CN107502631A - A kind of production method of candida utili β D glucans - Google Patents
A kind of production method of candida utili β D glucans Download PDFInfo
- Publication number
- CN107502631A CN107502631A CN201710898784.8A CN201710898784A CN107502631A CN 107502631 A CN107502631 A CN 107502631A CN 201710898784 A CN201710898784 A CN 201710898784A CN 107502631 A CN107502631 A CN 107502631A
- Authority
- CN
- China
- Prior art keywords
- candida utilis
- potato juice
- deproteinized
- glucan
- aqueous solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P19/00—Preparation of compounds containing saccharide radicals
- C12P19/04—Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds
- C12P19/08—Dextran
Landscapes
- Organic Chemistry (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Zoology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Microbiology (AREA)
- General Chemical & Material Sciences (AREA)
- Biotechnology (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Genetics & Genomics (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
Abstract
Description
技术领域technical field
本发明属于生物学领域,涉及一种产朊假丝酵母β-D-葡聚糖的生产方法。The invention belongs to the field of biology and relates to a production method of Candida utilis β-D-glucan.
背景技术Background technique
产朊假丝酵母与啤酒酵母、克鲁维酵母一起被许多国家认证为一种可作为食品添加剂的微生物,也是中国卫生部门允许的可用于保健食品的微生物,可利用工业废液,在培养基中不需要加入任何生长因子即可生长。Candida utilis, together with Saccharomyces cerevisiae and Kluyveromyces, has been certified as a microorganism that can be used as a food additive by many countries, and it is also a microorganism that can be used in health food permitted by the Chinese health department. can grow without adding any growth factors.
酵母β-葡聚糖是酵母细胞壁的结构多糖。它们具有不同的功能特性,如医疗,制药,食品,化妆品等行业。它们也可以作为免疫反应的生物修饰剂。除此之外,它们也有利于抗菌抗炎反应;促进霉毒素的吸收;减少低密度脂蛋白中的胆固醇颗粒等作用;还具有抗癌、抗诱变、抗氧化以及促进伤口愈合的特性。Yeast beta-glucan is a structural polysaccharide of the yeast cell wall. They have different functional properties, such as medical, pharmaceutical, food, cosmetic and other industries. They can also act as biological modifiers of the immune response. In addition, they are also beneficial to antibacterial and anti-inflammatory reactions; promote the absorption of mycotoxins; reduce cholesterol particles in low-density lipoproteins; they also have anti-cancer, anti-mutagenic, anti-oxidative and wound-healing properties.
目前国内生产酵母β-D-葡聚糖的酵母菌培养方法主要采用配制碳氮源或酵母浸出粉胨葡萄糖培养基,这样存在培养基成本高等缺点,且如果是生产过程中配制碳氮比,那么由于酵母菌种所需碳氮比等营养条件较为繁琐,因此存在研究工作量较大等问题,并且现有大部分文献中酵母β-D-葡聚糖的产率、得率和纯度都比较低,分别最高仅为80%、17%和86%。At present, the yeast culture method for producing yeast β-D-glucan in China mainly adopts the preparation of carbon and nitrogen sources or yeast extract powder peptone glucose medium, which has disadvantages such as high cost of the medium, and if the carbon-nitrogen ratio is prepared during the production process, Since the nutritional conditions such as the carbon-to-nitrogen ratio required by yeast strains are relatively complicated, there are problems such as a large research workload, and the yield, yield and purity of yeast β-D-glucan in most of the existing literature are all low. Relatively low, the highest is only 80%, 17% and 86%.
发明内容Contents of the invention
本发明的目的是为了解决上述的酵母β-D-葡聚糖生产方法中存在的生产成本高,研究工作量大等技术问题而提供一种产朊假丝酵母β-D-葡聚糖的生产方法,该生产方法可以利用废弃土豆汁经去蛋白后作为培养基,从而解决了现有技术中培养酵母菌要利用大量碳源和氮源且探索过程较为繁琐,从而大大的降低了工作量,同时降低了生产成本,同时变废为宝,符合绿色生产需求,并且最终得到高产量的产朊假丝酵母,产朊假丝酵母β-D-葡聚糖的产率最高可达87%,得率最高可达19%,纯度最高可达97%。The purpose of the present invention is to provide a kind of production method of Candida utilis β-D-glucan in order to solve technical problems such as high production cost and large research workload in the above-mentioned yeast β-D-glucan production method. The production method, which can use waste potato juice as a medium after deproteinization, thereby solving the problem that in the prior art, a large amount of carbon and nitrogen sources are used for cultivating yeast and the exploration process is relatively cumbersome, thereby greatly reducing the workload. , at the same time reduce the production cost, and turn waste into treasure, meet the needs of green production, and finally get a high yield of Candida utilis, the highest yield of Candida utilis β-D-glucan can reach 87% , the highest yield can reach 19%, and the highest purity can reach 97%.
本发明的技术方案Technical scheme of the present invention
一种产朊假丝酵母β-D-葡聚糖的生产方法,具体包括以下步骤:A production method of Candida utilis β-D-glucan, specifically comprising the following steps:
(1)、去除土豆淀粉的土豆汁的制备(1) Preparation of potato juice with potato starch removed
将土豆用粉碎机打碎,得到土豆泥,然后在土豆泥中加入10倍土豆质量的蒸馏水,充分搅拌混匀,10000r/min条件下离心20min去除沉淀,该沉淀即为土豆淀粉,得到的滤液放置5天即得去除土豆淀粉的土豆汁;Crush the potatoes with a pulverizer to obtain mashed potatoes, then add distilled water 10 times the mass of potatoes to the mashed potatoes, stir well, and centrifuge at 10,000 r/min for 20 minutes to remove the precipitate, which is potato starch, and the obtained filtrate Stand for 5 days to get the potato juice that removes the potato starch;
(2)、去蛋白的土豆汁水溶液的制备(2), preparation of protein-removed potato juice aqueous solution
将步骤(1)所得的去除土豆淀粉的土豆汁通过8层纱布进行过滤,所得的滤液中加入蒸馏水,其中蒸馏水的加入量为所得滤液体积的5倍,然后控制温度为121℃下进行抽提1h,得到抽提液;Filter the potato juice obtained in step (1) without potato starch through 8 layers of gauze, add distilled water to the obtained filtrate, wherein the amount of distilled water added is 5 times the volume of the obtained filtrate, and then control the temperature at 121°C for extraction 1h, to obtain the extract;
上述去除土豆淀粉的土豆汁可以用马铃薯淀粉工厂的废弃的土豆汁替代;The above-mentioned potato juice that removes potato starch can be replaced with the discarded potato juice of potato starch factory;
上述所得的抽提液用型号为SHZ-Ш型循环水真空泵在-0.1MPa的真空度下进行抽滤,以除去蛋白质,抽滤后所得的滤液中加入为所得的滤液体积10倍的蒸馏水,搅拌混匀后得到去蛋白的土豆汁水溶液;The above-mentioned extract is filtered with a SHZ-Ш type circulating water vacuum pump at a vacuum of -0.1MPa to remove the protein. Distilled water that is 10 times the volume of the obtained filtrate is added to the obtained filtrate after the suction filtration. After stirring and mixing, the protein-free potato juice aqueous solution is obtained;
(3)、灭菌后的去蛋白的土豆汁的制备(3) Preparation of sterilized protein-free potato juice
调节步骤(2)所得的去蛋白的土豆汁水溶液的pH为4-8,然后加入甘油,混匀后控制温度为121℃进行灭菌15min,得到灭菌后的去蛋白的土豆汁;Adjust the pH of the protein-free potato juice aqueous solution obtained in step (2) to 4-8, then add glycerin, mix well, control the temperature at 121° C., and sterilize for 15 minutes to obtain sterilized protein-free potato juice;
调节去蛋白的土豆汁水溶液的pH所用的碱为质量百分比浓度为1%的NaOH水溶液,酸为质量百分比浓度为0.1%的HCl水溶液;The alkali used to adjust the pH of the protein-free potato juice aqueous solution is a NaOH aqueous solution with a mass percentage concentration of 1%, and the acid is a 0.1% HCl aqueous solution with a mass percentage concentration;
上述甘油的添加量为pH为4-8的去蛋白的土豆汁水溶液体积的5-25%;The added amount of the above-mentioned glycerin is 5-25% of the volume of the deproteinized potato juice aqueous solution whose pH is 4-8;
(4)、接种发酵(4), inoculation fermentation
向步骤(3)所得的灭菌后的去蛋白的土豆汁中接种甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769,然后控制温度为24-32℃,转速为100-200r/min进行发酵培养24h,得到发酵液;Inoculate Candida utilis CICC 1769 preserved in a glycerol tube into the sterilized deproteinized potato juice obtained in step (3), and then control the temperature to 24-32°C and the rotation speed to 100-200r/ Min carries out fermentation culture 24h, obtains fermented liquid;
接种量按每100mL灭菌后的去蛋白土豆汁中接入1-8mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769;The amount of inoculation is to add 1-8mL of Candida utilis CICC 1769 preserved in glycerol tubes per 100mL of sterilized deproteinized potato juice;
每1mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769中,含有的产朊假丝酵母菌(Candida utilis)CICC 1769菌数为1.6×109 CFU;Candida utilis ( Candida utilis ) CICC 1769 stored in each 1mL glycerol tube contains 1.6×10 9 CFU of Candida utilis ( Candida utilis ) CICC 1769;
(5)、将步骤(4)所得的发酵液过滤,去除滤液,得到的滤饼即为胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体;(5), filtering the fermented liquid obtained in step (4), removing the filtrate, and the obtained filter cake is the cell of Candida utilis containing Candida utilis β-D-glucan;
(6)、在121℃条件下,采用蒸馏水将步骤(5)所得的胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体进行浸提30min,以使产朊假丝酵母菌体细胞进行细胞破壁,然后将所得的浸提液经过超声波细胞破碎仪在超声频率为20KHz,800W下进行超声处理60min,然后在10000r/min下离心15min,所得的沉淀用蒸馏水进行洗涤,直至流出液澄清,终止洗涤,然后再控制温度为-20℃,真空度为10Pa进行真空冷冻干燥,即得产朊假丝酵母β-D-葡聚糖。(6) Under the condition of 121°C, extract the Candida utilis cells containing Candida utilis β-D-glucan in the cells obtained in step (5) with distilled water for 30 minutes, so that The somatic cells of Candida utilis were subjected to cell wall breaking, and then the obtained extract was subjected to ultrasonic treatment at an ultrasonic frequency of 20KHz and 800W for 60min through an ultrasonic cell disruptor, and then centrifuged at 10000r/min for 15min, and the obtained precipitate Wash with distilled water until the effluent is clear, stop the washing, and then control the temperature to -20°C and vacuum to 10 Pa to carry out vacuum freeze-drying to obtain Candida utilis β-D-glucan.
上述的生产方法所得的产朊假丝酵母β-D-葡聚糖,由于其具有一般酵母β-D-葡聚糖的特性,因此可以改善食品的质地,能用作食品中膳食纤维的来源,作为一种非常优良的食品添加剂有着很大的发展前景。进一步,所得的产朊假丝酵母β-D-葡聚糖能显著增强水产动物的非特异性免疫系统,应用在水产养殖中可大大增强水产动物的抵抗力,是一种无公害、天然绿色的应用途径。更进一步,所得的产朊假丝酵母β-D-葡聚糖能利用其免疫调节活性来促进皮肤的再生,调节细胞的生长,然后达到抗衰老的作用效果,即上述所得的产朊假丝酵母β-D-葡聚糖可以用于食品、饲料、化妆品以及水产养殖中。The Candida utilis β-D-glucan obtained by the above production method can improve the texture of food because it has the characteristics of general yeast β-D-glucan, and can be used as a source of dietary fiber in food , as a very good food additive has great development prospects. Further, the obtained Candida utilis β-D-glucan can significantly enhance the non-specific immune system of aquatic animals, and can greatly enhance the resistance of aquatic animals when applied in aquaculture. It is a pollution-free, natural green Approach. Furthermore, the resulting Candida utilis β-D-glucan can use its immunomodulatory activity to promote skin regeneration, regulate cell growth, and then achieve anti-aging effects, that is, the above-mentioned Candida utilis Yeast β-D-glucan can be used in food, feed, cosmetics and aquaculture.
进一步,上述生产方法所得的产朊假丝酵母β-D-葡聚糖,由于因为人体内没有降解β-葡聚糖的酶,所以它们有着天然的营养纤维的作用。研究表明高纤维的饮食可以降低胆固醇,而且减少关节炎等慢性疾病和心脏病的发生率。当β-葡聚糖进入口腔,就会开始吸水膨胀。β-葡聚糖的膳食纤维可以增加肠道的运输时间,有减慢肠道吸收的作用,因此能显著地降血脂、降血糖以及提高免疫能力,对有糖尿病、肥胖症、便秘及高胆固醇等疾病的患者有良好的辅助治疗的作用。Further, the Candida utilis β-D-glucan obtained by the above production method has the function of natural nutritional fiber because there is no enzyme to degrade β-glucan in the human body. Studies have shown that a high-fiber diet can lower cholesterol and reduce the incidence of chronic diseases such as arthritis and heart disease. When β-glucan enters the mouth, it will start to absorb water and swell. The dietary fiber of β-glucan can increase the transit time of the intestinal tract and slow down the absorption of the intestinal tract, so it can significantly reduce blood fat, blood sugar and improve immunity. It is suitable for people with diabetes, obesity, constipation and high cholesterol Patients with other diseases have a good role in adjuvant therapy.
进一步,上述生产方法所得的产朊假丝酵母β-D-葡聚糖,由于可以刺激先天免疫系统,从而达到抵抗细菌、真菌以及病毒等的能力大大提高。更进一步,产朊假丝酵母β-D-葡聚糖可以通过活化T细胞、巨噬细胞以及自然杀伤细胞,还可以刺激T淋巴细胞的分化和活化,影响并激活途径补体的变化,最终达到增强机体细胞和体液免疫的效果,因此该产朊假丝酵母β-D-葡聚糖具有保肝护肝、保护胃黏膜,改善微循环、增强免疫力等保健功能。Furthermore, the Candida utilis β-D-glucan obtained by the above production method can greatly improve the ability to resist bacteria, fungi and viruses because it can stimulate the innate immune system. Furthermore, Candida utilis β-D-glucan can activate T cells, macrophages and natural killer cells, and can also stimulate the differentiation and activation of T lymphocytes, affect and activate the changes in complement, and finally achieve Enhance the effect of the body's cellular and humoral immunity, so the Candida utilis β-D-glucan has health functions such as protecting the liver, protecting the gastric mucosa, improving microcirculation, and enhancing immunity.
本发明的有益效果Beneficial effects of the present invention
本发明的一种产朊假丝酵母β-D-葡聚糖的生产方法,由于生产过程中利用的去淀粉的土豆汁经检测,pH值为4.82,COD值为29.8g O2/L及BOD5的值为15.6g O2/L,接近于马铃薯淀粉工厂废弃的土豆汁的pH、COD、BOD5指标,因此本发明的产朊假丝酵母β-D-葡聚糖的生产方法可以用马铃薯淀粉工厂的废弃土豆汁为培养基的原料来进行生产,从而缓解废弃土豆汁造成的环境污染问题,实现变废为宝,从而降低了酵母β-D-葡聚糖的生产成本,并且生产过程操作简单,便于规模化生产。A kind of production method of Candida utilis β-D-glucan of the present invention, because the potato juice of removing starch utilized in the production process is tested, pH value is 4.82, and COD value is 29.8g O 2 /L and The value of BOD 5 is 15.6g O 2 /L, close to pH, COD, BOD 5 index of the discarded potato juice of potato starch factory, so the production method of Candida utilis β-D-glucan of the present invention can be Use the waste potato juice from the potato starch factory as the raw material of the medium for production, thereby alleviating the environmental pollution problem caused by the waste potato juice, realizing turning waste into wealth, thereby reducing the production cost of yeast β-D-glucan, and The production process is simple to operate and is convenient for large-scale production.
进一步,本发明的一种产朊假丝酵母β-D-葡聚糖的生产方法,由于生产过程中所得的胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体通过采用高温浸提和超声破壁协同作用的提取方法,最终得到高产率、高纯度的产朊假丝酵母酵母β-D-葡聚糖,其纯度最高可达97%,得率最高可达19%,产率最高可达87%。Further, in a production method of Candida utilis β-D-glucan of the present invention, since the Candida utilis cells containing Candida utilis β-D-glucan obtained during the production process By adopting the extraction method of high-temperature extraction and ultrasonic wall breaking synergistically, high-yield and high-purity Candida utilis β-D-glucan can be obtained with a purity of up to 97%. Up to 19%, yield up to 87%.
附图说明Description of drawings
图1 产朊假丝酵母β-D-葡聚糖的红外光谱图;Figure 1 Infrared spectrum of Candida utilis β-D-glucan;
图2 产朊假丝酵母β-D-葡聚糖的紫外全扫描图谱。Figure 2 UV full scan spectrum of Candida utilis β-D-glucan.
具体实施方式detailed description
下面通过具体实施例并结合附图对本发明进一步阐述,但并不限制本发明。The present invention will be further described below through specific embodiments in conjunction with the accompanying drawings, but the present invention is not limited.
本发明各实施例中所用的菌种为产朊假丝酵母(Candida utilis),菌种编号CICC1769,购买于中国工业微生物菌种保藏管理中心,其于中国工业微生物菌种保藏管理中心保藏,保藏编号:ATCC 9950;保藏机构地址:北京市朝阳区酒仙桥中路24号6号楼,邮编:100015,供应日期:2015年7月13日。The strain used in each embodiment of the present invention is Candida utilis ( Candida utilis ), the strain number CICC1769, which was purchased from China Industrial Microorganism Culture Collection Management Center, and it was preserved in China Industrial Microbiology Culture Collection Management Center. Serial number: ATCC 9950; address of depository institution: Building 6, No. 24 Jiuxianqiao Middle Road, Chaoyang District, Beijing, postcode: 100015, date of supply: July 13, 2015.
本发明的各实施例中所用的仪器型号及生产厂家信息如下:Used instrument type and manufacturer's information in each embodiment of the present invention are as follows:
超声波细胞破碎仪,型号为JY99-IIDN,宁波新芝生物科技股份有限公司生产;Ultrasonic cell disruptor, model JY99-IIDN, produced by Ningbo Xinzhi Biotechnology Co., Ltd.;
循环水真空泵,型号为SHZ-Ш型,上海亚荣生化仪器生产。Circulating water vacuum pump, model SHZ-Ш, produced by Shanghai Yarong Biochemical Instruments.
傅里叶红外光谱仪,TENSOR系列,德国Bruker公司;Fourier transform infrared spectrometer, TENSOR series, German Bruker company;
紫外分光光度计,UV8000型,上海元析仪器有限公司。Ultraviolet spectrophotometer, UV8000 type, Shanghai Yuanxi Instrument Co., Ltd.
本发明的各实施例中产朊假丝酵母β-D-葡聚糖含量的测定,以葡萄糖为标准,采用苯酚-硫酸法测定各实施例中所得的产朊假丝酵母β-D-葡聚糖含量(参考文献:宋博, 赵峡, 李国强. 1种南海软珊瑚多糖的提取、分离及活性评价[J]. 中国海洋药物, 2016, 35(5):1-6.DOI:10.13400/j.cnki.cjmd.2016.05.001.);The mensuration of Candida utilis β-D-glucan content in each embodiment of the present invention, take glucose as standard, adopt phenol-sulfuric acid method to measure the Candida utilis β-D-glucan obtained in each embodiment Sugar content (references: Song Bo, Zhao Xia, Li Guoqiang. Extraction, separation and activity evaluation of a polysaccharide from soft corals in the South China Sea[J]. China Marine Medicine, 2016, 35(5):1-6.DOI:10.13400/ j.cnki.cjmd.2016.05.001.);
本发明各实施例中产朊假丝酵母β-D-葡聚糖的纯度(%)=酵母β-D-葡聚糖的质量÷产朊假丝酵母细胞壁中所得粗多糖的质量×100%;Purity (%) of Candida utilis β-D-glucan in each embodiment of the present invention = mass of yeast β-D-glucan ÷ mass of crude polysaccharide obtained in the cell wall of Candida utilis × 100%;
产朊假丝酵母β-D-葡聚糖的得率(%)=实际得到的产朊假丝酵母β-D-葡聚糖质量÷产朊假丝酵母菌菌体的质量×100%;Yield of Candida utilis β-D-glucan (%) = actually obtained mass of Candida utilis β-D-glucan ÷ mass of Candida utilis cell × 100%;
产朊假丝酵母β-D-葡聚糖的产率(%)=实际得到的产朊假丝酵母β-D-葡聚糖质量÷产朊假丝酵母菌细胞内理论上含有的β-D-葡聚糖的质量×100%。The yield of Candida utilis β-D-glucan (%) = the actual mass of Candida utilis β-D-glucan ÷ the theoretically contained β-glucan in Candida utilis cells The mass of D-glucan × 100%.
实施例1Example 1
一种产朊假丝酵母β-D-葡聚糖的生产方法,具体包括以下步骤:A production method of Candida utilis β-D-glucan, specifically comprising the following steps:
(1)、去除土豆淀粉的土豆汁的制备(1) Preparation of potato juice with potato starch removed
取40.0g土豆粉碎机打碎,得到土豆泥,然后在土豆泥中加入400mL的蒸馏水,充分搅拌混匀,10000r/min条件下离心20min除去沉淀即去除土豆淀粉,所得的去除土豆淀粉的滤液放置5天即得去除土豆淀粉的土豆汁;Take 40.0g of potatoes and smash them into mashed potatoes to obtain mashed potatoes, then add 400mL of distilled water to the mashed potatoes, stir and mix well, and centrifuge at 10000r/min for 20min to remove the precipitate, that is, remove the potato starch, and place the obtained filtrate from the removal of potato starch Potato juice with potato starch removed in 5 days;
经检测上述所得的土豆汁的pH值为4.82、COD值为29.8g O2/L及BOD5的值为15.6g O2/L;The pH value of the potato juice obtained above was tested to be 4.82, the COD value was 29.8g O 2 /L and the BOD 5 value was 15.6g O 2 /L;
(2)、去蛋白的土豆汁水溶液的制备(2), preparation of protein-removed potato juice aqueous solution
将280mL步骤(1)所得的去除土豆淀粉的土豆汁通过8层纱布进行过滤,取100mL所得的滤液,加入蒸馏水500mL,在温度为121℃下进行抽提1h,得到抽提液;Filter 280 mL of the potato juice obtained in step (1) without potato starch through 8 layers of gauze, take 100 mL of the obtained filtrate, add 500 mL of distilled water, and extract at a temperature of 121 °C for 1 hour to obtain an extract;
上述所得的抽提液用循环水真空泵在-0.1MPa的真空度下进行抽滤,以除去蛋白质,取200mL抽滤后所得的滤液,向其中加入2000mL蒸馏水,进行混匀,得到去蛋白的土豆汁水溶液;The extract obtained above is suction-filtered with a circulating water vacuum pump at a vacuum of -0.1MPa to remove protein. Take 200mL of the filtrate obtained after suction-filtration, add 2000mL of distilled water to it, and mix well to obtain protein-free potatoes. juice solution;
(3)、灭菌后的去蛋白的土豆汁的制备(3) Preparation of sterilized protein-free potato juice
用质量百分比浓度为1%的NaOH水溶液和质量百分比浓度为0.1%的HCl水溶液调节步骤(2)所得的去蛋白的土豆汁水溶液的pH为4,然后加入甘油,混匀后控制温度为121℃进行灭菌15min,得到灭菌后的去蛋白的土豆汁;Use 1% NaOH aqueous solution and 0.1% HCl aqueous solution to adjust the pH of the deproteinized potato juice aqueous solution obtained in step (2) to 4, then add glycerin, mix well and control the temperature to 121°C Sterilize for 15 minutes to obtain deproteinized potato juice after sterilization;
上述甘油的添加量为pH为4的去蛋白的土豆汁水溶液体积的25%;The addition of above-mentioned glycerin is 25% of the volume of the potato juice aqueous solution that the pH is 4;
(4)、接种发酵(4), inoculation fermentation
向步骤(3)所得的灭菌后的去蛋白的土豆汁中接种甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769,然后控制温度为24℃,转速为100r/min进行发酵培养24h,得到发酵液;Inoculate Candida utilis CICC 1769 preserved in a glycerol tube into the sterilized deproteinized potato juice obtained in step (3), and then control the temperature at 24°C and the rotation speed at 100r/min for fermentation culture 24h, obtain fermented liquid;
接种量按每100mL灭菌后的去蛋白的土豆汁中接入1mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769;The amount of inoculum is to insert 1 mL of Candida utilis CICC 1769 preserved in a glycerol tube into every 100 mL of sterilized protein-free potato juice;
每1mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769中,含有的产朊假丝酵母菌(Candida utilis)CICC 1769菌数为1.6×109 CFU(CFU表示单位体积中的活菌个数);The number of Candida utilis ( Candida utilis ) CICC 1769 stored in each 1mL glycerol tube is 1.6×10 9 CFU (CFU means the activity per unit volume) number of bacteria);
(5)、将步骤(4)所得的发酵液用布氏漏斗进行过滤,去除滤液,得到的滤饼即为胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体;(5) Filter the fermentation broth obtained in step (4) with a Buchner funnel, remove the filtrate, and obtain a filter cake that contains Candida utilis β-D-glucan in the cells Bacteria;
经测定,按每lmL发酵液计算,得到8.20mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌;After determination, calculate by every 1mL fermented liquid, obtain the Candida utilis bacterium that contains Candida utilis β-D-glucan in the cell of 8.20mg;
每mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌含β-D-葡聚糖0.0986mg;Candida utilis containing Candida utilis β-D-glucan per mg cell contains 0.0986mg of β-D-glucan;
每mL发酵液中含有产朊假丝酵母β-D-葡聚糖0.5394mg;Each mL of fermentation broth contains 0.5394 mg of Candida utilis β-D-glucan;
(6)、在121℃条件下,按质量比计算,胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体:蒸馏水为15:100的比例,用蒸馏水将步骤(5)所得的胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体进行浸提30min,以使产朊假丝酵母菌体进行细胞破壁,然后经过超声波细胞破碎仪在频率为20KHz,功率为800W下进行超声处理60min,然后在10000r/min下离心15min,所得的沉淀用蒸馏水进行洗涤,直至流出液澄清,终止洗涤,然后再控制温度为-20℃,真空度为10Pa进行真空冷冻干燥,即得产朊假丝酵母β-D-葡聚糖。(6) Under the condition of 121°C, the ratio of Candida utilis bacteria containing Candida utilis β-D-glucan in the cell: distilled water is 15:100 calculated by mass ratio. Extracting the Candida utilis cells containing Candida utilis β-D-glucan in the cells obtained in step (5) for 30 minutes, so that the cells of the Candida utilis cells are broken down, Then, the frequency of the ultrasonic cell disruptor is 20KHz, the power is 800W, and the ultrasonic treatment is carried out for 60min, and then centrifuged at 10000r/min for 15min, and the precipitate obtained is washed with distilled water until the effluent is clear, and the washing is terminated, and then the temperature is controlled to be -20°C, vacuum freeze-drying at 10 Pa to obtain Candida utilis β-D-glucan.
经测定,上述所得的产朊假丝酵母β-D-葡聚糖的产率为82%、得率为13%,纯度为96%。It was determined that the yield of the Candida utilis β-D-glucan obtained above was 82%, the yield was 13%, and the purity was 96%.
采用傅里叶红外光谱仪对上述所得的产朊假丝酵母β-D-葡聚糖进行测定,所得的产朊假丝酵母β-D-葡聚糖的红外光谱图如图1所示,从图1中可以看出所提取的葡聚糖在890cm-1附近的峰为β-型,在3200cm-1附近的峰为糖苷键的特征峰吸收峰,由此表明了通过本方法得到样品是糖苷键类型为β-构型的酵母葡聚糖;The Candida utilis β-D-glucan obtained above is measured by a Fourier transform infrared spectrometer, and the infrared spectrogram of the obtained Candida utilis β-D-glucan is shown in Figure 1, from It can be seen from Fig. 1 that the extracted dextran has a peak of β-type near 890cm -1 , and a peak near 3200cm -1 is the characteristic peak absorption peak of glycosidic bonds, which shows that the sample obtained by this method is glycoside Yeast glucan whose bond type is β-configuration;
采用紫外分光光度计对上述所得的产朊假丝酵母β-D-葡聚糖进行测定,所得的产朊假丝酵母β-D-葡聚糖的紫外光谱图如图2所示,从图2中可以看出,在波长190~400nm范围内,产朊假丝酵母β-D-葡聚糖中不含有蛋白质和核酸等杂质,由此表明了所得样品纯度较高。Adopt ultraviolet spectrophotometer to measure above-mentioned obtained Candida utilis β-D-glucan, the ultraviolet spectrogram of the obtained Candida utilis β-D-glucan is as shown in Figure 2, from the figure It can be seen in 2 that within the wavelength range of 190-400nm, Candida utilis β-D-glucan does not contain impurities such as protein and nucleic acid, which shows that the obtained sample has a high purity.
实施例2Example 2
一种产朊假丝酵母β-D-葡聚糖的生产方法,具体包括以下步骤:A production method of Candida utilis β-D-glucan, specifically comprising the following steps:
(1)、去除土豆淀粉的土豆汁的制备(1) Preparation of potato juice with potato starch removed
同实施例1的步骤(1);With the step (1) of embodiment 1;
(2)、去蛋白的土豆汁水溶液的制备(2), preparation of protein-removed potato juice aqueous solution
同实施例1的步骤(2);With the step (2) of embodiment 1;
(3)、灭菌后的去蛋白的土豆汁的制备(3) Preparation of sterilized protein-free potato juice
用质量百分比浓度为1%的NaOH水溶液和质量百分比浓度为0.1%的HCl水溶液调节步骤(2)所得的去蛋白的土豆汁水溶液的pH为8,然后加入甘油,混匀后控制温度为121℃进行灭菌15min,得到灭菌后的去蛋白的土豆汁;Use 1% NaOH aqueous solution and 0.1% HCl aqueous solution to adjust the pH of the deproteinized potato juice aqueous solution obtained in step (2) to 8, then add glycerin, mix well and control the temperature to 121°C Sterilize for 15 minutes to obtain deproteinized potato juice after sterilization;
上述甘油的添加量为pH为8的去蛋白的土豆汁水溶液体积的15%;The addition amount of above-mentioned glycerin is 15% of the volume of the potato juice aqueous solution that the pH is 8;
(4)、接种发酵(4), inoculation fermentation
向步骤(3)所得的灭菌后的去蛋白的土豆汁中接种甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769,然后控制温度为28℃,转速为150r/min进行发酵培养24h,得到发酵液;Inoculate Candida utilis CICC 1769 preserved in a glycerol tube into the sterilized deproteinized potato juice obtained in step (3), and then control the temperature at 28°C and the rotation speed at 150r/min for fermentation culture 24h, obtain fermented liquid;
接种量按每100mL灭菌后的去蛋白土豆汁中接入4mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769;The amount of inoculum is to add Candida utilis CICC 1769 preserved in a 4 mL glycerol tube per 100 mL of sterilized deproteinized potato juice;
每1mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769中,含有的产朊假丝酵母菌(Candida utilis)CICC 1769菌数为1.6×109 CFU;Candida utilis ( Candida utilis ) CICC 1769 stored in each 1mL glycerol tube contains 1.6×10 9 CFU of Candida utilis ( Candida utilis ) CICC 1769;
(5)、将步骤(4)所得的发酵液用布氏漏斗进行过滤,去除滤液,得到的滤饼即为胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体;(5) Filter the fermentation broth obtained in step (4) with a Buchner funnel, remove the filtrate, and obtain a filter cake that contains Candida utilis β-D-glucan in the cells Bacteria;
经测定,按每lmL发酵液计算,收得10.16mg(干重)胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌;After determination, 10.16mg (dry weight) of Candida utilis containing Candida utilis β-D-glucan in the cell was obtained on the basis of per 1mL fermentation broth;
每mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌含β-D-葡聚糖0.1039mg;Candida utilis containing Candida utilis β-D-glucan in each mg cell contains 0.1039mg of β-D-glucan;
每mL发酵液中含有产朊假丝酵母β-D-葡聚糖0.7988mg;Each mL of fermentation broth contains 0.7988 mg of Candida utilis β-D-glucan;
(6)、在121℃条件下,按质量比计算,胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体:蒸馏水为15:100的比例,用蒸馏水将步骤(5)所得的胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体进行浸提30min,以使产朊假丝酵母菌体进行细胞破壁,然后经过超声波细胞破碎仪在频率为20KHz,功率为800W下进行超声处理60min,然后在10000r/min下离心15min,所得的沉淀用蒸馏水进行洗涤,直至流出液澄清,终止洗涤,然后再控制温度为-20℃,真空度为10Pa进行真空冷冻干燥,即得产朊假丝酵母β-D-葡聚糖。(6) Under the condition of 121°C, the ratio of Candida utilis bacteria containing Candida utilis β-D-glucan in the cell: distilled water is 15:100 calculated by mass ratio. Extracting the Candida utilis cells containing Candida utilis β-D-glucan in the cells obtained in step (5) for 30 minutes, so that the cells of the Candida utilis cells are broken down, Then, the frequency of the ultrasonic cell disruptor is 20KHz, the power is 800W, and the ultrasonic treatment is carried out for 60min, and then centrifuged at 10000r/min for 15min, and the precipitate obtained is washed with distilled water until the effluent is clear, and the washing is terminated, and then the temperature is controlled to be -20°C, vacuum freeze-drying at 10 Pa to obtain Candida utilis β-D-glucan.
经测定,上述所得的产朊假丝酵母β-D-葡聚糖的产率为87%、得率为19%,纯度为97%。It was determined that the yield of the Candida utilis β-D-glucan obtained above was 87%, the yield was 19%, and the purity was 97%.
实施例3Example 3
一种产朊假丝酵母β-D-葡聚糖的生产方法,具体包括以下步骤:A production method of Candida utilis β-D-glucan, specifically comprising the following steps:
(1)、去除土豆淀粉的土豆汁的制备(1) Preparation of potato juice with potato starch removed
同实施例1的步骤(1);With the step (1) of embodiment 1;
(2)、去蛋白的土豆汁水溶液的制备(2), preparation of protein-removed potato juice aqueous solution
同实施例1的步骤(2);With the step (2) of embodiment 1;
(3)、灭菌后的去蛋白的土豆汁的制备(3) Preparation of sterilized protein-free potato juice
用质量百分比浓度为1%的NaOH水溶液和质量百分比浓度为0.1%的HCl水溶液调节步骤(2)所得的去蛋白的土豆汁水溶液的pH为7,然后加入甘油,混匀后控制温度为121℃进行灭菌15min,得到灭菌后的去蛋白的土豆汁;Use 1% NaOH aqueous solution and 0.1% HCl aqueous solution to adjust the pH of the deproteinized potato juice aqueous solution obtained in step (2) to 7, then add glycerin, mix well and control the temperature to 121°C Sterilize for 15 minutes to obtain deproteinized potato juice after sterilization;
上述甘油的添加量为pH为7的去蛋白的土豆汁水溶液体积的10%;The addition amount of above-mentioned glycerin is 10% of the volume of the potato juice aqueous solution that the pH is 7;
(4)、接种发酵(4), inoculation fermentation
向步骤(3)所得的灭菌后的去蛋白的土豆汁中接种甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769,然后控制温度为30℃,转速为200r/min进行发酵培养24h,得到发酵液;Inoculate Candida utilis CICC 1769 preserved in a glycerol tube into the sterilized deproteinized potato juice obtained in step (3), and then control the temperature at 30°C and the rotation speed at 200r/min for fermentation culture 24h, obtain fermented liquid;
接种量按每100mL灭菌后的去蛋白土豆汁中接入2mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769;The amount of inoculum is to add Candida utilis ( Candida utilis ) CICC 1769 preserved in a 2mL glycerol tube per 100mL of sterilized deproteinized potato juice;
每1mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769中,含有的产朊假丝酵母菌(Candida utilis)CICC 1769菌数为1.6×109 CFU;Candida utilis ( Candida utilis ) CICC 1769 stored in each 1mL glycerol tube contains 1.6×10 9 CFU of Candida utilis ( Candida utilis ) CICC 1769;
(5)、将步骤(4)所得的发酵液用布氏漏斗进行过滤,去除滤液,得到的滤饼即为胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体;(5) Filter the fermentation broth obtained in step (4) with a Buchner funnel, remove the filtrate, and obtain a filter cake that contains Candida utilis β-D-glucan in the cells Bacteria;
经测定,按每lmL发酵液计算,得到9.23mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌;After determination, calculate by every 1mL fermented liquid, obtain the Candida utilis bacterium that contains Candida utilis β-D-glucan in the cell of 9.23mg;
每mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌中含β-D-葡聚糖0.0998mg;0.0998 mg of β-D-glucan in Candida utilis containing Candida utilis β-D-glucan in each mg cell;
即本发明的生产方法所得的每mL发酵液中含有产朊假丝酵母β-D-葡聚糖0.6729mg;That is, each mL of fermented liquid obtained by the production method of the present invention contains 0.6729 mg of Candida utilis β-D-glucan;
(6)、在121℃条件下,按质量比计算,胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体:蒸馏水为15:100的比例,用蒸馏水将步骤(5)所得的胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体进行浸提30min,以使产朊假丝酵母菌体进行细胞破壁,然后经过超声波细胞破碎仪在频率为20KHz,功率为800W下进行超声处理60min,然后在10000r/min下离心15min,所得的沉淀用蒸馏水进行洗涤,直至流出液澄清,终止洗涤,然后再控制温度为-20℃,真空度为10Pa进行真空冷冻干燥,即得产朊假丝酵母β-D-葡聚糖。(6) Under the condition of 121°C, the ratio of Candida utilis bacteria containing Candida utilis β-D-glucan in the cell: distilled water is 15:100 calculated by mass ratio. Extracting the Candida utilis cells containing Candida utilis β-D-glucan in the cells obtained in step (5) for 30 minutes, so that the cells of the Candida utilis cells are broken down, Then, the frequency of the ultrasonic cell disruptor is 20KHz, the power is 800W, and the ultrasonic treatment is carried out for 60min, and then centrifuged at 10000r/min for 15min, and the precipitate obtained is washed with distilled water until the effluent is clear, and the washing is terminated, and then the temperature is controlled to be -20°C, vacuum freeze-drying at 10 Pa to obtain Candida utilis β-D-glucan.
经测定,上述所得的产朊假丝酵母β-D-葡聚糖的产率为83%、得率为17%,纯度为97%。It was determined that the yield of the Candida utilis β-D-glucan obtained above was 83%, the yield was 17%, and the purity was 97%.
实施例4Example 4
一种产朊假丝酵母β-D-葡聚糖的生产方法,具体包括以下步骤:A production method of Candida utilis β-D-glucan, specifically comprising the following steps:
(1)、去除土豆淀粉的土豆汁的制备(1) Preparation of potato juice with potato starch removed
同实施例1的步骤(1);With the step (1) of embodiment 1;
(2)、去蛋白的土豆汁水溶液的制备(2), preparation of protein-removed potato juice aqueous solution
同实施例1的步骤(2);With the step (2) of embodiment 1;
(3)、灭菌后的去蛋白的土豆汁的制备(3) Preparation of sterilized protein-free potato juice
用质量百分比浓度为1%的NaOH水溶液和质量百分比浓度为0.1%的HCl水溶液调节步骤(2)所得的去蛋白的土豆汁水溶液的pH为6,然后加入甘油,混匀后控制温度为121℃进行灭菌15min,得到灭菌后的去蛋白的土豆汁;Use 1% NaOH aqueous solution and 0.1% HCl aqueous solution to adjust the pH of the deproteinized potato juice aqueous solution obtained in step (2) to 6, then add glycerin, mix well and control the temperature to 121°C Sterilize for 15 minutes to obtain deproteinized potato juice after sterilization;
上述甘油的添加量为pH为7的去蛋白的土豆汁水溶液体积的20%;The addition amount of above-mentioned glycerol is 20% of the volume of the potato juice aqueous solution that the pH is 7;
(4)、接种发酵(4), inoculation fermentation
向步骤(3)所得的灭菌后的去蛋白的土豆汁中接种甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769,然后控制温度为32℃,转速为200r/min进行发酵培养24h,得到发酵液;Inoculate Candida utilis CICC 1769 preserved in glycerol tubes into the sterilized deproteinized potato juice obtained in step (3), and then control the temperature at 32°C and the rotation speed at 200r/min for fermentation culture 24h, obtain fermented liquid;
接种量按每100mL灭菌后的去蛋白土豆汁中接入8mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769;The amount of inoculum is to insert Candida utilis CICC 1769 preserved in 8 mL glycerol tubes into every 100 mL of sterilized protein-free potato juice;
每1mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769中,含有的产朊假丝酵母菌(Candida utilis)CICC 1769菌数为1.6×109 CFU;Candida utilis ( Candida utilis ) CICC 1769 stored in each 1mL glycerol tube contains 1.6×10 9 CFU of Candida utilis ( Candida utilis ) CICC 1769;
(5)、将步骤(4)所得的发酵液用布氏漏斗进行过滤,去除滤液,得到的滤饼即为胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体;(5) Filter the fermentation broth obtained in step (4) with a Buchner funnel, remove the filtrate, and obtain a filter cake that contains Candida utilis β-D-glucan in the cells Bacteria;
经测定,按每lmL发酵液计算,得到7.98mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌;After determination, calculate by every 1mL fermented liquid, obtain the Candida utilis bacterium that contains Candida utilis β-D-glucan in the cell of 7.98mg;
每mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌,含β-D-葡聚糖0.0993mg;Candida utilis containing Candida utilis β-D-glucan per mg cell, containing 0.0993mg of β-D-glucan;
即本发明的生产方法所得的每mL发酵液中含有产朊假丝酵母β-D-葡聚糖0.6236mg;That is, each mL of fermented liquid obtained by the production method of the present invention contains 0.6236 mg of Candida utilis β-D-glucan;
(6)、在121℃条件下,按质量比计算,胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体:蒸馏水为15:100的比例,用蒸馏水将步骤(5)所得的胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体进行浸提30min,以使产朊假丝酵母菌体进行细胞破壁,然后经过超声波细胞破碎仪在频率为20KHz,功率为800W下进行超声处理60min,然后在10000r/min下离心15min,所得的沉淀用蒸馏水进行洗涤,直至流出液澄清,终止洗涤,然后再控制温度为-20℃,真空度为10Pa进行真空冷冻干燥,即得产朊假丝酵母β-D-葡聚糖。(6) Under the condition of 121°C, the ratio of Candida utilis bacteria containing Candida utilis β-D-glucan in the cell: distilled water is 15:100 calculated by mass ratio. Extracting the Candida utilis cells containing Candida utilis β-D-glucan in the cells obtained in step (5) for 30 minutes, so that the cells of the Candida utilis cells are broken down, Then, the frequency of the ultrasonic cell disruptor is 20KHz, the power is 800W, and the ultrasonic treatment is carried out for 60min, and then centrifuged at 10000r/min for 15min, and the precipitate obtained is washed with distilled water until the effluent is clear, and the washing is terminated, and then the temperature is controlled to be -20°C, vacuum freeze-drying at 10 Pa to obtain Candida utilis β-D-glucan.
经测定,上述所得的产朊假丝酵母β-D-葡聚糖的产率为83%、得率为15%,纯度为96%。It was determined that the yield of the Candida utilis β-D-glucan obtained above was 83%, the yield was 15%, and the purity was 96%.
实施例5Example 5
一种产朊假丝酵母β-D-葡聚糖的生产方法,具体包括以下步骤:A production method of Candida utilis β-D-glucan, specifically comprising the following steps:
(1)、去除土豆淀粉的土豆汁的制备(1) Preparation of potato juice with potato starch removed
同实施例1的步骤(1);With the step (1) of embodiment 1;
(2)、去蛋白的土豆汁水溶液的制备(2), preparation of protein-removed potato juice aqueous solution
同实施例1的步骤(2);With the step (2) of embodiment 1;
(3)、灭菌后的去蛋白的土豆汁的制备(3) Preparation of sterilized protein-free potato juice
用质量百分比浓度为1%的NaOH水溶液和质量百分比浓度为0.1%的HCl水溶液调节步骤(2)所得的去蛋白的土豆汁水溶液的pH为5,然后加入甘油,混匀后控制温度为121℃进行灭菌15min,得到灭菌后的去蛋白的土豆汁;Use 1% NaOH aqueous solution and 0.1% HCl aqueous solution to adjust the pH of the deproteinized potato juice aqueous solution obtained in step (2) to 5, then add glycerin, mix well and control the temperature to 121°C Sterilize for 15 minutes to obtain deproteinized potato juice after sterilization;
上述甘油的添加量为pH为7的去蛋白的土豆汁水溶液体积的5%;The added amount of above-mentioned glycerin is 5% of the volume of the potato juice aqueous solution that the pH is 7;
(4)、接种发酵(4), inoculation fermentation
向步骤(3)所得的灭菌后的去蛋白的土豆汁中接种甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769,然后控制温度为26℃,转速为100r/min进行发酵培养24h,得到发酵液;Inoculate Candida utilis CICC 1769 preserved in glycerol tubes into the sterilized protein-free potato juice obtained in step (3), and then control the temperature at 26°C and the rotation speed at 100r/min for fermentation culture 24h, obtain fermented liquid;
接种量按每100mL灭菌后的去蛋白土豆汁中接入6mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769;The amount of inoculum is to insert Candida utilis ( Candida utilis ) CICC 1769 preserved in a 6mL glycerol tube into every 100mL of sterilized deproteinized potato juice;
每1mL甘油管保藏的产朊假丝酵母菌(Candida utilis)CICC 1769中,含有的产朊假丝酵母菌(Candida utilis)CICC 1769菌数为1.6×109 CFU;Candida utilis ( Candida utilis ) CICC 1769 stored in each 1mL glycerol tube contains 1.6×10 9 CFU of Candida utilis ( Candida utilis ) CICC 1769;
(5)、将步骤(4)所得的发酵液用布氏漏斗进行过滤,去除滤液,得到的滤饼即为胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体;(5) Filter the fermentation broth obtained in step (4) with a Buchner funnel, remove the filtrate, and obtain a filter cake that contains Candida utilis β-D-glucan in the cells Bacteria;
经测定,按每lmL发酵液计算,得到8.91mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌;After determination, calculate by every 1mL fermented liquid, obtain the Candida utilis bacterium that contains Candida utilis β-D-glucan in the cell of 8.91mg;
每mg胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌,含β-D-葡聚糖0.0991mg;Candida utilis containing Candida utilis β-D-glucan per mg cell, containing 0.0991mg of β-D-glucan;
即本发明的生产方法所得的每mL发酵液中含有产朊假丝酵母β-D-葡聚糖0.6021mg;That is, each mL of fermented liquid obtained by the production method of the present invention contains 0.6021 mg of Candida utilis β-D-glucan;
(6)、在121℃条件下,按质量比计算,胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体:蒸馏水为15:100的比例,用蒸馏水将步骤(5)所得的胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体进行浸提30min,以使产朊假丝酵母菌体进行细胞破壁,然后经过超声波细胞破碎仪在频率为20KHz,功率为800W下进行超声处理60min,然后在10000r/min下离心15min,所得的沉淀用蒸馏水进行洗涤,直至流出液澄清,终止洗涤,然后再控制温度为-20℃,真空度为10Pa进行真空冷冻干燥,即得产朊假丝酵母β-D-葡聚糖。(6) Under the condition of 121°C, the ratio of Candida utilis bacteria containing Candida utilis β-D-glucan in the cell: distilled water is 15:100 calculated by mass ratio. Extracting the Candida utilis cells containing Candida utilis β-D-glucan in the cells obtained in step (5) for 30 minutes, so that the cells of the Candida utilis cells are broken down, Then, the frequency of the ultrasonic cell disruptor is 20KHz, the power is 800W, and the ultrasonic treatment is carried out for 60min, and then centrifuged at 10000r/min for 15min, and the precipitate obtained is washed with distilled water until the effluent is clear, and the washing is terminated, and then the temperature is controlled to be -20°C, vacuum freeze-drying at 10 Pa to obtain Candida utilis β-D-glucan.
经测定,上述所得的产朊假丝酵母β-D-葡聚糖的产率为83%、得率为14%,纯度为96%。It was determined that the yield of the Candida utilis β-D-glucan obtained above was 83%, the yield was 14%, and the purity was 96%.
综上所述,本发明的一种产朊假丝酵母β-D-葡聚糖的生产方法,由于生产过程中利用的去淀粉的土豆汁原料经检测,pH值为4.82,为29.8g O2/L及BOD5的值为15.6g O2/L,其接近于马铃薯淀粉工厂废弃的土豆汁的pH、COD、BOD5指标,因此本发明的产朊假丝酵母β-D-葡聚糖的生产方法可以用马铃薯淀粉工厂的废弃土豆汁作为培养基的原料来进行生产,同时由于生产过程中所得的胞内含有产朊假丝酵母β-D-葡聚糖的产朊假丝酵母菌菌体通过采用高温浸提和超声破壁协同作用的提取方法,最终得到的高产率、高纯度、高得率的产朊假丝酵母酵母β-D-葡聚糖,其得率最高可达19%,其纯度最高可达97%,产率最高可达87%。In summary, a kind of production method of Candida utilis β-D-glucan of the present invention, because the potato juice raw material of removing starch utilized in the production process is tested, pH value is 4.82, is 29.8g. 2 /L and the value of BOD 5 is 15.6g O 2 /L, which is close to the pH, COD, BOD 5 index of the potato juice discarded by the potato starch factory, so the Candida utilis β-D-glucan of the present invention The production method of sugar can use the waste potato juice from the potato starch factory as the raw material of the medium for production. By adopting the extraction method of high-temperature extraction and ultrasonic wall breaking synergistically, the high-yield, high-purity, and high-yield Candida utilis yeast β-D-glucan is finally obtained, and the highest yield can be up to 19%, its purity can reach up to 97%, and its yield can reach up to 87%.
以上实施例仅用于说明本发明的内容,除此之外,本发明还有其他实施方式,但凡本领域技术人员因本发明所涉及之技术启示,而采用等同替换或等效变形方式形成的技术方案均落在本发明的保护范围内。The above embodiments are only used to illustrate the content of the present invention. In addition, the present invention also has other implementation modes, as long as those skilled in the art adopt equivalent replacement or equivalent deformation methods due to the technical inspiration involved in the present invention. The technical solutions all fall within the protection scope of the present invention.
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710898784.8A CN107502631A (en) | 2017-09-28 | 2017-09-28 | A kind of production method of candida utili β D glucans |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201710898784.8A CN107502631A (en) | 2017-09-28 | 2017-09-28 | A kind of production method of candida utili β D glucans |
Publications (1)
Publication Number | Publication Date |
---|---|
CN107502631A true CN107502631A (en) | 2017-12-22 |
Family
ID=60699006
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201710898784.8A Pending CN107502631A (en) | 2017-09-28 | 2017-09-28 | A kind of production method of candida utili β D glucans |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN107502631A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110656080A (en) * | 2019-11-22 | 2020-01-07 | 顾霆 | Directional culture method of yeast cells |
CN111635916A (en) * | 2020-06-28 | 2020-09-08 | 上海应用技术大学 | A kind of pretreatment method for yeast β-glucan extraction |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102337309A (en) * | 2011-09-28 | 2012-02-01 | 吴力克 | Potato residue culture medium |
CN106397628A (en) * | 2016-10-11 | 2017-02-15 | 上海应用技术大学 | Method for extracting beta-D-glucan from cell walls of candida utilis |
-
2017
- 2017-09-28 CN CN201710898784.8A patent/CN107502631A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102337309A (en) * | 2011-09-28 | 2012-02-01 | 吴力克 | Potato residue culture medium |
CN106397628A (en) * | 2016-10-11 | 2017-02-15 | 上海应用技术大学 | Method for extracting beta-D-glucan from cell walls of candida utilis |
Non-Patent Citations (4)
Title |
---|
BZDUCHA-WROBEL ANNA ET AL: "Biosynthesis of β(1,3)/(1,6)-glucans of cell wall of the yeast Candida utilis ATCC 9950 strains in the culture media supplemented with deproteinated potato juice water and glycerol", 《EUR FOOD RES TECHNOL》 * |
吕文博等: "从马铃薯淀粉废水中提取饲料蛋白的研究", 《工业安全与环保》 * |
崔耀明: "《兽药制剂工艺》", 31 August 2007, 中国农业大学出版社 * |
马霞: "提取方法对产朊假丝酵母β-葡聚糖性质的影响", 《食品科学》 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110656080A (en) * | 2019-11-22 | 2020-01-07 | 顾霆 | Directional culture method of yeast cells |
CN111635916A (en) * | 2020-06-28 | 2020-09-08 | 上海应用技术大学 | A kind of pretreatment method for yeast β-glucan extraction |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN109400734B (en) | Rosa roxburghii polysaccharide and preparation method and application thereof | |
CN101643759B (en) | A method and special medium for preparing schizophyllan | |
CN111285939B (en) | Artemisia annua polysaccharide with effects of resisting oxidation and regulating intestinal flora and preparation method and application thereof | |
Guo et al. | In vitro digestion and fermentation by human fecal microbiota of polysaccharides from Clitocybe squamulose | |
EP3730623A1 (en) | Small-molecule hyaluronic acid or salt thereof, and preparation method therefor | |
CN106387923B (en) | Soluble dietary fiber rich in galactomannan and preparation method thereof | |
CN101756174B (en) | Method for extracting sweet buckwheat dietary fibers | |
CN101020915A (en) | Process of preparing yeast beta-glucosan | |
CN111978421A (en) | A kind of mulberry phoenix polysaccharide and its preparation and use | |
CN101792783B (en) | Preparation method and application of banana natural resistant starch RS2 | |
CN111172216A (en) | Cordyceps militaris polysaccharide with function of inhibiting macrophage from secreting NO, and preparation method and application thereof | |
CN112972520B (en) | Method for improving active ingredient yield by deeply fermenting eucommia ulmoides leaves with inonotus obliquus liquid | |
CN102925527A (en) | Method for mixing and fermenting flammulina velutipes and lucid ganoderma | |
CN107502631A (en) | A kind of production method of candida utili β D glucans | |
CN112094359A (en) | Extraction method of morchella polysaccharide, morchella polysaccharide drink and preparation method of morchella polysaccharide drink | |
CN114847494B (en) | Method for extracting dietary fibers from reed shoots | |
CN113912750B (en) | Method for extracting ganoderma lucidum fruiting body polysaccharide through fermentation pretreatment | |
CN112961883B (en) | Heat-resistant white kidney bean amylase inhibitor and preparation method thereof | |
CN112079938A (en) | Highland barley polysaccharide extraction method, highland barley polysaccharide extract and application thereof | |
CN111700279A (en) | Preparation method of wheat bran dietary fiber | |
CN107236054B (en) | A kind of preparation method and application of low molecular weight alveoli | |
CN115838444B (en) | A method for extracting mugwort polysaccharides using microbial enzymatic hydrolysis | |
CN106036921A (en) | Preparation method of soluble olive dietary fibers | |
CN111264877A (en) | A kind of preparation method of medicinal and edible homologous high-fiber functional food | |
CN115944092A (en) | Method for preparing sargassum soluble dietary fiber through fermentation |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20171222 |
|
WD01 | Invention patent application deemed withdrawn after publication |