CN114395441A - A kind of extraction method of peony stamen oil - Google Patents
A kind of extraction method of peony stamen oil Download PDFInfo
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- 241000736199 Paeonia Species 0.000 title claims abstract description 129
- 235000006484 Paeonia officinalis Nutrition 0.000 title claims abstract description 129
- 238000000605 extraction Methods 0.000 title claims abstract description 42
- 239000003921 oil Substances 0.000 claims abstract description 87
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 60
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 48
- 238000000034 method Methods 0.000 claims abstract description 37
- 238000010992 reflux Methods 0.000 claims abstract description 22
- 239000010779 crude oil Substances 0.000 claims abstract description 21
- 238000010438 heat treatment Methods 0.000 claims abstract description 21
- 238000009210 therapy by ultrasound Methods 0.000 claims abstract description 15
- 239000012153 distilled water Substances 0.000 claims abstract description 13
- 238000000926 separation method Methods 0.000 claims abstract description 11
- 238000007670 refining Methods 0.000 claims abstract description 9
- 238000001035 drying Methods 0.000 claims abstract description 4
- 238000007873 sieving Methods 0.000 claims abstract 3
- 235000019441 ethanol Nutrition 0.000 claims abstract 2
- 238000005303 weighing Methods 0.000 claims abstract 2
- 238000004821 distillation Methods 0.000 claims description 8
- 235000000346 sugar Nutrition 0.000 abstract description 14
- 239000012535 impurity Substances 0.000 abstract description 6
- 102000004169 proteins and genes Human genes 0.000 abstract description 6
- 108090000623 proteins and genes Proteins 0.000 abstract description 6
- 239000002994 raw material Substances 0.000 abstract description 3
- 239000012178 vegetable wax Substances 0.000 abstract description 3
- 235000019198 oils Nutrition 0.000 description 65
- 241000196324 Embryophyta Species 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- 238000003825 pressing Methods 0.000 description 3
- 238000002604 ultrasonography Methods 0.000 description 3
- 238000002137 ultrasound extraction Methods 0.000 description 3
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 238000006911 enzymatic reaction Methods 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 238000011031 large-scale manufacturing process Methods 0.000 description 2
- 238000002791 soaking Methods 0.000 description 2
- 238000000638 solvent extraction Methods 0.000 description 2
- 238000001256 steam distillation Methods 0.000 description 2
- 150000008163 sugars Chemical class 0.000 description 2
- 238000003815 supercritical carbon dioxide extraction Methods 0.000 description 2
- YYGNTYWPHWGJRM-UHFFFAOYSA-N (6E,10E,14E,18E)-2,6,10,15,19,23-hexamethyltetracosa-2,6,10,14,18,22-hexaene Chemical compound CC(C)=CCCC(C)=CCCC(C)=CCCC=C(C)CCC=C(C)CCC=C(C)C YYGNTYWPHWGJRM-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- BHEOSNUKNHRBNM-UHFFFAOYSA-N Tetramethylsqualene Natural products CC(=C)C(C)CCC(=C)C(C)CCC(C)=CCCC=C(C)CCC(C)C(=C)CCC(C)C(C)=C BHEOSNUKNHRBNM-UHFFFAOYSA-N 0.000 description 1
- 239000004480 active ingredient Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 230000000975 bioactive effect Effects 0.000 description 1
- OHJMTUPIZMNBFR-UHFFFAOYSA-N biuret Chemical compound NC(=O)NC(N)=O OHJMTUPIZMNBFR-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 235000005487 catechin Nutrition 0.000 description 1
- 150000001765 catechin Chemical class 0.000 description 1
- ADRVNXBAWSRFAJ-UHFFFAOYSA-N catechin Natural products OC1Cc2cc(O)cc(O)c2OC1c3ccc(O)c(O)c3 ADRVNXBAWSRFAJ-UHFFFAOYSA-N 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- PRAKJMSDJKAYCZ-UHFFFAOYSA-N dodecahydrosqualene Natural products CC(C)CCCC(C)CCCC(C)CCCCC(C)CCCC(C)CCCC(C)C PRAKJMSDJKAYCZ-UHFFFAOYSA-N 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003925 fat Substances 0.000 description 1
