CN205133556U - Cinnamon essential oil separator - Google Patents
Cinnamon essential oil separator Download PDFInfo
- Publication number
- CN205133556U CN205133556U CN201520830267.3U CN201520830267U CN205133556U CN 205133556 U CN205133556 U CN 205133556U CN 201520830267 U CN201520830267 U CN 201520830267U CN 205133556 U CN205133556 U CN 205133556U
- Authority
- CN
- China
- Prior art keywords
- pipe
- oil
- condenser
- distillate
- still kettle
- 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.)
- Active
Links
Landscapes
- Fats And Perfumes (AREA)
Abstract
The utility model discloses a cinnamon essential oil separator, including stills, condenser and oil water separator, stills's distillation export is through inlet pipe and condenser inner chamber intercommunication, the inner chamber of condenser and oil water separator's feed inlet intercommunication, the condenser is vertical to be placed, the casing of inclosed cylinder around the condenser includes, the casing lower extreme is provided with coolant liquid import, and the upper end is provided with cooling liquid exit, and seal installation has and is spiral helicine distillate pipe in the casing, the last port of distillate pipe passes through inlet pipe and stills's export intercommunication, the port passes through discharging pipe and oil water separator's feed inlet intercommunication under the distillate pipe, cooling liquid exit is connected with the reservoir, the reservoir passes through transfer line and stills intercommunication. Spiral helicine distillate pipe makes the flowing through distance of high temperature distillate in the spiral pipe increase, the hot exchange time length of side, and the low temperature distillate that makes the high temperature distillate become has improved cinnamon essential oil's output rate.
Description
Technical field
The utility model relates to a kind of cinnamon essential oil tripping device.
Background technology
Chinese cassia tree is the medicinal and edible plants material that the Ministry of Health of China announces, and can eat, be again rare traditional Chinese medicine flJ.Cinnamon essential oil extracts from the dry branch of Chinese cassia tree, leaf the volatile oil obtained, and is the clarified liq in yellow or yellowish brown.Research finds, Oleum Cinnamomi have calmness, analgesia, antipyretic, anticonvulsion, strengthen gastrointestinal peristalsis, cholagogic, the effect B31 such as antitumor, be the main raw material of medicine industry, foodstuffs industry and chemical engineering industry, be usually used in the food such as beverage, candy, can in the food industry.
Extract in the process of cinnamon essential oil adopting distillation method, be evaporated mixing steam through condenser condenses post liquefaction from still kettle, carry out oily water separation again, that oil mixing with water vapour is by the condensation of horizontal straight pipe condensation device at existing condensation process, but because condensation time short-range missile causes, condensation effect is low, and distillate temperature mostly is more than 50 DEG C, a lot of alcohols aromatoising substance cannot fully be separated out, and distillate yield poorly.
Utility model content
The utility model provides a kind of cinnamon essential oil tripping device, at least one to solve the problem.
According to an aspect of the present utility model, provide a kind of cinnamon essential oil tripping device, comprise still kettle, condenser and water-and-oil separator, the distillation outlet of described still kettle is by feed-pipe and condenser inner space, the inner chamber of described condenser is communicated with the opening for feed of water-and-oil separator, described condenser is vertically placed, condenser comprises the airtight columnar housing of surrounding, described housing lower end is provided with cooling liquid inlet, upper end is provided with cooling liquid outlet, spiral distillate pipe is sealed and installed with in housing, the upper port of described distillate pipe is by the outlet of feed-pipe and still kettle, described distillate infratubal port is communicated with the opening for feed of water-and-oil separator by discharge nozzle, described cooling liquid outlet is connected with reservoir, described reservoir is communicated with still kettle by tubing.
Further, still kettle is hollow structure, and bottom is heating zone, and top is distillation zone, still kettle kettle is offered porose, and this hole is accompanied with sealing cover.
Further, reservoir is communicated with still kettle heating zone by tubing.
Further, feed-pipe is provided with first flow control valve, discharge nozzle is provided with second control valve.
Further, described water-and-oil separator comprises staving, and staving is provided with oil-in, staving bottom is provided with oil spilling outlet, the outlet of described oil spilling connects oil outlet pipe, and described staving is provided with the equilibration tube be communicated with staving, and the inwall lowest part of described equilibration tube is higher than the highest point of oil spilling leak.
The utility model has the advantage of: because condenser is vertically placed, being conducive to condensed distillating liquid is expelled to oil-liquid separator by gravity from the distillate infratubal port of condenser, be beneficial to the recovery of distillating liquid, spiral helicine distillate pipe, the flow through distance of high temperature distillate in spiral tube can be made to increase, the heat exchanger time length of side, thus the low temperature distillate that high temperature distillate can be made finally to become, be separated by water-and-oil separator again after the temperature reduction of distillate, improve the output capacity of Flos Rosae Rugosae quintessence oil.
Accompanying drawing explanation
Fig. 1 is the structural representation of the cinnamon essential oil tripping device of a kind of embodiment of the utility model.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
Fig. 1 show schematically show the cinnamon essential oil tripping device according to a kind of embodiment of the present utility model.
As shown in Figure 1, cinnamon essential oil tripping device of the present utility model, comprises still kettle 1, condenser 2 and water-and-oil separator 3; Still kettle 1 is positioned at condenser 2 side, and the distillation outlet of still kettle 1 is directly communicated with condenser 2 inside; Water-and-oil separator 3 is also positioned at condenser 2 opposite side, the mixing liquid of deriving from the condensate outlet of condenser 2 flows in water-and-oil separator 3 through discharge nozzle 6 from the opening for feed of water-and-oil separator 3, condenser 2 is vertically placed, and the upper end of condenser 2 is by the outlet of feed-pipe 5 with still kettle 1.
Still kettle 1 is hollow structure, and bottom is heating zone 11, and top is distillation zone 12, and still kettle 1 kettle offers porose 13, and this hole 13 is accompanied with sealing cover.Still kettle 1 also comprises dividing plate 14, and it is inner that dividing plate 14 is movably arranged on still kettle 1.Dividing plate 14 is folding, puts into still kettle 1 from hole 13.According to the difference of extracting process, direct water raw material being put into heating zone 11 had boils, and has plenty of to be placed on dividing plate 14 and steams, when water raw material being put into heating zone 11 boils, can take off dividing plate 14.
As shown in Figure 1, condenser 2 comprises the airtight columnar housing 21 of surrounding, housing 21 lower end is provided with cooling liquid inlet 23, upper end is provided with cooling liquid outlet 24, spiral distillate pipe 22 is sealed and installed with in housing 21, the upper port of distillate pipe 22 is by the outlet of feed-pipe 5 with still kettle 1, feed-pipe 5 is provided with first flow control valve 51, the flow of steam can be controlled, distillate pipe 22 lower port is communicated with the opening for feed of water-and-oil separator 3 by discharge nozzle 6, discharge nozzle 6 is provided with second control valve 61, the flow of distillate can be controlled, cooling liquid outlet 24 is connected with reservoir 4 by conduit 7, can reclaim the condensed fluid of condenser, reservoir 4 is communicated with the heating zone 11 of still kettle 1 by tubing 8, can reclaim again condensed fluid, cost-saving, tubing 8 is provided with the 3rd flowrate control valve 81, the flow of condensed fluid can be controlled.
As shown in Figure 1, water-and-oil separator 3, comprises staving, oil-in, oil spilling mouth, equilibration tube 32.Wherein, oil spilling mouth is arranged on bottom staving and is communicated with oil outlet pipe 31, and oil outlet pipe 31 connects oil plant storing device (not shown); The first half that oil-in is arranged on staving is communicated with conduit 18, and for injecting oil-water mixture in staving, oil-in setting position also can change according to actual needs; Equilibration tube 32 is arranged on the staving above oil spilling mouth, is communicated with staving, and equilibration tube 32 inwall lowest part is higher than oil spilling mouth end face 5CM-8CM, so that the oil after being separated flows out from oil outlet pipe 31; If equilibration tube 32 arranges too high, then easy by the water inflow oil outlet pipe 31 in oil mixing with water liquid when being separated, thus the oily purity reduced after separation maybe cannot be separated; If equilibration tube 32 arranges too low, then reduce separation efficiency, and cause the oil-in-water after being separated to divide content many, cause waste.
Working process of the present utility model is as follows: the sealing cover opening still kettle 1, adds appropriate water in still kettle 1 heating zone 11, raw material is directly put into the water of heating zone 11 or is put on dividing plate 14.Heat heating zone 11, thermal source can select electric heat source, naked light thermal source etc.Cooling fluid flows into housing 21 from cooling liquid inlet 23, cooling fluid is by coated distillate pipe 22, high temperature profit mixed vapour flows into distillate pipe 22 by feed-pipe 5, now, high temperature profit mixed vapour liquefies rapidly, and because condenser is vertically placed, oil mixing with water liquid gravitate flows downward, and flows into water-and-oil separator 3 by discharge nozzle 6; Because the density ratio water of cinnamon essential oil is large, proportion is relatively heavier, and after entering water-and-oil separator 3, essential oil is sunken under water.In staving, oil mixing with water liquid increases gradually, because equilibration tube 32 inwall lowest part is higher than the end face of oil spilling mouth, in staving, oil mixing with water liquid separation surface is passed in time and is continued to rise, after separation surface is higher than equilibration tube 32 end face, under cinnamon essential oil layer by layer can overflow from oil spilling mouth smoothly and flow into oil plant storing device through oil outlet pipe 31; Meanwhile, due to the effect of equilibration tube 32, can remain that the separation surface of oil mixing with water liquid in staving remains higher than oil outlet, thus prevent the water in oil mixing with water liquid from flowing out from oil outlet 31, cause the purity drop of separation.
Known by describing above, the utility model has the advantage of: because condenser is vertically placed, being conducive to condensed distillating liquid is expelled to oil-liquid separator by gravity from the distillate infratubal port of condenser, be beneficial to the recovery of distillating liquid, spiral helicine distillate pipe, the flow through distance of high temperature distillate in spiral tube can be made to increase, the heat exchanger time length of side, thus the low temperature distillate that high temperature distillate can be made finally to become, be separated by water-and-oil separator again after the temperature reduction of distillate, improve the output capacity of Flos Rosae Rugosae quintessence oil.
Above-described is only embodiments more of the present utility model.For the person of ordinary skill of the art, under the prerequisite not departing from the utility model creation design, can also make some distortion and improvement, these all belong to protection domain of the present utility model.
Claims (5)
1. a cinnamon essential oil tripping device, comprise still kettle, condenser and water-and-oil separator, the distillation outlet of described still kettle is by feed-pipe and condenser inner space, the inner chamber of described condenser is communicated with the opening for feed of water-and-oil separator, it is characterized in that, described condenser is vertically placed, condenser comprises the airtight columnar housing of surrounding, described housing lower end is provided with cooling liquid inlet, upper end is provided with cooling liquid outlet, spiral distillate pipe is sealed and installed with in housing, the upper port of described distillate pipe is by the outlet of feed-pipe and still kettle, described distillate infratubal port is communicated with the opening for feed of water-and-oil separator by discharge nozzle, described cooling liquid outlet is connected with reservoir, described reservoir is communicated with still kettle by tubing.
2. a kind of cinnamon essential oil tripping device according to claim 1, is characterized in that, described still kettle is hollow structure, and bottom is heating zone, and top is distillation zone, still kettle kettle is offered porose, and this hole is accompanied with sealing cover.
3. a kind of cinnamon essential oil tripping device according to claim 2, it is characterized in that, described reservoir is communicated with still kettle heating zone by tubing.
4. a kind of cinnamon essential oil tripping device according to claim 3, is characterized in that, feed-pipe is provided with first flow control valve, discharge nozzle is provided with second control valve.
5. a kind of cinnamon essential oil tripping device according to claim 1, it is characterized in that, described water-and-oil separator comprises staving, staving is provided with oil-in, staving bottom is provided with oil spilling outlet, the outlet of described oil spilling connects oil outlet pipe, and described staving is provided with the equilibration tube be communicated with staving, and the inwall lowest part of described equilibration tube is higher than the highest point of oil spilling leak.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520830267.3U CN205133556U (en) | 2015-10-21 | 2015-10-21 | Cinnamon essential oil separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520830267.3U CN205133556U (en) | 2015-10-21 | 2015-10-21 | Cinnamon essential oil separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205133556U true CN205133556U (en) | 2016-04-06 |
Family
ID=55619367
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520830267.3U Active CN205133556U (en) | 2015-10-21 | 2015-10-21 | Cinnamon essential oil separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205133556U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105918552A (en) * | 2016-05-05 | 2016-09-07 | 贵州绿太阳制药有限公司 | Chrysanthemum enzyme deactivating and drying system |
| CN106893636A (en) * | 2017-05-05 | 2017-06-27 | 湖北职业技术学院 | A kind of Rosa Damascana extraction element |
| CN105928332B (en) * | 2016-05-05 | 2018-06-29 | 贵州绿太阳制药有限公司 | A kind of chrysanthemum central heating suction type dries water-removing system |
-
2015
- 2015-10-21 CN CN201520830267.3U patent/CN205133556U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105918552A (en) * | 2016-05-05 | 2016-09-07 | 贵州绿太阳制药有限公司 | Chrysanthemum enzyme deactivating and drying system |
| CN105928332B (en) * | 2016-05-05 | 2018-06-29 | 贵州绿太阳制药有限公司 | A kind of chrysanthemum central heating suction type dries water-removing system |
| CN106893636A (en) * | 2017-05-05 | 2017-06-27 | 湖北职业技术学院 | A kind of Rosa Damascana extraction element |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102952629B (en) | Technological method for extracting natural cinnamon oil | |
| CN205133556U (en) | Cinnamon essential oil separator | |
| CN204939435U (en) | A kind of family expenses essential oil distillation extraction device | |
| CN206980170U (en) | A kind of Chinese medicine ethanol extracts rapid concentration equipment integrating | |
| CN205287666U (en) | Concentrated cauldron of extrinsic cycle fractionation by distillation | |
| CN202506170U (en) | Material extraction device | |
| CN104922921B (en) | A kind of self-loopa MVR thermo-compression evaporation systems | |
| CN204502440U (en) | One Plants sesame oil boiler | |
| CN205815150U (en) | A kind of decompression rectification device | |
| CN103007572B (en) | Medicine extraction device and technique thereof | |
| CN107937137A (en) | A kind of high efficient cryogenic extraction of essential oil system and its production technology | |
| CN208641815U (en) | A kind of acetone, methanol extraction rectifier unit | |
| CN103801102B (en) | A kind of variable post of many gradients imitates rectifier unit | |
| CN105273845A (en) | Rose oil distillation purification unit | |
| CN206881185U (en) | A kind of rectification experimental apparatus | |
| CN103992880B (en) | A kind of volatile oil high efficiency extraction separator | |
| CN207445611U (en) | A kind of Salvia root P.E enrichment facility | |
| CN2432935Y (en) | Continuous circulation extracting-concentration equipment | |
| CN207130215U (en) | A kind of system for producing middle matter washing oil | |
| CN206444249U (en) | Oil water separator and oil water separator system | |
| CN206995904U (en) | Condensing source heat pump driving multiple-effect horizontal tube falling film destilling tower | |
| CN205035348U (en) | Cinnamon essential oil extraction element | |
| CN100534407C (en) | Concentrated machine for distilling Chinese herbal medicine | |
| CN203425547U (en) | Reboiling and flash evaporation fractionating tower | |
| CN202968523U (en) | Natural cinnamon oil extraction equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: 527200 Shuangdong environmental protection industrial park, Luoding City, Yunfu City, Guangdong Province Patentee after: Guangdong Rongxing flavor Technology Co.,Ltd. Address before: 527245 No.98 Guanghai West Road, Silun Town, Luoding City, Yunfu City, Guangdong Province Patentee before: LUODING RONGXING PERFUMERY Co.,Ltd. |