A kind of essential oil extraction device
Technical field
It the utility model is related to plants essential oil extraction field, more particularly to a kind of essential oil extraction device.
Background technology
Plants essential oil is present in the different parts of different plants, and molecule forms sufficiently complex, it is necessary to takes suitable extraction
Method, just it is unlikely to destroy the vitality of its most original, so as to obtain most abundant, most complete essential oil, also only in this way, just may be used
Essential oil efficacy exertion in energy let us hand obtains incisively and vividly.The conventional way of distillation be by plant as distillation container, using water or
Steam heats plant, vapor transmission plant, and the smart matter oil heat resided in plant turns to gas effusion, then cold through conduit
But liquid condition is reverted back to produce.The distillation container of existing apparatus is relatively simple, cumbersome when changing distillation plant, typically
Needing to interrupt and disassembling distilling apparatus just can be removed residue and more renew the purpose of distillation, and continuous production is low;It is existing
Distilling apparatus needs constantly have new water to supply, and heat energy loss is larger, the Shortcomings in terms of energy sustainability.
Utility model content
It the utility model is related to plants essential oil extraction field, more particularly to a kind of simple operation, continuous production height, energy-conservation
Environmentally friendly and safe essential oil extracting device.
The utility model is realized using following scheme:
A kind of essential oil extraction device, it is characterised in that:Including distiller, observation panel, intake-outlet, water-oil separating
Device, oil catcher coolant jacket, steam pipe;
The distiller also includes backstop layer, feed drawer, raw material door;
The backstop layer is arranged in distiller casing, and the backstop layer is parallel to distiller bottom surface;
The feed drawer is square box-like structure, and four side walls of the feed drawer are externally provided with rubber sealant, institute
Feed drawer is stated to be positioned on backstop layer;
The raw material door, which is arranged in distiller side wall, to be used to pick and place feed drawer, the raw material door lower end with backstop layer
In in same level;
The oil water separator also includes flowline and outlet pipe, the flowline both ends connect respectively oil water separator and
Oil catcher, the outlet pipe both ends connect oil water separator and distiller respectively;
The coolant jacket bag is outside steam pipe, the cooled set cladding of a part of the outlet pipe;
The distiller top connects steam pipe.
Preferably, the essential oil extraction device also includes three-way pipe and condenser, and the end of three-way pipe three connects respectively
Connect steam pipe, oil water separator and condenser.
Preferably, the distiller side wall is provided with observation panel, and the observation panel is in same level with backstop layer.
Preferably, structure is led to during the condenser is.
Preferably, the feed drawer sectional dimension is less than raw material doorway footpath, and the feed drawer upper and lower surface is all net
Shape structure.
Preferably, the connecting portion of the outlet pipe and distiller and observation panel are in same level height.
Preferably, the distiller bottom is additionally provided with zone of heating, and the distiller bottom is additionally provided with intake-outlet.
The beneficial effects of the utility model:
By the design of feed drawer, only need directly to change the feed drawer equipped with raw material when changing raw material so that change
Raw material becomes convenient, improves and the complicated process of raw material is changed in Conventional process;
By condenser and coolant jacket and outlet pipe and it is used cooperatively so that the water isolated after water-oil separating is through supercooling
Heat exchange has been carried out with the steam in distiller out cooling effect is served to steam in steam pipe after set, the water separated
Recycled after coolant jacket absorbs steam heat heating in interior entrance distiller, eliminate needs and often add water to distiller
Process, the energy needed for substantial amounts of water resource and heating can be saved, simultaneously because portion will can also be carried in the water after water-oil separating
Divide essential oil, the water circulation separated after separation can be increased to the extracted amount of essential oil to a certain extent;
Condenser uses the pressure for causing whole production process to keep an atmospheric pressure, will not produce high pressure because of sealing,
So as to improve production security.
Brief description of the drawings
Fig. 1 is essential oil extraction device structure chart.
In figure mark for:1 distiller, 11 backstop layers, 12 rubber sealants, 13 feed drawers, 14 raw material doors, 15 heating
Layer, 3 observation panels, 4 intake-outlets, 5 oil water separators, 51 outlet pipes, 52 flowlines, 6 oil catchers, 7 coolant jackets, 8 condensers, 9
Steam pipe, 91 three-way pipes.
Embodiment
The utility model is further described below in conjunction with the accompanying drawings.
A kind of essential oil extraction device, including distiller 1, intake-outlet 4, oil water separator 5, oil catcher 6, coolant jacket
7th, steam pipe 9;
Distiller 1 also includes backstop layer 11, feed drawer 13, raw material door 14;
Backstop layer 11 is arranged in the casing of distiller 1, and backstop layer 11 is parallel to the bottom surface of distiller 1;
Feed drawer 13 is square box-like structure, and four side walls of the feed drawer 13 are externally provided with rubber sealant 12,
The feed drawer 13 is positioned on backstop layer 11;
Raw material door 14, which is arranged in the side wall of distiller 1, to be used to pick and place feed drawer 13, the lower end of raw material door 14 and backstop
Layer 11 is in same level;
Oil water separator 5 also includes flowline 52 and outlet pipe 51, and the both ends of flowline 52 connect water-oil separating respectively
Device 5 and oil catcher 6, the both ends of outlet pipe 51 connect oil water separator 5 and distiller 1 respectively;
Coolant jacket 7 is wrapped outside steam pipe 9, the cooled cladding of set 7 of a part of outlet pipe 51;
The top of distiller 1 connects steam pipe 9.
Essential oil extraction device also includes three-way pipe 91 and condenser 8, and the end of three-way pipe 91 3 connects steam respectively
Pipe 9, oil water separator 5 and condenser 8.
The side wall of distiller 1 is provided with observation panel 3, and observation panel 3 is in same level with backstop layer 11.
Condenser 8 leads to structure in being.
The sectional dimension of feed drawer 13 is less than the bore of raw material door 14, and the upper and lower surface of feed drawer 13 is all netted knot
Structure.
The connecting portion and observation panel 3 of outlet pipe 51 and distiller 1 are in same level height.
The bottom of distiller 1 is provided with zone of heating 15, and the bottom of distiller 1 is additionally provided with intake-outlet 4.
A kind of embodiment is as follows:
Raw material door 14 is opened, feed drawer 13 is taken out, raw material is uniformly piled to whole feed drawer 13, by feed drawer 13
It is pushed into the drawer case that backstop layer 11 and the inwall of distiller 1 are formed, raw material door 14 is shut into locking.Because the wall of feed drawer 13 4 is set
Rubber sealant 12 has been put so that four walls have sealing.
Begin to use before distiller by intake-outlet 4 plus water, water level is observed by observation panel 3 be slightly below drawer lower box part and keep off
Stratum reticulare 11.
After distiller 1 works, zone of heating 15 is constantly to water supply heat in distiller 1;Vapor is formed, vapor passes through
Feed drawer 13 constantly takes plants essential oil out of and forms stoste, and stoste passes through the steam pipe 9 with condenser jacket 7, and oil is entered after liquefaction
Separator 5;Condenser 8 plays a part of logical air and steam condensing reflux.
Stoste is separated into essential oil and water after oil water separator 5, and essential oil is directly entered oil catcher 6;Water after separation enters
Enter after outlet pipe 51 carries out heat exchange heating in the biography stratosphere of coolant jacket 7 with steam in steam pipe 9 and enter in distiller 1, improve
The initial temperature of recirculated water also achieves the auto recycling of water;And due to there is provided the pressure release of condenser 8, solving distiller
Stress problems in 1, the water in outlet pipe 51 will not be caused to flow back, also improve production security.
When a collection of raw material can not be fuel-displaced again, it is only necessary to which the feed drawer 13 equipped with raw material ready in advance is directly replaced into steaming
The feed drawer 13 in device is evaporated, without carrying out other steps, this process is very convenient quick.
It should be noted that:Outlet pipe 51 in coolant jacket 7 be one kind of the heat-exchange device of coolant jacket 7 and not with it is cold
But heat exchange occurs for other heat-exchange devices in set 7, and all heat-exchange devices are provided to displace steam pipe 9 in coolant jacket 7
The heat of interior steam.All pipeline preferred schemes should be equipped with valve.
The utility model embodiment is the foregoing is only, not thereby limits the scope of the claims of utility model, every utilization
The equivalent structure or equivalent flow conversion that the utility model description is done, or directly or indirectly it is used in other related skills
Art field, similarly it is included in scope of patent protection of the present utility model.