CN203498355U - Rose essential oil condensing equipment - Google Patents
Rose essential oil condensing equipment Download PDFInfo
- Publication number
- CN203498355U CN203498355U CN201320588904.1U CN201320588904U CN203498355U CN 203498355 U CN203498355 U CN 203498355U CN 201320588904 U CN201320588904 U CN 201320588904U CN 203498355 U CN203498355 U CN 203498355U
- Authority
- CN
- China
- Prior art keywords
- distillate
- oil
- level condenser
- essential oil
- condensing equipment
- 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.)
- Withdrawn - After Issue
Links
Images
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Fats And Perfumes (AREA)
Abstract
The utility model relates to rose essential oil condensing equipment. The rose essential oil condensing equipment comprises a first-level condenser and a second-level condenser, wherein the first-level condenser and the second-level condenser are vertically arranged; the-first level condenser comprises a first-level condenser shell which is cylindrical and airtight at the periphery, and the second-level condenser comprises a second-level condenser shell which is cylindrical and airtight at the periphery and a spiral pipe which is spirally arranged in an inner cavity of the second-level condenser shell; oil-water mixed steam firstly enters a closed inner cavity of the first-level condenser to be condensed so as to form a distillate the temperature of which is 55-70 DEG C, the distillate the temperature of which is 55-70 DEG C is conveyed by the spiral pipe which is spirally arranged in the inner cavity of the second-level condenser shell into the second-level condenser to be condensed for the second time so as to form a distillate the temperature of which is 25-35 DEG C, the distillate the temperature of which is 25-35 DEG C is finally conveyed to an oil-water separator, and finally, a rose essential oil is obtained. The rose essential oil condensing equipment provided by the utility model has the advantages that the oil extraction rate of the rose essential oil through two-time condensation is improved from 0.024% to 0.028% by adopting a horizontal type straight pipe condenser, and the output capacity of the rose essential oil is improved.
Description
Technical field
The utility model relates to Flos Rosae Rugosae quintessence oil and extracts production technical field, is specifically related to a kind of Flos Rosae Rugosae quintessence oil condensing equipment.
Background technology
Flos Rosae Rugosae quintessence oil is the king of natural plant essential oils, is widely used in beauty treatment, body beautification, food, tobacco and perfume makeup deodorant tune.Flos Rosae Rugosae quintessence oil processing is divided into three parts: distillation, condensation, oily water separation, key link is condensation.Tradition condensation process be oil mixing with water vapour by horizontal straight tube condenser condenses, still because condensation time short-range missile causes, condensation effect is low, distillate temperature mostly is more than 50 ℃, a lot of alcohols aromatoising substances cannot fully be separated out, and distillate yields poorly.
Utility model content
The utility model, in order to overcome the deficiency of above technology, provides a kind of Flos Rosae Rugosae quintessence oil condensing equipment that improves Flos Rosae Rugosae quintessence oil output capacity by time condensation.
The utility model overcomes the technical scheme that its technical problem adopts:
This Flos Rosae Rugosae quintessence oil condensing equipment, it is characterized in that: the first-stage condenser and the secondary condenser that comprise vertical setting, described first-stage condenser comprises the columnar first-stage condenser housing that surrounding is airtight, described first-stage condenser housing upper end is provided with its lower end of oil and gas import and is provided with distillate outlet I, in described first-stage condenser housing, be sealed and installed with some vertical cold water pipes, described cold water pipe is connected in water pump by valve, described oil and gas import is connected in the outlet of still kettle by pipeline, described secondary condenser comprises the secondary condenser housing that surrounding is airtight, helical disk cloth is installed on the spiral tube in secondary condenser housing inner chamber, be arranged at the cold water inlet of secondary condenser housing below, described cold water inlet is connected in water pump by valve, described spiral tube upper end is that its lower end of distillate import is distillate outlet II, described distillate import is connected in distillate outlet I by pipeline, described distillate outlet II is connected in the fluid inlet of water-and-oil separator by drain pipe.
