CN206751768U - A kind of high yield pulp1 production line of fir essential oil - Google Patents
A kind of high yield pulp1 production line of fir essential oil Download PDFInfo
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- CN206751768U CN206751768U CN201720480620.9U CN201720480620U CN206751768U CN 206751768 U CN206751768 U CN 206751768U CN 201720480620 U CN201720480620 U CN 201720480620U CN 206751768 U CN206751768 U CN 206751768U
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- conveying device
- breaking walls
- destilling tower
- refrigerating plant
- production line
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Abstract
The utility model discloses a kind of high yield pulp1 production line of fir essential oil, production line includes boiler, steam superheating device, cuts open block assembly, slicing device, reducing mechanism, agitating device, destilling tower, cooling tower, oily-water seperating equipment；The output jet chimney of boiler connects after being heated by steam superheating device with the entrance of destilling tower；Cut open block assembly, slicing device, reducing mechanism, agitating device and pass sequentially through corresponding conveying device connection；Destilling tower gas outlet connects with cooling tower air inlet；The condensate outlet of cooling tower connects with oily-water seperating equipment entrance；Also include freezer, means for breaking walls；Means for breaking walls includes the stone roller road of steel plate laying, vibrating roller；The output end of agitating device and the feeding mouth of refrigerating plant are connected by conveying device；The discharging opening of refrigerating plant and the feeding mouth of means for breaking walls are connected by conveying device；The discharging opening of means for breaking walls and the feeding mouth of destilling tower are connected by conveying device.Broken wall cost is low, time consumption and energy consumption is small, yield is high.
Description
Technical field
The utility model belongs to the extractive technique field of fir essential oil, is related to a kind of high yield pulp1 production line of fir essential oil.
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, it is typically only 1~2%, cedrene, the quality percentage of cedar wood alcohol contain in fir essential oil
Amount general be no greater than 20%.Several techniques compare, and steam distillation is the production technology of preferable environment-friendly type, but should also
This is optimized to improve yield and further reduce energy consumption.
Such as：Open (bulletin) number is CN105176690A, entitled " side of thing extraction fir essential oil to be remained using China fir three
A kind of method that thing extraction fir essential oil is remained using China fir three is disclosed in the patent application document technical scheme of method ", its is specific
Step is as follows：1. China fir three is remained into thing is processed into fir powder；2. fir powder is sent into the tempering tank of belt stirrer, to fir powder
Middle addition dietary alkali and Nacl are stirred mixing, and fir powder, dietary alkali, the weight of Nacl are：Fir powder 750
Part, 2.5~3.5 parts of dietary alkali, 1.8~2.2 parts of Nacl；3. the fir powder mixed is sent into destilling tower, to destilling tower
In to be passed through temperature be that 240~260 DEG C of water vapour is distilled, distillation time is 9~11 hours；4. the mixing discharged after distillation
Gas is cooled down by pipeline into cooling tower, and cooling water temperature control obtains profit below 60 DEG C, after cooling and mixed
Close liquid；5. oil mixing with water liquid obtains fir essential oil after water-oil separating.Oil yield and the China fir of fir essential oil can be effectively improved
The content of cedar wood alcohol, cedrene in another name for oil.
Using the production line for extracting fir essential oil of such technology it is of course possible to use, but because fir essential oil is to be present in
China fir it is intracellular, cell wall structure complexity is tough and tensile, and broken wall is more difficult, although as can be significantly using complicated technology broken wall
Essential oil yield is improved, but production cost can also increase substantially, but the heating power broken wall of the still-process of prior art is depended merely on, take
Power consumption, its production line is reasonable not enough, yield is high not enough, 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 high yield pulp1 life of the low fir essential oil of broken wall cost
Producing line, using effect are more preferable.
The utility model is that technical scheme is used by reaching above-mentioned technical purpose：A kind of high yield pulp1 life of fir essential oil
Producing line, production line include boiler, steam superheating device, cut open block assembly, slicing device, reducing mechanism, agitating device, destilling tower,
Cooling tower, oily-water seperating equipment；The output jet chimney of boiler enters after being heated by steam superheating device with the steam of destilling tower
Mouth connection；Cut open block assembly, slicing device, reducing mechanism, agitating device and pass sequentially through corresponding conveying device connection；Distillation
The gas outlet of tower connects with the air inlet of cooling tower；The condensate outlet of cooling tower connects with the entrance of oily-water seperating equipment；Also
Including refrigerating plant, means for breaking walls；Described refrigerating plant is freezer；Described means for breaking walls includes the stone roller of a steel plate laying
Road, a vibrating roller；The output end of agitating device and the feeding mouth of refrigerating plant are connected by conveying device；Freezing dress
The discharging opening and the feeding mouth of means for breaking walls put are connected by conveying device；The discharging opening of means for breaking walls and the feeding mouth of destilling tower
Connected by conveying device.
The utility model has the advantage of：
Due to also including refrigerating plant, means for breaking walls；Described refrigerating plant is freezer；Described means for breaking walls includes one
Nian Dao, a vibrating roller for bar steel plate laying；The output end of agitating device and the feeding mouth of refrigerating plant pass through conveying
Device connects；The discharging opening of refrigerating plant and the feeding mouth of means for breaking walls are connected by conveying device；The discharging opening of means for breaking walls
It is connected with the feeding mouth of destilling tower by conveying device；It can reduce the cell of China fir by the low simple freezing of broken wall cost
Toughness and it is brittle after carried out that quite a lot of a part of Chinese fir cell broken wall, portion will be made after oscillatory type crushes again with vibrating roller
Powder after point broken wall goes to distill again that obvious time consumption and energy consumption is smaller, and yield improves.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 production line of prior art；
Fig. 2 is the schematic diagram of production line of the present utility model.
Marker number in accompanying drawing is described as follows：Boiler 1, steam superheating device 2, slicing device 3, reducing mechanism 4, cut open block
Device 5, destilling tower 6, agitating device 7, cooling tower 8, oily-water seperating equipment 9, means for breaking walls 10, refrigerating plant 11
Embodiment
Embodiment of the present utility model, as shown in Fig. 2 a kind of high yield pulp1 production line of fir essential oil, production line includes pot
Stove 1, steam superheating device 2, cut open block assembly 5, slicing device 3, reducing mechanism 4, agitating device 7, destilling tower 6, cooling tower 8, oil
Water separation device 9；The output jet chimney of boiler 1 is connected by the steam inlet after the heating of steam superheating device 2 with destilling tower 6
It is logical；Cut open block assembly 5, slicing device 3, reducing mechanism 4, agitating device 7 four and pass sequentially through corresponding conveying device connection；Distillation
The gas outlet of tower 6 connects with the air inlet of cooling tower 8；The condensate outlet of cooling tower 8 connects with the entrance of oily-water seperating equipment 9
It is logical；Also include refrigerating plant 11, means for breaking walls 10；Described refrigerating plant 11 is freezer；Described means for breaking walls 10 includes one
Nian Dao, a vibrating roller for bar steel plate laying；The feeding mouth of the output end of agitating device 7 and refrigerating plant 11 passes through defeated
Device is sent to connect；The discharging opening of refrigerating plant 11 is connected with the feeding mouth of means for breaking walls 10 by conveying device；Means for breaking walls 10
Discharging opening be connected with the feeding mouth of destilling tower 6 by conveying device.
Comprised the following steps that using what a kind of high yield pulp1 production line of described fir essential oil was produced：
A, powder processed, by cuing open block, section, crushing, China fir raw material is ground into the fir powder of 80~120 mesh；
B, mix, add dietary alkali into fir powder and Nacl is stirred mixing, the weight of three is：China fir
750 parts of wood powder, 2.5~3.5 parts of dietary alkali, 1.8~2.2 parts of Nacl, 4~6 parts of urea；
C, freeze, the powder mixed is sent into freezer and put 18~24 hours, temperature of ice house control is subzero 6 degree~zero
It is lower 4 degree；
D, broken wall, the powder freezed is shakeout on road is ground, and has the stone roller road of freezing powder at stand with vibrating roller
Back pressure of coming up stone roller no less than three, rise again to room temperature naturally back and forth by the powder on Hou Jiangnian roads；
E, distill, the good fir powder of broken wall is sent into destilling tower, temperature is passed through into destilling tower as 240 DEG C~260 DEG C
Superheated steam distilled, distillation time be 5~7 hours；
F, cool down, the mixed gas discharged in still-process is cooled down by pipeline into cooling tower, cooling water
Temperature should be controlled below 60 DEG C, and condensed oil mixing with water liquid is sent into oily-water seperating equipment in cooling tower；
The oil that oil mixing with water liquid obtains after water-oil separating is China fir essence by G, water-oil separating, oily-water seperating equipment
Oil.
Claims (1)
1. a kind of high yield pulp1 production line of fir essential oil, production line includes boiler, steam superheating device, cuts open block assembly, section dress
Put, reducing mechanism, agitating device, destilling tower, cooling tower, oily-water seperating equipment；The output jet chimney of boiler passes through steam mistake
Connected after thermal heating with the steam inlet of destilling tower；Cut open block assembly, slicing device, reducing mechanism, agitating device according to
It is secondary to be connected by corresponding conveying device；The gas outlet of destilling tower connects with the air inlet of cooling tower；The condensate liquid of cooling tower goes out
Mouth connects with the entrance of oily-water seperating equipment；It is characterized in that：Also include refrigerating plant, means for breaking walls；Described refrigerating plant
It is freezer；Described means for breaking walls includes Nian Dao, a vibrating roller for a steel plate laying；The output end of agitating device
It is connected with the feeding mouth of refrigerating plant by conveying device；The discharging opening of refrigerating plant and the feeding mouth of means for breaking walls pass through conveying
Device connects；The discharging opening of means for breaking walls and the feeding mouth of destilling tower are connected by conveying device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720480620.9U CN206751768U (en) | 2017-05-03 | 2017-05-03 | A kind of high yield pulp1 production line of fir essential oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720480620.9U CN206751768U (en) | 2017-05-03 | 2017-05-03 | A kind of high yield pulp1 production line of fir essential oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206751768U true CN206751768U (en) | 2017-12-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720480620.9U Expired - Fee Related CN206751768U (en) | 2017-05-03 | 2017-05-03 | A kind of high yield pulp1 production line of fir essential oil |
Country Status (1)
| Country | Link |
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| CN (1) | CN206751768U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108636826A (en) * | 2018-04-16 | 2018-10-12 | 福建鑫绿林产品开发有限公司 | A kind of fir essential oil raw material screening batch processing method |
-
2017
- 2017-05-03 CN CN201720480620.9U patent/CN206751768U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108636826A (en) * | 2018-04-16 | 2018-10-12 | 福建鑫绿林产品开发有限公司 | A kind of fir essential oil raw material screening batch processing 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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171215 Termination date: 20210503 |