CN206706054U - A kind of fir essential oil production alembic of optimization design - Google Patents
A kind of fir essential oil production alembic of optimization design Download PDFInfo
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- CN206706054U CN206706054U CN201720432561.8U CN201720432561U CN206706054U CN 206706054 U CN206706054 U CN 206706054U CN 201720432561 U CN201720432561 U CN 201720432561U CN 206706054 U CN206706054 U CN 206706054U
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- Prior art keywords
- breathable membrane
- tank body
- slag notch
- plate face
- essential oil
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Abstract
The utility model discloses a kind of fir essential oil production alembic of optimization design, including tank body；In tank body bottom breathable membrane is provided with by bottom, tank body top surface is provided with charging aperture, the side wall of tank body is provided with gaseous mixture outlet pipe by top, the lower section of bottom breathable membrane is provided with steam inlet pipe, the slag notch top that tank wall is provided with connects with the top cavity volume positioned at bottom breathable membrane, slag notch bottom connects with cavity volume below the breathable membrane of bottom, and slag notch is provided with slag door；Also include side breathable membrane；The plate face of bottom breathable membrane and the bottom surface of tank body are at an acute angle；The domatic toe that bottom breathable membrane plate face is formed is abutted against with slag notch；The top of the slope of bottom breathable membrane plate face is connected along an oblate scarce shape space, the straight flange in space is installed between the internal face of side and tank body with the base of side breathable membrane, and other sides of side breathable membrane and the internal face of tank body connect；Side breathable membrane summit is less than gaseous mixture outlet pipe.Scarfing cinder is convenient, distillation efficiency is high.
Description
Technical field
The utility model belongs to the extractive technique field of fir essential oil, and the fir essential oil production for being related to a kind of optimization design is used
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, 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
Be provided with bottom breathable membrane 6 by bottom and the inner chamber of tank body 2 be set to two up big and down small cavity volumes 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, and bottom is saturating
Air bound plate 6 be arranged in parallel with the bottom surface of tank body 2.
Using the alembic of such technology it is of course possible to use, but because bottom breathable membrane 6 with the bottom surface of tank body 2 is parallel set
Put, therefore, the size that the direct contact surface of the overall border of material and water vapour accumulates in alembic just just corresponds to bottom and breathed freely
The area of dividing plate 6, direct contact surface product is big not enough, and because bottom breathable membrane 6 and the bottom surface of tank body 2 be arranged in parallel, goes out
Band wet slag material during slag in big cavity volume is not easy to drop out from slag notch 3, and scarfing cinder is less efficient, and 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 scarfing cinder is convenient, distillation efficiency
The fir essential oil production alembic of higher optimization design, using effect are more preferable.
The utility model is that technical scheme is used by reaching above-mentioned technical purpose：A kind of fir essential oil of optimization design
Production alembic, including tank body；Bottom breathable membrane is provided with by bottom in tank body, the top surface of cylindrical tank body is provided with charging
Mouthful, the side wall of tank body is provided with gaseous mixture outlet pipe by top, and the side wall of tank body leans on bottom and positioned at bottom breathable membrane
Lower section is inserted with steam inlet pipe, and the side wall of tank body is provided with slag notch, the top of slag notch and the top for being located at bottom breathable membrane
Partial tank body cavity volume connection, the bottom of slag notch connects with the cavity volume of the section below positioned at bottom breathable membrane, on slag notch
Provided with slag door；Also include side breathable membrane；The plate face of bottom breathable membrane and the bottom surface of tank body are that angle at an acute angle is set；Bottom is saturating
The domatic toe that air bound plate plate face is formed is abutted against with slag notch；The domatic top of the slope that bottom breathable membrane plate face is formed is along side and tank
Be installed with an oblate scarce shape space between the internal face of the corresponding position of body, the straight flange in oblate scarce shape space and inclined side it is ventilative every
The internal face of the base connection of plate, other sides of side breathable membrane and the corresponding position of tank body connects；The summit of side breathable membrane
Highly it is less than the height of the minimum point of the mouth of pipe of gaseous mixture outlet pipe；Both bottom breathable membrane and side breathable membrane are monolithically fabricated
The inner chamber of tank body is set to two up big and down small cavity volumes every setting up separately by combination bending shape plate face.
The described plate face of bottom breathable membrane and the bottom surface of tank body is set in 10-15 degree angle；Breathe freely described side
Dividing plate is set with tank body bottom surface in 80-85 degree angle.
The utility model has the advantage of：
Due to also including side breathable membrane；The plate face of bottom breathable membrane and the bottom surface of tank body are that angle at an acute angle is set；
The domatic toe that bottom breathable membrane plate face is formed is abutted against with slag notch；The domatic top of the slope that bottom breathable membrane plate face is formed is along side
An oblate scarce shape space is installed between the internal face of the corresponding position of tank body, the straight flange in oblate scarce shape space and inclined side are saturating
The internal face of the base connection of air bound plate, other sides of side breathable membrane and the corresponding position of tank body connects；The top of side breathable membrane
Height of the height of point less than the minimum point of the mouth of pipe of gaseous mixture outlet pipe；The overall structure of both bottom breathable membrane and side breathable membrane
Into combination bending shape plate face the inner chamber of tank body is set to two up big and down small cavity volumes every setting up separately.
Therefore, when slagging tap, the entirety of both bottom breathable membrane and side breathable membrane serves the effect for being oriented to slope, scarfing cinder
Faster it is more convenient.
Because the combination bending shape plate face being monolithically fabricated of both bottom breathable membrane and side breathable membrane is by the inner chamber of tank body
Two up big and down small cavity volumes are set to every setting up separately, and side breathable membrane has set out a steam in the side shelf of tank body and directly led to
Road.Therefore, steam enters being monolithically fabricated for the fashionable product with the direct contact surface of material and both bottom breathable membrane and side breathable membrane
Combination bending shape plate suqare it is suitable, area is obviously just more much bigger than traditional circular cross-section, and steam can be contained in tank body
High, medium and low three positions of overall " block " of material large area carried out to material " block " directly contacted, therefore distill effect
Can be much higher, distillation time can be greatly shortened, 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 partial cutaway sequential Stereoscopic schematic diagram of the present utility model；
Fig. 4 is the plane subdivision schematic diagram of a side 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, bottom it is ventilative every
Plate 6, gaseous mixture outlet pipe 7, side breathable membrane 8
Embodiment
Embodiment of the present utility model, as shown in Figure 3, Figure 4, a kind of fir essential oil production alembic of optimization design,
Including tank body 2；Bottom breathable membrane 6 is provided with by bottom in tank body 2, the top surface of cylindrical tank body 2 is provided with charging aperture 1, tank body 2
Side wall is provided with gaseous mixture outlet pipe 7 by top, and the side wall of tank body 2 is inserted by bottom and positioned at the lower section of bottom breathable membrane 6
Provided with steam inlet pipe 4, the side wall of tank body 2 is provided with slag notch 3, the top of slag notch 3 and the upper portion positioned at bottom breathable membrane 6
The cavity volume of tank body 2 connection divided, the bottom of slag notch 3 connect with the cavity volume of the section below positioned at bottom breathable membrane 6, slag notch 3
It is provided with slag door 5；Also include side breathable membrane 8；The plate face of bottom breathable membrane 6 is that angle at an acute angle is set with the bottom surface of tank body 2
's；The domatic toe that the plate face of bottom breathable membrane 6 is formed is abutted against with slag notch 3；The domatic slope that the plate face of bottom breathable membrane 6 is formed
Top is along an oblate scarce shape space is installed between the internal face of side and the corresponding position of tank body 2, the straight flange in oblate scarce shape space is with inclining
The base connection of oblique side breathable membrane 8, other sides of side breathable membrane 8 are connected with the internal face of the corresponding position of tank body 2；Side is saturating
Height of the height on the summit of air bound plate 8 less than the minimum point of the mouth of pipe of gaseous mixture outlet pipe 7；Bottom breathable membrane 6 and side it is ventilative every
The inner chamber of tank body 2 is set to two up big and down small cavity volumes every setting up separately by both the combination bending shape plate faces being monolithically fabricated of plate 8.
The plate face of described bottom breathable membrane 6 is set with the bottom surface of tank body 2 in 10-15 degree angle, and angle is too small to be changed
The effect entered is not obvious enough, the too big dischargeable capacity that can then take too many alembic of angle；Described side breathable membrane 8 and tank body
2 bottom surfaces are set in 80-85 degree angle, and angle too conference takes the dischargeable capacity of too many alembic.
Claims (2)
1. a kind of fir essential oil production alembic of optimization design, including tank body；Bottom breathable membrane is provided with by bottom in tank body,
The top surface of cylindrical tank body is provided with charging aperture, and the side wall of tank body is provided with gaseous mixture outlet pipe, the side wall of tank body by top
Be inserted with steam inlet pipe by bottom and below the breathable membrane of bottom, the side wall of tank body is provided with slag notch, slag notch
Top connects with the tank body cavity volume of the upper section positioned at bottom breathable membrane, and the bottom of slag notch is with being located under the breathable membrane of bottom
The cavity volume connection of square part, slag notch are provided with slag door；It is characterized in that：Also include side breathable membrane；The plate of bottom breathable membrane
Face and the bottom surface of tank body are that angle at an acute angle is set；The domatic toe that bottom breathable membrane plate face is formed is abutted against with slag notch；
The domatic top of the slope that bottom breathable membrane plate face is formed is along being installed with an oblate scarce shape between the internal face of side and the corresponding position of tank body
Space, the straight flange in oblate scarce shape space are connected with the base of inclined side breathable membrane, other sides of side breathable membrane and tank body
Corresponding position internal face connection；Height of the height on the summit of side breathable membrane less than the minimum point of the mouth of pipe of gaseous mixture outlet pipe
Degree；The inner chamber of tank body is set to every setting up separately by the combination bending shape plate face being monolithically fabricated of bottom breathable membrane and both side breathable membranes
Two up big and down small cavity volumes.
A kind of 2. fir essential oil production alembic of optimization design according to claim 1, it is characterised in that：Described
The plate face of bottom breathable membrane and the bottom surface of tank body are set in 10-15 degree angle；Described side breathable membrane and tank body bottom surface
It is to be set in 80-85 degree angles.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720432561.8U CN206706054U (en) | 2017-04-24 | 2017-04-24 | A kind of fir essential oil production alembic of optimization design |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720432561.8U CN206706054U (en) | 2017-04-24 | 2017-04-24 | A kind of fir essential oil production alembic of optimization design |
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| CN206706054U true CN206706054U (en) | 2017-12-05 |
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| CN201720432561.8U Expired - Fee Related CN206706054U (en) | 2017-04-24 | 2017-04-24 | A kind of fir essential oil production alembic of optimization design |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106867677A (en) * | 2017-04-24 | 2017-06-20 | 福建鑫绿林产品开发有限公司 | A kind of fir essential oil production alembic of optimization design |
-
2017
- 2017-04-24 CN CN201720432561.8U patent/CN206706054U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106867677A (en) * | 2017-04-24 | 2017-06-20 | 福建鑫绿林产品开发有限公司 | A kind of fir essential oil production alembic of optimization design |
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| 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: 20171205 Termination date: 20210424 |