CN206746022U - A kind of efficient distiller of fir essential oil production - Google Patents
A kind of efficient distiller of fir essential oil production Download PDFInfo
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- CN206746022U CN206746022U CN201720486207.3U CN201720486207U CN206746022U CN 206746022 U CN206746022 U CN 206746022U CN 201720486207 U CN201720486207 U CN 201720486207U CN 206746022 U CN206746022 U CN 206746022U
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- tank body
- permeability cell
- cavity volume
- top surface
- permeability
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Abstract
The utility model discloses a kind of fir essential oil production efficient distiller, including tank body；Breathable membrane is provided with by bottom in tank body, and tank inner chamber is set to up big and down small big cavity volume and small cavity volume 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 and slag door；Standing to detachable in tank body is inserted with multiple permeability cells；Gathered on permeability cell side face and offer air-vent；The top surface of permeability cell is sealing, and the position height of its top surface is less than the position height of gaseous mixture outlet pipe, hanger is provided with the top surface of permeability cell；The bottom surface of permeability cell offers ttom of pipe mouth；Bottom surface in tank body is provided with the base of the pluggable corresponding permeability cell equal with permeability cell quantity；The bulkhead apertures equal with permeability cell quantity are offered on breathable membrane.On the premise of the convenience and space availability ratio of feeding slag-tapping is ensured, distillation efficiency improves, distillation time significantly shortens.
Description
Technical field
The utility model belongs to the extractive technique field of fir essential oil, is related to a kind of fir essential oil production efficiently distillation
Device.
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：
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 into
In destilling tower, into destilling tower being passed through superheated steam is distilled, and distillation time is 9-11 hours；D, the mixing discharged after distilling
Gas is delivered to cooled down in cooling tower after obtain oil mixing with water liquid；E, oil mixing with water liquid obtains China fir after water-oil separating
Another name for oil.
Distiller 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 that the relationship between efficiency of distiller produces to whole fir essential oil.Make the efficiency high of distiller it is necessary to ensure
On the premise of the convenience of feeding slag-tapping and the utilization rate of the volume of guarantee distiller, the border of material in distiller is set to be steamed with water
The direct contact surface product of vapour can be as far as possible big, steam is flowed uniformly across as far as possible material bed.
The structure of fir essential oil production distiller of the prior art is as shown in figure 1, including tank body 2；Bottom is leaned in tank body 2
Portion is provided with breathable membrane 6 and the inner chamber of tank body 2 is set into up big and down small big cavity volume and small cavity volume every setting up separately, the top surface of tank body 2 be provided with into
Material mouth 1, the top of big cavity volume are provided with gaseous mixture outlet pipe 7, steam inlet pipe 4 are inserted with small cavity volume, 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；China fir
Powder, which fills up, to be arranged in big cavity volume.
Using the distiller of such technology it is of course possible to use, but due to distillation when, in order to maximally utilize in distiller
Space, fir powder is to fill up substantially in big cavity volume, and thick and close fir powder is passed through more densely cross-linked after water vapour, and gas permeability is bad
So that material is difficult to, steaming is saturating, it is even to steam, therefore required distillation time need to generally be up to 9-11 hours, the time required to distillation too
Long, distillation efficiency is relatively low, and using effect is preferable not enough.
Utility model content
For overcome the deficiencies in the prior art, the utility model provides a kind of distillation evenly, the time required to distillation significantly
The higher fir essential oil production of shortening, distillation efficiency is more preferable with efficient distiller, using effect.
The utility model is that technical scheme is used by reaching above-mentioned technical purpose：A kind of fir essential oil production is with efficiently
Distiller, including tank body；Breathable membrane is provided with by bottom in tank body, and tank inner chamber is set to up big and down small big cavity volume every setting up separately
With small cavity volume, tank body top surface is 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；Standing to detachable in tank body is inserted with multiple permeability cells；Gathered on permeability cell side face and offer air-vent；Thoroughly
The top surface of tracheae is sealing, and the position height of its top surface is less than the position height of gaseous mixture outlet pipe, set on the top surface of permeability cell
It is equipped with hanger；The bottom surface of permeability cell offers ttom of pipe mouth；Bottom surface in tank body is provided with equal with permeability cell quantity pluggable right
Answer the base of permeability cell；The bulkhead apertures equal with permeability cell quantity are offered on breathable membrane.
The aperture of the densely covered air-vent opened up is less than the particle diameter of China fir powder on described permeability cell side face.
Described tank body is circular tank；The quantity of described permeability cell is four, and four permeability cells are with the axis of tank body
For symmetry axis center symmetric setting；The inlet radius of charging aperture is more than the spacing of permeability cell pipe axle and tank body axis.
The utility model has the advantage of：Because standing to detachable in tank body is inserted with multiple permeability cells；Permeability cell week
Gathered on face and offer air-vent；The top surface of permeability cell is sealing, and the position height of its top surface is less than the position of gaseous mixture outlet pipe
Height is put, hanger is provided with the top surface of permeability cell；The bottom surface of permeability cell offers ttom of pipe mouth；Bottom surface in tank body be provided with it is saturating
The base of the equal pluggable corresponding permeability cell of tracheae quantity；The dividing plate equal with permeability cell quantity is offered on breathable membrane to open
Mouthful.
Therefore, in the basic structure without changing tank body, ensureing the convenience of feeding slag-tapping and ensureing the appearance of distiller
On the premise of long-pending utilization rate, the superheated steam being passed through from steam inlet pipe can partly pass through during being discharged to gaseous mixture outlet pipe
" steam gas column " is formed in the cavity that each permeability cell surrounds, the presence of " steam gas column " causes the China fir around " steam gas column " first
Wood powder is more effectively distilled, and overall distillation efficiency is higher, the direct contact surface of the border of material and water vapour in distiller
Product is bigger, steam is more uniformly passed through material bed, the presence of " the steam gas column " of scattering device also causes steam to penetrate greatly
The thick and resistance with wet China fir powder body greatly reduces in cavity volume, and the China fir powder body for making original thick close band wet becomes relative
" fluffy ", distillation evenly, overall distillation efficiency greatly improve, distill required time can be greatly shortened, using effect is more managed
Think.
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 distiller of prior art；
Fig. 2 is subdivision schematic diagram of the present utility model；
Fig. 3 is the fractionation schematic diagram of the ventilative tube portion in the 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, base 9, hanger 10, ttom of pipe mouth 11, bulkhead apertures 12
Embodiment
Embodiment of the present utility model, as shown in Figure 2 and Figure 3, a kind of fir essential oil production efficient distiller, 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 up big and down small big cavity volume and small cavity volume every setting up separately,
The top surface of tank body 2 is provided with charging aperture 1, and the top of big cavity volume is provided with gaseous mixture outlet pipe 7, steam inlet pipe 4, tank body 2 are inserted with small cavity volume
Side is provided with slag notch 3, and the top of slag notch 3 connects with big cavity volume, and the bottom of slag notch 3 connects with small cavity volume, slag notch 3
It is provided with slag door 5；Standing to detachable in tank body 2 is inserted with multiple permeability cells 8；Being gathered on the side face of permeability cell 8, it is ventilative to offer
Hole；The top surface of permeability cell 8 is sealing, and the position height of its top surface is less than the position height of gaseous mixture outlet pipe 7, permeability cell 8
Hanger 10 is provided with top surface；The bottom surface of permeability cell 8 offers ttom of pipe mouth 11；Bottom surface in tank body 2 is provided with and the quantity of permeability cell 8
The base 9 of equal pluggable corresponding permeability cell 8；The bulkhead apertures equal with the quantity of permeability cell 8 are offered on breathable membrane 6
12。
The aperture of the densely covered air-vent opened up is less than the particle diameter of China fir powder on the described side face of permeability cell 8.
Described tank body 2 is circular tank 2；The quantity of described permeability cell 8 is four, and four permeability cells 8 are with tank body 2
Axis is symmetry axis center symmetric setting；The inlet radius of charging aperture 1 is more than the spacing of the pipe axle of permeability cell 8 and the axis of tank body 2.
Application method of the present utility model：
When before distillation, first with hanger 10 by each permeability cell 8 lifted successively into tank body 2 from charging aperture 1 and through it is corresponding every
Plate opening 12 feeds the bottom of permeability cell 8 after grafting is good on corresponding base 9 again.Such as permeability cell 8 is fixedly connected with tank body 2
It is integrated, it is clear that the inconvenient and inner chamber of permeability cell 8 of slagging tap is difficult to clear up.
When slagging tap, first with hanger 10 by each permeability cell 8 successively from charging aperture 1 hang out after again with slagging tap, what is hung out is each ventilative
Pipe 8 is rinsed net with water.It is exactly that can enter unavoidably for the ease of removing in distillation that ttom of pipe mouth 11 is set on the bottom face of permeability cell 8
Tiny granulated slag in pipe.
The utility model does not have to the basic structure for changing tank body 2, only by simple but cleverly technology is achieved that and makes steaming
Evaporate evenly, distillation the time required to be greatly shortened, the purpose that distillation efficiency is higher, through the Comparability test under multiple equal conditions
Measure, original distillation time needs 9-11 hours, as long as existing 5-7 hours, distillation efficiency increase rate is obvious, and using effect is very
It is good.
Technology of the present utility model is not limited only to fir essential oil production distillation, can also be applied to other from granular material
The distillation of composition needed for steam distillation extracts.
Claims (3)
1. a kind of fir essential oil production efficient distiller, including tank body；Breathable membrane is provided with by tank body by bottom in tank body
Chamber is set to up big and down small big cavity volume and small cavity volume 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：In tank body stand to it is detachable be inserted with it is more
Individual permeability cell；Gathered on permeability cell side face and offer air-vent；The top surface of permeability cell is sealing, and the position height of its top surface is low
In being provided with hanger in the position height of gaseous mixture outlet pipe, the top surface of permeability cell；The bottom surface of permeability cell offers ttom of pipe mouth；Tank body
Interior bottom surface is provided with the base of the pluggable corresponding permeability cell equal with permeability cell quantity；Offered on breathable membrane and permeability cell
The equal bulkhead apertures of quantity.
A kind of 2. efficient distiller of fir essential oil production according to claim 1, it is characterised in that：Described permeability cell
The aperture of the densely covered air-vent opened up is less than the particle diameter of China fir powder on side face.
A kind of 3. efficient distiller of fir essential oil production according to claim 2, it is characterised in that：Described tank body is
Circular tank；The quantity of described permeability cell is four, and four permeability cells are using the axis of tank body as symmetry axis center symmetric setting；
The inlet radius of charging aperture is more than the spacing of permeability cell pipe axle and tank body axis.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720486207.3U CN206746022U (en) | 2017-05-04 | 2017-05-04 | A kind of efficient distiller of fir essential oil production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720486207.3U CN206746022U (en) | 2017-05-04 | 2017-05-04 | A kind of efficient distiller of fir essential oil production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206746022U true CN206746022U (en) | 2017-12-15 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720486207.3U Expired - Fee Related CN206746022U (en) | 2017-05-04 | 2017-05-04 | A kind of efficient distiller of fir essential oil production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206746022U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106924987A (en) * | 2017-05-04 | 2017-07-07 | 福建鑫绿林产品开发有限公司 | Efficient distiller is used in a kind of fir essential oil production |
-
2017
- 2017-05-04 CN CN201720486207.3U patent/CN206746022U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106924987A (en) * | 2017-05-04 | 2017-07-07 | 福建鑫绿林产品开发有限公司 | Efficient distiller is used in a kind of fir essential oil production |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171215 Termination date: 20210504 |