CN205740948U - A kind of plants essential oil extraction equipment - Google Patents
A kind of plants essential oil extraction equipment Download PDFInfo
- Publication number
- CN205740948U CN205740948U CN201620588839.6U CN201620588839U CN205740948U CN 205740948 U CN205740948 U CN 205740948U CN 201620588839 U CN201620588839 U CN 201620588839U CN 205740948 U CN205740948 U CN 205740948U
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- China
- Prior art keywords
- still
- heat exchange
- plants essential
- distillating still
- essential oil
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- 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.)
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Abstract
The utility model discloses a kind of plants essential oil extraction equipment, include the first distillating still, after-fractionating still, condensing unit, oil water separator and quintessence oil catcher, described first distillating still inner bottom part has electric heater unit, described electric heater unit is placed above support, material basket is placed on described support, squeezing extraction element is had in described material basket, described condensing unit includes the left hand inlet port being parallel-connected to heat exchange condensers no less than a heat exchange condensers, described first distillating still and after-fractionating still top by steam lead；Described heat exchange condensers outlet at bottom is connected to oil water separator by conduit, is connected to quintessence oil catcher by conduit bottom described oil water separator；Described heat exchange condensers top exit is parallel-connected to the first distillating still and after-fractionating still by hot water return conduit.This utility model reaches extractible plant material kind to be increased, and improves utilization rate of equipment and installations, reduces energy consumption, cost-effective effect.
Description
Technical field
This utility model relates to plants essential oil separation and extraction technology field, particularly relates to a kind of plants essential oil extraction equipment.
Background technology
Plants essential oil, is the volatile flavor refining extraction from the flower of plant, leaf, stem, root or fruit, quintessence oil by
The chemical molecular compositions such as terpenes, aldehydes, esters, alcohols.Quintessence oil can strengthen physiology and the function of psychology.Each plants essential oil
There is a chemical constitution to determine its fragrance, color, mobility and its mode with System Operation, also make each plantation
Thing quintessence oil is respectively arranged with a set of special function speciality.
Plants essential oil extracts mainly milling process, steam distillation, solvent extraction method, oils and fats partition method, carbon dioxide
Supercritical extraction etc..Wherein steam distillation is side the most frequently used from plant extract quintessence oil or volatile oil, most widely used
Method.The method has equipment simple, processing ease, the advantages such as treating capacity is big.But the traditional plant quintessence oil of application steam distillation
Extraction equipment has following shortcoming: 1, the distilling apparatus of equipment is generally only water and plant extract raw material Hybrid Heating, this
Sample does the most extractible plant material kind single (the typically just water heating volatile plant material of quintessence oil), and extracts
The solid-to-liquid ratio of quintessence oil is very big, and distillation time is long, and energy consumption is big, the condensed fluid serious emulsification that some quintessence oil distills out, and oil-water separation is stranded
Difficulty, for oil-water separation, need to stand 2～3 days condensed fluid, sometimes also need to after cold preservation with high speed centrifuge centrifugation or
Water layer after oil-water separation being carried out again multiple steaming, due to heating extraction for a long time, some heat-sensitive ingredients in quintessence oil can divide
Solve, the quality of quintessence oil is produced harmful effect；2, the condensing unit structure of equipment is single, causes whole equipment energy consumption big, to having
The utilization rate in usefulness source is not enough, inadequate environmental protection.
Utility model content
The purpose of this utility model is to overcome the above-mentioned problems in the prior art, it is provided that a kind of plants essential oil extracts
Equipment, double distillating still structure+heat exchange condensers structures, the most extractible plant material kind increases, and improves equipment profit
By rate, accelerate oil-water separation, it is to avoid the formation of emulsion, reduce energy consumption, cost-effective effect.
For realizing above-mentioned technical purpose, reaching above-mentioned technique effect, this utility model is achieved through the following technical solutions:
A kind of plants essential oil extraction equipment, includes the first distillating still, after-fractionating still, condensing unit, oil water separator
And quintessence oil catcher, described first distillating still inner bottom part has electric heater unit, described electric heater unit that support is placed above, institute
State placement material basket on support, in described material basket, have squeezing extraction element, the top of described first distillating still to be provided with charging aperture,
Bottom is provided with discharging opening, and the structure of described after-fractionating still is except being not provided with in material basket squeezing extraction element, other structures
Identical with the first distillating still；Described condensing unit includes no less than a heat exchange condensers, described first distillating still and second
Distillating still top is parallel-connected to the left hand inlet port of heat exchange condensers by steam lead, and two parallel connections of described steam lead are propped up
An electromagnetic valve it is respectively provided with on road；Described heat exchange condensers outlet at bottom is connected to oil water separator, described oil by conduit
It is connected to quintessence oil catcher by conduit bottom water separator, between described oil water separator and quintessence oil catcher, is provided with an electromagnetism
Valve；Described heat exchange condensers top exit is parallel-connected to the first distillating still and after-fractionating still by hot water return conduit,
It is respectively provided with an electromagnetic valve in two parallel branches of described hot water return conduit, described hot water return conduit is additionally provided with height
Press pump.
Further, described first distillating still is fitted with outlet(discharge) flange valve with the discharging opening of after-fractionating still, charging
Mouth is fitted with suction flange valve.Flange valve makes charging convenient and swift, after can also conveniently discharging distillation quintessence oil simultaneously
Waste material, convenient and swift also and then improve utilization rate of equipment and installations by handling material.
Further, described support is triangle travel(l)ing rest, is made up of metal material, and described is placed on electrical heating dress
Put upper end, but do not contact with electric heater unit.
Further, described electric heater unit is electric heating tube.
Further, described squeezing extraction element swing handle, screw rod, squeezing disk and squeezing bucket composition, on described squeezing bucket
It is densely covered with multiple oil outlet.Squeezing disk squeezing bucket in rotary press plant material, isolated plants essential oil be impure relatively
Many crude oil states, crude oil is discharged in material basket by oil outlet, further operates.
Further, described oil water separator includes ice bath device.Ice bath device is typical effectively oil-water separation dress
Put.
Further, the charging aperture of described first distillating still is connected with squeezing bucket.In the first distillating still, plant material enters
Enter in squeezing bucket rather than as after-fractionating still enters directly into material basket.
Further, described first distillating still and after-fractionating still size, volume are identical, and top flushes；Described
The left hand inlet port of heat exchange condensers is higher than the first distillating still top.
Further, described heat exchange condensers also includes a cold water inlet.
The beneficial effects of the utility model are:
1, of the present utility model pair of distillating still structure, the first distillating still therein includes the squeezing to plant material and extracts
Device, not only increases extractible plant material kind, and accelerates distillation speed, reduces distillation duration, and then reduces energy consumption；
2, heat exchange condensers structure of the present utility model, not only improves the precipitation efficiency of oil water mixture, and make use of
During condensation release heat, cool water heating is become hot water, by hot water return conduit feed back to distillating still again with, reduce
Extraction of essential oil water consumption, reduces energy consumption, has saved cost.
Accompanying drawing explanation
Fig. 1 is the structural representation of this utility model extraction equipment；
Fig. 2 is the structural representation of heat exchange condensers in embodiment one；
Fig. 3 is the structural representation of squeezing extraction element；
Wherein, the 1, first distillating still；2, after-fractionating still；3, support；4, electric heater unit；5, material basket；6, squeezing carries
Fetching is put；7, steam lead；8, electromagnetic valve；9, condensing unit；10, hot water return conduit；11, discharging opening；12, outlet(discharge) flange
Valve；13, charging aperture；14, suction flange valve；15, oil water separator；16, quintessence oil catcher；61, swing handle；62, screw rod；
63, squeezing disk；64, squeezing bucket；65, oil outlet；91, heat exchange condensers；101, high-pressure pump.
Detailed description of the invention
Below with reference to the accompanying drawings and in conjunction with the embodiments, this utility model is described in detail.
Embodiment one:
A kind of plants essential oil extraction equipment described in the present embodiment, as shown in Figure 1, Figure 2, Figure 3 shows, includes the first distillating still
1, after-fractionating still 2, condensing unit 9, oil water separator 15 and quintessence oil catcher 16, described first distillating still 1 inner bottom part has
Electric heater unit 4, described electric heater unit 4 is placed above support 3, described support 3 is placed material basket 5, in described material basket 5
Having squeezing extraction element 6, the top of described first distillating still 1 is provided with charging aperture 13, and bottom is provided with discharging opening 11, and described second steams
Evaporating the structure of still 2 except being not provided with in material basket 5 squeezing extraction element 6, other structures are identical with the first distillating still 1；Described
Condensing unit 9 includes two heat exchange condensers 91, is connected in series, and described first distillating still 1 and after-fractionating still 2 top are passed through
Steam lead 7 is parallel-connected to the left hand inlet port of heat exchange condensers 91, and two parallel branches of described steam lead 7 are respectively provided with
One electromagnetic valve 8；Described heat exchange condensers 91 outlet at bottom is connected to oil water separator 15, described oil-water separation by conduit
It is connected to quintessence oil catcher 16 by conduit bottom device 15, between described oil water separator 15 and quintessence oil catcher 16, is provided with an electricity
Magnet valve door 8；Described heat exchange condensers 91 top exit is parallel-connected to the first distillating still 1 and second by hot water return conduit 10
Distillating still 2, two parallel branches of described hot water return conduit 10 are respectively provided with an electromagnetic valve 8, and described hot water return is led
High-pressure pump 101 it is additionally provided with on pipe 10.In the present embodiment, equipment also has an electrical control panel, is used for controlling electromagnetic valve
8, high-pressure pump 101, electric heater unit 4 and the squeezing electric device such as extraction element 6.
Further, described first distillating still 1 is fitted with outlet(discharge) flange valve with the discharging opening 11 of after-fractionating still 2
12, charging aperture 13 is fitted with suction flange valve 14.Flange valve makes charging convenient and swift, can also conveniently discharge steaming simultaneously
Evaporate the waste material after quintessence oil, convenient and swift also and then improve utilization rate of equipment and installations by handling material.
Further, described support 3 is triangle travel(l)ing rest, is made up of metal material, and described support 3 is placed in electrical heating
Device 4 upper end, but do not contact with electric heater unit 4.
Further, described electric heater unit 4 is electric heating tube.
Further, described squeezing extraction element 6 swing handle 61, screw rod 62, squeezing disk 63 and squeezing bucket 64 form, described
It is densely covered with multiple oil outlet 65 on squeezing bucket 64.Electronic control swing handle 61 and screw rod 62 drive squeezing disk 63 in squeezing bucket 64 inward turning
Turning squeezing plant material, isolated plants essential oil is impure more crude oil state, and crude oil is discharged to by oil outlet 65
In material basket 5, further operate.
Further, described oil water separator 15 includes ice bath device.Ice bath device is typical effectively oil-water separation
Device.
Further, the charging aperture 13 of described first distillating still 1 is connected with squeezing bucket 64.In the first distillating still 1, plant
In raw material enters into squeezing bucket 64 rather than as after-fractionating still 2 enters directly into material basket 5.
Further, described first distillating still 1 and after-fractionating still 2 size, volume are identical, and top flushes；Institute
State the left hand inlet port of heat exchange condensers 91 higher than the first distillating still 1 top.
Further, described heat exchange condensers 91 also includes a cold water inlet.In the present embodiment, as in figure 2 it is shown,
Heat exchange condensers 91 internal structure includes steam pipework, cold water pipeline and the heat exchange chip being disposed there between, steam
Pipeline comprises vapor inlet port and oil water mixture delivery outlet, and vapor inlet port connects steam lead 7, oil water mixture delivery outlet
Oil water separator 15 is connected by conduit；Cold water pipeline includes cold water inlet and hot water outlet, and hot water outlet connects hot water and returns
Conduit 10.
The operation principle of the present embodiment is:
Of the present utility model pair of distillating still structure, the first distillating still 1 therein includes the squeezing to plant material and extracts
Device 6, not only increases extractible plant material kind, and accelerates distillation speed, reduces distillation duration, and then reduces energy
Consumption；
Heat exchange condensers structure of the present utility model, not only improves the precipitation efficiency of oil water mixture, and make use of cold
Time solidifying, the heat of release, becomes hot water by cool water heating, by hot water return conduit 10 feed back to distillating still again with, reduce
Extraction of essential oil water consumption, reduces energy consumption, has saved cost.
The foregoing is only preferred embodiment of the present utility model, not in order to limit this utility model, all at this
Within the spirit of utility model and principle, any modification, equivalent substitution and improvement etc. made, should be included in this utility model
Protection domain within.
Claims (9)
1. a plants essential oil extraction equipment, it is characterised in that: include the first distillating still (1), after-fractionating still (2), condensation
Device (9), oil water separator (15) and quintessence oil catcher (16), described first distillating still (1) inner bottom part has electric heater unit
(4), described electric heater unit (4) is placed above support (3), and described support (3) is placed material basket (5), described material basket (5)
Inside having squeezing extraction element (6), the top of described first distillating still (1) to be provided with charging aperture (13), bottom is provided with discharging opening (11),
The structure of described after-fractionating still (2) is except being not provided with in material basket (5) squeezing extraction element (6), other structures and first
Distillating still (1) is identical；Described condensing unit (9) includes no less than a heat exchange condensers (91), described first distillating still (1)
Pass through steam lead (7) with after-fractionating still (2) top and be parallel-connected to the left hand inlet port of heat exchange condensers (91), described steam
An electromagnetic valve (8) it is respectively provided with in two parallel branches of conduit (7)；Described heat exchange condensers (91) outlet at bottom is by leading
Pipe is connected to oil water separator (15), and described oil water separator (15) bottom is connected to quintessence oil catcher (16), institute by conduit
State and between oil water separator (15) and quintessence oil catcher (16), be provided with an electromagnetic valve (8)；Described heat exchange condensers (91) top
Exporting and be parallel-connected to the first distillating still (1) and after-fractionating still (2) by hot water return conduit (10), described hot water return is led
It is respectively provided with an electromagnetic valve (8) in two parallel branches of pipe (10), described hot water return conduit (10) is additionally provided with high pressure
Pump (101).
A kind of plants essential oil extraction equipment the most according to claim 1, it is characterised in that: described first distillating still (1) with
The discharging opening (11) of after-fractionating still (2) is fitted with outlet(discharge) flange valve (12), and charging aperture (13) is fitted with suction flange
Valve (14).
A kind of plants essential oil extraction equipment the most according to claim 1, it is characterised in that: described support (3) is triangle
Travel(l)ing rest, is made up of metal material, and described support (3) is placed in electric heater unit (4) upper end, but not with electric heater unit (4)
Contact.
4. according to a kind of plants essential oil extraction equipment described in claim 1 or 3, it is characterised in that: described electric heater unit (4)
For electric heating tube.
A kind of plants essential oil extraction equipment the most according to claim 1, it is characterised in that: described squeezing extraction element (6)
Swing handle (61), screw rod (62), squeezing disk (63) and squeezing bucket (64) composition, described squeezing bucket (64) is densely covered with multiple fuel-displaced
Hole (65).
A kind of plants essential oil extraction equipment the most according to claim 1, it is characterised in that: described oil water separator (15) wraps
Containing ice bath device.
A kind of plants essential oil extraction equipment, it is characterised in that: described first distillating still (1)
Charging aperture (13) with squeezing bucket (64) be connected.
A kind of plants essential oil extraction equipment the most according to claim 1, it is characterised in that: described first distillating still (1) with
After-fractionating still (2) size, volume are identical, and top flushes；The left hand inlet port of described heat exchange condensers (91) is higher than the
One distillating still (1) top.
A kind of plants essential oil extraction equipment the most according to claim 1, it is characterised in that: described heat exchange condensers (91) is also
Include a cold water inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620588839.6U CN205740948U (en) | 2016-06-12 | 2016-06-12 | A kind of plants essential oil extraction equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620588839.6U CN205740948U (en) | 2016-06-12 | 2016-06-12 | A kind of plants essential oil extraction equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205740948U true CN205740948U (en) | 2016-11-30 |
Family
ID=57385926
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620588839.6U Expired - Fee Related CN205740948U (en) | 2016-06-12 | 2016-06-12 | A kind of plants essential oil extraction equipment |
Country Status (1)
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| CN (1) | CN205740948U (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106590933A (en) * | 2016-12-19 | 2017-04-26 | 蕲春艾都生物科技有限公司 | Chinese mugwort essential oil refining device and Chinese mugwort essential oil refining method |
| CN107881010A (en) * | 2017-11-25 | 2018-04-06 | 防城港市润禾农林科技有限公司 | A kind of pressing device refined for balsamic essential oil |
| CN108102786A (en) * | 2018-01-10 | 2018-06-01 | 刘芬 | A kind of essential oil method of purification and equipment |
| CN108192736A (en) * | 2018-02-25 | 2018-06-22 | 广西向东沉香科技有限公司 | The equipment and its process of normal temperature and pressure distillation extraction agilawood essential oil |
| CN108467792A (en) * | 2018-05-17 | 2018-08-31 | 无锡市鹅湖玫瑰园艺文化有限公司 | Rosa Damascana extraction element |
| CN110396455A (en) * | 2019-06-27 | 2019-11-01 | 漳州职业技术学院 | A kind of essential oil extraction device |
| CN112094699A (en) * | 2020-09-27 | 2020-12-18 | 广西壮族自治区林业科学研究院 | Method for extracting camphor tree hydrosol |
| CN112322387A (en) * | 2020-09-27 | 2021-02-05 | 广西壮族自治区林业科学研究院 | Extraction system of camphor tree hydrosol and application thereof |
| CN112795433A (en) * | 2021-03-19 | 2021-05-14 | 江西天佳生物工程股份有限公司 | Plant essential oil and separation and purification method thereof |
| CN112973160A (en) * | 2019-12-12 | 2021-06-18 | 江苏民生特种设备集团有限公司 | Self-cleaning distillation tower |
| CN115466649A (en) * | 2022-09-26 | 2022-12-13 | 阜阳天祥食品科技有限公司 | Plant aromatic oil extraction device and extraction method |
-
2016
- 2016-06-12 CN CN201620588839.6U patent/CN205740948U/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106590933A (en) * | 2016-12-19 | 2017-04-26 | 蕲春艾都生物科技有限公司 | Chinese mugwort essential oil refining device and Chinese mugwort essential oil refining method |
| CN107881010A (en) * | 2017-11-25 | 2018-04-06 | 防城港市润禾农林科技有限公司 | A kind of pressing device refined for balsamic essential oil |
| CN108102786A (en) * | 2018-01-10 | 2018-06-01 | 刘芬 | A kind of essential oil method of purification and equipment |
| CN108192736A (en) * | 2018-02-25 | 2018-06-22 | 广西向东沉香科技有限公司 | The equipment and its process of normal temperature and pressure distillation extraction agilawood essential oil |
| CN108467792A (en) * | 2018-05-17 | 2018-08-31 | 无锡市鹅湖玫瑰园艺文化有限公司 | Rosa Damascana extraction element |
| CN110396455A (en) * | 2019-06-27 | 2019-11-01 | 漳州职业技术学院 | A kind of essential oil extraction device |
| CN112973160A (en) * | 2019-12-12 | 2021-06-18 | 江苏民生特种设备集团有限公司 | Self-cleaning distillation tower |
| CN112322387A (en) * | 2020-09-27 | 2021-02-05 | 广西壮族自治区林业科学研究院 | Extraction system of camphor tree hydrosol and application thereof |
| CN112094699A (en) * | 2020-09-27 | 2020-12-18 | 广西壮族自治区林业科学研究院 | Method for extracting camphor tree hydrosol |
| CN112094699B (en) * | 2020-09-27 | 2023-03-28 | 广西壮族自治区林业科学研究院 | Method for extracting camphor tree hydrosol |
| CN112795433A (en) * | 2021-03-19 | 2021-05-14 | 江西天佳生物工程股份有限公司 | Plant essential oil and separation and purification method thereof |
| CN115466649A (en) * | 2022-09-26 | 2022-12-13 | 阜阳天祥食品科技有限公司 | Plant aromatic oil extraction device and extraction method |
| CN115466649B (en) * | 2022-09-26 | 2023-12-19 | 阜阳天祥食品科技有限公司 | Plant aromatic oil extraction device and extraction method |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161130 Termination date: 20170612 |
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| CF01 | Termination of patent right due to non-payment of annual fee |