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CN102115690B - Method for comprehensively utilizing rice bran - Google Patents

Method for comprehensively utilizing rice bran Download PDF

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CN102115690B
CN102115690B CN2011100048401A CN201110004840A CN102115690B CN 102115690 B CN102115690 B CN 102115690B CN 2011100048401 A CN2011100048401 A CN 2011100048401A CN 201110004840 A CN201110004840 A CN 201110004840A CN 102115690 B CN102115690 B CN 102115690B
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rice bran
solution
peptide
protein
rice
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CN102115690A (en
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陈燕飞
亓培实
何东平
刘良忠
何莉萍
江思佳
黄迪惠
倪倩
刘雪姣
宋洋
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Wuhan Pashun Zhengyuan Biotech And Engineering Co ltd
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WUHAN BAIXIN FOOD CO Ltd
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Abstract

本发明公开了一种综合利用米糠的方法,可同时制备得到米糠油、米糠粗纤维、米糠蛋白、米糠肽4种产品。其制备过程为:以米糠为原料,先提取米糠中的油脂,再用“碱溶酸沉”法分离米糠粗纤维和米糠蛋白,然后对米糠蛋白添加蛋白酶水解蛋白质,再经过超滤分级、过阴阳离子交换树脂除去盐分,最后浓缩、干燥得到米糠生物活性肽。

The invention discloses a method for comprehensively utilizing rice bran, which can simultaneously prepare four kinds of products including rice bran oil, rice bran crude fiber, rice bran protein and rice bran peptide. The preparation process is as follows: using rice bran as raw material, first extract the oil in rice bran, then use the "alkali-soluble acid precipitation" method to separate rice bran crude fiber and rice bran protein, then add protease to the rice bran protein to hydrolyze the protein, and then go through ultrafiltration classification, filtration Anion and cation exchange resins are used to remove salt, and finally concentrated and dried to obtain rice bran bioactive peptides.

Description

一种综合利用米糠的方法A method for comprehensive utilization of rice bran

技术领域 technical field

本发明涉及一种综合利用米糠的方法。The invention relates to a method for comprehensively utilizing rice bran.

背景技术 Background technique

稻谷是我国第一大粮食品种。目前年产1.85亿吨左右,占全国粮食总产量的42%。世界上稻谷产量占粮食总产量的37%。稻谷在加工成精米的过程中要去掉外壳和占总重10%左右的种皮和胚,米糠就是由种皮和胚加工制成的,是稻谷加工的主要副产品。国内外的研究结果和资料表明,米糠中富含各种营养素和生理活性物质。由于加工米糠的原料和所采用的加工技术不同,米糠的组成成分并不完全一样。一般来说,米糠中平均含蛋白质15%,脂肪16%~22%,糖3%~8%,水分10%等。Rice is the largest grain variety in my country. At present, the annual output is about 185 million tons, accounting for 42% of the country's total grain output. Paddy production accounts for 37% of the total food production in the world. In the process of processing rice into polished rice, the shell and the seed coat and embryo accounting for about 10% of the total weight must be removed. Rice bran is made from the seed coat and embryo and is the main by-product of rice processing. Research results and data at home and abroad show that rice bran is rich in various nutrients and physiologically active substances. Due to the different raw materials and processing techniques used in processing rice bran, the composition of rice bran is not exactly the same. Generally speaking, rice bran contains an average of 15% protein, 16%-22% fat, 3%-8% sugar, and 10% water.

目前,国内外对米糠的加工方式比较单一,没有一种综合利用的方法,要么只提取米糠油,要么只提取米糠膳食纤维,并且对米糠蛋白和米糠肽的利用较少。现有米糠肽的制备工艺主要有三种:(1)基因工程方法;(2)化学合成方法;(3)酶解法。在目前用酶解法制备米糠肽的工艺中,在酶解过程中,均加入大量碱液或酸液来调节酶解反应时溶液的酸碱度,且没有脱盐工艺,使成品盐分含量过高;而且,对最终产品没有进行分级,最终产品的分子量分布差别较大,影响了产品的生理活性。At present, the processing methods of rice bran at home and abroad are relatively single, and there is no comprehensive utilization method. Either only extract rice bran oil or only extract rice bran dietary fiber, and the utilization of rice bran protein and rice bran peptide is less. There are three main preparation techniques of existing rice bran peptides: (1) genetic engineering method; (2) chemical synthesis method; (3) enzymatic hydrolysis method. In the current process of preparing rice bran peptides by enzymatic hydrolysis, a large amount of lye or acid solution is added to adjust the pH of the solution during the enzymatic hydrolysis reaction, and there is no desalination process, so that the salt content of the finished product is too high; and, The final product is not classified, and the molecular weight distribution of the final product is quite different, which affects the physiological activity of the product.

发明内容 Contents of the invention

本发明所要解决的问题是提供一种米糠综合利用的方法,可制备出米糠油、米糠粗纤维、米糠蛋白、米糠肽4种产品。The problem to be solved by the present invention is to provide a method for comprehensive utilization of rice bran, which can produce four kinds of products: rice bran oil, rice bran crude fiber, rice bran protein and rice bran peptide.

为了解决上述技术问题,本发明提供的米糠综合利用方法为:以米糠为原料,先提取米糠中的油脂,再用“碱溶酸沉”法分离米糠粗纤维和米糠蛋白,然后对米糠蛋白添加蛋白酶水解蛋白质,再经过超滤分级、过阴阳离子交换树脂除去盐分,最后浓缩、干燥得到米糠生物活性肽。In order to solve the above-mentioned technical problems, the comprehensive utilization method of rice bran provided by the present invention is as follows: using rice bran as raw material, first extracting the oil in rice bran, then using the "alkali-soluble acid precipitation" method to separate rice bran crude fiber and rice bran protein, and then adding rice bran protein Protease hydrolyzes the protein, then undergoes ultrafiltration classification, passes through anion and cation exchange resins to remove salt, and finally concentrates and dries to obtain rice bran bioactive peptides.

本发明的一种综合利用米糠的方法,可以是如下步骤:A method of comprehensively utilizing rice bran of the present invention may be as follows:

(1)将米糠粉碎,过60~80目筛,采用索氏抽提法,用95%正己烷溶剂在50℃条件下浸提2h,然后将正己烷溶液过滤,将米糠晾晒至正己烷完全挥发,为脱脂米糠;将滤液用旋转蒸发器将正己烷完全蒸发,剩下的为米糠油;(1) Crush the rice bran, pass through a 60-80 mesh sieve, use Soxhlet extraction method, use 95% n-hexane solvent to extract at 50°C for 2 hours, then filter the n-hexane solution, and dry the rice bran until the n-hexane is completely Volatile, it is defatted rice bran; use the rotary evaporator to completely evaporate the n-hexane from the filtrate, and the rest is rice bran oil;

(2)将步骤(1)脱脂米糠与水按1∶5~1∶10(质量比)溶解至水中,加热至45~55℃,用NaOH试剂调节pH至8.0~10.0,不停搅拌15min,在3000~4000r/min的转速下,离心15min,取上清液,将沉淀烘干,为米糠粗纤维;(2) Dissolve defatted rice bran and water in step (1) into water at a ratio of 1:5 to 1:10 (mass ratio), heat to 45 to 55°C, adjust the pH to 8.0 to 10.0 with NaOH reagent, and keep stirring for 15 minutes. Centrifuge for 15 minutes at a speed of 3000-4000r/min, take the supernatant, and dry the precipitate to obtain rice bran crude fiber;

(3)将步骤(2)的上清液加热至70~90℃,用柠檬酸试剂调节pH至3.0~5.0,不停搅拌10min,3000~4000r/min,15min,离心收集沉淀,为米糠蛋白,烘干可得米糠蛋白粉;(3) Heat the supernatant of step (2) to 70-90°C, adjust the pH to 3.0-5.0 with citric acid reagent, stir continuously for 10min, 3000-4000r/min, 15min, and centrifuge to collect the precipitate, which is rice bran protein , drying to obtain rice bran protein powder;

(4)将步骤(3)的米糠蛋白与水按1∶5~1∶10(质量比)溶解至水中,加热至90~100℃,保持15~30min,然后冷却至35~50℃,用NaOH试剂调节并保持pH在6.0~8.0,按E/S比3%~7%加入中性蛋白酶As1.398,酶解2~4h,酶解过程中不断搅拌,并用NaOH溶液保持pH值在6.0~8.0;(4) Dissolve the rice bran protein and water in step (3) into water at a ratio of 1:5 to 1:10 (mass ratio), heat to 90 to 100°C, keep for 15 to 30 minutes, then cool to 35 to 50°C, and use NaOH reagent to adjust and maintain the pH at 6.0-8.0, add neutral protease As1.398 according to the E/S ratio of 3%-7%, enzymolysis for 2-4 hours, keep stirring during the enzymolysis process, and use NaOH solution to maintain the pH value at 6.0 ~8.0;

(5)待待步骤(4)酶解结束后,迅速用HCl溶液调节pH至5.0~3.0,在3000~4000r/min的转速下,离心15min,取上清液,所得即为米糠肽粗制液;(5) After the enzymatic hydrolysis in step (4), quickly adjust the pH to 5.0-3.0 with HCl solution, centrifuge at a speed of 3000-4000r/min for 15min, take the supernatant, and obtain the crude rice bran peptide liquid;

(6)将步骤(5)所得的米糠肽粗制液注入储槽中,溶液经微滤后通过分子量截留量为1000Da超滤膜,溶液中的小分子物质经中空纤维膜的内壁渗透出来成为超滤液,收集超滤液,为米糠肽超滤液;溶液中的蛋白等大分子物质得以保留并得到浓缩,将浓缩液回收至步骤4中再次酶解;(6) Inject the crude rice bran peptide solution obtained in step (5) into the storage tank, and the solution passes through the ultrafiltration membrane with a molecular weight cut-off of 1000Da after microfiltration, and the small molecular substances in the solution permeate out through the inner wall of the hollow fiber membrane to become The ultrafiltrate, collecting the ultrafiltrate, is the rice bran peptide ultrafiltrate; the protein and other macromolecular substances in the solution are preserved and concentrated, and the concentrated solution is recovered to step 4 for enzymatic hydrolysis again;

(7)交换树脂于去离子水中浸泡处理24小时后装柱,然后分别用7.5%盐酸和10%NaOH对其进行浸泡,转化为H+型阳离子交换树脂和OH-型阴离子交换树脂,再用去离子水清洗至pH为7.0待用;(7) The exchange resin was soaked in deionized water for 24 hours and then packed into a column, then it was soaked with 7.5% hydrochloric acid and 10% NaOH respectively, converted into H + type cation exchange resin and OH - type anion exchange resin, and then used Wash with deionized water until the pH is 7.0 for use;

将步骤(6)中所得的超滤液,以5~10倍柱体积/h的流速通过H+型阳离子交换树脂来脱除阳离子,待流出液pH=4.0左右时停止加样,之后将此流出液以同样流速通过OH-型阴离子交换树脂来脱除阴离子,至流出液呈pH为7.0时停止加样,收集为米糠肽精制液;The ultrafiltrate obtained in step (6) is passed through the H + type cation exchange resin at a flow rate of 5 to 10 times the column volume/h to remove cations, and the sample addition is stopped when the pH of the effluent=4.0, and then the The effluent is passed through the OH - type anion exchange resin at the same flow rate to remove anions, and the sample addition is stopped when the pH of the effluent is 7.0, and it is collected as rice bran peptide refined liquid;

(8)由步骤6中得到的米糠肽精制液,减压浓缩至固型物含量20%~30%;(8) The rice bran peptide refined solution obtained in step 6 is concentrated under reduced pressure to a solid content of 20% to 30%;

(9)精制的米糠肽液浓缩后,经喷雾干燥或冷冻干燥制成干粉。(9) After the refined rice bran peptide solution is concentrated, it is spray-dried or freeze-dried to make a dry powder.

上述步骤(1)的目的是:米糠中油脂含量为16%左右,利用油脂溶解于正己烷的特性,将米糠中的油脂萃取出,并旋转蒸发将正己烷完全蒸发,得到米糠油。The purpose of the above step (1) is: the oil content in the rice bran is about 16%, and the oil in the rice bran is extracted by utilizing the property that the oil dissolves in n-hexane, and the n-hexane is completely evaporated by rotary evaporation to obtain rice bran oil.

上述步骤(2)的目的是:利用蛋白质在碱性条件下溶解的特性,将米糠蛋白和碱不溶性物质分离开,以提高米糠蛋白的含量;碱不溶成分为米糠粗纤维。The purpose of the above step (2) is to separate the rice bran protein from the alkali-insoluble matter by utilizing the property of protein dissolving under alkaline conditions, so as to increase the content of the rice bran protein; the alkali-insoluble component is rice bran crude fiber.

上述步骤(3)酸沉的目的是:利用蛋白质在酸性等电点条件下沉淀的特性,将米糠蛋白和酸溶性物质分开,以提高米糠蛋白的含量。The purpose of the acid precipitation in the above step (3) is to separate the rice bran protein from acid-soluble substances by utilizing the property of protein precipitation under acidic isoelectric point conditions, so as to increase the content of rice bran protein.

上述步骤(2)、(3)的目的是为了分离脱脂米糠中米糠粗纤维和米糠蛋白。同时,纯化用来水解的米糠蛋白,一般脱脂米糠中蛋白的含量为20%左右,经过上述方法处理后,蛋白含量可达80%以上。The purpose of the above steps (2) and (3) is to separate rice bran crude fiber and rice bran protein in defatted rice bran. At the same time, the rice bran protein used for hydrolysis is purified. Generally, the protein content in defatted rice bran is about 20%. After the above-mentioned treatment, the protein content can reach more than 80%.

上述步骤(4)酶解的目的是:将米糠中的大分子蛋白质酶解为小分子蛋白质和肽;The purpose of the above step (4) enzymolysis is: enzymatically hydrolyze the macromolecular protein in the rice bran into small molecular protein and peptide;

上述步骤(5)调酸的目的是为了使酶失活,停止酶解反应;离心的目的是为了固液分离,收集酶解液。The purpose of acid adjustment in the above step (5) is to inactivate the enzyme and stop the enzymolysis reaction; the purpose of centrifugation is to collect the enzymolysis solution for solid-liquid separation.

上述步骤(6)中超滤的目的是为了截取需要分子量的产品;二次酶解的目的是为了将分子量1000Da以上的大分子蛋白水解成小分子,提高利用原料利用。The purpose of the ultrafiltration in the above step (6) is to intercept the products with required molecular weight; the purpose of the secondary enzymatic hydrolysis is to hydrolyze the macromolecular protein with a molecular weight of 1000 Da or more into small molecules, so as to improve the utilization of raw materials.

上述步骤(7)中脱盐的目的是为了去除酶解液中因酶解过程中不断调节pH而带入的盐离子。没有经过脱盐处理的产品盐分含量大于8%,经过脱盐处理的产品研发含量小于2%;The purpose of desalting in the above step (7) is to remove the salt ions in the enzymolysis solution due to the constant adjustment of pH during the enzymolysis process. The salt content of products that have not undergone desalination treatment is greater than 8%, and the salt content of products that have undergone desalination treatment is less than 2%;

本发明与现有技术相比,具有如下优点和效果:Compared with the prior art, the present invention has the following advantages and effects:

(1)本方法提供一种综合利用米糠的方法,可同时制备得到米糠油、米糠粗纤维、米糠蛋白、米糠肽4种产品;(1) This method provides a method for comprehensive utilization of rice bran, which can simultaneously prepare four products of rice bran oil, rice bran crude fiber, rice bran protein, and rice bran peptide;

(2)用浸提法提取米糠中的油脂成分,每100g米糠制备得米糠油约10g。(2) Extract oil and fat components in rice bran by leaching method, and prepare about 10 g of rice bran oil per 100 g of rice bran.

(3)利用碱溶酸沉法分离米糠粗纤维和米糠蛋白,提取的米糠蛋白中粗蛋白含量70%左右,米糠粗纤维中膳食纤维含量40%左右;(3) Separating rice bran crude fiber and rice bran protein by alkali-soluble acid precipitation method, the crude protein content in the extracted rice bran protein is about 70%, and the dietary fiber content in the rice bran crude fiber is about 40%;

(4)采用超滤法对米糠肽进行分级处理,保证100%的米糠肽分子量在1000Da以下,并对于分子量1000Da以上的米糠肽进行二次酶解,使最终产品的分子量分布均在1000Da以下;(4) The ultrafiltration method is used to classify the rice bran peptide to ensure that 100% of the rice bran peptide has a molecular weight below 1000Da, and the rice bran peptide with a molecular weight above 1000Da is subjected to secondary enzymatic hydrolysis, so that the molecular weight distribution of the final product is all below 1000Da;

(5)利用阴阳交换树脂对米糠肽粗品进行脱盐,没有经过脱盐处理的产品盐分含量大于8%,经过本方法脱盐处理的产品盐分含量小于2%;(5) Desalting the crude rice bran peptide by using an anion-yang exchange resin, the salt content of the product that has not been desalted is greater than 8%, and the salt content of the product desalted by this method is less than 2%;

附图说明 Description of drawings

下面结合附图和具体实施方式对本发明做进一步详细的说明。The present invention will be described in further detail below in conjunction with the accompanying drawings and specific embodiments.

图1为本发明的综合利用米糠的方法的工艺流程图。Fig. 1 is the process flow chart of the method for comprehensive utilization of rice bran of the present invention.

具体实施方式 Detailed ways

本发明中所述的E/S比是指酶的用量与米糠蛋白的质量比;本发明中所述的中性蛋白酶As1.398的酶活性为130000U/g;本发明中的比例如无特别说明均指质量比。The E/S ratio described in the present invention refers to the mass ratio of the consumption of enzyme and rice bran protein; The enzymatic activity of neutral protease As1.398 described in the present invention is 130000U/g; The description refers to the mass ratio.

实施例1Example 1

一种综合利用米糠的方法,该方法包括如下步骤:A method for comprehensively utilizing rice bran, the method comprising the steps of:

(1)称取米糠100g,粉碎过60目筛,采用索氏抽提法,用95%正己烷溶剂在50℃条件下浸提2h,然后将正己烷溶液过滤,将米糠晾晒至正己烷完全挥发,为脱脂米糠;将滤液用旋转蒸发器将正己烷完全蒸发,剩下的为米糠油,称重为11.3g;(1) Weigh 100g of rice bran, crush it through a 60-mesh sieve, use Soxhlet extraction method, use 95% n-hexane solvent to extract at 50°C for 2 hours, then filter the n-hexane solution, and dry the rice bran until the n-hexane is completely Volatility is defatted rice bran; the filtrate is completely evaporated with n-hexane with a rotary evaporator, and the rest is rice bran oil, weighing 11.3g;

(2)将步骤(1)脱脂米糠倒入600mL水中,加热至45℃,用NaOH试剂调节pH至9.0,不停搅拌15min,在3000r/min的转速下,离心15min,取上清液;将沉淀烘干,为米糠粗纤维,称重为53.2g;(2) Pour the defatted rice bran in step (1) into 600mL water, heat to 45°C, adjust the pH to 9.0 with NaOH reagent, stir continuously for 15min, centrifuge at 3000r/min for 15min, and take the supernatant; Precipitated and dried, it was rice bran crude fiber, weighing 53.2g;

(3)将步骤(2)的上清液加热至80℃,用柠檬酸试剂调节pH至3.5,不停搅拌10min,3000r/min,15min,离心收集沉淀,为米糠蛋白,烘干可得米糠蛋白粉,称重为26.5g;(3) Heat the supernatant of step (2) to 80°C, adjust the pH to 3.5 with citric acid reagent, stir continuously for 10 minutes, 3000r/min, 15 minutes, centrifuge to collect the precipitate, which is rice bran protein, and dry it to get rice bran Protein powder, weighing 26.5g;

(4)将步骤(3)的沉淀加入200mL水中,加热至90℃,保持20min,然后冷却至45℃,用NaOH试剂调节并保持pH在7.0,加入中性蛋白酶As1.398(酶活性为130000U/g)1.5g,酶解2h,酶解过程中不断搅拌,并用NaOH溶液保持pH值在7.0;(4) Add the precipitate of step (3) to 200mL water, heat to 90°C, keep for 20min, then cool to 45°C, adjust and keep the pH at 7.0 with NaOH reagent, add neutral protease As1.398 (enzyme activity is 130000U /g) 1.5g, enzymatic hydrolysis for 2h, stirring continuously during the enzymolysis process, and keeping the pH value at 7.0 with NaOH solution;

(5)待待步骤(4)酶解结束后,迅速用HCl溶液调节pH至4.0,在3000r/min的转速下,离心15min,取上清液,所得即为米糠肽粗制液;(5) After the enzymatic hydrolysis in step (4), quickly adjust the pH to 4.0 with HCl solution, centrifuge for 15 minutes at a speed of 3000r/min, take the supernatant, and obtain the crude rice bran peptide liquid;

(6)将步骤(5)所得的米糠肽粗制液注入储槽中,溶液经微滤后通过分子量截留量为1000Da超滤膜,溶液中的小分子物质经中空纤维膜的内壁渗透出来成为超滤液,收集超滤液,为米糠肽超滤液;溶液中的蛋白等大分子物质得以保留并得到浓缩,将浓缩液回收至步骤4中再次酶解;(6) Inject the crude rice bran peptide solution obtained in step (5) into the storage tank, and the solution passes through the ultrafiltration membrane with a molecular weight cut-off of 1000Da after microfiltration, and the small molecular substances in the solution permeate out through the inner wall of the hollow fiber membrane to become The ultrafiltrate, collecting the ultrafiltrate, is the rice bran peptide ultrafiltrate; the protein and other macromolecular substances in the solution are preserved and concentrated, and the concentrated solution is recovered to step 4 for enzymatic hydrolysis again;

(7)交换树脂于去离子水中浸泡处理24小时后装柱,然后分别用7.5%盐酸和10%NaOH对其进行浸泡,转化为H+型阳离子交换树脂和OH-型阴离子交换树脂,再用去离子水清洗至pH为7.0待用;(7) The exchange resin was soaked in deionized water for 24 hours and then packed into a column, then it was soaked with 7.5% hydrochloric acid and 10% NaOH respectively, converted into H + type cation exchange resin and OH - type anion exchange resin, and then used Wash with deionized water until the pH is 7.0 for use;

将步骤(6)中所得的超滤液,以10倍柱体积/h的流速通过H+型阳离子交换树脂来脱除阳离子,待流出液pH=4.0左右时停止加样,之后将此流出液以同样流速通过OH-型阴离子交换树脂来脱除阴离子,至流出液呈pH为7.0时停止加样,收集为米糠肽精制液;The ultrafiltrate obtained in step (6) is passed through the H + type cation exchange resin at a flow rate of 10 times column volume/h to remove cations, and the sample addition is stopped when the pH of the effluent is about 4.0, and then the effluent is Remove anions by passing through OH - type anion exchange resin at the same flow rate, stop adding samples when the pH of the effluent is 7.0, and collect it as rice bran peptide refined solution;

(8)由步骤6中得到的米糠肽精制液,减压浓缩至固型物含量30%;(8) The rice bran peptide refined solution obtained in step 6 is concentrated under reduced pressure to a solid content of 30%;

(9)精制的米糠肽液浓缩后,经喷雾干燥或冷冻干燥制成干粉,称重为15.3g。(9) After the refined rice bran peptide solution is concentrated, it is spray-dried or freeze-dried to make a dry powder, weighing 15.3 g.

上述方法得到的米糠肽,经检测米糠肽总氮含量(以干基计)85.2%,肽含量(以干基计)≥80.4%,所得的相对分子质量均在1000Da以下,水分含量5.7%,灰分含量(以干基计)≤1.6%,粗脂肪含量(以干基计)≤0.8%。The rice bran peptide obtained by the above method has a total nitrogen content (on a dry basis) of 85.2% and a peptide content (on a dry basis) ≥ 80.4% after testing. The relative molecular weights obtained are all below 1000 Da and the moisture content is 5.7%. Ash content (on dry basis) ≤ 1.6%, crude fat content (on dry basis) ≤ 0.8%.

实施例2Example 2

一种综合利用米糠的方法,该方法包括如下步骤:A method for comprehensively utilizing rice bran, the method comprising the steps of:

(1)称取米糠500g,粉碎过60目筛,采用索氏抽提法,用95%正己烷溶剂在50℃条件下浸提2h,然后将正己烷溶液过滤,将米糠晾晒至正己烷完全挥发,为脱脂米糠;将滤液用旋转蒸发器将正己烷完全蒸发,剩下的为米糠油,称重为58.9g;(1) Weigh 500g of rice bran, crush it through a 60-mesh sieve, use Soxhlet extraction method, extract it with 95% n-hexane solvent at 50°C for 2 hours, then filter the n-hexane solution, and air-dry the rice bran until the n-hexane is completely Volatility is defatted rice bran; the filtrate is completely evaporated with n-hexane with a rotary evaporator, and the rest is rice bran oil, weighing 58.9g;

(2)将步骤(1)脱脂米糠倒入2.5L水中,加热至50℃,用NaOH试剂调节pH至8.5,不停搅拌15min,在3000r/min的转速下,离心15min,取上清液;将沉淀烘干,为米糠粗纤维,称重为247.3g;(2) Pour the defatted rice bran in step (1) into 2.5L of water, heat to 50°C, adjust the pH to 8.5 with NaOH reagent, stir continuously for 15min, centrifuge at 3000r/min for 15min, and take the supernatant; The precipitate was dried, and it was rice bran crude fiber, weighing 247.3g;

