CN1749279A - Preparation method and application of microwave acidolysis and esterification modified composite modified starch - Google Patents
Preparation method and application of microwave acidolysis and esterification modified composite modified starch Download PDFInfo
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Abstract
Description
技术领域technical field
在微波辐射条件下,一种同时进行酸解与酯化改性复合变性淀粉的制备方法和应用,属于变性淀粉技术领域。The invention relates to a preparation method and application of compound modified starch which is simultaneously modified by acid hydrolysis and esterification under the condition of microwave radiation, and belongs to the technical field of modified starch.
技术背景technical background
脂肪酸淀粉酯是由淀粉及其衍生物与脂肪酸、脂肪酸甲酯、脂肪酸酰氯或脂肪酸酐反应得到的酯化产品。由于疏水性有机碳链的引入,淀粉的疏水性增加,使之具备了亲水和亲油的双亲性质,具有乳化性,可用在食品、医药、日用化学品等领域。高取代度的脂肪酸淀粉酯因具有较高的乳化能力,可用于微胶囊化产品获得高的包埋率,代替昂贵的阿拉伯胶;低取代度的脂肪酸淀粉酯可用于脂肪替代品。有关有机溶剂法制备脂肪酸淀粉酯,国外已有不少报道。只有Saiyavit Varavinit等用干法合成了西米和木薯的硬脂酸淀粉酯。关于微波法对淀粉同时进行酸解与酯化反应制备复合变性淀粉的工艺迄今还未见报道。Fatty acid starch ester is an esterification product obtained by reacting starch and its derivatives with fatty acid, fatty acid methyl ester, fatty acid chloride or fatty acid anhydride. Due to the introduction of hydrophobic organic carbon chains, the hydrophobicity of starch increases, which makes it possess the amphiphilic properties of hydrophilic and lipophilic, and has emulsifying properties, which can be used in food, medicine, daily chemicals and other fields. Fatty acid starch esters with a high degree of substitution have high emulsifying ability and can be used in microencapsulated products to obtain a high embedding rate, replacing expensive gum arabic; fatty acid starch esters with a low degree of substitution can be used as fat substitutes. There have been many reports abroad about the preparation of fatty acid starch esters by the organic solvent method. Only Saiyavit Varavinit etc. synthesized starch stearate of sago and cassava by dry method. There is no report about the process of preparing compound modified starch by simultaneous acid hydrolysis and esterification of starch by microwave method.
发明内容Contents of the invention
本发明的目的是:提供一种在微波辐射条件下,脂肪酸和淀粉直接酯化合成脂肪酸淀粉酯的制备方法。由于本反应中采用酸作为催化剂,反应过程中会使淀粉酸解,所以制备工艺中酸解与酯化反应同时进行,产品具有众多优异特性。本反应采用热无水乙醇溶解脂肪酸,和淀粉充分混合,反应过程中乙醇会完全挥发,所以本发明属于干法制备。The purpose of the present invention is: to provide a kind of preparation method of fatty acid starch ester by direct esterification of fatty acid and starch under the condition of microwave radiation. Since acid is used as a catalyst in this reaction, the starch will be acidolyzed during the reaction process, so the acidolysis and esterification reactions are carried out simultaneously in the preparation process, and the product has many excellent characteristics. In this reaction, hot absolute ethanol is used to dissolve the fatty acid, and it is fully mixed with the starch. During the reaction, the ethanol will completely volatilize, so the present invention belongs to dry preparation.
本发明的技术方案:一种酸解与酯化复合变性淀粉是采用微波(常压或真空)方法对淀粉同时进行酸解与酯化变性的制备方法制得,使产品同时具有酸解与酯化变性淀粉的特性。The technical scheme of the present invention: a kind of acidolysis and esterification compound modified starch is prepared by adopting microwave (atmospheric pressure or vacuum) method to carry out the preparation method of acidolysis and esterification denaturation at the same time, so that the product has both acidolysis and esterification properties of modified starches.
所述的同时进行酸解与酯化改性复合变性淀粉的制备方法,是以淀粉为原料,将酯化剂溶于热无水乙醇溶剂中,加入一定量的酸,并加入适量水调节反应体系水分含量,缓慢加入到淀粉中,不断搅拌,得到的浆体在微波辐射(常压或真空)下同时进行酸解与酯化反应,制得酸解与酯化复合变性淀粉。The method for preparing the compound modified starch with acid hydrolysis and esterification modification at the same time is to use starch as raw material, dissolve the esterification agent in hot absolute ethanol solvent, add a certain amount of acid, and add an appropriate amount of water to adjust the reaction The water content of the system is slowly added to the starch and stirred continuously, and the obtained slurry is subjected to acidolysis and esterification reactions under microwave radiation (atmospheric pressure or vacuum) at the same time to obtain acidolysis and esterification compound modified starch.
淀粉原料可以是玉米淀粉、小麦淀粉、薯类淀粉等。The starch raw material can be corn starch, wheat starch, potato starch and the like.
酯化变性所用的酯化剂可以是高级脂肪酸,如硬脂酸、月桂酸、肉豆蔻酸、棕榈酸、油酸、亚油酸、花生酸等,溶解酯化剂所用的溶剂可以是无水乙醇。The esterification agent used for esterification denaturation can be a higher fatty acid, such as stearic acid, lauric acid, myristic acid, palmitic acid, oleic acid, linoleic acid, arachidic acid, etc., and the solvent used for dissolving the esterification agent can be anhydrous ethanol.
酸解变性所用的酸解试剂为盐酸、醋酸或甲酸等易挥发性酸。Acid hydrolysis reagents used for denaturation are volatile acids such as hydrochloric acid, acetic acid or formic acid.
微波反应可以是常压、真空等条件下进行。The microwave reaction can be carried out under conditions such as normal pressure and vacuum.
制备工艺的配方:Recipe for the preparation process:
淀粉,干基质量计 100Starch, dry basis mass 100
酯化剂,以质量计 2~4Esterifying agent, by mass 2~4
无水乙醇,以体积计 80~120Absolute ethanol, by volume 80~120
酸,以质量计 0.05~0.20Acid, by mass 0.05~0.20
水,以体积计 0~40Water, by volume 0~40
在实验室的具体配方为:The specific formula in the laboratory is:
淀粉(干基计) 100gStarch (dry basis) 100g
酯化剂 2~4gEsterifying agent 2~4g
无水乙醇 80~120mlAbsolute ethanol 80~120ml
酸 0.05~0.20gAcid 0.05~0.20g
水 0~40mlWater 0~40ml
反应工艺条件:酯化剂先溶于热无水乙醇后,加入催化剂酸,加或不加水调节反应体系至水分质量分数为14%~42%,然后将酯化剂溶剂缓慢加入到淀粉中,并不断搅拌,得到均匀混合物反应浆体。微波反应的功率为700~1200W,反应时间为3~10min,常压采用30s间歇式加热,并快速搅拌,或真空采用连续加热,真空度0.08~0.1Mpa。酯化剂溶剂的缓慢加入是在不断搅拌下进行。微波反应时反应浆料的水分质量分数控制在14%~30%为更佳。Reaction process conditions: after the esterification agent is first dissolved in hot absolute ethanol, a catalyst acid is added, and water is added or not to adjust the reaction system until the water mass fraction is 14% to 42%, and then the esterification agent solvent is slowly added to the starch, And keep stirring to obtain a homogeneous mixture reaction slurry. The power of the microwave reaction is 700-1200W, and the reaction time is 3-10min. It adopts 30s intermittent heating under normal pressure and rapid stirring, or adopts continuous heating under vacuum, and the vacuum degree is 0.08-0.1Mpa. The slow addition of the esterifying agent solvent is carried out under constant stirring. It is better to control the water mass fraction of the reaction slurry at 14% to 30% during the microwave reaction.
所述的在微波条件下同时进行酸解与酯化改性复合变性淀粉的应用,主要用于食品工业中的乳化剂,用于目前的乳化香精、微胶囊化产品等众多产品,也可作为低脂奶油中的脂肪替代物。The application of acidolysis and esterification modified composite modified starch under microwave conditions is mainly used as an emulsifier in the food industry, used in many products such as emulsified flavors and microencapsulated products, and can also be used as Fat substitute in low-fat cream.
本发明的有益效果:本发明针对微波新技术在变性淀粉中的应用和食品加工对变性淀粉的特殊性要求,有针对性地开发了一种变性淀粉的新工艺和新产品。利用微波干法反应器对淀粉同时进行酸解和酯化变性,特别是制备了一种具有膳食纤维功能的脂肪酸淀粉酯,在本发明的制备工艺中淀粉的酸解与酯化反应同时进行。产品具有众多优异特性,淀粉中由于脂肪酸基团的引入,使之具有亲水和亲油双亲基团,因而有一定的乳化性能,再加上高温酸解作用,降低了淀粉的粘度。由于分子结构的变化形成了难消化的糊精(膳食纤维功能),具有一定的保健功效。所得的产品可以应用于乳化香精、作为微胶囊壁材用于微胶囊化产品等众多产品,可替代目前价格较高的阿拉伯胶、藻酸丙二醇酯等,还可用于取代植脂奶油中的部分油脂,生产低脂植脂奶油,冰淇淋、色拉酱等。脂肪酸淀粉酯的加入减少了配方中的乳化剂、稳定剂的用量,从而降低了成本,有良好的经济效益。此工艺将酸解和酯化二种变性方法有机的结合在一起,并利用微波干法反应器进行反应,反应时间明显低于普通干法反应,反应效率明显提高,易于实施,并且环境污染小。Beneficial effects of the present invention: The present invention aims at the application of microwave technology in modified starch and the special requirements of food processing for modified starch, and develops a new process and new product of modified starch in a targeted manner. A microwave dry method reactor is used to carry out acidolysis and esterification denaturation of starch simultaneously, especially to prepare a fatty acid starch ester with dietary fiber function. In the preparation process of the invention, the acidolysis and esterification reactions of starch are carried out simultaneously. The product has many excellent characteristics. Due to the introduction of fatty acid groups in starch, it has hydrophilic and lipophilic amphiphilic groups, so it has certain emulsifying properties, and high temperature acid hydrolysis reduces the viscosity of starch. Due to the change of molecular structure, indigestible dextrin (dietary fiber function) is formed, which has certain health care effects. The obtained product can be used in many products such as emulsified essence, as microcapsule wall material for microencapsulated products, and can replace the current high-priced gum arabic, propylene glycol alginate, etc., and can also be used to replace part of non-dairy cream Grease, low-fat non-dairy cream, ice cream, salad dressing, etc. The addition of fatty acid starch ester reduces the amount of emulsifier and stabilizer in the formula, thereby reducing the cost and having good economic benefits. This process organically combines the two denaturation methods of acidolysis and esterification, and uses a microwave dry reactor for the reaction. The reaction time is significantly lower than that of the ordinary dry method, the reaction efficiency is significantly improved, it is easy to implement, and the environmental pollution is small. .
附图说明Description of drawings
图1微波条件下,同时进行酸解和酯化改性复合变性淀粉制备工艺示意图。Fig. 1 is a schematic diagram of the preparation process of simultaneous acid hydrolysis and esterification modified composite modified starch under microwave conditions.
具体实施方式Detailed ways
实施例1Example 1
称取2g硬脂酸,溶于80ml 70℃无水乙醇中,再加入盐酸0.05g,不加水,维持温度70℃,然后缓慢加入100g淀粉(干基)中,并不断搅拌,得到均匀混合物,将此混合物装入容器置于700W的微波炉中反应,采用30s间歇式加热,并快速搅拌,微波辐射时间为3min,冷却,粉碎,即得成品硬酯酸淀粉酯。微波炉为南京杰全微波设备有限公司生产的NJL07-3型实验用微波炉,下同。Weigh 2g of stearic acid, dissolve it in 80ml of 70°C dehydrated ethanol, add 0.05g of hydrochloric acid, keep the temperature at 70°C without adding water, then slowly add 100g of starch (dry basis), and keep stirring to obtain a uniform mixture. Put the mixture into a container and place it in a 700W microwave oven for reaction, heat intermittently for 30s, stir rapidly, and irradiate with microwaves for 3 minutes, cool and pulverize to obtain the finished starch stearate. The microwave oven is the NJL07-3 experimental microwave oven produced by Nanjing Jiequan Microwave Equipment Co., Ltd., the same below.
以硬脂酸与淀粉反应制备硬脂酯淀粉酯,采用普通常压干法,微波常压干法和微波真空干法三种不同方法以制备硬脂酸淀粉酯的产品性能如表1所示。反应效率为实际取代度与理论取代度之比,从表中可以看出微波法制备产品的反应时间明显低于普通干法反应,反应效率明显提高,乳化性有所改善。Prepare stearyl starch ester with stearic acid and starch reaction, adopt common pressure dry method, microwave normal pressure dry method and microwave vacuum dry method three different methods to prepare the product performance of stearic acid starch ester as shown in table 1 . The reaction efficiency is the ratio of the actual degree of substitution to the theoretical degree of substitution. It can be seen from the table that the reaction time of the product prepared by the microwave method is significantly lower than that of the ordinary dry method, the reaction efficiency is obviously improved, and the emulsification property is improved.
表1:微波干法(常压或真空)与普通干法反应比较
注:方法1为常压下干法制备。反应条件为:初始水分质量分数22%,温度150℃,硬脂酸质量分数3%(以淀粉干基计),反应时间4h,HCl 0.08%(以淀粉干基计)Note: Method 1 is dry preparation under normal pressure. The reaction conditions are: initial moisture mass fraction 22%, temperature 150°C, stearic acid mass fraction 3% (calculated on starch dry basis), reaction time 4h, HCl 0.08% (calculated on starch dry basis)
方法2为常压下微波干法制备。反应条件为:反应前水分含量为28%,硬脂酸质量分数3%(以淀粉干基计),微波反应功率800W,反应时间5min,HCl0.12%(以淀粉干基计)Method 2 is microwave dry preparation under normal pressure. The reaction conditions are: the moisture content before the reaction is 28%, the mass fraction of stearic acid is 3% (calculated on the dry basis of starch), the microwave reaction power is 800W, the reaction time is 5min, and HCl0.12% (calculated on the dry basis of starch)
方法3为真空下微波干法制备。反应条件为:反应前水分含量为28%,硬脂酸质量分数3%(以淀粉干基计),微波反应功率700W,反应时间10min,HCl 0.12%(以淀粉干基计)Method 3 is microwave dry preparation under vacuum. The reaction conditions are: the moisture content before the reaction is 28%, the mass fraction of stearic acid is 3% (calculated on the dry basis of starch), the microwave reaction power is 700W, the reaction time is 10min, and HCl 0.12% (calculated on the dry basis of starch)
实施例2Example 2
称取4g月桂酸,溶于120ml 70℃无水乙醇中,再加入醋酸0.2g,同时加入40ml水维持温度70℃,然后缓慢加入到100g淀粉(干基)中,并不断搅拌,得到均匀混合物,将此混合物装入容器置于1200W的微波炉中抽真空反应,微波辐射时间为10min,冷却,粉碎,即得成品月桂酸淀粉酯。Weigh 4g of lauric acid, dissolve it in 120ml of 70°C absolute ethanol, add 0.2g of acetic acid, and at the same time add 40ml of water to maintain the temperature at 70°C, then slowly add it to 100g of starch (dry basis), and keep stirring to obtain a homogeneous mixture , Put the mixture into a container and place it in a 1200W microwave oven to evacuate it for reaction. The microwave radiation time is 10 minutes. After cooling, it is pulverized to obtain the finished starch laurate ester.
实施例3Example 3
亚油酸作为酯化剂,其余配方和操作条件同实施例1或实施例2,制得成品亚油酸淀粉酯。Linoleic acid is used as esterifying agent, and all the other prescriptions and operating conditions are the same as embodiment 1 or embodiment 2, and make finished product linoleic acid starch ester.
实施例4Example 4
肉豆蔻酸作为酯化剂,其余配方和操作条件同实施例1或实施例2,制得成品肉豆蔻酸淀粉酯。Myristic acid is used as esterifying agent, and all the other prescriptions and operating conditions are with embodiment 1 or embodiment 2, make finished product starch myristate.
实施例5Example 5
棕榈酸作为酯化剂,其余配方和操作条件同实施例1或实施例2,制得成品棕榈酸淀粉酯。Palmitic acid is used as esterifying agent, and all the other prescriptions and operating conditions are with embodiment 1 or embodiment 2, make finished product palmitic acid starch ester.
实施例6Example 6
油酸作为酯化剂,其余配方和操作条件同实施例1或实施例2,制得成品油酸淀粉酯。Oleic acid is used as esterifying agent, and all the other prescriptions and operating conditions are with embodiment 1 or embodiment 2, make finished product oleic acid starch ester.
实施例7Example 7
花生酸作为酯化剂,其余配方和操作条件同实施例1或实施例2,制得成品花生酸淀粉酯。Arachidic acid is used as an esterifying agent, and all the other recipes and operating conditions are the same as in Example 1 or Example 2 to obtain the finished product arachidonic acid starch ester.
实施例8Example 8
工业化生产,淀粉投料量18~400kg/h,微波炉为南京杰全微波设备有限公司的NJ系列隧道式微波炉,或NJZ系列真空微波炉,其余配方比列和操作条件同实施例1或实施例2,制得成品脂肪酸淀粉酯,原料淀粉为玉米淀粉、小麦淀粉或薯类淀粉。Industrialized production, the starch feeding amount is 18-400kg/h, the microwave oven is the NJ series tunnel microwave oven of Nanjing Jiequan Microwave Equipment Co., Ltd., or the NJZ series vacuum microwave oven, and the other formula ratios and operating conditions are the same as in Example 1 or Example 2. The finished fatty acid starch ester is obtained, and the raw material starch is corn starch, wheat starch or potato starch.
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Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1425624A (en) * | 1973-08-10 | 1976-02-18 | Scholten Honig Research Bfv | Chemical modification of starches |
| CH658663A5 (en) * | 1984-02-01 | 1986-11-28 | Nestle Sa | PROCESS FOR THE PREPARATION OF A STARCH DISPERSIBLE IN BOILING WATER. |
| CN1050024A (en) * | 1989-09-09 | 1991-03-20 | 吉林大学 | Microwave dry process of preparation of cationic starch |
| FR2789995B1 (en) * | 1999-02-23 | 2001-04-27 | Toulouse Inst Nat Polytech | PROCESS FOR GIVING A HYDROPHOBIC CHARACTER TO A CELLULOSIC OR AMYLACEOUS SOLID MATERIAL |
| FI116142B (en) * | 2003-09-11 | 2005-09-30 | Kemira Oyj | The esterification process |
| CN1273490C (en) * | 2003-12-26 | 2006-09-06 | 江南大学 | Simultaneously acid hydrolysis and esterizing modified composite modified starch and its preparing method and use |
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2005
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