CN113229368B - A kind of macadamia nut meal processing method and its protein beverage - Google Patents
A kind of macadamia nut meal processing method and its protein beverage Download PDFInfo
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Classifications
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING OR TREATMENT THEREOF
- A23C11/00—Milk substitutes, e.g. coffee whitener compositions
- A23C11/02—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins
- A23C11/10—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing or not lactose but no other milk components as source of fats, carbohydrates or proteins
- A23C11/103—Milk substitutes, e.g. coffee whitener compositions containing at least one non-milk component as source of fats or proteins containing or not lactose but no other milk components as source of fats, carbohydrates or proteins containing only proteins from pulses, oilseeds or nuts, e.g. nut milk
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/87—Re-use of by-products of food processing for fodder production
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
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- Non-Alcoholic Beverages (AREA)
Abstract
本发明涉及自然资源综合利用开发技术领域,具体涉及一种澳洲坚果果粕加工方法及其蛋白饮料。一种澳洲坚果果粕加工方法,包括以下依次进行的步骤:S1浸泡果粕粉;S2使用木瓜蛋白酶酶解处理浸泡后的果粕粉,然后过滤取上清,获得酶解液;浓缩所述酶解液获得浓缩液;S3在浓缩液中加入助剂,经均质处理后获得蛋白饮料。本方案可以解决由澳洲坚果的果粕加工而成的蛋白饮料的感官和质量欠佳的技术问题。本方案将榨油后废弃的果粕进行精深加工,并转化成为富含蛋白的食品,可以实现澳洲坚果资源的综合利用。The invention relates to the technical field of comprehensive utilization and development of natural resources, in particular to a processing method for macadamia nut meal and a protein beverage thereof. A method for processing macadamia nut meal, comprising the following steps in sequence: S1 soaking the fruit meal powder; S2 enzymatically treating the soaked fruit meal powder with papain, and then filtering the supernatant to obtain an enzymatic solution; concentrating the Concentrate is obtained from enzymatic hydrolysis; S3 adds additives to the concentrate to obtain protein beverage after homogenization. The solution can solve the technical problem of poor sensory and quality of the protein drink processed from macadamia nut pulp. In this scheme, the discarded fruit meal after oil extraction is intensively processed and transformed into protein-rich food, which can realize the comprehensive utilization of macadamia nut resources.
Description
技术领域technical field
本发明涉及自然资源综合利用开发技术领域,具体涉及一种澳洲坚果果粕加工方法及其蛋白饮料。The invention relates to the technical field of comprehensive utilization and development of natural resources, in particular to a processing method for macadamia nut meal and a protein beverage thereof.
背景技术Background technique
澳洲坚果(Macadamia integrifolia)种子(果仁),含不饱和脂肪油达60%—80%,蛋白质和碳水化合物各约9%,并含有相当丰富的钙、磷、铁、氨基酸和维生素Bl、B2等,澳洲坚果仁内的蛋白质共含有17种氨基酸,其中10种是人体内不能合成而必须由食物供给的氨基酸。可见,澳洲坚果是一种富含热能、不含胆固醇、又有多种人体生长所必需营养物质的营养性食品。澳洲坚果果仁榨油后剩下的果粕中富含丰富的蛋白质,如果将澳洲坚果饼粕中富含的蛋白质进行深加工,通过技术改造,将其转化为富含蛋白的食品,将废弃的果粕重新加工再利用,可以极大地提升澳洲坚果的经济价值。例如,将澳洲坚果的果粕开发成为蛋白饮料,这是实现资源综合利用的有效途径之一。但是,果粕中的成分较为复杂,会影响由其制备的饮料的性状。将其制备成乳液状态的饮料后,在储存、加工和运输的过程中,会出现沉淀和脂肪析出的现象,严重影响产品的感官和质量。Macadamia integrifolia seeds (kernels) contain 60%-80% unsaturated fat oil, about 9% protein and carbohydrates, and are quite rich in calcium, phosphorus, iron, amino acids and vitamins B1 and B2 Etc., the protein in the macadamia nut contains 17 kinds of amino acids in total, 10 of which are amino acids that cannot be synthesized in the human body and must be supplied by food. It can be seen that macadamia nuts are a nutritious food rich in heat energy, cholesterol-free, and a variety of nutrients necessary for human growth. Macadamia nut kernels are rich in protein after oil extraction. If the protein rich in macadamia nut cake is further processed and transformed into protein-rich food through technological transformation, the discarded The reprocessing and reuse of fruit pulp can greatly increase the economic value of macadamia nuts. For example, developing the pulp of macadamia nuts into a protein drink is one of the effective ways to realize the comprehensive utilization of resources. However, the components in fruit meal are relatively complex, which will affect the properties of beverages prepared from it. After it is prepared into a beverage in an emulsion state, precipitation and fat precipitation will occur during storage, processing and transportation, which will seriously affect the sensory and quality of the product.
发明内容Contents of the invention
本发明意在提供一种澳洲坚果果粕加工方法,以解决由澳洲坚果的果粕加工而成的蛋白饮料的感官和质量欠佳的技术问题。The invention intends to provide a processing method of macadamia nut pulp to solve the technical problem of poor sensory and quality of protein drinks processed from macadamia nut pulp.
为达到上述目的,本发明采用如下技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种澳洲坚果果粕加工方法,包括以下依次进行的步骤:A method for processing macadamia nut pulp, comprising the following steps in sequence:
S1浸泡果粕粉;S2使用木瓜蛋白酶酶解处理浸泡后的果粕粉,然后过滤取上清,获得酶解液;浓缩所述酶解液获得浓缩液;S3在浓缩液中加入助剂,经均质处理后获得蛋白饮料。S1 soaking the fruit meal powder; S2 enzymatically treating the soaked fruit meal powder with papain, and then filtering the supernatant to obtain an enzymolysis solution; concentrating the enzymolysis solution to obtain a concentrate; S3 adding additives to the concentrate, A protein drink is obtained after homogenization.
本方案的原理及优点是:首先将果粕粉浸泡,使其吸水膨胀,便于后续的酶解反应的进行。然后使用木瓜蛋白酶酶解处理浸泡后膨胀的果粕粉,木瓜蛋白酶将果粕粉中的蛋白质分解成小分子蛋白或者多肽。这部分小分子蛋白或者多肽分散到水溶液体系中,最后富集在浓缩液中。在浓缩液中加入助剂,使得小分子蛋白或者多肽充分悬浮和分散在水中,获得稳定性好、蛋白不易沉淀析出、油脂不易析出分层的蛋白饮料。克服了现有技术的由澳洲坚果果粕制备的蛋白饮料,由于沉淀和脂肪析出的现象,导致的产品的感官和质量不佳的问题。The principle and advantages of this scheme are: firstly soak the fruit meal powder to make it absorb water and expand, which is convenient for the subsequent enzymatic hydrolysis reaction. Then papain is used to enzymatically treat the soaked and expanded fruit meal powder, and papain decomposes the protein in the fruit meal powder into small molecular proteins or polypeptides. These small molecular proteins or polypeptides are dispersed into the aqueous solution system, and finally enriched in the concentrated solution. Auxiliaries are added to the concentrate to fully suspend and disperse small molecular proteins or polypeptides in water, and obtain protein beverages with good stability, difficult protein precipitation and oil separation. The invention overcomes the problem of poor sensory and quality of the product caused by precipitation and fat precipitation in the protein drink prepared from macadamia nut pulp in the prior art.
在悬浊液和乳浊液体系中,蛋白质和油脂是引起体系不稳定的重要因素之一。在水环境中,蛋白质和油脂等大分子通过布朗运动、重力和界面张力等作用、电荷之间的相互作用,颗粒之间非常容易聚集成更大的颗粒,导致油脂和蛋白质分别出现上浮和沉淀的情况。虽然加入一些乳化剂和稳定剂等,可以缓解上述现象,但是,将澳洲坚果的果粕开发成为液体状的食品,尚属尝试阶段。对其果粕中的影响系统稳定性的物质成分尚不是非常清楚,这就给相关食品的研究造成了障碍。发明人从果粕的加工工艺路线以及助剂的使用等多个方面进行研究,发现了酶解处理过程非常关键。使用木瓜蛋白酶对浸泡后的果粕粉进行酶解处理,可将大分子的蛋白质分解成为合适大小和分子构型的小分子蛋白或者多肽,这些小分子蛋白或者多肽可在悬浊液环境中将其疏水基团充分暴露,有利于他们与增稠剂或表面活性剂等助剂相结合,可以更好地维持悬浊液的状态。综上所述,采用木瓜蛋白酶酶解结合加入助剂的方式,可以有效防止蛋白质类物质沉淀,以及有效防止油脂类物质析出上浮,保证了蛋白饮料在较长时间内维持良好的感官,提升蛋白饮料的品质。In suspension and emulsion systems, protein and oil are one of the important factors that cause system instability. In a water environment, macromolecules such as proteins and oils are easily aggregated into larger particles through Brownian motion, gravity, interfacial tension, and the interaction between charges, causing oils and proteins to float and precipitate respectively. Case. Although the above phenomenon can be alleviated by adding some emulsifiers and stabilizers, it is still in the trial stage to develop the pulp of macadamia nuts into a liquid food. The substances in the fruit meal that affect the stability of the system are not very clear, which has caused obstacles to the research of related foods. The inventor conducted research on the processing route of fruit meal and the use of additives, and found that the enzymatic treatment process is very critical. Use papain to enzymatically hydrolyze the soaked fruit meal powder, which can decompose macromolecular proteins into small molecular proteins or polypeptides of suitable size and molecular configuration. These small molecular proteins or polypeptides can be decomposed in the suspension environment Its hydrophobic groups are fully exposed, which is conducive to their combination with additives such as thickeners or surfactants, and can better maintain the state of the suspension. In summary, the combination of papain enzymatic hydrolysis and the addition of additives can effectively prevent the precipitation of protein substances, and effectively prevent the precipitation and floating of oil substances, ensuring that the protein drink maintains a good sense for a long time and improves the protein content. The quality of the drink.
在本方案中,果粕粉来源为:对澳洲坚果的果仁进行油脂压榨(常规冷榨工艺)后,经过干燥处理获得固体状物质,将固体物质粉碎处理,获得果粕粉。这种果粕粉中含有大量的蛋白质(质量分数可达25%以上)和油脂,可以用于蛋白饮料的加工。In this solution, the source of the fruit meal powder is: after oil pressing (conventional cold pressing process) of macadamia nut kernels, the solid matter is obtained through drying treatment, and the solid matter is crushed to obtain the fruit meal powder. The fruit meal powder contains a large amount of protein (mass fraction can reach more than 25%) and oil, and can be used for the processing of protein drinks.
进一步,在S2中,木瓜蛋白酶和果粕粉的质量比为0.01-0.04:1。Further, in S2, the mass ratio of papain to fruit meal powder is 0.01-0.04:1.
进一步,在S2中,酶解处理的条件为:pH值6.0、温度68℃和时长8h。Further, in S2, the conditions of the enzymatic hydrolysis treatment are: pH value 6.0, temperature 68° C. and duration 8 hours.
采用上述酶解处理的条件和木瓜蛋白酶的用量可以使得果粕粉中的蛋白质充分分解成为小分子,这些小分子在蛋白饮料体系中可与助剂充分结合,形成稳定悬浮和分散的胶粒,提高蛋白饮料的长期贮存的稳定性。Using the above enzymatic hydrolysis treatment conditions and the dosage of papain can fully decompose the protein in the fruit meal powder into small molecules, and these small molecules can be fully combined with additives in the protein beverage system to form stable suspended and dispersed colloidal particles. Improve the long-term storage stability of protein drinks.
进一步,在S3中,所述助剂包括吐温60、黄原胶和蔗糖。Further, in S3, the auxiliary agent includes Tween 60, xanthan gum and sucrose.
助剂类型的选择是稳定蛋白饮料中的油脂和蛋白质的关键,发明人对不同类型的表面活性剂和稳定剂等进行了测试,发现使用黄原胶和吐温60的效果最佳。他们非常适合于维持悬浊液/乳浊液的系统稳定。从澳洲坚果的果粕中提取出蛋白质、脂肪和碳水化合物等之后,卡拉胶、吐温60以及蔗糖能够使得上述物质以胶粒的形式,较为稳定地分散和悬浮在液体环境中。发明人尝试使用阿拉伯胶、卡拉胶等物质替换黄原胶,也尝试使用司盘40等表面活性剂替换吐温60,均不能获得理想效果。这说明了吐温60、黄原胶和蔗糖非常适合于稳定由澳洲坚果果粕制备的蛋白饮料。The selection of auxiliary agent type is the key to stabilizing oil and protein in protein drinks. The inventor has tested different types of surfactants and stabilizers, and found that xanthan gum and Tween 60 have the best effect. They are very suitable for maintaining the system stability of suspensions/emulsions. After extracting protein, fat and carbohydrates from the pulp of macadamia nuts, carrageenan, Tween 60 and sucrose can make the above substances dispersed and suspended in the liquid environment in the form of colloidal particles more stably. The inventor tried to replace xanthan gum with substances such as gum arabic and carrageenan, and also tried to use surfactants such as Span 40 to replace Tween 60, but the desired effect could not be obtained. This illustrates that Tween 60, xanthan gum and sucrose are well suited for stabilizing protein drinks prepared from macadamia pulp.
进一步,吐温60、黄原胶和蔗糖的质量分数分别为0.05%-0.3%、0.1%-0.4%和8%-12%。采用上述质量分数范围的吐温60、黄原胶和蔗糖,均可以获得体系稳定性理想的蛋白饮料。Further, the mass fractions of Tween 60, xanthan gum and sucrose are respectively 0.05%-0.3%, 0.1%-0.4% and 8%-12%. Using Tween 60, xanthan gum and sucrose in the above mass fraction ranges can all obtain protein drinks with ideal system stability.
进一步,在S3中,均质处理的温度为60℃,压强为30Mpa;均质处理重复两次。均质处理时影响产品稳定性的重要因素,采用本方案的压力和温度条件的均质效果理想,获得的蛋白饮料的体系稳定性佳Further, in S3, the temperature of the homogenization treatment is 60° C., and the pressure is 30 MPa; the homogenization treatment is repeated twice. An important factor affecting product stability during homogenization treatment. The homogenization effect of the pressure and temperature conditions of this scheme is ideal, and the obtained protein drink has good system stability
进一步,在S1中,使用碳酸氢钠水溶液浸泡果粕粉。碳酸氢钠可以抑制脂肪氧化酶等的活性,避免果粕粉在浸泡过程中营养成分被分解破坏,也避免了果粕粉在这些酶的作用下出现颜色变化等情况,起到护色作用。本方案进一步保证了获得的蛋白饮料的颜色不会变得过深,提升蛋白饮料的感官品质。Further, in S1, the fruit meal powder is soaked in an aqueous solution of sodium bicarbonate. Sodium bicarbonate can inhibit the activity of lipoxygenase, etc., prevent the nutritional components of the fruit meal powder from being decomposed and destroyed during the soaking process, and also avoid the color change of the fruit meal powder under the action of these enzymes, and play a role in color protection. This solution further ensures that the color of the obtained protein drink will not become too dark, and improves the sensory quality of the protein drink.
进一步,所述碳酸氢钠水溶液中碳酸氢钠的质量分数为0.5%,使用碳酸氢钠水溶液浸泡果粕粉的时长为4h。上述浓度的碳酸氢钠在起到护色作用的同时不会对果粕粉的营养成分产生破坏。上述浸泡时长可以保证果粕粉充分吸水膨胀,便于后续酶解反应的进行。Further, the mass fraction of sodium bicarbonate in the sodium bicarbonate aqueous solution is 0.5%, and the duration of soaking the fruit meal powder with the sodium bicarbonate aqueous solution is 4 hours. The sodium bicarbonate of above-mentioned concentration can not damage the nutritional labeling of fruit meal powder while having the effect of protecting color. The above soaking time can ensure that the fruit meal powder fully absorbs water and swells, which is convenient for the subsequent enzymatic hydrolysis reaction.
进一步,碳酸氢钠水溶液与果粕粉的用量比为10L:1kg。上述料液比可以使得果粕粉充分吸水膨胀,便于后续酶解反应的进行。Further, the dosage ratio of sodium bicarbonate aqueous solution to fruit meal powder is 10L: 1kg. The above-mentioned ratio of solid to liquid can make the fruit meal powder fully absorb water and swell, which facilitates the subsequent enzymatic hydrolysis reaction.
进一步,一种澳洲坚果果粕加工方法获得的蛋白饮料。Further, a protein drink obtained by processing macadamia nut pulp.
本方案采用酶解处理和加入助剂的手段获得的蛋白饮料,其稳定性良好,在加工、储藏和运输的过程中不容易出现沉淀和油脂析出的现象,可维持良好的外观,提升产品的品质。The protein beverage obtained by enzymatic hydrolysis treatment and adding additives in this solution has good stability, and is not prone to precipitation and oil precipitation during processing, storage and transportation, and can maintain a good appearance and improve product quality. quality.
具体实施方式Detailed ways
下面通过具体实施方式进一步详细说明:The following is further described in detail through specific implementation methods:
实施例1Example 1
取澳洲坚果的果粕粉进行蛋白饮料的制作,果粕粉来源为:对澳洲坚果的果仁进行油脂压榨(常规冷榨工艺)后,经过干燥处理获得固体状物质,将固体物质粉碎处理,过100目,获得果粕粉,其中含有大量的蛋白质等营养物质。在进行蛋白饮料的制作之前,对果粕粉的成分进行了检测,含水量为6.18%、蛋白质含量为26.55%,油脂含量为15.09%,碳水化合物含量为26.28%(均为质量分数)。The pulp powder of macadamia nuts is used to make protein drinks. The source of the pulp powder is: after the kernels of macadamia nuts are squeezed for oil (conventional cold pressing process), they are dried to obtain solid substances, and the solid substances are pulverized. Pass through 100 meshes to obtain fruit meal powder, which contains a lot of protein and other nutrients. Before making the protein drink, the composition of the fruit meal powder was tested, and the water content was 6.18%, the protein content was 26.55%, the fat content was 15.09%, and the carbohydrate content was 26.28% (both mass fractions).
将果粕粉加入纯水中(料液比为1kg:10L),再在纯水中加入碳酸氢钠,碳酸氢钠在水中的质量分数为0.5%,浸泡4h,使得果粕粉充分吸水。然后在水中加入木瓜蛋白酶(cas9001-73-4),将体系的pH值调整至6.0,木瓜蛋白酶与果粕粉的质量比为0.02:1,充分搅拌体系中的物料,使得酶和底物充分结合,然后68℃酶解反应8h。反应结束之后,充分搅拌,过滤取上清,获得酶解液,将酶解液加热至沸腾,并维持10min,获得提取液(其中含有大量的多肽、脂类等物质)。将提取液减压浓缩为原来体积的三分之一,获得浓缩液,待浓缩液冷却至室温之后,在浓缩液中加入吐温60、黄原胶和蔗糖,获得待均质体系。吐温60、黄原胶和蔗糖在待均质体系中的质量分数为0.2%、0.2%和10%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本实施例的蛋白饮料。Add the fruit meal powder into pure water (the ratio of solid to liquid is 1kg:10L), then add sodium bicarbonate into the pure water, the mass fraction of sodium bicarbonate in water is 0.5%, soak for 4 hours, so that the fruit meal powder can fully absorb water. Then add papain (cas9001-73-4) to the water, adjust the pH value of the system to 6.0, the mass ratio of papain to fruit meal powder is 0.02:1, fully stir the materials in the system, so that the enzyme and the substrate are fully Combined, then enzymatic hydrolysis at 68°C for 8h. After the reaction, stir well, filter and take the supernatant to obtain the enzymolysis solution, heat the enzymolysis solution to boiling, and keep it for 10 minutes to obtain the extract (which contains a large amount of polypeptides, lipids and other substances). The extract was concentrated under reduced pressure to one-third of its original volume to obtain a concentrated solution. After the concentrated solution was cooled to room temperature, Tween 60, xanthan gum and sucrose were added to the concentrated solution to obtain a homogeneous system. The mass fractions of Tween 60, xanthan gum and sucrose in the homogenized system were 0.2%, 0.2% and 10%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121° C. for 15 minutes to obtain the protein drink of this example.
实施例2Example 2
本实施例使用实施例1获得的浓缩液进行蛋白饮料的制作,在浓缩液中加入吐温60、黄原胶和蔗糖,获得待均质体系。吐温60、黄原胶和蔗糖在待均质体系中的质量分数为0.05%、0.1%和8%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本方案的蛋白饮料。In this example, the concentrate obtained in Example 1 was used to make a protein drink, and Tween 60, xanthan gum and sucrose were added to the concentrate to obtain a homogeneous system. The mass fractions of Tween 60, xanthan gum and sucrose in the homogenized system were 0.05%, 0.1% and 8%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121°C for 15 minutes to obtain the protein drink of this solution.
实施例3Example 3
本实施例使用实施例1获得的浓缩液进行蛋白饮料的制作,在浓缩液中加入吐温60、黄原胶和蔗糖,获得待均质体系。吐温60、黄原胶和蔗糖在待均质体系中的质量分数为0.3%、0.4%和12%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本方案的蛋白饮料。In this example, the concentrate obtained in Example 1 was used to make a protein drink, and Tween 60, xanthan gum and sucrose were added to the concentrate to obtain a homogeneous system. The mass fractions of Tween 60, xanthan gum and sucrose in the homogenized system were 0.3%, 0.4% and 12%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121°C for 15 minutes to obtain the protein drink of this solution.
实施例4Example 4
本实施例基本同实施例1,不同点在于,木瓜蛋白酶的用量,木瓜蛋白酶与果粕粉的质量比为0.01:1。The present embodiment is basically the same as Example 1, except that the amount of papain, the mass ratio of papain to fruit meal powder is 0.01:1.
实施例5Example 5
本实施例基本同实施例1,不同点在于,木瓜蛋白酶的用量,木瓜蛋白酶与果粕粉的质量比为0.04:1。The present embodiment is basically the same as Example 1, except that the amount of papain, the mass ratio of papain to fruit meal powder is 0.04:1.
对比例1Comparative example 1
本实施例使用实施例1获得的浓缩液进行蛋白饮料的制作,在浓缩液中加入吐温60、卡拉胶和蔗糖,获得待均质体系。吐温60、卡拉胶和蔗糖在待均质体系中的质量分数为0.2%、0.2%和10%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本方案的蛋白饮料。In this example, the concentrate obtained in Example 1 was used to make a protein drink, and Tween 60, carrageenan and sucrose were added to the concentrate to obtain a homogeneous system. The mass fractions of Tween 60, carrageenan and sucrose in the homogenized system were 0.2%, 0.2% and 10%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121°C for 15 minutes to obtain the protein drink of this solution.
对比例2Comparative example 2
本实施例使用实施例1获得的浓缩液进行蛋白饮料的制作,在浓缩液中加入吐温60、卡拉胶和蔗糖,获得待均质体系。吐温60、卡拉胶和蔗糖在待均质体系中的质量分数为0.2%、0.4%和10%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本方案的蛋白饮料。In this example, the concentrate obtained in Example 1 was used to make a protein drink, and Tween 60, carrageenan and sucrose were added to the concentrate to obtain a homogeneous system. The mass fractions of Tween 60, carrageenan and sucrose in the homogenized system were 0.2%, 0.4% and 10%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121°C for 15 minutes to obtain the protein drink of this solution.
对比例3Comparative example 3
本实施例使用实施例1获得的浓缩液进行蛋白饮料的制作,在浓缩液中加入吐温60、阿拉伯胶和蔗糖,获得待均质体系。吐温60、阿拉伯胶和蔗糖在待均质体系中的质量分数为0.2%、0.2%和10%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本方案的蛋白饮料。In this example, the concentrate obtained in Example 1 was used to make a protein drink, and Tween 60, gum arabic and sucrose were added to the concentrate to obtain a homogeneous system. The mass fractions of Tween 60, gum arabic and sucrose in the homogenized system were 0.2%, 0.2% and 10%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121°C for 15 minutes to obtain the protein drink of this solution.
对比例4Comparative example 4
本实施例使用实施例1获得的浓缩液进行蛋白饮料的制作,在浓缩液中加入吐温60、阿拉伯胶和蔗糖,获得待均质体系。吐温60、阿拉伯胶和蔗糖在待均质体系中的质量分数为0.2%、0.4%和10%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本方案的蛋白饮料。In this example, the concentrate obtained in Example 1 was used to make a protein drink, and Tween 60, gum arabic and sucrose were added to the concentrate to obtain a homogeneous system. The mass fractions of Tween 60, gum arabic and sucrose in the homogenized system were 0.2%, 0.4% and 10%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121°C for 15 minutes to obtain the protein drink of this solution.
对比例5Comparative example 5
本实施例使用实施例1获得的浓缩液进行蛋白饮料的制作,在浓缩液中加入司盘40、黄原胶和蔗糖,获得待均质体系。司盘40、黄原胶和蔗糖在待均质体系中的质量分数为0.2%、0.2%和10%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本方案的蛋白饮料。In this example, the concentrate obtained in Example 1 was used to make a protein drink, and Span 40, xanthan gum and sucrose were added to the concentrate to obtain a homogeneous system. The mass fractions of Span 40, xanthan gum and sucrose in the system to be homogenized are 0.2%, 0.2% and 10%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121°C for 15 minutes to obtain the protein drink of this solution.
对比例6Comparative example 6
本实施例使用实施例1获得的浓缩液进行蛋白饮料的制作,在浓缩液中加入司盘40、黄原胶和蔗糖,获得待均质体系。司盘40、黄原胶和蔗糖在待均质体系中的质量分数为0.4%、0.2%和10%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本方案的蛋白饮料。In this example, the concentrate obtained in Example 1 was used to make a protein drink, and Span 40, xanthan gum and sucrose were added to the concentrate to obtain a homogeneous system. The mass fractions of Span 40, xanthan gum and sucrose in the homogenized system were 0.4%, 0.2% and 10%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121°C for 15 minutes to obtain the protein drink of this solution.
对比例7Comparative example 7
本对比例基本同实施例1,但是在本对比例中不使用木瓜蛋白酶,而是将木瓜蛋白酶替换为中性蛋白酶,将酶解反应的pH值为7.0,中性蛋白酶与果粕粉的质量比为0.04:1,酶解反应的温度为40℃,时长为8h。This comparative example is basically the same as Example 1, but papain is not used in this comparative example, but papain is replaced by neutral protease, the pH value of the enzymolysis reaction is 7.0, the quality of neutral protease and fruit meal powder The ratio is 0.04:1, the temperature of the enzymatic hydrolysis reaction is 40°C, and the duration is 8h.
对比例8Comparative example 8
本对比例不使用木瓜蛋白酶酶解的方案,而是采用如下超声提取的技术方案:This comparative example does not use the scheme of papain enzymatic hydrolysis, but adopts the technical scheme of following ultrasonic extraction:
将果粕粉加入纯水中(料液比为1kg:10L),再在纯水中加入碳酸氢钠,碳酸氢钠在水中的质量分数为0.5%,浸泡4h,使得果粕粉充分吸水。然后200W超声处理5min,超声处理重复两次。超声处理结束之后,充分搅拌,过滤取上清,获得酶解液,将酶解液加热至沸腾,并维持10min,获得提取液(其中含有大量的多肽、脂类等物质)。将提取液减压浓缩为原来体积的三分之一,获得浓缩液,待浓缩液冷却至室温之后,在浓缩液中加入吐温60、黄原胶和蔗糖,获得待均质体系。吐温60、黄原胶和蔗糖在待均质体系中的质量分数为0.2%、0.2%和10%。然后将待均质体系加入饮料生产线中常规的均质机,在60℃和30Mpa的条件下,均质两次,获得均质体系。然后将均质体系在121℃下灭菌15min,获得本实施例的蛋白饮料。Add the fruit meal powder into pure water (the ratio of solid to liquid is 1kg:10L), then add sodium bicarbonate into the pure water, the mass fraction of sodium bicarbonate in water is 0.5%, soak for 4 hours, so that the fruit meal powder can fully absorb water. Then 200W ultrasonic treatment for 5min, and the ultrasonic treatment was repeated twice. After the ultrasonic treatment, fully stir, filter and take the supernatant to obtain the enzymolysis solution, heat the enzymolysis solution to boiling, and keep it for 10 minutes to obtain the extract (which contains a large amount of polypeptides, lipids and other substances). The extract was concentrated under reduced pressure to one-third of its original volume to obtain a concentrated solution. After the concentrated solution was cooled to room temperature, Tween 60, xanthan gum and sucrose were added to the concentrated solution to obtain a homogeneous system. The mass fractions of Tween 60, xanthan gum and sucrose in the homogenized system were 0.2%, 0.2% and 10%. Then put the homogenized system into a conventional homogenizer in the beverage production line, and homogenize twice under the conditions of 60° C. and 30 MPa to obtain a homogeneous system. Then the homogeneous system was sterilized at 121° C. for 15 minutes to obtain the protein drink of this example.
实验例Experimental example
本实验例测量了蛋白饮料的乳化稳定性,测量指标包括脂肪上浮率(CR)以及沉淀率(SR)。将未经过灭菌处理的30ml蛋白饮料放入具塞试管中,121℃下灭菌15min,然后在30℃的条件下静置两天(48h),从管底精确吸取2ml样品,分别测定放置前后管底的脂肪含量与总固体物质含量。脂肪上浮率和沉淀率的计算方法为:CR=(M1-M2)/M1;W1=A1-M1;W2=A2-M2;SR=(W2-W1)/W1;其中,M1和M2为放置前后管底脂肪含量,A1和A2为放置前后管底总固体物质含量。In this experimental example, the emulsification stability of the protein drink was measured, and the measurement indicators included the fat floating rate (CR) and the sedimentation rate (SR). Put 30ml of unsterilized protein drink into a stoppered test tube, sterilize at 121°C for 15min, then let it stand at 30°C for two days (48h), accurately draw 2ml of sample from the bottom of the tube, and measure the Fat content and total solids content at the bottom of the front and rear tubes. The calculation method of fat floating rate and sedimentation rate is: CR=(M1-M2)/M1; W1=A1-M1; W2=A2-M2; SR=(W2-W1)/W1; The fat content at the bottom of the tube before and after, A1 and A2 are the total solid matter content at the bottom of the tube before and after placement.
对实施例1-实施例5、对比例1-8获得的蛋白饮料进行脂肪上浮率和沉淀率的检测,每个实施例和对比例重复测量三次,检测结果如表1所示。The protein drinks obtained in Examples 1-Example 5 and Comparative Examples 1-8 were tested for fat floating rate and sedimentation rate. Each Example and Comparative Example was measured three times. The test results are shown in Table 1.
由表1的数据可知,采用实施例1-5的方法制备的蛋白饮料的稳定性较好,不易出现沉淀和脂肪析出的现象,产品感官良好,适合于较为长期的储存。对比例1和2中,使用卡拉胶作为增稠剂代替黄原胶,卡拉胶在稳定油脂和防止沉淀析出上的效果较黄原胶有显著差异。对比例3和4中,使用阿拉伯胶作为增稠剂代替黄原胶,阿拉伯胶在稳定油脂和防止沉淀析出上的效果较黄原胶有显著差异。对比例5和6中,使用司盘40作为表面活性剂代替吐温60,司盘40在稳定油脂和防止沉淀析出上的效果较吐温60有显著差异。综合对比例1-6的情况,使用吐温60和卡拉胶是防止油脂和沉淀析出的最佳手段。虽然使用加入助剂的方式来实现对饮料的稳定是较为常用的手段。但是,对于澳洲坚果的果粕的食品开发研究较少,对其果粕中的影响系统稳定性的物质成分尚不是非常清楚,这就给相关食品的研究造成了障碍。发明人对制备方法以及助剂进行了大量的研究,发现使用卡拉胶和吐温60作为助剂,非常适合于维持悬浊液/乳浊液的系统稳定。从澳洲坚果的果粕中提取出蛋白质、脂肪和碳水化合物等之后,卡拉胶、吐温60以及蔗糖能够使得上述物质以胶粒的形式,较为稳定地分散和悬浮在液体环境中。对比例7使用了中性蛋白酶酶解处理果粕,由此分解产生的小分子蛋白或者多肽在水溶液体系中的稳定性欠佳,容易析出沉淀。发明人分析原因在于由中性蛋白酶酶解产生的小分子蛋白或者多肽的三维结构不适合将其疏水基团充分暴露,不利于小分子蛋白质或者多肽与增稠剂或表面活性剂等助剂相结合,所以难以维持悬浊液的状态,容易析出沉淀。对比例8没有使用酶解的方案,而是使用超声提取的方案。虽然超声提取的方案用时较短,可将果粕中的营养成分充分提取,但是获得的蛋白质分子由于分子量较大的原因,较难稳定地分散在蛋白饮料的体系中,导致沉淀率较高。From the data in Table 1, it can be seen that the protein beverage prepared by the method of Examples 1-5 has good stability, is not prone to precipitation and fat precipitation, and has a good sensory feeling, which is suitable for relatively long-term storage. In Comparative Examples 1 and 2, carrageenan was used as a thickener instead of xanthan gum, and the effect of carrageenan on stabilizing oil and preventing precipitation was significantly different from that of xanthan gum. In comparative examples 3 and 4, gum arabic was used as a thickener instead of xanthan gum, and the effect of gum arabic on stabilizing oil and preventing precipitation was significantly different from that of xanthan gum. In Comparative Examples 5 and 6, Span 40 was used as the surfactant instead of Tween 60, and the effect of Span 40 on stabilizing oil and preventing precipitation was significantly different from that of Tween 60. Based on the situation of Comparative Examples 1-6, the use of Tween 60 and carrageenan is the best means to prevent grease and precipitation. Although it is a relatively common means to realize the stability of the beverage by adding additives. However, there are few studies on the food development of macadamia nut pulp, and the material components in the pulp that affect the system stability are not very clear, which has caused obstacles to the research of related foods. The inventor has conducted a lot of research on the preparation method and auxiliary agents, and found that using carrageenan and Tween 60 as auxiliary agents is very suitable for maintaining the stability of the suspension/emulsion system. After extracting protein, fat and carbohydrates from the pulp of macadamia nuts, carrageenan, Tween 60 and sucrose can make the above substances dispersed and suspended in the liquid environment in the form of colloidal particles more stably. In Comparative Example 7, neutral protease was used to enzymatically treat the fruit pulp, and the small molecular protein or polypeptide produced by this decomposition had poor stability in the aqueous solution system and was easy to precipitate and precipitate. The inventor analyzed that the reason is that the three-dimensional structure of the small molecular protein or polypeptide produced by the enzymatic hydrolysis of neutral protease is not suitable for fully exposing its hydrophobic groups, which is not conducive to the interaction of small molecular protein or polypeptide with additives such as thickeners or surfactants. Combined, it is difficult to maintain the state of suspension, and it is easy to precipitate. Comparative Example 8 did not use the solution of enzymatic hydrolysis, but used the solution of ultrasonic extraction. Although the ultrasonic extraction method takes a short time and can fully extract the nutrients in the fruit meal, the obtained protein molecules are difficult to stably disperse in the protein drink system due to the large molecular weight, resulting in a high precipitation rate.
以上所述的仅是本发明的实施例,方案中公知的具体技术方案和/或特性等常识在此未作过多描述。应当指出,对于本领域的技术人员来说,在不脱离本发明技术方案的前提下,还可以作出若干变形和改进,这些也应该视为本发明的保护范围,这些都不会影响本发明实施的效果和专利的实用性。本申请要求的保护范围应当以其权利要求的内容为准,说明书中的具体实施方式等记载可以用于解释权利要求的内容。What is described above is only an embodiment of the present invention, and common knowledge such as specific technical solutions and/or characteristics known in the solutions will not be described here too much. It should be pointed out that for those skilled in the art, without departing from the technical solutions of the present invention, some modifications and improvements can also be made, which should also be regarded as the protection scope of the present invention, and these will not affect the implementation of the present invention effect and utility of the patent. The scope of protection required by this application shall be based on the content of the claims, and the specific implementation methods and other records in the specification may be used to interpret the content of the claims.
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Application publication date: 20210810 Assignee: YUNNAN REVERT MEDICAL & BIOTECHNOLOGY CO.,LTD. Assignor: SOUTHWEST FORESTRY University Contract record no.: X2024980008354 Denomination of invention: A processing method for Australian nut meal and its protein beverage Granted publication date: 20230620 License type: Open License Record date: 20240719 |