Controlled in order to realize flow, flowrate control valve I is installed on the connecting pipeline between above-mentioned oil and gas import and still kettle.
Controlled in order to realize flow, on the connecting pipeline between above-mentioned distillate outlet I and distillate import, flowrate control valve II is installed.
The beneficial effects of the utility model are: oil mixing with water vapour becomes the high temperature distillate of 55-70 ℃ after by first-stage condenser, the spiral tube of flowing through again afterwards in secondary condenser, because spiral tube is spiral, therefore the flow through distance of high temperature distillate in spiral tube increases, the heat exchanger time length of side, thereby can make high temperature distillate finally become temperature is the low temperature distillate of 25-35 ℃, the temperature of distillate after reducing again the oil yield by making Flos Rosae Rugosae quintessence oil after water-and-oil separator separation by what adopt horizontal straight tube condenser condenses, 0.024% bring up to 0.028%, improved the output capacity of Flos Rosae Rugosae quintessence oil.By the geraniol in Flos Rosae Rugosae quintessence oil after 2 condensations, become 40%-45% from original 48%-55%, Geraniol becomes 10%-15% from original 15%-20%.And with respect to traditional technology, trans rose oxide, cis rose oxide, а-Terpineol 350, bata-phenethyl alcohol, 2, the compositions such as 7-dimethyl-1-octanol and geraniol formate are effectively separated out, and Flos Rosae Rugosae quintessence oil quality is improved, and composition range meets international Flos Rosae Rugosae quintessence oil standard.
Accompanying drawing explanation
Fig. 1 is condensing equipment structural representation of the present utility model;
Fig. 2 is a condensing works structural representation of the present utility model;
Fig. 3 is secondary condensing unit structural representation of the present utility model;
In figure, 1. still kettle 2. first-stage condenser 3. secondary condenser 4. drain pipe 5. water-and-oil separator 6. first-stage condenser housing 7. oil and gas import 8. cold water pipe 9. distillate outlet I 10. secondary condenser housing 11. spiral tube 12. distillate import 13. distillates export II 14. cold water inlets.
Embodiment
Below in conjunction with accompanying drawing 1, accompanying drawing 2,3 pairs of the utility model of accompanying drawing, be described further.
This Flos Rosae Rugosae quintessence oil condensing equipment, the first-stage condenser 2 and the secondary condenser 3 that comprise vertical setting, described first-stage condenser 2 comprises the columnar first-stage condenser housing 6 that surrounding is airtight, described first-stage condenser housing 6 upper ends are provided with oil and gas import 7 its lower ends and are provided with distillate outlet I 9, in described first-stage condenser housing 6, be sealed and installed with some vertical cold water pipes 8, described cold water pipe 8 is connected in water pump by valve, described oil and gas import 7 is connected in the outlet of still kettle 1 by pipeline, described secondary condenser 3 comprises the secondary condenser housing 10 that surrounding is airtight, helical disk cloth is installed on the spiral tube 11 in secondary condenser housing 10 inner chambers, be arranged at the cold water inlet 14 of secondary condenser housing 10 belows, described cold water inlet 14 is connected in water pump by valve, described spiral tube 11 upper ends are that distillate import 12 its lower ends are distillate outlet II 13, described distillate import 12 is connected in distillate outlet I 9 by pipeline, described distillate outlet II 13 is connected in the fluid inlet of water-and-oil separator 5 by drain pipe 4.It is the oil mixing with water vapour of 95-100 ℃ that still kettle 1 is distilled formation temperature by fresh rose flower, by pipeline, utilize oil and gas import 7 to enter in the inner chamber of first-stage condenser housing 6 afterwards, Open valve makes to pass into cold water in cold water pipe 8, oil mixing with water vapour is the high temperature distillate of 55-70 ℃ in the interior condensation formation temperature of first-stage condenser 2, high temperature distillate exports I 9 by distillate and flows out and enter in the spiral tube 11 of secondary condenser housing 10 inside through distillate import 12, Open valve makes to be full of cold water in secondary condenser 3 by cold water inlet 14, because making high temperature distillate length of flow across, spiral tube 11 becomes, thereby the high temperature distillate distillate that after long-time and cold water heat exchange condensation, formation temperature is 25-35 ℃ through spiral pipeline 11, finally by distillate, export II 13 outflows and in drain pipe 4 is input to water-and-oil separator 5, carry out oily water separation, thereby finally obtain Flos Rosae Rugosae quintessence oil.Because spiral tube 11 is spiral, therefore the flow through distance of high temperature distillate in spiral tube 11 increases, the heat exchanger time length of side, thereby can make high temperature distillate finally become temperature is the low temperature distillate of 25-35 ℃, the temperature of distillate after reducing again the oil yield by making Flos Rosae Rugosae quintessence oil after water-and-oil separator 5 separation by what adopt horizontal straight tube condenser condenses, 0.024% bring up to 0.028%, and the condensation time short-range missile of traditional technology causes distillate temperature more than 50 ℃, a lot of alcohols aromatoising substances cannot fully be separated out.And by after 2 condensations, because distillate condensation effect is good, distillate temperature is low, thereby the geraniol in Flos Rosae Rugosae quintessence oil becomes 40%-45% from original 48%-55%, and Geraniol becomes 10%-15% from original 15%-20%.And with respect to traditional technology, trans rose oxide, cis rose oxide, а-Terpineol 350, bata-phenethyl alcohol, 2, the compositions such as 7-dimethyl-1-octanol and geraniol formate are effectively separated out, and Flos Rosae Rugosae quintessence oil quality is improved, and composition range meets international Flos Rosae Rugosae quintessence oil standard.
On connecting pipeline between above-mentioned oil and gas import 7 and still kettle 1, flowrate control valve I can be installed.On connecting pipeline between distillate outlet I 9 and distillate import 12, flowrate control valve II can be installed.By flowrate control valve I and flowrate control valve II, can adjust the oil mixing with water vapour 5L/min in first-stage condenser 2, and the flow 2-3L/min that adjusts low temperature distillate, make it can guarantee the condensation time, can guarantee production efficiency again.
Claims (3)
1. a rhodamine b extra 500 condensing equipment, it is characterized in that: the first-stage condenser (2) and the secondary condenser (3) that comprise vertical setting, described first-stage condenser (2) comprises the columnar first-stage condenser housing (6) that surrounding is airtight, described first-stage condenser housing (6) upper end is provided with its lower end of oil and gas import (7) and is provided with distillate outlet I (9), in described first-stage condenser housing (6), be sealed and installed with some vertical cold water pipes (8), described cold water pipe (8) is connected in water pump by valve, described oil and gas import (7) is connected in the outlet of still kettle (1) by pipeline, described secondary condenser (3) comprises the secondary condenser housing (10) that surrounding is airtight, helical disk cloth is installed on the spiral tube (11) in secondary condenser housing (10) inner chamber, be arranged at the cold water inlet (14) of secondary condenser housing (10) below, described cold water inlet (14) is connected in water pump by valve, described spiral tube (11) upper end is that its lower end of distillate import (12) is distillate outlet II (13), described distillate import (12) is connected in distillate outlet I (9) by pipeline, described distillate outlet II (13) is connected in the fluid inlet of water-and-oil separator (5) by drain pipe (4).
2. Flos Rosae Rugosae quintessence oil condensing equipment according to claim 1, is characterized in that: on the connecting pipeline between described oil and gas import (7) and still kettle (1), flowrate control valve I is installed.
3. Flos Rosae Rugosae quintessence oil condensing equipment according to claim 1, is characterized in that: on the connecting pipeline between described distillate outlet I (9) and distillate import (12), flowrate control valve II is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320588904.1U CN203498355U (en) | 2013-09-24 | 2013-09-24 | Rose essential oil condensing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320588904.1U CN203498355U (en) | 2013-09-24 | 2013-09-24 | Rose essential oil condensing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203498355U true CN203498355U (en) | 2014-03-26 |
Family
ID=50329352
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320588904.1U Withdrawn - After Issue CN203498355U (en) | 2013-09-24 | 2013-09-24 | Rose essential oil condensing equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203498355U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103484255A (en) * | 2013-09-24 | 2014-01-01 | 济南惠农玫瑰花精油有限公司 | Secondary condensation extraction process and condensation equipment for rose essential oil |
| CN105062690A (en) * | 2015-09-09 | 2015-11-18 | 魏新强 | Plant essential oil extraction device |
| CN105441196A (en) * | 2015-12-30 | 2016-03-30 | 安徽银丰药业股份有限公司 | Device for extracting peppermint oil |
-
2013
- 2013-09-24 CN CN201320588904.1U patent/CN203498355U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103484255A (en) * | 2013-09-24 | 2014-01-01 | 济南惠农玫瑰花精油有限公司 | Secondary condensation extraction process and condensation equipment for rose essential oil |
| CN103484255B (en) * | 2013-09-24 | 2015-03-25 | 济南惠农玫瑰花精油有限公司 | Secondary condensation extraction process and condensation equipment for rose essential oil |
| CN105062690A (en) * | 2015-09-09 | 2015-11-18 | 魏新强 | Plant essential oil extraction device |
| CN105062690B (en) * | 2015-09-09 | 2018-12-07 | 四川艾朗特生物科技有限公司 | Essential oil extraction device |
| CN105441196A (en) * | 2015-12-30 | 2016-03-30 | 安徽银丰药业股份有限公司 | Device for extracting peppermint oil |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203498355U (en) | Rose essential oil condensing equipment | |
| CN103484255B (en) | Secondary condensation extraction process and condensation equipment for rose essential oil | |
| CN204853428U (en) | Energy -efficient cast aluminium body | |
| CN205133556U (en) | Cinnamon essential oil separator | |
| CN201688387U (en) | Steam generator | |
| CN204563648U (en) | A kind of reboiler of energy efficiency | |
| CN207468568U (en) | A kind of forced-ventilated plants essential oil extraction equipment | |
| CN204434587U (en) | Fruit wine vacuum distillation device | |
| CN205133558U (en) | Rose essential oil extraction device | |
| CN204602153U (en) | Liquid material recycling of condensed steam utilizes device | |
| CN204265469U (en) | A kind of negative pressure ammonia still | |
| CN205035344U (en) | Jar is drawed to rose essential oil negative pressure | |
| CN203803146U (en) | Dendrobe active ingredient extraction mechanism | |
| CN105586231A (en) | Two-time-distillation and two-time-cooling brewing extraction device | |
| CN102698450A (en) | Two-stage falling-climbing film evaporator | |
| CN201710983U (en) | Solvent distilling apparatus for extracting capsochrome | |
| CN204665955U (en) | The cold broken preheater of a kind of liquid material | |
| CN205501273U (en) | Distillation cooling production system of morat | |
| CN204607960U (en) | A kind of device slightly carrying natural Broneolum Syntheticum from borneol camphor tree | |
| CN103908790B (en) | A kind of tannin extract is produced the unpowered of evaporization process and is automatically turned liquid method | |
| CN205933290U (en) | Energy -saving water purification machine | |
| CN205295285U (en) | Draw device of peppermint oil | |
| CN104355345A (en) | Negative-pressure ammonia distillation tower and ammonia distillation method | |
| CN202671462U (en) | Ethanol purification equipment with precise temperature control function | |
| CN209161982U (en) | A kind of water-oil separating mechanism extracted for plants essential oil |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140326 Effective date of abandoning: 20150325 |
|
| AV01 | Patent right actively abandoned |
Granted publication date: 20140326 Effective date of abandoning: 20150325 |
|
| RGAV | Abandon patent right to avoid regrant |