CN103923225B - A kind of preparation method of citrus pectin - Google Patents
A kind of preparation method of citrus pectin Download PDFInfo
- Publication number
- CN103923225B CN103923225B CN201410168320.8A CN201410168320A CN103923225B CN 103923225 B CN103923225 B CN 103923225B CN 201410168320 A CN201410168320 A CN 201410168320A CN 103923225 B CN103923225 B CN 103923225B
- Authority
- CN
- China
- Prior art keywords
- citrus
- preparation
- citrus pectin
- volume
- pectin
- 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.)
- Active
Links
Landscapes
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Preparation Of Fruits And Vegetables (AREA)
Abstract
Description
技术领域technical field
本发明涉及天然产物加工领域中一种果胶的制备,具体涉及一种柑橘果胶的制备方法。The invention relates to the preparation of pectin in the field of natural product processing, in particular to a preparation method of citrus pectin.
背景技术Background technique
果胶是一种胶体性多糖类化合物,其基本结构是主链以β-D-吡喃醛酸以1,4-糖苷键连接,侧链则是在L-鼠李糖残基的O4上以α-1,2-糖苷键连接β-1,2-糖苷键的半乳糖,其分子式为(C6H10O7)n。通常以部分甲酯化状态存在,分子量为10000~400000,相应的聚合度超过1,000单位。果胶存在于高等植物的叶、根、茎、果实的细胞壁内,与植物细胞彼此黏合在一起,尤其在果实和叶中的质量分数较多,果胶是胞间层黏连细胞的主要成分。Pectin is a colloidal polysaccharide compound. Its basic structure is that the main chain is connected by β-D-pyranuronic acid with 1,4-glycosidic bonds, and the side chain is O in the L-rhamnose residue. The molecular formula of galactose on 4 linked with β-1,2-glycosidic bond by α-1,2-glycosidic bond is (C 6 H 10 O 7 ) n . It usually exists in the state of partial methyl esterification, the molecular weight is 10,000-400,000, and the corresponding degree of polymerization exceeds 1,000 units. Pectin exists in the cell walls of leaves, roots, stems, and fruits of higher plants, and is bonded to plant cells, especially in fruits and leaves. Pectin is the main component of intercellular layer adhesion cells .
果胶广泛应用于食品工业,在果冻、果酱、软糖等的制作中可作为胶凝剂,在酸乳制品中,果胶可改善其风味,还可起到稳定和保鲜作用,防止果肉在酸乳中的漂浮及酪蛋白凝结,延长酸乳制品食用期限。果胶作为食品添加剂,已通过FAO/WHO食品添加剂联合委员会评审,宣布其无毒,并且添加量不受限制。Pectin is widely used in the food industry. It can be used as a gelling agent in the production of jelly, jam, soft candy, etc. In yogurt products, pectin can improve its flavor, stabilize and keep fresh, and prevent pulp from Floating and casein coagulation in yogurt prolong the shelf life of yogurt products. As a food additive, pectin has passed the review of the FAO/WHO Joint Committee on Food Additives, declaring that it is non-toxic and the amount of addition is not limited.
果胶在医药、日用化工领域应用也颇多,如它对高血压、肠癌、肥胖症具有良好的疗效,能够抑制人类结肠癌和白血病细胞的增生。果胶还能降低血清胆固醇、血糖含量,预防癌症发生与转移,防止重金属离子中毒,尤其是铅中毒。此外,果胶不仅能降低胆固醇,还具有抗氧化活性,且经过羟肟酸改性后的果胶,抗自由基活性比天然果胶更强。Pectin is also widely used in the fields of medicine and daily chemical industry. For example, it has good curative effect on hypertension, colon cancer and obesity, and can inhibit the proliferation of human colon cancer and leukemia cells. Pectin can also reduce serum cholesterol and blood sugar levels, prevent cancer occurrence and metastasis, and prevent heavy metal ion poisoning, especially lead poisoning. In addition, pectin can not only lower cholesterol, but also has antioxidant activity, and pectin modified with hydroxamic acid has stronger anti-free radical activity than natural pectin.
目前果胶的制备方法有很多,工业生产果胶最常见的是传统酸提法,利用稀酸溶液将非水溶性的原果胶转化成水溶性果胶,然后加入醇或多价金属盐类,析出果胶沉淀,经洗涤、干燥、粉碎制得果胶成品。传统酸提法工艺简单,成本低廉,但是由于受提取条件的影响较大,效率较低,生产周期也较长。At present, there are many preparation methods of pectin. The most common method of industrial production of pectin is the traditional acid extraction method, which uses dilute acid solution to convert non-water-soluble protopectin into water-soluble pectin, and then adds alcohol or polyvalent metal salts. , the pectin precipitates out, and the pectin product is obtained by washing, drying and crushing. The traditional acid extraction method is simple in process and low in cost, but because it is greatly affected by the extraction conditions, the efficiency is low and the production cycle is also long.
发明内容Contents of the invention
本发明的目的是提供一种柑橘果胶的制备方法,采用该方法不仅能显著提高果胶得率和品质,缩短生产周期,还能减少能耗和环境污染。The purpose of the present invention is to provide a method for preparing citrus pectin, which can not only significantly increase the yield and quality of pectin, shorten the production cycle, but also reduce energy consumption and environmental pollution.
本发明的目的是通过以下技术方案来实现:The purpose of the present invention is to realize through the following technical solutions:
一种柑橘果胶的制备方法,所述制备方法包括以下步骤:A preparation method of citrus pectin, said preparation method comprising the following steps:
①称取柑橘作为原料,清洗干净后绞碎,烘干;① Weigh citrus as raw material, wash it, mince it, and dry it;
②将步骤①中烘干后的原料进行粉碎,过40-80目筛,并加入原料体积5-15倍的醇溶液,60-80℃浸提1-4h;②Crush the dried raw materials in step ①, pass through a 40-80 mesh sieve, add an alcohol solution 5-15 times the volume of the raw materials, and extract at 60-80°C for 1-4 hours;
⑧将步骤②中浸提的原料进行压榨过滤,滤渣加入5-15倍体积的水,并用盐酸调至PH2-4;8. Squeeze and filter the raw material extracted in step 2, add 5-15 times the volume of water to the filter residue, and adjust it to PH2-4 with hydrochloric acid;
④采用高压脉冲电场处理,间歇式加热提取,离心,如此循环重复2~4次,优选重复3次,合并滤液,并将滤液浓缩,向浓缩液中加入1-5倍体积量的酸性醇溶液,静置2-6h,抽滤;④Using high-voltage pulsed electric field treatment, intermittent heating and extraction, centrifugation, repeat this cycle 2 to 4 times, preferably 3 times, combine the filtrate, concentrate the filtrate, and add 1-5 times the volume of acidic alcohol solution to the concentrated solution , standing for 2-6h, suction filtration;
⑤在步骤④中抽滤后的沉淀中加95%乙醇搅拌10min,抽滤,将得到的沉淀在45℃下进行真空干燥,粉碎,过60目筛,得柑橘果胶成品。5. Add 95% ethanol to the precipitate after suction filtration in step 4 and stir for 10 min, suction filter, vacuum-dry the obtained precipitate at 45° C., pulverize, and pass through a 60-mesh sieve to obtain the finished product of citrus pectin.
进一步地,步骤①所述的柑橘为柑橘残次果或柑橘食品加工废料。Further, the citrus described in step ① is citrus residual fruit or citrus food processing waste.
进一步地,步骤①所述干燥的温度为60-80℃。Further, the drying temperature in step ① is 60-80°C.
进一步地,步骤②中所述的醇溶液为40%-100%醇溶液。Further, the alcohol solution described in step ② is a 40%-100% alcohol solution.
进一步地,所述的醇溶液为60%-75%乙醇溶液Further, the alcohol solution is 60%-75% ethanol solution
进一步地,步骤④中所述的高压脉冲电场的电场强度为10至24kV/cm,脉冲数为5~12,温度为40-80℃。Further, the electric field strength of the high voltage pulsed electric field described in step ④ is 10 to 24 kV/cm, the number of pulses is 5 to 12, and the temperature is 40-80°C.
进一步地,步骤④中所述的间歇式加热提取具体过程为:先进行高压脉冲电场处理,然后再进行保温搅拌提取,所述保温搅拌提取的温度为40-80℃,保温搅拌提取的时间为10-60min。Further, the specific process of the intermittent heating and extraction described in step ④ is: first conduct high-voltage pulse electric field treatment, and then perform heat preservation and stirring extraction, the temperature of the heat preservation and stirring extraction is 40-80 ° C, and the time of heat preservation and stirring extraction is 10-60min.
进一步地,步骤④中向浓缩液中边搅拌边加入2-4倍体积量的酸性醇溶液。Further, in step ④, add 2-4 times the volume of acidic alcohol solution to the concentrated solution while stirring.
进一步地,步骤④中所述的所述的酸性醇溶液为含0.5mol/L HC1的醇溶液。Further, the acidic alcoholic solution described in step ④ is an alcoholic solution containing 0.5mol/L HCl.
进一步地,所述的醇溶液为95%乙醇溶液。Further, the alcohol solution is 95% ethanol solution.
本发明提供了一种柑橘果胶的制备方法,其主要具有的有益效果为。The invention provides a preparation method of citrus pectin, which mainly has the following beneficial effects.
①本发明将高压脉冲电场处理技术应用于果胶的提取过程中,采用间歇式高压脉冲电场辅助酸提法,在确定的电场强度、脉冲数和温度范围内,能快速有效的提取果胶,果胶得率和品质稳定。① The present invention applies high-voltage pulsed electric field treatment technology to the extraction process of pectin, adopts intermittent high-voltage pulsed electric field-assisted acid extraction method, and can quickly and effectively extract pectin within the determined electric field strength, pulse number and temperature range, Pectin yield and quality are stable.
②此外,本发明方法通过提取前原料进行醇处理可有效去除色素和脂质成分等杂质,有利于后续工序的进行,有利于提高果胶产品的品质。②In addition, the method of the present invention can effectively remove impurities such as pigments and lipid components by carrying out alcohol treatment on raw materials before extraction, which is beneficial to the subsequent process and improves the quality of pectin products.
③本发明方法简单易操作,提取效率高,适合工业化生产,解决了传统果胶提取法存在的提取时间长,生产效率低,果胶得率低,果胶品质差,不稳定等问题,有利于提高果胶产品在市场上的竞争力。3. the inventive method is simple and easy to operate, and extraction efficiency is high, is suitable for industrialized production, has solved the extraction time long that traditional pectin extraction method exists, and production efficiency is low, pectin yield rate is low, pectin quality is poor, problems such as instability, have It is conducive to improving the competitiveness of pectin products in the market.
④本发明所述的方法具有重要的工业市场应用价值,该果胶产品可广泛用于食品、保健品、化妆品、医药等领域。④ The method of the present invention has important industrial market application value, and the pectin product can be widely used in fields such as food, health products, cosmetics, and medicine.
具体实施方式detailed description
本发明实施例所述的一种柑橘果胶的制备方法,所述制备方法包括以下步骤:①称取柑橘作为原料,清洗干净后绞碎,烘干;②将步骤①中烘干后的原料进行粉碎,过40-80目筛,并加入5-15倍体积的醇溶液,60-80℃浸提1-4h;③将步骤②中浸提的原料进行压榨过滤,滤渣加入5-15倍体积的水,并用盐酸调至PH2-4;④采用高压脉冲电场处理,间歇式加热提取,离心,如此循环重复2~4次,合并滤液,并将滤液浓缩,向浓缩液中加入1-5倍体积量的酸性醇溶液,静置2-6h,抽滤;⑤在步骤④中抽滤后的沉淀中加95%乙醇搅拌10min,抽滤,将得到的沉淀在45℃下进行真空干燥,粉碎,过60目筛,得柑橘果胶成品。The preparation method of a kind of citrus pectin described in the embodiment of the present invention, the preparation method comprises the following steps: 1. Weigh the citrus as raw material, wash it, mince it, and dry it; 2. Dry the raw material in step 1. Crush, pass through a 40-80 mesh sieve, add 5-15 times the volume of alcohol solution, and extract at 60-80°C for 1-4 hours; ③Press and filter the raw materials extracted in step ②, and add 5-15 times the volume of the filter residue volume of water, and adjusted to PH2-4 with hydrochloric acid; ④Using high-voltage pulse electric field treatment, intermittent heating extraction, centrifugation, repeating this cycle 2 to 4 times, combining the filtrate, and concentrating the filtrate, adding 1-5 Double the volume of acidic alcohol solution, let stand for 2-6h, and suction filter; ⑤add 95% ethanol to the precipitate after suction filtration in step ④, stir for 10min, and suction filter, and vacuum-dry the obtained precipitate at 45°C, Pulverize and pass through a 60-mesh sieve to obtain the finished product of citrus pectin.
作为进一步优选地,步骤①所述的柑橘为柑橘残次果或柑橘食品加工废料。As further preferably, the citrus described in step ① is citrus residual fruit or citrus food processing waste.
作为进一步优选地,步骤①所述干燥的温度为60-80℃。As a further preference, the drying temperature in step ① is 60-80°C.
作为进一步优选地,步骤②中所述的醇溶液为40%-100%醇溶液。As a further preference, the alcohol solution described in step ② is a 40%-100% alcohol solution.
作为进一步优选地,所述的醇溶液为60%-75%乙醇溶液As further preferably, the alcohol solution is 60%-75% ethanol solution
作为进一步优选地,步骤④中所述的高压脉冲电场的电场强度为10至24kV/cm,脉冲数为5~12,温度为40-80℃。As a further preference, the electric field strength of the high-voltage pulsed electric field described in step ④ is 10-24 kV/cm, the number of pulses is 5-12, and the temperature is 40-80°C.
作为进一步优选地,步骤④中所述的间歇式加热提取具体过程为:先进行高压脉冲电场处理,然后再进行保温搅拌提取,所述保温搅拌提取的温度为40-80℃,保温搅拌提取的时间为10-60min。As a further preference, the specific process of the intermittent heating and extraction described in step ④ is: firstly perform high-voltage pulse electric field treatment, and then perform heat preservation and stirring extraction, the temperature of the heat preservation and stirring extraction is 40-80 ° C, and the heat preservation and stirring extraction The time is 10-60min.
作为进一步优选地,步骤④中向浓缩液中边搅拌边加入2-4倍体积量的酸性醇溶液。As a further preference, in step ④, add 2-4 volumes of acidic alcohol solution to the concentrated solution while stirring.
作为进一步优选地,步骤④中所述的所述的酸性醇溶液为含0.5mol/L HC1的醇溶液。As a further preference, the acidic alcoholic solution described in step ④ is an alcoholic solution containing 0.5mol/L HCl.
作为进一步优选地,所述的醇溶液为95%乙醇溶液。As a further preference, the alcohol solution is 95% ethanol solution.
具体实施时,高压脉冲电场是一种非热处理技术,在处理热敏性物质方面具有巨大的优势。高压脉冲电场可利用高电位差破坏植物细胞膜,不仅能使细胞内酶类物质等失活,还能显著增加细胞内物质溶出。In practice, high-voltage pulsed electric field is a non-thermal treatment technology, which has great advantages in the treatment of heat-sensitive substances. The high-voltage pulsed electric field can use the high potential difference to destroy the plant cell membrane, which can not only inactivate intracellular enzymes, but also significantly increase the dissolution of intracellular substances.
下面以具体实验案例为例来说明具体实施方式,应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。The following uses specific experimental cases as examples to illustrate specific implementation methods. It should be understood that the specific embodiments described here are only used to explain the present invention, and are not intended to limit the present invention.
实施例1Example 1
取柑橘原料,清洗干净后绞碎,65-75℃烘干,粉碎,过40-80目筛,加入15倍体积的70%乙醇溶液,75-80℃浸提1h,压榨过滤,滤渣加入12倍体积的水,用盐酸调PH至2;再用高压脉冲电场处理,该高压脉冲电场处理的电场强度为10kV/cm,脉冲数为10,温度为60℃,高压脉冲电场处理后,保持温度60℃搅拌加热提取30min,离心,如此循环重复3次,合并滤液,滤液浓缩,向浓缩液中边搅拌边加入等体积量的含0.5mol/L HC1的95%乙醇溶液,静置2h,抽滤,所得沉淀加95%乙醇搅拌10min,抽滤,将得到的沉淀在45℃下进行真空干燥,粉碎并过60目筛,得柑橘果胶成品。Take citrus raw materials, clean them, mince them, dry them at 65-75°C, crush them, pass through a 40-80 mesh sieve, add 15 times the volume of 70% ethanol solution, extract at 75-80°C for 1 hour, squeeze and filter, and add 12 Double the volume of water, adjust the pH to 2 with hydrochloric acid; then use high-voltage pulse electric field treatment, the electric field strength of the high-voltage pulse electric field treatment is 10kV/cm, the number of pulses is 10, and the temperature is 60°C. After the high-voltage pulse electric field treatment, keep the temperature Stir and heat extraction at 60°C for 30 minutes, centrifuge, and repeat this cycle 3 times, combine the filtrate, concentrate the filtrate, add an equal volume of 95% ethanol solution containing 0.5mol/L HC1 to the concentrated solution while stirring, let it stand for 2 hours, pump Filtrate, add 95% ethanol to the obtained precipitate, stir for 10 min, suction filter, vacuum dry the obtained precipitate at 45°C, pulverize and pass through a 60-mesh sieve to obtain the finished product of citrus pectin.
实施例2Example 2
取柑橘原料,清洗干净后绞碎,60-70℃烘干,粉碎,过40-80目筛,加入10倍体积的80%乙醇溶液,60-70℃浸提3h,压榨过滤,滤渣加入10倍体积的水,用盐酸调PH至3;再用高压脉冲电场处理,该高压脉冲电场处理的电场强度为15kV/cm,脉冲数为12,温度为80℃,高压脉冲电场处理后,保持温度80℃搅拌加热提取40min,离心,如此循环重复3次,合并滤液,滤液浓缩,向浓缩液中边搅拌边加入2倍体积量的含0.5mol/L HC1的95%乙醇溶液,静置3~5h,抽滤,所得沉淀加95%乙醇搅拌10min,抽滤,将得到的沉淀在45℃下进行真空干燥,粉碎并过60目筛,得柑橘果胶成品。Take citrus raw materials, clean them, mince them, dry them at 60-70°C, crush them, pass through a 40-80 mesh sieve, add 10 times the volume of 80% ethanol solution, extract at 60-70°C for 3 hours, squeeze and filter, and add 10 Double the volume of water, adjust the pH to 3 with hydrochloric acid; then use high-voltage pulse electric field treatment, the electric field intensity of the high-voltage pulse electric field treatment is 15kV/cm, the number of pulses is 12, and the temperature is 80 ° C. After the high-voltage pulse electric field treatment, keep the temperature Stir and heat at 80°C for 40 minutes, centrifuge, and repeat this cycle 3 times, combine the filtrate, concentrate the filtrate, add 2 times the volume of 95% ethanol solution containing 0.5mol/L HC1 to the concentrated solution while stirring, and let it stand for 3~ After 5 hours, filter with suction, add 95% ethanol to the obtained precipitate, stir for 10 min, filter with suction, vacuum-dry the obtained precipitate at 45°C, pulverize and pass through a 60-mesh sieve to obtain the finished product of citrus pectin.
实施例3Example 3
取柑橘原料,清洗干净后绞碎,70-80℃烘干,粉碎,过40-80目筛,加入6倍体积的60%乙醇溶液,75-80℃浸提1.5h,压榨过滤,滤渣加入15倍体积的水,用盐酸调PH至4;再用高压脉冲电场处理,该高压脉冲电场处理的电场强度为20kV/cm,脉冲数为8,温度为40℃,高压脉冲电场处理后,保持温度40℃搅拌加热提取45min,离心,如此循环重复3次,合并滤液,滤液浓缩,向浓缩液中边搅拌边加入3倍体积量的含0.5mol/L HC1的95%乙醇溶液,静置4.5h,抽滤,所得沉淀加95%乙醇搅拌10min,抽滤,将得到的沉淀在45℃下进行真空干燥,粉碎并过60目筛,得柑橘果胶成品。Take citrus raw materials, clean them, mince them, dry them at 70-80°C, crush them, pass through a 40-80 mesh sieve, add 6 times the volume of 60% ethanol solution, extract at 75-80°C for 1.5h, squeeze and filter, and add the filter residue 15 times the volume of water, adjust the pH to 4 with hydrochloric acid; then use high-voltage pulse electric field treatment, the electric field strength of the high-voltage pulse electric field treatment is 20kV/cm, the number of pulses is 8, and the temperature is 40 ° C. After high-voltage pulse electric field treatment, keep Stir and heat at 40°C for extraction for 45 minutes, centrifuge, repeat this cycle 3 times, combine the filtrate, concentrate the filtrate, add 3 times the volume of 95% ethanol solution containing 0.5mol/L HC1 to the concentrated solution while stirring, and let it stand for 4.5 h, filter with suction, add 95% ethanol to the obtained precipitate, stir for 10 min, filter with suction, vacuum dry the obtained precipitate at 45°C, pulverize and pass through a 60-mesh sieve to obtain the finished product of citrus pectin.
本发明不局限于上述最佳实施方式,任何人在本发明的启示下所作的有关本发明的任何修饰或变更,凡是具有与本申请相同或相近似的技术方案,均落在本发明的保护范围之内。The present invention is not limited to the above-mentioned best implementation mode, and anyone who makes any modifications or changes related to the present invention under the inspiration of the present invention, who has the same or similar technical solutions as the present application, all falls under the protection of the present invention. within range.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410168320.8A CN103923225B (en) | 2014-04-23 | 2014-04-23 | A kind of preparation method of citrus pectin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410168320.8A CN103923225B (en) | 2014-04-23 | 2014-04-23 | A kind of preparation method of citrus pectin |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103923225A CN103923225A (en) | 2014-07-16 |
CN103923225B true CN103923225B (en) | 2017-01-18 |
Family
ID=51141637
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410168320.8A Active CN103923225B (en) | 2014-04-23 | 2014-04-23 | A kind of preparation method of citrus pectin |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103923225B (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2019061018A1 (en) * | 2017-09-26 | 2019-04-04 | 浙江大学 | Method for extracting pectin rich in rg-i |
CN108285499A (en) * | 2017-12-03 | 2018-07-17 | 新疆阜丰生物科技有限公司 | A kind of energy-efficient technique for preparing pectin |
CN108424940A (en) * | 2018-04-13 | 2018-08-21 | 安徽宇宁果胶股份有限公司 | A kind of production method of the medicinal pectin of targeted therapy |
CN114685690B (en) * | 2022-04-08 | 2023-05-23 | 江南大学 | Method for extracting edible fungi polysaccharide by intermittent induction thermal reactor |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5975453B2 (en) * | 2008-11-14 | 2016-08-23 | 株式会社 アスキー | Extraction method of polysaccharides |
CN102702379A (en) * | 2012-04-26 | 2012-10-03 | 赛珂睿德生物医药科技(上海)有限公司 | Extraction and preparation process of citrus pectin |
-
2014
- 2014-04-23 CN CN201410168320.8A patent/CN103923225B/en active Active
