WO2024066140A1 - 同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统 - Google Patents

同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统 Download PDF

Info

Publication number
WO2024066140A1
WO2024066140A1 PCT/CN2023/072281 CN2023072281W WO2024066140A1 WO 2024066140 A1 WO2024066140 A1 WO 2024066140A1 CN 2023072281 W CN2023072281 W CN 2023072281W WO 2024066140 A1 WO2024066140 A1 WO 2024066140A1
Authority
WO
WIPO (PCT)
Prior art keywords
roxburghii
treatment
treatment device
sod
retentate
Prior art date
Application number
PCT/CN2023/072281
Other languages
English (en)
French (fr)
Inventor
廖小军
李楚源
杨焕治
翁少全
赵靓
郑荣波
王永涛
赵阳
Original Assignee
中国农业大学
广州王老吉大健康产业有限公司
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 中国农业大学, 广州王老吉大健康产业有限公司 filed Critical 中国农业大学
Publication of WO2024066140A1 publication Critical patent/WO2024066140A1/zh

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
    • C08B37/0003—General processes for their isolation or fractionation, e.g. purification or extraction from biomass
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D307/56—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D307/62—Three oxygen atoms, e.g. ascorbic acid
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12M—APPARATUS FOR ENZYMOLOGY OR MICROBIOLOGY; APPARATUS FOR CULTURING MICROORGANISMS FOR PRODUCING BIOMASS, FOR GROWING CELLS OR FOR OBTAINING FERMENTATION OR METABOLIC PRODUCTS, i.e. BIOREACTORS OR FERMENTERS
    • C12M21/00—Bioreactors or fermenters specially adapted for specific uses
    • C12M21/18—Apparatus specially designed for the use of free, immobilized or carrier-bound enzymes

