CN201485438U - A kind of processing and extracting equipment of Ainaxiang - Google Patents
A kind of processing and extracting equipment of Ainaxiang Download PDFInfo
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- CN201485438U CN201485438U CN2009202163953U CN200920216395U CN201485438U CN 201485438 U CN201485438 U CN 201485438U CN 2009202163953 U CN2009202163953 U CN 2009202163953U CN 200920216395 U CN200920216395 U CN 200920216395U CN 201485438 U CN201485438 U CN 201485438U
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- 238000009833 condensation Methods 0.000 claims abstract description 54
- 230000005494 condensation Effects 0.000 claims abstract description 54
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- 240000000572 Blumea balsamifera Species 0.000 abstract description 2
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- DTGKSKDOIYIVQL-WEDXCCLWSA-N (+)-borneol Chemical compound C1C[C@@]2(C)[C@@H](O)C[C@@H]1C2(C)C DTGKSKDOIYIVQL-WEDXCCLWSA-N 0.000 description 4
- REPVLJRCJUVQFA-UHFFFAOYSA-N (-)-isopinocampheol Natural products C1C(O)C(C)C2C(C)(C)C1C2 REPVLJRCJUVQFA-UHFFFAOYSA-N 0.000 description 4
- CKDOCTFBFTVPSN-UHFFFAOYSA-N borneol Natural products C1CC2(C)C(C)CC1C2(C)C CKDOCTFBFTVPSN-UHFFFAOYSA-N 0.000 description 4
- 229940116229 borneol Drugs 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- DTGKSKDOIYIVQL-UHFFFAOYSA-N dl-isoborneol Natural products C1CC2(C)C(O)CC1C2(C)C DTGKSKDOIYIVQL-UHFFFAOYSA-N 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- DSSYKIVIOFKYAU-XCBNKYQSSA-N (R)-camphor Chemical compound C1C[C@@]2(C)C(=O)C[C@@H]1C2(C)C DSSYKIVIOFKYAU-XCBNKYQSSA-N 0.000 description 3
- 241000723346 Cinnamomum camphora Species 0.000 description 3
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- 229930006703 (-)-borneol Natural products 0.000 description 2
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- XMGQYMWWDOXHJM-UHFFFAOYSA-N limonene Chemical compound CC(=C)C1CCC(C)=CC1 XMGQYMWWDOXHJM-UHFFFAOYSA-N 0.000 description 2
- 230000008961 swelling Effects 0.000 description 2
- WEEGYLXZBRQIMU-UHFFFAOYSA-N 1,8-cineole Natural products C1CC2CCC1(C)OC2(C)C WEEGYLXZBRQIMU-UHFFFAOYSA-N 0.000 description 1
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Abstract
Description
技术领域technical field
本实用新型涉及植物挥发油提取领域,具体地说涉及一种艾纳香加工提取设备。The utility model relates to the field of plant volatile oil extraction, in particular to a kind of processing and extraction equipment for Ainaxiang.
背景技术Background technique
艾纳香(Blumea balsamifera(L.)DC.)为菊科药用植物,其辛、苦、温,具温中活血、调经、祛风除湿之功能,可用于治疗外感风寒、泻痢、腹痛、肠鸣、肿胀、月经不调、筋骨疼痛等病症。艾纳香叶含挥发油,其中以L-龙脑为主,另含桉叶油素、柠檬烯、倍半萜烯醇等。从艾纳香中提取的左旋龙脑和其它挥发油的混合物习称艾粉,具有疏风散热、消肿止痛、清利咽喉的作用,主要用于风热喉痹。通常,艾纳香是提取艾粉和天然冰片的重要原料。因艾纳香产地多为山区,运输不便,因此从艾纳香中提取艾粉的方式主要为农户就地提取,提取效率低下,损失较大。虽然产地提取已有改进设备(见中国国家知识产权局公布的“艾粉提取装置”,专利申请号:200920003961.2),但蒸馏桶和冷凝锅处于上下结合这种结构的固有缺陷使其只适合产地直接提取,提取效率和提取率方面仍与工业化提取设备无法比拟。目前工业化加工提取艾纳香设备未见报道,见有相似提取方法的中国国家知识产权局公布的“樟脑及挥发油提取器”(专利申请号:88214807.9),它由蒸馏锅、导气管、脑油收集器、油水分离器构成,脑油收集器是由内、外桶构成的双层冷却系统,并在两桶之间形成一个冷却夹层,通过蒸馏的樟脑气体在冷却夹层内受冷凝结成结晶体并吸附在冷却夹层内壁上。该设备脑油收集器结构复杂,提取艾纳香收粉时操作不便,无法连续作业,且不需要油水分离器。另见有中国国家知识产权局公布的“天然冰片高效提取设备”(专利申请号:200810031385.2),它由料桶、蒸馏罐、加水管、料液蒸汽管、冷凝收集器组成。蒸馏罐侧面开有料桶出入口、底部有排污口,在蒸馏罐内,底部有加热盘管,该加热盘管上方有导轨,料桶坐落在导轨上可从出入口伸出蒸馏罐装料或卸料。加水管伸进蒸馏罐内添加蒸馏时所需水量,料液蒸汽管的一端从蒸馏罐的顶部与蒸馏罐连通,另一端从冷凝器的下端与冷凝器连通,冷凝收集器包括桶体、桶体外围的循环水水套和桶体内的电动刮板。该设备为提取龙脑樟中的冰片而设计,亦可提取艾粉,但其冷凝收集器为竖式,当带有艾粉的蒸汽冷凝时吸附结晶主要在上部分,因为据申请人观察,其下部吸附艾粉时受到上部冷凝水的快速冲击造成传质吸附时间过短而减少吸附量,并且已经被吸附的艾粉又有部分被冲洗下来从而降低收率。由于艾粉为固体物质,该装置通过细小的出粉口收粉并不方便。另外其加热方式固定,不能调节蒸汽量,使用受到限制。Ainaxiang (Blumea balsamifera (L.) DC.) is a medicinal plant of Compositae. It is pungent, bitter, and warm. It has the functions of warming the middle and promoting blood circulation, regulating menstruation, and expelling wind and dampness. It can be used to treat exogenous wind-cold, diarrhea, and abdominal pain. , borborygmus, swelling, irregular menstruation, muscle and bone pain and other diseases. Aina japonica leaves contain volatile oils, mainly L-borneol, and also contain eucalyptol, limonene, and sesquiterpene alcohols. The mixture of L-borneol and other volatile oils extracted from Ainaxiang is commonly known as moi powder. It has the functions of dispelling wind and heat, reducing swelling and pain, and clearing the throat. It is mainly used for wind-heat sore throat. Usually, Ainaxiang is an important raw material for extracting moxa powder and natural borneol. Because Ainaxiang is mostly produced in mountainous areas and transportation is inconvenient, the method of extracting Ainaxiang powder from Ainaxiang is mainly carried out by farmers on the spot, and the extraction efficiency is low and the loss is relatively large. Although there are improved equipment for the extraction of the place of origin (see the "Ai powder extraction device" published by the State Intellectual Property Office of China, patent application number: 200920003961.2), the inherent defects of the structure of the distillation barrel and the condensing pot combined up and down make it only suitable for the place of origin Direct extraction, extraction efficiency and extraction rate are still incomparable with industrial extraction equipment. At present, there is no report on the extraction of Ai Naxiang equipment in industrialized processing. See "camphor and volatile oil extractor" (patent application number: 88214807.9) announced by the State Intellectual Property Office of China with similar extraction methods. The naphtha collector is composed of a double-layer cooling system composed of inner and outer barrels, and a cooling interlayer is formed between the two barrels, and the distilled camphor gas is condensed into crystals in the cooling interlayer And adsorbed on the inner wall of the cooling interlayer. The brain oil collector of this equipment has a complicated structure, and it is inconvenient to operate when extracting Ainaxiang and collecting powder, and cannot work continuously, and does not need an oil-water separator. See also "natural borneol efficient extraction equipment" (patent application number: 200810031385.2) announced by the State Intellectual Property Office of China. There is a barrel inlet and outlet on the side of the distillation tank, and a sewage outlet at the bottom. In the distillation tank, there is a heating coil at the bottom. There is a guide rail above the heating coil. . The water supply pipe extends into the distillation tank to add the amount of water required for distillation. One end of the feed liquid steam pipe communicates with the distillation tank from the top of the distillation tank, and the other end communicates with the condenser from the lower end of the condenser. The condensation collector includes a barrel body, a barrel The circulating water jacket around the body and the electric scraper in the barrel. This equipment is designed for extracting borneol in camphor borneol, and can also extract moxa powder, but its condensation collector is vertical, and when the steam with moxa powder condenses, the adsorption crystallization is mainly in the upper part, because according to the applicant's observation, When the lower part absorbs the moxa powder, it is impacted by the condensed water on the upper part quickly, which causes the mass transfer adsorption time to be too short to reduce the adsorption amount, and the moxa powder that has been adsorbed is partially washed down to reduce the yield. Because moxa powder is a solid substance, it is inconvenient for the device to collect powder through a small powder outlet. In addition, its heating method is fixed, and the amount of steam cannot be adjusted, so its use is limited.
发明内容Contents of the invention
本实用新型的目的是克服上述现有技术存在的缺点,提供一种能够加工提取艾纳香的设备。The purpose of the utility model is to overcome the above-mentioned shortcomings in the prior art, and provide a kind of equipment capable of processing and extracting Ainaxiang.
为了实现本实用新型的目的,本实用新型提供了一种艾纳香加工提取设备,其包括蒸馏装置、连接装置、和冷凝收集装置,所述蒸馏装置通过所述连接装置与所述冷凝收集装置连接。其中,In order to realize the purpose of the utility model, the utility model provides a kind of processing and extracting equipment of Ainaxiang, which comprises a distillation device, a connection device, and a condensation collection device, and the distillation device is connected with the condensation collection device through the connection device. connect. in,
所述蒸馏装置包括:蒸馏器主体、蒸汽导入口、料篮、排污口、控制开关和蒸馏器上盖。所述连接装置包括:蒸汽导管和控制开关。The distillation device comprises: a distiller main body, a steam inlet, a material basket, a sewage outlet, a control switch and an upper cover of the distiller. The connection device includes: a steam conduit and a control switch.
可选择地,所述蒸馏器主体和所述蒸馏器上盖之间设置密封圈。另外,可选择地,所述蒸馏器主体和所述蒸馏器上盖之间、以及所述蒸馏器上盖和所述蒸汽导管之间采用方便拆卸的锁扣连接方式连接,这样可以在蒸馏完毕后方便装料和卸料。所述蒸馏器主体和所述蒸馏器上盖可以为双层保温设置,使蒸馏温度不损失以节约能源。所述料篮中放置原料,水蒸汽从所述料篮的网眼中流经原料,根据需要所述料篮可以在蒸馏完毕后一次性取出卸料。所述蒸汽导入口连接普通蒸汽锅炉,蒸汽量可调,并在所述蒸汽导入口和所述料篮之间留有一定空间使蒸汽以相同流速经过物料。Optionally, a sealing ring is provided between the main body of the distiller and the upper cover of the distiller. In addition, optionally, the body of the distiller and the upper cover of the distiller, as well as the upper cover of the distiller and the steam conduit, are connected in a conveniently detachable lock-and-buckle connection, so that they can be connected after the distillation. Convenient loading and unloading. The main body of the distiller and the upper cover of the distiller can be provided with double-layer insulation, so that the distillation temperature will not be lost to save energy. The raw material is placed in the material basket, and the water vapor flows through the raw material through the mesh of the material basket, and the material basket can be taken out and unloaded at one time after the distillation is completed as required. The steam inlet is connected to an ordinary steam boiler, and the steam volume is adjustable, and a certain space is left between the steam inlet and the material basket so that the steam passes through the material at the same flow rate.
所述冷凝收集装置包括:至少一个冷凝收集器主体、冷凝水池、冷凝收集器盖、蒸汽挡板和排水口。可选择地,所述冷凝收集器主体和所述冷凝收集器盖之间设置密封圈,所述冷凝收集器主体和所述冷凝收集器盖采用单开门方式和锁扣控制开关方式设置,从而可以方便随时收粉。The condensation collecting device includes: at least one condensation collector main body, a condensation water pool, a condensation collector cover, a steam baffle and a drain port. Optionally, a sealing ring is provided between the condensation collector body and the condensation collector cover, and the condensation collector body and the condensation collector cover are set in a single door and lock control switch mode, so that It is convenient to collect powder at any time.
所述冷凝收集器主体与所述冷凝水池以适当夹角连接在一起。优选地,所述冷凝收集器主体与所述冷凝水池的水平面的夹角在0度至50度之间,更优选地,所述夹角在1度至5度之间。The main body of the condensation collector is connected with the condensation pool at an appropriate angle. Preferably, the included angle between the main body of the condensation collector and the horizontal plane of the condensed pool is between 0° and 50°, more preferably, the included angle is between 1° and 5°.
所述蒸馏装置可以根据需要设置容量,并进行相应配套部件的改变,例如,产地小容量加工时可以改所述蒸馏装置为底部直接加水加热方式,其他部件按比例缩小即可。优选地,所述至少一个冷凝收集器主体是并联或串联的。其中所述冷凝收集器主体可以根据需要并联多个以方便刮取艾粉,也可利用控制开关随时刮取艾粉。The capacity of the distillation device can be set according to the needs, and the corresponding supporting parts can be changed. For example, the distillation device can be changed to directly add water to the bottom for heating when the production area is small-capacity processing, and other components can be scaled down. Preferably, said at least one condensation collector body is connected in parallel or in series. Wherein the main body of the condensation collector can be connected in parallel as required to facilitate the scraping of the moxa powder, and the control switch can also be used to scrape the moxa powder at any time.
本实用新型所述冷凝收集器主体为横式,可以减缓冷凝水对冷凝收集器主体下部的冲击和增加艾粉传质吸附时间从而增加收率,并且可以根据需要并联多个冷凝收集器主体以方便刮取艾粉,并联后刮取艾粉可利用控制开关随时进行。另外可根据实际需要按比例设置蒸馏器的容量和冷凝收集器主体的数量,既适合工业化生产又适合产地直接加工。The main body of the condensation collector described in the utility model is horizontal, which can slow down the impact of condensed water on the lower part of the main body of the condensation collector and increase the mass transfer and adsorption time of moxa powder to increase the yield. It is convenient to scrape moxa powder, and after parallel connection, scraping moxa powder can be carried out at any time by using the control switch. In addition, the capacity of the distiller and the number of condensation collector bodies can be set in proportion according to actual needs, which is suitable for both industrial production and direct processing at the production site.
本实用新型具有如下有益效果:本实用新型的艾纳香加工提取设备既能显著提高艾纳香产地加工提取艾粉的收率和提取效率,结构简单,便于在产区推广使用,又因独特结构设计能够非常方便地刮取艾粉,可以不占用额外时间收粉,增大提取容量后收率增加,实现工业化生产。因此本实用新型既可为艾纳香工业化生产又可为产地直接加工提供优良的技术方案。The utility model has the following beneficial effects: the Ainaxiang processing and extracting equipment of the utility model can not only significantly improve the yield and extraction efficiency of the Ainaxiang processing and extracting moxa powder in the production area, but also has a simple structure and is convenient for popularization and use in the production area. The structural design can scrape the moxa powder very conveniently, and can collect the powder without taking extra time. After increasing the extraction capacity, the yield increases, and industrial production is realized. Therefore, the utility model can provide an excellent technical solution for both the industrialized production of Ainaxiang and the direct processing at the place of production.
附图说明Description of drawings
图1为本实用新型的艾纳香加工提取设备的结构示意图。Fig. 1 is the structural representation of the processing and extracting equipment of Ai Naxiang of the present utility model.
图2为本实用新型的艾纳香加工提取设备的冷凝收集装置的结构示意图。Fig. 2 is a structural schematic diagram of the condensation collection device of the Ainaxiang processing and extracting equipment of the present invention.
图中,1、蒸馏器主体,2、蒸汽导入口,3、料篮,4、排污口,5’、控制开关,5”、控制开关,6、蒸馏器上盖,7、蒸汽导管,8、冷凝收集器主体,9、冷凝水池,10、冷凝收集器盖,11、蒸汽挡板,12、排水口。In the figure, 1. Distiller body, 2. Steam inlet, 3. Basket, 4. Sewage outlet, 5', control switch, 5", control switch, 6. Distiller cover, 7. Steam conduit, 8 . Condensation collector main body, 9. Condensation pool, 10. Condensation collector cover, 11. Steam baffle, 12. Drain outlet.
具体实施方式Detailed ways
下面结合附图和实施例对本实用新型进一步说明。Below in conjunction with accompanying drawing and embodiment the utility model is further described.
实施例1:Example 1:
图1示出一种艾纳香加工提取设备,其包括蒸馏装置、连接装置、和冷凝收集装置,所述蒸馏装置通过所述连接装置与所述冷凝收集装置连接。其中所述蒸馏装置包括:蒸馏器主体1、蒸汽导入口2、料篮3、排污口4、控制开关5’和蒸馏器上盖6;所述连接装置包括:蒸汽导管7和控制开关5”;所述冷凝收集装置包括:冷凝收集器主体8、冷凝水池9、冷凝收集器盖10、蒸汽挡板11和排水口12。Fig. 1 shows a kind of Ai Naxiang processing and extracting equipment, and it comprises distillation device, connection device and condensation collection device, and described distillation device is connected with described condensation collection device by described connection device. Wherein the distillation device includes: a still main body 1, a
操作方法如下:把艾纳香原料放入料蓝3中并压实。盖上蒸馏器上盖6,密封锁紧,连接并密封好蒸汽导管7。开始从蒸汽导入口2通入蒸汽进行蒸馏。带有艾纳香挥发油的蒸汽通过蒸汽导管7流入冷凝收集装置。冷凝水池9中通入冷凝水进行循环冷凝。带有艾纳香挥发油的蒸汽在蒸汽挡板11的阻挡下慢慢扩散并冷凝。冷凝收集器主体8与冷凝水池9的水平面之间的角度为5度以使冷凝水缓慢流向排水口12而被收集。蒸馏完毕后停止冷凝循环水,打开带有密封圈的冷凝收集器盖10刮取艾粉。收粉后打开控制开关5’从排污口4放出污水准备下一次蒸馏。The operation method is as follows: Put the raw material of Ainaxiang into the material blue 3 and compact it. Cover the distiller
实施例2:Example 2:
图2示出了一种艾纳香加工提取设备,其中2个冷凝收集器主体8是并联的。Fig. 2 shows a kind of Ainaxiang processing and extracting equipment, wherein two condensation collector
操作方法如下:装料和蒸馏的操作过程与实施例1一致,收粉可以选择在蒸馏过程中进行,即,选择要收粉的冷凝收集器主体,关闭其前面的控制开关5”,打开冷凝收集器盖10进行收粉,收粉后关闭冷凝收集器盖10,打开其前面的控制开关5’继续冷凝即可。选择实施例2的收粉方式可以不必拘泥于蒸馏完毕马上进行收粉的方法,节约了时间和人力成本。The operation method is as follows: the operation process of charging and distillation is consistent with that of Example 1, and the collection of powder can be carried out during the distillation process, that is, select the main body of the condensation collector to collect powder, close the
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