CN203866274U - Circulating cedar oil production equipment - Google Patents
Circulating cedar oil production equipment Download PDFInfo
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- CN203866274U CN203866274U CN201420292818.0U CN201420292818U CN203866274U CN 203866274 U CN203866274 U CN 203866274U CN 201420292818 U CN201420292818 U CN 201420292818U CN 203866274 U CN203866274 U CN 203866274U
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- cunninghamiae lanceolatae
- oleum cunninghamiae
- accommodation space
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- extractor
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Abstract
Circulating cedar oil production equipment comprises a steam generating device, a cedar oil extracting device, a condensation pipe device, an oil-water separation device and a cedar oil collecting device. The cedar oil extracting device comprises a cedar oil extracting tank comprising an extracting pot and an external jacket, the external jacket and the outer wall of the extracting pot enclose jointly to form an accommodating space, the extracting pot comprises a main steam dispersing pipe and a plurality of auxiliary steam dispersing pipes, one end of each auxiliary steam dispersing pipe is communicated with the accommodating space while the other ends of the auxiliary steam dispersing pipes are converged and communicated with the main steam dispersing pipe, and a vent hole is formed in the bottom of the main steam dispersing pipe. The circulating cedar oil production equipment can guarantee that cedar oil attached to steam can be completely isolated from an external heat source and cannot be too high in temperature, and thereby burning of the cedar oil can be avoided, and cedar oil quality is guaranteed powerfully.
Description
Technical field
The utility model relates to oleum Cunninghamiae lanceolatae production field, refers in particular to a kind of circulating oleum Cunninghamiae lanceolatae production unit.
Background technology
China fir is the most important reproducting tree species of south China.Fir height is large, and texture is straight, and structure is careful, and material is light and soft, and handling ease is not stuck up and do not split, corrosion resistant insect protected, and wear resistance is strong, and has aromatic odour, is therefore widely used in the aspects such as building, bridge, vessel, electric pole, furniture.Root-bark of Chinese Fir and processing waste are not well utilized at present, or stay in mountain forest and leave to rot, or as low value-added utilizations such as burnings, have caused the serious waste of resource.
A large amount of data show, contain a large amount of fir essential oils, and Root-bark of Chinese Fir are the highest positions of essential oil content in whole Chinese fir in China fir.The main component of fir essential oil is cedar wood oil alcohol, eneα-cedar, β-chamene, thujopsene, α-pinene and alpha-terpineol etc., from main chemical constitution and fragrance, all approach very much cedar(wood)oil, so can be used for substituting Cypress ethereal oil completely for perfume industry.Cedar(wood)oil has the strong banksia rose-Moschus-grane ambra fragrance, is mainly used in cosmetics class makeup and the soap classes such as toilet powder shui, muffin, kermes, also applicable to allocating in illusion type essence.Cedar(wood)oil is one of the world's ten large essential oils, being in great demand of market.Because the growth cycle of cypress is very long, within approximately 60 years, just can become a useful person, thus caused cypress scarcity of resources, thus had a strong impact on the development of China's cedar(wood)oil industry.China fir has the feature of Fast Growth, and a large amount of tree root resources that stay after its trees felling can be used for the production of fir essential oil, and alternative cedar(wood)oil is for perfume industry.
By oleum Cunninghamiae lanceolatae list, from the cypress camphor obtaining, chamene, can directly as spices, be used, also can carry out the spices of the synthetic high added value of deep processing.The synthetic perfume of cypress series mainly contains: Methyl cedryl ether, vertofix coeur, cedryl acetate, epoxycedrane, cedranone and cypress olefine aldehydr etc., be all widely used in essence and flavoring agent industry.
The extraction of oleum Cunninghamiae lanceolatae at present mainly adopts wet distillation, solvent extraction and dry distillation.The fir essential oil fragrance that adopts steam method to extract is pure, substantially meet blending requirement, but yield is very low; The fir essential oil yield of extract by solvents is high compared with water vapour, but needs a large amount of solvents, and subsequent disposal is complicated, exists energy consumption high, the problem of dissolvent residual; It is high that dry distillation is extracted yield, can obtain the products such as wood vinegar, charcoal, wood tar oil and inflammable gas, but empyreumatic oil contains the materials such as a large amount of tar, phenol, aldehyde and ketone simultaneously, has a strong impact on the quality of oleum Cunninghamiae lanceolatae.Thick empyreumatic oil must be processed through the burnt deodorization of dispelling, and could substantially meet blending requirement.
Although the yield of extraction by steam distillation oleum Cunninghamiae lanceolatae is come lowly than solvent-extraction process, its cost is comparatively cheap, and without the treatment process of follow-up complexity, thereby most domestic producer adopts steam distillation to extract oleum Cunninghamiae lanceolatae at present.Existing oleum Cunninghamiae lanceolatae production unit is generally to produce water vapour by steam-generating installation, and water vapour is passed in the retort that is stacked with China fir or China fir tree root, by retort is carried out to continuous heating, to allow water vapour constantly penetrate in China fir or China fir tree root, thereby take away oleum Cunninghamiae lanceolatae.Existing oleum Cunninghamiae lanceolatae production unit is because the direct outer wall in retort is with heating, with the oleum Cunninghamiae lanceolatae being attached on steam, be easy to occur burning because retort inwall local temperature is too high, so not only restricting the yield of extracting oleum Cunninghamiae lanceolatae, in the oleum Cunninghamiae lanceolatae extracting, can contain a large amount of tar or other unfavorable materials, can have a strong impact on the quality of oleum Cunninghamiae lanceolatae like this, this just equally also inevitable requirement through the burnt deodorization of dispelling, process, could substantially meet blending requirement.
Utility model content
The utility model provides a kind of circulating oleum Cunninghamiae lanceolatae production unit, and its main purpose is to overcome the defect that oleum Cunninghamiae lanceolatae yield is low, product contains a large amount of tar that existing oleum Cunninghamiae lanceolatae production unit exists.
For solving the problems of the technologies described above, the utility model adopts following technical scheme:
A kind of circulating oleum Cunninghamiae lanceolatae production unit, comprise steam-generating installation, oleum Cunninghamiae lanceolatae extraction element, prolong device, oily-water seperating equipment and oleum Cunninghamiae lanceolatae collection device, the outlet of described steam-generating installation is communicated in the import of described oleum Cunninghamiae lanceolatae extraction element, described oleum Cunninghamiae lanceolatae extraction element outlet is communicated in the import of described prolong device, the outlet of described prolong device is communicated in the import of described oily-water seperating equipment, described oily-water seperating equipment is provided with two outlets, one is communicated in described steam-generating installation, another is communicated in described oleum Cunninghamiae lanceolatae collection device, described oleum Cunninghamiae lanceolatae extraction element comprises at least one oleum Cunninghamiae lanceolatae extractor, described oleum Cunninghamiae lanceolatae extractor comprises the external chuck that extracts pot and be coated on this extraction outer wall of wall, described external chuck is enclosed to form an accommodation space jointly with extraction outer wall of wall, the described pot that extracts comprises by bottom centre position and extending axially to the main dispersion steam pipe at top and complex root by the aid dispersion vapour pipe that extracts pot sidewall and tiltedly extend downward described main dispersion steam pipe, one end of every aid dispersion vapour pipe is all communicated in described accommodation space, and the other end converges and is communicated on described main dispersion steam pipe, the bottom of described main dispersion steam pipe offers breather hole.
Further, described oleum Cunninghamiae lanceolatae extraction element includes two oleum Cunninghamiae lanceolatae extractors, be respectively the first oleum Cunninghamiae lanceolatae extractor and the second oleum Cunninghamiae lanceolatae extractor, wherein the described external chuck of the first oleum Cunninghamiae lanceolatae extractor is enclosed to form one first accommodation space jointly with extracting outer wall of wall, in the extraction pot of the first oleum Cunninghamiae lanceolatae extractor, the second accommodation space is set; The described external chuck of the second oleum Cunninghamiae lanceolatae extractor is enclosed to form one the 3rd accommodation space jointly with extraction outer wall of wall, the 4th accommodation space is set in the extraction pot of the second oleum Cunninghamiae lanceolatae extractor, described the first accommodation space and the 3rd accommodation space are connected, the outlet of described the second accommodation space is communicated in described the 4th accommodation space, the import of described the 3rd accommodation space is communicated in the outlet of described steam-generating installation, and the outlet of described the 4th accommodation space is communicated in the import of described prolong device.
Further, the equal unilaterally connected in entrance one end of every aid dispersion vapour pipe is in described the first/three accommodation space, and described main dispersion steam pipe is all converged and is communicated in the outlet of each aid dispersion vapour pipe.
Further, the outlet of described the second accommodation space is gone back unilaterally connected on the entrance of the described dispersion steam pipe of the second oleum Cunninghamiae lanceolatae extractor or the described main dispersion steam pipe of the second oleum Cunninghamiae lanceolatae extractor.
Further, described complex root aid dispersion vapour pipe is at least one row and arranges, aid dispersion vapour pipe on every row is consistent with the junction height of described main dispersion steam pipe, aid dispersion vapour pipe on same every row is also consistent with the junction height of described extraction pot sidewall, and every row's aid dispersion vapour pipe integral body is radial arrangement.
Compared to the prior art, the beneficial effect that the utility model produces is:
1, the utility model reasonable in design, oleum Cunninghamiae lanceolatae extraction efficiency is high and fir essential oil fragrance is pure, by the structure of oleum Cunninghamiae lanceolatae extractor being arranged to form by extracting pot and external chuck, described extraction pot does not just directly carry out Contact Heating with extraneous thermal source, but first the water vapour in accommodation space is heated by extraneous thermal source, and then utilize water vapour to enter in extraction pot and carry out heat transmission, thereby oleum Cunninghamiae lanceolatae and the extraneous thermal source that can guarantee to be attached on steam are kept apart completely, guarantee that oleum Cunninghamiae lanceolatae there will not be excess Temperature, thereby avoid occurring that oleum Cunninghamiae lanceolatae burns situation, effectively guaranteed the quality of oleum Cunninghamiae lanceolatae.
2, in the utility model, by external chuck integral body is placed in extraneous thermal source, make the steam passing into become superheated vapour under the effect of extraneous thermal source, use superheated vapour to be conducive to the extraction to oleum Cunninghamiae lanceolatae composition on China fir, and can improve the quality of extracting rear oleum Cunninghamiae lanceolatae.
3, in utility model, by the first oleum Cunninghamiae lanceolatae extractor and the second oleum Cunninghamiae lanceolatae extractor are set, and passing into of steam is arranged to successively by the 3rd accommodation space to the first accommodation space again to the second accommodation space finally to the mode of the 4th accommodation space, there is situation about directly contacting with extraneous thermal source in the oleum Cunninghamiae lanceolatae that can substantially stop to be attached to like this on steam, adopt two oleum Cunninghamiae lanceolatae extractor series connection to extract and can save the energy, improve extraction solubility and the oleum Cunninghamiae lanceolatae quality of oleum Cunninghamiae lanceolatae, by being also conducive to improve the oleum Cunninghamiae lanceolatae oil yield of Board Lot China fir raw material.
4, in utility model, the water producing in oily-water seperating equipment can directly be drained in steam generating device and recycle, thereby the whole process that utility model is produced there is no any waste water of external discharge, can not cause contaminated wastewater to environment, also can avoid the loss of the not separated oleum Cunninghamiae lanceolatae of part in water, thereby pass through repeatedly cyclic production, in utility model, the oleum Cunninghamiae lanceolatae oil yield of Board Lot China fir raw material can effectively be promoted.
5, in the utility model, by described main dispersion steam pipe and aid dispersion vapour pipe are set, can be so that the whole China fir raw material that extracts each position in pot can both act on mutually with water vapour fully and water vapour can be kept to comparatively stable temperature, can be so that water vapour can be uniformly distributed in to be extracted in pot, and then guarantee that oleum Cunninghamiae lanceolatae extracts stability and the consistence of quality product.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the enlarged diagram at A place in the utility model.
Fig. 3 is the structural representation of the first oleum Cunninghamiae lanceolatae extractor described in the utility model.
Fig. 4 is that Fig. 3 is along the diagrammatic cross-section at B-B place.
Embodiment
Embodiment of the present utility model is described with reference to the accompanying drawings.
