CN202030729U - Plant distillation separating device - Google Patents
Plant distillation separating device Download PDFInfo
- Publication number
- CN202030729U CN202030729U CN2011201307555U CN201120130755U CN202030729U CN 202030729 U CN202030729 U CN 202030729U CN 2011201307555 U CN2011201307555 U CN 2011201307555U CN 201120130755 U CN201120130755 U CN 201120130755U CN 202030729 U CN202030729 U CN 202030729U
- Authority
- CN
- China
- Prior art keywords
- essential oil
- pipe
- water
- condenser
- pipeline
- 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 - Lifetime
Links
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a plant distillation separating device. When the plant distillation separating device is used in an essential oil extraction process, less water-soluble content in essential oil is lost, and extraction efficiency of the essential oil is higher. The plant distillation separating device comprises a still kettle, the still kettle consists of a kettle body, a sealing cover is detachably connected to an opening end of the kettle body, a gas outlet of the sealing cover is connected with an inlet of a condenser by a pipeline, an outlet of the condenser is connected with an oil-water separating device via a pipeline, the oil-water separating device is arranged below the condenser, a carrying device is disposed inside the kettle body and comprises a carrying table used for carrying plants, the carrying table is provided with a ventilating hole, a steam blowing structure is disposed below the carrying table and connected with a gas outlet of a steam delivery pipe, and a gas inlet of the steam delivery pipe is positioned outside the kettle body. The plants cannot be directly soaked in water, essential oil inside the plants is fed into the condenser via steam blown out of the steam blowing structure, accordingly less water-soluble content in the essential oil is lost, and yield of the essential oil is higher.
Description
Technical field
The utility model relates to a kind of plant fractionation by distillation device that is used to make essential oil.
Background technology
Plant volatile oil also claims essential oil usually, is to be present in the intravital a kind of oily liquids that has volatility and can come out with vapor distillation of plant, and fragrance is arranged mostly.One comprises steamer, condenser and the oily-water seperating equipment that links to each other successively by pipeline the existing device that is used for extracting in the plant materials essential oil.Be that plant and water are together put into steamer in the prior art, then steamer is heated, the intravital essential oil of plant is dissolved in and is admitted to condenser in the water vapour, after the condenser cooling, form oil-water mixture, oil-water mixture separates by oily-water seperating equipment, essential oil is taken out in oily-water seperating equipment again.Adopt aforesaid way to extract essential oil, because the plant in the steamer is immersed in the overlong time in the water, make that water soluble components is lost in a large number in the essential oil, the intravital essential oil output of unit weight plant is lower; One is the container of one one end opening and the other end sealing for existing oily-water seperating equipment, and oil-water mixture is shelved in this container, and until taking out by the essential oil on manually will bubbling through the water column after the layering, whole process wastes time and energy again.
The utility model content
The technical problem that the utility model solves provides a kind of in the essential oil leaching process, the less plant fractionation by distillation device of water soluble components loss in the essential oil.
The technical scheme that its technical problem that solves the utility model adopts is: plant fractionation by distillation device, comprise still pot, described still pot comprises a pot body, the opening end of described pot body is removably connected with sealing cover, the air outlet of described sealing cover links to each other with the inlet of condenser by pipeline, the outlet of described condenser links to each other with the oily-water seperating equipment that is arranged on the condenser below by pipeline, the inside of described pot body is provided with carrying apparatus, described carrying apparatus comprises the Stage microscope that is used to carry plant, described Stage microscope is provided with ventilating pit, described Stage microscope below is provided with the steam blast structure, described steam blast structure links to each other with the air outlet of steam pipeline, and the inlet mouth of described steam pipeline is positioned at a pot external body.
Further be: described carrying apparatus comprises the hanging box that removably connects with the pot body, and described Stage microscope is the base plate of described hanging box, and the base plate of described hanging box is turbogrid plates, and the ventilating pit that is provided with on the described Stage microscope is the grid hole on the described turbogrid plates.
Further be: described steam blast structure comprises annular coil pipe, and described annular coil pipe comprises one group of nested successively from inside to outside ring pipe, and by pipeline connection, described annular coil pipe is provided with gas orifice between adjacent two ring pipes.
Further be: described oily-water seperating equipment comprises the cylindrical shell of sealing, and described cylindrical shell links to each other with the outlet of described condenser by pipeline; The top of described cylindrical shell is connected with oil outlet pipe; The sidewall bottom of described cylindrical shell is connected with rising pipe, and described rising pipe is provided with water control valve.
Further be: the bottom of described cylindrical shell is connected with blow-off pipe, and described blow-off pipe is provided with wash water valve.
Further be: also comprise and look handleless cup, the described handleless cup of looking comprises the sealed vessel of vertically shelving, and the top of described container is provided with container entrance, and described container entrance links to each other with described oil outlet pipe, the bottom of described container is provided with container outlet, and described container outlet is provided with the control fuel tap; The sidewall of described container is made by transparent material.
The beneficial effects of the utility model are: because the plant of pot nside can directly not be immersed in the water, the intravital essential oil of plant is to send in the condenser by the steam blast structure steam that of jetting, therefore the water soluble components loss is less in the essential oil, and the also corresponding raising of the intravital essential oil output of the plant of unit weight.In addition, oily-water seperating equipment of the present utility model is convenient to collecting after essential oil and the water sepn, and is time saving and energy saving.
Description of drawings
Fig. 1 is a plant fractionation by distillation schematic representation of apparatus of the present utility model;
Fig. 2 is the enlarged view of a-quadrant among Fig. 1;
Fig. 3 is the synoptic diagram of annular coil pipe.
Be labeled as among the figure: 1-carrying apparatus, 2-Stage microscope, 3-sealing cover, 4-pot body, 5-steam blast structure, 6-inlet mouth, 7-steam pipeline, 8-rising pipe, the 9-water control valve, 10-condenser, 11-oil outlet pipe, the 12-container, the 13-sidewall, 14-is controlled fuel tap, the 15-cylindrical shell, 16-blow-off pipe, 17-wash water valve, the 18-ventilating pit, 19-gas orifice, 20-annular coil pipe.
Embodiment
Below in conjunction with the drawings and specific embodiments the utility model is further specified.
As depicted in figs. 1 and 2, plant fractionation by distillation device of the present utility model, comprise still pot, described still pot comprises pot body 4, the opening end of described pot body 4 is removably connected with sealing cover 3, the air outlet of described sealing cover 3 links to each other by the inlet of pipeline with condenser 10, the outlet of described condenser 10 links to each other with the oily-water seperating equipment that is arranged on condenser 10 belows by pipeline, the inside of described pot body 4 is provided with carrying apparatus 1, described carrying apparatus 1 comprises the Stage microscope 2 that is used to carry plant, described Stage microscope 2 is provided with ventilating pit 18, described Stage microscope 2 belows are provided with steam blast structure 5, described steam blast structure 5 links to each other with the air outlet of steam pipeline 7, and the inlet mouth 6 of described steam pipeline 7 is positioned at pot body 4 outsides.
During use, the inlet mouth 6 of steam pipeline 7 is linked to each other with steam manifold, steam enters steam blast structure 5 by steam pipeline 7, the plant blowing steam of shelving to Stage microscope 2 tops by steam blast structure 5 then, the intravital essential oil of plant enters condenser 10 with steam, through the cooling of condenser 10, forms oil-water mixture, oil-water mixture enters oily-water seperating equipment to be separated, and finally can in oily-water seperating equipment essential oil be extracted.Because in the aforesaid way, plant can not be immersed in the water for a long time, make that water soluble components is kept in the essential oil, the amount of losing in water significantly reduces, this just makes the corresponding raising of the intravital essential oil output of plant of unit weight, for example, and compared with prior art, use device of the present utility model, 1 kilogram of essential oil output raising 5% that mentha leave extracts.
Above-mentioned carrying apparatus can only comprise a Stage microscope, preferred implementation is: described carrying apparatus 1 comprises the hanging box that removably connects with pot body 4, described Stage microscope 2 is the base plate of described hanging box, the base plate of described hanging box is turbogrid plates, and the ventilating pit 18 that is provided with on the described Stage microscope 2 is the grid hole on the described turbogrid plates.Adopt said structure, after distillation finishes, hanging box can be taken out in the pot body, change the plant in the hanging box then, hanging box is linked to each other with the pot body again, whole process is efficient and convenient, can improve extracts essential oil efficient.Above-mentioned hanging box can or be suspended on pot nside with the clamping of pot body.
The embodiment of above-mentioned steam blast structure 5 has multiple, for example can be many straight tube roads, pipeline is provided with jet thrust, preferred implementation is: as shown in Figure 3, described steam blast structure 5 comprises annular coil pipe 20, described annular coil pipe 20 comprises one group of nested successively from inside to outside ring pipe, and by pipeline connection, described annular coil pipe 20 is provided with gas orifice 19 between adjacent two ring pipes.Above-mentioned annular coil pipe 20 comprises one group of nested successively from inside to outside ring pipe, and ring pipe can be 2,3, and 4 or other quantity, for example among Fig. 3, the ring pipe 22 outer ring pipes 21 that are nested with, ring pipe 21 and ring pipe 22 are interconnected by pipeline.Above-mentioned annular coil pipe 20 is provided with gas orifice 19, and gas orifice 19 can be arranged on the ring pipe, also can be arranged on the pipeline that is used to connect adjacent two ring pipes.By using annular coil pipe 20 can increase the steam blast area, help improving the distillation efficiency of plant, and then help improving extracts essential oil efficient.
For the ease of essential oil is taken out in oily-water seperating equipment, described oily-water seperating equipment comprises the cylindrical shell 15 of sealing, and described cylindrical shell 15 links to each other by the outlet of pipeline with described condenser 10; The top of described cylindrical shell 15 is connected with oil outlet pipe 11; The sidewall bottom of described cylindrical shell 15 is connected with rising pipe 8, and described rising pipe 8 is provided with water control valve 9.Above-mentioned oily-water seperating equipment mainly is the extraction that is used for light oil, and just the density of essential oil is littler than water, and essential oil can swim on the water surface.Adopt said structure, during use, close water control valve 9, after oil-water mixture enters the cylindrical shell 15 of oily-water seperating equipment, essential oil can swim on the water surface, just the upper strata is the essential oil layer, lower floor is a water layer, along with increasing gradually of the oil-water mixture of cylindrical shell 15 inside, the essential oil layer can be gradually near the oil outlet pipe 11 at cylindrical shell 15 tops, when the oil-water mixture in the cylindrical shell 15 reach a certain amount of after, essential oil can flow out to the outside of cylindrical shell 15 from oil outlet pipe 11, by collection container is linked to each other with oil outlet pipe 11, essential oil can be collected, whole process is efficient and convenient, and is time saving and energy saving; When the water excess in the cylindrical shell 15, just there is water to flow out from oil outlet pipe 11, at this moment can open water control valve 9, too much water in the cylindrical shell 15 is emitted, close water control valve 9 then and continue to collect essential oil.
For the ease of the dirt in the cylindrical shell 15 is discharged, the bottom of described cylindrical shell 15 is connected with blow-off pipe 16, and described blow-off pipe 16 is provided with wash water valve 17.By opening wash water valve 17, the dirt in the cylindrical shell 15 can be expelled to cylindrical shell 15 outsides.
In addition, essential oil may be carried some water secretly from oil outlet pipe 11 outflow processes, for these water are separated with essential oil, obtain the higher essential oil of purity, on the basis of the above, also comprise and look handleless cup, the described handleless cup of looking comprises the sealed vessel of vertically shelving 12, and the top of described container 12 is provided with container entrance, and described container entrance links to each other with described oil outlet pipe 11, the bottom of described container 12 is provided with container outlet, and described container outlet is provided with control fuel tap 14; The sidewall 13 of described container 12 is made by transparent material.During use, after essential oil flows in the container 12 by container entrance, can observe the essential oil of internal tank by the sidewall 13 of container 12, if be entrained with water in the essential oil, then the upper strata is an essential oil in the container 12, and lower floor is a water, by opening control fuel tap 14 water is discharged, and then the collection essential oil, can obtain the higher essential oil of purity.Above-mentioned transparent material can be glass or transparent plastics etc.
Claims (6)
1. plant fractionation by distillation device, comprise still pot, described still pot comprises a pot body (4), the opening end of described pot body (4) is removably connected with sealing cover (3), the air outlet of described sealing cover (3) links to each other by the inlet of pipeline with condenser (10), the outlet of described condenser (10) links to each other with the oily-water seperating equipment that is arranged on condenser (10) below by pipeline, it is characterized in that: the inside of described pot body (4) is provided with carrying apparatus (1), described carrying apparatus (1) comprises the Stage microscope (2) that is used to carry plant, described Stage microscope (2) is provided with ventilating pit (18), described Stage microscope (2) below is provided with steam blast structure (5), described steam blast structure (5) links to each other with the air outlet of steam pipeline (7), and the inlet mouth (6) of described steam pipeline (7) is positioned at a pot body (4) outside.
2. plant fractionation by distillation device as claimed in claim 1, it is characterized in that: described carrying apparatus (1) comprises the hanging box that removably connects with pot body (4), described Stage microscope (2) is the base plate of described hanging box, the base plate of described hanging box is turbogrid plates, and the ventilating pit (18) that described Stage microscope (2) upward is provided with is the grid hole on the described turbogrid plates.
3. plant fractionation by distillation device as claimed in claim 1, it is characterized in that: described steam blast structure (5) comprises annular coil pipe (20), described annular coil pipe (20) comprises one group of nested successively from inside to outside ring pipe (21,22), by pipeline connection, described annular coil pipe (20) is provided with gas orifice (19) between adjacent two ring pipes.
4. plant fractionation by distillation device as claimed in claim 1 is characterized in that: described oily-water seperating equipment comprises the cylindrical shell (15) of sealing, and described cylindrical shell (15) links to each other by the outlet of pipeline with described condenser (10); The top of described cylindrical shell (15) is connected with oil outlet pipe (11); The sidewall bottom of described cylindrical shell (15) is connected with rising pipe (8), and described rising pipe (8) is provided with water control valve (9).
5. plant fractionation by distillation device as claimed in claim 4 is characterized in that: the bottom of described cylindrical shell (15) is connected with blow-off pipe (16), and described blow-off pipe (16) is provided with wash water valve (17).
6. plant fractionation by distillation device as claimed in claim 4, it is characterized in that: also comprise and look handleless cup, the described handleless cup of looking comprises the sealed vessel of vertically shelving (12), the top of described container (12) is provided with container entrance, described container entrance links to each other with described oil outlet pipe (11), the bottom of described container (12) is provided with container outlet, and described container outlet is provided with control fuel tap (14); The sidewall (13) of described container (12) is made by transparent material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201307555U CN202030729U (en) | 2011-04-28 | 2011-04-28 | Plant distillation separating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201307555U CN202030729U (en) | 2011-04-28 | 2011-04-28 | Plant distillation separating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202030729U true CN202030729U (en) | 2011-11-09 |
Family
ID=44893035
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201307555U Expired - Lifetime CN202030729U (en) | 2011-04-28 | 2011-04-28 | Plant distillation separating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202030729U (en) |
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102952629A (en) * | 2012-12-06 | 2013-03-06 | 广西京桂香料有限公司 | Technological method for extracting natural cinnamon oil |
| CN102952644A (en) * | 2012-12-06 | 2013-03-06 | 广西京桂香料有限公司 | Device for extracting natural cinnamon oil |
| CN102994232A (en) * | 2012-12-24 | 2013-03-27 | 高连波 | Device for extracting plant essential oil |
| CN103215137A (en) * | 2013-05-08 | 2013-07-24 | 宜宾学院 | Method for continuously distilling aromatic oil by subsectional temperature control |
| CN104194939A (en) * | 2014-09-22 | 2014-12-10 | 西藏圣香海螺民族产品开发有限公司 | Essential oil extraction device |
| CN105001973A (en) * | 2015-07-21 | 2015-10-28 | 广西壮族自治区林业科学研究院 | Comprehensive processing equipment for dry ginger slices and ginger oil |
| CN105199833A (en) * | 2015-07-21 | 2015-12-30 | 广西大学 | Comprehensive processing method of dried ginger slices and ginger oil |
| CN106929157A (en) * | 2017-04-21 | 2017-07-07 | 福建鑫绿林产品开发有限公司 | The uniform fir essential oil production alembic of one kind distillation |
| CN107400562A (en) * | 2017-09-03 | 2017-11-28 | 南京同仁堂黄山精制药业有限公司 | A kind of ethereal oil collection device and method |
| CN108676624A (en) * | 2018-07-26 | 2018-10-19 | 高延厅 | The extracting method and Rosa Damascana of Rosa Damascana |
| CN108707514A (en) * | 2018-07-26 | 2018-10-26 | 高延厅 | Steam inlet endless tube and distillation still |
| CN111304002A (en) * | 2020-03-17 | 2020-06-19 | 陈国全 | High-pressure distillation essential oil separation and purification treatment device and separation and purification method |
| CN112791446A (en) * | 2021-01-07 | 2021-05-14 | 南京益趣渠商贸有限公司 | Energy-concerving and environment-protective oil-water separation equipment of using |
-
2011
- 2011-04-28 CN CN2011201307555U patent/CN202030729U/en not_active Expired - Lifetime
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102952629A (en) * | 2012-12-06 | 2013-03-06 | 广西京桂香料有限公司 | Technological method for extracting natural cinnamon oil |
| CN102952644A (en) * | 2012-12-06 | 2013-03-06 | 广西京桂香料有限公司 | Device for extracting natural cinnamon oil |
| CN102952629B (en) * | 2012-12-06 | 2014-04-02 | 广西京桂香料有限公司 | Technological method for extracting natural cinnamon oil |
| CN102994232A (en) * | 2012-12-24 | 2013-03-27 | 高连波 | Device for extracting plant essential oil |
| CN103215137A (en) * | 2013-05-08 | 2013-07-24 | 宜宾学院 | Method for continuously distilling aromatic oil by subsectional temperature control |
| CN103215137B (en) * | 2013-05-08 | 2014-11-05 | 宜宾学院 | Method for continuously distilling aromatic oil by subsectional temperature control |
| CN104194939A (en) * | 2014-09-22 | 2014-12-10 | 西藏圣香海螺民族产品开发有限公司 | Essential oil extraction device |
| CN105199833A (en) * | 2015-07-21 | 2015-12-30 | 广西大学 | Comprehensive processing method of dried ginger slices and ginger oil |
| CN105001973A (en) * | 2015-07-21 | 2015-10-28 | 广西壮族自治区林业科学研究院 | Comprehensive processing equipment for dry ginger slices and ginger oil |
| CN106929157A (en) * | 2017-04-21 | 2017-07-07 | 福建鑫绿林产品开发有限公司 | The uniform fir essential oil production alembic of one kind distillation |
| CN107400562A (en) * | 2017-09-03 | 2017-11-28 | 南京同仁堂黄山精制药业有限公司 | A kind of ethereal oil collection device and method |
| CN108676624A (en) * | 2018-07-26 | 2018-10-19 | 高延厅 | The extracting method and Rosa Damascana of Rosa Damascana |
| CN108707514A (en) * | 2018-07-26 | 2018-10-26 | 高延厅 | Steam inlet endless tube and distillation still |
| CN108707514B (en) * | 2018-07-26 | 2022-02-08 | 高延厅 | Steam inlet ring pipe and distillation still applied to rose essential oil extraction |
| CN108676624B (en) * | 2018-07-26 | 2022-02-11 | 高延厅 | Extraction method of rose essential oil and rose essential oil |
| CN111304002A (en) * | 2020-03-17 | 2020-06-19 | 陈国全 | High-pressure distillation essential oil separation and purification treatment device and separation and purification method |
| CN112791446A (en) * | 2021-01-07 | 2021-05-14 | 南京益趣渠商贸有限公司 | Energy-concerving and environment-protective oil-water separation equipment of using |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202030729U (en) | Plant distillation separating device | |
| CN104606909B (en) | One kind of plant Oleum sesami boiler | |
| CN101768509B (en) | Portable device for extracting aromatic oil | |
| CN204939435U (en) | A kind of family expenses essential oil distillation extraction device | |
| CN200999238Y (en) | Biomass themal pyrolytic gas dust removing-washing-fractional distillation-decoking purification-storing apparatus | |
| CN204502440U (en) | One Plants sesame oil boiler | |
| CN201634659U (en) | Portable perfume oil extraction device | |
| CN206375877U (en) | Yellow rice wine wine base pressure filters purification devices | |
| CN2869023Y (en) | Plant volatile oil extractor | |
| CN207418323U (en) | A kind of split type condensing unit | |
| CN210765224U (en) | Volatile oil continuous distillation oil-water separator | |
| CN206318964U (en) | A kind of new Rosa Damascana distilling apparatus | |
| CN210103875U (en) | Multi-functional aromatic plant draws processingequipment | |
| CN106943769A (en) | A kind of Kiwi berry high concentration extractor | |
| CN108905291B (en) | High-efficiency oil-water separator and volatile oil extraction and separation equipment | |
| CN207210367U (en) | A kind of plants essential oil extraction equipment | |
| CN2813047Y (en) | Automatic control multifunction extracting thickener sets | |
| CN212560170U (en) | Volatile oil extraction equipment | |
| CN208292961U (en) | A kind of novel plant essential oil extracting device | |
| CN201208517Y (en) | Natural herbals light-oil heavy-oil extraction device | |
| CN209098422U (en) | A kind of full-automatic oil removal lifting means | |
| CN105032042B (en) | Full-automatic waste gas, waste water and waste residue treatment system | |
| CN204981817U (en) | Volatile oil extraction device with multilayer partition plate | |
| CN106479668A (en) | Device for extracting star anise oil by negative pressure circulating water | |
| CN209144109U (en) | A kind of essential oil extract knockout drum |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20111109 |
|
| CX01 | Expiry of patent term |