 solution should be added after the oxidized starch-probiotics-polysaccharide mixed solution is added to the soybean oil and stirred for 10-20 minutes.
优选的,步骤(5)中所述的固化剂为0.5M CaCl2溶液,所述CaCl2溶液的添加量为整体混合溶液的40%,所述CaCl2溶液应在氧化淀粉-益生菌-多糖混合溶液加入大豆油中继续搅拌15min后加入。Preferably, the curing agent in step (5) is a 0.5M CaCl2 solution, and the amount of the CaCl2 solution added is 40% of the entire mixed solution. The CaCl2 solution should be added after the oxidized starch-probiotics-polysaccharide mixed solution is added to the soybean oil and stirred for 15 minutes.
在一种实施方式中,步骤(5)中的油相为Span80和大豆油的混合油相,所述混合油相中Span80的添加量为2.5~3%(w/v)。In one embodiment, the oil phase in step (5) is a mixed oil phase of Span 80 and soybean oil, and the added amount of Span 80 in the mixed oil phase is 2.5-3% (w/v).
优选的,所述步骤(5)中混合油相中Span80的添加量为2.5%(w/v)。Preferably, the amount of Span 80 added to the mixed oil phase in step (5) is 2.5% (w/v).
在一种实施方式中,步骤(5)所述混合溶液中,水相和油相的体积比为1:3~3:1。In one embodiment, in the mixed solution of step (5), the volume ratio of the water phase to the oil phase is 1:3 to 3:1.
优选的,所述步骤(5)中水相和油相的体积比为1:1。Preferably, the volume ratio of the water phase to the oil phase in step (5) is 1:1.
在一种实施方式中,步骤(5)中加入所述固化剂后,进行搅拌,所述搅拌的转速为700~800rpm,所述搅拌时间为10~20min。In one embodiment, after adding the curing agent in step (5), stirring is performed, the stirring speed is 700 to 800 rpm, and the stirring time is 10 to 20 minutes.
优选的,所述步骤(5)中搅拌的转速为700rpm,所述搅拌时间为10min。Preferably, the stirring speed in step (5) is 700 rpm and the stirring time is 10 min.
在一种实施方式中,所述步骤(6)中湿微胶囊的处理方法为,将湿微胶囊在-80℃下预冷冻24h后,使用冷冻干燥法干燥,得到益生菌粉末。In one embodiment, the method for treating the wet microcapsules in step (6) is to pre-freeze the wet microcapsules at -80°C for 24 hours and then dry them using a freeze-drying method to obtain probiotic powder.
本发明还提供了一种益生菌微胶囊。The invention also provides a probiotic microcapsule.
本发明还提供了一种益生菌微胶囊在制备耐胃酸口服产品中的应用,其特征在于,所述产品包括食品、药品、保健品;所述保健品包括益生菌制剂。The present invention also provides an application of probiotic microcapsules in the preparation of gastric acid-resistant oral products, characterized in that the products include food, medicine, and health products; and the health products include probiotic preparations.
有益效果:Beneficial effects:
(1)本发明通过TEMPO媒介氧化体系对高直链淀粉进行氧化制备氧化高直链淀粉,并将其与海藻酸钠复配成为氧化淀粉-多糖的复合物,以此作为益生菌微胶囊的外壳,优化了微胶囊的核壳结构,与氧化高直链淀粉制备的乳液相比,本发明制备得到的含鼠李糖乳杆菌的微胶囊其稳定性和缓释效果均有所提高,pH响应性也有所增加;(1) The present invention oxidizes high-amylose starch by oxidizing high-amylose starch through a TEMPO-mediated oxidation system, and compounding the oxidized high-amylose starch with sodium alginate to form an oxidized starch-polysaccharide complex, which is used as the shell of probiotic microcapsules, thereby optimizing the core-shell structure of the microcapsules. Compared with the emulsion prepared by oxidizing high-amylose starch, the microcapsules containing Lactobacillus rhamnosus prepared by the present invention have improved stability and sustained release effect, and the pH responsiveness is also increased;
(2)本发明所得的益生菌微胶囊能够有效保护所包埋益生菌在贮藏期间的活性,相比未包埋的益生菌,本发明所得的益生菌微胶囊在储存28天后其益生菌的存活率提高了2.5倍,在胃液环境中的存活率提高了1倍,并且其在胃环境中的存活率能稳定在90%以上;另外在肠道环境中,相比高直链淀粉和普通氧化淀粉为壁材的益生菌微胶囊,本发明所得的益生菌微胶囊在4h内具有更好的缓释效果,提高了益生菌在肠道中的定植率;(2) The probiotic microcapsules obtained by the present invention can effectively protect the activity of the embedded probiotics during storage. Compared with the unencapsulated probiotics, the survival rate of the probiotics in the probiotic microcapsules obtained by the present invention is increased by 2.5 times after storage for 28 days, and the survival rate in the gastric fluid environment is increased by 1 times, and the survival rate in the gastric environment can be stabilized at more than 90%; in addition, in the intestinal environment, compared with the probiotic microcapsules with high-amylose starch and ordinary oxidized starch as the wall material, the probiotic microcapsules obtained by the present invention have a better sustained release effect within 4 hours, thereby improving the colonization rate of probiotics in the intestine;
(3)本发明所得的益生菌微胶囊的原料为氧化淀粉-多糖复合物,此复合物除了具有pH响应性和缓释效果外,还能够黏附于肠道表面,与高直链淀粉和普通氧化淀粉为壁材的益生菌微胶囊相比,本发明制备的益生菌微胶囊黏附率分别提高了1.32倍和1.74倍,更有利于益生菌定植肠道,并且提高了益生菌的利用率;(3) The raw material of the probiotic microcapsules obtained by the present invention is an oxidized starch-polysaccharide complex. In addition to having pH responsiveness and sustained release effect, the complex can also adhere to the intestinal surface. Compared with the probiotic microcapsules with high amylose starch and ordinary oxidized starch as wall materials, the adhesion rates of the probiotic microcapsules prepared by the present invention are increased by 1.32 times and 1.74 times, respectively, which is more conducive to the colonization of probiotics in the intestine and improves the utilization rate of probiotics;
(4)本发明将氧化高直链淀粉和植物或微生物来源的多糖作为微胶囊壁材,包埋益生菌制备微胶囊粉末,由于本发明使用了反相乳液法,使得微胶囊化的过程中条件温和,不涉及高温、高速搅拌、高压均质等工艺流程,能够有效地保护益生菌的活性,此外,本发明的工艺环节相对简单,原料廉价易得,有利于生产企业控制生产成本,提高生产效率。(4) The present invention uses oxidized high-amylose starch and polysaccharides from plants or microorganisms as microcapsule wall materials to encapsulate probiotics to prepare microcapsule powder. Since the present invention uses a reverse emulsion method, the conditions in the microencapsulation process are mild and do not involve high temperature, high-speed stirring, high-pressure homogenization and other process flows, which can effectively protect the activity of the probiotics. In addition, the process steps of the present invention are relatively simple, and the raw materials are cheap and easily available, which is beneficial for production enterprises to control production costs and improve production efficiency.
综上,本发明通过使用氧化高直链淀粉和植物或微生物来源的多糖共同作为微胶囊壁材,使用反相乳液的方法制备益生菌微胶囊,并采用CaCl2溶液进行固化,能够以较低成本和较为简单的工艺方法制得具有较高保护能力的益生菌微胶囊。In summary, the present invention uses oxidized high-amylose starch and polysaccharides from plants or microorganisms as microcapsule wall materials, uses an inverse emulsion method to prepare probiotic microcapsules, and uses CaCl2 solution for solidification, so that probiotic microcapsules with higher protection ability can be prepared at a lower cost and with a simpler process.
具体实施方式Detailed ways
本发明提供一种基于氧化高直链淀粉载体制备益生菌微胶囊的方法,包括以下步骤:The present invention provides a method for preparing probiotic microcapsules based on oxidized high-amylose starch carrier, comprising the following steps:
(1)将高直链淀粉氧化,得到氧化高直链淀粉;(1) oxidizing high-amylose starch to obtain oxidized high-amylose starch;
(2)将所述氧化高直链淀粉溶液与益生菌混合得到氧化淀粉-益生菌混合溶液,每100mL的氧化高直链淀粉溶液与3×108~3×1010cfu的益生菌混合;(2) mixing the oxidized high-amylose starch solution with probiotics to obtain an oxidized starch-probiotic mixed solution, wherein 3×10 8 to 3×10 10 cfu of probiotics are mixed with every 100 mL of the oxidized high-amylose starch solution;
(3)将多糖溶解于水中,得到浓度为2.0~3.0%的多糖溶液;(3) dissolving the polysaccharide in water to obtain a polysaccharide solution with a concentration of 2.0 to 3.0%;
(4)将步骤(2)制得的氧化淀粉-益生菌混合溶液与多糖溶液混合后,保持体系温度在40~50℃,调整体系pH在4.5~4.8,得到氧化淀粉-益生菌-多糖混合溶液;(4) after mixing the oxidized starch-probiotic mixed solution obtained in step (2) with the polysaccharide solution, maintaining the system temperature at 40-50° C., adjusting the system pH at 4.5-4.8, to obtain an oxidized starch-probiotic-polysaccharide mixed solution;
(5)取上述氧化淀粉-益生菌-多糖混合溶液2~4mL,在搅拌状态下缓慢加入油相,继续搅拌10~20min后,加入固化剂,继续搅拌10~20min。多次离心、生理盐水洗涤2~3次后获得湿微胶囊;(5) Take 2-4 mL of the above oxidized starch-probiotic-polysaccharide mixed solution, slowly add the oil phase under stirring, continue stirring for 10-20 minutes, add the curing agent, and continue stirring for 10-20 minutes. Centrifuge several times and wash with physiological saline 2-3 times to obtain wet microcapsules;
(6)将上述湿微胶囊冷冻干燥,得到益生菌微胶囊粉末;(6) freeze-drying the wet microcapsules to obtain probiotic microcapsule powder;
在本发明中,将高直链淀粉加入到沸水中混合均匀后冷却后再加入氧化剂2,2,6,6-四甲基-1-哌啶基氧基(TEMPO)和NaBr进行氧化,得到氧化高直链淀粉溶液。在本发明中,所述的高直链淀粉溶液的质量浓度为1~2g/100mL,进一步优选为1.6g/100mL。所述氧化物的添加量分别为高直链淀粉含量的0.8~0.9%和35~40%,分别进一步优选为0.85%和35%。所述氧化的pH条件为9.5~10,进一步优化为10。所述氧化的温度为4~5℃,进一步优选为4℃。所述搅拌的转速为500~700rpm,进一步优选为600rpm。搅拌时间为20~30min,进一步优选为20min。In the present invention, high-amylose starch is added to boiling water, mixed evenly, cooled, and then oxidized by adding oxidants 2,2,6,6-tetramethyl-1-piperidinyloxy (TEMPO) and NaBr to obtain an oxidized high-amylose starch solution. In the present invention, the mass concentration of the high-amylose starch solution is 1-2 g/100 mL, and more preferably 1.6 g/100 mL. The addition amount of the oxide is 0.8-0.9% and 35-40% of the high-amylose starch content, respectively, and more preferably 0.85% and 35%, respectively. The pH condition of the oxidation is 9.5-10, and further optimized to 10. The temperature of the oxidation is 4-5°C, and more preferably 4°C. The stirring speed is 500-700 rpm, and more preferably 600 rpm. The stirring time is 20-30 min, and more preferably 20 min.
本发明在获得氧化淀粉溶液后,将所述氧化淀粉溶液与益生菌混合得到氧化淀粉-益生菌混合溶液。在本发明中,所述益生菌是经冷冻保藏的益生菌培养物在4℃下离心,去除上清后获得,或使用灭菌后的生理盐水溶液洗涤2次后离心获得的益生菌菌泥或菌悬液;所述氧化高直链淀粉溶液与益生菌混合后需经磁力搅拌器使溶液混合均匀。After obtaining the oxidized starch solution, the present invention mixes the oxidized starch solution with probiotics to obtain an oxidized starch-probiotic mixed solution. In the present invention, the probiotics are obtained by centrifuging a frozen probiotic culture at 4°C and removing the supernatant, or by washing twice with a sterilized saline solution and then centrifuging to obtain a probiotic mud or suspension; after the oxidized high-amylose starch solution and the probiotics are mixed, a magnetic stirrer is used to mix the solution evenly.
在本发明中,将多糖溶解于水中,得到浓度为2.0~3.0%的多糖溶液,所述多糖溶液的浓度优化为2.0%。In the present invention, polysaccharide is dissolved in water to obtain a polysaccharide solution with a concentration of 2.0-3.0%, and the concentration of the polysaccharide solution is optimized to be 2.0%.
本发明在制备获得氧化淀粉-益生菌混合溶液与多糖溶液后,将二者混合得到氧化淀粉-益生菌-多糖混合溶液。在本发明中,所述氧化淀粉-益生菌混合溶液与多糖溶液混合时为等体积混合;所述混合后及调节体系pH后均需进行搅拌处理,所述搅拌处理的搅拌速度优选为600~800rpm,进一步优选为700rpm;本发明对氧化淀粉-益生菌混合溶液与多糖溶液混合后的搅拌时间没有特殊限定,以混合均匀为宜;所述调节体系pH后的搅拌时间优选为10~20min,进一步优选为15min;所述体系温度优选为保持在40~50℃,进一步优选为45℃;所述调节体系pH优选为4.5~5.0,进一步优选为4.7。After preparing the oxidized starch-probiotic mixed solution and the polysaccharide solution, the present invention mixes the two to obtain the oxidized starch-probiotic-polysaccharide mixed solution. In the present invention, the oxidized starch-probiotic mixed solution and the polysaccharide solution are mixed in equal volumes; stirring treatment is required after the mixing and after adjusting the pH of the system, and the stirring speed of the stirring treatment is preferably 600-800rpm, and more preferably 700rpm; the present invention does not specifically limit the stirring time after the oxidized starch-probiotic mixed solution and the polysaccharide solution are mixed, and it is advisable to mix evenly; the stirring time after adjusting the pH of the system is preferably 10-20min, and more preferably 15min; the temperature of the system is preferably maintained at 40-50°C, and more preferably 45°C; the pH of the adjustment system is preferably 4.5-5.0, and more preferably 4.7.
本发明在制备获得氧化淀粉-益生菌-多糖混合溶液后,将此水相加入到油相中继续搅拌10~20min后,加入固化剂,继续搅拌10~20min。多次离心、生理盐水洗涤2~3次后获得湿微胶囊。在本发明中,所述油相为Span80和大豆油的混合油相,所述混合油相中Span80的添加量为2.5~3%(w/v);进一步优选为2.5%(w/v)。本发明中的水相和油相比例为1:3~3:1,进一步优选为1:1。本发明所述水相加入到油相后的搅拌为磁力搅拌器搅拌,搅拌的转速为700~800rpm,进一步优选为700rpm;所述搅拌时间为10~20min;进一步优选为10min。After preparing the oxidized starch-probiotic-polysaccharide mixed solution, the present invention adds the aqueous phase to the oil phase and continues to stir for 10 to 20 minutes, then adds the curing agent and continues to stir for 10 to 20 minutes. Wet microcapsules are obtained after multiple centrifugation and 2 to 3 times of washing with physiological saline. In the present invention, the oil phase is a mixed oil phase of Span80 and soybean oil, and the amount of Span80 added to the mixed oil phase is 2.5 to 3% (w/v); more preferably 2.5% (w/v). The ratio of the aqueous phase to the oil phase in the present invention is 1:3 to 3:1, and more preferably 1:1. The stirring after the aqueous phase of the present invention is added to the oil phase is a magnetic stirrer stirring, and the stirring speed is 700 to 800 rpm, more preferably 700 rpm; the stirring time is 10 to 20 minutes; more preferably 10 minutes.
本发明在获得所述湿微胶囊后,将湿微胶囊冷冻干燥,得到益生菌粉末。在本发明中,对所述的湿微胶囊的冷冻干燥处理方法为,将湿微胶囊在-80℃下预冷冻12~36h,优选为24h。After obtaining the wet microcapsules, the present invention freeze-dries the wet microcapsules to obtain probiotic powder. In the present invention, the freeze-drying treatment method for the wet microcapsules is to pre-freeze the wet microcapsules at -80°C for 12 to 36 hours, preferably 24 hours.
本发明还提供了上述制备方法制备获得的益生菌微胶囊。所述获得的益生菌微胶囊具有产品尺寸较小,产品结构稳定性良好,易于在多种产品形态中添加,应用范围广泛的特点,尤其适合口服益生菌制剂在药品中添加和使用。本发明制得的益生菌微胶囊能够有效保护所包埋益生菌在贮藏期间的活性,且能够实现其在胃液环境中对所包埋益生菌的保护,添加于药品时,可将益生菌递送到肠道中并缓慢释放,能够很好地发挥益生菌的益生作用。The present invention also provides probiotic microcapsules prepared by the above-mentioned preparation method. The probiotic microcapsules obtained have the characteristics of small product size, good product structural stability, easy to add in a variety of product forms, and a wide range of applications, and are particularly suitable for oral probiotic preparations to be added and used in medicines. The probiotic microcapsules prepared by the present invention can effectively protect the activity of the embedded probiotics during storage, and can achieve the protection of the embedded probiotics in the gastric fluid environment. When added to the medicine, the probiotics can be delivered to the intestine and slowly released, and the probiotic effect of the probiotics can be well exerted.
本发明还提供了上述益生菌微胶囊在制备耐胃酸口服益生菌制剂中的应用。本发明对所述耐胃酸口服益生菌微胶囊制剂的剂型以及辅料没有特殊限定,采用本领域常规的益生菌剂型和辅料即可。The present invention also provides the use of the probiotic microcapsules in preparing a gastric acid-resistant oral probiotic preparation. The present invention has no special restrictions on the dosage form and excipients of the gastric acid-resistant oral probiotic microcapsule preparation, and conventional probiotic dosage forms and excipients in the art can be used.
下面结合实施例对本发明提供的技术方案进行详细的说明,但是不能把它们理解为对本发明保护范围的限定。The technical solutions provided by the present invention are described in detail below in conjunction with the embodiments, but they should not be construed as limiting the protection scope of the present invention.
实施例1一种基于氧化高直链淀粉载体制备鼠李糖乳杆菌微胶囊的方法Example 1 A method for preparing Lactobacillus rhamnosus microcapsules based on oxidized high-amylose starch carrier
具体制备方法如下:The specific preparation method is as follows:
(1)制备菌悬液:将冷冻保藏的鼠李糖乳杆菌LGG解冻后取100μL加入MRS液体培养基中,37℃培养36h活化后,再将活化后的鼠李糖乳杆菌LGG取100μL置于MRS液体培养基中,37℃培养24h后,培养物在4℃下离心,去除上清,获得3×108cfu/mL的鼠李糖乳杆菌悬液。(1) Preparation of bacterial suspension: 100 μL of the frozen Lactobacillus rhamnosus LGG was thawed and added to MRS liquid culture medium. After incubation at 37°C for 36 h, 100 μL of the activated Lactobacillus rhamnosus LGG was placed in MRS liquid culture medium. After incubation at 37°C for 24 h, the culture was centrifuged at 4°C and the supernatant was removed to obtain a Lactobacillus rhamnosus suspension of 3×10 8 cfu/mL.
(2)制备氧化高直链淀粉:将用作微胶囊壁材的高直链淀粉(上海源叶生物科技有限公司;货号:S27326;直链淀粉含量:90%)8.1g溶解于90℃的500mL水中,于加热磁力搅拌器中搅拌均匀后冷却至室温,称取0.0648g TEMPO和3.24g NaBr加入上述溶液中;将整个反应体系置于恒温磁力搅拌器,保持反应温度4℃,将pH调节至10,搅拌转速600rpm,搅拌20min反应完毕,使用3500Da透析袋流水透析3天。冷冻干燥后获得氧化度为10%的氧化高直链淀粉。(2) Preparation of oxidized high-amylose starch: 8.1 g of high-amylose starch (Shanghai Yuanye Biotechnology Co., Ltd.; product number: S27326; amylose content: 90%) used as microcapsule wall material was dissolved in 500 mL of water at 90°C, stirred evenly in a heated magnetic stirrer, and then cooled to room temperature. 0.0648 g of TEMPO and 3.24 g of NaBr were weighed and added to the above solution; the entire reaction system was placed in a constant temperature magnetic stirrer, the reaction temperature was maintained at 4°C, the pH was adjusted to 10, the stirring speed was 600 rpm, the reaction was stirred for 20 min, and the reaction was completed. A 3500Da dialysis bag was used for dialysis for 3 days. After freeze drying, an oxidized high-amylose starch with an oxidation degree of 10% was obtained.
(3)制备水相(3) Preparation of aqueous phase
分别称取上述氧化高直链淀粉和海藻酸钠粉末(青岛明月海藻集团有限公司;货号:MY-BCT-HZSN-1KG;纯度:90%)溶于无菌水中,制得浓度为1.6g/100mL的氧化高直链淀粉溶液和浓度为2g/100mL的海藻酸钠溶液。先将0.5mL氧化高直链淀粉溶液与200μL菌悬液混合,磁力搅拌器搅拌,转速700rpm,保持30min,制得氧化高直链淀粉-益生菌混合液,然后在其中加入0.5mL海藻酸钠溶液,磁力搅拌器搅拌,搅拌转速700rpm,搅拌时间30min,获得氧化淀粉-益生菌-多糖混合溶液,保持体系温度在45℃,调整体系pH在4.7,磁力搅拌器搅拌,搅拌转速700rpm,搅拌时间30min,得到氧化淀粉-益生菌-多糖混合溶液(水相)。所述水相中,氧化高直链淀粉终浓度为0.66g/100mL,多糖的终浓度为0.83g/100mL,益生菌的活菌数为5×107cfu/mL。The above-mentioned oxidized high-amylose starch and sodium alginate powder (Qingdao Mingyue Seaweed Group Co., Ltd.; Article No.: MY-BCT-HZSN-1KG; Purity: 90%) were weighed and dissolved in sterile water to prepare an oxidized high-amylose starch solution with a concentration of 1.6 g/100 mL and a sodium alginate solution with a concentration of 2 g/100 mL. First, 0.5 mL of the oxidized high-amylose starch solution was mixed with 200 μL of the bacterial suspension, stirred with a magnetic stirrer at a speed of 700 rpm for 30 min to prepare an oxidized high-amylose starch-probiotic mixed solution, and then 0.5 mL of the sodium alginate solution was added thereto, stirred with a magnetic stirrer at a stirring speed of 700 rpm for 30 min to obtain an oxidized starch-probiotic-polysaccharide mixed solution, the system temperature was maintained at 45 ° C, the system pH was adjusted to 4.7, the magnetic stirrer was stirred at a stirring speed of 700 rpm for 30 min to obtain an oxidized starch-probiotic-polysaccharide mixed solution (aqueous phase). In the aqueous phase, the final concentration of oxidized high-amylose starch was 0.66 g/100 mL, the final concentration of polysaccharide was 0.83 g/100 mL, and the number of viable probiotics was 5×10 7 cfu/mL.
(4)制备油相(4) Preparation of oil phase
将20mL大豆油中混合0.5g Span80,搅拌均匀获得油相。0.5 g of Span80 was mixed into 20 mL of soybean oil and stirred to obtain an oil phase.
(5)制备益生菌微胶囊:在温和搅拌状态下将水相缓慢加入油相中,磁力搅拌器搅拌,转速700rpm,室温下搅拌10min。随后,加入20mL 0.5M CaCl2溶液,继续搅拌10min。通过多次离心(2500rpm、5min)、生理盐水洗涤2~3次后获得湿益生菌微胶囊,将湿益生菌微胶囊在-80℃预冷冻24.0h后,使用冷冻干燥法干燥,得到鼠李糖乳杆菌微胶囊粉末。(5) Preparation of probiotic microcapsules: The aqueous phase was slowly added to the oil phase under gentle stirring, and the mixture was stirred with a magnetic stirrer at a speed of 700 rpm for 10 min at room temperature. Subsequently, 20 mL of 0.5 M CaCl 2 solution was added and stirring was continued for 10 min. Wet probiotic microcapsules were obtained by multiple centrifugation (2500 rpm, 5 min) and washing with physiological saline 2 to 3 times. The wet probiotic microcapsules were pre-frozen at -80°C for 24.0 h and then dried by freeze drying to obtain Lactobacillus rhamnosus microcapsule powder.
实施例2一种基于氧化高直链淀粉载体制备植物乳杆菌微胶囊的方法Example 2 A method for preparing Lactobacillus plantarum microcapsules based on oxidized high-amylose starch carrier
将实施例1中的鼠李糖乳杆菌替换为植物乳杆菌植物亚种SGBCC D14056,制得植物乳杆菌微胶囊粉末,其余步骤与实施例1相同。The Lactobacillus rhamnosus in Example 1 was replaced by Lactobacillus plantarum subspecies SGBCC D14056 to prepare Lactobacillus plantarum microcapsule powder. The remaining steps were the same as in Example 1.
实施例3一种基于氧化高直链淀粉载体制备干酪乳杆菌微胶囊的方法Example 3 A method for preparing Lactobacillus casei microcapsules based on oxidized high-amylose starch carrier
将实施例1中的鼠李糖乳杆菌替换为干酪乳杆菌JYLC-374,制得干酪乳杆菌微胶囊粉末,其余步骤与实施例1相同。The Lactobacillus rhamnosus in Example 1 was replaced by Lactobacillus casei JYLC-374 to prepare Lactobacillus casei microcapsule powder. The remaining steps were the same as in Example 1.
实施例4一种基于氧化高直链淀粉载体制备双歧杆菌微胶囊的方法Example 4 A method for preparing bifidobacterium microcapsules based on oxidized high-amylose starch carrier
将实施例1中的鼠李糖乳杆菌替换为乳双歧杆菌HN019,制得双歧杆菌微胶囊粉末,其余步骤与实施例1相同。The Lactobacillus rhamnosus in Example 1 was replaced by Bifidobacterium lactis HN019 to prepare Bifidobacterium microcapsule powder. The remaining steps were the same as in Example 1.
对比例1省略高直链淀粉的氧化操作Comparative Example 1 Omitting the oxidation operation of high amylose starch
具体实施方式参考实施例1,区别在于,将实施例1中的氧化高直链淀粉替换为未氧化的高直链淀粉(上海源叶生物科技有限公司;货号:S27326;直链淀粉含量为90%)作为微胶囊壁材原料,制备鼠李糖乳杆菌微胶囊粉末,其余步骤与实施例1相同。Specific implementation method Refer to Example 1, except that the oxidized high-amylose starch in Example 1 is replaced with unoxidized high-amylose starch (Shanghai Yuanye Biotechnology Co., Ltd.; Product No.: S27326; amylose content is 90%) as the raw material for microcapsule wall material to prepare Lactobacillus rhamnosus microcapsule powder, and the remaining steps are the same as Example 1.
对比例2降低氧化高直链淀粉的直链淀粉含量Comparative Example 2 Reducing the amylose content of oxidized high amylose starch
具体实施方式参考实施例1,区别在于,将实施例1中的氧化高直链淀粉(直链淀粉含量为90%)替换为普通氧化淀粉(直链淀粉含量为5%)作为微胶囊壁材原料,制备鼠李糖乳杆菌微胶囊粉末,其余步骤与实施例1相同。Specific implementation method Referring to Example 1, the difference is that the oxidized high-amylose starch (amylose content of 90%) in Example 1 is replaced by ordinary oxidized starch (amylose content of 5%) as the raw material of microcapsule wall material to prepare Lactobacillus rhamnosus microcapsule powder, and the remaining steps are the same as Example 1.
对比例3改变氧化高直链淀粉的氧化度Comparative Example 3: Changing the degree of oxidation of oxidized high-amylose starch
具体实施方式参考实施例1,区别在于,将实施例1中的氧化度为10%氧化高直链淀粉(直链淀粉含量为90%)替换为氧化度为4%的氧化高直链淀粉作为微胶囊壁材原料,制备鼠李糖乳杆菌微胶囊粉末,其余步骤与实施例1相同。其中,氧化度以羧基的质量分数表示,通过调节TEMPO的添加量来控制氧化高直链淀粉的氧化度。氧化度测量方法具体为,称取0.12g氧化高直链淀粉溶解于20mL沸水中,趁热加入2滴酚酞指示剂,用0.1mol/L NaOH溶液滴定至淡粉色,且半分钟内不变色,记录NaOH溶液的消耗量(V1,mL)。称取相同质量的氧化高直链淀粉重复上述操作,记录NaOH溶液的消耗量(V2,mL)。依据下式分别计算不同氧化高直链淀粉的氧化度。Specific implementation method Refer to Example 1, the difference is that the oxidized high-amylose starch (amylose content is 90%) with an oxidation degree of 10% in Example 1 is replaced by an oxidized high-amylose starch with an oxidation degree of 4% as the raw material of the microcapsule wall material to prepare the rhamnosus Lactobacillus microcapsule powder, and the remaining steps are the same as Example 1. Among them, the oxidation degree is expressed as the mass fraction of the carboxyl group, and the oxidation degree of the oxidized high-amylose starch is controlled by adjusting the amount of TEMPO added. The oxidation degree measurement method is specifically as follows: weigh 0.12g of oxidized high-amylose starch and dissolve it in 20mL of boiling water, add 2 drops of phenolphthalein indicator while hot, titrate with 0.1mol/L NaOH solution to light pink, and do not change color within half a minute, and record the consumption of NaOH solution (V1, mL). Weigh the same mass of oxidized high-amylose starch and repeat the above operation, and record the consumption of NaOH solution (V2, mL). The oxidation degrees of different oxidized high-amylose starches are calculated according to the following formula.
氧化度(%)=(((V_1-V_2)×C×0.045)/m)×100Oxidation degree (%) = (((V_1-V_2)×C×0.045)/m)×100
式中m为样品质量(g),C为NaOH溶液浓度,mol/L。Where m is the sample mass (g), C is the concentration of NaOH solution, mol/L.
对比例4省略添加氧化高直链淀粉Comparative Example 4: Omitting the addition of oxidized high-amylose starch
具体实施方式参考实施例1,区别在于,将实施例1中的氧化高直链淀粉(直链淀粉含量为90%)去除,仅以海藻酸钠作为微胶囊壁材原料,制备鼠李糖乳杆菌微胶囊粉末,其余步骤与实施例1相同。Specific implementation method Referring to Example 1, the difference is that the oxidized high-amylose starch (amylose content of 90%) in Example 1 is removed, and only sodium alginate is used as the raw material of microcapsule wall material to prepare Lactobacillus rhamnosus microcapsule powder. The remaining steps are the same as Example 1.
对比例5用磷酸化高直链淀粉替换氧化高直链淀粉Comparative Example 5: Replacing oxidized high-amylose starch with phosphorylated high-amylose starch
具体实施方式参考实施例1,区别在于,将实施例1中的氧化高直链淀粉(直链淀粉含量为90%)替换为磷酸化高直链淀粉作为微胶囊壁材原料,制备鼠李糖乳杆菌微胶囊粉末,其余步骤与实施例1相同。其中,磷酸钠化高直链淀粉的制备方法为,将80g高直链淀粉溶解于120mL去离子水中,加入混合磷酸盐(磷酸钠2.8g、磷酸二氢钠14.5g、磷酸氢二钠1.2g、)和硬脂酸聚氧化乙烯醚5g,调节pH5.5,53℃条件下80rpm/min搅拌10h后离心分离后气流干燥得到磷酸化高直链淀粉。Specific implementation method Refer to Example 1, the difference is that the oxidized high-amylose starch (amylose content of 90%) in Example 1 is replaced by phosphorylated high-amylose starch as the raw material of microcapsule wall material to prepare Lactobacillus rhamnosus microcapsule powder, and the remaining steps are the same as Example 1. Among them, the preparation method of sodium phosphate high-amylose starch is to dissolve 80g of high-amylose starch in 120mL of deionized water, add mixed phosphate (2.8g of sodium phosphate, 14.5g of sodium dihydrogen phosphate, 1.2g of disodium hydrogen phosphate) and 5g of stearic acid polyoxyethylene ether, adjust pH 5.5, stir at 80rpm/min at 53°C for 10h, centrifuge and air flow dry to obtain phosphorylated high-amylose starch.
实施例5微胶囊的结构表征Example 5 Structural Characterization of Microcapsules
本发明实施例1~4所得微胶囊为单层包埋结构,微胶囊平均粒径为300μm左右,是由氧化高直链淀粉和海藻酸钠交联而成。The microcapsules obtained in Examples 1 to 4 of the present invention are single-layer embedding structures, and the average particle size of the microcapsules is about 300 μm. The microcapsules are formed by cross-linking oxidized high-amylose starch and sodium alginate.
1、包封率检测1. Encapsulation rate detection
分别将实施例1~4和对比例1~5制得的益生菌微胶囊粉末溶解于生理盐水,制成终浓度为5%的溶液,用磷酸二氢钾缓冲液(0.05M,pH 6.8)分别与上述溶液以体积比1:4混合后,室温搅拌破碎0.5h,随后稀释涂布于MRS固体培养基,于37℃孵育2天后计数。计算益生菌微胶囊的包封率(EE,%):The probiotic microcapsule powders prepared in Examples 1 to 4 and Comparative Examples 1 to 5 were dissolved in physiological saline to prepare a solution with a final concentration of 5%, and potassium dihydrogen phosphate buffer (0.05M, pH 6.8) was mixed with the above solutions at a volume ratio of 1:4, stirred at room temperature for 0.5 h, and then diluted and coated on MRS solid culture medium, and counted after incubation at 37°C for 2 days. The encapsulation efficiency (EE, %) of the probiotic microcapsule was calculated as follows:
EE(%)=W2/W1×100%EE(%)=W2/W1×100%
式中W1表示包封前活菌LGG的总数量(CFU/mL),W2表示包封后微球释放的活菌LGG的数量(CFU/mL),结果如表1所示:Where W1 represents the total number of live LGG before encapsulation (CFU/mL), and W2 represents the number of live LGG released by the microspheres after encapsulation (CFU/mL). The results are shown in Table 1:
表1:不同鼠李糖乳杆菌微胶囊粉末的包封率Table 1: Encapsulation efficiency of different Lactobacillus rhamnosus microcapsule powders
结果显示,以氧化高直链淀粉作为微胶囊壁材,可以有效提高包括鼠李糖乳杆菌在内的几种常见益生菌的包封率,与使用未氧化的高直链淀粉作为微胶囊壁材相比,包封率提高2倍;与普通的氧化淀粉作为微胶囊壁材相比,包封率提高2倍;与低氧化度的氧化淀粉作为微胶囊壁材相比,包封率提高1.8倍;与未含有氧化高直链淀粉,仅以海藻酸钠作为微胶囊壁材相比,包封率提高了2倍;与磷酸化高直链淀粉作为微胶囊壁材相比,包封率提高了1.3倍。该实验结果表明,本发明制备的氧化高直链淀粉为壁材的益生菌微胶囊适用于一般益生菌的包埋,与本发明中的氧化高直链淀粉相比,未氧化的高直链淀粉、普通的氧化淀粉、低氧化度的氧化高直链淀粉、海藻酸钠和磷酸化高直链淀粉作为微胶囊壁材时,其包封率明显低于氧化高直链淀粉,本发明制备的益生菌微胶囊具有优异的包封率。The results showed that using oxidized high-amylose starch as microcapsule wall material can effectively improve the encapsulation rate of several common probiotics including Lactobacillus rhamnosus. Compared with using unoxidized high-amylose starch as microcapsule wall material, the encapsulation rate is increased by 2 times; compared with ordinary oxidized starch as microcapsule wall material, the encapsulation rate is increased by 2 times; compared with low-oxidized oxidized starch as microcapsule wall material, the encapsulation rate is increased by 1.8 times; compared with not containing oxidized high-amylose starch and only using sodium alginate as microcapsule wall material, the encapsulation rate is increased by 2 times; compared with phosphorylated high-amylose starch as microcapsule wall material, the encapsulation rate is increased by 1.3 times. The experimental results show that the probiotic microcapsules with oxidized high-amylose starch as the wall material prepared by the present invention are suitable for the encapsulation of general probiotics. Compared with the oxidized high-amylose starch in the present invention, the encapsulation rates of unoxidized high-amylose starch, ordinary oxidized starch, oxidized high-amylose starch with low oxidation degree, sodium alginate and phosphorylated high-amylose starch as microcapsule wall materials are significantly lower than those of oxidized high-amylose starch. The probiotic microcapsules prepared by the present invention have excellent encapsulation rates.
2、存活率检测2. Survival rate detection
将实施例1~4和对比例1~5制得的益生菌微胶囊粉末保存在25℃的环境中,检测28天内的存活率(%),The probiotic microcapsule powders prepared in Examples 1 to 4 and Comparative Examples 1 to 5 were stored in an environment of 25° C., and the survival rate (%) within 28 days was detected.
存活率的计算方法:(存活细菌数/总细菌数)×100%;The calculation method of survival rate: (number of surviving bacteria/total number of bacteria) × 100%;
活菌数测定方法:采用流式细胞仪分别测定保存前和保存过程中的活细菌数量,以此来计算益生菌微胶囊在25℃的环境中不同时间的存活率;Method for determination of viable bacteria count: flow cytometry was used to determine the number of viable bacteria before and during storage, so as to calculate the survival rate of probiotic microcapsules at different times in an environment of 25°C;
结果如表2所示:The results are shown in Table 2:
表2:不同益生菌微胶囊粉末在25℃环境下的存活率Table 2: Survival rate of different probiotic microcapsule powders at 25°C
结果显示,根据实施例1制备的益生菌微胶囊,其在7天、14天、21天和28天的存活率比根据实施例2制备的益生菌微胶囊的存活率高1.05倍、1.08倍、1.08倍和1.10倍;比根据实施例3制备的益生菌微胶囊的存活率高1.06倍、1.09倍、1.09倍和1.11倍;比根据实施例4制备的益生菌微胶囊的存活率高1.05倍、1.10倍、1.12倍和1.14倍,这表明氧化高直链淀粉作为益生菌微胶囊壁材时,包埋鼠李糖乳杆菌后的存活率比包埋其他益生菌后的存活率高,因此,本发明制备的基于氧化高直链淀粉的微胶囊材料更适合包埋鼠李糖乳杆菌。The results showed that the survival rates of the probiotic microcapsules prepared according to Example 1 at 7 days, 14 days, 21 days and 28 days were 1.05 times, 1.08 times, 1.08 times and 1.10 times higher than those of the probiotic microcapsules prepared according to Example 2; 1.06 times, 1.09 times, 1.09 times and 1.11 times higher than those of the probiotic microcapsules prepared according to Example 3; and 1.05 times, 1.10 times, 1.12 times and 1.14 times higher than those of the probiotic microcapsules prepared according to Example 4. This indicates that when oxidized high-amylose starch is used as the wall material of the probiotic microcapsules, the survival rate after encapsulating Lactobacillus rhamnosus is higher than that after encapsulating other probiotics. Therefore, the microcapsule material based on oxidized high-amylose starch prepared by the present invention is more suitable for encapsulating Lactobacillus rhamnosus.
另外,根据实施例1制备的益生菌微胶囊,其在7天、14天、21天和28天的存活率比根据对比例1制备的益生菌微胶囊的存活率高1.25倍、1.35倍、1.53倍和1.64倍,这表明作为益生菌微胶囊壁材,氧化后的高直链淀粉比未氧化的高直链淀粉对益生菌有更强的保护作用;根据实施例1制备的益生菌微胶囊,其在7天、14天、21天和28天的存活率比根据对比例2制备的益生菌微胶囊的存活率高1.37倍、1.51倍、1.71倍和1.82倍,这表明作为益生菌微胶囊壁材,氧化高直链淀粉比普通氧化淀粉对益生菌有更强的保护作用;根据实施例1制备的益生菌微胶囊,其在7天、14天、21天和28天的存活率比根据对比例3制备的益生菌微胶囊的存活率高1.24倍、1.34倍、1.47倍和1.56倍,这表明作为益生菌微胶囊壁材,高氧化度的氧化高直链淀粉比低氧化度的氧化高直链淀粉对益生菌有更强的保护作用;根据实施例1制备的益生菌微胶囊,其在7天、14天、21天和28天的存活率比根据对比例4制备的益生菌微胶囊的存活率高1.46倍、1.63倍、1.80倍和2.0倍,这表明作为益生菌微胶囊壁材,氧化高直链淀粉和海藻酸钠的复合材料比海藻酸钠对益生菌有更好的保护作用;根据实施例1制备的益生菌微胶囊,其在7天、14天、21天和28天的存活率比根据对比例5制备的益生菌微胶囊的存活率高1.21倍、1.29倍、1.32倍和1.40倍,这表明作为益生菌微胶囊壁材,氧化高直链淀粉比磷酸化高直链淀粉对益生菌有更好的保护作用。根据实施例1制备的益生菌微胶囊,其在7天、14天、21天和28天的存活率比未包埋的益生菌微胶囊的存活率高1.67倍、1.86倍、2.07倍和2.52倍。该实验结果表明,本发明所制备的益生菌微胶囊能够在常温条件下确保益生菌的存活率,氧化后的高直链淀粉能够有效提升微胶囊对益生菌的保护能力。In addition, the survival rate of the probiotic microcapsules prepared according to Example 1 at 7 days, 14 days, 21 days and 28 days was 1.25 times, 1.35 times, 1.53 times and 1.64 times higher than that of the probiotic microcapsules prepared according to Comparative Example 1, which indicates that as a wall material for probiotic microcapsules, oxidized high-amylose starch has a stronger protective effect on probiotics than unoxidized high-amylose starch; the probiotic microcapsules prepared according to Example 1 at 7 days, 14 days, 21 days and 28 days were 1.25 times, 1.35 times, 1.53 times and 1.64 times higher than that of the probiotic microcapsules prepared according to Comparative Example 1, which indicates that as a wall material for probiotic microcapsules, oxidized high-amylose starch has a stronger protective effect on probiotics than unoxidized high-amylose starch; The survival rates of the probiotic microcapsules prepared according to Example 1 at 7 days, 14 days, 21 days and 28 days were 1.37 times, 1.51 times, 1.71 times and 1.82 times higher than those of the probiotic microcapsules prepared according to Comparative Example 2, which indicates that oxidized high-amylose starch has a stronger protective effect on probiotics than ordinary oxidized starch as a wall material for probiotic microcapsules; the survival rates of the probiotic microcapsules prepared according to Example 1 at 7 days, 14 days, 21 days and 28 days were 1.24 times, 1.34 times and 1.6 times higher than those of the probiotic microcapsules prepared according to Comparative Example 3. times, 1.47 times and 1.56 times, which shows that as a wall material for probiotic microcapsules, oxidized high-amylose starch with a high oxidation degree has a stronger protective effect on probiotics than oxidized high-amylose starch with a low oxidation degree; the survival rate of the probiotic microcapsules prepared according to Example 1 at 7 days, 14 days, 21 days and 28 days is 1.46 times, 1.63 times, 1.80 times and 2.0 times higher than that of the probiotic microcapsules prepared according to Comparative Example 4, which shows that as a wall material for probiotic microcapsules , the composite material of oxidized high-amylose starch and sodium alginate has a better protective effect on probiotics than sodium alginate; the survival rate of the probiotic microcapsules prepared according to Example 1 at 7 days, 14 days, 21 days and 28 days is 1.21 times, 1.29 times, 1.32 times and 1.40 times higher than that of the probiotic microcapsules prepared according to Comparative Example 5, which shows that as a wall material for probiotic microcapsules, oxidized high-amylose starch has a better protective effect on probiotics than phosphorylated high-amylose starch. The probiotic microcapsules prepared according to Example 1 have a survival rate of 1.67 times, 1.86 times, 2.07 times and 2.52 times higher than that of the unembedded probiotic microcapsules at 7 days, 14 days, 21 days and 28 days. The experimental results show that the probiotic microcapsules prepared by the present invention can ensure the survival rate of probiotics under normal temperature conditions, and the oxidized high-amylose starch can effectively improve the protection ability of the microcapsules to probiotics.
3、胃液耐受性检测3. Gastric juice tolerance test
将实施例1~4和对比例1~5制得的益生菌微胶囊加入无菌人工胃液(上海源叶生物科技有限公司,pH=2.0)中,制备益生菌胶囊含量为0.1g/ml的溶液,于37℃、150rpm水浴震荡孵育2h进行胃环境模拟。随后用生理盐水稀释涂布于MRS固体培养基上,于37℃孵育2天后计数。计算益生菌的存活率(%),结果如表3所示:The probiotic microcapsules prepared in Examples 1 to 4 and Comparative Examples 1 to 5 were added to sterile artificial gastric juice (Shanghai Yuanye Biotechnology Co., Ltd., pH = 2.0) to prepare a solution with a probiotic capsule content of 0.1 g/ml, and incubated at 37°C, 150 rpm in a water bath for 2 hours to simulate the gastric environment. Subsequently, the solution was diluted with physiological saline and coated on MRS solid culture medium, and counted after incubation at 37°C for 2 days. The survival rate (%) of the probiotics was calculated, and the results are shown in Table 3:
表3:不同益生菌微胶囊粉末在人工胃液中的存活率Table 3: Survival rates of different probiotic microcapsule powders in artificial gastric juice
结果显示,根据实施例1制备的益生菌微胶囊在人工胃液中,10min、20min、30min和40min的存活率比根据实施例2制备的益生菌微胶囊存活率高1.01倍、1.03倍、1.08倍和1.18倍;比根据实施例3制备的益生菌微胶囊存活率高1.01倍、1.02倍、1.07倍和1.19倍;比根据实施例4制备的益生菌微胶囊存活率高1.01倍、1.03倍、1.08倍和1.18倍。显然,在人工胃液中,鼠李糖乳杆菌的存活率高于其他三种益生菌,这说明在基于氧化高直链淀粉制备的益生菌微胶囊中,氧化高直链淀粉对鼠李糖乳杆菌的保护作用高于其他三种益生菌,因此氧化高直链淀粉更适合作为鼠李糖乳杆菌的微胶囊材料,能更好的保护鼠李糖乳杆菌。The results show that the survival rates of the probiotic microcapsules prepared according to Example 1 in artificial gastric juice at 10min, 20min, 30min and 40min are 1.01 times, 1.03 times, 1.08 times and 1.18 times higher than those of the probiotic microcapsules prepared according to Example 2; 1.01 times, 1.02 times, 1.07 times and 1.19 times higher than those of the probiotic microcapsules prepared according to Example 3; 1.01 times, 1.03 times, 1.08 times and 1.18 times higher than those of the probiotic microcapsules prepared according to Example 4. Obviously, in artificial gastric juice, the survival rate of Lactobacillus rhamnosus is higher than that of the other three probiotics, which indicates that in the probiotic microcapsules prepared based on oxidized high-amylose starch, the protective effect of oxidized high-amylose starch on Lactobacillus rhamnosus is higher than that of the other three probiotics, so oxidized high-amylose starch is more suitable as a microcapsule material for Lactobacillus rhamnosus and can better protect Lactobacillus rhamnosus.
另外,根据实施例1制备的益生菌微胶囊在人工胃液中,10min、20min、30min和40min的存活率比根据对比例1制备的益生菌微胶囊存活率高1.01倍、1.06倍、1.15倍和1.34倍,这表明在人工胃液中,相比未氧化高直链淀粉,氧化高直链淀粉对鼠李糖乳杆菌有更有效的保护作用;根据实施例1制备的益生菌微胶囊在人工胃液中,10min、20min、30min和40min的存活率比根据对比根据对比例2制备的益生菌微胶囊存活率高1.02倍、1.08倍、1.22倍和1.4倍,这表明在人工胃液中,相比普通氧化淀粉,氧化高直链淀粉对鼠李糖乳杆菌有更有效的保护作用;根据实施例1制备的益生菌微胶囊在人工胃液中,10min、20min、30min和40min的存活率比根据对比根据对比例3制备的益生菌微胶囊存活率高1.01倍、1.05倍、1.12倍和1.27倍,这表明在人工胃液中,相比低氧化度的氧化高直链淀粉,高氧化度的氧化高直链淀粉对鼠李糖乳杆菌有更有效的保护作用;根据实施例1制备的益生菌微胶囊在人工胃液中,10min、20min、30min和40min的存活率比根据对比根据对比例4制备的益生菌微胶囊存活率高1.03倍、1.10倍、1.27倍和1.44倍,这表明在人工胃液中,相比海藻酸钠,氧化高直链淀粉和海藻酸钠的复合物对鼠李糖乳杆菌有更有效的保护作用;根据实施例1制备的益生菌微胶囊在人工胃液中,10min、20min、30min和40min的存活率比根据对比根据对比例5制备的益生菌微胶囊存活率高1.01倍、1.03倍、1.08倍和1.19倍,这表明在人工胃液中,相比磷酸化高直链淀粉,氧化高直链淀粉对鼠李糖乳杆菌有更有效的保护作用。根据实施例1制备的益生菌微胶囊在人工胃液中,10min、20min、30min和40min的存活率比未包埋的益生菌微胶囊存活率高1.29倍、1.42倍、1.71倍和1.94倍。该实验结果表明,在37℃的模拟胃液环境中,本发明所制备的益生菌微胶囊壁材层可以在40min内对益生菌起到更有效的防护作用,也就意味着益生菌具备较好的人工胃液耐受能力。In addition, the survival rates of the probiotic microcapsules prepared according to Example 1 in artificial gastric juice at 10 min, 20 min, 30 min and 40 min were 1.01 times, 1.06 times, 1.15 times and 1.34 times higher than those of the probiotic microcapsules prepared according to Comparative Example 1, which indicates that in artificial gastric juice, oxidized high-amylose starch has a more effective protective effect on Lactobacillus rhamnosus than unoxidized high-amylose starch; ... The survival rates of the probiotic microcapsules prepared according to Example 1 at 10 min, 20 min, 30 min and 40 min in artificial gastric juice were 1.02 times, 1.08 times, 1.22 times and 1.4 times higher than those of the probiotic microcapsules prepared according to Comparative Example 2, which indicates that in artificial gastric juice, compared with ordinary oxidized starch, oxidized high-amylose starch has a more effective protective effect on Lactobacillus rhamnosus; the survival rates of the probiotic microcapsules prepared according to Example 1 at 10 min, 20 min, 30 min and 40 min in artificial gastric juice were 1.01 times, 1.08 times, 1.22 times and 1.4 times higher than those of the probiotic microcapsules prepared according to Comparative Example 3. .05 times, 1.12 times and 1.27 times, which shows that in artificial gastric juice, compared with oxidized high-amylose starch with low oxidation degree, oxidized high-amylose starch with high oxidation degree has a more effective protective effect on Lactobacillus rhamnosus; the survival rate of the probiotic microcapsules prepared according to Example 1 in artificial gastric juice at 10min, 20min, 30min and 40min is 1.03 times, 1.10 times, 1.27 times and 1.44 times higher than that of the probiotic microcapsules prepared according to Comparative Example 4, which shows that in artificial gastric juice, compared with Sodium alginate, oxidized high-amylose starch and sodium alginate complex have more effective protective effects on Lactobacillus rhamnosus; the survival rates of the probiotic microcapsules prepared according to Example 1 in artificial gastric juice at 10min, 20min, 30min and 40min are 1.01 times, 1.03 times, 1.08 times and 1.19 times higher than those of the probiotic microcapsules prepared according to Comparative Example 5, which indicates that in artificial gastric juice, oxidized high-amylose starch has a more effective protective effect on Lactobacillus rhamnosus than phosphorylated high-amylose starch. The survival rates of the probiotic microcapsules prepared according to Example 1 in artificial gastric juice at 10min, 20min, 30min and 40min are 1.29 times, 1.42 times, 1.71 times and 1.94 times higher than those of the unencapsulated probiotic microcapsules. The experimental results show that in a simulated gastric fluid environment at 37°C, the wall material layer of the probiotic microcapsule prepared by the present invention can provide more effective protection for the probiotics within 40 minutes, which means that the probiotics have better tolerance to artificial gastric fluid.
4、人工肠液中的释放性能表征4. Characterization of release performance in artificial intestinal fluid
将实施例1~4和对比例1~5制得的益生菌微胶囊加入无菌人工肠液(上海源叶生物科技有限公司,pH=6.8)中,制得益生菌微胶囊含量为0.1g/ml的溶液,于37℃、150rpm水浴震荡孵育3h进行肠环境模拟,在1、2、3、4h时分别取样500μL,用生理盐水稀释涂布于MRS固体培养基上,于37℃孵育2天后计数。考察鼠李糖乳杆菌的的释放性能(以活菌数logcfu/g计算),结果如表4所示:The probiotic microcapsules prepared in Examples 1 to 4 and Comparative Examples 1 to 5 were added to sterile artificial intestinal fluid (Shanghai Yuanye Biotechnology Co., Ltd., pH = 6.8) to prepare a solution with a probiotic microcapsule content of 0.1 g/ml, and incubated at 37°C, 150 rpm in a water bath for 3 h to simulate the intestinal environment. 500 μL of samples were taken at 1, 2, 3, and 4 h, respectively, diluted with physiological saline and coated on MRS solid culture medium, and counted after incubation at 37°C for 2 days. The release performance of Lactobacillus rhamnosus (calculated as viable count logcfu/g) was investigated, and the results are shown in Table 4:
表4:不同益生菌微胶囊粉末在人工肠液中的释放性能(每小时内的释放量)Table 4: Release performance of different probiotic microcapsule powders in artificial intestinal fluid (release amount per hour)
结果显示,实施例1~4中的益生菌微胶囊在模拟肠液中,1h~4h内每小时益生菌释放率呈现缓慢增加的状态。在模拟肠液环境中,氧化高直链淀粉作为微胶囊的壁材层可以实现对所固定益生菌的缓慢释放,有助于益生菌在肠道中的定植。这是因为益生菌微胶囊释放速率越慢,益生菌在肠道中的定植时间越长,从而能够更好地发挥益生菌的功能。这表明,基于氧化高直链淀粉制备的益生菌微胶囊在人工肠液中具有缓慢释放的效果,可以帮助益生菌在肠道内的定植。对比例1~3中的益生菌微胶囊在模拟肠液中,1h~4h内每小时益生菌释放率呈现先增加后减小的状态;对比例4中的益生菌微胶囊在模拟肠液中,1h~4h内每小时益生菌释放率呈现逐步减小的状态。而益生菌微胶囊释放率先快后慢和逐步递减存在不足之处。首先,释放速率先快后慢会导致益生菌在肠道中的定植不均匀,部分益生菌会在肠道中过早释放或者过量释放,而另一部分益生菌则无法充分释放和定植。这种不均匀的释放速率会影响益生菌的生存和功能发挥;其次,逐步递减的释放速率会导致益生菌在肠道中的停留时间不足,无法达到长期稳定的定植效果。因此益生菌需要在肠道中持续一定的时间才能够有效地发挥调节肠道菌群的作用,而释放速率逐步递减可能会导致部分益生菌在肠道中的停留时间过短,影响其生长和繁殖。这表明,基于氧化高直链淀粉与海藻酸钠的复合物的益生菌微胶囊在人工肠液中益生菌的释放效果比基于未氧化的高直链淀粉、普通淀粉、低氧化度的氧化高直链淀粉和海藻酸钠的益生菌微胶囊的释放效果更优异,更有利于益生菌在肠道中的定植。虽然对比例5中的益生菌微胶囊在模拟肠液中,1h~4h内每小时益生菌释放率也呈现逐步增加的状态,但其释放速率过于缓慢,这会导致益生菌的释放量不足或需要更长时间才能释放,从而影响益生菌的作用效果和稳定性,因此,基于氧化高直链淀粉的鼠李糖乳杆菌微胶囊比基于磷酸化高直链淀粉为壁材的鼠李糖乳杆菌微胶囊更适合鼠李糖乳杆菌在肠道中的释放和定植。The results show that the probiotic microcapsules in Examples 1 to 4 show a slowly increasing probiotic release rate per hour within 1h to 4h in the simulated intestinal fluid. In the simulated intestinal fluid environment, oxidized high-amylose starch as the wall material layer of the microcapsule can achieve the slow release of the fixed probiotics, which is helpful for the colonization of the probiotics in the intestine. This is because the slower the release rate of the probiotic microcapsules, the longer the colonization time of the probiotics in the intestine, so that the function of the probiotics can be better exerted. This shows that the probiotic microcapsules prepared based on oxidized high-amylose starch have a slow release effect in artificial intestinal fluid, which can help the colonization of probiotics in the intestine. In the simulated intestinal fluid, the probiotic microcapsules in Comparative Examples 1 to 3 show a state of first increasing and then decreasing in the hourly probiotic release rate within 1h to 4h; the probiotic microcapsules in Comparative Example 4 show a state of gradually decreasing in the hourly probiotic release rate within 1h to 4h in the simulated intestinal fluid. However, the probiotic microcapsules have the disadvantages of first fast and then slow release and gradual decrease. First, the release rate is fast at first and then slow, which will lead to uneven colonization of probiotics in the intestine. Some probiotics will be released prematurely or excessively in the intestine, while other probiotics cannot be fully released and colonized. This uneven release rate will affect the survival and function of probiotics; secondly, the gradually decreasing release rate will lead to insufficient residence time of probiotics in the intestine, and it is impossible to achieve a long-term and stable colonization effect. Therefore, probiotics need to stay in the intestine for a certain period of time to effectively play the role of regulating intestinal flora, and the gradually decreasing release rate may cause some probiotics to stay in the intestine for too short a time, affecting their growth and reproduction. This shows that the probiotic microcapsules based on the complex of oxidized high-amylose starch and sodium alginate have a better release effect on probiotics in artificial intestinal fluid than the probiotic microcapsules based on unoxidized high-amylose starch, ordinary starch, low-oxidized oxidized high-amylose starch and sodium alginate, and are more conducive to the colonization of probiotics in the intestine. Although the probiotic microcapsules in Comparative Example 5 also showed a gradually increasing probiotic release rate within 1 h to 4 h in the simulated intestinal fluid, the release rate was too slow, which would result in insufficient probiotic release or require a longer time to release, thereby affecting the effect and stability of the probiotics. Therefore, the Lactobacillus rhamnosus microcapsules based on oxidized high-amylose starch were more suitable for the release and colonization of Lactobacillus rhamnosus in the intestine than the Lactobacillus rhamnosus microcapsules based on phosphorylated high-amylose starch as the wall material.
5、体外肠道粘液黏附表征5. In vitro intestinal mucus adhesion characterization
将实施例1~4和对比例1~5所述的益生菌微胶囊进行体外肠道粘液黏附实验,具体方法为:在无菌操作台中,将雄性大鼠肠道刨开,取4份1.5cm×1.5cm×2mm的肠道于无菌载玻片上,分别滴加50μL鼠李糖乳杆菌菌悬液(空白组)、实施例1~4益生菌微胶囊和对比例1~5益生菌微胶囊,并将其分别置于灭菌的离心管中,置于37℃水浴振荡器中振荡2h后取出,用300μL生理盐水冲洗,收集冲洗液进行梯度稀释,并计数活菌数,根据以下公式计算黏附率,结果如表5所示。The probiotic microcapsules described in Examples 1 to 4 and Comparative Examples 1 to 5 were subjected to an in vitro intestinal mucus adhesion experiment. The specific method was as follows: on a sterile operating table, the intestines of male rats were cut open, and 4 portions of 1.5 cm×1.5 cm×2 mm of the intestines were taken on a sterile glass slide, and 50 μL of Lactobacillus rhamnosus suspension (blank group), probiotic microcapsules of Examples 1 to 4, and probiotic microcapsules of Comparative Examples 1 to 5 were added dropwise, respectively, and placed in sterilized centrifuge tubes, placed in a 37°C water bath oscillator for 2 hours, and then taken out, rinsed with 300 μL of physiological saline, the rinse fluid was collected for gradient dilution, and the number of viable bacteria was counted. The adhesion rate was calculated according to the following formula, and the results are shown in Table 5.
黏附率(%)=(总益生菌数-未黏附的益生菌数)/总益生菌数×100%Adhesion rate (%) = (total number of probiotics - number of unadhered probiotics) / total number of probiotics × 100%
表5不同益生菌微胶囊在体外肠道中的黏附率Table 5 Adhesion rate of different probiotic microcapsules in the intestine in vitro
结果显示,本发明制备的鼠李糖乳杆菌微胶囊(实施例1)在肠道中的黏附率达到83.78%,比实施例2高1.15倍,比实施例3高1.16倍,比实施例4高1.15倍。显然,基于氧化高直链淀粉的鼠李糖乳杆菌微胶囊比其他三种同样外壳的益生菌微胶囊在肠道中的黏附率高,这说明氧化高直链淀粉更适合作为包埋鼠李糖乳杆菌的壁材。The results show that the adhesion rate of the Lactobacillus rhamnosus microcapsules (Example 1) prepared by the present invention in the intestine reaches 83.78%, which is 1.15 times higher than that of Example 2, 1.16 times higher than that of Example 3, and 1.15 times higher than that of Example 4. Obviously, the adhesion rate of the Lactobacillus rhamnosus microcapsules based on oxidized high-amylose starch in the intestine is higher than that of the other three probiotic microcapsules with the same shell, which indicates that the oxidized high-amylose starch is more suitable as a wall material for encapsulating Lactobacillus rhamnosus.
本发明制备的鼠李糖乳杆菌微胶囊(实施例1)在肠道中的黏附率比对比例1高1.32倍,说明与未氧化的高直链淀粉相比,氧化高直链淀粉作为益生菌微胶囊外壳会在肠道中有更高的黏附率。本发明制备的鼠李糖乳杆菌微胶囊(实施例1)在肠道中的黏附率比对比例2高1.74倍,说明与普通的氧化淀粉相比,氧化高直链淀粉作为益生菌微胶囊外壳会在肠道中有更高的黏附率。本发明制备的鼠李糖乳杆菌微胶囊(实施例1)在肠道中的黏附率比对比例3高1.23倍,说明与低氧化度的氧化高直链淀粉相比,高氧化度的氧化高直链淀粉作为益生菌微胶囊外壳会在肠道中有更高的黏附率。本发明制备的鼠李糖乳杆菌微胶囊(实施例1)在肠道中的黏附率比对比例4高1.84倍,说明与海藻酸钠相比,氧化高直链淀粉与海藻酸钠的复合物作为益生菌微胶囊外壳会在肠道中有更高的黏附率。本发明制备的鼠李糖乳杆菌微胶囊(实施例1)在肠道中的黏附率比对比例5高1.20倍。说明与磷酸化高直链淀粉相比,氧化高直链淀粉作为益生菌微胶囊外壳会在肠道中有更高的黏附率。该实验结果表明,以氧化高直链淀粉作为壁材的益生菌微胶囊,其在肠道中的黏附效果更好。进一步地,综合肠道模拟实验结果表明,氧化高直链淀粉作为壁材的益生菌微胶囊更有利于益生菌在肠道中的缓释和定植。The adhesion rate of the Lactobacillus rhamnosus microcapsules (Example 1) prepared by the present invention in the intestine is 1.32 times higher than that of Comparative Example 1, indicating that compared with unoxidized high-amylose starch, oxidized high-amylose starch as the shell of probiotic microcapsules will have a higher adhesion rate in the intestine. The adhesion rate of the Lactobacillus rhamnosus microcapsules (Example 1) prepared by the present invention in the intestine is 1.74 times higher than that of Comparative Example 2, indicating that compared with ordinary oxidized starch, oxidized high-amylose starch as the shell of probiotic microcapsules will have a higher adhesion rate in the intestine. The adhesion rate of the Lactobacillus rhamnosus microcapsules (Example 1) prepared by the present invention in the intestine is 1.23 times higher than that of Comparative Example 3, indicating that compared with low-oxidized oxidized high-amylose starch, high-oxidized oxidized high-amylose starch as the shell of probiotic microcapsules will have a higher adhesion rate in the intestine. The adhesion rate of the Lactobacillus rhamnosus microcapsules (Example 1) prepared by the present invention in the intestine is 1.84 times higher than that of Comparative Example 4, indicating that compared with sodium alginate, the complex of oxidized high-amylose starch and sodium alginate as the shell of probiotic microcapsules will have a higher adhesion rate in the intestine. The adhesion rate of the Lactobacillus rhamnosus microcapsules (Example 1) prepared by the present invention in the intestine is 1.20 times higher than that of Comparative Example 5. It is shown that compared with phosphorylated high-amylose starch, oxidized high-amylose starch as the shell of probiotic microcapsules will have a higher adhesion rate in the intestine. The experimental results show that the probiotic microcapsules with oxidized high-amylose starch as the wall material have better adhesion effect in the intestine. Furthermore, the comprehensive intestinal simulation experiment results show that the probiotic microcapsules with oxidized high-amylose starch as the wall material are more conducive to the sustained release and colonization of probiotics in the intestine.
虽然本发明已以较佳实施例公开如上,但其并非用以限定本发明,任何熟悉此技术的人,在不脱离本发明的精神和范围内,都可做各种的改动与修饰,因此本发明的保护范围应该以权利要求书所界定的为准。Although the present invention has been disclosed as above in the preferred embodiment, it is not intended to limit the present invention. Anyone familiar with this technology can make various changes and modifications without departing from the spirit and scope of the present invention. Therefore, the scope of protection of the present invention should be based on the definition of the claims.
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