CN104450156A - Method for extracting grease in fructus cannabis by using aqueous enzymatic method and fructus cannabis protein drink - Google Patents
Method for extracting grease in fructus cannabis by using aqueous enzymatic method and fructus cannabis protein drink Download PDFInfo
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- CN104450156A CN104450156A CN201410676901.2A CN201410676901A CN104450156A CN 104450156 A CN104450156 A CN 104450156A CN 201410676901 A CN201410676901 A CN 201410676901A CN 104450156 A CN104450156 A CN 104450156A
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- 239000004519 grease Substances 0.000 title claims 9
- 102000004169 proteins and genes Human genes 0.000 title abstract description 28
- 108090000623 proteins and genes Proteins 0.000 title abstract description 28
- 238000006911 enzymatic reaction Methods 0.000 title abstract description 12
- 241000218236 Cannabis Species 0.000 title 2
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- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 claims abstract description 78
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 claims abstract description 78
- 235000009120 camo Nutrition 0.000 claims abstract description 78
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- ODKSFYDXXFIFQN-BYPYZUCNSA-P L-argininium(2+) Chemical compound NC(=[NH2+])NCCC[C@H]([NH3+])C(O)=O ODKSFYDXXFIFQN-BYPYZUCNSA-P 0.000 description 2
- HNDVDQJCIGZPNO-YFKPBYRVSA-N L-histidine Chemical compound OC(=O)[C@@H](N)CC1=CN=CN1 HNDVDQJCIGZPNO-YFKPBYRVSA-N 0.000 description 2
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- DTOSIQBPPRVQHS-PDBXOOCHSA-N alpha-linolenic acid Chemical compound CC\C=C/C\C=C/C\C=C/CCCCCCCC(O)=O DTOSIQBPPRVQHS-PDBXOOCHSA-N 0.000 description 2
- 235000020661 alpha-linolenic acid Nutrition 0.000 description 2
- ODKSFYDXXFIFQN-UHFFFAOYSA-N arginine Natural products OC(=O)C(N)CCCNC(N)=N ODKSFYDXXFIFQN-UHFFFAOYSA-N 0.000 description 2
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- 239000000706 filtrate Substances 0.000 description 2
- FTSSQIKWUOOEGC-RULYVFMPSA-N fructooligosaccharide Chemical compound OC[C@H]1O[C@@](CO)(OC[C@@]2(OC[C@@]3(OC[C@@]4(OC[C@@]5(OC[C@@]6(OC[C@@]7(OC[C@@]8(OC[C@@]9(OC[C@@]%10(OC[C@@]%11(O[C@H]%12O[C@H](CO)[C@@H](O)[C@H](O)[C@H]%12O)O[C@H](CO)[C@@H](O)[C@@H]%11O)O[C@H](CO)[C@@H](O)[C@@H]%10O)O[C@H](CO)[C@@H](O)[C@@H]9O)O[C@H](CO)[C@@H](O)[C@@H]8O)O[C@H](CO)[C@@H](O)[C@@H]7O)O[C@H](CO)[C@@H](O)[C@@H]6O)O[C@H](CO)[C@@H](O)[C@@H]5O)O[C@H](CO)[C@@H](O)[C@@H]4O)O[C@H](CO)[C@@H](O)[C@@H]3O)O[C@H](CO)[C@@H](O)[C@@H]2O)[C@@H](O)[C@@H]1O FTSSQIKWUOOEGC-RULYVFMPSA-N 0.000 description 2
- 229940107187 fructooligosaccharide Drugs 0.000 description 2
- HNDVDQJCIGZPNO-UHFFFAOYSA-N histidine Natural products OC(=O)C(N)CC1=CN=CN1 HNDVDQJCIGZPNO-UHFFFAOYSA-N 0.000 description 2
- 229960004488 linolenic acid Drugs 0.000 description 2
- KQQKGWQCNNTQJW-UHFFFAOYSA-N linolenic acid Natural products CC=CCCC=CCC=CCCCCCCCC(O)=O KQQKGWQCNNTQJW-UHFFFAOYSA-N 0.000 description 2
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- 150000003839 salts Chemical class 0.000 description 2
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- 239000011593 sulfur Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 208000005156 Dehydration Diseases 0.000 description 1
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical class OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 102000006395 Globulins Human genes 0.000 description 1
- 108010044091 Globulins Proteins 0.000 description 1
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- FFEARJCKVFRZRR-BYPYZUCNSA-N L-methionine Chemical compound CSCC[C@H](N)C(O)=O FFEARJCKVFRZRR-BYPYZUCNSA-N 0.000 description 1
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
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- 238000010793 Steam injection (oil industry) Methods 0.000 description 1
- 241001506047 Tremella Species 0.000 description 1
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- HHEAADYXPMHMCT-UHFFFAOYSA-N dpph Chemical compound [O-][N+](=O)C1=CC([N+](=O)[O-])=CC([N+]([O-])=O)=C1[N]N(C=1C=CC=CC=1)C1=CC=CC=C1 HHEAADYXPMHMCT-UHFFFAOYSA-N 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
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- 238000005189 flocculation Methods 0.000 description 1
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- 239000003205 fragrance Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 235000020778 linoleic acid Nutrition 0.000 description 1
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
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- 238000003801 milling Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 230000035764 nutrition Effects 0.000 description 1
- 239000004006 olive oil Substances 0.000 description 1
- 235000008390 olive oil Nutrition 0.000 description 1
- 235000020660 omega-3 fatty acid Nutrition 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 230000001863 plant nutrition Effects 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
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- 239000004094 surface-active agent Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
- 235000020985 whole grains Nutrition 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Preparation or treatment thereof
- A23L2/38—Other non-alcoholic beverages
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Preparation or treatment thereof
- A23L2/52—Adding ingredients
- A23L2/60—Sweeteners
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/02—Pretreatment
- C11B1/04—Pretreatment of vegetable raw material
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Nutrition Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Non-Alcoholic Beverages (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
Abstract
本发明公开一种水酶法提取火麻仁中油脂的方法,该方法包括挤压膨化、提取火麻蛋白及油脂、酶解和灭酶离心的步骤;离心分离后得到游离油、液相和火麻仁渣,游离油过滤、脱水处理后得到火麻仁油,渣作为饲料原料。本发明还提供一种火麻仁蛋白饮料,该饮料的原料是对水酶法提取火麻仁中油脂的液相副产物的回收利用,是液相经过过滤后加入水、甜味剂,均质、灭菌后得到。本产品的蛋白含量在3%~8%,与其他市售的火麻饮料相比,本产品的添加剂用量大大降低,具有天然植物香味。
The invention discloses an aqueous enzymatic method for extracting oil from hemp seeds. The method comprises the steps of extruding and puffing, extracting hemp protein and oil, enzymatic hydrolysis, and centrifuging to inactivate the enzyme; free oil, liquid phase and centrifugation are obtained after centrifugal separation. The hemp seed slag and the free oil are filtered and dehydrated to obtain the hemp seed oil, and the slag is used as a feed material. The present invention also provides a hemp seed protein beverage. The raw material of the beverage is the recovery and utilization of the liquid phase by-products of the oil and fat in the hemp seed extracted by the aqueous enzymatic method. obtained after sterilization. The protein content of this product is between 3% and 8%. Compared with other commercially available hemp drinks, the amount of additives in this product is greatly reduced, and it has natural plant flavor.
Description
技术领域technical field
本发明涉及提取加工的技术领域。更具体地,涉及一种水酶法提取火麻仁中油脂的方法和一种火麻仁蛋白质饮料。The invention relates to the technical field of extraction processing. More specifically, it relates to a method for extracting oil from hemp seeds by aqueous enzymatic method and a protein drink from hemp seeds.
背景技术Background technique
火麻仁是火麻籽经过脱壳的产物,脂肪含量43%~48%,除油以外,还含有30%左右的蛋白质,5%左右的糖以及丰富的钙、磷、铁、锌、锰等。火麻仁油中不饱和脂肪酸含量超过85%,尤其是亚麻酸含量较高,在16%以上。亚油酸和亚麻酸的比值(ω-6):(ω-3)接近3:1,符合国际公认的营养比例标准;火麻仁油可以提高SOD/GSH-Px等酶活力,清除DPPH自由基的能力超过了橄榄油,适合作为一种抗氧化的膳食资源。火麻仁蛋白质的主要氨基酸是精氨酸、组氨酸、含硫氨基酸,精氨酸、组氨酸在儿童生长期非常重要,含硫氨基酸中的甲硫氨酸和半胱氨酸是产生生物酶所必需的,火麻仁是优质植物蛋白来源之一。Hemp seed is the shelled product of hemp seeds, with a fat content of 43% to 48%. In addition to oil, it also contains about 30% protein, about 5% sugar, and rich calcium, phosphorus, iron, zinc, and manganese. wait. The content of unsaturated fatty acid in hemp seed oil is more than 85%, especially the content of linolenic acid is higher, more than 16%. The ratio of linoleic acid to linolenic acid (ω-6):(ω-3) is close to 3:1, which meets the internationally recognized nutritional ratio standard; hemp seed oil can improve the activity of enzymes such as SOD/GSH-Px, and remove DPPH free The capacity of the base exceeds that of olive oil and is suitable as an antioxidant dietary resource. The main amino acids of hemp seed protein are arginine, histidine, and sulfur-containing amino acids. Arginine and histidine are very important during the growth period of children. Methionine and cysteine in sulfur-containing amino acids are the main Necessary for biological enzymes, hemp seed is one of the high-quality vegetable protein sources.
水酶法提油做为一种生物提油方法,以其条件温和、效率高、操作简单安全、油质高、环保性等优点成为近年来国内油脂提取研究的热点。在水酶法提取过程中,较多采用总油提取率评价提油率,即:总油提取率(%)=(原料总油质量-残渣中总有质量)*100%/原料中总油质量,由于乳状液的存在以及无法彻底破乳,一般实际游离清油得率(清油提取率(%)=游离清油质量*100%/原料总油质量)大大低于总油提取率。因而,减少乳化,提高清油得率是酶法提油非常重要的环节。As a biological oil extraction method, aqueous enzymatic oil extraction has become a hot spot in domestic oil extraction research in recent years due to its advantages such as mild conditions, high efficiency, simple and safe operation, high oil quality, and environmental protection. In the water enzymatic extraction process, the total oil extraction rate is often used to evaluate the oil extraction rate, that is: total oil extraction rate (%) = (total oil quality of raw materials - total mass in residue) * 100% / total oil in raw materials Quality, due to the existence of the emulsion and the inability to completely break the emulsion, the general actual free clear oil yield (clear oil extraction rate (%)=free clear oil quality*100%/raw material total oil quality) is much lower than the total oil extraction rate. Therefore, reducing emulsification and increasing the yield of clear oil are very important steps in enzymatic oil extraction.
挤压膨化技术作为一种植物油料的前处理技术,原理是利用挤压膨化机内断齿螺旋和剪切销钉的联合挤压、揉搓、剪切等机械作用,以及摩擦生热和喷入蒸汽的湿热作用,使物料处于瞬间高温高压环境,从而破坏细胞组织结构。在物料挤压出模孔的瞬间,压力瞬间释放,水分迅速蒸发,细胞组织再次被破坏。作为酶法提油的前处理技术,可以与酶先后协同作用,起到促进油料中油脂释放及易于提取目的。As a pre-treatment technology of vegetable oil, extrusion technology is based on the combined extrusion, kneading, shearing and other mechanical effects of the broken-toothed spiral and shearing pins in the extrusion machine, as well as frictional heat generation and steam injection. The effect of heat and humidity puts the material in an instantaneous high-temperature and high-pressure environment, thereby destroying the cell structure. When the material is extruded out of the die hole, the pressure is released instantly, the water evaporates rapidly, and the cell tissue is destroyed again. As a pretreatment technology for enzymatic oil extraction, it can work synergistically with enzymes to promote the release of oil in oil plants and facilitate extraction.
专利CN102816631A公开了一种酸法挤压膨化水酶法提取火麻籽油脂的方法,其在挤压膨化前用物料重量2%-5%的2mol/L的硫酸喷洒物料,硫酸对设备会存在一定腐蚀,同时,在后续利用碱性蛋白酶酶解时需要在酶解体系中引入更多的碱,高含量的盐会对水相质量带来不利影响;而且专利中以“总油提油率”为指标,未提及清油提取率;加酶量以混合液总量计,用酶量较大,且未提及副产物液相的再利用。专利CN103445259A利用火麻仁直接磨浆酶解后制作蛋白质饮料,通过整粒煮沸、打浆、胶体磨细磨三个环节使蛋白质溶解,但最终液相中溶解蛋白质的量并不明确。专利CN101828739A公开了一种银耳火麻仁饮料食品及其制备方法,是在常规的直接利用火麻仁制作饮料的基础上加入银耳起到增稠剂的作用,在制备过程中,将火麻仁打浆过滤的滤液进行调配,也未提及滤液中蛋白质的含量,而大部分的营养物质脂肪及蛋白质等尚存在残渣中,是对整体资源利用的极大浪费。Patent CN102816631A discloses a method for extracting hemp seed oil by acid extrusion and water enzymatic method, which sprays the material with 2mol/L sulfuric acid of 2%-5% of the material weight before extrusion and expansion, and the sulfuric acid will cause damage to the equipment. certain corrosion, and at the same time, more alkali needs to be introduced into the enzymolysis system in the enzymatic hydrolysis with alkaline protease, and a high content of salt will have an adverse effect on the quality of the water phase; and the patent uses "total oil extraction rate " is used as an indicator, and the extraction rate of clear oil is not mentioned; the amount of enzyme added is based on the total amount of the mixed solution, and the amount of enzyme used is relatively large, and the reuse of the by-product liquid phase is not mentioned. Patent CN103445259A uses hemp seeds to directly grind and enzymatically hydrolyze to make a protein drink. The protein is dissolved through three steps of whole grain boiling, beating, and colloid milling, but the final amount of dissolved protein in the liquid phase is not clear. Patent CN101828739A discloses a tremella hemp seed beverage food and its preparation method. On the basis of the conventional direct use of hemp seed to make beverages, white fungus is added to play the role of thickener. During the preparation process, hemp seed The filtrate obtained by beating and filtering is prepared, and the protein content in the filtrate is not mentioned, and most of the nutrients such as fat and protein still exist in the residue, which is a great waste of overall resource utilization.
要使火麻仁等小油料产业健康发展,必须重视资源的整体加工效益。因此,需要提供一种能最大程度保障清油提取率的水酶法提取火麻仁中油脂的方法,同时还能提供一种将液相回收利用制作成蛋白质饮料,避免油脂含量高导致口感及稳定性不佳的火麻仁蛋白质饮料。In order to make the hemp seed and other small oil industries develop healthily, we must pay attention to the overall processing efficiency of resources. Therefore, it is necessary to provide a method for extracting oil from hemp seeds by water enzymatic method that can guarantee the extraction rate of clear oil to the greatest extent. At the same time, it can also provide a method for recycling the liquid phase to make protein drinks, so as to avoid the high oil content that will lead to taste and stability. Sexually unhealthy hemp seed protein drink.
发明内容Contents of the invention
本发明的一个目的在于提供一种水酶法提取火麻仁中油脂的方法,该方法可以克服现有技术中水酶法存在的乳化严重,破乳繁琐,清油得率低,液相利用不充分的问题,该方法是一种无乳化或者微乳化的高清油得率的酶法提油技术。An object of the present invention is to provide a method for extracting oil from hemp seeds by an aqueous enzymatic method, which can overcome the severe emulsification, cumbersome demulsification, low yield of clear oil, and poor utilization of the liquid phase in the prior art. Sufficient problem, this method is an enzymatic oil extraction technology with high oil yield without emulsification or microemulsion.
本发明的另一个目的在于提供一种火麻仁蛋白质饮料,该饮料的原料是对水酶法提取火麻仁中油脂的液相副产物的回收利用,且液相中富含蛋白质,因此本产品的蛋白含量在3%~5%,与其他市售的火麻饮料相比,本产品的添加剂用量大大降低,具有天然植物香味。Another object of the present invention is to provide a kind of hemp seed protein beverage, the raw material of this beverage is the recovery and utilization of the liquid phase by-product of oil and fat in hemp seed extracted by water enzymatic method, and the liquid phase is rich in protein, so this The protein content of the product is 3% to 5%. Compared with other commercially available hemp drinks, the amount of additives in this product is greatly reduced, and it has natural plant flavor.
为达到上述目的,本发明采用下述技术方案:To achieve the above object, the present invention adopts the following technical solutions:
一种水酶法提取火麻仁中油脂的方法,包括以下步骤:A method for hydroenzymatically extracting oil from hemp seeds, comprising the following steps:
(1)挤压膨化:将火麻仁粗粉碎后进行挤压膨化;(1) extrusion puffing: carry out extrusion puffing after the hemp seed is coarsely crushed;
(2)提取火麻蛋白和油脂体:将挤压膨化后的火麻仁粉碎,加入水,得到混合液,用稀碱溶液调节混合液的pH至8.0~8.5,50~65℃下搅拌提取20~40min;(2) Extract hemp protein and oil bodies: crush the hemp seeds after extrusion, add water to obtain a mixed solution, adjust the pH of the mixed solution to 8.0-8.5 with a dilute alkali solution, and stir and extract at 50-65°C 20~40min;
火麻仁中的蛋白质主要是球蛋白,可以溶解在稀碱溶液中,蛋白质的溶解可以促进油的释放,提高油脂的提取率,但pH不宜过高,碱用量过大会影响体系中可溶物的色泽、增加液相中的盐浓度,不利于后期利用液相制备蛋白质饮料。The protein in hemp seed is mainly globulin, which can be dissolved in dilute alkali solution. The dissolution of protein can promote the release of oil and improve the extraction rate of oil, but the pH should not be too high, and the excessive amount of alkali will affect the soluble matter in the system. The color and the increase of the salt concentration in the liquid phase are not conducive to the later use of the liquid phase to prepare protein beverages.
(3)酶解:搅拌提取后调节混合液pH至酶的最适作用pH,加入挤压膨化后的火麻仁重量0.5%~2.0%的碱性蛋白酶,酶解2~6h;加入挤压膨化后的火麻仁重量0.5%~1.5%的中性蛋白酶,酶解2~4小时后得到酶解液;(3) Enzymolysis: After stirring and extracting, adjust the pH of the mixed solution to the optimum pH of the enzyme, add 0.5% to 2.0% of the weight of the extruded hemp seeds with alkaline protease, and perform enzymolysis for 2 to 6 hours; add the extruded 0.5% to 1.5% neutral protease by weight of the puffed hemp seeds, and enzymolysis is obtained after 2 to 4 hours;
碱性蛋白酶是针对火麻仁水酶法提油使用效果较好的蛋白质内切酶,但单独使用该酶易形成乳化层,与中性蛋白酶复合使用,几乎无乳化层,可以大大提高清油及总油提取率。这是因为碱性蛋白酶与中性蛋白酶对蛋白质的作用位点不同,单独使用碱性蛋白酶时依然有大分子蛋白质存在,易作为表面活性剂促成稳定乳状液的形成,使用中性蛋白酶对碱性蛋白酶作用的蛋白质C-端或N-端在此进行降解,减少蛋白质分子的分子量和柔性程度,降低其乳化能力,从而可以提高清油提取率。Alkaline protease is an endoproteinase with good effect on hemp seed water enzymatic oil extraction, but it is easy to form an emulsified layer when used alone, and it is used in combination with neutral protease, almost no emulsified layer, which can greatly improve the oil and Total oil extraction rate. This is because alkaline protease and neutral protease have different action sites on proteins. When alkaline protease is used alone, there are still macromolecular proteins, which can easily be used as surfactants to promote the formation of stable emulsions. The C-terminal or N-terminal of the protein acted by protease is degraded here, reducing the molecular weight and flexibility of the protein molecule, reducing its emulsifying ability, thereby improving the extraction rate of clear oil.
控制碱性蛋白酶和中性蛋白酶用量以及酶解时间,既使各种酶充分发挥酶解效力,油脂从被包裹的蛋白质中释放,又能节省成本,降低能耗。Controlling the amount of alkaline protease and neutral protease and the time of enzymatic hydrolysis not only enables all kinds of enzymes to fully exert their enzymatic hydrolysis effectiveness, but also releases oil from the wrapped protein, which can save costs and reduce energy consumption.
(4)灭酶离心:将酶解液在90~95℃进行灭酶处理5~10min,然后离心分离,得到游离油、液相和残渣三部分;游离油脱水处理后即得。(4) Enzyme-inactivating centrifugation: the enzymolysis solution is subjected to enzyme-inactivating treatment at 90-95°C for 5-10 minutes, and then centrifuged to obtain three parts: free oil, liquid phase and residue; the free oil can be obtained after dehydration treatment.
灭酶离心使体系中的碱性蛋白酶和中性蛋白酶失活,防止蛋白质过度水解,保证后续饮料的口感。残渣可以作为饲料原料。Enzyme-inactivating centrifugation inactivates alkaline protease and neutral protease in the system, prevents excessive protein hydrolysis, and ensures the taste of subsequent beverages. The residue can be used as feed material.
优选地,步骤(1)所述粗粉碎是将火麻仁粉碎为目数≥10目的颗粒。Preferably, the coarse crushing in the step (1) is crushing the hemp seed into particles with a mesh size ≥ 10 mesh.
优选地,步骤(1)所述挤压膨化过程中,控制膨化机转速60-90rpm,喂料机转速160-200rpm,膨化机套管温度5-70℃,控制膨化后火麻仁含水率为5.0%~10.0%。Preferably, during the extrusion and puffing process described in step (1), the speed of the extruder is controlled to 60-90rpm, the speed of the feeder is 160-200rpm, the temperature of the casing of the puffing machine is 5-70°C, and the moisture content of the hemp seed after control is controlled to be 5.0% to 10.0%.
由于火麻仁含油量及蛋白质含量均较高,蒸汽较大时使物料吸水后含水量增大,性状粘稠极易造成堵腔并影响膨化效果,因此保持适宜蒸汽量尤为重要;喂料转速过快,膨化机转速较慢时造成喂料口堵料,反之使膨化出料断断续续,因此协调的转速才能保证膨化的顺利进行;套管温度过高,会使物料中蛋白质发生变性,对后期水酶法提油产生不利影响。Due to the high oil content and protein content of hemp seeds, when the steam is large, the water content of the material will increase after absorbing water, and the sticky property will easily cause cavity blockage and affect the puffing effect. Therefore, it is particularly important to maintain an appropriate steam amount; feeding speed If the speed is too fast, the feed port will be blocked when the speed of the extruder is slow, otherwise the puffed material will be discharged intermittently. Therefore, a coordinated speed can ensure the smooth progress of the puffing; Aqueous enzymatic oil extraction has adverse effects.
优选地,步骤(2)将膨化后的火麻仁粉碎至平均粒径≤50μm;加入水的重量为火麻仁重量的3-8倍;Preferably, step (2) pulverizes the expanded hemp seeds to an average particle size of ≤50 μm; the weight of the added water is 3-8 times the weight of the hemp seeds;
物料粉碎的细度影响水酶法的提油率,粉碎粒径越小,提油率越高,但粉碎过细,乳化层严重,增加破乳的难度。The fineness of the crushed material affects the oil extraction rate of the aqueous enzymatic method. The smaller the particle size of the crushed material, the higher the oil extraction rate. However, if the crushing is too fine, the emulsification layer will be serious, which will increase the difficulty of demulsification.
更优选地,加入水的重量为火麻仁重量的4-6倍。More preferably, the weight of adding water is 4-6 times of the weight of hemp seed.
优选地,步骤(3)所述碱性蛋白酶选自食品级Alcalase 2.4L、FoodPro蛋白酶、2709碱性蛋白酶或木瓜蛋白酶中的一种或多种;Preferably, the alkaline protease described in step (3) is selected from one or more of food grade Alcalase 2.4L, FoodPro protease, 2709 alkaline protease or papain;
上述碱性蛋白酶最适pH范围分别为:Alcalase 2.4L6.5~8.5、FoodPro蛋白酶9~10,2709碱性蛋白酶8.5~9.5、木瓜蛋白酶8.0~9.5;The optimum pH ranges of the above-mentioned alkaline proteases are: Alcalase 2.4L6.5-8.5, FoodPro protease 9-10, 2709 alkaline protease 8.5-9.5, papain 8.0-9.5;
所述中性蛋白酶选自食品级蛋白酶Alphalase、复合风味蛋白酶或Neutrase中的一种或多种;The neutral protease is selected from one or more of food-grade protease Alphalase, compound flavor protease or Neutrase;
上述中性蛋白酶最适pH范围分别为:食品级蛋白酶Alphalase6~8、复合风味蛋白酶5.0~7.0、Neutrase5.5~7.5;The optimum pH ranges of the above-mentioned neutral proteases are: food-grade protease Alphalase 6-8, compound flavor protease 5.0-7.0, Neutrase 5.5-7.5;
优选地,所述碱性蛋白酶为Alcalase 2.4L,中性蛋白酶为Alphalase;Preferably, the alkaline protease is Alcalase 2.4L, and the neutral protease is Alphalase;
优选地,所述碱性蛋白酶用量为火麻仁重量的0.5%~1.5%,中性蛋白酶用量为火麻仁重量的0.5%~1%。Preferably, the amount of the alkaline protease is 0.5%-1.5% of the weight of the hemp seed, and the amount of the neutral protease is 0.5%-1% of the weight of the hemp seed.
优选地,步骤(4)所述离心分离采用三相离心机或者卧式离心机。Preferably, the centrifugal separation in step (4) adopts a three-phase centrifuge or a horizontal centrifuge.
一种火麻仁蛋白质饮料,所述火麻仁蛋白饮料的主要原料为本发明所述的水酶法提取火麻仁中油脂的方法中得到的液相。A hemp seed protein drink, the main raw material of the hemp seed protein drink is the liquid phase obtained in the method for extracting oil from hemp seed by aqueous enzymatic method in the present invention.
优选地,所述火麻仁蛋白饮料中蛋白质含量为3%-8%。Preferably, the protein content in the hemp seed protein drink is 3%-8%.
优选地,所述火麻仁蛋白饮料的原料中还包括甜味剂和水,优选地,所述甜味剂的重量为所述液相重量的1%-10%;所述水的重量为液相的0-1倍。加水的目的是,直接出来的液相中蛋白质含量太高,加水不但可以适当稀释,达到饮料稳定的作用,又可以一定程度上增加产品产量。Preferably, the raw material of the hemp seed protein beverage also includes sweetener and water, preferably, the weight of the sweetener is 1%-10% of the weight of the liquid phase; the weight of the water is 0-1 times of the liquid phase. The purpose of adding water is that the protein content in the liquid phase that comes out directly is too high. Adding water can not only properly dilute and stabilize the beverage, but also increase the output of the product to a certain extent.
所述甜味剂选自蔗糖或低聚果糖。The sweetener is selected from sucrose or fructooligosaccharides.
本发明还提供一种火麻仁蛋白饮料的制备方法,是将上述水酶法提取火麻仁中油脂的方法中得到的液相经过过滤后加入水、甜味剂,均质、灭菌后得到产品火麻仁蛋白饮料。The present invention also provides a preparation method of hemp seed protein drink, which is to filter the liquid phase obtained in the method of extracting hemp seed oil by the above water enzymatic method, add water and sweetener, homogenize and sterilize Get the product hemp seed protein drink.
优选地,均质压力为20~50Mpa;灭菌条件为121℃下15min。Preferably, the homogeneous pressure is 20-50Mpa; the sterilization condition is 121°C for 15min.
在水酶法提油过程中,大量的水解蛋白、可溶性碳水化合物、矿物质等溶解于液相,制备的饮品营养丰富,对促进人体健康具有多种功效,是很好保健功能植物营养饮料。调配时,加入甜味剂低聚果糖使饮料口感更好,均质处理可以提高饮料的稳定性。In the process of water enzymatic oil extraction, a large amount of hydrolyzed protein, soluble carbohydrates, minerals, etc. are dissolved in the liquid phase, and the prepared drink is rich in nutrition and has various effects on promoting human health. It is a good health-care functional plant nutrition drink. When blending, the sweetener fructooligosaccharide is added to make the drink taste better, and the homogenization treatment can improve the stability of the drink.
本发明中的各项指标的测定依据:The measurement basis of each index among the present invention:
清油得率(%)=清油质量*100%/原料中油质量Clean oil yield (%) = clean oil quality * 100% / oil quality in raw materials
总油得率(%)=(原料中油质量-残渣中油质量)*100%/原料中油质量。Total oil yield (%) = (mass of oil in raw material - mass of oil in residue) * 100%/mass of oil in raw material.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
本发明与有机溶剂提油工艺相比,不使用有机溶剂,属于环境友好型,且毛油质量好,减少精炼环节,节省设备投资;与压榨法制油相比,在保证油质的同时可以再利用蛋白质,最大程度开发该资源的价值。Compared with the organic solvent oil extraction process, the present invention does not use organic solvents, is environmentally friendly, and has good quality crude oil, reduces refining links, and saves equipment investment; Utilize protein to maximize the value of this resource.
本发明与其它火麻仁水酶法提油专利相比,加酶量以原料的百分比计算,用酶量少,降低了经济成本;采用碱性蛋白酶+中性蛋白酶进行酶解,极大的减少了乳化的程度,降低了破乳工序负担,并提高了清油提取率;利用液相直接制备植物蛋白饮品,提高了副产物的利用率。Compared with other patents of hemp seed water enzymatic oil extraction, the amount of enzyme added is calculated by the percentage of raw materials, and the amount of enzyme used is small, which reduces the economic cost; using alkaline protease + neutral protease for enzymatic hydrolysis, greatly The degree of emulsification is reduced, the burden of the demulsification process is reduced, and the extraction rate of clear oil is improved; the vegetable protein drink is directly prepared by using the liquid phase, and the utilization rate of by-products is improved.
本发明与其它火麻仁饮料相比,是将火麻仁中含量最高的油脂提取后对富含水解蛋白的液相的利用。与其他市售的火麻饮料相比,添加剂用量大大降低,蛋白含量在3%~8%,含有天然植物香味,适于不同人群饮用。Compared with other hemp seed beverages, the invention utilizes the liquid phase rich in hydrolyzed protein after extracting the oil with the highest content in the hemp seed. Compared with other commercially available hemp drinks, the amount of additives is greatly reduced, the protein content is 3% to 8%, contains natural plant fragrance, and is suitable for drinking by different groups of people.
附图说明Description of drawings
下面结合附图对本发明的具体实施方式作进一步详细的说明。The specific implementation manners of the present invention will be further described in detail below in conjunction with the accompanying drawings.
图1示出本发明实施例1的工艺流程图。Fig. 1 shows the process flow chart of embodiment 1 of the present invention.
具体实施方式Detailed ways
为了更清楚地说明本发明,下面结合优选实施例和附图对本发明做进一步的说明。附图中相似的部件以相同的附图标记进行表示。本领域技术人员应当理解,下面所具体描述的内容是说明性的而非限制性的,不应以此限制本发明的保护范围。In order to illustrate the present invention more clearly, the present invention will be further described below in conjunction with preferred embodiments and accompanying drawings. Similar parts in the figures are denoted by the same reference numerals. Those skilled in the art should understand that the content specifically described below is illustrative rather than restrictive, and should not limit the protection scope of the present invention.
实施例1Example 1
称取2kg脱壳火麻仁,粗粉碎后进行挤压膨化,模具孔径8mm,膨化机转速90rpm,喂料机转速200rpm,套管温度为60℃,挤压膨化后物料含水量为9.6%;Weigh 2kg of shelled hemp seeds, coarsely pulverize and extrude and expand, the die aperture is 8mm, the rotating speed of the extruder is 90rpm, the rotating speed of the feeder is 200rpm, the casing temperature is 60°C, and the moisture content of the material after extrusion is 9.6%;
取挤压膨化后的火麻仁,经粉碎机粗粉碎再过碾磨机碾磨至粒径≤50μm,称量1kg,加入4L去离子水,搅拌均匀后调节体系pH至8.5,温度为60℃,提取35min;Take the extruded and puffed hemp seeds, coarsely pulverize them with a pulverizer, and then grind them with a mill until the particle size is ≤50 μm, weigh 1kg, add 4L of deionized water, stir evenly, adjust the pH of the system to 8.5, and the temperature is 60 ℃, extract for 35min;
然后调节体系pH至8.5,加入碱性蛋白酶Alcalase 2.4L(加入量为挤压膨化后的火麻仁重量的2%),作用4小时后,加入中性蛋白酶Alphalase(加入量为挤压膨化后的火麻仁重量的0.5%),搅拌酶解3h得到酶解液;Then adjust system pH to 8.5, add alkaline protease Alcalase 2.4L (addition is 2% of the hemp seed weight after extrusion puffing), after acting for 4 hours, add neutral protease Alphalase (addition is after extrusion puffing) 0.5% of the weight of the hemp seed), stirred and enzymolyzed for 3h to obtain the enzymolyzate;
将得到酶解液温度升至90℃并保持5min灭酶,4000rpm下离心分离15min,酶解液分为清油、液相及残渣三层;清油得率为86.12%,总油得率为89.44%。Raise the temperature of the obtained enzymolysis solution to 90°C and keep it for 5 minutes to inactivate the enzyme, centrifuge at 4000rpm for 15 minutes, the enzymolysis solution is divided into three layers: clear oil, liquid phase and residue; the yield of clear oil is 86.12%, and the yield of total oil is 89.44% .
所得液相经过滤、加入甜味剂(加入量为液体重量的5%)、等量的水,在30Mpa下均质(2min/次,2次)、灌装,121℃灭菌15min,冷却后得到饮料。饮料中植物蛋白含量4.8%,饮料具有特有的烘培香味。一般植物蛋白饮料中蛋白质含量是3%以下,国家行业标准一般是0.6%以上。The obtained liquid phase is filtered, added with a sweetener (the addition amount is 5% of the liquid weight), an equal amount of water, homogenized at 30Mpa (2min/time, twice), filled, sterilized at 121°C for 15min, and cooled After getting drinks. The vegetable protein content in the beverage is 4.8%, and the beverage has a unique roasted aroma. Generally, the protein content in vegetable protein drinks is less than 3%, and the national industry standard is generally more than 0.6%.
实施例2Example 2
称取3kg脱壳火麻仁,粗粉碎后进行挤压膨化,模具孔径6mm,膨化机转速70rpm,喂料机转速175rpm,套管温度为55℃,挤压膨化后物料含水量为6.2%;Weigh 3kg of shelled hemp seeds, carry out extrusion and puffing after coarse crushing, the die aperture is 6mm, the speed of the extruder is 70rpm, the speed of the feeder is 175rpm, the casing temperature is 55°C, and the water content of the material after extrusion is 6.2%;
取挤压膨化后的火麻仁,经粉碎机粗粉碎再过碾磨机碾磨至粒径≤50μm,称量500g,加入1.5L去离子水,搅拌均匀后调节体系pH至8.0,温度为60℃,提取30min;Take the extruded and puffed hemp seeds, coarsely pulverize them with a grinder, and then grind them with a mill until the particle size is ≤50 μm, weigh 500 g, add 1.5 L of deionized water, stir evenly, adjust the pH of the system to 8.0, and the temperature is 60°C, extract for 30min;
调节体系pH至8.5,加入挤压膨化后的火麻仁重量1%的碱性蛋白酶Alcalase 2.4L和挤压膨化后的火麻仁重量1%的中性蛋白酶Alphalase,慢速搅拌酶解6h;Adjust the pH of the system to 8.5, add 2.4L of alkaline protease Alcalase 1% by weight of extruded and expanded hemp seeds and neutral protease Alphalase of 1% by weight of extruded and expanded hemp seeds, and slowly stir for 6 hours;
将体系温度升至95℃并保持5min灭酶,4500rpm下离心分离15min,酶解液分为清油、液相及残渣三层;清油得率为90.69%,总油得率为91.06%。Raise the temperature of the system to 95°C and maintain it for 5 minutes to inactivate the enzyme, centrifuge at 4500 rpm for 15 minutes, and the enzymolysis liquid is divided into three layers: clear oil, liquid phase and residue; the yield of clear oil is 90.69%, and the yield of total oil is 91.06%.
所得液相经过滤、加入甜味剂(加入量为液相重量的3%)、液相等量的水,在20Mpa下均质(3min/次,3次)、121℃灭菌等处理后得到饮料。饮料中植物蛋白含量6.9%,饮料具有特有的烘培香味。The obtained liquid phase is filtered, added with a sweetener (the addition amount is 3% of the liquid phase weight), water in the same amount as the liquid phase, homogenized at 20Mpa (3min/time, 3 times), and sterilized at 121°C. get drinks. The vegetable protein content in the beverage is 6.9%, and the beverage has a unique roasted aroma.
实施例3Example 3
称取5kg脱壳火麻仁,粗粉碎后进行挤压膨化,模具孔径6mm,膨化机转速80rpm,喂料机转速188rpm,套管温度为70℃,挤压膨化后物料含水量为7.8%;Take by weighing 5kg shelled hemp seeds, carry out extrusion puffing after coarse pulverization, die aperture 6mm, extruder rotating speed 80rpm, feeder rotating speed 188rpm, casing temperature is 70 ℃, and the material moisture content after extrusion puffing is 7.8%;
取挤压膨化后的火麻仁,经粉碎机粗粉碎再过碾磨机碾磨至粒径≤50μm,称量1.5kg,加入7.5L去离子水,搅拌均匀后调节体系pH至8.0,温度为60℃,提取30min;Take the extruded and expanded hemp seeds, coarsely pulverize them with a pulverizer, and then grind them with a mill until the particle size is ≤50 μm, weigh 1.5kg, add 7.5L deionized water, and adjust the pH of the system to 8.0 after stirring evenly. at 60°C, extract for 30 minutes;
调节体系pH至9.0,加入火麻仁重量1.5%的碱性蛋白酶Alcalase2.4L和1%的中性蛋白酶Alphalase,慢速搅拌酶解5h;Adjust the pH of the system to 9.0, add 1.5% of the weight of the hemp seed Alcalase 2.4L and 1% of the neutral protease Alphalase, and stir slowly for 5 hours;
将体系温度升至95℃并保持5min灭酶,4500rpm下离心分离15min,酶解液分为清油、液相及残渣三层;清油得率为89.21%,总油得率为92.40%。The temperature of the system was raised to 95°C and kept for 5 minutes to inactivate the enzyme, centrifuged at 4500 rpm for 15 minutes, and the enzymolysis liquid was divided into three layers: clear oil, liquid phase and residue; the yield of clear oil was 89.21%, and the yield of total oil was 92.40%.
液相经过滤、加入甜味剂7%,在35Mpa下均质(3min/次,3次)、121℃灭菌等处理后得到饮料。饮料中植物蛋白含量7.6%,饮料具有特有的烘培香味The liquid phase is filtered, added with 7% sweetener, homogenized at 35Mpa (3 min/time, 3 times), sterilized at 121°C, etc. to obtain a beverage. The vegetable protein content in the beverage is 7.6%, and the beverage has a unique roasted aroma
实施例4Example 4
称取2kg脱壳火麻仁,粗粉碎后进行挤压膨化,模具孔径10mm,膨化机转速70rpm,喂料机转速175rpm,套管温度为65℃,挤压膨化后物料含水量为9.6%;Weigh 2kg of shelled hemp seeds, coarsely pulverize and extrude and expand, the die aperture is 10mm, the rotating speed of the extruder is 70rpm, the rotating speed of the feeder is 175rpm, the casing temperature is 65°C, and the moisture content of the material after extrusion is 9.6%;
取挤压膨化后的火麻仁,经粉碎机粗粉碎再过碾磨机碾磨至粒径≤50μm,称量1kg,加入5L去离子水,搅拌均匀后调节体系pH至8.5,温度为50℃,提取40min;Take the extruded and puffed hemp seeds, coarsely pulverize them with a pulverizer, and then grind them with a mill until the particle size is ≤50 μm, weigh 1 kg, add 5 L of deionized water, stir evenly, adjust the pH of the system to 8.5, and the temperature is 50 ℃, extract for 40min;
然后调节体系pH至8.5,加入碱性蛋白酶Alcalase 2.4L(加入量为火麻仁重量的2%),作用4小时后,加入中性蛋白酶Alphalase(加入量为火麻仁重量的0.5%),搅拌酶解3h得到酶解液;Regulate system pH to 8.5 then, add alkaline protease Alcalase 2.4L (add-on is 2% of hemp seed weight), after effecting 4 hours, add neutral protease Alphalase (add-on is 0.5% of hemp seed weight), Stir the enzymolysis for 3h to obtain the enzymolysis solution;
将得到酶解液温度升至90℃并保持5min灭酶,采用卧式离心机离心分离,酶解液分为清油、液相及残渣三层;清油得率为90.38%,总油得率为93.25%。Raise the temperature of the obtained enzymolysis solution to 90°C and keep it for 5 minutes to inactivate the enzyme, and use a horizontal centrifuge to separate the enzymolysis solution into three layers: clear oil, liquid phase and residue; the yield of clear oil is 90.38%, and the yield of total oil is 93.25%.
所得液相经过滤、加入甜味剂低聚果糖(加入量为液相重量的1%),在30Mpa下均质(2min/次,2次)、灌装,121℃灭菌15min,冷却后得到饮料。The obtained liquid phase is filtered, added with sweetener fructooligosaccharide (addition amount is 1% of liquid phase weight), homogenized (2min/time, 2 times) at 30Mpa, filled, sterilized at 121°C for 15min, after cooling get drinks.
实施例5Example 5
称取2kg脱壳火麻仁,粗粉碎后进行挤压膨化,模具孔径8mm,膨化机转速60rpm,喂料机转速160rpm,套管温度为60℃,挤压膨化后物料含水量为9.6%;Weigh 2 kg of shelled hemp seeds, coarsely pulverize and extrude and expand, the die aperture is 8mm, the speed of the extruder is 60rpm, the speed of the feeder is 160rpm, the temperature of the casing is 60°C, and the water content of the material after extrusion is 9.6%;
取挤压膨化后的火麻仁,经粉碎机粉碎再过碾磨机碾磨至平均粒径≤50μm;称量1kg,加入8L去离子水,搅拌均匀后调节体系pH至8.5,温度为65℃,提取20min;Take the extruded hemp seeds, pulverize them with a pulverizer, and then grind them with a mill until the average particle size is ≤50 μm; weigh 1kg, add 8L deionized water, stir evenly, adjust the pH of the system to 8.5, and the temperature is 65 ℃, extract for 20min;
然后调节体系pH至8.5,加入碱性蛋白酶Alcalase 2.4L(加入量为火麻仁重量的2%),作用4小时后,加入中性蛋白酶Alphalase(加入量为火麻仁重量的0.5%),搅拌酶解3h得到酶解液;Regulate system pH to 8.5 then, add alkaline protease Alcalase 2.4L (add-on is 2% of hemp seed weight), after effecting 4 hours, add neutral protease Alphalase (add-on is 0.5% of hemp seed weight), Stir the enzymolysis for 3h to obtain the enzymolysis solution;
将得到酶解液温度升至90℃并保持10min灭酶,采用三相离心机离心分,酶解液分为清油、液相及残渣三层;清油得率为88.67%,总油得率为91.73%。Raise the temperature of the enzymolysis solution to 90°C and keep it for 10 minutes to inactivate the enzyme, and use a three-phase centrifuge to separate the enzymolysis solution into three layers: clear oil, liquid phase and residue; the yield of clear oil is 88.67%, and the yield of total oil is 91.73%.
所得液相经过滤、加入甜味剂蔗糖(加入量为液相重量的10%),在50Mpa下均质(2min/次,2次)、灌装,121℃灭菌15min,冷却后得到饮料。饮料中植物蛋白含量4.97%,饮料具有特有的烘培香味The obtained liquid phase is filtered, added with sweetener sucrose (the added amount is 10% of the liquid phase weight), homogenized at 50Mpa (2min/time, 2 times), filled, sterilized at 121°C for 15min, and obtained beverage after cooling . The vegetable protein content in the beverage is 4.97%, and the beverage has a unique roasted aroma
实施例6-8Example 6-8
同实施例1,其不同之处仅在于:所述碱性蛋白酶分别为FoodPro蛋白酶、2709碱性蛋白酶或木瓜蛋白酶。With embodiment 1, its difference is only: described alkaline protease is respectively FoodPro protease, 2709 alkaline protease or papain.
实施例9-11Examples 9-11
同实施例1,其不同之处仅在于:所述中性蛋白酶分别为食品级蛋白酶Alphalase、复合风味蛋白酶或蛋白酶Neutrase。Same as Example 1, the only difference is that the neutral proteases are food-grade protease Alphalase, compound flavor protease or protease Neutrase respectively.
实施例10Example 10
采用现有技术中CN102816631A公开的一种酸法挤压膨化水酶法提取火麻籽油脂的液相,将液相经过滤、加入甜味剂蔗糖(加入量为液相重量的10%),在50Mpa下均质(2min/次,2次)、灌装,121℃灭菌15min,冷却后得到饮料。饮料产生絮凝,不能成为稳定均一的饮品体系,且略带不良的刺鼻味道。The liquid phase of the hemp seed oil is extracted by an acid-extrusion-expanding water enzymatic method disclosed in CN102816631A in the prior art, the liquid phase is filtered, and the sweetener sucrose is added (the addition amount is 10% of the liquid phase weight), Homogenize under 50Mpa (2min/time, twice), fill, sterilize at 121°C for 15min, and obtain beverage after cooling. The beverage produces flocculation, cannot become a stable and uniform beverage system, and has a slightly undesirable pungent taste.
显然,本发明的上述实施例仅仅是为清楚地说明本发明所作的举例,而并非是对本发明的实施方式的限定,对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其它不同形式的变化或变动,这里无法对所有的实施方式予以穷举,凡是属于本发明的技术方案所引伸出的显而易见的变化或变动仍处于本发明的保护范围之列。Apparently, the above-mentioned embodiments of the present invention are only examples for clearly illustrating the present invention, and are not intended to limit the implementation of the present invention. Those of ordinary skill in the art can also make It is impossible to exhaustively list all the implementation modes here, and any obvious changes or changes derived from the technical solutions of the present invention are still within the scope of protection of the present invention.
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