(3)将步骤(2)的上清液加热至90℃,用柠檬酸试剂调节pH至3.0,不停搅拌10min,3000r/min,15min,离心收集沉淀,为米糠蛋白,烘干可得米糠蛋白粉,称重为105.6g;(3) Heat the supernatant of step (2) to 90°C, adjust the pH to 3.0 with citric acid reagent, stir continuously for 10 minutes, 3000r/min, 15 minutes, centrifuge to collect the precipitate, which is rice bran protein, and dry it to get rice bran Protein powder, weighing 105.6g;

(4)将步骤(3)的沉淀加入1L水中,加热至90℃,保持20min,然后冷却至40℃,用NaOH试剂调节并保持pH在7.5,加入中性蛋白酶As1.398(酶活性为130000U/g)5g,酶解3h,酶解过程中不断搅拌,并用NaOH溶液保持pH值在7.5;(4) Add the precipitate of step (3) into 1L of water, heat to 90°C, keep for 20min, then cool to 40°C, adjust with NaOH reagent and keep the pH at 7.5, add neutral protease As1.398 (enzyme activity is 130000U /g) 5g, enzymolysis for 3h, stirring constantly during the enzymolysis process, and keeping the pH value at 7.5 with NaOH solution;

(5)待待步骤(4)酶解结束后,迅速用HCl溶液调节pH至4.0,在3000r/min的转速下,离心15min,取上清液,所得即为米糠肽粗制液;(5) After the enzymatic hydrolysis in step (4), quickly adjust the pH to 4.0 with HCl solution, centrifuge for 15 minutes at a speed of 3000r/min, take the supernatant, and obtain the crude rice bran peptide liquid;

(6)将步骤(5)所得的米糠肽粗制液注入储槽中,溶液经微滤后通过分子量截留量为1000Da超滤膜,溶液中的小分子物质经中空纤维膜的内壁渗透出来成为超滤液,收集超滤液,为米糠肽超滤液;溶液中的蛋白等大分子物质得以保留并得到浓缩,将浓缩液回收至步骤4中再次酶解;(6) Inject the crude rice bran peptide solution obtained in step (5) into the storage tank, and the solution passes through the ultrafiltration membrane with a molecular weight cut-off of 1000Da after microfiltration, and the small molecular substances in the solution permeate out through the inner wall of the hollow fiber membrane to become The ultrafiltrate, collecting the ultrafiltrate, is the rice bran peptide ultrafiltrate; the protein and other macromolecular substances in the solution are preserved and concentrated, and the concentrated solution is recovered to step 4 for enzymatic hydrolysis again;

(7)交换树脂于去离子水中浸泡处理24小时后装柱,然后分别用7.5%盐酸和10%NaOH对其进行浸泡,转化为H+型阳离子交换树脂和OH-型阴离子交换树脂,再用去离子水清洗至pH为7.0待用;(7) The exchange resin was soaked in deionized water for 24 hours and then packed into a column, then it was soaked with 7.5% hydrochloric acid and 10% NaOH respectively, converted into H + type cation exchange resin and OH - type anion exchange resin, and then used Wash with deionized water until the pH is 7.0 for use;

将步骤(6)中所得的超滤液,以10倍柱体积/h的流速通过H+型阳离子交换树脂来脱除阳离子,待流出液pH=4.0左右时停止加样,之后将此流出液以同样流速通过OH-型阴离子交换树脂来脱除阴离子,至流出液呈pH为7.0时停止加样,收集为米糠肽精制液;The ultrafiltrate obtained in step (6) is passed through the H + type cation exchange resin at a flow rate of 10 times column volume/h to remove cations, and the sample addition is stopped when the pH of the effluent is about 4.0, and then the effluent is Remove anions by passing through OH - type anion exchange resin at the same flow rate, stop adding samples when the pH of the effluent is 7.0, and collect it as rice bran peptide refined solution;

(8)由步骤6中得到的米糠肽精制液,减压浓缩至固型物含量30%;(8) The rice bran peptide refined solution obtained in step 6 is concentrated under reduced pressure to a solid content of 30%;

(9)精制的米糠肽液浓缩后,经喷雾干燥或冷冻干燥制成干粉,称重为67.6g。(9) After the refined rice bran peptide solution is concentrated, it is spray-dried or freeze-dried to make a dry powder, weighing 67.6 g.

上述方法得到的米糠肽,经检测米糠肽总氮含量(以干基计)84.1%,肽含量(以干基计)≥79.5%,所得的相对分子质量均在1000Da以下,水分含量8.1%,灰分含量(以干基计)≤1.9%,粗脂肪含量(以干基计)≤0.9%。The rice bran peptide obtained by the above method has a total nitrogen content of rice bran peptide (on a dry basis) of 84.1% and a peptide content (on a dry basis) of ≥79.5%. Ash content (on dry basis) ≤ 1.9%, crude fat content (on dry basis) ≤ 0.9%.

实施例3Example 3

一种综合利用米糠的方法,该方法包括如下步骤:A method for comprehensively utilizing rice bran, the method comprising the steps of:

(1)称取米糠1000g,粉碎过80目筛,采用索氏抽提法,用95%正己烷溶剂在50℃条件下浸提2h,然后将正己烷溶液过滤,将米糠晾晒至正己烷完全挥发,为脱脂米糠;将滤液用旋转蒸发器将正己烷完全蒸发,剩下的为米糠油,称重为110.2g;(1) Weigh 1000g of rice bran, crush it through a 80-mesh sieve, use Soxhlet extraction method, use 95% n-hexane solvent to extract at 50°C for 2 hours, then filter the n-hexane solution, and dry the rice bran until the n-hexane is completely Volatility is defatted rice bran; the filtrate is completely evaporated with n-hexane with a rotary evaporator, and the rest is rice bran oil, weighing 110.2g;

(2)将步骤(1)脱脂米糠倒入7L水中,加热至45℃,用NaOH试剂调节pH至9.0,不停搅拌15min,在3000r/min的转速下,离心15min,取上清液;将沉淀烘干,为米糠粗纤维,称重为537.6g;(2) Pour the defatted rice bran in step (1) into 7L water, heat to 45°C, adjust the pH to 9.0 with NaOH reagent, stir continuously for 15min, centrifuge for 15min at a speed of 3000r/min, and take the supernatant; Precipitated and dried, it was rice bran crude fiber, weighing 537.6g;

(3)将步骤(2)的上清液加热至90℃,用柠檬酸试剂调节pH至3.0,不停搅拌10min,3000r/min,15min,离心收集沉淀,为米糠蛋白,烘干可得米糠蛋白粉,称重为206.8g;(3) Heat the supernatant of step (2) to 90°C, adjust the pH to 3.0 with citric acid reagent, stir continuously for 10 minutes, 3000r/min, 15 minutes, centrifuge to collect the precipitate, which is rice bran protein, and dry it to get rice bran Protein powder, weighing 206.8g;

(4)将步骤(3)的沉淀加入1500mL水中,加热至90℃,保持20min,然后冷却至45℃,用NaOH试剂调节并保持pH在7.0,加入中性蛋白酶As1.398(酶活性为130000U/g)10g,酶解4h,酶解过程中不断搅拌,并用NaOH溶液保持pH值在7.5;(4) Add the precipitate of step (3) into 1500mL water, heat to 90°C, keep for 20min, then cool to 45°C, adjust and keep the pH at 7.0 with NaOH reagent, add neutral protease As1.398 (enzyme activity is 130000U /g) 10g, enzymolysis for 4h, stirring constantly during the enzymolysis process, and keeping the pH value at 7.5 with NaOH solution;

(5)待待步骤(4)酶解结束后,迅速用HCl溶液调节pH至4.0,在3000r/min的转速下,离心15min,取上清液,所得即为米糠肽粗制液;(5) After the enzymatic hydrolysis in step (4), quickly adjust the pH to 4.0 with HCl solution, centrifuge for 15 minutes at a speed of 3000r/min, take the supernatant, and obtain the crude rice bran peptide liquid;

(6)将步骤(5)所得的米糠肽粗制液注入储槽中,溶液经微滤后通过分子量截留量为1000Da超滤膜,溶液中的小分子物质经中空纤维膜的内壁渗透出来成为超滤液,收集超滤液,为米糠肽超滤液;溶液中的蛋白等大分子物质得以保留并得到浓缩,将浓缩液回收至步骤4中再次酶解;(6) Inject the crude rice bran peptide solution obtained in step (5) into the storage tank, and the solution passes through the ultrafiltration membrane with a molecular weight cut-off of 1000Da after microfiltration, and the small molecular substances in the solution permeate out through the inner wall of the hollow fiber membrane to become The ultrafiltrate, collecting the ultrafiltrate, is the rice bran peptide ultrafiltrate; the protein and other macromolecular substances in the solution are preserved and concentrated, and the concentrated solution is recovered to step 4 for enzymatic hydrolysis again;

(7)交换树脂于去离子水中浸泡处理24小时后装柱,然后分别用7.5%盐酸和10%NaOH对其进行浸泡,转化为H+型阳离子交换树脂和OH-型阴离子交换树脂,再用去离子水清洗至pH为7.0待用;(7) The exchange resin was soaked in deionized water for 24 hours and then packed into a column, then it was soaked with 7.5% hydrochloric acid and 10% NaOH respectively, converted into H + type cation exchange resin and OH - type anion exchange resin, and then used Wash with deionized water until the pH is 7.0 for use;

将步骤(6)中所得的超滤液,以10倍柱体积/h的流速通过H+型阳离子交换树脂来脱除阳离子,待流出液pH=4.0左右时停止加样,之后将此流出液以同样流速通过OH-型阴离子交换树脂来脱除阴离子,至流出液呈pH为7.0时停止加样,收集为米糠肽精制液;The ultrafiltrate obtained in step (6) is passed through the H + type cation exchange resin at a flow rate of 10 times column volume/h to remove cations, and when the effluent pH=4.0, the sample addition is stopped, and the effluent is then Remove anions by passing through OH - type anion exchange resin at the same flow rate, stop adding samples when the pH of the effluent is 7.0, and collect it as rice bran peptide refined solution;

(8)由步骤6中得到的米糠肽精制液,减压浓缩至固型物含量30%;(8) The rice bran peptide refined solution obtained in step 6 is concentrated under reduced pressure to a solid content of 30%;

(9)精制的米糠肽液浓缩后,经喷雾干燥或冷冻干燥制成干粉,称重为158.9g。(9) After the refined rice bran peptide solution is concentrated, it is spray-dried or freeze-dried to make a dry powder, weighing 158.9 g.

上述方法得到的米糠肽,经检测米糠肽总氮含量(以干基计)81.8%,肽含量(以干基计)≥76.2%,所得的相对分子质量均在1000Da以下,水分含量8.5%,灰分含量(以干基计)≤1.9%,粗脂肪含量(以干基计)≤1.0%。The rice bran peptide obtained by the above method has a total nitrogen content of rice bran peptide (on a dry basis) of 81.8% and a peptide content (on a dry basis) ≥ 76.2%. Ash content (on dry basis) ≤ 1.9%, crude fat content (on dry basis) ≤ 1.0%.

Claims (1)

1. a method that fully utilizes rice bran, is characterized in that the method comprises the steps:
(1) rice bran is pulverized, crossed 60~80 mesh sieves, adopt the Soxhlet extraction process, with 95% normal hexane solvent lixiviate 2h under 50 ℃ of conditions, then hexane solution is filtered, rice bran airing to normal hexane is volatilized fully, be defatted rice bran; Filtrate is evaporated normal hexane fully with rotatory evaporator, and remaining is Rice pollard oil;
(2) step (1) defatted rice bran and the water mass ratio by 1: 5~1: 10 is dissolved in water, be heated to 45~55 ℃, regulate pH to 8.0~10.0 with NaOH reagent, do not stop to stir 15min, under the rotating speed of 3000~4000r/min, centrifugal 15min gets supernatant liquor, to precipitate oven dry, be the rice-bran crude fiber;
(3) supernatant liquor with step (2) is heated to 70~90 ℃, regulates pH to 3.0~5.0 with citric acid reagent, does not stop to stir 10min, 3000~4000r/min, and 15min, centrifugal collecting precipitation is rice bran protein, dries to get the rice bran protein powder;
(4) rice bran protein of step (3) and the water mass ratio by 1: 5~1: 10 is dissolved in water, be heated to 90~100 ℃, keep 15~30min, then be cooled to 35~50 ℃, regulate and keep pH 6.0~8.0 with NaOH reagent, adding neutral protease As1.398 by E/S than 3%~7%, enzymolysis 2~4h, constantly stir in enzymolysis process, and keep the pH value 6.0~8.0 with NaOH solution;
(5) after step (4) enzymolysis finishes, regulate pH to 5.0~3.0 with HCl solution rapidly, under the rotating speed of 3000~4000r/min, centrifugal 15min gets supernatant liquor, and gained is the rough liquid of rice bran peptide;
(6) the rough liquid of the rice bran peptide of step (5) gained is injected storage tank, solution is the 1000Da ultra-filtration membrane by the molecular weight interception after micro-filtration, small-molecule substance in solution infiltrates through the inwall of hollow-fibre membrane becomes ultrafiltrated, collects ultrafiltrated, is rice bran peptide ultrafiltrated; Solution comprises that albumen is kept and concentrated at interior macromolecular substance, and concentrated solution is recycled in step (4) enzymolysis again;
(7) exchange resin immersion treatment in deionized water filled post after 24 hours, then with 7.5% hydrochloric acid and 10%NaOH, it was soaked respectively, was converted into H +Type Zeo-karb and OH -Type anionite-exchange resin, then be 7.0 stand-by with washed with de-ionized water to pH;
With the ultrafiltrated of gained in step (6), pass through H with the flow velocity of 5~10 times of column volume/h +The type Zeo-karb removes positively charged ion, stops application of sample when effluent liquid pH=4.0, afterwards this effluent liquid is passed through OH with same flow velocity -Type anionite-exchange resin removes negatively charged ion, is pH to effluent liquid and stops application of sample at 7.0 o'clock, is collected as rice bran peptide refined liquid;
(8) by the rice bran peptide refined liquid that obtains in step 6, be evaporated to solid content 20%~30%;
(9) after refining rice bran peptide liquid concentrated, dry powder was made in spray-dried or lyophilize.
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CN112481022A (en) * 2020-12-22 2021-03-12 霍邱县敏东米业有限公司 Method for synchronously preparing rice bran oil and high-purity active peptide by using rice bran

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1439625A (en) * 2003-03-17 2003-09-03 江南大学 Preparation for active octacosa alkanol and triaconta alkanol in rice bran
CN101301067A (en) * 2008-06-06 2008-11-12 浙江大学 Method for comprehensively extracting active substances in rice bran by separation technology
CN101575620A (en) * 2009-06-10 2009-11-11 北京化工大学 Method for producing fermentation raw material, rice bran oil and protein feed by comprehensively utilizing rice bran

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1439625A (en) * 2003-03-17 2003-09-03 江南大学 Preparation for active octacosa alkanol and triaconta alkanol in rice bran
CN101301067A (en) * 2008-06-06 2008-11-12 浙江大学 Method for comprehensively extracting active substances in rice bran by separation technology
CN101575620A (en) * 2009-06-10 2009-11-11 北京化工大学 Method for producing fermentation raw material, rice bran oil and protein feed by comprehensively utilizing rice bran

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
何欢等.米糠生物活性肽生产工艺的研究.《粮食加工》.2008,第33卷(第1期),38-39,41. *

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