Definitions

  • the present invention relates to the field of food, and in particular to a method and system for simultaneously extracting roxburghii polysaccharides, roxburghii polyphenols, roxburghii SOD and Vc from roxburghii residues.
  • Rosa roxburghiiTratt is the fruit of the perennial deciduous shrub Rosa roxburghiiTratt of the Rosaceae family. It is rich in SOD, Vc, polyphenols, trace elements and other active ingredients and is known as the "Three King Fruits”. Rosa roxburghiiTratt is widely planted in southwest my country, mainly in Guizhou.
  • roxburghii residue is limited to the extraction of dietary fiber and polysaccharides, ultrafine powder of roxburghii residue, fermentation of fruit vinegar, production of feed and cultivation fertilizer, etc.
  • Roxburghii residue also contains rich active ingredients such as polysaccharides, polyphenols, SOD, Vc, etc., and has excellent processing performance and high utilization value.
  • most of the roxburghii residue is discarded and has not been reasonably and effectively developed and utilized, resulting in serious waste of resources and environmental pollution.
  • the present invention aims to solve the technical problems existing in the prior art at least to a certain extent.
  • the present invention proposes a method and system for simultaneously extracting roxburgh roxburgh polysaccharides, roxburgh polyphenols, roxburgh SOD and Vc from roxburgh roxburgh residues, and the method and system can effectively extract roxburgh roxburgh polysaccharides, roxburgh polyphenols, roxburgh SOD and Vc from roxburgh roxburgh residues with high yield, realize the efficient utilization of roxburgh roxburgh by-products, produce high value-added products, and promote the development of roxburgh roxburgh industry, which is of great significance.
  • the present invention proposes a method for simultaneously extracting roxburgh polysaccharides, roxburgh polyphenols, roxburgh SOD and Vc from roxburgh residue.
  • the method comprises: enzymolysis treatment of roxburgh residue to obtain an enzymolysis treatment product; grinding treatment of the enzymolysis treatment product to obtain grinding slurry; ultrasonic treatment of the grinding slurry to obtain an ultrasonic treatment product; centrifugation treatment of the ultrasonic treatment product to collect the supernatant; ceramic membrane ultrafiltration treatment of the supernatant to obtain a first permeate and a first retentate, wherein the first retentate contains roxburgh polysaccharides; macroporous adsorption resin treatment of the first permeate to obtain roxburgh de-astringent liquid and treated macroporous adsorption resin; elution treatment and evaporation concentration treatment of the treated macroporous adsorption resin with
  • the roxburghii slag is subjected to enzymolysis treatment, and the enzymolysis can effectively destroy the roxburghii tissue fiber, so that the active ingredients in the roxburghii slag are released. Then the product after enzymolysis is ground to make a grinding slurry.
  • the grinding slurry is subjected to ultrasonic treatment, which can further break the roxburghii cell wall and fully release the active ingredients in the roxburghii slag.
  • the ultrasonic treatment product is centrifuged to remove the precipitate, and the supernatant is subjected to ceramic membrane ultrafiltration treatment.
  • roxburghii polysaccharides Since the molecular weight of roxburghii polysaccharides is large and cannot pass through the ceramic membrane, it can be effectively retained, and the retained liquid containing roxburghii polysaccharides is collected, and the (first) permeate will be used for subsequent treatment.
  • the inventor found through a large number of experiments that macroporous adsorption resin has a good adsorption effect on roxburghii polyphenols, and then macroporous adsorption resin can be used to adsorb it, and it can be eluted from the macroporous adsorption resin after elution treatment.
  • the de-astringent liquid obtained in the previous step is subjected to a spiral membrane ultrafiltration treatment to effectively separate the highly active SOD, and the (second) permeate is subjected to a reverse osmosis treatment to effectively separate Vc.
  • the inventor creatively obtained the above series of treatment methods through a large number of experiments, thereby achieving the effect of simultaneously extracting roxburghii polysaccharides, roxburghii polyphenols, roxburghii SOD and Vc from roxburghii residues.
  • the method for simultaneously extracting roxburghii polysaccharides, roxburghii polyphenols, roxburghii SOD and Vc from roxburghii residues may also have the following additional technical features:
  • the enzymatic hydrolysis treatment comprises: soaking the roxburghii residue in an enzymatic hydrolysis solution; the enzyme in the enzymatic hydrolysis solution is selected from at least one of cellulase and pectinase; the concentration of the enzymatic hydrolysis solution is 0.1-0.5 volume %; the solid-liquid ratio of the roxburghii residue to the enzymatic hydrolysis solution is 1:40-1:50 g/mL; the soaking temperature is 30-40°C, and the time is 10-30 minutes.
  • the inventor obtained the above-mentioned preferred enzymatic hydrolysis treatment conditions through a large number of experiments, thereby effectively destroying the roxburghii tissue fibers and improving the release rate of active ingredients in the roxburghii residue.
  • the ultrasonic treatment time is 30 to 60 minutes, and the power is 100 to 300 W.
  • the inventors obtained the above-mentioned optimal conditions through experimental optimization, thereby effectively breaking the cell wall and fully releasing the active ingredients in the roxburghii residue.
  • the rotation speed of the centrifugal treatment is 1000-5000 rpm and the time is 10-30 minutes, thereby effectively removing the precipitate and reducing the loss of effective components, which is helpful for subsequent experiments.
  • the pore size of the ceramic membrane is 50-150 kDa.
  • the inventors obtained the above-mentioned preferred pore size through a large number of experiments, thereby being able to retain roxburghii polysaccharides to achieve the purpose of separation and extraction, and the obtained retentate containing roxburghii polysaccharides has a high concentration of roxburghii polysaccharides and few impurities.
  • the macroporous adsorption resin is selected from AB-8, and the eluent is selected from food-grade anhydrous ethanol, thereby polyphenols can be adsorbed, and the polyphenols adsorbed on the macroporous adsorption resin can be washed off by eluting with anhydrous ethanol.
  • the pore size of the spiral membrane is 10 to 30 kDa.
  • the pore size is better, so that the highly active SOD can be effectively retained to achieve the purpose of separation and extraction.
  • the SOD-containing retentate has a high SOD concentration and few impurities.
  • the pore size of the reverse osmosis membrane used in the reverse osmosis treatment is 0.3-2 nm.
  • the inventors obtained the above-mentioned preferred pore size through a large number of experiments, thereby effectively retaining Vc.
  • the method further comprises: drying the retentate containing roxburghii polysaccharide, roxburghii polyphenol, roxburghii SOD and retentate containing Vc respectively to obtain roxburghii polysaccharide powder, roxburghii polyphenol powder, roxburghii SOD powder and roxburghii Vc powder respectively; the drying process is carried out by freeze drying, wherein the cold well temperature is -65 to -80°C and the time is 24 to 48 hours.
  • the feed liquid can be dried and the loss of nutrients can be reduced.
  • the present invention proposes a system for implementing the aforementioned method of simultaneously extracting roxburghii polysaccharides, roxburghii polyphenols, roxburghii SOD and Vc from roxburghii residues.
  • the system includes: an enzymatic hydrolysis treatment device, the enzymatic hydrolysis treatment device is suitable for enzymatic hydrolysis treatment of roxburghii residues to obtain an enzymatic hydrolysis treatment product; a pulping treatment device, the pulping treatment device is connected to the enzymatic hydrolysis treatment device, and is suitable for pulping the enzymatic hydrolysis product to obtain a grinding slurry; an ultrasonic treatment device, the ultrasonic treatment device is connected to the pulping treatment device, and is suitable for centrifuging the ultrasonic treatment product to collect the supernatant; a ceramic membrane ultrafiltration treatment device, the ceramic membrane ultrafiltration treatment device is connected to the ultrasonic treatment device, and is suitable for ceramic membrane ultrafiltration treatment of the supernatant to obtain a first permeate and a first retentate, wherein the first retentate contains roxburghii polysaccharides; a macroporous adsorption resin treatment device, the macroporous adsorption resin treatment device, the macropor
  • the system of the invention can effectively extract roxburgh polysaccharides, roxburgh polyphenols, roxburgh SOD and Vc in roxburgh residue with high yield, realizes efficient utilization of roxburgh by-products, produces high value-added products, and promotes the development of roxburgh industry, which is of great significance.
  • the system further comprises: a drying device, wherein the drying device is respectively connected to the ceramic membrane ultrafiltration treatment device, the evaporation concentration treatment device, the spiral membrane ultrafiltration treatment device and the reverse osmosis treatment device, and is suitable for respectively drying the retentate containing roxburghii polysaccharide, roxburghii polyphenols, the retentate containing roxburghii SOD and the retentate containing Vc.
  • the liquid is dried to obtain roxburghii polysaccharide powder, roxburghii polyphenol powder, roxburghii SOD powder and roxburghii Vc powder.
  • the liquid can be dried and the loss of nutrients can be avoided.
  • the present invention adopts enzymatic hydrolysis (cellulase and/or pectinase), pulping and ultrasonic crushing to jointly treat the roxburghii residue, which can effectively destroy the tissue fibers and cell walls of the roxburghii residue and fully extract the active substances in the roxburghii residue.
  • the grinding slurry after ultrasonic extraction of the present invention is centrifuged to obtain a centrifuge of active substances of roxburghii, and the precipitate obtained by centrifugation can be used as an animal feed additive for cattle, sheep and the like, which is both environmentally friendly and can be fully utilized.
  • the present invention uses macroporous adsorption resin AB-8 to treat the centrifuge liquid, which can effectively adsorb the roxburghii polyphenols to obtain the roxburghii de-astringent liquid.
  • the present invention uses ultrafiltration and reverse osmosis technology to process the roxburghii de-astringent liquid, effectively separates and concentrates the roxburghii active ingredients, and improves the content of nutrients, especially SOD, Vc, etc.
  • the present invention adopts freeze drying treatment, can obtain roxburghii powder with different components in large quantities, and retains the original nutrients in roxburghii to the maximum extent, is convenient for transportation and storage, has the advantages of low cost, high efficiency, strong practicability, and suitability for industrial production.
  • the roxburghii polysaccharide powder, polyphenol powder, SOD powder and Vc powder obtained by the method of the present invention have high purity and high activity, which improves the nutritional value of the product and effectively solves the loss and instability of nutrients such as Vc and SOD during processing.
  • the preparation method is simple, low in cost, and suitable for large-scale production. Therefore, the product obtained by the method of the present invention is more beneficial to human health.
  • FIG1 shows a schematic flow chart of a method for simultaneously extracting roxburghii polysaccharides, roxburghii polyphenols, roxburghii SOD and Vc from roxburghii residues according to an embodiment of the present invention.
  • the following method is used to simultaneously extract roxburghii polysaccharides, roxburghii polyphenols, roxburghii SOD and Vc from roxburghii residues:
  • the roxburghii pulp is subjected to ultrasonic extraction, the ultrasonic extraction tank is 100 L, the ultrasonic time is 45 min, and the ultrasonic power is 300 W to obtain the roxburghii pulp.
  • the roxburghii extract pulp is centrifuged by horizontal screw centrifugation at a speed of 4000 rpm for 20 min to obtain the roxburghii centrifuge liquid.
  • the roxburghii centrifuge liquid was subjected to ceramic membrane ultrafiltration treatment, the pore size of the ceramic membrane was 100 kDa, and a retentate 1 (roxburghii polysaccharide liquid) and a permeate 1 were obtained.
  • the permeate 1 was treated with AB-8 macroporous adsorption resin, the resin column height was 2 m, and the column inner diameter was 40 cm, to obtain the roxburghii de-astringent liquid.
  • the de-astringent liquid of the roxburghii roxburghii was subjected to ultrafiltration treatment: a spiral membrane with a pore size of 10 kDa was used to obtain a retentate 2 (roxburghii roxburghii SOD liquid) and a permeate 2.
  • the permeate 2 is subjected to reverse osmosis treatment, the pore size of the reverse osmosis membrane is 2 nm, and a retentate 3 (Vc) and a permeate 3 are obtained.
  • the retentate 1, the roxburghii polyphenols, the retentate 2, and the retentate 3 are dried by freeze drying at a cold well temperature of -65°C for 48 hours to obtain roxburghii polysaccharide powder, roxburghii polyphenol powder, roxburghii SOD powder, and roxburghii Vc powder, respectively.
  • roxburghii powder The different components of roxburghii powder were prepared according to the method of Example 1, except that the enzymatic hydrolysate in step (2) was replaced by Drinking water, without enzymatic treatment.
  • Example 1 The method of Example 1 is followed, except that the ultrasonic extraction treatment in step (4) is not performed.
  • Example 1 The method of Example 1 is followed, except that the enzymatic hydrolysis treatment in step (2) and the ultrasonic extraction treatment in step (4) are not performed.
  • Example 1 The method of Example 1 is followed, except that the AB-8 macroporous adsorption resin in step (7) is replaced by D101 macroporous adsorption resin.
  • Example 1 The results are shown in Table 1. It can be seen that the yields of the roxburghii polysaccharide powder, polyphenol powder, SOD powder and Vc powder prepared in Example 1 are the highest. Compared with Example 1, the different roxburghii powders obtained by the treatment of Comparative Example 1 (no enzymolysis), Comparative Example 2 (no ultrasound) and Comparative Example 3 (no enzymolysis + no ultrasound) are reduced to varying degrees, among which Comparative Example 3 is the most reduced.
  • Comparative Example 4 (D101 macroporous adsorption resin) has no effect on the yields of roxburghii polysaccharides, SOD and Vc, but the yield of the roxburghii polyphenol powder obtained by the treatment is about 10% lower than that of Example 1, indicating that Example 1 can more effectively adsorb polyphenols and improve the yield of polyphenols by using AB-8 macroporous adsorption resin treatment. Therefore, it is more conducive to preparing roxburghii powders of different components from roxburghii residues through processes such as enzymolysis, ultrasound, AB-8 macroporous adsorption resin treatment, ultrafiltration, reverse osmosis, freeze drying and the like.
  • Table 1 Yields of different components of roxburghii powder prepared in different cases

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Biochemistry (AREA)
  • Zoology (AREA)
  • Wood Science & Technology (AREA)
  • Genetics & Genomics (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Sustainable Development (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Biomedical Technology (AREA)
  • Biotechnology (AREA)
  • Microbiology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

本发明提出了同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统，所述方法包括：酶解处理、磨浆处理、超声处理、离心处理、陶瓷膜超滤处理、大孔吸附树脂处理、洗脱处理、蒸发浓缩处理、卷式膜超滤处理和反渗透处理。

Description

同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统 技术领域
本发明涉及食品领域。具体地，本发明涉及同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统。
背景技术
刺梨(Rosa roxburghiiTratt)是蔷薇科多年生落叶灌木缫丝花的果实，富含SOD、Vc、多酚、微量元素等多种活性成分，被誉为“三王水果”。我国西南地区广泛种植刺梨，主产于贵州。
现今，对刺梨渣的开发仅限于膳食纤维及多糖提取、刺梨渣超微粉、发酵果醋、生产饲料及栽培肥料等。刺梨渣中还存在含量丰富的多糖、多酚、SOD、Vc等活性成分，同时加工性能优良，具有很高的利用价值。但极大部分的刺梨渣被丢弃，未被合理有效地开发利用，造成了严重的资源浪费和环境污染。
因此，如何有效地提取出刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法仍有待研究。
发明内容
本发明旨在至少在一定程度上解决现有技术中存在的技术问题。为此，本发明提出了同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统，利用该方法和系统可以有效地提取出刺梨渣中的刺梨多糖、刺梨多酚、刺梨SOD和Vc，收率高，实现了刺梨副产物的高效利用，生产高附加值产品，促进刺梨产业发展，具有重要意义。
本发明提出了一种同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法。根据本发明的实施例，所述方法包括：将刺梨渣进行酶解处理，得到酶解处理产物；将所述酶解处理产物进行磨浆处理，得到研磨浆；将所述研磨浆进行超声处理，得到超声处理产物；将所述超声处理产物进行离心处理，收集上清液；将所述上清液进行陶瓷膜超滤处理，得到第一透过液和第一截留液，所述第一截留液中含有刺梨多糖；将所述第一透过液进行大孔吸附树脂处理，得到刺梨脱涩液和处理后的大孔吸附树脂；将所述处理后的大孔吸附树脂采用乙醇溶液进行洗脱处理和蒸发浓缩处理，得到刺梨多酚物；将所述刺梨脱涩液进行卷式膜超滤处理，得到第二透过液和第二截留液，所述第二截留液中含有刺梨SOD；将所述第二透过液进行反渗透处理，收集第三截留液，所述第三截留液中含有Vc。
根据本发明实施例的方法中，通过对刺梨渣进行酶解处理，酶解能有效破坏刺梨组织纤维，使刺梨渣中活性成分得到释放。然后将酶解后的产物进行磨浆，制成研磨浆。将研磨浆进行超声处理，可以进一步破碎刺梨细胞壁，使刺梨渣中活性成分充分释放。将超声处理产物进行离心处理，以便除去沉淀，将上清液进行陶瓷膜超滤处理，由于刺梨多糖的分子量较大无法通过陶瓷膜，从而可以有效地将其截留，收集含有刺梨多糖的截留液，(第一)透过液将用于后续处理。发明人通过大量实验发现，大孔吸附树脂对刺梨多酚的吸附效果较好，进而可以采用大孔吸附树脂将其吸附，后续经过洗脱处理可以将其从大孔吸附树脂上洗脱下来。同时，多酚类物质存在会导致产品具有涩味，通过大孔吸附树脂吸附，可以有效地起到脱涩效果。将上步所得脱涩液进行卷式膜超滤处理，可以有效地分离出活性高的SOD，(第二)透过液进行反渗透处理，可以有效地分离出Vc。发明人经过大量实验创造性地获得上述一系列处理方式，由此可以实现同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的效果。
根据本发明的实施例，上述同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法还可以具有下列附加技术特征：
根据本发明的实施例，所述酶解处理包括：将刺梨渣浸泡于酶解液中；所述酶解液中的酶选自纤维素酶和果胶酶中的至少之一；所述酶解液的浓度为0.1～0.5体积％；所述刺梨渣与酶解液的料液比为1:40～1:50g/mL；所述浸泡的温度为30～40℃，时间为10～30分钟。发明人经过大量实验得到上述较优酶解处理条件，由此，可以有效地破坏刺梨组织纤维，提高刺梨渣中活性成分释放率。
根据本发明的实施例，所述超声处理的时间为30～60分钟，功率为100～300W。发明人经过实验优化得到上述较优条件，由此，可以有效地破碎细胞壁，使刺梨渣中活性成分充分释放。
根据本发明的实施例，所述离心处理的转速为1000～5000rpm，时间为10～30分钟。由此，可以有效地去除沉淀，且减少有效成分损失，有助于后续实验进行。
根据本发明的实施例，所述陶瓷膜的孔径为50～150kDa。发明人经过大量实验得到上述较优孔径，由此，可以截留刺梨多糖，达到分离提取的目的，得到的含有刺梨多糖的截留液中刺梨多糖浓度高、杂质少。
根据本发明的实施例，所述大孔吸附树脂选自AB-8，洗脱剂选自食品级无水乙醇。由此，可以吸附多酚类物质，并且经无水乙醇洗脱可以洗下吸附于大孔吸附树脂上的多酚类物质。
根据本发明的实施例，所述卷式膜的孔径为10～30kDa。发明人经过大量实验得到上述 较优孔径，由此，可以有效地截留活性高的SOD，达到分离提取目的，含有SOD的截留液中SOD浓度高、杂质少。
根据本发明的实施例，所述反渗透处理采用的反渗透膜的孔径为0.3～2nm。发明人经过大量实验得到上述较优孔径，由此，可以有效地截留Vc。
根据本发明的实施例，所述方法进一步包括：分别将含有刺梨多糖的截留液、刺梨多酚物、含有刺梨SOD的截留液和含有Vc的截留液进行干燥处理，分别得到刺梨多糖粉、刺梨多酚粉、刺梨SOD粉和刺梨Vc粉；所述干燥处理是采用冷冻干燥进行的，其中，冷井温度为-65～-80℃，时间为24～48小时。由此，可以使料液干燥，且减少营养成分损失。
在本发明的另一方面，本发明提出了一种实施前面所述同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法的系统。根据本发明的实施例，所述系统包括：酶解处理装置，所述酶解处理装置适于将刺梨渣进行酶解处理，得到酶解处理产物；磨浆处理装置，所述磨浆处理装置与所述酶解处理装置相连，适于将所述酶解处理产物进行磨浆处理，得到研磨浆；超声处理装置，所述超声处理装置与所述磨浆处理装置相连，适于将所述超声处理产物进行离心处理，收集上清液；陶瓷膜超滤处理装置，所述陶瓷膜超滤处理装置与所述超声处理装置相连，适于将所述上清液进行陶瓷膜超滤处理，得到第一透过液和第一截留液，所述第一截留液中含有刺梨多糖；大孔吸附树脂处理装置，所述大孔吸附树脂处理装置与所述陶瓷膜超滤处理装置相连，适于将所述第一透过液进行大孔吸附树脂处理，得到刺梨脱涩液和处理后的大孔吸附树脂；洗脱处理装置，所述洗脱处理装置与所述大孔吸附树脂处理装置相连，适于将所述处理后的大孔吸附树脂采用乙醇溶液进行洗脱处理；蒸发浓缩处理装置，所述蒸发浓缩处理装置与所述洗脱处理装置相连，适于将所述洗脱处理所得洗脱液进行蒸发浓缩处理，得到刺梨多酚物；卷式膜超滤处理装置，所述卷式膜超滤处理装置与所述蒸发浓缩处理装置相连，适于将所述刺梨脱涩液进行卷式膜超滤处理，得到第二透过液和第二截留液，所述第二截留液中含有刺梨SOD；反渗透处理装置，所述反渗透处理装置与所述卷式膜超滤处理装置相连，适于将所述第二透过液进行反渗透处理，收集第三截留液，所述第三截留液中含有Vc。
利用本发明的系统可以有效地提取出刺梨渣中的刺梨多糖、刺梨多酚、刺梨SOD和Vc，收率高，实现了刺梨副产物的高效利用，生产高附加值产品，促进刺梨产业发展，具有重要意义。
根据本发明的实施例，所述系统进一步包括：干燥装置，所述干燥装置分别与所述陶瓷膜超滤处理装置、蒸发浓缩处理装置、卷式膜超滤处理装置和反渗透处理装置相连，适于分别将含有刺梨多糖的截留液、刺梨多酚物、含有刺梨SOD的截留液和含有Vc的截留 液进行干燥处理，分别得到刺梨多糖粉、刺梨多酚粉、刺梨SOD粉和刺梨Vc粉。由此，可以使料液干燥，且避免营养成分损失。
需要说明的是，前面针对同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法所描述的特征和优点，同样适用于该系统，在此不再赘述。
本发明的有益效果在于：
1)本发明采用酶解(纤维素酶和/或果胶酶)、磨浆和超声破碎等技术联合处理刺梨渣，能高效破坏刺梨渣组织纤维、细胞壁，充分提取刺梨渣中活性物质。
2)本发明超声提取后的研磨浆采用离心获得刺梨活性物质离心液，离心获得的沉淀可作为牛羊等动物饲料添加剂，既环保，又可得到充分利用。
3)本发明采用大孔吸附树脂AB-8对离心液进行处理，可以有效地吸附刺梨多酚类物质，获得刺梨脱涩液。
4)本发明采用超滤和反渗透技术对刺梨脱涩液进行处理，有效对刺梨活性成分进行分离和浓缩，提高营养成分含量，尤其是SOD、Vc等。
5)本发明采用冷冻干燥处理，可大批量获得不同成分刺梨粉，并最大限度保留刺梨中原有营养成分，同时便于运输与贮藏，具有成本低、效率高、实践性强、适合于工业生产等优点。
6)经过本发明方法处理得到的刺梨多糖粉、多酚粉、SOD粉、Vc粉的纯度高、活性高，提升了产品的营养价值，有效解决了Vc、SOD等营养成分在加工过程中的损失和不稳定的问题。同时制备方法简便、成本低，适于规模化生产。因此，经本发明方法制得的产品更有益于人体健康。
本发明的附加方面和优点将在下面的描述中部分给出，部分将从下面的描述中变得明显，或通过本发明的实践了解到。
附图说明
本发明的上述和/或附加的方面和优点从结合下面附图对实施例的描述中将变得明显和容易理解，其中：
图1显示了根据本发明一个实施例的同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc方法流程示意图。
具体实施方式
下面将结合实施例对本发明的方案进行解释。本领域技术人员将会理解，下面的实施 例仅用于说明本发明，而不应视为限定本发明的范围。实施例中未注明具体技术或条件的，按照本领域内的文献所描述的技术或条件或者按照产品说明书进行。所用试剂或仪器未注明生产厂商者，均为可以通过市购获得的常规产品。
实施例1
在该实施例中，参见图1，按照下列方法同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc：
(1)选用新鲜无腐烂变质的刺梨渣为原料。
(2)刺梨渣用0.2％体积的酶液(纤维素酶与果胶酶的体积比为1:1)于40℃浸泡时间30min，料液比为1:45g/mL。
(3)将上步处理后的刺梨渣进行胶体磨磨浆，产量为1t/h，温度为40℃，得到刺梨浆。
(4)将刺梨浆进行超声提取，超声提取罐为100L，超声时间为45min，超声功率为300W，得到刺梨提取浆。
(5)将刺梨提取浆进行离心处理，采用卧螺离心，转速为4000rpm，时间为20min，得到刺梨离心液。
(6)将刺梨离心液进行陶瓷膜超滤处理，陶瓷膜孔径为100kDa，获得截留液1(刺梨多糖液)和透过液1。
(7)将透过液1进行AB-8大孔吸附树脂处理，树脂柱高为2m，柱内径为40cm，得到刺梨脱涩液。
(8)采用2倍柱体积的无水乙醇对树脂吸附的多酚进行洗脱，收集洗脱液进行浓缩，得到刺梨多酚物，然后采用50L旋转蒸发仪，50℃水浴浓缩。
(9)将刺梨脱涩液进行超滤处理：采用卷式膜，孔径为10kDa，获得截留液2(刺梨SOD液)和透过液2。
(10)将透过液2进行反渗透处理，反渗透膜的孔径为2nm，获得截留液3(Vc)和透过液3。
(11)将截留液1、刺梨多酚物、截留液2、截留液3进行干燥处理，干燥方式为：冷冻干燥，冷井温度-65℃，冷冻时间为48h。分别得到刺梨多糖粉、刺梨多酚粉、刺梨SOD粉、刺梨Vc粉。
对比例1
按照实施例1的方法制备不同组分刺梨粉，区别在于，将步骤(2)中将酶解液替换成 饮用水，不进行酶解处理。
对比例2
按照实施例1的方法进行，区别在于，不进行步骤(4)的超声提取处理。
对比例3
按照实施例1的方法进行，区别在于，不进行步骤(2)的酶解处理和步骤(4)的超声提取处理。
对比例4
按照实施例1的方法进行，区别在于，将步骤(7)中AB-8大孔吸附树脂替换为D101大孔吸附树脂。
结果如表1所示，可以看出，实施例1制备得到的刺梨多糖粉、多酚粉、SOD粉、Vc粉的得率是最高。相比较于实施例1，对比例1(无酶解)处理、对比例2(无超声)处理，对比例3(无酶解+无超声)处理，所得到的不同刺梨粉均有不同程度地降低，其中对比例3降低地最多。对比例4(D101大孔吸附树脂)处理，对刺梨多糖、SOD和Vc的得率没有影响，但该处理得到的刺梨多酚粉得率相比较于实施例1下降了10％左右，表明实施例1用AB-8大孔吸附树脂处理，能更有效吸附多酚，提高多酚的得率。所以，通过酶解、超声、AB-8大孔吸附树脂处理、超滤、反渗透，冷冻干燥等工艺，更有利于从刺梨渣中制备不同组分的刺梨粉。
表1不同案例制备的不同组分刺梨粉得率

在本说明书的描述中，参考术语“一个实施例”、“一些实施例”、“示例”、“具体示例”、或“一些示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本发明的至少一个实施例或示例中。在本说明书中，对上述术语的示意性表述不必须针对的是相同的实施例或示例。而且，描述的具体特征、结构、材料或者特点可以在任一个或多个实施例或示例中以合适的方式结合。此外，在不相互矛盾的情况下，本领域的技术人员可以将本说明书中描述的不同实施例或示例以及不同实施例或示例的特征进行结合和组合。
尽管上面已经示出和描述了本发明的实施例，可以理解的是，上述实施例是示例性的，不能理解为对本发明的限制，本领域的普通技术人员在本发明的范围内可以对上述实施例进行变化、修改、替换和变型。

Claims (7)

  1. 一种同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法，其特征在于，包括：
    将刺梨渣进行酶解处理，得到酶解处理产物；
    将所述酶解处理产物进行磨浆处理，得到研磨浆；
    将所述研磨浆进行超声处理，得到超声处理产物；
    将所述超声处理产物进行离心处理，收集上清液；
    将所述上清液进行陶瓷膜超滤处理，得到第一透过液和第一截留液，所述第一截留液中含有刺梨多糖；
    将所述第一透过液进行大孔吸附树脂处理，得到刺梨脱涩液和处理后的大孔吸附树脂；
    将所述处理后的大孔吸附树脂采用乙醇溶液进行洗脱处理和蒸发浓缩处理，得到刺梨多酚物；
    将所述刺梨脱涩液进行卷式膜超滤处理，得到第二透过液和第二截留液，所述第二截留液中含有刺梨SOD；
    将所述第二透过液进行反渗透处理，收集第三截留液，所述第三截留液中含有Vc。
  2. 根据权利要求1所述的方法，其特征在于，所述酶解处理包括：将刺梨渣浸泡于酶解液中；
    所述酶解液中的酶选自纤维素酶和果胶酶中的至少之一；
    所述酶解液的浓度为0.1～0.5体积％；
    所述刺梨渣与酶解液的料液比为1:40～1:50g/mL；
    所述浸泡的温度为30～40℃，时间为10～30分钟。
  3. 根据权利要求1所述的方法，其特征在于，所述超声处理的时间为30～60分钟，功率为100～300W；
    所述离心处理的转速为1000～5000rpm，时间为10～30分钟。
  4. 根据权利要求1所述的方法，其特征在于，所述陶瓷膜的孔径为50～150kDa；
    所述大孔吸附树脂选自AB-8，洗脱剂选自食品级无水乙醇；
    所述卷式膜的孔径为10～30kDa；
    所述反渗透处理采用的反渗透膜的孔径为0.3～2nm。
  5. 根据权利要求1所述的方法，其特征在于，进一步包括：
    分别将含有刺梨多糖的截留液、刺梨多酚物、含有刺梨SOD的截留液和含有Vc的截留液进行干燥处理，分别得到刺梨多糖粉、刺梨多酚粉、刺梨SOD粉和刺梨Vc粉；
    所述干燥处理是采用冷冻干燥进行的，其中，冷井温度为-65～-80℃，时间为24～48小时。
  6. 一种实施权利要求1～5任一项所述同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法的系统，其特征在于，包括：
    酶解处理装置，所述酶解处理装置适于将刺梨渣进行酶解处理，得到酶解处理产物；
    磨浆处理装置，所述磨浆处理装置与所述酶解处理装置相连，适于将所述酶解处理产物进行磨浆处理，得到研磨浆；
    超声处理装置，所述超声处理装置与所述磨浆处理装置相连，适于将所述超声处理产物进行离心处理，收集上清液；
    陶瓷膜超滤处理装置，所述陶瓷膜超滤处理装置与所述超声处理装置相连，适于将所述上清液进行陶瓷膜超滤处理，得到第一透过液和第一截留液，所述第一截留液中含有刺梨多糖；
    大孔吸附树脂处理装置，所述大孔吸附树脂处理装置与所述陶瓷膜超滤处理装置相连，适于将所述第一透过液进行大孔吸附树脂处理，得到刺梨脱涩液和处理后的大孔吸附树脂；
    洗脱处理装置，所述洗脱处理装置与所述大孔吸附树脂处理装置相连，适于将所述处理后的大孔吸附树脂采用乙醇溶液进行洗脱处理；
    蒸发浓缩处理装置，所述蒸发浓缩处理装置与所述洗脱处理装置相连，适于将所述洗脱处理所得洗脱液进行蒸发浓缩处理，得到刺梨多酚物；
    卷式膜超滤处理装置，所述卷式膜超滤处理装置与所述蒸发浓缩处理装置相连，适于将所述刺梨脱涩液进行卷式膜超滤处理，得到第二透过液和第二截留液，所述第二截留液中含有刺梨SOD；
    反渗透处理装置，所述反渗透处理装置与所述卷式膜超滤处理装置相连，适于将所述第二透过液进行反渗透处理，收集截留液，所述第三截留液中含有Vc。
  7. 根据权利要求6所述的系统，其特征在于，进一步包括：
    干燥装置，所述干燥装置分别与所述陶瓷膜超滤处理装置、蒸发浓缩处理装置、卷式膜超滤处理装置和反渗透处理装置相连，适于分别将含有刺梨多糖的截留液、刺梨多酚物、含有刺梨SOD的截留液和含有Vc的截留液进行干燥处理，分别得到刺梨多糖粉、刺梨多酚粉、刺梨SOD粉和刺梨Vc粉。
PCT/CN2023/072281 2022-09-28 2023-01-16 同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统 WO2024066140A1 (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN202211191416.7 2022-09-28
CN202211191416.7A CN115260335B (zh) 2022-09-28 2022-09-28 同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统

Publications (1)

Publication Number Publication Date
WO2024066140A1 true WO2024066140A1 (zh) 2024-04-04

Family

ID=83757028

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2023/072281 WO2024066140A1 (zh) 2022-09-28 2023-01-16 同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统

Country Status (2)

