CN116286731B - Protein-based immobilized enzyme, preparation method thereof and method for efficiently preparing diglyceride - Google Patents
Protein-based immobilized enzyme, preparation method thereof and method for efficiently preparing diglyceride Download PDFInfo
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- 102000004169 proteins and genes Human genes 0.000 title claims abstract description 43
- 108090000623 proteins and genes Proteins 0.000 title claims abstract description 43
- 108010093096 Immobilized Enzymes Proteins 0.000 title claims abstract description 31
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- 238000000034 method Methods 0.000 title claims description 24
- 235000017060 Arachis glabrata Nutrition 0.000 claims abstract description 67
- 235000010777 Arachis hypogaea Nutrition 0.000 claims abstract description 67
- 235000018262 Arachis monticola Nutrition 0.000 claims abstract description 67
- 102000006395 Globulins Human genes 0.000 claims abstract description 67
- 108010044091 Globulins Proteins 0.000 claims abstract description 67
- 235000020232 peanut Nutrition 0.000 claims abstract description 67
- 239000002245 particle Substances 0.000 claims abstract description 35
- 108090001060 Lipase Proteins 0.000 claims abstract description 34
- 239000004367 Lipase Substances 0.000 claims abstract description 34
- 102000004882 Lipase Human genes 0.000 claims abstract description 34
- 235000019421 lipase Nutrition 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000004132 cross linking Methods 0.000 claims abstract description 12
- 239000008367 deionised water Substances 0.000 claims abstract description 11
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 11
- 239000006185 dispersion Substances 0.000 claims abstract description 11
- 239000002244 precipitate Substances 0.000 claims abstract description 11
- 150000003839 salts Chemical class 0.000 claims abstract description 10
- 238000006243 chemical reaction Methods 0.000 claims abstract description 8
- 238000010438 heat treatment Methods 0.000 claims abstract description 7
- 238000010008 shearing Methods 0.000 claims abstract description 7
- 230000021736 acetylation Effects 0.000 claims abstract description 6
- 238000006640 acetylation reaction Methods 0.000 claims abstract description 6
- 230000004048 modification Effects 0.000 claims abstract description 4
- 238000012986 modification Methods 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims abstract description 3
- 241001553178 Arachis glabrata Species 0.000 claims abstract 24
- 239000000243 solution Substances 0.000 claims description 36
- 239000000839 emulsion Substances 0.000 claims description 18
- 239000003153 chemical reaction reagent Substances 0.000 claims description 11
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 8
- 238000005119 centrifugation Methods 0.000 claims description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 6
- 239000006228 supernatant Substances 0.000 claims description 6
- 108010048733 Lipozyme Proteins 0.000 claims description 5
- FCCDDURTIIUXBY-UHFFFAOYSA-N lipoamide Chemical group NC(=O)CCCCC1CCSS1 FCCDDURTIIUXBY-UHFFFAOYSA-N 0.000 claims description 5
- 239000011780 sodium chloride Substances 0.000 claims description 4
- FALRKNHUBBKYCC-UHFFFAOYSA-N 2-(chloromethyl)pyridine-3-carbonitrile Chemical compound ClCC1=NC=CC=C1C#N FALRKNHUBBKYCC-UHFFFAOYSA-N 0.000 claims description 3
- 238000000502 dialysis Methods 0.000 claims description 3
- 229940014800 succinic anhydride Drugs 0.000 claims description 3
- 150000001982 diacylglycerols Chemical class 0.000 claims description 2
- 238000002715 modification method Methods 0.000 claims description 2
- 239000008055 phosphate buffer solution Substances 0.000 claims description 2
- 239000000843 powder Substances 0.000 claims description 2
- 238000003287 bathing Methods 0.000 claims 1
- 230000000694 effects Effects 0.000 abstract description 14
- 235000013305 food Nutrition 0.000 abstract description 5
- 238000006555 catalytic reaction Methods 0.000 abstract description 4
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 244000105624 Arachis hypogaea Species 0.000 description 43
- 230000003197 catalytic effect Effects 0.000 description 12
- 102000004190 Enzymes Human genes 0.000 description 9
- 108090000790 Enzymes Proteins 0.000 description 9
- 235000012424 soybean oil Nutrition 0.000 description 6
- 239000003549 soybean oil Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 150000003384 small molecules Chemical class 0.000 description 4
- 239000004094 surface-active agent Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 235000019198 oils Nutrition 0.000 description 3
- 239000012188 paraffin wax Substances 0.000 description 3
- 239000000741 silica gel Substances 0.000 description 3
- 229910002027 silica gel Inorganic materials 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 2
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 2
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- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920001661 Chitosan Polymers 0.000 description 1
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 1
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 1
- XJLXINKUBYWONI-DQQFMEOOSA-N [[(2r,3r,4r,5r)-5-(6-aminopurin-9-yl)-3-hydroxy-4-phosphonooxyoxolan-2-yl]methoxy-hydroxyphosphoryl] [(2s,3r,4s,5s)-5-(3-carbamoylpyridin-1-ium-1-yl)-3,4-dihydroxyoxolan-2-yl]methyl phosphate Chemical compound NC(=O)C1=CC=C[N+]([C@@H]2[C@H]([C@@H](O)[C@H](COP([O-])(=O)OP(O)(=O)OC[C@@H]3[C@H]([C@@H](OP(O)(O)=O)[C@@H](O3)N3C4=NC=NC(N)=C4N=C3)O)O2)O)=C1 XJLXINKUBYWONI-DQQFMEOOSA-N 0.000 description 1
- 108091005646 acetylated proteins Proteins 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
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- 238000007796 conventional method Methods 0.000 description 1
- 239000011258 core-shell material Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 125000005456 glyceride group Chemical group 0.000 description 1
- 125000001165 hydrophobic group Chemical group 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 229920000592 inorganic polymer Polymers 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000004005 microsphere Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229930027945 nicotinamide-adenine dinucleotide Natural products 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000006053 organic reaction Methods 0.000 description 1
- 239000012430 organic reaction media Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000005185 salting out Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N9/00—Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
- C12N9/14—Hydrolases (3)
- C12N9/16—Hydrolases (3) acting on ester bonds (3.1)
- C12N9/18—Carboxylic ester hydrolases (3.1.1)
- C12N9/20—Triglyceride splitting, e.g. by means of lipase
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K14/00—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof
- C07K14/415—Peptides having more than 20 amino acids; Gastrins; Somatostatins; Melanotropins; Derivatives thereof from plants
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- C12N11/00—Carrier-bound or immobilised enzymes; Carrier-bound or immobilised microbial cells; Preparation thereof
- C12N11/02—Enzymes or microbial cells immobilised on or in an organic carrier
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- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/64—Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats
- C12P7/6436—Fatty acid esters
- C12P7/6445—Glycerides
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- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12Y—ENZYMES
- C12Y301/00—Hydrolases acting on ester bonds (3.1)
- C12Y301/01—Carboxylic ester hydrolases (3.1.1)
- C12Y301/01003—Triacylglycerol lipase (3.1.1.3)
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Abstract
Description
技术领域Technical Field
本发明涉及脂肪酶固定化与应用技术领域。更具体地说,本发明涉及一种蛋白基固定化酶及其制备方法及高效制备甘油二酯的方法。The present invention relates to the technical field of lipase immobilization and application, and more specifically, to a protein-based immobilized enzyme and a preparation method thereof and a method for efficiently preparing diglyceride.
背景技术Background technique
生物酶是一种常见的生物催化剂,因其具有较高的化学、区域和立体选择性且能在温和的反应条件下表现出较高的催化活性可用于多种有机反应。然而亲水性的生物酶在催化疏水性底物时,两相界面小,底物在两相之间传质效率低,酶与底物接触不充分,导致催化效率低。为了适应有机反应介质,提高回收利用性,目前常用乳化的手段增大反应接触面积,提高催化效率。为了维持乳液稳定和催化界面,通常需要加入小分子表面活性剂或者剧烈的搅拌。然而小分子表面活性剂难以与产物分离,会带来安全性问题。此外,小分子表面活性剂和剧烈搅拌都会不同程度的破坏酶结构,进而影响酶活。Biological enzymes are a common biocatalyst. They can be used in a variety of organic reactions because of their high chemical, regional and stereoselectivity and high catalytic activity under mild reaction conditions. However, when hydrophilic biological enzymes catalyze hydrophobic substrates, the two-phase interface is small, the mass transfer efficiency of the substrate between the two phases is low, and the contact between the enzyme and the substrate is insufficient, resulting in low catalytic efficiency. In order to adapt to organic reaction media and improve recycling, emulsification is currently commonly used to increase the reaction contact area and improve catalytic efficiency. In order to maintain the stability of the emulsion and the catalytic interface, it is usually necessary to add small molecule surfactants or violent stirring. However, small molecule surfactants are difficult to separate from the product, which will bring safety issues. In addition, small molecule surfactants and violent stirring will destroy the enzyme structure to varying degrees, thereby affecting enzyme activity.
中国申请,申请号为201810430317.7的实施例1中公开了一种选取硅胶为载体固定GDH制备NADPH。使用硅胶作为生物酶的载体,硅胶降解性低、具有一定的生物毒性,限制了其在食品领域的应用。而本发明使用花生球蛋白天然材料得到安全性高,不存在生物降解性等问题的蛋白基脂肪酶固体颗粒。In Example 1 of the Chinese application with application number 201810430317.7, a method for preparing NADPH by fixing GDH using silica gel as a carrier is disclosed. When silica gel is used as a carrier of biological enzymes, silica gel has low degradability and certain biological toxicity, which limits its application in the food field. However, the present invention uses natural peanut globulin materials to obtain protein-based lipase solid particles with high safety and no problems such as biodegradability.
中国申请,申请号为202111552631.0的实施例1中公开了一种使用石蜡、壳聚糖、聚丙烯酰胺、单硬酯酰甘油酯在高速均质机作用下制备固定化酶,将脂肪酶包封在石蜡微球的核壳式结构中。该法中引入了聚丙烯酰胺、石蜡等材料,限制了其在生物医药与食品领域的应用,而本发明无此类物质的引入,拓宽了其在食品催化中的应用。The Chinese application, with application number 202111552631.0, discloses in Example 1 a method of preparing an immobilized enzyme using paraffin, chitosan, polyacrylamide, and monostearyl glyceride under the action of a high-speed homogenizer, and encapsulating the lipase in a core-shell structure of paraffin microspheres. This method introduces materials such as polyacrylamide and paraffin, which limits its application in the fields of biomedicine and food. However, the present invention does not introduce such substances, which broadens its application in food catalysis.
Pickering乳液已被证明可用于提高催化效率,该体系在避免添加小分子表面活性剂的同时高能乳化也是非必要的。目前常用无机颗粒、无机聚合物颗粒等交联固定生物酶进而构建Pickering乳液催化体系。但是这些颗粒生物相容性低、安全性问题突出,可见基于天然大分子制备食品级颗粒用于固定生物酶构建Pickering乳液催化体系是有必要的。鉴于此,特提出本发明。Pickering emulsions have been proven to be useful for improving catalytic efficiency. This system avoids the addition of small molecule surfactants and high-energy emulsification is not necessary. At present, inorganic particles, inorganic polymer particles, etc. are commonly used to cross-link and fix biological enzymes to construct Pickering emulsion catalytic systems. However, these particles have low biocompatibility and prominent safety issues. It can be seen that it is necessary to prepare food-grade particles based on natural macromolecules for fixing biological enzymes to construct Pickering emulsion catalytic systems. In view of this, the present invention is specially proposed.
发明内容Summary of the invention
本发明的一个目的是解决至少上述问题,并提供至少后面将说明的优点。An object of the present invention is to solve at least the above problems and to provide at least the advantages which will be described hereinafter.
为了实现根据本发明的这些目的和其它优点,提供了一种蛋白基固定化酶的制备方法,包括以下步骤:In order to achieve these purposes and other advantages according to the present invention, a method for preparing a protein-based immobilized enzyme is provided, comprising the following steps:
步骤一、提取得到花生球蛋白;Step 1, extracting and obtaining peanut globulin;
步骤二、将花生球蛋白加去离子水制备得到花生球蛋白分散液,调节pH至碱性,进行乙酰化改性得到乙酰化花生球蛋白溶液;Step 2: adding deionized water to peanut globulin to prepare a peanut globulin dispersion, adjusting the pH to alkaline, and performing acetylation modification to obtain an acetylated peanut globulin solution;
步骤三、乙酰化花生球蛋白溶液依次经热处理、盐处理得到乙酰化花生球蛋白颗粒;Step 3, the acetylated peanut globulin solution is subjected to heat treatment and salt treatment in sequence to obtain acetylated peanut globulin particles;
步骤四、使用戊二醛将乙酰化球蛋白颗粒和脂肪酶进行交联固定,交联反应结束后,离心取沉淀,加入去离子水剪切破碎,得到蛋白基固定化酶。Step 4: Use glutaraldehyde to cross-link and fix the acetylated globulin particles and lipase. After the cross-linking reaction is completed, centrifuge to obtain the precipitate, add deionized water to shear and crush it, and obtain the protein-based immobilized enzyme.
优选的是,花生球蛋白的提取方法具体为:将花生脱脂粉用pH为6.9~7.5、浓度为0.35~0.45mol/L的磷酸缓冲溶液以料液比1g:1.5~3.5mL混合,于6000~10000rpm离心20~40min,去除沉淀,取上清液于2~5℃条件下冷沉一定时间,于2~5℃、6000~10000rpm离心20~40min,取沉淀,冷冻干燥或喷雾干燥得到花生球蛋白。Preferably, the method for extracting peanut globulin is as follows: peanut defatted powder is mixed with a phosphate buffer solution having a pH value of 6.9 to 7.5 and a concentration of 0.35 to 0.45 mol/L at a solid-liquid ratio of 1 g:1.5 to 3.5 mL, centrifuged at 6000 to 10000 rpm for 20 to 40 min, the precipitate is removed, the supernatant is cooled and precipitated at 2 to 5° C. for a certain period of time, centrifuged at 2 to 5° C. and 6000 to 10000 rpm for 20 to 40 min, the precipitate is taken, and freeze-dried or spray-dried to obtain peanut globulin.
优选的是,乙酰化改性的方法具体为:调节花生球蛋白分散液的pH值为9.5~11,花生球蛋白分散液中花生球蛋白的含量为6.5wt%,加入花生球蛋白0~50wt%的丁二酸酐,搅拌20~50min,并保持pH值为9.5~11,于2~4℃条件下采用10kDa的透析袋透析24~48h,得到乙酰化花生球蛋白溶液。Preferably, the acetylation modification method is as follows: adjusting the pH value of the peanut globulin dispersion to 9.5-11, the content of peanut globulin in the peanut globulin dispersion to 6.5wt%, adding 0-50wt% succinic anhydride of peanut globulin, stirring for 20-50min, and maintaining the pH value at 9.5-11, dialyzing at 2-4°C using a 10kDa dialysis bag for 24-48h to obtain an acetylated peanut globulin solution.
优选的是,步骤三中的热处理具体为:于85~95℃水浴15~45min。Preferably, the heat treatment in step three is specifically: water bath at 85-95° C. for 15-45 min.
优选的是,步骤三中的盐处理具体为:采用盐酸调节pH至5~6.5,然后加入NaCl颗粒至NaCl的浓度为500~900mmol,即得乙酰化花生球蛋白颗粒。Preferably, the salt treatment in step 3 is specifically as follows: adjusting the pH to 5-6.5 with hydrochloric acid, and then adding NaCl particles to a concentration of 500-900 mmol to obtain acetylated peanut globulin particles.
优选的是,步骤四中乙酰化花生球蛋白溶液中的花生球蛋白的浓度为2.0~7.0wt%,戊二醛试剂的浓度为0~3.0%,脂肪酶液浓度为5.0~15.0%,交联时间为0.5~4.0h,脂肪酶液与乙酰化花生球蛋白溶液的体积比例为1:3~7,戊二醛试剂与乙酰化花生球蛋白溶液的体积比为20~30:1。Preferably, in step 4, the concentration of peanut globulin in the acetylated peanut globulin solution is 2.0-7.0wt%, the concentration of the glutaraldehyde reagent is 0-3.0%, the concentration of the lipase solution is 5.0-15.0%, the cross-linking time is 0.5-4.0h, the volume ratio of the lipase solution to the acetylated peanut globulin solution is 1:3-7, and the volume ratio of the glutaraldehyde reagent to the acetylated peanut globulin solution is 20-30:1.
优选的是,交联结束后,离心的条件为120000rpm,离心15min,去除上清液,取沉淀,加入去离子水至离心前体积,并于6000rpm剪切破碎1min。Preferably, after the cross-linking is completed, the centrifugation condition is 120,000 rpm for 15 min, the supernatant is removed, the precipitate is taken, deionized water is added to the volume before centrifugation, and shearing and crushing is performed at 6,000 rpm for 1 min.
优选的是,脂肪酶为Lipozyme TL 100L。Preferably, the lipase is Lipozyme TL 100L.
提供一种上述的制备方法制备得到的蛋白基固定化酶。Provided is a protein-based immobilized enzyme prepared by the above preparation method.
提供一种基于上述蛋白基固定化酶制备甘油二酯的方法,包括以下步骤:A method for preparing diglyceride based on the above protein-based immobilized enzyme is provided, comprising the following steps:
步骤a、将蛋白基固定化酶加入油相制备得到Pickering乳液;Step a, adding protein-based immobilized enzyme into oil phase to prepare Pickering emulsion;
步骤b、Pickering乳液于45℃条件下反应一定时间,得到甘油二酯。Step b: reacting the Pickering emulsion at 45° C. for a certain period of time to obtain diglyceride.
本发明至少包括以下有益效果:The present invention has at least the following beneficial effects:
第一、本发明将脂肪酶与乙酰化花生球蛋白进行交联固定,所得蛋白基固定化酶颗粒经优化后,具有较高的固载效率和比活性,并能稳定W/O型Pickering乳液,构建Pickering乳液催化体系。First, the present invention cross-links and fixes lipase and acetylated peanut globulin, and the obtained protein-based immobilized enzyme particles have higher immobilization efficiency and specific activity after optimization, and can stabilize W/O type Pickering emulsion to construct a Pickering emulsion catalytic system.
第二、本发明构建的催化体系可以有效地提升催化制备甘油二酯油的效率,为制备甘油二酯油开创了新的途径和方法。Second, the catalytic system constructed by the present invention can effectively improve the efficiency of catalytic preparation of diglyceride oil, and create a new approach and method for preparing diglyceride oil.
第三、本发明提供的蛋白基固定化酶制备方法,操作简单,使用安全,催化效率提高,有利于其实现在食品工业中生产。Third, the method for preparing the protein-based immobilized enzyme provided by the present invention is simple to operate, safe to use, and has improved catalytic efficiency, which is conducive to its implementation in production in the food industry.
本发明的其它优点、目标和特征将部分通过下面的说明体现,部分还将通过对本发明的研究和实践而为本领域的技术人员所理解。Other advantages, objectives and features of the present invention will be embodied in part through the following description, and in part will be understood by those skilled in the art through study and practice of the present invention.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为本发明的比活性测试数据图;Fig. 1 is a graph showing specific activity test data of the present invention;
图2为本发明的甘油二酯含量曲线;Fig. 2 is a diglyceride content curve of the present invention;
图3为本发明花生球蛋白和乙酰化花生球蛋白在pH5.5时的分散状态图;FIG3 is a diagram showing the dispersion state of peanut globulin and acetylated peanut globulin of the present invention at pH 5.5;
图4为本发明未热盐法处理和使用热盐法处理乙酰化花生球蛋白的疏水性。FIG. 4 shows the hydrophobicity of acetylated arachidone without hot salt treatment and with hot salt treatment according to the present invention.
具体实施方式Detailed ways
下面结合附图对本发明做进一步的详细说明,以令本领域技术人员参照说明书文字能够据以实施。The present invention will be further described in detail below in conjunction with the accompanying drawings so that those skilled in the art can implement the invention with reference to the description.
需要说明的是,下述实施方案中所述实验方法,如无特殊说明,均为常规方法,所述试剂和材料,如无特殊说明,均可从商业途径获得。It should be noted that the experimental methods described in the following embodiments are conventional methods unless otherwise specified, and the reagents and materials can be obtained from commercial channels unless otherwise specified.
<实施例1><Example 1>
提供一种蛋白基固定化脂肪酶颗粒,其制备方法包括如下步骤:Provided is a protein-based immobilized lipase particle, the preparation method of which comprises the following steps:
步骤1、称取一定质量的花生球蛋白,边搅拌边加入到一定体积去离子水中,制备得到花生蛋白分散液,并调节其pH值调节为10.5,然后加入花生球蛋白干基质量30%的丁二酸酐,期间保持pH值为10.5,并搅拌30min,然后于4℃条件下使用10kDa的透析袋透析24h,得到乙酰化花生球蛋白溶液;Step 1, weigh a certain mass of peanut globulin, add it into a certain volume of deionized water while stirring, to prepare a peanut protein dispersion, and adjust its pH value to 10.5, then add 30% of the dry weight of peanut globulin succinic anhydride, keep the pH value at 10.5, stir for 30 minutes, and then dialyze at 4°C using a 10kDa dialysis bag for 24 hours to obtain an acetylated peanut globulin solution;
乙酰化花生球蛋白溶液置于90℃恒温水浴锅中水浴热处理30min;The acetylated peanut globulin solution was placed in a constant temperature water bath at 90°C for 30 min;
采用1M盐酸调节乙酰化花生球蛋白溶液pH值为5.5,并添加700mmol的NaCl颗粒,得到乙酰化花生球蛋白颗粒。The pH value of the acetylated arachidone solution was adjusted to 5.5 with 1 M hydrochloric acid, and 700 mmol of NaCl particles were added to obtain acetylated arachidone particles.
步骤2、乙酰化花生球蛋白颗粒浓度为6.5%(以干基花生球蛋白的质量计),戊二醛试剂浓度为0.5%,戊二醛试剂添加量为400μL,Lipozyme TL(脂肪酶液)100L浓度为10.0%(采用Tris-HC缓冲液配制脂肪酶的浓度),脂肪酶液与乙酰化花生球蛋白颗粒的比例为1:4(2mL:8mL),乙酰化花生球蛋白颗粒、戊二醛试剂、脂肪酶液混合,于室温下以300rpm搅拌交联反应1.0h;Step 2, the concentration of acetylated peanut globulin particles is 6.5% (based on the mass of dry peanut globulin), the concentration of glutaraldehyde reagent is 0.5%, the amount of glutaraldehyde reagent added is 400 μL, the concentration of Lipozyme TL (lipase solution) 100L is 10.0% (the concentration of lipase prepared using Tris-HC buffer), the ratio of lipase solution to acetylated peanut globulin particles is 1:4 (2mL:8mL), the acetylated peanut globulin particles, glutaraldehyde reagent, and lipase solution are mixed, and the cross-linking reaction is stirred at 300 rpm at room temperature for 1.0 h;
交联反应结束后,取反应后的混合液于120000rpm条件下离心15min,去除上清液,取沉淀,加入去离子水至离心前的体积,并于6000rpm剪切破碎1min,得到蛋白基固定化酶液。After the cross-linking reaction was completed, the reaction mixture was centrifuged at 120,000 rpm for 15 min, the supernatant was removed, the precipitate was taken, deionized water was added to the volume before centrifugation, and sheared and crushed at 6,000 rpm for 1 min to obtain a protein-based immobilized enzyme solution.
步骤3、使用步骤2制备的蛋白基固定化酶液制备Pickering乳液,具体剪切方法为:将大豆油先于10000rpm条件剪切1min,然后加入蛋白基固定化酶液,再剪切1min,得到Pickering乳液;其中,大豆油与蛋白基固定化酶液的质量为4:1。Step 3, using the protein-based immobilized enzyme solution prepared in step 2 to prepare a Pickering emulsion, the specific shearing method is: soybean oil is first sheared at 10000 rpm for 1 minute, then the protein-based immobilized enzyme solution is added, and then sheared for another 1 minute to obtain a Pickering emulsion; wherein the mass ratio of soybean oil to protein-based immobilized enzyme solution is 4:1.
Pickering乳液于45℃条件反应0~240min,测定甘油二酯含量。The Pickering emulsion was reacted at 45°C for 0 to 240 min, and the diglyceride content was determined.
本实施例中的蛋白基固定化脂肪酶颗粒的固载效率和比活性如表1所示,比活性如图1较深色单柱所示。The immobilization efficiency and specific activity of the protein-based immobilized lipase particles in this example are shown in Table 1, and the specific activity is shown in the darker single column in FIG1 .
表1蛋白基固定化脂肪酶颗粒的固载效率和比活性Table 1 Immobilization efficiency and specific activity of protein-based immobilized lipase particles
<实施例2><Example 2>
提供一种蛋白基固定化脂肪酶颗粒的制备方法及催化应用,其制备方法包括如下步骤:Provided are a preparation method and catalytic application of protein-based immobilized lipase particles, the preparation method comprising the following steps:
步骤1、同实施例1制备得到乙酰化花生球蛋白颗粒。Step 1: Prepare acetylated peanut globulin particles in the same manner as in Example 1.
步骤2、乙酰化花生球蛋白颗粒浓度为6.5%(以干基花生球蛋白的质量计),戊二醛试剂浓度为1.0%,戊二醛试剂添加量为400μL,Lipozyme TL(脂肪酶液)100L浓度为10.0%,脂肪酶液与乙酰化花生球蛋白颗的比例为1:4(2mL:8mL),乙酰化花生球蛋白颗粒、戊二醛试剂、脂肪酶液混合,于室温下以300rpm搅拌交联反应1.0h;Step 2, the concentration of acetylated peanut globulin particles is 6.5% (based on the mass of dry peanut globulin), the concentration of glutaraldehyde reagent is 1.0%, the amount of glutaraldehyde reagent added is 400 μL, the concentration of Lipozyme TL (lipase solution) 100L is 10.0%, the ratio of lipase solution to acetylated peanut globulin particles is 1:4 (2mL:8mL), the acetylated peanut globulin particles, glutaraldehyde reagent, and lipase solution are mixed, and the cross-linking reaction is stirred at 300 rpm at room temperature for 1.0h;
交联结束后,取反应后的混合液于120000rpm条件下离心15min,去除上清液,取沉淀,加入去离子水至离心前的体积,并于6000rpm剪切破碎1min,得到蛋白基固定化酶液。After the cross-linking was completed, the reaction mixture was centrifuged at 120,000 rpm for 15 min, the supernatant was removed, the precipitate was taken, deionized water was added to the volume before centrifugation, and sheared and crushed at 6,000 rpm for 1 min to obtain a protein-based immobilized enzyme solution.
步骤3、使用步骤2制备的蛋白基固定化酶液制备Pickering乳液,具体剪切方法为:将大豆油先于10000rpm条件剪切1min,然后加入蛋白基固定化酶液后再剪切1min。得到的Pickering乳液;其中,大豆油与蛋白基固定化酶液的质量为4:1。Step 3: Prepare a Pickering emulsion using the protein-based immobilized enzyme solution prepared in step 2. The specific shearing method is: first shear the soybean oil at 10,000 rpm for 1 minute, then add the protein-based immobilized enzyme solution and shear for another 1 minute. The obtained Pickering emulsion has a mass ratio of soybean oil to protein-based immobilized enzyme solution of 4:1.
Pickering乳液于45℃条件反应0~240min,测定甘油二酯含量。The Pickering emulsion was reacted at 45°C for 0 to 240 min, and the diglyceride content was determined.
本实施例中的蛋白基固定化脂肪酶颗粒的固载效率和比活性如表2所示,比活性如图1深色单柱所示。本实施例中甘油二酯含量曲线如图2深色圆点曲线所示。The immobilization efficiency and specific activity of the protein-based immobilized lipase particles in this example are shown in Table 2, and the specific activity is shown in the dark single column in Figure 1. The diglyceride content curve in this example is shown in the dark dot curve in Figure 2.
表2蛋白基固定化脂肪酶颗粒的固载效率和比活性Table 2 Immobilization efficiency and specific activity of protein-based immobilized lipase particles
<对比例1><Comparative Example 1>
提供一种游离脂肪酶催化制备甘油二酯的方法,包括如下步骤:A method for preparing diglyceride by catalysis of free lipase is provided, comprising the following steps:
步骤1、配制0.26%的Lipozyme TL 100L(脂肪酶液)。Step 1: Prepare 0.26% Lipozyme TL 100L (lipase solution).
步骤2、使用上述游离脂肪酶液,与大豆油混合剪切,制备两相催化反应体系。剪切方法为,将大豆油先于10000rpm条件剪切1min,加入游离脂肪酶液后再剪切1min,得到的两相体系;Step 2: Use the above-mentioned free lipase solution and mix with soybean oil for shearing to prepare a two-phase catalytic reaction system. The shearing method is to shear the soybean oil at 10,000 rpm for 1 minute, add the free lipase solution and then shear for another 1 minute to obtain a two-phase system;
两相体系于45℃条件反应0~240min,测定甘油二酯含量。The two-phase system was reacted at 45°C for 0 to 240 min, and the diglyceride content was determined.
本对比例中的游离脂肪酶比活性如图1浅色单柱所示,甘油二酯含量曲线如图2浅色方块曲线所示。The specific activity of free lipase in this comparative example is shown in the light-colored single column in FIG1 , and the diacylglycerol content curve is shown in the light-colored square curve in FIG2 .
<对比例2><Comparative Example 2>
乙酰化后的花生球蛋白,其中的氨基结合酰基,正电荷被消除,电子云密度增加,分子所带负电荷增加,等电点左移,在此pH条件下改性颗粒带负电,彼此之间相互排斥,未发生聚集沉淀,使得花生球蛋白在pH5.5时仍能保持均匀分散的状态,而不会发生沉降,有利于后续的脂肪酶固定化和稳定乳液。After acetylation, the amino group of peanut globulin is combined with the acyl group, the positive charge is eliminated, the electron cloud density increases, the negative charge of the molecule increases, and the isoelectric point shifts to the left. Under this pH condition, the modified particles are negatively charged and repel each other without aggregation and precipitation. Therefore, the peanut globulin can still maintain a uniform dispersion state at pH 5.5 without sedimentation, which is beneficial to the subsequent lipase immobilization and emulsion stabilization.
采用未乙酰化的花生球蛋白,pH5.5时的分散状态如图3所示。同时,乙酰化后的蛋白表面疏水性(Ho)提高(如图4),更倾向于稳定W/O型Pickering乳液。The dispersion state of unacetylated peanut globulin at pH 5.5 is shown in Figure 3. At the same time, the surface hydrophobicity (Ho) of the acetylated protein is improved (as shown in Figure 4), which is more inclined to stabilize the W/O Pickering emulsion.
<对比例3><Comparative Example 3>
其它与实施例1相同,只是没有进行热处理、盐处理。The other steps are the same as those in Example 1, except that no heat treatment or salt treatment is performed.
实验中使用热盐法制备乙酰化花生球蛋白颗粒,经过热处理后,乙酰化花生球蛋白分子内的疏水基团暴露出来,蛋白的疏水作用增强,Ho显著提高(如图4);同时经过盐处理后,由于静电屏蔽作用,蛋白分子间的静电斥力减小,蛋白质发生轻微“盐析”,得到乙酰化花生球蛋白颗粒。In the experiment, the hot salt method was used to prepare acetylated peanut globulin particles. After heat treatment, the hydrophobic groups in the acetylated peanut globulin molecules were exposed, the hydrophobic effect of the protein was enhanced, and Ho was significantly improved (as shown in Figure 4); at the same time, after salt treatment, due to the electrostatic shielding effect, the electrostatic repulsion between protein molecules was reduced, and the protein underwent slight "salting out", resulting in acetylated peanut globulin particles.
尽管本发明的实施方案已公开如上,但其并不仅仅限于说明书和实施方式中所列运用,它完全可以被适用于各种适合本发明的领域,对于熟悉本领域的人员而言,可容易地实现另外的修改,因此在不背离权利要求及等同范围所限定的一般概念下,本发明并不限于特定的细节和这里示出与描述的图例。Although the embodiments of the present invention have been disclosed as above, they are not limited to the applications listed in the specification and the implementation modes, and they can be fully applied to various fields suitable for the present invention. For those familiar with the art, additional modifications can be easily implemented. Therefore, without departing from the general concept defined by the claims and the scope of equivalents, the present invention is not limited to the specific details and the illustrations shown and described herein.
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