CN207276584U - A kind of fragrant plant hydrosol extraction of essential oil system - Google Patents
A kind of fragrant plant hydrosol extraction of essential oil system Download PDFInfo
- Publication number
- CN207276584U CN207276584U CN201721251538.5U CN201721251538U CN207276584U CN 207276584 U CN207276584 U CN 207276584U CN 201721251538 U CN201721251538 U CN 201721251538U CN 207276584 U CN207276584 U CN 207276584U
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- level
- autoclave body
- extraction
- essential oil
- distillation device
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Abstract
A kind of fragrant plant hydrosol extraction of essential oil system, including level-one distilling apparatus, secondary distillation device, condenser and oil water separator, the level-one distilling apparatus is connected by charging gear with secondary distillation device, and level-one distilling apparatus is respectively communicated with the condenser and oil water separator of one group of interconnection with secondary distillation device respectively.The utility model overcomes the not high technical barrier of hydrosol quality during traditional extensive extraction of essential oil, using secondary distillation device, high-quality hydrosol in fresh flower is directed in level-one distillation and is extracted the extraction for being delivered to by charging gear essential oil is carried out in secondary distillation device again, full section extraction process is recycled continuous operation, it ensure that the extraction efficiency of essential oil while high-quality hydrosol extraction operation is remained, avoid the forfeiture of fragrance and active ingredient in just section extraction in fresh flower.
Description
Technical field
The utility model belongs to fragrant plant processing, extraction field, especially a kind of fragrant plant hydrosol extraction of essential oil system
System.
Background technology
At present, during conventional fragrant plant carries out extraction of essential oil, generally essence is improved using the means such as immersion, broken
The extraction efficiency of oil, but so way can seriously affect the extraction quality of first section hydrosol, make especially for using fresh petal
For in the fragrant plant hydrosol extraction of raw material, the hydrosol extraction of first section high concentration high quality is difficult to apply to large-scale production and works as
In.
Rose is the byproduct in Rosa Damascana production process, its fragrance is simple and elegant, rich in a variety of beneficial to human body
Component, has antiallergy, anti-inflammatory, sterilization and other effects, is widely used in daily chemical product.The preparation side of Rosa Damascana and hydrosol at present
Method mainly has three kinds：(1) steam distillation；(2) carbon dioxide supercritical extraction；(3) organic solvent extraction.
Conventional steam distillation, distillation time length, and vapo(u)rizing temperature is high, the fragrance loss of essential oil and hydrosol seriously affects
Product quality, and yield is low.Carbon dioxide supercritical extraction has ensured in terms of product yield and quality, but the extraction process
High, production cost height is required production equipment.Organic solvent extraction, because causing product dissolvent residual using organic solvent,
Influence product quality.
The content of the invention
The purpose of the utility model is to overcome in place of the deficiencies in the prior art, there is provided a kind of energy consumption is small, easy to use
Hydrosol extraction of essential oil system, the system can not only improve the extraction of essential oil during being extracted for fresh petal
Efficiency, while the hydrosol of high-purity, high-quality can also be extracted, it is particularly suitable for the fragrant plants such as new fresh-rose, lavender
Processing.
The purpose of this utility model is achieved through the following technical solutions：
A kind of fragrant plant hydrosol extraction of essential oil system, including level-one distilling apparatus, secondary distillation device, condenser and
Oil water separator, the level-one distilling apparatus is connected by charging gear with secondary distillation device, and level-one distilling apparatus
Respectively it is communicated with the condenser and oil water separator of one group of interconnection respectively with secondary distillation device.
Moreover, the level-one distilling apparatus includes autoclave body, feed inlet, into discharge outlet, filter plate, gas outlet, discharge port, heating
Overcoat and high-pressure nozzle, the autoclave body top are formed with feed inlet and gas outlet, and autoclave body is internally provided with annular filter plate, filter plate
Discharge port is provided centrally with, the high-pressure nozzle for material to be washed away to feed inlet and outlet is additionally provided with below filter plate；The autoclave body bottom
Portion is formed with into discharge outlet, autoclave body outer cover and heating jacket is housed.
