CN204550505U - A kind of volatile oil extractor - Google Patents
A kind of volatile oil extractor Download PDFInfo
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- CN204550505U CN204550505U CN201520053102.XU CN201520053102U CN204550505U CN 204550505 U CN204550505 U CN 204550505U CN 201520053102 U CN201520053102 U CN 201520053102U CN 204550505 U CN204550505 U CN 204550505U
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- pipe
- separator tube
- return branch
- flask
- volatile oil
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Abstract
The utility model discloses a kind of volatile oil extractor, described extractor comprises flask, vapor uptake, separator tube, measure pipe, return branch and prolong, described flask is connected with the lower end of described vapor uptake, the upper end of described vapor uptake is connected with the top of separator tube, the upper end of described separator tube is connected with prolong, the lower end of described separator tube is connected by the top of connected entrance with described mensuration pipe, one end of described return branch is connected with the top measuring pipe, the other end of described return branch is connected with vapor uptake, the junction of described return branch and mensuration pipe is higher than the connected entrance between described separator tube and mensuration pipe.Volatile oil extractor described in the utility model, structure is simple, exquisite composition, cost of manufacture, can simultaneously extracting and developing, measure heavy oil in volatile oil and light oil, measurement result is accurate, there is higher extraction efficiency, therefore can be widely used in the extraction of various essential oil.
Description
Technical field
The utility model discloses a kind of volatile oil extractor, especially a kind of can the volatile oil extractor of heavy oil simultaneously in extracting and developing volatile oil and light oil.
Background technology
Volatile oil in herbal medicine, natural drug, plant is many be greater than containing relative density simultaneously 1 heavy oil and the relative density light oil that is less than 1.The volatile oil extractor that current extraction volatile oil is conventional is subject to design limit, cannot extract heavy oil and light oil simultaneously.In extractor, liquid level is in scale tubule part, scale tubule is instilled after oil-containing water vapor condensation, heavy oil cannot be separated with light oil, the mixing oil formed to drop in graduated tube after enrichment, easy blocking graduated tube causes oil reservoir segmentation, be not easy to reading of data, oil reservoir is easily entered arm by hydraulic pressure and flows back in flask, problems such as causing loss of volatile oil, reduce extraction efficiency, measurement result is inaccurate.More cannot heavy oil simultaneously in separation determination sample and light oil.
Utility model content
The purpose of this utility model be to overcome above-mentioned the deficiencies in the prior art part and provide that a kind of structure is simple, exquisite composition, with low cost, can the volatile oil extractor of heavy oil simultaneously in extraction and isolation volatile oil and light oil.
For achieving the above object, the technical solution adopted in the utility model is: a kind of volatile oil extractor, comprise flask, vapor uptake, separator tube, measure pipe, return branch and prolong, described flask is connected with the lower end of described vapor uptake, the upper end of described vapor uptake is connected with the top of separator tube, the upper end of described separator tube is connected with prolong, the lower end of described separator tube is connected by the top of connected entrance with described mensuration pipe, one end of described return branch is connected with the top measuring pipe, the other end of described return branch is connected with vapor uptake, the junction of described return branch and mensuration pipe is higher than the connected entrance between described separator tube and mensuration pipe.
Volatile oil extractor described in the utility model, during use, oil-containing water steam in flask enters into separator tube by the vapor uptake be connected with described flask, and then enter into the prolong be connected with described separator tube upper end, oil-containing water steam is able to condensation in prolong, the oil-water mixture obtained after condensation enters into separator tube, and layering is carried out in separator tube, lower floor is heavy oil, middle level is water, upper strata is light oil, because the lower end of separator tube is connected with the top measuring pipe by connected entrance, therefore in separator tube, after layering, the heavy oil of lower floor enters into mensuration pipe by connected entrance, and sink to the bottom measuring pipe, the part water in separator tube middle level then enters into the top measuring pipe by connected entrance, until the liquid level reached in separator tube is identical with the liquid level measured in pipe.When separator tube and the liquid level measured in pipe reach return branch and measure the junction height of pipe, the water in described mensuration pipe flows through vapor uptake by return branch, finally flow in flask and recycles.Because the water measured in pipe is discharged to flask through return branch, therefore the liquid level measured in pipe declines, make liquid level in separator tube higher than the liquid level measured in pipe, under the effect of pressure difference, the part water in separator tube middle level continues through connected entrance and enters into mensuration pipe, until separator tube is identical with the liquid level in mensuration pipe.Along with return branch reclaims the discharge of water, finally to make in separator tube remaining light oil, and heavy oil sinks down into the bottom measuring pipe, thus extracting and developing obtains heavy oil in volatile oil and light oil simultaneously.
As the further improvement to technique scheme, the upper end open sealing of described mensuration pipe, the lower end of described mensuration pipe is provided with leakage fluid dram, and described leakage fluid dram is provided with cock switch.Arrange leakage fluid dram in the lower end of described mensuration pipe, the heavy oil that can be obtained by extraction and isolation easily and light oil take out successively.Heavy oil in described mensuration pipe bottom is from the process that leakage fluid dram takes out, and the light oil in separator tube is also progressively flow into by connected entrance and measures in pipe, after the heavy oil in mensuration pipe all takes out, light oil can be continued to be taken out by the leakage fluid dram measuring pipe.Described leakage fluid dram arranging cock switch, by opening or closing described cock switch, leakage fluid dram to be opened or closed, conveniently neatly heavy oil and light oil to be taken out successively.And the setting of described leakage fluid dram, at any time the heavy oil measured in pipe can be taken out in leaching process and measure, need not leaching process be interrupted, improve extraction efficiency.
As the further improvement to technique scheme, the bottom of described mensuration pipe is provided with scale.Bottom in described mensuration pipe arranges scale, can read the heavy oil volume measuring pipe bottom easily, intuitive and convenient more.
As the further improvement to technique scheme, described flask is round-bottomed flask.
As the further improvement to technique scheme, described flask is connected by the lower end of ground with described vapor uptake.
As the further improvement to technique scheme, the upper end of described separator tube is connected with prolong by ground.
As the further improvement to technique scheme, described return branch and the liquid level in separator tube when measuring the junction of pipe and extract are at sustained height.When extractor described in the utility model uses, only have the liquid level in separator tube and described return branch and measure the junction of pipe when sustained height, water could be discharged in flask by return branch smoothly and recycle.Otherwise, when the liquid level in separator tube higher than described return branch with when measuring the junction of pipe, under the effect of pressure difference, water in separator tube flow into and measures in pipe, and be discharged to flask by return branch and recycle, until the liquid level in the junction of return branch and mensuration pipe and separator tube is up to the standard.When the liquid level in separator tube lower than described return branch with when measuring the junction of pipe, the liquid level in separator tube cannot reach return branch and the junction measuring pipe, and then water cannot be discharged to flask by return branch and recycle.
Volatile oil extractor described in the utility model, structure is simple, exquisite composition, cost of manufacture, can simultaneously extracting and developing, measure heavy oil in volatile oil and light oil, measurement result is accurate, there is higher extraction efficiency, therefore can be widely used in the extraction of various essential oil.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of embodiment of volatile oil extractor described in the utility model.
In figure, 10 be flask, 20 being vapor uptake, 30 being separator tube, 34 be connected entrance, 40 being leakage fluid dram for measuring pipe, 42,44 be cock switch, 50 be return branch, 60 for prolong.
Embodiment
For the purpose of this utility model, technical scheme and advantage are better described, below in conjunction with the drawings and specific embodiments, the utility model is described in further detail.
A kind of volatile oil extractor, as shown in Figure 1, described volatile oil extractor comprises flask 10, vapor uptake 20, separator tube 30, measure pipe 40, return branch 50 and prolong 60, described flask 10 is connected with the lower end of described vapor uptake 20, the upper end of described vapor uptake 20 is connected with the top of separator tube 30, the upper end of described separator tube 30 is connected with prolong 60, the lower end of described separator tube 30 is connected with the top of described mensuration pipe 40 by connected entrance 34, one end of described return branch 50 is connected with the top measuring pipe 40, the other end of described return branch 50 is connected with vapor uptake 20, the junction of described return branch 50 and mensuration pipe 40 is higher than the connected entrance 34 between described separator tube 30 and mensuration pipe 40.
Volatile oil extractor described above, during use, oil-containing water steam in flask 10 enters into separator tube 30 by the vapor uptake 20 be connected with described flask 10, and the prolong 60 be connected with described separator tube 30 upper end is entered into through separator tube 30, oil-containing water steam is able to condensation in prolong 60, and the oil-water mixture obtained after condensation enters into separator tube 30, and layering is carried out in separator tube 30, lower floor is heavy oil, and middle level is water, and upper strata is light oil.Because the lower end of separator tube 30 is connected with the top measuring pipe 40 by connected entrance 34, therefore in separator tube 30, after layering, the heavy oil of lower floor enters into mensuration pipe 40 by connected entrance 34, and sink to the bottom measuring pipe 40, the part water in separator tube 30 middle level then enters into the top measuring pipe 40 by connected entrance 34, until the liquid level reached in separator tube 30 is identical with the liquid level measured in pipe 40.When separator tube 30 and the liquid level measured in pipe 40 reach return branch 50 and measure the junction height of pipe 40, the water in described mensuration pipe 40 flows through vapor uptake 20 by return branch 50, finally flow in flask 10 and recycles.Because the water measured in pipe 40 is discharged to flask 10 through return branch 50, therefore the liquid level measured in pipe 40 declines, make liquid level in separator tube 30 higher than the liquid level measured in pipe 40, under the effect of pressure difference, the part water in separator tube 30 middle level continues through connected entrance 34 and enters into mensuration pipe 40, until separator tube 30 is identical with the liquid level measured in pipe 40.Along with the discharge of return branch 50 pairs of water is reclaimed, finally to make in separator tube 30 remaining light oil, and heavy oil sinks down into the bottom measuring pipe 40, thus heavy oil in volatile oil and light oil can be obtained by extracting and developing simultaneously.
Preferably, as shown in Figure 1, the upper end open sealing of described mensuration pipe 40, the lower end of described mensuration pipe 40 is provided with leakage fluid dram 42, and described leakage fluid dram 42 is provided with cock switch 44.Arrange leakage fluid dram 42 in the lower end of described mensuration pipe 40, the heavy oil that can be obtained by extraction and isolation easily and light oil take out successively.Heavy oil in described mensuration pipe 40 bottom is from the process that leakage fluid dram 42 takes out, light oil in separator tube 30 is also progressively flow into by connected entrance 34 and measures in pipe 40, after the heavy oil in mensuration pipe 40 all takes out, light oil can be continued to be taken out by the leakage fluid dram 42 measuring pipe 40.Described leakage fluid dram 42 arranging cock switch 44, by opening or closing described cock switch 44, leakage fluid dram 42 to be opened or closed, conveniently neatly heavy oil and light oil to be taken out successively.And the setting of described leakage fluid dram 42, at any time the heavy oil measured in pipe 40 can be taken out in leaching process and measure, need not leaching process be interrupted, improve extraction efficiency.
Preferably, as shown in Figure 1, the bottom of described mensuration pipe 40 is provided with scale.Bottom in described mensuration pipe 40 arranges scale, can read the heavy oil volume measuring pipe 40 bottom easily, intuitive and convenient more.
Preferably, as shown in Figure 1, described flask 10 is round-bottomed flask.When described flask 10 is designed to round-bottomed flask, the oil in the plant be extracted in flask 10 etc. can better be obtained by water vapour distillation.Certainly, described flask 10 preferably but be not limited to round-bottomed flask, also can be Florence flask, erlenmeyer flask etc.
Preferably, described flask 10 is connected by the lower end of ground with described vapor uptake 20, and the upper end of described separator tube 30 is connected with prolong 60 by ground.Ground connects not to be needed to use packing ring, can avoid packing ring at high temperature usually problem the problem includes: inefficacy or release the problem of objectionable impurities.
Preferably, as shown in Figure 1, described return branch 50 and the liquid level in separator tube 30 when measuring the junction of pipe 40 and extract are at sustained height.When described extractor uses, only have the liquid level in separator tube 30 and described return branch 50 and measure the junction of pipe 40 when sustained height, water could be discharged in flask 10 by return branch 50 smoothly and recycle.Otherwise, when the liquid level in separator tube 30 higher than described return branch 50 with when measuring the junction of pipe 40, under the effect of pressure difference, water in separator tube 30 flow into and measures in pipe 40, and be discharged to flask 10 by return branch 50 and recycle, until return branch 50 is up to the standard with the liquid level measured in the junction of pipe 40 and separator tube 30.When the liquid level in separator tube 30 lower than described return branch 50 with when measuring the junction of pipe 40, the liquid level in separator tube 30 cannot reach return branch 50 and the junction measuring pipe 40, and then water cannot be discharged to flask 10 by return branch 50 and recycle.
Finally to should be noted that; above embodiment is only in order to illustrate the technical solution of the utility model but not restriction to the utility model protection domain; although be explained in detail the utility model with reference to preferred embodiment; those of ordinary skill in the art is to be understood that; can modify to the technical solution of the utility model or equivalent replacement, and not depart from essence and the scope of technical solutions of the utility model.
Claims (7)
1. a volatile oil extractor, it is characterized in that, comprise flask, vapor uptake, separator tube, measure pipe, return branch and prolong, described flask is connected with the lower end of described vapor uptake, the upper end of described vapor uptake is connected with the top of separator tube, the upper end of described separator tube is connected with prolong, the lower end of described separator tube is connected by the top of connected entrance with described mensuration pipe, one end of described return branch is connected with the top measuring pipe, the other end of described return branch is connected with vapor uptake, the junction of described return branch and mensuration pipe is higher than the connected entrance between described separator tube and mensuration pipe.
2. volatile oil extractor as claimed in claim 1, is characterized in that, the upper end open sealing of described mensuration pipe, the lower end of described mensuration pipe is provided with leakage fluid dram, and described leakage fluid dram is provided with cock switch.
3. volatile oil extractor as claimed in claim 2, it is characterized in that, the bottom of described mensuration pipe is provided with scale.
4. volatile oil extractor as claimed in claim 1, it is characterized in that, described flask is round-bottomed flask.
5. the volatile oil extractor as described in claim 1 or 4, is characterized in that, described flask is connected by the lower end of ground with described vapor uptake.
6. volatile oil extractor as claimed in claim 1, it is characterized in that, the upper end of described separator tube is connected with prolong by ground.
7. volatile oil extractor as claimed in claim 1, is characterized in that, described return branch and the liquid level in separator tube when measuring the junction of pipe and extract are at sustained height.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520053102.XU CN204550505U (en) | 2015-01-26 | 2015-01-26 | A kind of volatile oil extractor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520053102.XU CN204550505U (en) | 2015-01-26 | 2015-01-26 | A kind of volatile oil extractor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204550505U true CN204550505U (en) | 2015-08-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520053102.XU Expired - Fee Related CN204550505U (en) | 2015-01-26 | 2015-01-26 | A kind of volatile oil extractor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204550505U (en) |
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2015
- 2015-01-26 CN CN201520053102.XU patent/CN204550505U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information |
Inventor after: Li Yuanyuan Inventor after: Yin Hong Inventor after: Chen Lin Inventor before: Li Yuanyuan |
|
| COR | Change of bibliographic data | ||
| 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: 20150812 Termination date: 20200126 |