CN206700819U - A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap - Google Patents
A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap Download PDFInfo
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- CN206700819U CN206700819U CN201720418505.9U CN201720418505U CN206700819U CN 206700819 U CN206700819 U CN 206700819U CN 201720418505 U CN201720418505 U CN 201720418505U CN 206700819 U CN206700819 U CN 206700819U
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- tank body
- slag notch
- cavity volume
- breathable membrane
- essential oil
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Abstract
The utility model discloses a kind of fir essential oil production alembic slagged tap and facilitate efficiency higher, 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；Breathable membrane plate face is that angle at an acute angle is set with tank body bottom surface；The domatic toe that breathable membrane plate face is formed is towards slag notch.Structure is more reasonable, and scarfing cinder is convenient, the direct contact surface product of the overall border of material and vapor is bigger in alembic, and distillation efficiency is higher.
Description
Technical field
The utility model belongs to the extractive technique field of fir essential oil, is related to a kind of China fir essence slagged tap and facilitate efficiency higher
Oily production 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.The step of extraction by steam distillation 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 vapor 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
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, breathes freely
Dividing 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 breathable membrane 6 and the bottom surface of tank body 2 are to be arranged in parallel
, therefore, the size of the direct contact surface product of the overall border of material and vapor is equivalent to breathable membrane 6 in alembic
Area, direct contact surface product is big not enough, and because breathable membrane 6 and the bottom surface of tank body 2 be arranged in parallel, great Rong when slagging tap
The band wet slag material of intracavitary 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
Higher fir essential oil production alembic, using effect are more preferable.
The utility model is that technical scheme is used by reaching above-mentioned technical purpose：A kind of slag tap facilitates efficiency higher
Fir essential oil production alembic, including tank body；Breathable membrane is provided with by bottom in tank body to be set to tank inner chamber every setting up separately
Two small cavity volumes, tank body top surface are provided with charging aperture under big, and the top of big cavity volume is provided with gaseous mixture outlet pipe, is inserted with small cavity volume
Steam inlet pipe, tank body side are 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
Logical, slag notch is provided with slag door；Breathable membrane plate face is that angle at an acute angle is set with tank body bottom surface；Breathable membrane plate face is formed
Domatic toe towards slag notch.
Described breathable membrane plate face is set with tank body bottom surface in 10-15 degree angle.
The utility model has the advantage of：
Because the plate face of breathable membrane 6 and the bottom surface of tank body 2 are that angle at an acute angle is set.Therefore, when slagging tap, breathable membrane 6
The effect for being oriented to slope is served, scarfing cinder is faster more convenient.
Equally also due to the plate face of breathable membrane 6 and the bottom surface of tank body 2 are angle settings at an acute angle.Therefore, breathable membrane 6 exists
The section ellipse of the inner chamber of tank body 2, area is obviously just bigger than traditional circular cross-section, therefore distillation efficiency is higher,
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
Embodiment
Embodiment of the present utility model, as shown in figure 3, a kind of fir essential oil production distillation for facilitating efficiency higher of slagging tap
Tank, 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 appearances every setting up separately
Chamber, the top surface of tank body 2 are 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 are inserted with small cavity volume
The side of body 2 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, slags tap
Mouth 3 is provided with slag door 5；The plate face of breathable membrane 6 is that angle at an acute angle is set with the bottom surface of tank body 2.What the plate face of breathable membrane 6 was formed
Domatic toe is towards slag notch 3.
The described plate face of breathable membrane 6 is set with the bottom surface of tank body 2 in 10-15 degree angle.The too small improved effect of angle
Fruit is not obvious enough, the too big dischargeable capacity that can then take too many alembic of angle.
Claims (2)
1. a kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap, including tank body；It is provided with thoroughly by bottom in tank body
Tank inner chamber is set to two up big and down small cavity volumes every setting up separately by air bound plate, and tank body top surface is provided with charging aperture, the top of big cavity volume
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 and big cavity volume
Connection, the bottom of slag notch connect with small cavity volume, and slag notch is provided with slag door；It is characterized in that：Breathable membrane plate face and tank body
Bottom surface is that angle at an acute angle is set；The domatic toe that breathable membrane plate face is formed is towards slag notch.
2. a kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap according to claim 1, its feature exist
In：Described breathable membrane plate face is set with tank body bottom surface in 10-15 degree angle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720418505.9U CN206700819U (en) | 2017-04-20 | 2017-04-20 | A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720418505.9U CN206700819U (en) | 2017-04-20 | 2017-04-20 | A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206700819U true CN206700819U (en) | 2017-12-05 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720418505.9U Expired - Fee Related CN206700819U (en) | 2017-04-20 | 2017-04-20 | A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206700819U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106880956A (en) * | 2017-04-20 | 2017-06-23 | 福建鑫绿林产品开发有限公司 | A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap |
| CN114774196A (en) * | 2022-03-30 | 2022-07-22 | 南京昌阳科技发展有限公司 | Distillation device for extracting plant essential oil by steam distillation method |
-
2017
- 2017-04-20 CN CN201720418505.9U patent/CN206700819U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106880956A (en) * | 2017-04-20 | 2017-06-23 | 福建鑫绿林产品开发有限公司 | A kind of fir essential oil production alembic for facilitating efficiency higher of slagging tap |
| CN114774196A (en) * | 2022-03-30 | 2022-07-22 | 南京昌阳科技发展有限公司 | Distillation device for extracting plant essential oil by steam distillation method |
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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: 20210420 |
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| CF01 | Termination of patent right due to non-payment of annual fee |