CN104906161B - Processing and extracting equipment for blumea balsamifera - Google Patents

Processing and extracting equipment for blumea balsamifera Download PDF

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Publication number
CN104906161B
CN104906161B CN201510371138.7A CN201510371138A CN104906161B CN 104906161 B CN104906161 B CN 104906161B CN 201510371138 A CN201510371138 A CN 201510371138A CN 104906161 B CN104906161 B CN 104906161B
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distiller
main body
upper cover
blumea balsamifera
steam
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CN104906161A (en
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王华磊
顾岑
唐成林
朱力
赵小敏
杨长成
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Guizhou University
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Guizhou University
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Abstract

The invention discloses blumea balsamifera processing and extracting equipment which comprises a distiller main body, wherein a sewage outlet with a valve is arranged at the bottom of the distiller main body, and a distiller upper cover is arranged at the top of the distiller main body; the top of the distiller upper cover is communicated with the condensation collector body through a steam conduit, and the side surface of the distiller upper cover is communicated with the volatile oil collecting pipe through a steam return pipe. The method can obviously improve the yield and the extraction efficiency of the blumea balsamifera powder extracted by processing, can extract volatile oil while extracting the blumea balsamifera powder, has simple structure, saves the extraction cost, and is convenient for popularization and use in production. The invention can provide an excellent technical scheme for the industrial production of blumea balsamifera and the processing of production places.

Description

Processing and extracting equipment for blumea balsamifera
Technical Field
The invention relates to the field of plant volatile oil extraction, and particularly relates to blumea balsamifera processing and extracting equipment.
Background
Blumea balsamifera is a Miao medicine, and is Compositae (Compositae)Asteraceae) Blumea genus (BlumeaDC.) perennial plant blumea balsamiferaBlumea balsamifera(L.)DC.) whole plant, alias: blumea balsamifera, borneol blumea balsamifera, blumea balsamifera and blumea balsamiferaAnd blumea balsamifera and the like, which are perennial woody herbaceous plants. The blumea balsamifera has the effects of warming middle-jiao and promoting blood circulation, dispelling wind and eliminating dampness and killing parasites, can be used for treating symptoms such as cold-dampness diarrhea and dysentery, abdominal pain and borborygmus, swelling, arthralgia and myalgia, traumatic injury, tinea and sore, and the mixture of the levorotatory borneol extracted from the blumea balsamifera and other volatile oil is called blumea balsamifera powder and has the functions of dispelling wind and relieving swelling and pain and clearing and benefiting throat. The blumea balsamifera leaves contain volatile oil, the blumea balsamifera oil is yellow oily liquid extracted from the blumea balsamifera, has unique fragrance, has the functions of clearing heat and removing toxicity, relieving swelling and pain, relieving itching, promoting blood circulation and removing blood stasis and the like, is particularly used for treating sore throat, aphtha, burn, scald, skin injury and mosquito bite, and is widely favored by medical cosmetology and essence industries. At present, blumea balsamifera oil is mainly added into Jinhoujian spray, Yanlishuang buccal drop pills, Wanjin fragrant fog, Yankang buccal tablets and other medicines and has good curative effect, the blumea balsamifera oil is mainly volatile components, wherein L-borneol is mainly used, and eucalyptol, limonene, sesquiterpene alcohol and the like are contained.
In view of the special efficacy and wide application of the blumea balsamifera powder and blumea balsamifera oil, a large number of researches on methods for efficiently extracting the blumea balsamifera powder and volatile oil are imperative. The traditional method for extracting the blumea balsamifera oil is a steam direct distillation method or a method for extracting the blumea balsamifera raw material → blumea balsamifera powder → blumea balsamifera oil. The method of blumea balsamifera raw material → blumea balsamifera powder → blumea balsamifera oil has high yield and is suitable for industrial production, but the operation of firstly extracting blumea balsamifera powder from the blumea balsamifera raw material and then extracting blumea balsamifera oil exists in the extraction process, which is not beneficial to the comprehensive analysis and utilization of the effective components of the blumea balsamifera oil. The prior art mugwort powder extraction device is a supercritical carbon dioxide extraction device or a large-scale steam distillation raw material. However, the blumea balsamifera production area is inconvenient to transport by multiple means and has scattered planting plots, so that an advanced extraction mode device with high cost is not suitable to be adopted. Generally, the method is used for local extraction of pesticide farmers, and has low extraction rate and large loss. Although there are improved equipments for extracting mugwort powder in the producing area (see the device for extracting mugwort powder, patent application No. 200920003961.2, and the device for processing and extracting blumea balsamifera, patent application No. 200920216395.3, published by the national patent and intellectual Property office), the methods can only extract mugwort powder singly, and can not collect volatile oil during the process of extracting mugwort powder.
Disclosure of Invention
The purpose of the invention is: provides a processing and extracting device of blumea balsamifera, which can simultaneously extract blumea balsamifera powder and blumea balsamifera oil so as to overcome the defects of the prior art.
The invention is realized by the following steps: the blumea balsamifera processing and extracting equipment comprises a distiller main body, wherein a material basket is arranged in the distiller main body, a steam inlet is arranged at the lower part of the side wall of the distiller main body, a sewage outlet with a valve is arranged at the bottom of the distiller main body, and a distiller upper cover is arranged at the top of the distiller main body; the top of the distiller upper cover is provided with a steam guide pipe, the side wall of the distiller upper cover is provided with two symmetrically arranged steam return pipes, and the steam return pipes are inclined downwards; a condensation collector main body is arranged above the distiller upper cover, a condensation pipe is arranged outside the condensation collector main body, a water inlet and a water outlet are arranged on the condensation pipe, volatile oil collecting pipes are connected with two ends of the condensation collector main body, and a control switch is arranged at the bottom ends of the volatile oil collecting pipes; the top of the distiller upper cover is communicated with the condensation collector body through a steam conduit, and the side surface of the distiller upper cover is communicated with the volatile oil collecting pipe through a steam return pipe.
And a sealing ring is arranged at the joint of the distiller main body and the distiller upper cover.
The distiller main body is connected with the distiller upper cover in a locking manner. Thus, the loading and unloading can be convenient after the distillation is finished.
The distiller main body and the distiller upper cover are both provided with double-layer heat-insulating layers. The loss of distillation temperature is reduced to save energy.
Rubber connecting pieces are arranged at the connecting positions of the steam return pipe, the steam guide pipe and the condensation collector main body and the volatile oil collecting pipe. The rubber connecting piece enables the steam backflow pipe and the steam guide pipe to be of a structure which can be disassembled into two sections, so that the connection and the disassembly of the condensation collector main body and the volatile oil collecting pipe with the upper cover of the distiller are facilitated, the installation and the disassembly of the condensation collector main body and the volatile oil collecting pipe are also facilitated, and the corresponding sealing effect is also achieved when the condensation collector main body and the volatile oil collecting pipe are connected, so that the powder can be conveniently collected at any time.
The volatile oil collecting pipe and the steam return pipe are both transparent structures. Therefore, the amount of the extracted volatile oil can be conveniently observed, so that the control switch can be turned on in time to discharge excessive water and collect the volatile oil.
According to the invention, the material basket is used for placing 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 material in the material basket is uniformly heated by adjusting the steam quantity, and a certain space is reserved between the steam inlet and the material basket, so that the steam can pass through the material at the same flow rate.
Due to the adoption of the technical scheme, the invention has the following beneficial effects: the method can obviously improve the yield and the extraction efficiency of the blumea balsamifera powder extracted by processing, can extract volatile oil while extracting the blumea balsamifera powder, has simple structure, saves the extraction cost, and is convenient for popularization and use in production. The invention can provide an excellent technical scheme for the industrial production of blumea balsamifera and the processing of production places.
Drawings
FIG. 1 is a schematic structural diagram of the present invention.
Detailed Description
The invention is described in further detail below with reference to the following figures and examples, but the invention is not limited thereto.
The embodiment of the invention comprises the following steps: the blumea balsamifera processing and extracting equipment comprises a distiller main body 1, wherein a material basket 3 is arranged in the distiller main body 1, a steam inlet 2 is arranged at the lower part of the side wall of the distiller main body 1, a sewage outlet 4 with a valve 5 is arranged at the bottom of the distiller main body 1, and a distiller upper cover 6 is arranged at the top of the distiller main body 1; a steam guide pipe 14 is arranged at the top of the distiller upper cover 6, two symmetrically arranged steam return pipes 7 are arranged on the side wall of the distiller upper cover 6, and the steam return pipes 7 are inclined downwards; a condensation collector main body 8 is arranged above the distiller upper cover 6, a condensation pipe 9 is arranged outside the condensation collector main body 8, a water inlet 10 and a water outlet 11 are arranged on the condensation pipe 9, two ends of the condensation collector main body 8 are connected with a volatile oil collecting pipe 12, and a control switch 15 is arranged at the bottom end of the volatile oil collecting pipe 12; the top of the distiller upper cover 6 is communicated with the condensation collector body 8 through a steam conduit 14, and the side surface of the distiller upper cover 6 is communicated with the volatile oil collecting pipe 12 through a steam return pipe 7; rubber connecting pieces 13 are arranged at the connecting positions of the steam return pipe 7, the steam guide pipe 14, the condensation collector main body 8 and the volatile oil collecting pipe 12; a sealing ring is arranged at the joint of the distiller main body 1 and the distiller upper cover 6; the distiller main body 1 is connected with the distiller upper cover 6 in a locking way; the distiller main body 1 and the distiller upper cover 6 are both provided with double-layer heat-insulating layers; the volatile oil collecting pipe 12 and the steam return pipe 7 are both transparent structures.
The operation method comprises the following steps: putting the blumea balsamifera raw material into a material basket 3, compacting, covering a distiller upper cover 6, sealing, locking, and connecting and sealing a steam guide pipe 14, a steam return pipe 7, a condensation collector main body 8 and a volatile oil collecting pipe 12. Starting to introduce steam from the steam inlet 2 for distillation, allowing the steam with the volatile oil of blumea balsamifera to flow into the condensation collector body 8 through the steam guide pipe 14, introducing condensed water into the condensation pipe 9 for cyclic condensation, and slowly diffusing and condensing the steam with the volatile oil of blumea balsamifera. The condensed vapor with the blumea balsamifera oil enters the volatile oil collecting pipe 12, the blumea balsamifera oil floats on the water surface, the pressure is continuously increased along with the continuous increase of the condensed vapor, the redundant water flows back to the distiller body 1 through the vapor return pipe 7, the amount of the blumea balsamifera oil in the volatile oil collecting pipe 12 is paid attention to at any time during the distillation process, and when the content of the blumea balsamifera oil is lower than that of the vapor return pipe 7, the control switch 15 is opened to collect the volatile oil. And stopping circulating cold and warm water after distillation, opening the condensation collector main body 8 to scrape the moxa powder, collecting volatile oil, opening the valve 5 after powder collection, and discharging sewage from the sewage outlet 4 for next distillation.

Claims (6)

1. The utility model provides a blumea balsamifera processing and extracting equipment, includes distiller main part (1), its characterized in that: a material basket (3) is arranged in the distiller main body (1), a steam inlet (2) is arranged at the lower part of the side wall of the distiller main body (1), a sewage outlet (4) with a valve (5) is arranged at the bottom of the distiller main body (1), and a distiller upper cover (6) is arranged at the top of the distiller main body (1); a steam guide pipe (14) is arranged at the top of the distiller upper cover (6), two symmetrically arranged steam return pipes (7) are arranged on the side wall of the distiller upper cover (6), and the steam return pipes (7) are inclined downwards; a condensation collector main body (8) is arranged above the distiller upper cover (6), a condensation pipe (9) is arranged outside the condensation collector main body (8), a water inlet (10) and a water outlet (11) are arranged on the condensation pipe (9), two ends of the condensation collector main body (8) are connected with a volatile oil collecting pipe (12), and a control switch (15) is arranged at the bottom end of the volatile oil collecting pipe (12); the top of the distiller upper cover (6) is communicated with the condensation collector body (8) through a steam conduit (14), and the side surface of the distiller upper cover (6) is communicated with the volatile oil collecting pipe (12) through a steam return pipe (7).
2. The blumea balsamifera processing and extracting device according to claim 1, which is characterized in that: and a sealing ring is arranged at the joint of the distiller main body (1) and the distiller upper cover (6).
3. The blumea balsamifera processing and extracting device according to claim 1 or 2, which is characterized in that: the distiller main body (1) is connected with the distiller upper cover (6) in a locking way.
4. The blumea balsamifera processing and extracting device according to claim 1, which is characterized in that: the distiller main body (1) and the distiller upper cover (6) are both provided with double-layer heat-insulating layers.
5. The blumea balsamifera processing and extracting device according to claim 1, which is characterized in that: rubber connecting pieces (13) are arranged on the steam return pipe (7), the steam guide pipe (14) and the connecting position of the condensation collector main body (8) and the volatile oil collecting pipe (12).
6. The blumea balsamifera processing and extracting device according to claim 1, which is characterized in that: the volatile oil collecting pipe (12) and the steam return pipe (7) are both transparent structures.
CN201510371138.7A 2015-06-30 2015-06-30 Processing and extracting equipment for blumea balsamifera Active CN104906161B (en)

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CN104906161B true CN104906161B (en) 2019-12-27

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107737147A (en) * 2017-10-20 2018-02-27 贵州农业职业学院 Active ingredient separates and collects device in a kind of Blumea balsamifera leaf

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101538510A (en) * 2009-05-04 2009-09-23 中国科学院植物研究所 Plant volatile oil extractor and application thereof
CN201485438U (en) * 2009-09-14 2010-05-26 中国热带农业科学院热带作物品种资源研究所 Blumea balsamifera processing and extracting 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

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN204951680U (en) * 2015-06-30 2016-01-13 贵州大学 Equipment is drawed in processing of blumea balsamifera

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101538510A (en) * 2009-05-04 2009-09-23 中国科学院植物研究所 Plant volatile oil extractor and application thereof
CN201485438U (en) * 2009-09-14 2010-05-26 中国热带农业科学院热带作物品种资源研究所 Blumea balsamifera processing and extracting 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

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