With reference to Fig. 1-Fig. 4.A kind of circulating oleum Cunninghamiae lanceolatae production unit, comprise steam-generating installation 1, oleum Cunninghamiae lanceolatae extraction element 2, prolong device 3, oily-water seperating equipment 4 and oleum Cunninghamiae lanceolatae collection device 5, the outlet of described steam-generating installation 1 is communicated in the import of described oleum Cunninghamiae lanceolatae extraction element 2, described oleum Cunninghamiae lanceolatae extraction element 2 outlets are communicated in the import of described prolong device 3, the outlet of described prolong device 3 is communicated in the import of described oily-water seperating equipment 4, described oily-water seperating equipment 4 is provided with two outlets, one is communicated in described steam-generating installation 1, another is communicated in described oleum Cunninghamiae lanceolatae collection device 5, described oleum Cunninghamiae lanceolatae extraction element 2 comprises at least one oleum Cunninghamiae lanceolatae extractor 20, described oleum Cunninghamiae lanceolatae extractor 20 comprises the external chuck 22 that extracts pot 21 and be coated on these extraction pot 21 outer walls, described external chuck 22 is enclosed to form an accommodation space jointly with extraction pot 21 outer walls, the described pot 21 that extracts comprises by bottom centre position and extending axially to the main dispersion steam pipe 23 at top and complex root by the aid dispersion vapour pipe 24 that extracts pot 21 sidewalls and tiltedly extend downward described main dispersion steam pipe 23, one end of every aid dispersion vapour pipe 24 is all communicated in described accommodation space, and the other end converges and is communicated on described main dispersion steam pipe 23, the bottom of described main dispersion steam pipe 23 offers breather hole.The present embodiment reasonable in design, oleum Cunninghamiae lanceolatae extraction efficiency is high and fir essential oil fragrance is pure, by the structure of oleum Cunninghamiae lanceolatae extractor 20 being arranged to form by extracting pot 21 and external chuck 22, described extraction pot 21 does not just directly carry out Contact Heating with extraneous thermal source, but first the water vapour in accommodation space is heated by extraneous thermal source, and then utilize water vapour to enter in extraction pot 21 and carry out heat transmission, thereby oleum Cunninghamiae lanceolatae and the extraneous thermal source that can guarantee to be attached on steam are kept apart completely, guarantee that oleum Cunninghamiae lanceolatae there will not be excess Temperature, thereby avoid occurring that oleum Cunninghamiae lanceolatae burns situation, effectively guaranteed the quality of oleum Cunninghamiae lanceolatae.In addition, the present embodiment is by being placed on external chuck 22 integral body in extraneous thermal source, make the steam passing into become superheated vapour under the effect of extraneous thermal source, use superheated vapour to be conducive to the extraction to oleum Cunninghamiae lanceolatae composition on China fir, and can improve the quality of extracting rear oleum Cunninghamiae lanceolatae.
With reference to Fig. 1-Fig. 4.Preferred version as the present embodiment, described oleum Cunninghamiae lanceolatae extraction element 2 includes two oleum Cunninghamiae lanceolatae extractors 20, be respectively the first oleum Cunninghamiae lanceolatae extractor 201 and the second oleum Cunninghamiae lanceolatae extractor 2022, wherein the described external chuck 22 of the first oleum Cunninghamiae lanceolatae extractor 201 and extraction pot 21 outer walls are enclosed to form interior second accommodation space 252 that arranges of extraction pot 21 of one first accommodation space 251, the first oleum Cunninghamiae lanceolatae extractors 201 jointly; The described external chuck 22 of the second oleum Cunninghamiae lanceolatae extractor 202 is enclosed to form one the 3rd accommodation space 253 jointly with extraction pot 21 outer walls, interior the 4th accommodation space 254 that arranges of extraction pot 21 of the second oleum Cunninghamiae lanceolatae extractor 202, described the first accommodation space 251 and the 3rd accommodation space 253 are connected, the outlet of described the second accommodation space 252 is communicated in described the 4th accommodation space 254, the import of described the 3rd accommodation space 253 is communicated in the outlet of described steam-generating installation 1, and the outlet of described the 4th accommodation space 254 is communicated in the import of described prolong device 3.In the utility model, by the first oleum Cunninghamiae lanceolatae extractor 201 and the second oleum Cunninghamiae lanceolatae extractor 202 are set, and passing into of steam is arranged to successively by the 3rd accommodation space 253 to first accommodation spaces 251 again to the second accommodation space 252 finally to the mode of the 4th accommodation space 254, there is situation about directly contacting with extraneous thermal source in the oleum Cunninghamiae lanceolatae that can substantially stop to be attached to like this on steam, adopt 20 series connection of two oleum Cunninghamiae lanceolatae extractors to extract and can save the energy, improve extraction solubility and the oleum Cunninghamiae lanceolatae quality of oleum Cunninghamiae lanceolatae, by being also conducive to improve the oleum Cunninghamiae lanceolatae oil yield of Board Lot China fir raw material.
