CN206706053U - One kind distills uniform fir essential oil production alembic - Google Patents
One kind distills uniform fir essential oil production alembic Download PDFInfo
- Publication number
- CN206706053U CN206706053U CN201720424580.6U CN201720424580U CN206706053U CN 206706053 U CN206706053 U CN 206706053U CN 201720424580 U CN201720424580 U CN 201720424580U CN 206706053 U CN206706053 U CN 206706053U
- Authority
- CN
- China
- Prior art keywords
- tank body
- cavity volume
- big
- permeability cell
- slag notch
- 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.)
- Expired - Fee Related
Links
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
The utility model discloses one kind to distill uniform fir essential oil production alembic, including tank body；Breathable membrane is provided with by bottom in tank body, and tank inner chamber is set to two up big and down small cavity volumes every setting up separately, tank body top surface is provided with charging aperture, the top of big cavity volume is provided with gaseous mixture outlet pipe, steam inlet pipe is inserted with small cavity volume, tank body side is provided with slag notch, the top of slag notch connects with big cavity volume, and the bottom of slag notch connects with small cavity volume, and slag notch is provided with slag door；It is big that the more permeability cells for passing through breathable membrane are provided with and communicated between cavity volume and small cavity volume；The top end face of permeability cell be sealing, bottom face be open；The pipe outer wall face of each permeability cell recline tank body internal face corresponding position set；Gathered on the tube wall of permeability cell and be provided with air-vent.Structure is more reasonable, and evenly, distillation efficiency is higher, and distillation time can substantially shorten, and using effect is more preferable for distillation.
Description
Technical field
The utility model belongs to the extractive technique field of fir essential oil, is related to a kind of uniform fir essential oil production of distillation and uses
Alembic.
Background technology
Contain substantial amounts of fir essential oil in China fir, its main component is cedrene, cedar wood alcohol etc., available for perfume industry
In.At present, the extraction processing of fir essential oil is mainly using solvent extraction method, cracking process, steam distillation.Using solvent extraction
The oil yield of method extraction fir essential oil is high compared with the oil yield of steam distillation, but needs substantial amounts of solvent, and subsequent treatment is complicated,
The problem of high energy consumption, dissolvent residual be present.Oil yield using cracking process extraction fir essential oil is higher, but it is a chemical mistake
Journey, obtained essential oil contain the materials such as substantial amounts of tar, phenol, aldehyde and ketone, have a strong impact on the quality of fir essential oil.Steam distillation
The fir essential oil quality of method extraction is best, clear, aroma of pure, is best suitable for being used for blending, and its extraction process is pure thing
Reason process, it is pollution-free, but oil yield is relatively low.Several techniques compare, and steam distillation is the production work of preferable environment-friendly type
Skill, but should also optimize to improve yield and further reduce energy consumption.Steam distillation extracts the step of fir essential oil
It is：A, China fir is ground into fir powder；B, dispensing is added into fir powder and is stirred mixing；C, the fir powder mixed is sent
Enter in destilling tower, superheated steam is passed through into destilling tower and is distilled, distillation time is 9-11 hours；That is discharged after D, distilling is mixed
Close gas be delivered to cooled down in cooling tower after obtain oil mixing with water liquid；E, oil mixing with water liquid obtains after water-oil separating
Fir essential oil.
Alembic is the equipment of core in steam distillation, and it is small need to be generally up to 9-11 for distillation time in whole technique
When, therefore the efficiency of alembic is related to the efficiency of whole fir essential oil production.The efficiency of alembic is set to improve it is necessary to protect
On the premise of the utilization rate for demonstrate,proving the volume of alembic, accumulate the border of material entirety and the direct contact surface of water vapour in alembic
Can be as far as possible big, it is as far as possible uniform, while also to ensure that scarfing cinder will facilitate after the completion of distilling.
The structure of fir essential oil production alembic of the prior art as shown in Figure 1 and Figure 2, including tank body 2；In tank body 2
Breathable membrane 6 being provided with by bottom the inner chamber of tank body 2 being set to two up big and down small cavity volumes every setting up separately, the top surface of tank body 2 is provided with charging
Mouth 1, the top of big cavity volume is provided with gaseous mixture outlet pipe 7, and steam inlet pipe 4 is inserted with small cavity volume, and the side of tank body 2 is provided with slag notch 3,
The top of slag notch 3 connects with big cavity volume, and the bottom of slag notch 3 connects with small cavity volume, and slag notch 3 is provided with slag door 5.