Moreover, the filter plate inside the autoclave body is set diagonally downward for annular, filter plate minimum point is connected with discharge port, and
Butterfly valve control discharge port opening and closing is additionally provided with positioned at junction；The discharge port is connected by charging gear with secondary distillation device
It is logical；The gas outlet is connected by pipeline with condenser.
Moreover, the secondary distillation device includes two level autoclave body, two level feed inlet, two level water inlet, two level gas outlet, two
Level heating jacket, discharge gate and agitating device, are formed with two level feed inlet and two level gas outlet at the top of the two level autoclave body, and two
Agitating device is provided with level autoclave body；Two level autoclave body bottom is communicated with two level water inlet and discharge gate, two level autoclave body outer cover
Equipped with two level heating jacket.
Moreover, the agitating device includes top motor, bottom motors, rotates forward blade, reversion blade and shaft coupling, top
Portion's motor output end rotates forward blade by rotating forward rotation axis connection, and bottom motors connect reversion blade by reversion rotation axis, just,
Derotation shaft is connected by being arranged at the shaft coupling inside two level autoclave body, and shaft coupling is fixed on two level kettle by coupling support stand
Internal portion.
It is connected respectively with multiple level-one distilling apparatus moreover, may be provided with multiple two level feed inlets at the top of the two level autoclave body
It is logical.
Moreover, the condenser includes water tank, condensation cycle and passes through from SAPMAC method, the condensation cycle by water tank
Water be pumped into via water pump in condenser pipe and by pipeline flow back inlet water tank, it is described it is self cooling cycle through in water tank install additional spray
Device and cooling net are simultaneously connected with condensing circuit and reach self cooling result.
The advantages of the utility model and economic effect are：
1st, the utility model overcomes the not high technical barrier of hydrosol quality during traditional extensive extraction of essential oil, uses
Secondary distillation device, is extracted for high-quality hydrosol in fresh flower in level-one distillation and is delivered to two level by charging gear again
The extraction of essential oil is carried out in distilling apparatus, full section extraction process is recycled continuous operation, is remaining high-quality hydrosol extraction behaviour
As while ensure that the extraction efficiency of essential oil, avoid the forfeiture of fragrance and active ingredient in just section extraction in fresh flower.
2nd, the utility model in level-one distilling apparatus by setting high-pressure nozzle to may be such that the raw material completed level-one and distilled
Can be via nozzle automatically into secondary distillation device, both ensure that pressure, temperature will not be lost in secondary distillation device, at the same time
Charging, extraction efficiency are improved, ensure that the high-efficiency and continuous of the system in process of production.
Brief description of the drawings
Fig. 1 is the structure diagram of the utility model；
Fig. 2 is the structure diagram of the utility model level-one distilling apparatus；
Fig. 3 is the structure diagram of the utility model secondary distillation device；
Fig. 4 is the structure diagram of the utility model condenser.
Embodiment
For that can further appreciate that the contents, features and effects of the utility model, the following examples are hereby given, and coordinates attached drawing
Describe in detail as follows.It should be noted that the present embodiment is descriptive, it is not limited, it is impossible to thus limit this practicality
New protection domain.
A kind of fragrant plant hydrosol extraction of essential oil system, including level-one distilling apparatus 1, secondary distillation device 2, condenser 4
And oil water separator 5, the level-one distilling apparatus are connected by charging gear 15 with secondary distillation device, and level-one is steamed
Distillation unit is respectively communicated with one group of condenser and oil water separator being connected with each other by pipeline 3 respectively with secondary distillation device.
The level-one distilling apparatus include autoclave body 8, feed inlet 6, into discharge outlet 13, filter plate 10, gas outlet 7, discharge port 14,
Heating jacket 9 and high-pressure nozzle 11, the autoclave body top are formed with feed inlet and gas outlet, and autoclave body is internally provided with annular filter
Plate, filter plate are provided centrally with discharge port, the high-pressure nozzle for material to be washed away to feed inlet and outlet are additionally provided with below filter plate；It is described
Autoclave body bottom is formed with into discharge outlet, autoclave body outer cover and heating jacket is housed.Filter plate inside the autoclave body for annular diagonally downward
Set, filter plate minimum point is connected with discharge port 12, and is additionally provided with butterfly valve 14 positioned at junction and is controlled discharge port opening and closing；It is described
Discharge port is connected by charging gear with secondary distillation device；The gas outlet is connected by pipeline with condenser.