Country Link
CN (1) CN115260335B (zh)
WO (1) WO2024066140A1 (zh)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115260335B (zh) * 2022-09-28 2023-01-03 中国农业大学 同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统
CN115720972A (zh) * 2022-11-18 2023-03-03 国药集团贵州大健康产业发展有限公司 一种强化美白功效的刺梨汁饮品及其制备方法
CN116139258B (zh) * 2023-01-31 2024-05-10 中国农业大学 刺梨sod在制备用于预防或治疗肠道疾病药物中的用途

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102675482A (zh) * 2012-05-28 2012-09-19 南京农业大学 一种梨渣综合利用的方法
CN105061621A (zh) * 2015-08-07 2015-11-18 广西南宁派腾科技有限公司 一种刺梨果糖的超声提取方法
KR20180072456A (ko) * 2016-12-21 2018-06-29 김시엽 천년초 추출물의 제조방법과 이에 의해 제조된 천년초 추출물을 포함하는 화장료 조성물 및 식품 조성물
CN109232487A (zh) * 2018-09-26 2019-01-18 春归保健科技有限公司 一种从刺梨中提取维生素c的方法
CN109400734A (zh) * 2018-10-17 2019-03-01 华南理工大学 一种刺梨多糖及其制备方法与应用
CN115260335A (zh) * 2022-09-28 2022-11-01 中国农业大学 同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PL353772A1 (en) * 1999-08-19 2003-12-01 Tate & Lyle Sugar Holdings, Inc.Tate & Lyle Sugar Holdings, Inc. Sugar beet membrane filtration process
EP2338500A1 (en) * 2009-12-23 2011-06-29 Phenofarm S.r.l. Process for producing concentrated and refined actives from tissues and byproducts of Olea europaea with membrane technologies
CN109402073B (zh) * 2018-03-31 2021-11-09 大连豪翔生物酶工程有限公司 一种大蒜中多种生物活性成分的集成提取方法

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102675482A (zh) * 2012-05-28 2012-09-19 南京农业大学 一种梨渣综合利用的方法
CN105061621A (zh) * 2015-08-07 2015-11-18 广西南宁派腾科技有限公司 一种刺梨果糖的超声提取方法
KR20180072456A (ko) * 2016-12-21 2018-06-29 김시엽 천년초 추출물의 제조방법과 이에 의해 제조된 천년초 추출물을 포함하는 화장료 조성물 및 식품 조성물
CN109232487A (zh) * 2018-09-26 2019-01-18 春归保健科技有限公司 一种从刺梨中提取维生素c的方法
CN109400734A (zh) * 2018-10-17 2019-03-01 华南理工大学 一种刺梨多糖及其制备方法与应用
CN115260335A (zh) * 2022-09-28 2022-11-01 中国农业大学 同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
WANG YI, LI GUI-RONG;ZHU YI: "Research Progress of Rosa roxburghii Food", FOOD RESEARCH AND DEVELOPMENT, vol. 40, no. 18, 20 September 2019 (2019-09-20), CN , pages 213 - 218, XP093151572, ISSN: 1005-6521, DOI: 10.12161/j.issn.1005-6521.2019.18.038 *

Also Published As

Publication number Publication date
CN115260335A (zh) 2022-11-01
CN115260335B (zh) 2023-01-03

Similar Documents

Publication Publication Date Title
WO2024066140A1 (zh) 同时提取刺梨渣中刺梨多糖、刺梨多酚、刺梨SOD和Vc的方法和系统
CN105949163B (zh) 一种黑果腺肋花楸果渣中花青素的提取纯化方法
WO2015010497A1 (zh) 黑果枸杞多糖的制备方法
CN103315129B (zh) 纯物理工艺提取大米蛋白和淀粉的方法
CN103571609A (zh) 一种同步制取高稳定化米糠油和米糠蛋白的方法
CN111019011B (zh) 一种米糠多糖的提取方法
CN1580079A (zh) 一种木耳多糖的提取方法
CN104045724B (zh) 从桦褐孔菌中提取制备桦褐孔菌多糖的方法
CN103238892A (zh) 雪莲果原汁及原汁粉的生产方法
CN110684128A (zh) 一种黄精多糖的提取精制方法
CN105238551A (zh) 一种超临界co2萃取纯化油茶籽油的方法
CN103305492A (zh) 一种高纯度医药级菠萝蛋白酶的提取方法
CN105603029A (zh) 活性核桃肽的提取方法
CN1827755A (zh) 扇贝内脏活性成分的制备方法
CN106349405A (zh) 一种采用酶解超声从柚子皮中提取果胶的方法
CN108277248A (zh) 一种超声波提取沙棘活性多肽的方法
CN103980121A (zh) 一种以杜仲鲜叶生产绿原酸的方法
CN106754834A (zh) 一种高活性木瓜蛋白酶的制备工艺
CN101139370A (zh) 水苏糖提取方法
CN109627353B (zh) 一种提取花椒渣中水溶性多糖和麻味物质的方法
CN104017028A (zh) 从异麦芽酮糖母液中分离异麦芽酮糖和海藻酮糖的方法
AU2017416080B2 (en) Method for preparing betanin
CN105859916B (zh) 一种南菊芋9号菊芋菊粉的制备方法
CN109134414B (zh) 一种用戊二醛改性磁性壳聚糖纳米颗粒分离紫薯花青素的方法
CN110810619A (zh) 一种从大豆中提取硒蛋白的提取工艺

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 23869404

Country of ref document: EP

Kind code of ref document: A1