CN2869023Y - Plant volatile oil extractor - Google Patents
Plant volatile oil extractor Download PDFInfo
- Publication number
- CN2869023Y CN2869023Y CN 200520121279 CN200520121279U CN2869023Y CN 2869023 Y CN2869023 Y CN 2869023Y CN 200520121279 CN200520121279 CN 200520121279 CN 200520121279 U CN200520121279 U CN 200520121279U CN 2869023 Y CN2869023 Y CN 2869023Y
- Authority
- CN
- China
- Prior art keywords
- volatile oil
- extraction device
- oil extractor
- prolong
- distillation extraction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000000341 volatile oil Substances 0.000 title claims abstract description 37
- 238000004821 distillation Methods 0.000 claims abstract description 34
- 238000000605 extraction Methods 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 24
- 239000003921 oil Substances 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 8
- 238000009835 boiling Methods 0.000 abstract description 3
- 238000002474 experimental method Methods 0.000 abstract description 2
- 238000005070 sampling Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract description 2
- 230000005484 gravity Effects 0.000 abstract 2
- 239000000284 extract Substances 0.000 description 5
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000000895 extractive distillation Methods 0.000 description 3
- 238000001256 steam distillation Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
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- Fats And Perfumes (AREA)
Abstract
The utility model discloses a plant volatile oil extractor, including vapor generator, distillation extractor, condenser pipe and acceptor, vapor generator upper portion is arranged in to the distillation extractor, and the lower part of distillation extractor is equipped with the air inlet, and distillation extractor upper portion communicates with each other through communicating pipe and condenser pipe, and the condenser pipe is arranged in acceptor upper portion and rather than communicating with each other. The utility model discloses closely combine steam generator and distillation extractor together, improved the temperature of steam in the distillation extractor, can draw out higher boiling volatile oil fast. The condenser pipe and the receiver are vertically arranged instead of the original horizontal arrangement, so that the volatile oil with different specific gravity can be separated, and the separation of the volatile oil with different specific gravity is facilitated. In addition, the utility model discloses simple structure, safe and reliable can be used to the volatile oil of different proportion in the quick extraction plant, and the field sampling of specially adapted, collection plant volatile oil composition still can be used to student's plant volatile oil extraction experiment.
Description
Technical field
The utility model relates to plant volatile oil extractive technique field, is specifically related to an ESSENTIAL OIL extractor.
Background technology
Often all contain volatile oil in the plant, the steam distillation method is normally adopted in the extraction of plant volatile oil effective constituent, this method has been used the steam distillation device, and this device is made up of steam generator, volatile oil extractive distillation device and condensation susceptor three parts.Steam generator and volatile oil extractive distillation device are independently to separate, by being communicated with communicating pipe.When the water vapor in the steam generator entered extraction volatile oil distiller, the volatile oil that plant includes entered the purpose that the condensation susceptor reaches extraction separation with water vapor.Yet,, usually extract owing to temperature is difficult to the volatile oil that boiling point in the plant is higher inadequately by arriving the water vapour that extracts the volatile oil distiller communicating pipe because steam generator and volatile oil extractive distillation device are independently to separate; In addition, the condensation susceptor of traditional steam distillation device is a horizontal positioned, and the volatile oil of different specific weight mixes, and has increased the difficulty of subsequent disposal.
The utility model content
The purpose of this utility model is to overcome the shortcoming that above-mentioned prior art exists, and provides a kind of and high lower boiling volatile oil in the plant can be extracted and isolating phytovolatilization oil extractor in addition.
To achieve these goals, the technical scheme that the utility model adopted is:
One ESSENTIAL OIL extractor, comprise steam generator, distillation extraction device, prolong and susceptor, the distillation extraction device places steam generator top, and the bottom of distillation extraction device is provided with inlet mouth, distillation extraction device top communicated with prolong by communicating pipe, and prolong places susceptor top and communicates with it.
Above-mentioned prolong all is vertical placements with susceptor, helps the volatile oil of different specific weight is separated.
Be provided with safety tube in the above-mentioned steam generator, safety tube top is provided with safety-valve, and the lower end is stretched in the liquid level of steam generator, to adjust the pressure of steam generator.