Using the alembic of such technology it is of course possible to use, but due to the overall border of material in alembic and water vapour
The size of direct contact surface product be equivalent to the area of breathable membrane 6, direct contact surface product is big not enough, and direct contact point is complete
Portion is located at the overall bottom surface of material, and distribution is not uniform enough, and distillation is not uniform enough, and distillation efficiency is not high enough, and distillation time is relatively
Long, using effect is preferable not enough.
Utility model content
For overcome the deficiencies in the prior art, a kind of structure of the utility model offer is more reasonable, and evenly, distillation is imitated for distillation
Can be higher, the fir essential oil production alembic that distillation time can substantially shorten, using effect is more preferable.
The utility model is that technical scheme is used by reaching above-mentioned technical purpose：One kind distills uniform fir essential oil
Production alembic, including tank body；In tank body by bottom be provided with breathable membrane by tank inner chamber every set up separately be set to it is up big and down small
Two cavity volumes, tank body top surface are provided with charging aperture, and the top of big cavity volume is provided with gaseous mixture outlet pipe, steam inlet pipe is inserted with small cavity volume,
Tank body side is provided with slag notch, and the top of slag notch connects with big cavity volume, and the bottom of slag notch connects with small cavity volume, slag notch
It is provided with slag door；It is big that the more permeability cells for passing through breathable membrane are provided with and communicated between cavity volume and small cavity volume；The top of permeability cell
Face be sealing, bottom face be open；The pipe outer wall face of each permeability cell recline tank body internal face corresponding position set；Permeability cell
Tube wall on gather be provided with air-vent.
The top end face of described permeability cell stretches into the mouth of pipe most lower edge of tank interior point less than gaseous mixture outlet pipe.
Described permeability cell is to be uniformly arranged using the axis of tank body as rotation axes of symmetry along the inner circumferential of tank body.
The utility model has the advantage of：
Due to being provided with and communicated with the more permeability cells for passing through breathable membrane between big cavity volume and small cavity volume；The top of permeability cell
Face be sealing, bottom face be open；The pipe outer wall face of each permeability cell recline tank body internal face corresponding position set；Permeability cell
Tube wall on gather be provided with air-vent.
Therefore, water vapour and the area of material directly contact are obviously just bigger than traditional circular cross-section, and directly contact
Point is more evenly distributed, therefore distills evenly, and distillation efficiency is higher, and distillation time can substantially shorten, and using effect is more preferable.
Brief description of the drawings
The utility model is described in further detail with reference to the accompanying drawings and examples.Wherein：
Fig. 1 is the schematic diagram of the alembic of prior art；
Fig. 2 is the local subdivision schematic diagram of the alembic of prior art；
Fig. 3 is local subdivision schematic diagram of the present utility model.
Marker number in accompanying drawing is described as follows：Charging aperture 1, tank body 2, slag notch 3, steam inlet pipe 4, slag door 5, breathable membrane
6th, gaseous mixture outlet pipe 7, permeability cell 8
Embodiment
Embodiment of the present utility model, as shown in figure 3, a kind of uniform fir essential oil production alembic of distillation, including
Tank body 2；Breathable membrane 6 is provided with by bottom in tank body 2, and the inner chamber of tank body 2 is set to two up big and down small cavity volumes, tank body 2 every setting up separately
Top surface is provided with charging aperture 1, and the top of big cavity volume is provided with gaseous mixture outlet pipe 7, is inserted with steam inlet pipe 4 in small cavity volume, on the side of tank body 2
Provided with slag notch 3, the top of slag notch 3 is connected with big cavity volume, and the bottom of slag notch 3 connects with small cavity volume, and slag notch 3 is provided with
Slag door 5；It is big that the more permeability cells 8 for passing through breathable membrane 6 are provided with and communicated between cavity volume and small cavity volume；The top end face of permeability cell 8
Be sealing, bottom face be open；The pipe outer wall face of each permeability cell 8 recline tank body 2 internal face corresponding position set；Permeability cell
Gathered on 8 tube wall and be provided with air-vent.
The top end face of described permeability cell 8 stretches into the mouth of pipe most lower edge of the inside points of tank body 2 less than gaseous mixture outlet pipe 7.
Described permeability cell 8 is uniformly arranged by inner circumferential of the rotation axes of symmetry along tank body 2 of the axis of tank body 2.Thoroughly
Tracheae 8 set very little improved effect it is not obvious enough, permeability cell 8 sets the too many dischargeable capacity that can then take too many alembic,
The quantity of permeability cell 8 is preferably 4-8 roots.
Claims (3)
1. one kind distills uniform fir essential oil production alembic, including tank body；Will provided with breathable membrane by bottom in tank body
Tank inner chamber is set to two up big and down small cavity volumes every setting up separately, and tank body top surface is provided with charging aperture, and the top of big cavity volume is provided with mixing
Gas outlet pipe, steam inlet pipe is inserted with small cavity volume, tank body side is provided with slag notch, and the top of slag notch connects with big cavity volume, gone out
The bottom of cinder notch connects with small cavity volume, and slag notch is provided with slag door；It is characterized in that：Setting is connected between cavity volume and small cavity volume greatly
There are the more permeability cells for passing through breathable membrane；The top end face of permeability cell be sealing, bottom face be open；The pipe of each permeability cell
Outside wall surface recline tank body internal face corresponding position set；Gathered on the tube wall of permeability cell and be provided with air-vent.
A kind of 2. uniform fir essential oil production alembic of distillation according to claim 1, it is characterised in that：Described
The top end face of permeability cell stretches into the mouth of pipe most lower edge of tank interior point less than gaseous mixture outlet pipe.
A kind of 3. uniform fir essential oil production alembic of distillation according to claim 2, it is characterised in that：Described
Permeability cell is to be uniformly arranged using the axis of tank body as rotation axes of symmetry along the inner circumferential of tank body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720424580.6U CN206706053U (en) | 2017-04-21 | 2017-04-21 | One kind distills uniform fir essential oil production alembic |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720424580.6U CN206706053U (en) | 2017-04-21 | 2017-04-21 | One kind distills uniform fir essential oil production alembic |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206706053U true CN206706053U (en) | 2017-12-05 |
Family
ID=60455630
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720424580.6U Expired - Fee Related CN206706053U (en) | 2017-04-21 | 2017-04-21 | One kind distills uniform fir essential oil production alembic |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206706053U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106929157A (en) * | 2017-04-21 | 2017-07-07 | 福建鑫绿林产品开发有限公司 | The uniform fir essential oil production alembic of one kind distillation |
-
2017
- 2017-04-21 CN CN201720424580.6U patent/CN206706053U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106929157A (en) * | 2017-04-21 | 2017-07-07 | 福建鑫绿林产品开发有限公司 | The uniform fir essential oil production alembic of one kind distillation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104761538B (en) | The method of wet distillation and sour absorption extraction nicotine | |
| CN103194252B (en) | Complete set of equipment and method for separating high-temperature coal tar components via low-temperature rapid extraction method | |
| CN102517340B (en) | Process method for separating and drying lees produced in production process of ethanol with potatoes | |
| CN206706053U (en) | One kind distills uniform fir essential oil production alembic | |
| CN206700819U (en) | A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap | |
| CN204910874U (en) | Tar ammonia water separator | |
| CN206934773U (en) | A kind of Miniature Chinese medicine material crushes enrichment facility | |
| CN206298529U (en) | A kind of system of separation water and propylene glycol monomethyl ether | |
| CN206872779U (en) | A kind of new and effective Brewing equipment using plant fermentation | |
| CN206706054U (en) | A kind of fir essential oil production alembic of optimization design | |
| CN106929157A (en) | The uniform fir essential oil production alembic of one kind distillation | |
| CN206746022U (en) | A kind of efficient distiller of fir essential oil production | |
| CN204550477U (en) | A kind of device using waste plastic catalysis oiling to produce oil fuel | |
| CN206706055U (en) | One kind, which is stirred, turns over formula fir essential oil production alembic | |
| CN205933728U (en) | Improved generation rosin filter | |
| CN206700818U (en) | A kind of dynamical fir essential oil production distilling apparatus | |
| CN106880956A (en) | A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap | |
| CN206706056U (en) | One kind, which is stirred, turns over efficient fir essential oil preparation distilling apparatus | |
| CN203436854U (en) | Ultrasonic-assisted supercritical fluid extraction device for gutta percha | |
| CN206577144U (en) | The decoloration device of extract oral liquid formulation | |
| CN205287700U (en) | Multi -functional traditional chinese medicine volatile oil and extract draw jar | |
| CN207727062U (en) | A kind of installation for fermenting for pure plant extraction formaldehyde scavenger | |
| CN206746047U (en) | A kind of fir essential oil production oily-water seperating equipment of optimization design | |
| CN106867677A (en) | A kind of fir essential oil production alembic of optimization design | |
| CN205965071U (en) | But distillation plant of serialization distillation, row's residue |
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: 20171205 Termination date: 20210421 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |