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CN106243242A - A kind of utilize degraded the solubilization technique method that Fructus Jujubae pectin is prepared in extraction from Fructus Jujubae Fructus Jujubae slag - Google Patents

A kind of utilize degraded the solubilization technique method that Fructus Jujubae pectin is prepared in extraction from Fructus Jujubae Fructus Jujubae slag Download PDF

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CN106243242A
CN106243242A CN201610775084.5A CN201610775084A CN106243242A CN 106243242 A CN106243242 A CN 106243242A CN 201610775084 A CN201610775084 A CN 201610775084A CN 106243242 A CN106243242 A CN 106243242A
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pectin
jujube
fructus jujubae
extract
dregs
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李涛
门燕
康振奎
张富刚
张佩舜
朱玥明
李晨光
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SHANXI TIANJIAO BIOLOGICAL GROUP CO Ltd
Shanxi Tianjiao Food Co ltd
Tianjin Institute of Industrial Biotechnology of CAS
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SHANXI TIANJIAO BIOLOGICAL GROUP CO Ltd
Shanxi Tianjiao Food Co ltd
Tianjin Institute of Industrial Biotechnology of CAS
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    • C08B37/00Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
    • C08B37/0006Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
    • C08B37/0045Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid alpha-D-Galacturonans, e.g. methyl ester of (alpha-1,4)-linked D-galacturonic acid units, i.e. pectin, or hydrolysis product of methyl ester of alpha-1,4-linked D-galacturonic acid units, i.e. pectinic acid; Derivatives thereof

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Abstract

The present invention is a kind of utilizes the degraded solubilization technique method that Fructus Jujubae pectin is prepared in extraction from Fructus Jujubae Fructus Jujubae slag, belongs to technical field of food biotechnology;Comprising the following steps, Fructus Jujubae slag pretreatment, demetalization ion, the multienzyme method of fractional steps is extracted, and first carries out cellulase, hemicellulose complex enzyme zymohydrolysis, then carries out protease, lipase complex enzyme zymohydrolysis, centrifugal, and decolouring concentrates, and is dried, prepares finished product;The present invention uses many enzyme extraction methods to combine chelating method and extracts Fructus Jujubae pectin;Obtain the specific Fructus Jujubae pectin product with enhancing human body immunity that a kind of purity is high, gelation is good, make full use of Fructus Jujubae and be worth, improve Fructus Jujubae resource utilization, reduce environmental pollution and the wasting of resources simultaneously;Through technology purification pectin products such as decolouring and membrance separation, product purity is high, and extraction ratio is high.

Description

一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的 方法A method for preparing jujube pectin from jujube dregs by using degradation and solubilization technology method

技术领域technical field

本发明一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,属于食品生物技术领域。The invention discloses a method for extracting and preparing jujube pectin from jujube dregs by using degradation and solubilization technology, belonging to the field of food biotechnology.

背景技术Background technique

果胶是组织物细胞壁的成分之一,存在于相邻细胞壁间的细胞层中,起着将细胞壁黏在一起的作用。不同来源的果胶,其特性也各有差异。天然果胶是以线性多糖为主,含有从几百到1000多个糖元形成的链状结构,平均分子量为50万-150万。果胶主链分子的基本成分是D-半乳糖醛酸,还有一些天然中性糖如鼠李糖、阿拉伯糖、木糖、半乳糖、葡萄糖等也存在于果胶中。果胶为略带黄色的白色粉状物,溶于水中,形成粘稠的无味溶液,带负电。果胶是一种天然高分子化合物,具有良好的胶凝性和乳化稳定性作用,已经广泛用于食品、医药、日化及纺织品行业。Pectin is one of the components of the cell wall of tissues. It exists in the cell layer between adjacent cell walls and plays the role of sticking the cell walls together. Different sources of pectin have different properties. Natural pectin is mainly linear polysaccharides, containing a chain structure of several hundred to more than 1,000 glycogens, with an average molecular weight of 500,000-1.5 million. The basic component of the main chain molecule of pectin is D-galacturonic acid, and some natural neutral sugars such as rhamnose, arabinose, xylose, galactose, glucose, etc. also exist in pectin. Pectin is a yellowish white powder that dissolves in water to form a viscous, odorless solution that is negatively charged. Pectin is a natural polymer compound with good gelation and emulsification stability, and has been widely used in food, medicine, daily chemical and textile industries.

据报道,全世界果胶的年需求量近4.5万t,目前我国每年约消耗果胶1500t以上,其中80%从国外进口。果胶作为食品添加剂,其需求量在相当长的时间内仍将以每年15%的速度增长。因进口果胶的价格是国产果胶价格的1~2倍,所以生产中迫切需要低价、高质量的国产果胶,增加果胶产量、改善果胶质量是我国果胶产业发展的目标,充分利用我国丰富的果胶资源,生产出优质果胶,满足国内市场需求,符合我国食品添加剂行业的发展方向。According to reports, the annual demand for pectin in the world is nearly 45,000 tons. At present, my country consumes more than 1,500 tons of pectin every year, of which 80% are imported from abroad. As a food additive, the demand for pectin will continue to grow at an annual rate of 15% for quite a long time. Because the price of imported pectin is 1 to 2 times the price of domestic pectin, there is an urgent need for low-priced, high-quality domestic pectin in production. Increasing pectin production and improving pectin quality are the goals of the development of my country's pectin industry. Make full use of my country's rich pectin resources to produce high-quality pectin to meet the needs of the domestic market and in line with the development direction of my country's food additive industry.

红枣是中国的特色果品,具有悠久的栽培历史,红枣营养丰富而全面,是一种具有很高营养和药用价值的果品。红枣枣渣是红枣加工后的副产物,但是由于枣渣、枣皮中功能性物质含量较低导致提取率低,提取过程复杂,所用有机溶剂极易污染环境,同时其他大部分果胶多糖不能充分利用,因此不能大范围应用于工业生产。除此之外,由于技术薄弱,红枣加工副产物枣渣枣皮的开发利用仍处于初级阶段,主要用作家畜饲料或作为废弃物排放,造成了环境污染和资源浪费。Jujube is a special fruit in China with a long history of cultivation. Jujube is rich in nutrition and comprehensive, and it is a fruit with high nutritional and medicinal value. Jujube dregs are the by-products of jujube processing. However, due to the low content of functional substances in jujube dregs and jujube skin, the extraction rate is low, the extraction process is complicated, and the organic solvents used are easy to pollute the environment. At the same time, most other pectin polysaccharides cannot Fully utilized, so it cannot be widely used in industrial production. In addition, due to weak technology, the development and utilization of jujube dregs and jujube skin, a by-product of jujube processing, is still in its infancy. It is mainly used as livestock feed or discharged as waste, causing environmental pollution and waste of resources.

红枣中果胶资源含量非常丰富,尤其是在枣皮以及枣渣。红枣果胶分子量在2000kD以上(凝胶程度高、质量稳定的果胶产品均集中在分子量大的范围内),远远大于其他植物提取的果胶分子量,同时研究表明红枣果胶具有一定的增强机体免疫的作用。故选用红枣枣渣作为果胶提取的原料,可以得到凝胶效果好,具有增强机体免疫特异性的果胶物质。The content of pectin resources in jujube is very rich, especially in jujube skin and jujube dregs. The molecular weight of jujube pectin is above 2000kD (the pectin products with high gel degree and stable quality are all concentrated in the range of large molecular weight), which is far greater than the molecular weight of pectin extracted from other plants. At the same time, studies have shown that jujube pectin has a certain enhancement The role of the body's immunity. Therefore, jujube jujube dregs are selected as raw materials for pectin extraction, and pectin substances with good gel effect and specificity for enhancing the body's immunity can be obtained.

但是红枣中果胶具有难脱色、难纯化的特点。红枣中红色素较深,含有相对多的钙、铁离子,而钙、铁离子对果胶有很强的封闭作用,其存在的情况下不利于果胶溶出(脱封闭离子),红枣果胶在细胞中螯合了大量的钙离子,同时与纤维素、蛋白质、脂类物质以及淀粉物质等以共价键、非共价键形式形成纤维状空间结构,使果胶很难溶解出来。同时,红枣果胶中还含有大量脂溶性成分,对果胶的纯化有很大的影响(脱脂质物)。但是普通的酸碱提取法不能够完全将红枣中果胶物质提取出来,而且还会破坏果胶物质的分子结构。However, pectin in jujube is difficult to decolorize and purify. The red pigment in jujube is darker and contains relatively more calcium and iron ions, and calcium and iron ions have a strong sealing effect on pectin, which is not conducive to the dissolution of pectin (deblocking ions). Jujube pectin A large amount of calcium ions are chelated in the cell, and at the same time, it forms a fibrous space structure with cellulose, protein, lipid and starch in the form of covalent or non-covalent bonds, making it difficult to dissolve pectin. At the same time, jujube pectin also contains a large amount of fat-soluble components, which have a great impact on the purification of pectin (skimmed matter). However, the common acid-base extraction method cannot completely extract the pectin substance in jujube, and it will also destroy the molecular structure of the pectin substance.

发明内容Contents of the invention

本发明克服现有技术的不足,所要解决的技术问题是提供一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,得到一种纯度高、凝胶性好的具有增强机体免疫的特异性的红枣果胶产品;使用红枣枣渣提取果胶产品,充分利用红枣价值,提高红枣资源利用率。The present invention overcomes the deficiencies of the prior art, and the technical problem to be solved is to provide a method for extracting and preparing jujube pectin from jujube dregs by using degradation and solubilization technology, so as to obtain a kind of pectin with high purity and good gelling property and enhanced body Immune specific jujube pectin products; use jujube dregs to extract pectin products, make full use of the value of jujube, and improve the utilization rate of jujube resources.

为解决上述技术问题,本发明所采用的技术方案为:一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,包括以下步骤:In order to solve the above-mentioned technical problems, the technical solution adopted in the present invention is: a method for extracting and preparing jujube pectin from jujube dregs by using degradation and solubilization technology, comprising the following steps:

第一步,枣渣预处理,灭菌;将枣渣粉碎,过100目筛,加入体积的95%乙醇回流20min,过滤除去乙醇,用蒸馏水冲洗枣渣至洗涤液无色为止,60℃烘干后备用;The first step is pretreatment and sterilization of jujube dregs; crush jujube dregs, pass through a 100-mesh sieve, add 95% ethanol by volume to reflux for 20 minutes, filter to remove ethanol, rinse jujube dregs with distilled water until the washing liquid is colorless, and bake at 60°C dry and ready for use;

枣渣组织中除了含有丰富的果胶外,还含有能够分解果胶的果胶酶系,包括果胶酯酶、果胶裂解酶等,若不进行预处理灭酶活,在加热提取的过程中,果胶分子上的中性糖侧链,就会大量被降解消除掉,使果胶的分子量变小、空间结构发生改变,进而导致提取率和品质降低。故而提取果胶之前一般先预处理枣渣,以达到灭活果胶酶的目的。In addition to rich pectin, jujube dregs also contain pectinases that can decompose pectin, including pectinesterase and pectin lyase. In the process, the neutral sugar side chains on the pectin molecules will be degraded and eliminated in large quantities, making the molecular weight of pectin smaller and the spatial structure changed, which will lead to a decrease in extraction rate and quality. Therefore, jujube dregs are generally pretreated before pectin is extracted to achieve the purpose of inactivating pectinase.

第二步,脱金属离子;采用EDTA螯合剂辅助法,将上步的得到的枣渣样品加入到0.05mol/L的EDTA溶液中,使液固比为24:1(L/kg),提取温度35℃,时间3-4h,得到提取液;The second step is to remove metal ions; using EDTA chelating agent-assisted method, add the jujube dregs sample obtained in the previous step into 0.05mol/L EDTA solution, so that the liquid-solid ratio is 24:1 (L/kg), extract The temperature is 35°C, the time is 3-4h, and the extract is obtained;

红枣细胞中含有相对多的钙、铁离子,而钙、铁离子对果胶有很强的封闭作用,其存在的情况下不利于果胶溶出(脱封闭离子),同时,金属离子的存在会对酶的作用产生抑制作用。故在使用酶法提取果胶之前,所以先采用螯合剂将Ga离子从果胶结构中脱离下来。Jujube cells contain relatively many calcium and iron ions, and calcium and iron ions have a strong sealing effect on pectin, and the presence of calcium and iron ions is not conducive to the dissolution of pectin (deblocking ions). At the same time, the existence of metal ions will Inhibits the action of enzymes. Therefore, before enzymatic extraction of pectin, a chelating agent is used to remove Ga ions from the pectin structure.

第三步,多酶分步法提取;先进行纤维素酶、半纤维素复合酶酶解,将上述提取液进行纤维素酶、半纤维素复合酶酶解,通过正交试验得到最佳的酶解条件为:以纤维素酶:半纤维素酶1.2:1混合的复合酶,温度45℃、pH4.5、酶加量为0.8%,提取时间4-5h;The third step is multi-enzyme step-by-step extraction; firstly carry out enzymatic hydrolysis with cellulase and hemicellulose compound enzyme, then carry out the enzymatic hydrolysis of the above extract with cellulase and hemicellulose compound enzyme, and obtain the best The enzymatic hydrolysis conditions are: compound enzyme mixed with cellulase: hemicellulase 1.2:1, temperature 45°C, pH 4.5, enzyme dosage 0.8%, extraction time 4-5h;

再进行蛋白酶、脂肪酶复合酶酶解,上述酶解反应结束后,将反应液温度调节到55℃,pH6,将木瓜蛋白酶及脂肪酶按1:1的比例加入到反应液中,酶加量为1.0%,提取时间为3-4h。得到果胶酶解液;Then carry out protease and lipase compound enzyme enzymatic hydrolysis. After the above enzymatic hydrolysis reaction is completed, adjust the temperature of the reaction solution to 55 ° C and pH 6, and add papain and lipase to the reaction solution in a ratio of 1:1. 1.0%, the extraction time is 3-4h. Obtain pectin enzymatic hydrolysis solution;

目前,果胶的提取方法主要有酸提取法、酶提法、微生物发酵法等。酸提法其原理是采用稀酸将果皮细胞中的非水溶性原果胶水解为水溶性果胶,果胶产率能达到26%以上,但提取过程中果胶分子会发生局部水解,降低了果胶相对分子质量,从而影响果胶收率和质量,如提取过程一般采用较高温度和长时间的加热,使原料中的果胶不可避免的产生变形和分解破环,质量较差。此外,由于提取液粘度大、过滤慢,因而导致生产周期长、效率低;酶提取法是近年来天然提取领域发展迅速的提取方法,与传统碱法和酸法相比,具有提取时间短、产品质量高和节省能耗等优点,但由于不同原料对酶的要求不一,因此增加了技术难度。此外,单一酶系进行提取,并不能完全提取果胶物质造成提取率低。故采用多酶分步提取方法,根据果胶的结构分步使用不同的酶系,使红枣果胶完全的从其纤维网状结构中分离出来。At present, the extraction methods of pectin mainly include acid extraction, enzyme extraction, microbial fermentation and so on. The principle of the acid extraction method is to use dilute acid to hydrolyze the non-water-soluble protopectin in the pericarp cells into water-soluble pectin, and the yield of pectin can reach more than 26%, but the pectin molecules will be partially hydrolyzed during the extraction process, reducing the yield of pectin. The relative molecular weight of pectin is affected, thereby affecting the yield and quality of pectin. For example, the extraction process generally adopts higher temperature and long-term heating, so that the pectin in the raw material is inevitably deformed, decomposed and damaged, and the quality is poor. In addition, due to the high viscosity of the extract and slow filtration, the production cycle is long and the efficiency is low; the enzyme extraction method is an extraction method that has developed rapidly in the field of natural extraction in recent years. It has the advantages of high quality and energy saving, but because different raw materials have different requirements for enzymes, it increases the technical difficulty. In addition, the extraction by a single enzyme system cannot completely extract the pectin substance, resulting in a low extraction rate. Therefore, a multi-enzyme step-by-step extraction method is adopted, and different enzyme systems are used step by step according to the structure of the pectin, so that the jujube pectin is completely separated from its fiber network structure.

(1)纤维素酶、半纤维素酶:大多数果胶类物质以共价键或非共价键的形式与细胞壁的纤维素、半纤维素等大分子缔合,同时它们与其它细胞壁多聚体通过次级键相互缔合形成纤维状的空间结构。(1) Cellulase, hemicellulase: most pectin substances are associated with macromolecules such as cellulose and hemicellulose in the cell wall in the form of covalent or non-covalent bonds, and they are more The polymers associate with each other through secondary bonds to form a fibrous spatial structure.

(2)蛋白酶及脂肪酶:红枣中含有丰富的蛋白质、脂肪类物质,这些物质均以共价键或非共价键的形式结合在果胶结构中,造成果胶水溶性下降。(2) Protease and lipase: Red dates are rich in protein and fat substances, which are combined in the pectin structure in the form of covalent bonds or non-covalent bonds, resulting in a decrease in the water solubility of pectin.

第四步,离心;将第三步得到的果胶酶解液15000r/min离心5min,去除不溶物以及酶剂,得到果胶提取液。The fourth step is centrifugation; the pectin enzymatic hydrolysis solution obtained in the third step is centrifuged at 15,000 r/min for 5 minutes to remove insoluble matter and enzyme agent to obtain a pectin extract.

去除不溶物以及酶剂,但是经过酶解提取后,酶解液中会融入色素等小分子的杂质,需要经过脱色以及膜分离等技术纯化果胶产品。Remove insoluble matter and enzymes, but after enzymatic hydrolysis and extraction, small molecular impurities such as pigments will be incorporated into the enzymatic hydrolysis solution, and pectin products need to be purified by decolorization and membrane separation.

第五步,脱色;将处理过的D900型脱色树脂装入规格为600mm×50mm的层析柱中,装入量为柱子高度的2/3,调节pH值为6备用,将第四步得到的果胶提取液在室温条件下,以200mL/h的流速下通过树脂进行脱色,收集脱色后果胶提取液备用;The fifth step is decolorization; the processed D900 type decolorization resin is loaded into a chromatographic column with a specification of 600mm × 50mm, and the loading amount is 2/3 of the height of the column, and the pH value is adjusted to 6 for subsequent use, and the fourth step is obtained The pectin extract solution is decolorized by resin at a flow rate of 200mL/h at room temperature, and the decolorized pectin extract solution is collected for subsequent use;

红枣中红色素较深,具有难脱色的特点,在第一步中乙醇处理虽然可以出去部分表面的色素,但是大部分的色素分子还存在与枣渣种,随着果胶的提取溶解到酶解液中,影响到果胶的纯度。故需要选择合适的脱色方法进行脱色。The red pigment in jujube is deep and difficult to decolorize. In the first step, ethanol treatment can remove part of the pigment on the surface, but most of the pigment molecules still exist in the jujube dregs. With the extraction of pectin, they dissolve into the enzyme solution, affecting the purity of pectin. Therefore, it is necessary to choose a suitable decolorization method for decolorization.

选用大孔吸附树脂法脱色,该方法处理能力大,脱色容量高,能除去各种不同的色素,可以反复再生使用,使用寿命长,成本费用低,减少化学物质对果胶的污染。The macroporous adsorption resin method is used for decolorization. This method has large processing capacity, high decolorization capacity, can remove various pigments, can be recycled repeatedly, has a long service life, low cost, and reduces the pollution of chemical substances to pectin.

第六步,浓缩;采用5种不同截留分子量(300KD、100KD、30KD、10KD、5KD)的超滤膜组件分离果胶,在室温条件、入口压力70kPa、出口压力30kPa下,将脱色后果胶提取液经循环泵依次输入到分子量由大到小的膜组件中,经超滤分离后得到大于300KD、300KD-100KD、100KD-30KD、30KD-10KD、10KD-5KD以及小于5KD六部分果胶样品液;The sixth step is concentration; 5 kinds of ultrafiltration membrane modules with different molecular weight cut-offs (300KD, 100KD, 30KD, 10KD, 5KD) are used to separate pectin. The liquid is sequentially input into the membrane modules with molecular weight from large to small through the circulation pump, and after ultrafiltration separation, six parts of pectin sample liquids greater than 300KD, 300KD-100KD, 100KD-30KD, 30KD-10KD, 10KD-5KD and less than 5KD are obtained. ;

采用膜分离浓缩法。真空浓缩方法易导致果胶溶液褐变,影响品质,故采用膜分离浓缩方法,该方法可从果胶提取液中有选择性地分离出糖类物质和其他低分子化合物,从而得到优质果胶,此技术简单高效,低碳环保,有利于设备的维护和对果胶优良品质的保持,同时可根据不同膜分子量可得到不同分子量范围的果胶产品,不同分子量的果胶产品具有不同的功效,而凝胶程度高、质量稳定的果胶产品均集中在分子量大的范围内。Using membrane separation and concentration method. The vacuum concentration method is easy to cause browning of the pectin solution, which affects the quality. Therefore, the membrane separation and concentration method is adopted. This method can selectively separate sugars and other low-molecular compounds from the pectin extract, thereby obtaining high-quality pectin , this technology is simple and efficient, low-carbon and environmentally friendly, which is conducive to the maintenance of equipment and the maintenance of the excellent quality of pectin. At the same time, pectin products with different molecular weight ranges can be obtained according to different molecular weights of the membranes. Pectin products with different molecular weights have different effects , while pectin products with high gel degree and stable quality are all concentrated in the range of large molecular weight.

第七步,干燥;采用喷雾干燥机干燥,将不同组分的果胶样品液在130℃~160℃瞬时雾化干燥得到不同分子量的果胶成品;干燥后的产品经60目筛筛粉,即得到不同分子量果胶粉;The seventh step is drying; use a spray dryer to dry, spray and dry pectin sample liquids of different components at 130°C to 160°C instantaneously to obtain pectin products with different molecular weights; the dried products are sieved through a 60-mesh sieve, That is, different molecular weight pectin powders are obtained;

果胶的干燥技术对果胶的品质有着重要的影响,主要的干燥方法有低温干燥、喷雾干燥和真空冷冻干燥三种。其中低温干燥得到的果胶产品溶解性差,色泽较深,真空冷冻干燥具有耗能大,时间长等缺点。故选用喷雾干燥法,该法可不经沉淀字节用喷雾干燥技术得到产品,所得产品粉粒小,溶解性好,成本低。The drying technology of pectin has an important influence on the quality of pectin. There are three main drying methods: low temperature drying, spray drying and vacuum freeze drying. Among them, the pectin product obtained by low-temperature drying has poor solubility and darker color, and vacuum freeze-drying has the disadvantages of large energy consumption and long time. Therefore, the spray-drying method is selected, and the product can be obtained by spray-drying technology without precipitation, and the obtained product has small particles, good solubility and low cost.

第八步,制备成品;选择100KD以上的超滤膜组件分离的果胶,得到分子量大于100KD的红枣果胶成品。The eighth step is to prepare the finished product; select the pectin separated by the ultrafiltration membrane module above 100KD to obtain the finished product of jujube pectin with a molecular weight greater than 100KD.

由于高分子量的果胶物质具有更优的凝胶性和稳定性,故选择分子量大于100KD的超滤膜组件分离果胶,得到分子量大于100KD的红枣果胶物质。Since the high molecular weight pectin substance has better gelatinity and stability, the ultrafiltration membrane module with a molecular weight greater than 100KD is selected to separate pectin, and the jujube pectin substance with a molecular weight greater than 100KD is obtained.

所述的一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,第八步所得红枣果胶成品,为淡黄色或浅棕色粉末,干燥减量为5.43 w%±0.12,二氧化硫:32.21mg/kg±0.24,酸不溶灰分:0.73 w%±0.03,总半乳糖醛酸:89.96 w%±0.64,铅:0.35 mg/kg±0.02。。The method for preparing jujube pectin from jujube dregs by using degradation and solubilization technology, the finished product of jujube pectin obtained in the eighth step is light yellow or light brown powder, and the drying loss is 5.43 w%±0.12, Sulfur dioxide: 32.21 mg/kg±0.24, acid-insoluble ash: 0.73 w%±0.03, total galacturonic acid: 89.96 w%±0.64, lead: 0.35 mg/kg±0.02. .

所述的一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,第六步,浓缩红枣果胶主要集中在大分子量部分,达到90%以上;其中分子量大于300KD达到78.24%以上, 300KD-100KD部分占14.31%以上。In the method for preparing jujube pectin from jujube dregs by using degradation and solubilization technology, in the sixth step, the concentrated jujube pectin is mainly concentrated in the large molecular weight part, reaching more than 90%; wherein the molecular weight is greater than 300KD and reaches 78.24% Above, the 300KD-100KD part accounts for more than 14.31%.

与现有技术相比本发明具有以下有益效果。Compared with the prior art, the present invention has the following beneficial effects.

1、红枣果胶独特的营养价值,红枣中果胶资源含量非常丰富,尤其是在枣皮以及枣渣。红枣果胶分子量在2000kD以上(凝胶程度高、质量稳定的果胶产品均集中在分子量大的范围内),远远大于其他植物提取的果胶分子量,同时研究表明红枣果胶具有一定的增强机体免疫的作用。1. The unique nutritional value of jujube pectin. The pectin resource content in jujube is very rich, especially in jujube skin and jujube dregs. The molecular weight of jujube pectin is above 2000kD (the pectin products with high gel degree and stable quality are all concentrated in the range of large molecular weight), which is far greater than the molecular weight of pectin extracted from other plants. At the same time, studies have shown that jujube pectin has a certain enhancement The role of the body's immunity.

2、本发明采用多酶提取法结合螯合法提取红枣果胶;得到一种纯度高、凝胶性好的具有增强机体免疫的特异性的红枣果胶产品。2. The present invention adopts a multi-enzyme extraction method combined with a chelation method to extract jujube pectin; a jujube pectin product with high purity and good gelatinity and the specificity of enhancing body immunity is obtained.

3、使用红枣枣渣提取果胶产品,可以充分利用红枣价值,提高红枣资源利用率。同时减少环境污染和资源浪费。3. Using jujube dregs to extract pectin products can make full use of the value of jujube and improve the utilization rate of jujube resources. At the same time reduce environmental pollution and waste of resources.

4、采用多酶分步提取方法,根据果胶的结构分步使用不同的酶系,使红枣果胶完全的从其纤维网状结构中分离出来。先进行纤维素酶、半纤维素复合酶酶解,破坏物质的空间结构,更有利于下一步破坏共价键或非共价键结构;再进行蛋白酶、脂肪酶复合酶酶解,使果胶完全的从空间结构中脱离出来。4. Using multi-enzyme step-by-step extraction method, different enzyme systems are used step by step according to the structure of pectin, so that jujube pectin can be completely separated from its fiber network structure. Carry out cellulase and hemicellulose compound enzyme enzymolysis first to destroy the spatial structure of the substance, which is more conducive to the next step to destroy the covalent bond or non-covalent bond structure; then carry out protease and lipase compound enzyme enzymolysis to make pectin Completely break away from the spatial structure.

5、经过脱色以及膜分离等技术纯化果胶产品,产品纯度高,提取率高。5. The pectin product is purified by decolorization and membrane separation technology, so the product has high purity and high extraction rate.

6、由于红枣果胶主要集中在大分子量部分,达到90%以上,分子量大于300KD的占大多数,达到78.24%,其次是300KD-100KD部分,占14.31%。故通过膜分离技术得到分子量大于100KD的红枣果胶物质。6. Since jujube pectin is mainly concentrated in the large molecular weight part, reaching more than 90%, the molecular weight greater than 300KD accounts for the majority, reaching 78.24%, followed by the 300KD-100KD part, accounting for 14.31%. Therefore, the jujube pectin substance with a molecular weight greater than 100KD is obtained by membrane separation technology.

7、提取过程低温、无污染。整个提取过程除喷雾干燥的瞬时高温,温度均未超过60℃,避免了高温对果胶质量的影响。此外整个过程未加入任何的化学物质,避免了化学物质对果胶的污染。7. The extraction process is low temperature and pollution-free. Except for the instantaneous high temperature of spray drying during the whole extraction process, the temperature does not exceed 60°C, which avoids the influence of high temperature on the quality of pectin. In addition, no chemical substances are added in the whole process, which avoids the pollution of pectin by chemical substances.

具体实施方式detailed description

以下结合具体实施例对本发明作进一步说明。The present invention will be further described below in conjunction with specific examples.

实施例1Example 1

一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,包括以下步骤:A method for extracting and preparing jujube pectin from jujube dregs by using degradation solubilization technology, comprising the following steps:

第一步,枣渣预处理,灭菌;将枣渣粉碎,过100目筛,加入体积的95%乙醇回流20min,过滤除去乙醇,用蒸馏水冲洗枣渣至洗涤液无色为止,60℃烘干后得到枣渣样品备用;The first step is pretreatment and sterilization of jujube dregs; crush jujube dregs, pass through a 100-mesh sieve, add 95% ethanol by volume to reflux for 20 minutes, filter to remove ethanol, rinse jujube dregs with distilled water until the washing liquid is colorless, and bake at 60°C Obtain the jujube dregs sample after drying for subsequent use;

第二步,脱金属离子;采用EDTA螯合剂辅助法,将上步的得到的枣渣样品加入到0.05mol/L的EDTA溶液中,使液固比为24:1(L/kg),提取温度35℃,时间3h,得到提取液;The second step is to remove metal ions; using EDTA chelating agent-assisted method, add the jujube dregs sample obtained in the previous step into 0.05mol/L EDTA solution, so that the liquid-solid ratio is 24:1 (L/kg), extract The temperature is 35°C, and the time is 3h to obtain the extract;

第三步,多酶分步法提取;先进行纤维素酶、半纤维素复合酶酶解,将上述提取液进行纤维素酶、半纤维素复合酶酶解,酶解条件为:以纤维素酶:半纤维素酶1.2:1混合的复合酶,温度45℃、pH4.5、酶加量为提取液质量的0.8%,提取时间为4h, 得到反应液;The third step is multi-enzyme step-by-step extraction; firstly, carry out enzymatic hydrolysis with cellulase and hemicellulose compound enzyme, and then carry out the enzymatic hydrolysis of the above extract with cellulase and hemicellulose compound enzyme. The enzymatic hydrolysis conditions are: use cellulose Enzyme: compound enzyme mixed with hemicellulase 1.2:1, temperature 45°C, pH 4.5, the amount of enzyme added is 0.8% of the mass of the extract, and the extraction time is 4 hours to obtain a reaction solution;

再进行蛋白酶、脂肪酶复合酶酶解,将反应液温度调节到55℃,pH6,将木瓜蛋白酶及脂肪酶按1:1的比例加入到反应液中,酶 的总量为反应液质量的1.0%,提取时间为4h,得到果胶酶解液;Then carry out protease and lipase compound enzymatic hydrolysis, adjust the temperature of the reaction solution to 55°C, pH6, add papain and lipase to the reaction solution in a ratio of 1:1, the total amount of enzyme is 1.0% of the mass of the reaction solution %, the extraction time is 4h, and the pectin enzymatic hydrolyzate is obtained;

第四步,离心;将第三步得到的果胶酶解液15000r/min离心5min,去除不溶物以及酶剂,得到果胶提取液;The fourth step is centrifugation; the pectin enzymatic hydrolysis solution obtained in the third step is centrifuged at 15,000 r/min for 5 minutes to remove insoluble matter and enzymes to obtain a pectin extract;

第五步,脱色;将处理过的D900型脱色树脂装入规格为600mm×50mm的层析柱中,装入量为柱子高度的2/3,调节pH值为6备用,将第四步得到的果胶提取液在室温条件下,以200mL/h的流速下通过树脂进行脱色,收集脱色后果胶提取液备用;The fifth step is decolorization; the processed D900 type decolorization resin is loaded into a chromatographic column with a specification of 600mm × 50mm, and the loading amount is 2/3 of the height of the column, and the pH value is adjusted to 6 for subsequent use, and the fourth step is obtained The pectin extract solution is decolorized by resin at a flow rate of 200mL/h at room temperature, and the decolorized pectin extract solution is collected for subsequent use;

第六步,浓缩;采用不同截留分子量(300KD、100KD、30KD、10KD、5KD)的5种超滤膜组件分离果胶,在室温条件、入口压力70kPa、出口压力30kPa下,将脱色后果胶提取液经循环泵依次输入到分子量由大到小的膜组件中,经超滤分离后得到大于300KD、300KD-100KD、100KD-30KD、30KD-10KD、10KD-5KD以及小于5KD六部分果胶样品液;The sixth step is concentration; 5 kinds of ultrafiltration membrane modules with different molecular weight cut-offs (300KD, 100KD, 30KD, 10KD, 5KD) are used to separate pectin, and at room temperature, the inlet pressure is 70kPa, and the outlet pressure is 30kPa. The liquid is sequentially input into the membrane modules with molecular weight from large to small through the circulation pump, and after ultrafiltration separation, six parts of pectin sample liquids greater than 300KD, 300KD-100KD, 100KD-30KD, 30KD-10KD, 10KD-5KD and less than 5KD are obtained. ;

第七步,干燥;采用喷雾干燥机干燥,将不同组分的果胶样品液在130℃~160℃瞬时雾化干燥得到不同分子量的果胶成品;干燥后的产品经60目筛筛粉,即得到不同分子量果胶粉;The seventh step is drying; use a spray dryer to dry, spray and dry pectin sample liquids of different components at 130°C to 160°C instantaneously to obtain pectin products with different molecular weights; the dried products are sieved through a 60-mesh sieve, That is, different molecular weight pectin powders are obtained;

第八步,制备成品;选择100KD以上的超滤膜组件分离的果胶,得到分子量大于100KD的红枣果胶成品。The eighth step is to prepare the finished product; select the pectin separated by the ultrafiltration membrane module above 100KD to obtain the finished product of jujube pectin with a molecular weight greater than 100KD.

所得红枣果胶成品,为淡黄色或浅棕色粉末,干燥减量为5.43 w%±0.12,二氧化硫:32.21 mg/kg±0.24,酸不溶灰分:0.73 w%±0.03,总半乳糖醛酸:89.96 w%±0.64,铅:0.35 mg/kg±0.02。。The obtained jujube pectin product is light yellow or light brown powder, drying loss is 5.43 w%±0.12, sulfur dioxide: 32.21 mg/kg±0.24, acid-insoluble ash: 0.73 w%±0.03, total galacturonic acid: 89.96 w%±0.64, lead: 0.35 mg/kg±0.02. .

实施例2Example 2

一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,包括以下步骤:A method for extracting and preparing jujube pectin from jujube dregs by using degradation solubilization technology, comprising the following steps:

第一步,枣渣预处理,灭菌;将枣渣粉碎,过100目筛,加入一定体积的95%乙醇回流20min,过滤除去乙醇,用蒸馏水冲洗枣渣至洗涤液无色为止,60℃烘干后备用;The first step, jujube dregs pretreatment, sterilization; crush jujube dregs, pass through a 100-mesh sieve, add a certain volume of 95% ethanol to reflux for 20 minutes, filter to remove ethanol, wash jujube dregs with distilled water until the washing liquid is colorless, 60 ° C dry and ready for use;

第二步,脱金属离子;采用EDTA螯合剂辅助法,将上步的得到的枣渣样品加入到0.05mol/L的EDTA溶液中,使液固比为24:1(L/kg),提取温度35℃,时间4h,得到提取液;The second step is to remove metal ions; using EDTA chelating agent-assisted method, add the jujube dregs sample obtained in the previous step into 0.05mol/L EDTA solution, so that the liquid-solid ratio is 24:1 (L/kg), extract The temperature is 35°C, and the time is 4h to obtain the extract;

第三步,多酶分步法提取;先进行纤维素酶、半纤维素复合酶酶解,将上述提取液进行纤维素酶、半纤维素复合酶酶解,酶解条件为:以纤维素酶:半纤维素酶1.2:1混合的复合酶,温度45℃、pH4.5、酶加量为0.8%,提取时间为5h;The third step is multi-enzyme step-by-step extraction; firstly, carry out enzymatic hydrolysis with cellulase and hemicellulose compound enzyme, and then carry out the enzymatic hydrolysis of the above extract with cellulase and hemicellulose compound enzyme. The enzymatic hydrolysis conditions are: use cellulose Enzyme: Hemicellulase 1.2:1 mixed enzyme, temperature 45°C, pH 4.5, enzyme dosage 0.8%, extraction time 5h;

再进行蛋白酶、脂肪酶复合酶酶解,将反应液温度调节到55℃,pH6,将木瓜蛋白酶及脂肪酶按1:1的比例加入到反应液中,酶加量为1.0%,提取时间为3h,得到果胶酶解液;Then carry out protease and lipase compound enzyme enzymolysis, adjust the temperature of the reaction solution to 55 ° C, pH 6, add papain and lipase to the reaction solution in a ratio of 1:1, the enzyme addition is 1.0%, and the extraction time is 3h, obtain pectin enzymatic hydrolysis solution;

第四步,离心;将第三步得到的果胶酶解液15000r/min离心5min,去除不溶物以及酶剂,得到果胶提取液;The fourth step is centrifugation; the pectin enzymatic hydrolysis solution obtained in the third step is centrifuged at 15,000 r/min for 5 minutes to remove insoluble matter and enzymes to obtain a pectin extract;

第五步,脱色;将处理过的D900型脱色树脂装入规格为600mm×50mm的层析柱中,装入量为柱子高度的2/3,调节pH值为6备用,将第四步得到的果胶提取液在室温条件下,以200mL/h的流速下通过树脂进行脱色,收集脱色后果胶提取液备用;The fifth step is decolorization; the processed D900 type decolorization resin is loaded into a chromatographic column with a specification of 600mm × 50mm, and the loading amount is 2/3 of the height of the column, and the pH value is adjusted to 6 for subsequent use, and the fourth step is obtained The pectin extract solution is decolorized by resin at a flow rate of 200mL/h at room temperature, and the decolorized pectin extract solution is collected for subsequent use;

第六步,浓缩;采用5种不同截留分子量(300KD、100KD、30KD、10KD、5KD)的超滤膜组件分离果胶,在室温条件、入口压力70kPa、出口压力30kPa下,将脱色后果胶提取液经循环泵依次输入到分子量由大到小的膜组件中,经超滤分离后得到大于300KD、300KD-100KD、100KD-30KD、30KD-10KD、10KD-5KD以及小于5KD六部分果胶样品液;The sixth step is concentration; 5 kinds of ultrafiltration membrane modules with different molecular weight cut-offs (300KD, 100KD, 30KD, 10KD, 5KD) are used to separate pectin. The liquid is sequentially input into the membrane modules with molecular weight from large to small through the circulation pump, and after ultrafiltration separation, six parts of pectin sample liquids greater than 300KD, 300KD-100KD, 100KD-30KD, 30KD-10KD, 10KD-5KD and less than 5KD are obtained. ;

第七步,干燥;采用喷雾干燥机干燥,将不同组分的果胶样品液在130℃~160℃瞬时雾化干燥得到不同分子量的果胶成品;干燥后的产品经60目筛筛粉,即得到不同分子量果胶粉;The seventh step is drying; use a spray dryer to dry, spray and dry pectin sample liquids of different components at 130°C to 160°C instantaneously to obtain pectin products with different molecular weights; the dried products are sieved through a 60-mesh sieve, That is, different molecular weight pectin powders are obtained;

第八步,制备成品;选择100KD以上的超滤膜组件分离的果胶,得到分子量大于100KD的红枣果胶成品。The eighth step is to prepare the finished product; select the pectin separated by the ultrafiltration membrane module above 100KD to obtain the finished product of jujube pectin with a molecular weight greater than 100KD.

所得红枣果胶成品,为淡黄色或浅棕色粉末,干燥减量为干燥减量为5.43 w%±0.12,二氧化硫:32.21 mg/kg±0.24,酸不溶灰分:0.73 w%±0.03,总半乳糖醛酸:89.96w%±0.64,铅:0.35 mg/kg±0.02。。The obtained jujube pectin product is light yellow or light brown powder, the drying loss is 5.43 w% ± 0.12, sulfur dioxide: 32.21 mg/kg ± 0.24, acid insoluble ash: 0.73 w% ± 0.03, total galactose Alkyd acid: 89.96w%±0.64, lead: 0.35 mg/kg±0.02. .

实施例3Example 3

一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,包括以下步骤:A method for extracting and preparing jujube pectin from jujube dregs by using degradation solubilization technology, comprising the following steps:

第一步,枣渣预处理,灭菌;将枣渣粉碎,过100目筛,加入一定体积的95%乙醇回流20min,过滤除去乙醇,用蒸馏水冲洗枣渣至洗涤液无色为止,60℃烘干后备用;The first step, jujube dregs pretreatment, sterilization; crush jujube dregs, pass through a 100-mesh sieve, add a certain volume of 95% ethanol to reflux for 20 minutes, filter to remove ethanol, wash jujube dregs with distilled water until the washing liquid is colorless, 60 ° C dry and ready for use;

第二步,脱金属离子;采用EDTA螯合剂辅助法,将上步的得到的枣渣样品加入到0.05mol/L的EDTA溶液中,使液固比为24:1(L/kg),提取温度35℃,时间3.5h,得到提取液;The second step is to remove metal ions; using EDTA chelating agent-assisted method, add the jujube dregs sample obtained in the previous step into 0.05mol/L EDTA solution, so that the liquid-solid ratio is 24:1 (L/kg), extract The temperature is 35°C, and the time is 3.5h to obtain the extract;

第三步,多酶分步法提取;先进行纤维素酶、半纤维素复合酶酶解,将上述提取液进行纤维素酶、半纤维素复合酶酶解,酶解条件为:以纤维素酶:半纤维素酶1.2:1混合的复合酶,温度45℃、pH4.5、酶加量为0.8%,提取时间为4.5h;The third step is multi-enzyme step-by-step extraction; firstly, carry out enzymatic hydrolysis with cellulase and hemicellulose compound enzyme, and then carry out the enzymatic hydrolysis of the above extract with cellulase and hemicellulose compound enzyme. The enzymatic hydrolysis conditions are: use cellulose Enzyme: compound enzyme mixed with hemicellulase 1.2:1, temperature 45°C, pH 4.5, enzyme dosage 0.8%, extraction time 4.5h;

再进行蛋白酶、脂肪酶复合酶酶解,将反应液温度调节到55℃,pH6,将木瓜蛋白酶及脂肪酶按1:1的比例加入到反应液中,酶加量为1.0%,提取时间为3.5h,得到果胶酶解液;Then carry out protease and lipase compound enzyme enzymolysis, adjust the temperature of the reaction solution to 55 ° C, pH 6, add papain and lipase to the reaction solution in a ratio of 1:1, the enzyme addition is 1.0%, and the extraction time is 3.5h, obtain pectin enzymatic hydrolysis solution;

第四步,离心;将第三步得到的果胶酶解液15000r/min离心5min,去除不溶物以及酶剂,得到果胶提取液;The fourth step is centrifugation; the pectin enzymatic hydrolysis solution obtained in the third step is centrifuged at 15,000 r/min for 5 minutes to remove insoluble matter and enzymes to obtain a pectin extract;

第五步,脱色;将处理过的D900型脱色树脂装入规格为600mm×50mm的层析柱中,装入量为柱子高度的2/3,调节pH值为6备用,将第四步得到的果胶提取液在室温条件下,以200mL/h的流速下通过树脂进行脱色,收集脱色后果胶提取液备用;The fifth step is decolorization; the processed D900 type decolorization resin is loaded into a chromatographic column with a specification of 600mm × 50mm, and the loading amount is 2/3 of the height of the column, and the pH value is adjusted to 6 for subsequent use, and the fourth step is obtained The pectin extract solution is decolorized by resin at a flow rate of 200mL/h at room temperature, and the decolorized pectin extract solution is collected for subsequent use;

第六步,浓缩;采用5种不同截留分子量(300KD、100KD、30KD、10KD、5KD)的超滤膜组件分离果胶,在室温条件、入口压力70kPa、出口压力30kPa下,将脱色后果胶提取液经循环泵依次输入到分子量由大到小的膜组件中,经超滤分离后得到大于300KD、300KD-100KD、100KD-30KD、30KD-10KD、10KD-5KD以及小于5KD六部分果胶样品液;The sixth step is concentration; 5 kinds of ultrafiltration membrane modules with different molecular weight cut-offs (300KD, 100KD, 30KD, 10KD, 5KD) are used to separate pectin. The liquid is sequentially input into the membrane modules with molecular weight from large to small through the circulation pump, and after ultrafiltration separation, six parts of pectin sample liquids greater than 300KD, 300KD-100KD, 100KD-30KD, 30KD-10KD, 10KD-5KD and less than 5KD are obtained. ;

第七步,干燥;采用喷雾干燥机干燥,将不同组分的果胶样品液在130℃~160℃瞬时雾化干燥得到不同分子量的果胶成品;干燥后的产品经60目筛筛粉,即得到不同分子量果胶粉;The seventh step is drying; use a spray dryer to dry, spray and dry pectin sample liquids of different components at 130°C to 160°C instantaneously to obtain pectin products with different molecular weights; the dried products are sieved through a 60-mesh sieve, That is, different molecular weight pectin powders are obtained;

第八步,制备成品;选择100KD以上的超滤膜组件分离的果胶,得到分子量大于100KD的红枣果胶成品。The eighth step is to prepare the finished product; select the pectin separated by the ultrafiltration membrane module above 100KD to obtain the finished product of jujube pectin with a molecular weight greater than 100KD.

所得红枣果胶成品,为淡黄色或浅棕色粉末,干燥减量为干燥减量为5.43 w%±0.12,二氧化硫:32.21 mg/kg±0.24,酸不溶灰分:0.73 w%±0.03,总半乳糖醛酸:89.96w%±0.64,铅:0.35 mg/kg±0.02。。The obtained jujube pectin product is light yellow or light brown powder, the drying loss is 5.43 w% ± 0.12, sulfur dioxide: 32.21 mg/kg ± 0.24, acid insoluble ash: 0.73 w% ± 0.03, total galactose Alkyd acid: 89.96w%±0.64, lead: 0.35 mg/kg±0.02. .

实施例4Example 4

一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,包括以下步骤:A method for extracting and preparing jujube pectin from jujube dregs by using degradation solubilization technology, comprising the following steps:

第一步,枣渣预处理,灭菌;将枣渣粉碎,过100目筛,加入一定体积的95%乙醇回流20min,过滤除去乙醇,用蒸馏水冲洗枣渣至洗涤液无色为止,60℃烘干后备用;The first step, jujube dregs pretreatment, sterilization; crush jujube dregs, pass through a 100-mesh sieve, add a certain volume of 95% ethanol to reflux for 20 minutes, filter to remove ethanol, wash jujube dregs with distilled water until the washing liquid is colorless, 60 ° C dry and ready for use;

第二步,脱金属离子;采用EDTA螯合剂辅助法,将上步的得到的枣渣样品加入到0.05mol/L的EDTA溶液中,使液固比为24:1(L/kg),提取温度35℃,时间3h,得到提取液;The second step is to remove metal ions; using EDTA chelating agent-assisted method, add the jujube dregs sample obtained in the previous step into 0.05mol/L EDTA solution, so that the liquid-solid ratio is 24:1 (L/kg), extract The temperature is 35°C, and the time is 3h to obtain the extract;

第三步,多酶分步法提取;先进行纤维素酶、半纤维素复合酶酶解,将上述提取液进行纤维素酶、半纤维素复合酶酶解,酶解条件为:以纤维素酶:半纤维素酶1.2:1混合的复合酶,温度45℃、pH4.5、酶加量为0.8%,提取时间为5h;The third step is multi-enzyme step-by-step extraction; firstly, carry out enzymatic hydrolysis with cellulase and hemicellulose compound enzyme, and then carry out the enzymatic hydrolysis of the above extract with cellulase and hemicellulose compound enzyme. The enzymatic hydrolysis conditions are: use cellulose Enzyme: Hemicellulase 1.2:1 mixed enzyme, temperature 45°C, pH 4.5, enzyme dosage 0.8%, extraction time 5h;

再进行蛋白酶、脂肪酶复合酶酶解,将反应液温度调节到55℃,pH6,将木瓜蛋白酶及脂肪酶按1:1的比例加入到反应液中,酶加量为1.0%,提取时间为3h,得到果胶酶解液;Then carry out protease and lipase compound enzyme enzymolysis, adjust the temperature of the reaction solution to 55 ° C, pH 6, add papain and lipase to the reaction solution in a ratio of 1:1, the enzyme addition is 1.0%, and the extraction time is 3h, obtain pectin enzymatic hydrolysis solution;

第四步,离心;将第三步得到的果胶酶解液15000r/min离心5min,去除不溶物以及酶剂,得到果胶提取液;The fourth step is centrifugation; the pectin enzymatic hydrolysis solution obtained in the third step is centrifuged at 15,000 r/min for 5 minutes to remove insoluble matter and enzymes to obtain a pectin extract;

第五步,脱色;将处理过的D900型脱色树脂装入规格为600mm×50mm的层析柱中,装入量为柱子高度的2/3,调节pH值为6备用,将第四步得到的果胶提取液在室温条件下,以200mL/h的流速下通过树脂进行脱色,收集脱色后果胶提取液备用;The fifth step is decolorization; the processed D900 type decolorization resin is loaded into a chromatographic column with a specification of 600mm × 50mm, and the loading amount is 2/3 of the height of the column, and the pH value is adjusted to 6 for subsequent use, and the fourth step is obtained The pectin extract solution is decolorized by resin at a flow rate of 200mL/h at room temperature, and the decolorized pectin extract solution is collected for subsequent use;

第六步,浓缩;采用5种不同截留分子量(300KD、100KD、30KD、10KD、5KD)的超滤膜组件分离果胶,在室温条件、入口压力70kPa、出口压力30kPa下,将脱色后果胶提取液经循环泵依次输入到分子量由大到小的膜组件中,经超滤分离后得到大于300KD、300KD-100KD、100KD-30KD、30KD-10KD、10KD-5KD以及小于5KD六部分果胶样品液;The sixth step is concentration; 5 kinds of ultrafiltration membrane modules with different molecular weight cut-offs (300KD, 100KD, 30KD, 10KD, 5KD) are used to separate pectin. The liquid is sequentially input into the membrane modules with molecular weight from large to small through the circulation pump, and after ultrafiltration separation, six parts of pectin sample liquids greater than 300KD, 300KD-100KD, 100KD-30KD, 30KD-10KD, 10KD-5KD and less than 5KD are obtained. ;

第七步,干燥;采用喷雾干燥机干燥,将不同组分的果胶样品液在130℃~160℃瞬时雾化干燥得到不同分子量的果胶成品;干燥后的产品经60目筛筛粉,即得到不同分子量果胶粉;The seventh step is drying; use a spray dryer to dry, spray and dry pectin sample liquids of different components at 130°C to 160°C instantaneously to obtain pectin products with different molecular weights; the dried products are sieved through a 60-mesh sieve, That is, different molecular weight pectin powders are obtained;

第八步,制备成品;选择100KD以上的超滤膜组件分离的果胶,得到分子量大于100KD的红枣果胶成品。The eighth step is to prepare the finished product; select the pectin separated by the ultrafiltration membrane module above 100KD to obtain the finished product of jujube pectin with a molecular weight greater than 100KD.

所得红枣果胶成品,为淡黄色或浅棕色粉末,干燥减量为5.43 w%±0.12,二氧化硫:32.21 mg/kg±0.24,酸不溶灰分:0.73 w%±0.03,总半乳糖醛酸:89.96 w%±0.64,铅:0.35 mg/kg±0.02。。The obtained jujube pectin product is light yellow or light brown powder, drying loss is 5.43 w%±0.12, sulfur dioxide: 32.21 mg/kg±0.24, acid-insoluble ash: 0.73 w%±0.03, total galacturonic acid: 89.96 w%±0.64, lead: 0.35 mg/kg±0.02. .

本发明可用其他的不违背本发明的精神或主要特征的具体形式来概述。因此,无论从哪一点来看,本发明的上述实施方案都只能认为是对本发明的说明而不能限制发明,权利要求书指出了本发明的范围,而上述的说明并未指出本发明的范围,因此,在与本发明的权利要求书相当的含义和范围内的任何变化,都应认为是包括在权利要求书的范围内。The present invention may be embodied in other specific forms without departing from the spirit or main characteristics of the invention. Therefore, no matter from which point of view, the above-mentioned embodiments of the present invention can only be considered as explanations of the present invention and can not limit the invention. The claims indicate the scope of the present invention, but the above description does not indicate the scope of the present invention. Therefore, any changes within the meaning and scope equivalent to the claims of the present invention should be considered to be included in the scope of the claims.

Claims (5)

1.一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,其特征在于,包括以下步骤:1. a method utilizing degradation solubilization technology to extract and prepare jujube pectin from jujube dregs, is characterized in that, comprises the following steps: 第一步,枣渣预处理,灭菌;将枣渣粉碎,过100目筛,加入95%乙醇回流20min,过滤除去乙醇,用蒸馏水冲洗枣渣至洗涤液无色为止,60℃烘干后得到枣渣样品备用;The first step is pretreatment and sterilization of jujube dregs; crush jujube dregs, pass through a 100-mesh sieve, add 95% ethanol to reflux for 20 minutes, filter to remove ethanol, rinse jujube dregs with distilled water until the washing liquid is colorless, and dry at 60°C Obtain the jujube dregs sample for subsequent use; 第二步,脱金属离子;采用EDTA螯合剂辅助法,将上步的得到的枣渣样品加入到0.05mol/L的EDTA溶液中,使液固比为24 L:1kg,提取温度35℃,时间3-4h,得到提取液;The second step is to remove metal ions; using the EDTA chelating agent-assisted method, the jujube dregs sample obtained in the previous step is added to a 0.05mol/L EDTA solution, so that the liquid-solid ratio is 24 L: 1kg, and the extraction temperature is 35 ° C. Time 3-4h, get the extract; 第三步,多酶分步法提取;先进行纤维素酶、半纤维素复合酶酶解,将上述提取液进行纤维素酶、半纤维素复合酶酶解,酶解条件为:以纤维素酶:半纤维素酶1.2:1混合的复合酶,温度45℃、pH4.5、酶加量为提取液质量的0.8%,提取时间为4-5h,得到反应液;The third step is multi-enzyme step-by-step extraction; firstly, carry out enzymatic hydrolysis with cellulase and hemicellulose compound enzyme, and then carry out the enzymatic hydrolysis of the above extract with cellulase and hemicellulose compound enzyme. The enzymatic hydrolysis conditions are: use cellulose Enzyme: compound enzyme mixed with hemicellulase 1.2:1, temperature 45°C, pH 4.5, enzyme dosage 0.8% of the quality of the extract, extraction time 4-5h, to obtain a reaction solution; 再进行蛋白酶、脂肪酶复合酶酶解,将反应液温度调节到55℃,pH6,将木瓜蛋白酶及脂肪酶按1:1的比例加入到反应液中,酶的总量为反应液质量的1.0%,提取时间为3-4h,得到果胶酶解液;Then carry out protease and lipase compound enzymatic hydrolysis, adjust the temperature of the reaction solution to 55°C, pH6, add papain and lipase to the reaction solution in a ratio of 1:1, the total amount of enzyme is 1.0% of the mass of the reaction solution %, the extraction time is 3-4h, and the pectin enzymatic hydrolysis solution is obtained; 第四步,离心;将第三步得到的果胶酶解液15000r/min离心5min,去除不溶物以及酶剂,得到果胶提取液;The fourth step is centrifugation; the pectin enzymatic hydrolysis solution obtained in the third step is centrifuged at 15000r/min for 5min to remove insoluble matter and enzyme agent to obtain a pectin extract; 第五步,脱色;将处理过的D900型脱色树脂装入规格为600mm×50mm的层析柱中,装入量为柱子高度的2/3,调节pH值为6备用,将第四步得到的果胶提取液在室温条件下,以200mL/h的流速下通过树脂进行脱色,收集脱色后果胶提取液备用;The fifth step is decolorization; the processed D900 type decolorization resin is loaded into a chromatographic column with a specification of 600mm × 50mm, and the loading amount is 2/3 of the height of the column, and the pH value is adjusted to 6 for subsequent use, and the fourth step is obtained The pectin extract solution is decolorized by resin at a flow rate of 200mL/h at room temperature, and the decolorized pectin extract solution is collected for subsequent use; 第六步,浓缩;采用截留分子量分别为300KD、100KD、30KD、10KD、5KD的5种超滤膜组件分离果胶,在室温条件、入口压力70kPa、出口压力30kPa下,将脱色后果胶提取液经循环泵依次输入到截留分子量由大到小的膜组件中,经超滤分离后得到大于300KD、300KD-100KD、100KD-30KD、30KD-10KD、10KD-5KD以及小于5KD六部分果胶样品液;The sixth step is to concentrate; use 5 kinds of ultrafiltration membrane modules with molecular weight cut-offs of 300KD, 100KD, 30KD, 10KD, and 5KD to separate pectin, and extract the pectin after decolorization under room temperature, inlet pressure 70kPa, and outlet pressure 30kPa Through the circulation pump, it is input into the membrane modules with molecular weight cut off in order from large to small, and after ultrafiltration and separation, six parts of pectin sample liquids greater than 300KD, 300KD-100KD, 100KD-30KD, 30KD-10KD, 10KD-5KD and less than 5KD are obtained. ; 第七步,干燥;采用喷雾干燥机干燥,将不同组分的果胶样品液在130℃~160℃瞬时雾化干燥得到不同分子量的果胶成品;干燥后的产品经60目筛筛粉,即得到不同分子量果胶粉。The seventh step is drying; use a spray dryer to dry, spray and dry pectin sample liquids of different components at 130°C to 160°C instantaneously to obtain pectin products with different molecular weights; the dried products are sieved through a 60-mesh sieve, That is, different molecular weight pectin powders are obtained. 2.根据权利要求1所述的一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,其特征在于,选择100KD以上的超滤膜组件分离的果胶,得到分子量大于100KD的红枣果胶成品。2. a kind of method that utilizes degradation solubilization technology to extract and prepare jujube pectin from jujube dregs according to claim 1, is characterized in that, select the pectin separated by the ultrafiltration membrane module more than 100KD, obtain molecular weight greater than 100KD Jujube pectin finished product. 3.根据权利要求1所述的一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,其特征在于,浓缩红枣果胶主要集中在大分子量部分,100KD部分以上达到90%以上。3. A method of extracting and preparing jujube pectin from jujube dregs by utilizing degradation solubilization technology according to claim 1, characterized in that concentrated jujube pectin is mainly concentrated in the large molecular weight part, and more than 100KD part reaches 90% above. 4.根据权利要求1所述的一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,其特征在于,其中分子量大于300KD占78.24%以上, 300KD-100KD部分占14.31%以上。4. A method of extracting and preparing jujube pectin from jujube dregs using degradation and solubilization technology according to claim 1, wherein the molecular weight is greater than 300KD and accounts for more than 78.24%, and the part of 300KD-100KD accounts for more than 14.31% . 5.根据权利要求2所述的一种利用降解增溶技术从红枣枣渣中提取制备红枣果胶的方法,其特征在于,所得红枣果胶成品,为淡黄色或浅棕色粉末,干燥减量为5.43 w%±0.12,二氧化硫:32.21 mg/kg±0.24,酸不溶灰分:0.73 w%±0.03,总半乳糖醛酸:89.96 w%±0.64,铅:0.35 mg/kg±0.02。5. A method of extracting and preparing jujube pectin from jujube dregs using degradation and solubilization technology according to claim 2, characterized in that the finished product of jujube pectin is light yellow or light brown powder, and the weight loss is reduced by drying 5.43 w%±0.12, sulfur dioxide: 32.21 mg/kg±0.24, acid-insoluble ash: 0.73 w%±0.03, total galacturonic acid: 89.96 w%±0.64, lead: 0.35 mg/kg±0.02.
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