Be provided with air pressure adjustment pipe in the above-mentioned steam generator, air pressure adjustment pipe top is provided with safety-valve, can be used for adjusting vapor pressure, prevents the excessive so that steam generator explosion of air pressure.
Above-mentioned distillation extraction device is provided with openable top cover, and top cover and distillation extraction device are tightly connected by frosted.The effect of top cover is can open to put into plant to be extracted, with the frosted of distillation extraction device be tightly connected guarantee air tight.
Above-mentioned inlet mouth is connected with inclined tube, and inclined tube is downward-sloping to be stretched in the distillation extraction device.Inclined tube stretches in the distillation extraction device with 45, mainly is to prevent from that the liquid that splashes is low-priced to go out.
Above-mentioned susceptor bottom is provided with valve and top is provided with valve, and two valves can be used for emitting the volatile oil of different specific weight.
Above-mentioned prolong outside is provided with water condensing unit, and the water condensing unit bottom is provided with water-in, and top is provided with water outlet.
The top of above-mentioned prolong is provided with atmosphere phase port.
Above-mentioned susceptor is provided with scale.
Compared with prior art, the utlity model has following beneficial effect: the utility model is closely linked steam generator and distillation extraction device, has improved the temperature of water vapor, the volatile oil of higher can be extracted.Change prolong into vertical placement with susceptor by original horizontal positioned, make that the volatile oil of different specific weight can layering, be beneficial to the volatilization oil separating.In addition, the utility model is simple in structure, safe and reliable, can be used for the volatile oil of different specific weight in the rapid extraction plant, is specially adapted to field sampling, collects the phytovolatilization oil component, also can be used for student's plant volatile oil and extracts experiment.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Wherein, the section line among the figure represents that frosted is tightly connected.
Embodiment
As shown in Figure 1, an ESSENTIAL OIL extractor comprises steam generator 1, distillation extraction device 2, prolong 3 and susceptor 4, and distillation extraction device 2 places steam generator 1 top; Distillation extraction device 2 bottoms are stretched in the steam generator 1; The inlet mouth 6 of distillation extraction device 2 bottoms connects inclined tubes, and inclined tube tilts 45 ° and stretches in the distillation extraction device 2, conducting steam generator 1 and distillation extraction device 2.Distillation extraction device 2 tops communicated with prolong 3 by communicating pipe 8, and susceptor 4 places prolong 3 bottoms and communicates with it; Prolong 3 all is vertical placements with susceptor 4.Safety tube 5 is arranged in the steam generator 1, and safety tube 5 tops are provided with safety-valve, and the lower end is stretched in the liquid level of steam generator 1.Steam generator 1 is provided with air pressure adjustment pipe 7, and the air pressure adjustment is managed 7 tops and is provided with safety-valve, and the lower end remains on the liquid level top of steam generator 1.Openable top cover 14 is arranged at the top of distillation extraction device 2, and top cover 14 and distillation extraction device 2 are tightly connected by frosted.On the susceptor 4 scale is arranged, valve 9 is arranged at the bottom, and valve 10 is arranged at top.There is water condensing unit prolong 3 outsides, and water condensing unit has water-in 11, water outlet 12, and the top of prolong 3 has and atmosphere port 13 mutually.
Working method: toward water vapour producer 1 dress water, the water surface must be lower than inlet mouth 6, and safety tube 5 lower ends are stretched in the water.Open top cover 14, the plant of needs being extracted volatile oil places distillation extraction device 2, sealing cover upper top cover 14.Add the water among the hot water steam generator 1, the water vapor that produces enters distillation extraction device 2 by inlet mouth 6, water vapor extracts the volatile oil in the plant, water vapor is brought volatile oil into prolong 3 together, water condensing unit becomes water vapor and volatile oil condensation into liquid, liquid directly is collected into susceptor 4, isolates the volatile oil of different specific weight at last from the valve 9 of susceptor 4 and valve 10.Thereby reach simple and easy, extract the purpose of minimum plant volatile oil fast and efficiently.
Claims (10)
1, an ESSENTIAL OIL extractor, comprise steam generator (1), distillation extraction device (2), prolong (3) and susceptor (4), it is characterized in that distillation extraction device (2) places steam generator (1) top, and the bottom of distillation extraction device (2) is provided with inlet mouth (6), distillation extraction device (2) top communicated with prolong (3) by communicating pipe (8), and prolong (3) places susceptor (4) top and communicates with it.
2, phytovolatilization oil extractor as claimed in claim 1 is characterized in that described prolong (3) all is vertical placements with susceptor (4).
3, phytovolatilization oil extractor as claimed in claim 2 is characterized in that being provided with in the described steam generator (1) safety tube (5), and safety tube (5) top is provided with safety-valve, and the lower end is stretched in the liquid level of vapour generator (1).
4, as claim 2 or 3 described phytovolatilization oil extractors, it is characterized in that being provided with in the described steam generator (1) air pressure adjustment pipe (7), air pressure adjustment pipe (7) top is provided with safety-valve, and the lower end remains on the liquid level top of vapour generator (1).
5, phytovolatilization oil extractor as claimed in claim 4 is characterized in that described distillation extraction device (2) is provided with openable top cover (14), and top cover (14) is tightly connected by frosted with distillation extraction device (2).
6, phytovolatilization oil extractor as claimed in claim 5 is characterized in that described inlet mouth (6) is connected with inclined tube, and inclined tube is downward-sloping to be stretched in the distillation extraction device (2).
7, phytovolatilization oil extractor as claimed in claim 6 is characterized in that described susceptor (4) bottom is provided with valve (9) and top is provided with valve (10).
8, phytovolatilization oil extractor as claimed in claim 7 is characterized in that described prolong (3) outside is provided with water condensing unit, and the water condensing unit bottom is provided with water-in (11), and top is provided with water outlet (12).
9, phytovolatilization oil extractor as claimed in claim 8 is characterized in that the top of described prolong (3) is provided with atmosphere phase port (13).
10, phytovolatilization oil extractor as claimed in claim 9 is characterized in that described susceptor (4) is provided with scale.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520121279 CN2869023Y (en) | 2005-12-29 | 2005-12-29 | Plant volatile oil extractor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200520121279 CN2869023Y (en) | 2005-12-29 | 2005-12-29 | Plant volatile oil extractor |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2869023Y true CN2869023Y (en) | 2007-02-14 |
Family
ID=37723957
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200520121279 Expired - Fee Related CN2869023Y (en) | 2005-12-29 | 2005-12-29 | Plant volatile oil extractor |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2869023Y (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101693853B (en) * | 2009-10-27 | 2012-02-01 | 北京林业大学 | Method for preparing bamboo leaf essential oil |
CN102586025A (en) * | 2012-03-22 | 2012-07-18 | 四川农业大学 | Novel device for extracting and measuring essential oil of ligusticum chuanxiong and use method thereof |
CN103706142A (en) * | 2012-09-29 | 2014-04-09 | 九芝堂股份有限公司 | Extracting and collecting device and application thereof |
CN103961899A (en) * | 2013-02-06 | 2014-08-06 | 浙江大学 | Simultaneous distillation extraction device with controllable temperatures and using method thereof |
CN105001987A (en) * | 2015-07-03 | 2015-10-28 | 厦门大学 | Pretreatment method and device of wood biomass |
CN105907474A (en) * | 2016-06-12 | 2016-08-31 | 刘小华 | Essence oil extraction technology and device |
-
2005
- 2005-12-29 CN CN 200520121279 patent/CN2869023Y/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101693853B (en) * | 2009-10-27 | 2012-02-01 | 北京林业大学 | Method for preparing bamboo leaf essential oil |
CN102586025A (en) * | 2012-03-22 | 2012-07-18 | 四川农业大学 | Novel device for extracting and measuring essential oil of ligusticum chuanxiong and use method thereof |
CN103706142A (en) * | 2012-09-29 | 2014-04-09 | 九芝堂股份有限公司 | Extracting and collecting device and application thereof |
CN103961899A (en) * | 2013-02-06 | 2014-08-06 | 浙江大学 | Simultaneous distillation extraction device with controllable temperatures and using method thereof |
CN103961899B (en) * | 2013-02-06 | 2015-08-19 | 浙江大学 | Extraction equipment and using method while controllable temperature |
CN105001987A (en) * | 2015-07-03 | 2015-10-28 | 厦门大学 | Pretreatment method and device of wood biomass |
CN105907474A (en) * | 2016-06-12 | 2016-08-31 | 刘小华 | Essence oil extraction technology and device |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |