CN201208517Y - Natural herbals light-oil heavy-oil extraction device - Google Patents
Natural herbals light-oil heavy-oil extraction device Download PDFInfo
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- CN201208517Y CN201208517Y CNU2008200670709U CN200820067070U CN201208517Y CN 201208517 Y CN201208517 Y CN 201208517Y CN U2008200670709 U CNU2008200670709 U CN U2008200670709U CN 200820067070 U CN200820067070 U CN 200820067070U CN 201208517 Y CN201208517 Y CN 201208517Y
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Abstract
Description
技术领域 technical field
本实用新型属于天然本草类物质的提取技术领域,具体涉及一种适应天然本草轻油和重油两种密度挥发油提取的装置。The utility model belongs to the technical field of extraction of natural herbal substances, and in particular relates to a device suitable for extracting volatile oils with two densities of natural herbal light oil and heavy oil.
背景技术 Background technique
从天然本草中萃取挥发油是很麻烦的过程,因为植物的挥发油含量非常少。所以,需要大量的植物才能提取到少量的挥发油,最终导致挥发油非常昂贵。例如:约3~5吨的玫瑰花瓣,才能萃取1kg玫瑰挥发油;约200kg的新鲜薰衣草,才能萃取1kg薰衣草挥发油;约1吨橙花花瓣,才能萃取1kg橙花挥发油;约3000个柠檬,才能榨出1kg柠檬挥发油;约6~7吨香蜂草,才能提取1kg香蜂草挥发油,是最难萃取的药草挥发油。Extracting volatile oil from natural herbs is a troublesome process because the volatile oil content of plants is very small. Therefore, it takes a lot of plants to extract a small amount of volatile oil, which ends up being very expensive. For example: about 3 to 5 tons of rose petals can extract 1 kg of rose volatile oil; about 200 kg of fresh lavender can extract 1 kg of lavender volatile oil; about 1 ton of orange flower petals can extract 1 kg of neroli volatile oil; about 3000 lemons can be squeezed It takes about 6-7 tons of lemon balm to extract 1kg of lemon volatile oil, which is the most difficult herbal volatile oil to extract.
目前,从天然本草中萃取挥发油的方法很多,一般有以下几种:At present, there are many methods for extracting volatile oil from natural herbal medicines, generally there are the following:
1、水蒸气蒸馏法:此方法操作简单,成本低,是最常用的萃取方法。将新鲜的或经干燥处理的芳香植物原料放到蒸馏器中加热,让植物内的挥发油跟着蒸气蒸发出来。含有挥发油的水蒸气经由导管收集冷却后,蒸气会冷却成液体,再依照水与挥发油的比重、密度的差异而分离出来。剩下来的水分当中,或多或少都有些挥发油溶在里面,这就是所谓的花水,大部分挥发油是以此方法提炼出来的。2、冷冻压缩法(压榨法):此方法专门用来萃取贮藏在果皮部分的挥发油。3、化学溶剂萃取法:此方法是树胶、树脂和花类挥发油的常用萃取方法。4、油脂分离法(脂吸法):此方法是花朵挥发油的昂贵的萃取方法。5、超临界二氧化碳萃取法:此方法是一种十分昂贵的方法。6、浸泡法(为浸泡油):此方法将花朵浸泡在热油中,使植物中的挥发油释放出来,再用过滤法萃取即可。1. Steam distillation: This method is simple to operate and low in cost, and is the most commonly used extraction method. Put the fresh or dried aromatic plant material into the still and heat it, so that the volatile oil in the plant evaporates with the steam. After the water vapor containing volatile oil is collected and cooled through the tube, the vapor will be cooled into liquid, and then separated according to the specific gravity and density difference between water and volatile oil. Among the remaining water, there are more or less volatile oils dissolved in it. This is the so-called flower water, and most of the volatile oils are extracted by this method. 2. Freezing compression method (pressing method): This method is specially used to extract the volatile oil stored in the peel. 3. Chemical solvent extraction: This method is a common extraction method for volatile oils of gums, resins and flowers. 4. Grease separation method (fat suction method): This method is an expensive extraction method of flower volatile oil. 5. Supercritical carbon dioxide extraction method: This method is a very expensive method. 6. Soaking method (soaking oil): In this method, the flowers are soaked in hot oil to release the volatile oil in the plant, and then extracted by filtration.
这六种方法比较而言,目前最常用的,操作简单,成本低的挥发油提取方法是水蒸气蒸馏法。通过水蒸气蒸馏法所得到的挥发油是和水蒸汽一起蒸发出来的,含有挥发油的水蒸气经由导管收集冷却后,蒸气会冷却成液体,再依照水与挥发油的比重、密度的差异而分离出来,从而得到纯净的挥发油。根据挥发油与水密度的比较,挥发油分为轻油和重油两种。即:比水轻的是轻油,比水重的是重油。目前,对于这两种挥发油的提取,采用的是两套不同的装置。这就要求根据挥发油的密度性质,采用不同的装置。对于大型生产而言,仪器的拆卸十分不便,并且有严重的安全隐患。Compared with these six methods, the most commonly used, simple and low-cost essential oil extraction method is steam distillation. The volatile oil obtained by the steam distillation method is evaporated together with the water vapor. After the water vapor containing the volatile oil is collected and cooled through a tube, the steam will be cooled into a liquid, and then separated according to the specific gravity and density difference between water and volatile oil. Thereby obtaining pure volatile oil. According to the comparison of the density of volatile oil and water, volatile oil is divided into light oil and heavy oil. That is: light oil is lighter than water, and heavy oil is heavier than water. At present, for the extraction of these two kinds of volatile oils, two sets of different devices are used. This requires the use of different devices according to the density properties of the volatile oil. For large-scale production, the disassembly of the instrument is very inconvenient and has serious safety hazards.
实用新型内容Utility model content
针对现有技术的上述不足,本实用新型要解决的技术问题是提供一种天然本草轻油重油提取器,它将轻油提取装置和重油提取装置融合在一起,适应天然本草轻油和重油两种密度挥发油的提取。Aiming at the above-mentioned deficiencies in the prior art, the technical problem to be solved by the utility model is to provide a natural herbal light oil heavy oil extractor, which integrates the light oil extraction device and the heavy oil extraction device, and is suitable for both natural herbal light oil and heavy oil. Extraction of volatile oils of various densities.
本实用新型的技术方案是:天然本草轻油重油提取器含有冷凝管、蒸气收集管、水循环回流管、蒸馏器、油水分离器,水循环回流管中设置一个控制阀,蒸气收集管与油水分离器之间的夹角A为65~120度,蒸气收集管与水循环回流管之间的夹角B为15~75度。The technical scheme of the utility model is: the extractor of natural herbal light oil and heavy oil contains a condensation pipe, a steam collection pipe, a water circulation return pipe, a distiller, and an oil-water separator, and a control valve is arranged in the water circulation return pipe, and the steam collection pipe and the oil-water separator The included angle A between them is 65-120 degrees, and the included angle B between the steam collecting pipe and the water circulation return pipe is 15-75 degrees.
所述的蒸馏器的体积为500—50,000ml。所述的蒸汽收集管外径为10—30mm,内径为5—20mm。所述的冷凝管为15—50cm蛇形冷凝管。所述的油水分离器的体积为10—500mL。所述的水循环回流管的外径为10—30mm,内径为5—20mm。The volume of the distiller is 500-50,000ml. The outer diameter of the steam collecting pipe is 10-30mm, and the inner diameter is 5-20mm. The condensing pipe is a 15-50cm serpentine condensing pipe. The volume of the oil-water separator is 10-500mL. The outer diameter of the water circulation return pipe is 10-30mm, and the inner diameter is 5-20mm.
本实用新型设计合理,结构简单,操作方便,将轻油提取装置和重油提取装置融合在一起,适应天然本草轻油和重油两种密度挥发油的提取,既满足实验研究需要,又满足规模化生产的要求;满足不同密度挥发油的提取。The utility model is reasonable in design, simple in structure and convenient in operation. It integrates the light oil extraction device and the heavy oil extraction device, and is suitable for the extraction of volatile oils with two densities of natural herbal light oil and heavy oil. It not only meets the needs of experimental research, but also meets the needs of large-scale production. Requirements; meet the extraction of different densities of volatile oils.
附图说明 Description of drawings
附图1是本实用新型一实施例结构示意图。Accompanying drawing 1 is the structural representation of an embodiment of the utility model.
附图中标记分述如下:1—蒸馏器;2—蒸气收集管;3—冷凝管;4—油水分离器;5—水循环回流管;6—排放阀;7—控制阀。The marks in the accompanying drawings are described as follows: 1—distiller; 2—steam collection pipe; 3—condensation pipe; 4—oil-water separator; 5—water circulation return pipe; 6—discharging valve; 7—control valve.
具体实施方式 Detailed ways
下面结合附图对本实用新型的具体实施方式作进一步详细的描述。如附图1所示,在水循环回流管5中设置有控制阀7,蒸气收集管2与油水分离器4之间的夹角A为75度,蒸气收集管2与回循环回流管5之间的夹角B为65度。在使用本实用新型进行工作时,将天然本草和水放入蒸馏器1中,天然本草和水的体积介于蒸馏器1体积的1/2—3/4。在提取时,天然本草和水在蒸馏器1中加热至沸腾,携带有挥发油的水蒸气经蒸汽收集管道2收集,上升至冷凝管3。经冷凝后的油水混合液滴落入油水分离器4中,并完成油水分离。对于轻油而言,油水分离后挥发油位于上层,水位于下层;此时,将水循环回流管道5上的阀门6打开,下层的水经回流管道5流回蒸馏器1,循环使用。对于重油而言,油水分离后挥发油位于下层,水位于上层,此时,将水循环回流管道上的阀门6关闭,上层的水经蒸汽收集管2流回蒸馏器1,循环使用。Below in conjunction with accompanying drawing, the specific embodiment of the present utility model is described in further detail. As shown in Figure 1, a control valve 7 is provided in the water circulation return pipe 5, the angle A between the
下面是采用本实用新型的图示提取器进行天然本草轻油重油提取的实例:Below is the example that adopts the pictorial extractor of the present utility model to carry out natural herbal light oil heavy oil extraction:
实例1、小茴香油(轻油)提取:Example 1, cumin oil (light oil) extraction:
选用2,000mL蒸馏器中,外径为10mm,内径为5mm的蒸汽收集管道,25cm的蛇形冷凝管,20mL的油水分离器和外径为10mm,内径为5mm的水循环回流管道构成,用以提取小茴香轻油。In a 2,000mL distiller, a steam collection pipe with an outer diameter of 10mm and an inner diameter of 5mm, a 25cm serpentine condenser, a 20mL oil-water separator and a water circulation return pipe with an outer diameter of 10mm and an inner diameter of 5mm are used to extract Cumin light oil.
取200g小茴香,1,000g水放入蒸馏器中,静置24小时后,加热至微沸。提取5小时后,静置12小时,收集油水分离器中的小茴香油。所得到的小茴香油为黄绿色油状液体,产率为2.1%,密度为0.92,折光为1.48。Take 200g of cumin and 1,000g of water into a distiller, let it stand for 24 hours, then heat to a slight boil. After extracting for 5 hours, stand still for 12 hours to collect the cumin oil in the oil-water separator. The obtained fennel oil was a yellow-green oily liquid with a yield of 2.1%, a density of 0.92 and a refractive index of 1.48.
2、丁香花蕾油(重油)提取:2. Extraction of clove bud oil (heavy oil):
选用5,000mL蒸馏器中,外径为20mm,内径为10mm的蒸汽收集管道,50cm的蛇形冷凝管,50mL的油水分离器和外径为20mm,内径为10mm的水循环回流管道构成,用以提取丁香花蕾重油。In a 5,000mL distiller, a steam collection pipe with an outer diameter of 20mm and an inner diameter of 10mm, a 50cm serpentine condenser, a 50mL oil-water separator and a water circulation return pipe with an outer diameter of 20mm and an inner diameter of 10mm are used to extract Heavy oil of clove buds.
取500g丁香花蕾,3,000g水放入蒸馏器中,静置24小时后,加热至微沸。提取5小时后,静置12小时,收集油水分离器中的丁香花蕾油。所得到的丁香花蕾油为无色油状液体,产率为1.8%,密度为1.05,折光为1.53。Take 500g of clove buds and put 3,000g of water into a distiller, let it stand for 24 hours, then heat to a slight boil. After extracting for 5 hours, stand still for 12 hours to collect the clove bud oil in the oil-water separator. The obtained clove bud oil is a colorless oily liquid with a yield of 1.8%, a density of 1.05 and a refractive index of 1.53.
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| CNU2008200670709U CN201208517Y (en) | 2008-05-12 | 2008-05-12 | Natural herbals light-oil heavy-oil extraction device |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101732893B (en) * | 2010-01-18 | 2014-03-05 | 湖南大学 | A continuous oil-water separation and solvent recycling device for chemical synthesis or azeotropic distillation |
| CN103992880A (en) * | 2014-05-15 | 2014-08-20 | 河北中烟工业有限责任公司 | Volatile oil high-efficiency extraction separator |
| CN106281701A (en) * | 2016-08-17 | 2017-01-04 | 上海清轩生物科技有限公司 | Essential oil extraction device and plants essential oil extracting method |
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2008
- 2008-05-12 CN CNU2008200670709U patent/CN201208517Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101732893B (en) * | 2010-01-18 | 2014-03-05 | 湖南大学 | A continuous oil-water separation and solvent recycling device for chemical synthesis or azeotropic distillation |
| CN103992880A (en) * | 2014-05-15 | 2014-08-20 | 河北中烟工业有限责任公司 | Volatile oil high-efficiency extraction separator |
| CN103992880B (en) * | 2014-05-15 | 2015-12-09 | 河北中烟工业有限责任公司 | A high-efficiency extraction separator for volatile oil |
| CN106281701A (en) * | 2016-08-17 | 2017-01-04 | 上海清轩生物科技有限公司 | Essential oil extraction device and plants essential oil extracting method |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: WUHAN HUANGHELOU ESSENCE AND SPICE CO., LTD. Free format text: FORMER OWNER: CHINA TOBACCO HUNAN INDUSTRIAL CO., LTD. Effective date: 20100920 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20100920 Address after: 430040 Wuhan, East and West Lake District, Jinshan Road, No. 1355, Hubei Patentee after: Wuhan Huanghelou Flavors Co., Ltd. Address before: 430040 Wuhan, East and West Lake District, Jinshan Road, No. 1355, Hubei Patentee before: China Tobacco Hunan Industrial Co., Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090318 Termination date: 20170512 |