The secondary distillation device includes two level autoclave body 21, two level feed inlet 16, two level water inlet 29, two level gas outlet
19th, two level heating jacket 22, discharge gate 28 and agitating device, the two level autoclave body top are formed with two level feed inlet and two level
Gas outlet, is provided with agitating device in two level autoclave body；Two level autoclave body bottom is communicated with two level water inlet and discharge gate, two level kettle
Two level heating jacket is set with outside body.The agitating device includes top motor 17, bottom motors 24, rotates forward blade 20, is anti-
Turn blade 23 and shaft coupling 26, top motor output end rotates forward blade by rotating forward the connection of rotation axis 18, and bottom motors pass through
The connection reversion blade of reversion rotation axis 27, positive and negative rotation axis is connected by being arranged at the shaft coupling inside two level autoclave body, and shaft coupling
Device is fixed on inside two level autoclave body by coupling support stand 25.It may be provided with multiple two level feed inlets point at the top of the two level autoclave body
It is not connected with multiple level-one distilling apparatus.
The condenser includes water tank 34, condensation cycle 32 and passes through from SAPMAC method, the condensation cycle by water tank
Water be pumped into via water pump 33 in condenser pipe and by pipeline flow back inlet water tank, it is described it is self cooling cycle through in water tank install additional spray
Shower device 30 and cooling net 31 are simultaneously connected with condensing circuit and reach self cooling result.
When the utility model is used, the fresh petal in material pond is imported in the feed inlet of level-one distilling apparatus, then
Sealed feed inlet, while according to inlet amount to carrying out adding water operation into discharge outlet, in level-one distilling apparatus after water is added
Autoclave body heated, when heat is to 60 ° open gas outlet valve, carry out condensation collection.When the inlet amount according to fresh petal
After extracting a certain amount of high-purity hydrosol, you can stop heating, and open discharge port and high-pressure nozzle, pass through high pressure water flow
Material on filter plate is washed away into feed inlet and outlet, and by using screw feeder structure charging gear by have collected the thing of hydrosol
Material is sent to the feed inlet of secondary distillation device, and the discharging of level-one distilling apparatus is closed after material fully enters secondary distillation device
Mouth simultaneously opens the two level water inlet in secondary distillation device to carrying out immersion operation into material, and starts repetitive operation level-one
Distilling apparatus carries out charging distillation.The extraction efficiency for such as needing to accelerate essential oil can connect two level at the same time using multiple level-one distilling apparatus
Distilling apparatus, when in secondary distillation device material reach saturation state after begin to warm up secondary distillation device and open two level outlet
Mouth carries out extraction of essential oil operation.
The system level-one distilling apparatus during extraction aromatic essential oil and hydrosol is tentatively extracted, maximum limit
The fragrance and active ingredient of fresh petal are saved degree, can be transferred to secondary distillation device automatically after rapid extraction and be carried out deeply
Degree extraction, not only ensure that the quality of hydrosol but also had improved extraction of essential oil efficiency so that secondary distillation device is in insulation, pressurize environment
In continue high efficiency extraction, by using reverse agitating function device, can farthest reduce soaking time, improve extraction efficiency, it is whole
A system continuously can uninterruptedly carry out the extraction operation of hydrosol and essential oil, when being effectively saved fresh petal from picking to extracting
Stand-by period, improve extraction efficiency again while high-quality is ensured.
Claims (7)
1. a kind of fragrant plant hydrosol extraction of essential oil system, including level-one distilling apparatus, secondary distillation device, condenser and oil
Separator, the level-one distilling apparatus are connected by charging gear with secondary distillation device, and level-one distilling apparatus with
Secondary distillation device is respectively communicated with the condenser and oil water separator of one group of interconnection respectively.
A kind of 2. fragrant plant hydrosol extraction of essential oil system according to claim 1, it is characterised in that：The level-one distillation
Device includes autoclave body, feed inlet, into discharge outlet, filter plate, gas outlet, discharge port, heating jacket and high-pressure nozzle, the autoclave body
Top is formed with feed inlet and gas outlet, and autoclave body is internally provided with annular filter plate, and filter plate is provided centrally with discharge port, filter plate lower section
It is additionally provided with the high-pressure nozzle for material to be washed away to feed inlet and outlet；The autoclave body bottom is formed with into discharge outlet, autoclave body outer cover
Equipped with heating jacket.
A kind of 3. fragrant plant hydrosol extraction of essential oil system according to claim 2, it is characterised in that：Inside the autoclave body
Filter plate for annular set diagonally downward, filter plate minimum point is connected with discharge port, and is additionally provided with butterfly valve control positioned at junction
Make material mouth opening and closing；The discharge port is connected by charging gear with secondary distillation device；The gas outlet by pipeline with
Condenser is connected.
A kind of 4. fragrant plant hydrosol extraction of essential oil system according to claim 1, it is characterised in that：The secondary distillation
Device includes two level autoclave body, two level feed inlet, two level water inlet, two level gas outlet, two level heating jacket, discharge gate and stirring
Device, the two level autoclave body top are formed with two level feed inlet and two level gas outlet, agitating device are provided with two level autoclave body；Two
Level autoclave body bottom is communicated with two level water inlet and discharge gate, and two level autoclave body outer cover is equipped with two level heating jacket.
A kind of 5. fragrant plant hydrosol extraction of essential oil system according to claim 4, it is characterised in that：The agitating device
Including top motor, bottom motors, blade, reversion blade and shaft coupling are rotated forward, top motor output end is rotated by rotating forward
Axis connection rotates forward blade, and bottom motors connect reversion blade by reversion rotation axis, and positive and negative rotation axis is by being arranged at two level kettle
The shaft coupling connection in internal portion, and shaft coupling is fixed on inside two level autoclave body by coupling support stand.
A kind of 6. fragrant plant hydrosol extraction of essential oil system according to claim 4, it is characterised in that：The two level autoclave body
Top may be provided with multiple two level feed inlets and be connected respectively with multiple level-one distilling apparatus.
A kind of 7. fragrant plant hydrosol extraction of essential oil system according to claim 1, it is characterised in that：The condenser bag
Include water tank, condensation cycle and from SAPMAC method, the condensation cycle is by the way that the water in water tank is pumped into condenser pipe via water pump
And install spray equipment and cooling net additional in water tank by pipeline reflux inlet water tank, self cooling cycle through and followed with condensation
Loop back path, which is connected, reaches self cooling result.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721251538.5U CN207276584U (en) | 2017-09-27 | 2017-09-27 | A kind of fragrant plant hydrosol extraction of essential oil system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721251538.5U CN207276584U (en) | 2017-09-27 | 2017-09-27 | A kind of fragrant plant hydrosol extraction of essential oil system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207276584U true CN207276584U (en) | 2018-04-27 |
Family
ID=61988047
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721251538.5U Expired - Fee Related CN207276584U (en) | 2017-09-27 | 2017-09-27 | A kind of fragrant plant hydrosol extraction of essential oil system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207276584U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108467790A (en) * | 2018-05-17 | 2018-08-31 | 无锡市鹅湖玫瑰园艺文化有限公司 | A kind of equipment convenient for the extraction of Rosa Damascana hydrosol |
| CN108587792A (en) * | 2018-06-21 | 2018-09-28 | 何华英 | A kind of chemical experiment vapor water proof distillation essential oil extraction equipment |
-
2017
- 2017-09-27 CN CN201721251538.5U patent/CN207276584U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108467790A (en) * | 2018-05-17 | 2018-08-31 | 无锡市鹅湖玫瑰园艺文化有限公司 | A kind of equipment convenient for the extraction of Rosa Damascana hydrosol |
| CN108587792A (en) * | 2018-06-21 | 2018-09-28 | 何华英 | A kind of chemical experiment vapor water proof distillation essential oil extraction equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180427 Termination date: 20200927 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |