CN201485438U - Blumea balsamifera processing and extracting equipment - Google Patents
Blumea balsamifera processing and extracting equipment Download PDFInfo
- Publication number
- 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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- Prior art keywords
- blumea balsamifera
- condensation
- condensing
- processing
- powder
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- Expired - Lifetime
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- 240000000572 Blumea balsamifera Species 0.000 title claims abstract description 35
- 238000012545 processing Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 25
- 238000009833 condensation Methods 0.000 claims description 51
- 230000005494 condensation Effects 0.000 claims description 51
- 238000004821 distillation Methods 0.000 claims description 26
- 238000000605 extraction Methods 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 10
- 239000010865 sewage Substances 0.000 claims description 6
- 239000000843 powder Substances 0.000 abstract description 32
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000007790 scraping Methods 0.000 abstract description 3
- 238000010521 absorption reaction Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- 239000000341 volatile oil Substances 0.000 description 7
- 229940116229 borneol Drugs 0.000 description 5
- 238000007789 sealing Methods 0.000 description 5
- 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
- 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 4
- 241000723346 Cinnamomum camphora Species 0.000 description 4
- 241000196324 Embryophyta Species 0.000 description 4
- CKDOCTFBFTVPSN-UHFFFAOYSA-N borneol Natural products C1CC2(C)C(C)CC1C2(C)C CKDOCTFBFTVPSN-UHFFFAOYSA-N 0.000 description 4
- 229930008380 camphor Natural products 0.000 description 4
- 229960000846 camphor 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
- 238000001179 sorption measurement Methods 0.000 description 4
- 235000010894 Artemisia argyi Nutrition 0.000 description 3
- 244000030166 artemisia Species 0.000 description 3
- 238000009776 industrial production Methods 0.000 description 3
- 239000011229 interlayer Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 240000006891 Artemisia vulgaris Species 0.000 description 2
- 235000003261 Artemisia vulgaris Nutrition 0.000 description 2
- 239000010624 camphor oil Substances 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 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
- DTGKSKDOIYIVQL-QXFUBDJGSA-N (-)-borneol Chemical compound C1C[C@]2(C)[C@H](O)C[C@H]1C2(C)C DTGKSKDOIYIVQL-QXFUBDJGSA-N 0.000 description 1
- 229930006703 (-)-borneol Natural products 0.000 description 1
- WEEGYLXZBRQIMU-UHFFFAOYSA-N 1,8-cineole Natural products C1CC2CCC1(C)OC2(C)C WEEGYLXZBRQIMU-UHFFFAOYSA-N 0.000 description 1
- 208000004998 Abdominal Pain Diseases 0.000 description 1
- 208000006820 Arthralgia Diseases 0.000 description 1
- 241000208838 Asteraceae Species 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- WEEGYLXZBRQIMU-WAAGHKOSSA-N Eucalyptol Chemical compound C1C[C@H]2CC[C@]1(C)OC2(C)C WEEGYLXZBRQIMU-WAAGHKOSSA-N 0.000 description 1
- 208000019255 Menstrual disease Diseases 0.000 description 1
- 208000000112 Myalgia Diseases 0.000 description 1
- 208000002193 Pain Diseases 0.000 description 1
- 201000007100 Pharyngitis Diseases 0.000 description 1
- 206010042674 Swelling Diseases 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000017531 blood circulation Effects 0.000 description 1
- 229960005233 cineole Drugs 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 208000001848 dysentery Diseases 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012994 industrial processing Methods 0.000 description 1
- 229940087305 limonene Drugs 0.000 description 1
- 235000001510 limonene Nutrition 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000005906 menstruation Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001717 pathogenic effect Effects 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 229930004725 sesquiterpene Natural products 0.000 description 1
- 150000004354 sesquiterpene derivatives Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
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- Medicines Containing Plant Substances (AREA)
Abstract
The utility model discloses blumea balsamifera processing and extracting equipment, which comprises a distilling device, a connecting device and a condensing and collecting device, wherein the distilling device is connected with the condensing and collecting device through the connecting device. The main body of the condensing and collecting device is transversely placed in a condensed water tank to reduce relieve the impact of condensed water on the lower part of the main body of the condensing and collecting device and increase blumea balsamifera powder mass transfer absorption time, so yield is increased. And according to needs, a plurality of main bodies of condensing and collecting devices can be connected in parallel to make blumea balsamifera scraping convenient. After the parallel connection, the blumea balsamifera powder can be scraped freely by using a control switch. In addition, the capacity of the distilling device and the number of the main bodies of the condensing and collecting devices can be set in proportion according to actual needs, so the equipment is suitable for industrial product and direct processing in production areas.
Description
Technical Field
The utility model relates to a plant volatile oil draws the field, and specifically speaking relates to a blumea balsamifera processing and extracting equipment.
Background
Blumea balsamifera (L.) DC, which is a medicinal plant of Compositae, has effects of pungent, bitter, warm, warming middle-jiao, promoting blood circulation, regulating menstruation, dispelling pathogenic wind and removing dampness, and can be used for treating wind cold, dysentery, abdominal pain, borborborygmus, swelling, menoxenia, and arthralgia and myalgia. The blumea balsamifera leaf contains volatile oil, mainly L-borneol, and additionally contains eucalyptol, limonene, sesquiterpene alcohol and the like. The mixture of levo-borneol extracted from blumea balsamifera and other volatile oil is called blumea balsamifera powder, has the functions of dispelling wind and clearing heat, reducing swelling and relieving pain and clearing throat, and is mainly used for treating wind-heat pharyngitis. Generally, blumea balsamifera is an important raw material for extracting blumea balsamifera powder and natural borneol. As the blumea balsamifera is produced in mountainous areas and is inconvenient to transport, the method for extracting the blumea balsamifera powder from the blumea balsamifera is mainly used for on-site extraction by farmers, the extraction efficiency is low, and the loss is large. Although the improved equipment is available for extracting mugwort powder in the producing area (see the 'mugwort powder extraction device' published by the national intellectual property office of China, patent application number: 200920003961.2), the distillation barrel and the condensation pot are arranged at the upper part and the lower part, and the inherent defects of the structure make the distillation barrel and the condensation pot only suitable for direct extraction in the producing area, and the extraction efficiency and the extraction rate are still incomparable with the industrial extraction equipment. The prior industrial processing and extracting device for blumea balsamifera is not reported, and a camphor and volatile oil extractor (patent application number: 88214807.9) published by the Chinese national intellectual property office with a similar extracting method is disclosed, the camphor and volatile oil extractor comprises a distilling pan, a gas guide pipe, a naphtha collector and an oil-water separator, the naphtha collector is a double-layer cooling system consisting of an inner barrel and an outer barrel, a cooling interlayer is formed between the two barrels, and the distilled camphor gas is cooled and condensed into crystals in the cooling interlayer and is adsorbed on the inner wall of the cooling interlayer. The equipment has a complicated naphtha collector structure, is inconvenient to operate when the blumea balsamifera powder is extracted, cannot continuously operate, and does not need an oil-water separator. In addition, the patent application number of 200810031385.2 discloses a high-efficiency extraction device for natural borneol, which consists of a charging basket, a distillation retort, a water feeding pipe, a feed liquid steam pipe and a condensation collector. The side surface of the distillation tank is provided with a charging basket access, the bottom of the distillation tank is provided with a sewage discharge outlet, the bottom of the distillation tank is provided with a heating coil, a guide rail is arranged above the heating coil, and the charging basket is located on the guide rail and can extend out of the distillation tank from the access for charging or discharging. The water adding pipe extends into the distillation retort to add the water required by distillation, one end of the feed liquid steam pipe is communicated with the distillation retort from the top of the distillation retort, the other end of the feed liquid steam pipe is communicated with the condenser from the lower end of the condenser, and the condensation collector comprises a barrel body, a circulating water jacket on the periphery of the barrel body and an electric scraper in the barrel body. The device is designed for extracting borneol in borneol camphor and can also be used for extracting moxa powder, but the condensation collector is vertical, when steam with the moxa powder is condensed, adsorption and crystallization are mainly carried out on the upper part, according to the observation of an applicant, the lower part of the condensation collector is quickly impacted by condensed water on the upper part when the moxa powder is adsorbed, so that the mass transfer adsorption time is too short, the adsorption capacity is reduced, and part of the adsorbed moxa powder is washed down, so that the yield is reduced. Because the moxa powder is a solid substance, the device is inconvenient to receive the powder through a fine powder outlet. In addition, the heating mode is fixed, the steam quantity cannot be adjusted, and the use is limited.
Disclosure of Invention
The utility model aims at overcoming the shortcomings of the prior art and providing a device which can process and extract blumea balsamifera.
In order to realize the utility model discloses a purpose, the utility model provides a blumea balsamifera processing draws equipment, it includes distillation plant, connecting device and condensation collection device, distillation plant passes through connecting device with condensation collection device connects. Wherein,
the distillation apparatus comprises: the distiller comprises a distiller body, a steam introducing port, a material basket, a drain outlet, a control switch and a distiller upper cover. The connecting device includes: a steam conduit and a control switch.
Optionally, a sealing ring is arranged between the distiller body and the distiller upper cover. In addition, optionally, the distiller main body and the distiller upper cover and the steam guide pipe are connected in a conveniently detachable locking connection mode, so that loading and unloading can be conveniently carried out after distillation is finished. The distiller main body and the distiller upper cover can be arranged in a double-layer heat preservation mode, so that the distillation temperature is not lost, and energy is saved. The material basket is internally provided with raw materials, water vapor flows through the raw materials from meshes of the material basket, and the material basket can be taken out for discharging at one time after distillation is finished according to requirements. The steam inlet is connected with a common steam boiler, the steam quantity is adjustable, and a certain space is reserved between the steam inlet and the material basket, so that steam passes through the materials at the same flow rate.
The condensation collection device includes: at least one condensation collector body, a condensation water pool, a condensation collector cover, a steam baffle and a water outlet. Optionally, a sealing ring is arranged between the condensation collector body and the condensation collector cover, and the condensation collector body and the condensation collector cover are arranged in a single-door opening mode and a lock catch control switch mode, so that powder can be conveniently collected at any time.
The condensation collector body and the condensation water pool are connected together at a proper included angle. Preferably, the angle between the condensation collector body and the horizontal plane of the condensation water pool is between 0 and 50 degrees, more preferably between 1 and 5 degrees.
The distillation device can be provided with capacity according to needs, and corresponding matching parts are changed, for example, when the production area is in small-capacity processing, the distillation device can be changed into a mode of directly adding water to the bottom for heating, and other parts can be reduced in proportion. Preferably, the at least one condensation collector body is connected in parallel or in series. Wherein the condensation collector main part can be connected in parallel a plurality of moxa powder of conveniently scraping as required, also can utilize control switch to scrape the moxa powder at any time.
Condensation collector main part is horizontal, thereby can slow down the comdenstion water and to the impact of condensation collector main part lower part and increase chinese mugwort powder mass transfer adsorption time increase the yield to can connect in parallel a plurality of condensation collector main parts as required and get chinese mugwort powder with convenient scraping, scrape after parallelly connected and get the available control switch of chinese mugwort powder and go on at any time. In addition, the capacity of the distiller and the number of the condensation collector bodies can be proportionally set according to actual needs, and the distillation device is suitable for industrial production and direct processing in production places.
The utility model discloses following beneficial effect has: the utility model discloses a blumea balsamifera processing draws equipment can show the yield and the extraction efficiency that improve blumea balsamifera producing area processing and draw the blumea balsamifera powder, and simple structure is convenient for use widely in the producing area, can scrape very conveniently because of unique structural design again and get the blumea balsamifera powder, can not occupy the extra time and receive the powder, and the increase is drawn yield increase behind the capacity, realizes the industrial production. Therefore, the utility model can not only provide a good technical scheme for the industrial production of blumea balsamifera but also for the direct processing of production areas.
Drawings
FIG. 1 is a schematic structural view of the blumea balsamifera processing and extracting device of the present invention.
FIG. 2 is the schematic structural diagram of the condensation collecting device of the blumea balsamifera processing and extracting device of the present invention.
In the figure, the distiller comprises a distiller body 1, a distiller body 2, a steam inlet 3, a material basket 4, a sewage outlet 5 ', a control switch 5', a control switch 6, a distiller upper cover 7, a steam guide pipe 8, a condensation collector body 9, a condensation water tank 10, a condensation collector cover 11, a steam baffle 12 and a water outlet.
Detailed Description
The present invention will be further explained with reference to the drawings and examples.
Example 1:
FIG. 1 shows a blumea balsamifera processing and extracting device, which comprises a distilling device, a connecting device and a condensation and collection device, wherein the distilling device is connected with the condensation and collection device through the connecting device. Wherein the distillation apparatus comprises: the distiller comprises a distiller body 1, a steam introducing port 2, a material basket 3, a sewage outlet 4, a control switch 5' and a distiller upper cover 6; the connecting device includes: steam conduit 7 and control switch 5 "; the condensation collection device includes: a condensation collector body 8, a condensation water pool 9, a condensation collector cover 10, a steam baffle 11 and a water outlet 12.
The operation method comprises the following steps: putting the blumea balsamifera raw material into the material blue 3 and compacting. And (4) covering the distiller upper cover 6, sealing and locking, and connecting and sealing the steam guide pipe 7. The distillation was started by introducing steam from the steam inlet 2. The vapor with the volatile oil of blumea balsamifera flows into the condensing and collecting device through the vapor conduit 7. And condensed water is introduced into the condensed water tank 9 for circulating condensation. The vapor with the blumea balsamifera volatile oil slowly diffuses and condenses under the barrier of the vapor baffle 11. The angle between the condensation collector body 8 and the horizontal plane of the condensate sump 9 is 5 degrees so that the condensate flows slowly toward the drain port 12 to be collected. And stopping condensing circulating water after the distillation is finished, and opening a condensation collector cover 10 with a sealing ring to scrape the moxa powder. After the powder is collected, the control switch 5' is opened to discharge the sewage from the sewage discharge outlet 4 for next distillation.
Example 2:
FIG. 2 shows a blumea balsamifera processing and extracting device, wherein 2 condensation collector bodies 8 are connected in parallel.
The operation method comprises the following steps: the operation process of charging and distilling is the same as that of embodiment 1, and the powder collection can be carried out during the distilling process, namely, the main body of the condensation collector for collecting the powder is selected, the control switch 5 'in front of the main body is closed, the cover 10 of the condensation collector is opened for collecting the powder, the cover 10 of the condensation collector is closed after collecting the powder, and the control switch 5' in front of the main body is opened for continuing the condensation. The powder collecting mode of the embodiment 2 is selected, so that the method for collecting the powder immediately after distillation is not required, and the time and labor cost are saved.
Claims (3)
1. A blumea balsamifera processing and extracting device comprises a distilling device, a connecting device and a condensing and collecting device, wherein the distilling device is connected with the condensing and collecting device through the connecting device,
the distillation apparatus comprises: the distiller comprises a distiller main body (1), a steam introducing port (2), a material basket (3), a sewage outlet (4), a control switch (5') and a distiller upper cover (6);
the connecting device includes: a steam conduit (7) and a control switch (5 ");
the condensation collection device includes: at least one condensation collector body (8), a condensation water basin (9), a condensation collector cover (10), a steam baffle (11) and a drain opening (12).
2. The blumea balsamifera processing and extracting device according to claim 1, wherein the angle between the at least one condensation collector body (8) and the horizontal plane of the condensation water pool (9) is between 0 and 50 degrees.
3. The blumea balsamifera processing and extraction equipment according to claim 1, wherein the at least one condensation collector body (8) is connected in parallel or in series.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2009202163953U CN201485438U (en) | 2009-09-14 | 2009-09-14 | Blumea balsamifera processing and extracting equipment |
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CN2009202163953U CN201485438U (en) | 2009-09-14 | 2009-09-14 | Blumea balsamifera processing and extracting equipment |
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CN201485438U true CN201485438U (en) | 2010-05-26 |
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CN2009202163953U Expired - Lifetime CN201485438U (en) | 2009-09-14 | 2009-09-14 | Blumea balsamifera processing and extracting equipment |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102851120A (en) * | 2012-08-27 | 2013-01-02 | 中国热带农业科学院热带作物品种资源研究所 | Method for extracting Blumea balsamifera oil |
CN103184096A (en) * | 2012-01-01 | 2013-07-03 | 湖南绿步科技有限责任公司 | Vegetable fat distillation method capable of improving production efficiency and auxiliary equipment |
CN104030888A (en) * | 2014-06-03 | 2014-09-10 | 江口县苗药生物科技有限公司 | High-purity Borneolum Luodian extractor |
CN104906161A (en) * | 2015-06-30 | 2015-09-16 | 贵州大学 | Processing and extracting equipment of blumea balsamifera |
CN106110373A (en) * | 2016-06-30 | 2016-11-16 | 贵州省罗甸县全兴药业开发有限责任公司 | A kind of manufacture method of Herba Blumeae Balsamiferae hygienic article |
CN107129872A (en) * | 2017-07-11 | 2017-09-05 | 贵州道地中药材开发有限公司 | A kind of Blumea balsamifera extraction equipment |
CN107164097A (en) * | 2017-07-11 | 2017-09-15 | 贵州道地中药材开发有限公司 | A kind of Blumea balsamifera distillation equipment |
-
2009
- 2009-09-14 CN CN2009202163953U patent/CN201485438U/en not_active Expired - Lifetime
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103184096A (en) * | 2012-01-01 | 2013-07-03 | 湖南绿步科技有限责任公司 | Vegetable fat distillation method capable of improving production efficiency and auxiliary equipment |
CN102851120A (en) * | 2012-08-27 | 2013-01-02 | 中国热带农业科学院热带作物品种资源研究所 | Method for extracting Blumea balsamifera oil |
CN104030888A (en) * | 2014-06-03 | 2014-09-10 | 江口县苗药生物科技有限公司 | High-purity Borneolum Luodian extractor |
CN104030888B (en) * | 2014-06-03 | 2015-12-09 | 江口县苗药生物科技有限公司 | A kind of high purity L-Borneol extraction element |
CN104906161A (en) * | 2015-06-30 | 2015-09-16 | 贵州大学 | Processing and extracting equipment of blumea balsamifera |
CN104906161B (en) * | 2015-06-30 | 2019-12-27 | 贵州大学 | Processing and extracting equipment for blumea balsamifera |
CN106110373A (en) * | 2016-06-30 | 2016-11-16 | 贵州省罗甸县全兴药业开发有限责任公司 | A kind of manufacture method of Herba Blumeae Balsamiferae hygienic article |
CN106110373B (en) * | 2016-06-30 | 2019-11-19 | 贵州省罗甸县全兴药业开发有限责任公司 | A kind of production method of Blumea balsamifera amenities |
CN107129872A (en) * | 2017-07-11 | 2017-09-05 | 贵州道地中药材开发有限公司 | A kind of Blumea balsamifera extraction equipment |
CN107164097A (en) * | 2017-07-11 | 2017-09-15 | 贵州道地中药材开发有限公司 | A kind of Blumea balsamifera distillation equipment |
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Granted publication date: 20100526 |