Also Published As
Publication number | Publication date |
---|---|
CN103923225A (en) | 2014-07-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104086667B (en) | A kind of method preparing citruss skin slag pectin using ultrasonic assistant extraction | |
CN103719880B (en) | Preparation method of high-activity purple sweet potato dietary fiber | |
CN107141369B (en) | A kind of preparation method of modified pectin | |
CN106905440A (en) | The new method that a kind of tremella polysaccharides is extracted | |
CN103923225B (en) | A kind of preparation method of citrus pectin | |
CN102757515B (en) | Method for extracting high-purity flavonoid and pectin from citrus peel | |
CN106146687A (en) | A kind of extract the method for pectin in citrus peel residue | |
CN101148482A (en) | A kind of extraction method of pectin in banana peel | |
CN109535278A (en) | A method of pectin is extracted from passion fruit pericarp | |
CN105567762A (en) | Enteromorpha prolifera oligosaccharide with auxiliary blood sugar decreasing function and preparation method thereof | |
CN108912242A (en) | A method of extracting high degree of gelation pectin from the pomelo peel of Pingshan | |
CN104957552A (en) | Instant loquat powder | |
CN108794651A (en) | The method that pectin is extracted in passion fruit pericarp | |
CN105237654A (en) | Method for extracting pectin from orange peel | |
CN101869231B (en) | Method for eliminating alkaloid in konjaku flour | |
CN102432579A (en) | Process for extracting anthocyanin from blueberry pomace | |
CN105440155A (en) | Pectin extraction method | |
CN105111278A (en) | Method for preparing crude phycobiliprotein and crude polysaccharide from porphyra yezoensis | |
CN104031172A (en) | Method for extracting pectin from banana peel by ultrasonic synergistic ammonium oxalate method | |
CN108314748A (en) | Extraction process of aloe peel pectin | |
CN114213555B (en) | A kind of okra polysaccharide extract and preparation method thereof | |
CN103833870A (en) | Method for extracting low-methoxy pectin from apple pomace | |
CN103073657B (en) | A kind of Sunflower Receptacle low-fat pectin production method | |
CN104262507A (en) | Method for preparing lobster shell chitosan through cooperation of ultrasonic wave and CDA (Chitin Deacetylase) | |
CN107011454A (en) | A kind of sea cucumber fucoidan preparation method of the high sulphation of low molecule amount |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C41 | Transfer of patent application or patent right or utility model | ||
TR01 | Transfer of patent right |
Effective date of registration: 20170119 Address after: 215123 Jiangsu Province Industrial Park of Suzhou Dushu Lake higher education if the waterway No. 398 Patentee after: ANIQUE BIOLOGICAL MEDICINE (SUZHOU) CO.,LTD. Patentee after: SACCHARIDIA BIO-PHARMACEUTICAL TECHNOLOGY (SHANGHAI) Co.,Ltd. Address before: 201203 Shanghai city Pudong New Area Cailun Road No. 781 room 1204 Patentee before: SACCHARIDIA BIO-PHARMACEUTICAL TECHNOLOGY (SHANGHAI) Co.,Ltd. |
|
DD01 | Delivery of document by public notice |
Addressee: ANIQUE BIOLOGICAL MEDICINE (SUZHOU) CO.,LTD. Person in charge of patents Document name: payment instructions |
|
DD01 | Delivery of document by public notice | ||
DD01 | Delivery of document by public notice |
Addressee: Jiang Jinghua Document name: Notice of Qualified Procedures |
|
DD01 | Delivery of document by public notice |