CN102952644A - Device for extracting natural cinnamon oil - Google Patents
Device for extracting natural cinnamon oil Download PDFInfo
- Publication number
- CN102952644A CN102952644A CN201210519008XA CN201210519008A CN102952644A CN 102952644 A CN102952644 A CN 102952644A CN 201210519008X A CN201210519008X A CN 201210519008XA CN 201210519008 A CN201210519008 A CN 201210519008A CN 102952644 A CN102952644 A CN 102952644A
- Authority
- CN
- China
- Prior art keywords
- water
- tank body
- oil
- kettle
- chamber
- 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.)
- Granted
Links
- 239000010630 cinnamon oil Substances 0.000 title abstract 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 50
- 238000004821 distillation Methods 0.000 claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 claims abstract description 12
- 235000019198 oils Nutrition 0.000 claims description 43
- 235000013372 meat Nutrition 0.000 claims description 14
- 238000009826 distribution Methods 0.000 claims description 8
- 238000000605 extraction Methods 0.000 claims description 8
- 235000019476 oil-water mixture Nutrition 0.000 claims description 8
- 230000008676 import Effects 0.000 claims description 7
- 239000010865 sewage Substances 0.000 claims description 7
- 238000001556 precipitation Methods 0.000 claims description 6
- 230000015572 biosynthetic process Effects 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 5
- 239000012530 fluid Substances 0.000 claims description 4
- 238000007789 sealing Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 abstract description 2
- 239000003921 oil Substances 0.000 description 65
- 238000002156 mixing Methods 0.000 description 13
- 241000522254 Cassia Species 0.000 description 11
- 239000000203 mixture Substances 0.000 description 8
- 238000009833 condensation Methods 0.000 description 7
- 230000005494 condensation Effects 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 238000004062 sedimentation Methods 0.000 description 4
- 239000002826 coolant Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000000284 extract Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000010620 bay oil Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000007667 floating Methods 0.000 description 2
- 238000001256 steam distillation Methods 0.000 description 2
- 241000723346 Cinnamomum camphora Species 0.000 description 1
- 235000019082 Osmanthus Nutrition 0.000 description 1
- 241000333181 Osmanthus Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000002026 carminative effect Effects 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 244000045947 parasite Species 0.000 description 1
- 239000002304 perfume Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a device for extracting natural cinnamon oil, which relates to the technical field of manufacturing a forest chemical device. The device comprises a condenser, multiple distillation kettles and multiple oil-water separators, wherein the multiple distillation kettles are mutually connected, a re-distillation kettle is connected between the distillation kettles and the condenser, and a water pump is connected between the multiple oil-water separators and the re-distillation kettle. According to the device disclosed by the invention, the problems of low output rate and high production cost during the extracting of the cinnamon oil can be solved.
Description
Technical field
The present invention relates to forest chemical equipment manufacturing technology field, especially a kind of equipment for extract the natural meat oil of bay from the branch of xylocinnamomum and leaf.
Background technology
Chinese cassia tree is Lauraceae camphor tree aiphyllium, has another name called beautiful osmanthus.Mainly be distributed at home the damp-heat areas such as Guangxi, Guangdong, Fujian, Taiwan, Yunnan.From the branch of xylocinnamomum, leaf, all can extract perfume oil, i.e. the natural meat oil of bay.The natural meat oil of bay has higher pharmaceutical use, is good carminative and stomachic.In addition, it also has the effect of expelling parasite, mildew-resistant and sterilization, is widely used in food, beverage, cigarette, medicine and other fields.
The extracting method of natural meat oil of bay is a lot, but the method for generally using is steam distillation.The equipment of common extraction by steam distillation natural meat oil of bay mainly contains three parts: 1, still kettle, 2, condenser, 3, water-and-oil separator; The flow process of extracting the natural meat oil of bay is: Chinese cassia tree branch, basyleaves are put into still kettle, add again certain water, under normal pressure, be heated to boiling, water vapor steams the steam that rear formation contains oil of bay with the Oleum Cinnamomi in Chinese cassia tree branch, the basyleaves in the still, contains the steam of oil of bay through condenser condenses, and the gained phlegma enters the water-and-oil separator layering, oil reservoir is the oil of bay product, still contain a small amount of oil of bay in the water layer, be milky white shape, return in the still kettle; The extraction of adopting these equipment to carry out the natural meat oil of bay exists the oil of bay oil yield low, the problem that production cost is high.
Summary of the invention
The problem to be solved in the present invention provides a kind of natural meat oil of bay extraction equipment, and it is low that it can solve natural meat oil of bay extraction Oleum Cinnamomi oil yield, the problem that production cost is high.
In order to address the above problem, the technical solution used in the present invention is: this natural meat oil of bay extraction equipment includes condenser, a plurality of interconnective still kettles and water-and-oil separator; Between described still kettle and described condenser, be connected with multiple still kettle; Be connected with water pump between described a plurality of water-and-oil separator and the described multiple still kettle;
Described multiple still kettle, comprise the multiple distillation kettle that is provided with liquid outlet and fluid inlet, the described kettle inside of distilling again is provided with the vapor distribution device, described vapor distribution device surrounds annular by pipe, cross pipes is arranged in annular, and all pipes interconnect, and have at least one to stretch out the external pipe formation of described multiple still kettle, are distributed with a plurality of production wells on the described pipe of described vapor distribution device; The described kettle top of distilling again is equipped with tensimeter; The described autoclave body bottom that distills again is provided with sewage draining exit, with pipeline that described sewage draining exit is communicated with in be provided with wash water valve;
Described condenser, include tank body and the steam inlet, condensate outlet, water-in and the water outlet that are located on the described tank body, described tank inner chamber is equipped with by two by side plate and the upper port of sealing this two block side plates and the vortex steam flow passage that lower port form of center to the inner rotary expansion; The import of described vortex steam flow passage is communicated with the described steam inlet that is located at tank body upper end, and the outlet of described vortex steam flow passage is communicated with condensate outlet on being located at described tank wall; The bottom of described tank body is provided with and fills valvular drain outlet;
Described water-and-oil separator, comprise that the tank body that is provided with oil-water mixture import, oil export and water out is equipped with dividing plate at described tank inner chamber, the bottom of described dividing plate becomes certain inclination angle and is fixed on the sidewall of described tank body with the bottom of described tank body, described dividing plate is separated into precipitation chamber and profit chamber two chambers with described tank inner chamber, described precipitation chamber and profit chamber are provided with oil export by the cross current that is installed on the described dividing plate in bottom, described profit chamber.
Owing to adopted technique scheme, the present invention compared with prior art has following beneficial effect:
1, because the mixture of Oleum Cinnamomi and water passes through natural sedimentation at water-and-oil separator, the oil of bay sedimentation, waterborne floating, but oil of bay and moisture are thorough not from getting, and also contain certain oil of bay in the water on upper strata.The mixture of the oil of bay on water-and-oil separator upper strata and water is drawn into multiple still kettle, utilizes from still pot mixing steam out and make its heating, the oil of bay revaporization in the mixture of the oil of bay on water-and-oil separator upper strata and water out; And after the multiple steaming of the mixture of the oil of bay of multiple still kettle and water process, the still pot that is extracted into again an operation is reused as bottom pot water, therefore adopts again still kettle, and the oil of bay oil yield can improve 10%, also reduces production costs simultaneously.
2, the present invention is owing to used the slab type spiral water-cooled tube in the condenser tank body, so that the area that the Chinese cassia tree profit mixing steam that draws through the still kettle evaporation contacts with water-cooled tube in the condenser tank body has increased, the corresponding time that stops in the condenser tank body has also increased, thereby improved the condensation efficiency of condenser, also reduced production cost simultaneously.
3, the present invention is owing to increased dividing plate and crossed water pipe in the water-and-oil separator tank body, so that the stroke of oil-water mixture in water-and-oil separator increased, the corresponding time of oil-water mixture in water-and-oil separator has also increased, thereby so that the efficient of oily water separation improves, thereby can reduce the quantity of using water-and-oil separator, originally needed at least 15 water-and-oil separators, it is just enough to show 7 to 10 of a need, has reduced cost when raising the efficiency.
Description of drawings
Fig. 1 is structural representation of the present invention.
Fig. 2 is that the master of condenser looks synoptic diagram among the present invention.
Fig. 3 is A among Fig. 2-A sectional view.
Fig. 4 is that the master of water-and-oil separator looks synoptic diagram among the present invention
Fig. 5 is B among Fig. 4-B sectional view.
Fig. 6 is that the master of multiple still kettle among the present invention looks synoptic diagram
Fig. 7 is C among Fig. 6-C sectional view.
Embodiment
Below in conjunction with the accompanying drawing example structure of the present invention is described in further detail:
The natural meat oil of bay extraction equipment of Fig. 1 includes two with the interconnective still kettle 1 of pipe, and one of them still kettle 1 is connected with the steam-pipe of boiler 6; Condenser 2 and 8 are with the interconnective water-and-oil separator 3 of pipe; With pipe and two still kettles, 1 one of them multiple still kettle 4 that is connected; Be connected with pipe between multiple still kettle 4 and the condenser 2; Be connected with water pump 5 between 8 water-and-oil separators 3 and the multiple still kettle 4.
Fig. 2 and shown in Figure 3 be condenser 2 among the present invention, include tank body 2-1 and steam inlet 2-1-1, the condensate outlet 2-1-2, water-in 2-2-1 and the water outlet 2-2-2 that are located on the tank body 2-1, tank body 2-1 inner chamber is equipped with by two by side plate and the upper port of sealing this two block side plates and the vortex steam flow passage 2-2 that lower port form of center to the inner rotary expansion; The import of vortex steam flow passage 2-2 is communicated with the steam inlet 2-1-1 that is located at tank body 2-1 upper end, and the outlet of vortex steam flow passage 2-2 is communicated with condensate outlet 2-1-2 on being located at tank body 2-1 sidewall; The bottom of tank body 2-1 is provided with the drain outlet 2-1-3 that valve 2-3 is housed; The profile cross section of vortex steam flow passage 2-2 is that length is 1 meter, and wide is 0.02 meter rectangle; The upper head plate of vortex steam flow passage 2-2 and tank body 2-1 and bottom plate are separated into eddy airstream passage and the vortex water flow passage 2-2-3 that is parallel to each other with the inner chamber of tank body 2-1, water-in 2-2-1 is located at the bottom of tank body 2-1 sidewall, and water outlet 2-2-2 is located on the upper head plate of tank body 2-1.
In the production process of extracting Oleum Cinnamomi, evaporate the Chinese cassia tree profit mixing steam that draws through multiple still kettle 4, steam inlet 2-1-1 through tank body 2-1 enters in the interior vortex steam flow passage 2-2 of tank body 2-1, carry out heat exchange and obtain condensation with the water coolant of the vortex water flow passage 2-2-3 of tank body 2-1 inner chamber, the oil-water mixture that condensation obtains enters water-and-oil separator from condensate outlet 2-1-2 output; The water coolant of tank body 2-1 inner chamber is to pass into from the water-in 2-2-1 that is located at tank body 2-1 lower sidewall, water coolant is after the Chinese cassia tree profit mixing steam of vortex water flow passage 2-2-3 in tank body 2-1 inner chamber and vortex steam flow passage 2-2 carries out heat exchange, water outlet 2-2-2 from the upper head plate that is located at tank body 2-1 flows out, constantly circulation makes Chinese cassia tree profit mixing steam obtain sufficient condensation;
Condenser after using for some time is opened the valve 2-3 among the sewage draining exit 2-1-3, will discharge outside tank body 2-1 by residue in tank body 2-1; Vortex steam flow passage 2-2 is set, has increased the heat exchange contact area of Chinese cassia tree profit mixing steam and water of condensation, improved condensation effect and reduced production cost.
Fig. 4 and shown in Figure 5 be water-and-oil separator 3 among the present invention, the tank body 3-1 of water-and-oil separator 3 is provided with oil-water mixture import 3-1-1, water out 3-1-2, oil export 3-1-3 and oil export 3-1-4, be installed by welding with dividing plate 3-3 at tank body 3-1 inner chamber, the bottom of dividing plate 3-3 becomes the inclination angle of one 20 degree and is welded on the tank body 3-1 sidewall with the bottom of tank body 3-1, dividing plate 3-3 is separated into precipitation chamber 3-4 and two chambers of profit chamber 3-5 with tank body 3-1 inner chamber, described precipitation chamber 3-4 and profit chamber 3-5 are communicated with by water pipe 3-2, and water pipe 3-2 passes dividing plate 3-3 and firmly is welded on the dividing plate 3-3.
Owing to increased dividing plate 3-3 and water pipe 3-2, so that after oil-water mixture enters tank body 3-1 from oil-water mixture import 3-1-1, in tank body 3-1, separate in two chambers, stroke in tank body 3-1 has increased, corresponding profit also increased in the time of tank body 3-1, thereby so that the efficient of oily water separation has improved, can effectively reduce the quantity of using water-and-oil separator 3, prior art needs 15 water-and-oil separators at least, the present invention only 8 of need is just enough, has reduced cost when raising the efficiency.
Fig. 6 and shown in Figure 7 be multiple still kettle 4 among the present invention, include multiple distillation kettle 4-1, distill again kettle 4-1 and be provided with liquid outlet 4-1-1 and fluid inlet 4-1-3, distill again kettle 4-1 bottom and be provided with vapor distribution device 4-2, vapor distribution device 4-2 surrounds annular by 8 pipes, two tubes crisscross in annular, and all pipes interconnect formation, offer a plurality of production wells above the pipe, these pipes have one to stretch out outside the multiple distillation kettle 4-1.Distill again kettle 4-1 top tensimeter 4-4 is installed; Distill again kettle 4-1 bottom and be provided with sewage draining exit 4-1-2, with pipeline that sewage draining exit 4-1-2 is communicated with in be provided with wash water valve 4-3.
The mixture of Oleum Cinnamomi and water is water-and-oil separator 3 process natural sedimentations, oil of bay sedimentation, waterborne floating; But oil of bay and moisture are thorough not from getting, in the water on upper strata, also contain oil of bay, the mixture of the oil of bay on water-and-oil separator 3 upper stratas and water is input in the multiple distillation kettle 4-1 from fluid inlet 4-1-3, the mixing steam that distills from still kettle 1 enters in the multiple distillation kettle 4-1 from delivery of steam gas-distributing pipe road 4-2, hole steam out from the delivery of steam gas-distributing pipe 4-2, mixture to oil of bay and water heats, and monitors the pressure that distills again in the kettle 4-1 by tensimeter 4-4 in the process of multiple distillation; The mixture of oil of bay and water is through behind the revaporization, and the oil of bay that includes is evaporated enters condenser 2 through liquid outlet 4-1-1, and remaining water distills outside the kettle 4-1 again via wash water valve 4-3 discharge.
The natural meat oil of bay extracts: with the Chinese cassia tree branch, basyleaves are put into respectively two still kettles 1, then the water vapor in the boiler 6 is sprayed into the bottom of first still kettle 1 by steam-pipe, water vapor is with Chinese cassia tree branch in the still, Oleum Cinnamomi in the basyleaves steams rear formation mixing steam, mixing steam is through the bottom of second still kettle 1 of the top of first still kettle 1 input, Chinese cassia tree branch in second still kettle 1, Oleum Cinnamomi in the basyleaves also is evaporated together, mixing steam is through the thermal source of the multiple still kettle 4 do distillation mixing steams of the top of second still kettle 1 input, and multiple still kettle 4 tops mixing steam out is through condenser 2 condensations, enter water-and-oil separator 3 after the cooling and carry out oily water separation; Behind the steam supply number minute, the multiple still kettle 4 of mixing steam input of separating in the water-and-oil separator 3 is carried out multiple distillation; Distill complete after, residual waste liquid in the multiple still kettle 4 is transported to first still kettle 1, in next time distillation more once afterwards discharging of multiple distillation when carrying out.
Claims (1)
1. a natural meat oil of bay extraction equipment includes condenser (2), and a plurality of interconnective still kettles (1) and water-and-oil separator (3) is characterized in that: be connected with multiple still kettle (4) between described still kettle (1) and described condenser (2); Be connected with water pump (5) between described a plurality of water-and-oil separator (3) and the described multiple still kettle (4);
Described multiple still kettle (4), comprise the multiple distillation kettle (4-1) that is provided with liquid outlet (4-1-1) and fluid inlet (4-1-3), described kettle (4-1) inside of distilling again is provided with vapor distribution device (4-2), described vapor distribution device (4-2) surrounds annular by pipe, cross pipes is arranged in annular, and all pipes interconnect, and have at least one to stretch out the described outer pipe formation of kettle (4-1) of distilling again, on the described pipe of described vapor distribution device (4-2), be distributed with a plurality of production wells;
Described kettle (4-1) top of distilling again is equipped with tensimeter (4-4); Described kettle (4-1) bottom of distilling again is provided with sewage draining exit (4-1-2), with pipeline that described sewage draining exit (4-1-2) is communicated with in be provided with wash water valve (4-3);
Described condenser (2), include tank body (2-1) and be located at steam inlet (2-1-1), condensate outlet (2-1-2), water-in (2-2-1) and water outlet (2-2-2) on the described tank body (2-1), described tank body (2-1) inner chamber is equipped with by two by side plate and the upper port of sealing this two block side plates and the vortex steam flow passage (2-2) that lower port form of center to the inner rotary expansion; The import of described vortex steam flow passage (2-2) is communicated with the described steam inlet (2-1-1) that is located at tank body (2-1) upper end, and the outlet of described vortex steam flow passage (2-2) is communicated with condensate outlet (2-1-2) on being located at described tank body (2-1) sidewall; The bottom of described tank body (2-1) is provided with the drain outlet (2-1-3) that valve (2-3) is housed;
Described water-and-oil separator (3), comprise and be provided with oil-water mixture import (3-1-1), the tank body (3-1) of oil export (3-1-4) and water out (3-1-2), at described tank body (3-1) inner chamber dividing plate (3-3) is installed, the bottom of described dividing plate (3-3) becomes certain inclination angle with the bottom of described tank body (3-1) and is fixed on the sidewall of described tank body (3-1), described dividing plate (3-3) is separated into precipitation chamber (3-4) and profit chamber (3-5) two chambers with described tank body (3-1) inner chamber, described precipitation chamber (3-4) and profit chamber (3-5) are communicated with by the water pipe (3-2) that is installed on the described dividing plate (3-3), are provided with oil export (3-1-3) in bottom, described profit chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210519008.XA CN102952644B (en) | 2012-12-06 | 2012-12-06 | Device for extracting natural cinnamon oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210519008.XA CN102952644B (en) | 2012-12-06 | 2012-12-06 | Device for extracting natural cinnamon oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102952644A true CN102952644A (en) | 2013-03-06 |
| CN102952644B CN102952644B (en) | 2014-04-23 |
Family
ID=47762033
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210519008.XA Active CN102952644B (en) | 2012-12-06 | 2012-12-06 | Device for extracting natural cinnamon oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102952644B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019024132A1 (en) * | 2017-08-01 | 2019-02-07 | 张永森 | Distillation system |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87215211U (en) * | 1987-12-23 | 1988-08-31 | 湖南省津市市香料厂 | Equipment for refining fragrant oil |
| CN1347971A (en) * | 2001-09-18 | 2002-05-08 | 沈雪荣 | Cassia oil extracting process from cassia twig and leaf |
| CN1528871A (en) * | 2003-09-26 | 2004-09-15 | 沈雪荣 | Improved method for extracting cinnamon barkoil from cinnamon branck and leaf |
| CN1563311A (en) * | 2004-03-31 | 2005-01-12 | 邱云彪 | Technique for extracting rhodamine oil |
| CN2721190Y (en) * | 2003-07-02 | 2005-08-31 | 冯锦堃 | Oil and water separator |
| CN201940071U (en) * | 2011-03-03 | 2011-08-24 | 河北奥星集团药业有限公司 | Separation and collection device for traditional Chinese medicinevolatile oil |
| CN202030729U (en) * | 2011-04-28 | 2011-11-09 | 成都永泰制药化工机械厂 | Plant distillation separating device |
| CN202968523U (en) * | 2012-12-06 | 2013-06-05 | 广西京桂香料有限公司 | Natural cinnamon oil extraction equipment |
-
2012
- 2012-12-06 CN CN201210519008.XA patent/CN102952644B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN87215211U (en) * | 1987-12-23 | 1988-08-31 | 湖南省津市市香料厂 | Equipment for refining fragrant oil |
| CN1347971A (en) * | 2001-09-18 | 2002-05-08 | 沈雪荣 | Cassia oil extracting process from cassia twig and leaf |
| CN2721190Y (en) * | 2003-07-02 | 2005-08-31 | 冯锦堃 | Oil and water separator |
| CN1528871A (en) * | 2003-09-26 | 2004-09-15 | 沈雪荣 | Improved method for extracting cinnamon barkoil from cinnamon branck and leaf |
| CN1563311A (en) * | 2004-03-31 | 2005-01-12 | 邱云彪 | Technique for extracting rhodamine oil |
| CN201940071U (en) * | 2011-03-03 | 2011-08-24 | 河北奥星集团药业有限公司 | Separation and collection device for traditional Chinese medicinevolatile oil |
| CN202030729U (en) * | 2011-04-28 | 2011-11-09 | 成都永泰制药化工机械厂 | Plant distillation separating device |
| CN202968523U (en) * | 2012-12-06 | 2013-06-05 | 广西京桂香料有限公司 | Natural cinnamon oil extraction equipment |
Non-Patent Citations (2)
| Title |
|---|
| 徐怀德: "《天然产物提取工艺学》", 30 June 2008, 中国轻工业出版社 * |
| 路乘风 等: "《防尘防毒技术》", 31 March 2004, 化学工业出版社 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2019024132A1 (en) * | 2017-08-01 | 2019-02-07 | 张永森 | Distillation system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102952644B (en) | 2014-04-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102952629B (en) | Technological method for extracting natural cinnamon oil | |
| CN202359093U (en) | Plant essential oil extraction device | |
| CN102363085A (en) | Method and special device for extracting and concentrating water extraction liquid medicine of Chinese medicine | |
| CN105251226A (en) | Anti-scaling concentration treatment process of traditional Chinese medicine water extraction solution | |
| CN202968523U (en) | Natural cinnamon oil extraction equipment | |
| CN2879085Y (en) | Condensing device for vacuum extracting concentrated packaging machine | |
| CN206705724U (en) | A kind of environmental protection and energy saving waste water distilling apparatus | |
| CN102952644B (en) | Device for extracting natural cinnamon oil | |
| CN103055536B (en) | A kind of circumfluence distillation concentrator | |
| CN205974481U (en) | Wine liquid heating evaporation system of cyclic utilization wine vapour heat energy | |
| WO2008138212A1 (en) | Multitower energysaving distillation system | |
| CN2778277Y (en) | Chinese medicinal liquor vacuum condensation equipment | |
| CN208641815U (en) | A kind of acetone, methanol extraction rectifier unit | |
| CN101358157B (en) | Method for extracting cinnamon oil using fluidized-bed and apparatus thereof | |
| CN103908799A (en) | Extracting and concentrating all-in-one machine | |
| CN109529403A (en) | Energy-saving dual-use traditional Chinese medicine extraction, concentrator | |
| CN206121195U (en) | Many materials multiple effect evaporation device | |
| CN209548763U (en) | Energy-saving dual-use traditional Chinese medicine extraction, concentrator | |
| CN202542898U (en) | Heat pipe type low-temperature multi-effect seawater dilution system | |
| CN202968521U (en) | Natural cinnamon oil redistillation still | |
| CN102964229A (en) | Natural cinnamaldehyde extraction device | |
| CN202223933U (en) | Cycle extrusion extraction and low-temperature concentration equipment | |
| CN104906161B (en) | Processing and extracting equipment for blumea balsamifera | |
| CN206142860U (en) | Device is used multipurposely to used heat | |
| CN205182241U (en) | Continuous extracting device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Application publication date: 20130306 Assignee: Guangxi Tengxian Fuhua Chemical Co.,Ltd. Assignor: Guangxi Jingguo Perfume Co.,Ltd. Contract record no.: X2024980000323 Denomination of invention: Natural cinnamon oil extraction equipment Granted publication date: 20140423 License type: Common License Record date: 20240108 |