- 229930003935 flavonoid Natural products 0.000 description 1
- 235000017173 flavonoids Nutrition 0.000 description 1
- 150000002215 flavonoids Chemical class 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 235000014593 oils and fats Nutrition 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- OQUKIQWCVTZJAF-UHFFFAOYSA-N phenol;sulfuric acid Chemical compound OS(O)(=O)=O.OC1=CC=CC=C1 OQUKIQWCVTZJAF-UHFFFAOYSA-N 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 229940031439 squalene Drugs 0.000 description 1
- TUHBEKDERLKLEC-UHFFFAOYSA-N squalene Natural products CC(=CCCC(=CCCC(=CCCC=C(/C)CCC=C(/C)CC=C(C)C)C)C)C TUHBEKDERLKLEC-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 235000019871 vegetable fat Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
Classifications
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- 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
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
-
- 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
-
- 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
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/106—Production of fats or fatty oils from raw materials by extracting using ultra-sounds
-
- 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
- C11B1/10—Production of fats or fatty oils from raw materials by extracting
- C11B1/108—Production of fats or fatty oils from raw materials by extracting after-treatment, e.g. of miscellae
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- 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
- C11B3/00—Refining fats or fatty oils
- C11B3/001—Refining fats or fatty oils by a combination of two or more of the means hereafter
-
- 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
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
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- Fats And Perfumes (AREA)
Abstract
Description
技术领域technical field
本发明属于化妆品领域,特别涉及一种牡丹花蕊油的提取方法。The invention belongs to the field of cosmetics, in particular to a method for extracting peony stamen oil.
背景技术Background technique
牡丹花蕊富含角鲨烯、儿茶素、黄酮化合物和多糖等多种活性成分,且含有大量矿物质和微量元素。关于牡丹花蕊中生物活性成分的定性定量研究已经有了初步进展。Peony stamens are rich in various active ingredients such as squalene, catechins, flavonoids and polysaccharides, and contain a large amount of minerals and trace elements. Preliminary progress has been made in the qualitative and quantitative research on bioactive components in peony stamens.
目前植物油脂的提取方法主要有以下几种:(1)压榨法:其工作原理是通过压力使植物细胞破裂,压榨时,油脂就会流出,通过静置或离心就可得到油脂;(2)水酶法:其工作原理是将植物受到机械损伤后,通过添加酶抑制乳化或破乳,使油脂释放到水相中,再通过离心等方法将油相与水相或其他杂质进行分离。(3)溶剂浸提法:是一种利用沸点低、易分离和对油脂具有溶解性的有机溶剂,通过浸泡将油脂提取出来的方法;(4)超临界二氧化碳萃取法:以超临界流体为萃取剂进行活性物质萃取的一种新型分离技术;(5)超声波提取法:一种大于20KHz的声波,工作原理是利用超声波具有波动双重性和能量,能够产生空化现象,加速油脂渗透,提高提取率。At present, the extraction methods of vegetable oils and fats mainly include the following: (1) Pressing method: the working principle is that the plant cells are ruptured by pressure. When pressing, the oil will flow out, and the oil can be obtained by standing or centrifuging; (2) Water enzymatic method: Its working principle is that after the plant is mechanically damaged, the oil is released into the water phase by adding enzymes to inhibit emulsification or demulsification, and then the oil phase is separated from the water phase or other impurities by centrifugation and other methods. (3) Solvent extraction method: It is a method of extracting oil by soaking by using an organic solvent with a low boiling point, easy separation and solubility in oil; (4) Supercritical carbon dioxide extraction method: using supercritical fluid as the A new separation technology for extracting active substances with extractant; (5) Ultrasonic extraction method: a sound wave greater than 20KHz, the working principle is to use ultrasonic waves with duality and energy, which can produce cavitation, accelerate oil penetration, and improve extraction rate.
传统的压榨法制备的油脂不纯,保存期短,油料综合利用率不高;水酶法虽然工艺简单,设备要求低,但是工艺所需时间较长,酶的价格较高,不适合大规模生产;超临界二氧化碳萃取法无毒无害,萃取过程稳定,但设备成本高,不易操作;超声波提取法提取效率高,提取温度低,但超声提取罐体积不能太大,否则会产生超声空白区;溶剂浸提法出油率较高,操作简单,易于规模化生产和自动化,但提取的油脂可能杂质较多,有溶剂残留。The oil prepared by the traditional pressing method is impure, the shelf life is short, and the comprehensive utilization rate of oil plants is not high; although the water enzymatic method has a simple process and low equipment requirements, the process requires a long time and the price of the enzyme is high, which is not suitable for large-scale production. Production; supercritical carbon dioxide extraction method is non-toxic and harmless, and the extraction process is stable, but the equipment cost is high and it is not easy to operate; the ultrasonic extraction method has high extraction efficiency and low extraction temperature, but the volume of the ultrasonic extraction tank should not be too large, otherwise an ultrasonic blank area will be generated ; The solvent extraction method has high oil yield, simple operation, easy large-scale production and automation, but the extracted oil may have many impurities and solvent residues.
因此,亟需提供一种牡丹花蕊油的提取方法,以解决现有技术中提取率低,油脂杂质多和溶剂残留问题。Therefore, there is an urgent need to provide a method for extracting peony stamen oil to solve the problems of low extraction rate, many grease impurities and solvent residues in the prior art.
发明内容SUMMARY OF THE INVENTION
针对上述问题,本发明提供一种牡丹花蕊油的提取方法,采用组合提取牡丹花蕊油的方法,通过超声提高油脂提取率,醇类浸提提取油脂,再利用水蒸汽法减少油脂中植物蜡,糖类和蛋白质等杂质。高超声功率可以提高传质速率,加快溶剂与植物原料的接触速度,同时超声也会对植物细胞组织产生一种物理剪切力,使之变性破碎,并释放出内含物,加快后续溶液浸提的提取速率,提高提取率。In view of the above problems, the present invention provides a method for extracting peony stamen oil, which adopts a combined method for extracting peony stamen oil, improves the oil extraction rate by ultrasound, extracts oil by alcohol leaching, and then uses water vapor to reduce vegetable wax in oil, Impurities such as sugars and proteins. High ultrasonic power can increase the mass transfer rate and speed up the contact speed between the solvent and the plant raw material. At the same time, the ultrasonic will also produce a physical shear force on the plant cell tissue, denature and break it, and release the contents, which will speed up the subsequent soaking of the solution. Improve the extraction rate and improve the extraction rate.
一种牡丹花蕊油的提取方法,所述提取方法包括以下步骤:A kind of extraction method of peony stamen oil, described extraction method comprises the following steps:
干燥牡丹花蕊后进行粉碎过筛;After drying the peony stamens, pulverize and sieve;
称取一定量粉碎过筛后的牡丹花蕊放入滤纸包,加入一定量的无水乙醇,进行超声处理;Weigh a certain amount of pulverized and sieved peony stamens into a filter paper bag, add a certain amount of absolute ethanol, and carry out ultrasonic treatment;
将超声处理后的滤纸包及无水乙醇加入索氏提取器中,水浴加热回流提取牡丹花蕊油;The filter paper bag after ultrasonic treatment and absolute ethanol are added to the Soxhlet extractor, and the peony stamen oil is extracted by heating and refluxing in a water bath;
收集所述索氏提取器中的乙醇,减压浓缩得到牡丹花蕊粗油;The ethanol in the Soxhlet extractor is collected, and concentrated under reduced pressure to obtain the crude oil of peony stamens;
向所述牡丹花蕊粗油中加入一定量蒸馏水,蒸馏精制后进行油水分离,得到澄清透明的牡丹花蕊油。A certain amount of distilled water is added to the crude oil of peony stamens, and oil-water separation is carried out after distillation and refining to obtain clear and transparent peony stamen oil.
进一步地,所述超声处理的条件是40KHz,50W。Further, the conditions of the ultrasonic treatment are 40KHz, 50W.
进一步地,所述超声处理的时间为20~60分钟。Further, the time of the ultrasonic treatment is 20-60 minutes.
进一步地,所述干燥牡丹花蕊后进行粉碎过筛,牡丹花蕊粉碎至40~80目。Further, the dried peony stamens are crushed and sieved, and the peony stamens are crushed to 40-80 mesh.
进一步地,further,
所述牡丹花蕊的质量和无水乙醇的体积比例为1:4~1:10。The mass ratio of the peony stamens to the volume of absolute ethanol is 1:4 to 1:10.
进一步地,further,
所述水浴加热回流的温度为50~80℃。The temperature at which the water bath is heated and refluxed is 50-80°C.
进一步地,further,
所述水浴加热回流提取牡丹花蕊油的提取时间为2~6小时。The extraction time of the water bath heating and refluxing to extract the peony stamen oil is 2-6 hours.
进一步地,further,
所述牡丹花蕊粗油的质量和蒸馏水的体积比例为1:4~1:8。The mass ratio of the crude oil of peony stamens to the volume ratio of distilled water is 1:4-1:8.
进一步地,牡丹花蕊油的提取率采用以下公式计算得到:Further, the extraction rate of peony stamen oil is calculated by the following formula:
进一步地,further,
所述牡丹花蕊油的提取率为15.6%~22.1%。The extraction rate of the peony stamen oil is 15.6%-22.1%.
本发明提供的一种牡丹花蕊油的提取方法,采用组合提取牡丹花蕊油的提取方法,最大限度的从牡丹花蕊中提取牡丹花蕊油,提高了原料利用率,减少了油脂中植物蜡,糖类和蛋白质等杂质。本发明的其它特征和优点将在随后的说明书中阐述,并且,部分地从说明书中变得显而易见,或者通过实施本发明而了解。本发明的目的和其他优点可通过在说明书以及权利要求书中所指出的结构来实现和获得。The invention provides a method for extracting peony stamen oil, which adopts a combined extraction method for extracting peony stamen oil, extracts peony stamen oil from peony stamens to the maximum extent, improves the utilization rate of raw materials, and reduces vegetable waxes and sugars in oils and fats. and impurities such as protein. Other features and advantages of the present invention will be set forth in the description which follows, and in part will be apparent from the description, or may be learned by practice of the invention. The objectives and other advantages of the invention may be realized and attained by the structure pointed out in the description and claims.
具体实施方式Detailed ways
为使本发明的目的、技术方案和优点更加清楚,下面将结合本发明实施例,对本发明中的技术方案进行清楚、完整地说明,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the objectives, technical solutions and advantages of the present invention clearer, the technical solutions in the present invention will be clearly and completely described below with reference to the embodiments of the present invention. Obviously, the described embodiments are part of the embodiments of the present invention, and Not all examples. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
本发明提供一种牡丹花蕊油的提取方法,提取方法包括以下步骤:The invention provides a method for extracting peony stamen oil, which comprises the following steps:
干燥牡丹花蕊后进行粉碎过筛,牡丹花蕊要粉碎至40~80目;After drying the peony stamens, crush and sieve, and crush the peony stamens to 40-80 mesh;
称取一定量粉碎过筛后的牡丹花蕊放入滤纸包,加入一定量的无水乙醇,进行超声处理;Weigh a certain amount of pulverized and sieved peony stamens into a filter paper bag, add a certain amount of absolute ethanol, and carry out ultrasonic treatment;
其中,超声处理的条件是40KHz,50W,超声时间是20~60分钟;牡丹花蕊的质量和无水乙醇的体积比例为1:4~1:10(g:mL)。Wherein, the conditions of ultrasonic treatment are 40KHz, 50W, and the ultrasonic time is 20-60 minutes; the mass ratio of peony stamens to the volume of absolute ethanol is 1:4-1:10 (g:mL).
将超声处理后的滤纸包及无水乙醇加入索氏提取器中,水浴加热回流提取牡丹花蕊油,其中,水浴加热回流的温度为50~80℃,提取牡丹花蕊油的提取时间为2~6小时;The filter paper bag after the ultrasonic treatment and absolute ethanol are added to the Soxhlet extractor, and the peony stamen oil is extracted by heating and refluxing in a water bath, wherein the temperature of the water bath heating and refluxing is 50-80 DEG C, and the extraction time for extracting the peony stamen oil is 2-6 Hour;
收集索氏提取器中的乙醇,减压浓缩得到牡丹花蕊粗油;The ethanol in the Soxhlet extractor was collected, and concentrated under reduced pressure to obtain the crude oil of peony stamens;
向牡丹花蕊粗油中加入一定量蒸馏水,蒸馏精制后进行油水分离,得到澄清透明的牡丹花蕊油。其中,牡丹花蕊粗油的质量和蒸馏水的体积比例为1:4~1:8。A certain amount of distilled water is added to the crude oil of peony stamens, and oil-water separation is carried out after distillation and refining to obtain clear and transparent peony stamen oil. Wherein, the mass ratio of the crude oil of peony stamens to the volume of distilled water is 1:4 to 1:8.
牡丹花蕊油的提取率采用以下公式计算得到,采用本发明提供的方法得到的牡丹花蕊油提取率为15.6%~22.1%。The extraction rate of peony stamen oil is calculated by the following formula, and the extraction rate of peony stamen oil obtained by the method provided by the present invention is 15.6% to 22.1%.
实施例1Example 1
干燥牡丹花蕊进行粉碎过40目筛;称取50g粉碎过筛后的牡丹花蕊放入滤纸包,加入200mL无水乙醇,在40KHz,50W条件下超声处理20分钟;再将上述滤纸包及无水乙醇加入索氏提取器中,水浴加热回流(0.075MPa)提取牡丹花蕊油,其中,水浴加热回流的温度为50℃,提取牡丹花蕊油的提取时间为2小时;收集索氏提取器中的乙醇,减压浓缩得到牡丹花蕊粗油;进而向牡丹花蕊粗油中按料液比1:4(g:mL)加入一定量蒸馏水,蒸馏精制后进行油水分离,得到澄清透明的牡丹花蕊油。The dried peony stamens were pulverized and passed through a 40-mesh sieve; 50g of pulverized and sieved peony stamens were weighed and put into a filter paper bag, 200 mL of absolute ethanol was added, and sonicated for 20 minutes at 40KHz, 50W; then the above-mentioned filter paper bag and anhydrous Ethanol was added to the Soxhlet extractor, and the peony stamen oil was extracted by heating and refluxing in a water bath (0.075MPa), wherein the temperature of the water bath heating and refluxing was 50°C, and the extraction time for extracting the peony stamen oil was 2 hours; the ethanol in the Soxhlet extractor was collected. , concentrated under reduced pressure to obtain peony stamen crude oil; and then add a certain amount of distilled water to the peony stamen crude oil by a material-to-liquid ratio of 1:4 (g:mL), and carry out oil-water separation after distillation and refining to obtain clear and transparent peony stamen oil.
通过上述方法,经计算得到牡丹花蕊油的提取率为15.6%。Through the above method, the extraction rate of peony stamen oil was calculated to be 15.6%.
实施例2Example 2
干燥牡丹花蕊进行粉碎过60目筛;称取50g粉碎过筛后的牡丹花蕊放入滤纸包,加入300mL无水乙醇,在40KHz,50W条件下超声处理20分钟;再将上述滤纸包及无水乙醇加入索氏提取器中,水浴加热回流(0.075MPa)提取牡丹花蕊油,其中,水浴加热回流的温度为60℃,提取牡丹花蕊油的提取时间为3小时;收集索氏提取器中的乙醇,减压浓缩得到牡丹花蕊粗油;进而向牡丹花蕊粗油中按料液比1:5(g:mL)加入一定量蒸馏水,蒸馏精制后进行油水分离,得到澄清透明的牡丹花蕊油。The dried peony stamens were pulverized and passed through a 60-mesh sieve; 50g of pulverized and sieved peony stamens were weighed and put into a filter paper bag, 300 mL of absolute ethanol was added, and sonicated for 20 minutes at 40KHz, 50W; then the above-mentioned filter paper bag and anhydrous Ethanol was added to the Soxhlet extractor, and the peony stamen oil was extracted by heating and refluxing in a water bath (0.075MPa), wherein the temperature of the water bath heating and refluxing was 60°C, and the extraction time for extracting the peony stamen oil was 3 hours; the ethanol in the Soxhlet extractor was collected. , concentrated under reduced pressure to obtain peony stamen crude oil; and then add a certain amount of distilled water to the peony stamen crude oil by a material-to-liquid ratio of 1:5 (g:mL), and carry out oil-water separation after distillation and refining to obtain clear and transparent peony stamen oil.
通过上述方法,经计算得到牡丹花蕊油的提取率为18.3%。Through the above method, the extraction rate of peony stamen oil was calculated to be 18.3%.
实施例3Example 3
干燥牡丹花蕊进行粉碎过80目筛;称取50g粉碎过筛后的牡丹花蕊放入滤纸包,加入300mL无水乙醇,在40KHz,50W条件下超声处理30分钟;再将上述滤纸包及无水乙醇加入索氏提取器中,水浴加热回流(0.075MPa)提取牡丹花蕊油,其中,水浴加热回流的温度为65℃,提取牡丹花蕊油的提取时间为4小时;收集索氏提取器中的乙醇,减压浓缩得到牡丹花蕊粗油;进而向牡丹花蕊粗油中按料液比1:7(g:mL)加入一定量蒸馏水,蒸馏精制后进行油水分离,得到澄清透明的牡丹花蕊油。The dried peony stamens were pulverized and passed through an 80-mesh sieve; 50g of pulverized and sieved peony stamens were weighed and put into a filter paper bag, 300 mL of absolute ethanol was added, and sonicated for 30 minutes at 40KHz, 50W; then the above-mentioned filter paper bag and anhydrous Ethanol was added to the Soxhlet extractor, and the peony stamen oil was extracted by heating and refluxing in a water bath (0.075MPa), wherein the temperature of the water bath heating and refluxing was 65°C, and the extraction time for extracting the peony stamen oil was 4 hours; the ethanol in the Soxhlet extractor was collected. , concentrated under reduced pressure to obtain peony stamen crude oil; then add a certain amount of distilled water to the peony stamen crude oil by a material-to-liquid ratio of 1:7 (g:mL), and carry out oil-water separation after distillation and refining to obtain clear and transparent peony stamen oil.
通过上述方法,经计算得到牡丹花蕊油的提取率为22.1%。Through the above method, the extraction rate of peony stamen oil was calculated to be 22.1%.
实施例4Example 4
干燥牡丹花蕊进行粉碎过80目筛;称取50g粉碎过筛后的牡丹花蕊放入滤纸包,加入300mL无水乙醇,在40KHz,50W条件下超声处理60分钟;再将上述滤纸包及无水乙醇加入索氏提取器中,水浴加热回流(0.075MPa)提取牡丹花蕊油,其中,水浴加热回流的温度为80℃,提取牡丹花蕊油的提取时间为6小时;收集索氏提取器中的乙醇,减压浓缩得到牡丹花蕊粗油;进而向牡丹花蕊粗油中按料液比1:10(g:mL)加入一定量蒸馏水,蒸馏精制后进行油水分离,得到澄清透明的牡丹花蕊油。The dried peony stamens were pulverized and passed through an 80-mesh sieve; 50g of pulverized and sieved peony stamens were weighed and put into a filter paper bag, 300 mL of absolute ethanol was added, and sonicated for 60 minutes at 40KHz, 50W; then the above-mentioned filter paper bag and anhydrous Ethanol was added to the Soxhlet extractor, and the peony stamen oil was extracted by heating and refluxing in a water bath (0.075MPa), wherein the temperature of the water bath heating and refluxing was 80°C, and the extraction time for extracting the peony stamen oil was 6 hours; the ethanol in the Soxhlet extractor was collected. , concentrated under reduced pressure to obtain peony stamen crude oil; then add a certain amount of distilled water to the peony stamen crude oil by a material-to-liquid ratio of 1:10 (g:mL), and carry out oil-water separation after distillation and refining to obtain clear and transparent peony stamen oil.
通过上述方法,经计算得到牡丹花蕊油的提取率为20.5%。Through the above method, the extraction rate of peony stamen oil was calculated to be 20.5%.
实施例5Example 5
干燥牡丹花蕊进行粉碎过80目筛;称取50g粉碎过筛后的牡丹花蕊放入滤纸包,加入300mL无水乙醇,将上述滤纸包及无水乙醇加入索氏提取器中,水浴加热回流提取牡丹花蕊油,其中,水浴加热回流(0.075MPa)的温度为65℃,提取牡丹花蕊油的提取时间为4小时;收集索氏提取器中的乙醇,减压浓缩得到牡丹花蕊粗油;进而向牡丹花蕊粗油中按料液比1:7(g:mL)加入一定量蒸馏水,蒸馏精制后进行油水分离,得到澄清透明的牡丹花蕊油。The dried peony stamens were pulverized and passed through an 80-mesh sieve; 50 g of pulverized and sieved peonies were weighed and put into a filter paper bag, 300 mL of absolute ethanol was added, the above-mentioned filter paper bag and absolute ethanol were added to a Soxhlet extractor, and the extraction was performed by heating and refluxing in a water bath. Peony stamen oil, wherein, the temperature of heating and refluxing (0.075MPa) in a water bath is 65° C., and the extraction time for extracting peony stamen oil is 4 hours; the ethanol in the Soxhlet extractor is collected, and concentrated under reduced pressure to obtain peony stamen crude oil; A certain amount of distilled water is added to the crude oil of peony stamens according to a material-liquid ratio of 1:7 (g:mL), and after distillation and refining, oil-water separation is carried out to obtain clear and transparent peony stamen oil.
通过上述方法,经计算得到牡丹花蕊油的提取率为13.5%。Through the above method, the extraction rate of peony stamen oil was calculated to be 13.5%.
实施例6Example 6
为了验证加入蒸馏水蒸馏精制对牡丹花蕊油中总糖、乙醇残留和总蛋白含量的影响。In order to verify the effect of adding distilled water on the content of total sugar, ethanol residue and total protein in peony oil.
干燥牡丹花蕊进行粉碎过80目筛;称取50g粉碎过筛后的牡丹花蕊放入滤纸包,加入300mL无水乙醇,在40KHz,50W条件下超声处理30分钟;再将上述滤纸包及无水乙醇加入索氏提取器中,水浴加热回流(0.075MPa)提取牡丹花蕊油,其中,水浴加热回流的温度为65℃,提取牡丹花蕊油的提取时间为4小时;收集索氏提取器中的乙醇,减压浓缩得到牡丹花蕊油。The dried peony stamens were pulverized and passed through an 80-mesh sieve; 50g of pulverized and sieved peony stamens were weighed and put into a filter paper bag, 300 mL of absolute ethanol was added, and sonicated for 30 minutes at 40KHz, 50W; then the above-mentioned filter paper bag and anhydrous Ethanol was added to the Soxhlet extractor, and the peony stamen oil was extracted by heating and refluxing in a water bath (0.075MPa), wherein the temperature of the water bath heating and refluxing was 65°C, and the extraction time for extracting the peony stamen oil was 4 hours; the ethanol in the Soxhlet extractor was collected. , concentrated under reduced pressure to obtain peony stamen oil.
通过上述方法,经计算得到牡丹花蕊油的提取率为23.8%。Through the above method, the extraction rate of peony stamen oil was calculated to be 23.8%.
由实施例1-5可以得出,在回流萃取前先将牡丹花蕊和溶剂进行超声处理,有助于提高提取率。对比之下,优选条件为花蕊粉碎至80目、花蕊与乙醇质量比1:6、40KW,50Hz处理30分钟、65℃加热回流提取4小时。From Examples 1-5, it can be concluded that ultrasonic treatment of peony stamens and solvent before reflux extraction is helpful to improve the extraction rate. In contrast, the preferred conditions are that the stamens are crushed to 80 mesh, the mass ratio of stamens to ethanol is 1:6, 40 KW, 50 Hz treatment for 30 minutes, and heating and refluxing extraction at 65°C for 4 hours.
从实施例1-4可知,实施例3是牡丹花蕊油提取的优选条件,因此,选取实施例3与实施例5、实施例6进行比较,来验证组合提取方法对牡丹花蕊油中总糖、乙醇残留和总蛋白含量的影响。总糖含量采用苯酚-硫酸法进行测定,以葡萄糖为标准品制作标准曲线,表1为实施例3、5和6的总糖含量结果。As can be seen from Examples 1-4, Example 3 is the optimal condition for the extraction of peony oil. Therefore, Example 3 was selected to compare with Example 5 and Example 6 to verify that the combined extraction method had a significant effect on the total sugar, total sugar in peony oil, Effects of ethanol residues and total protein content. The total sugar content was measured by the phenol-sulfuric acid method, and a standard curve was prepared with glucose as the standard substance. Table 1 shows the results of the total sugar content of Examples 3, 5 and 6.
表1各实施例总糖含量测定Table 1 Determination of total sugar content of each embodiment
由表1可以得出,实施例3总糖含量比实施例6低,这说明经过水汽蒸馏可以有效降低牡丹花蕊油中的总糖含量;实施例3总糖含量比实施例5略高,这可能是由于超声作用导致。As can be drawn from Table 1, the total sugar content of Example 3 is lower than that of Example 6, which shows that the total sugar content in the peony stamen oil can be effectively reduced through steam distillation; the total sugar content of Example 3 is slightly higher than that of Example 5. Possibly due to ultrasound.
采用液相色谱测定各实施例所得牡丹花蕊油中乙醇残留,表2为实施例3、5和6的乙醇残留量。The residual ethanol in the peony oil obtained in each example was determined by liquid chromatography. Table 2 shows the residual amount of ethanol in Examples 3, 5 and 6.
表2各实施例乙醇含量测定Table 2 Determination of ethanol content of each embodiment
由表2可以得出,实施例3乙醇残留比实施例6低,这说明经过水汽蒸馏可以有效降低牡丹花蕊油中的乙醇残留;实施例3总糖含量比实施例5略高,这可能是由于超声作用导致。It can be drawn from Table 2 that the ethanol residue in Example 3 is lower than that in Example 6, which shows that the ethanol residue in the peony stamen oil can be effectively reduced through steam distillation; the total sugar content of Example 3 is slightly higher than that of Example 5, which may be due to ultrasound.
采用双缩脲试剂法测定各实施例所得牡丹花蕊油中总蛋白测定,表3为实施例3、5和6的总蛋白测定结果。The biuret reagent method was used to determine the total protein in the peony oil obtained in each example, and Table 3 shows the total protein determination results of Examples 3, 5 and 6.
表3各实施例总蛋白含量测定Table 3 Determination of total protein content of each embodiment
由表3可以得出,实施例3总蛋白含量比实施例5高,和实施例6产别不大,这说明超声处理可以提高牡丹花蕊油中总蛋白含量;但后处理水汽蒸馏对总蛋白含量影响不大。As can be drawn from Table 3, the total protein content of Example 3 is higher than that of Example 5, and is not much different from that of Example 6, which shows that ultrasonic treatment can improve the total protein content in the peony oil; The content has little effect.
尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的精神和范围。Although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: it is still possible to modify the technical solutions described in the foregoing embodiments, or perform equivalent replacements to some of the technical features; and these Modifications or substitutions do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the embodiments of the present invention.
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