With reference to Fig. 1-Fig. 4.The equal unilaterally connected in entrance one end of every aid dispersion vapour pipe 24 is in described the first/three accommodation space 253, and described main dispersion steam pipe 23 is all converged and is communicated in the outlet of each aid dispersion vapour pipe 24.The outlet of described the second accommodation space 252 is gone back unilaterally connected on the entrance of the described dispersion steam pipe of the second oleum Cunninghamiae lanceolatae extractor 202 or the described main dispersion steam pipe 23 of the second oleum Cunninghamiae lanceolatae extractor 202.Described complex root aid dispersion vapour pipe 24 is at least one row and arranges, aid dispersion vapour pipe 24 on every row is consistent with the junction height of described main dispersion steam pipe 23, aid dispersion vapour pipe 24 on same every row is also consistent with the junction height of described extraction pot 21 sidewalls, and every row's aid dispersion vapour pipe 24 integral body are radial arrangement.In the present embodiment, by described main dispersion steam pipe 23 and aid dispersion vapour pipe 24 are set, can be so that the whole China fir raw material that extracts each position in pot 21 can both act on mutually with water vapour fully and water vapour can be kept to comparatively stable temperature, can be so that water vapour can be uniformly distributed in to be extracted in pot 21, and then guarantee that oleum Cunninghamiae lanceolatae extracts stability and the consistence of quality product.
With reference to Fig. 1-Fig. 4.In the utility model, use above-mentioned circulating oleum Cunninghamiae lanceolatae production unit to make the technique of oleum Cunninghamiae lanceolatae, comprise the following steps:
The first step: described the first oleum Cunninghamiae lanceolatae extractor 201 and the second oleum Cunninghamiae lanceolatae extractor 202 are placed in to thermal source and heat;
Second step: heat described steam-generating installation 1, by this steam-generating installation 1, produce water vapour and be passed in described the 3rd accommodation space 253 in the second oleum Cunninghamiae lanceolatae extractor 202,
The 3rd step: the steam part in the 3rd accommodation space 253 flows in the first accommodation space 251, another part flows to the aid dispersion vapour pipe 24 of the second oleum Cunninghamiae lanceolatae extractor 202, in steam in the aid dispersion vapour pipe 24 of above-mentioned the second oleum Cunninghamiae lanceolatae extractor 202 converges on described main dispersion steam pipe 23, flow downward and come out by the breather hole of main dispersion steam pipe 23, upwards diffusion and with the abundant combination of China fir raw material of extracting pot 21 interior middle parts and bottom position, take away the oleum Cunninghamiae lanceolatae of this China fir raw material, after abundant combination is extracted, water vapour with oleum Cunninghamiae lanceolatae flows into the import of described prolong device 3 from the outlet at the second oleum Cunninghamiae lanceolatae extractor 202 tops,
The 4th step: the interior steam of the first accommodation space 251 all flows to the aid dispersion vapour pipe 24 of the first oleum Cunninghamiae lanceolatae extractor 201, in steam in the aid dispersion vapour pipe 24 of above-mentioned the first oleum Cunninghamiae lanceolatae extractor 201 converges on described main dispersion steam pipe 23, flow downward and by the breather hole of main dispersion steam pipe 23 come out, upwards diffusion and with the abundant combination of China fir raw material of extracting pot 21 interior middle parts and bottom position, take away the oleum Cunninghamiae lanceolatae of this China fir raw material; After abundant combination is extracted, with the water vapour of oleum Cunninghamiae lanceolatae, from the outlet at the first oleum Cunninghamiae lanceolatae extractor 201 tops, flow into the below of breather hole of the described main dispersion steam pipe 23 of described the first oleum Cunninghamiae lanceolatae extractor 201, then repeating step c, until should flow into the water vapour of oleum Cunninghamiae lanceolatae the import of described prolong device 3;
The 5th step: the water vapour with oleum Cunninghamiae lanceolatae flows into after the import of described prolong device 3, thereby form moisture oleum Cunninghamiae lanceolatae through described prolong device 3 is cooling, then pass into oily-water seperating equipment 4 oleum Cunninghamiae lanceolatae is separated with water, after oleum Cunninghamiae lanceolatae separation, pass into described oleum Cunninghamiae lanceolatae collection device 5, after water separation, pass into described steam-generating installation 1.
In sum, in an embodiment, the water producing in oily-water seperating equipment 4 can directly be drained in steam generating device and recycle, thereby the whole process that utility model is produced there is no any waste water of external discharge, can not cause contaminated wastewater to environment, also can avoid the loss of the not separated oleum Cunninghamiae lanceolatae of part in water, thereby pass through repeatedly cyclic production, in utility model, the oleum Cunninghamiae lanceolatae oil yield of Board Lot China fir raw material can effectively be promoted.
Above are only embodiment of the present utility model, but design concept of the present utility model is not limited to this, allly utilizes this design to carry out the change of unsubstantiality to the utility model, all should belong to the behavior of invading the utility model protection domain.
Claims (5)
1. a circulating oleum Cunninghamiae lanceolatae production unit, it is characterized in that: comprise steam-generating installation, oleum Cunninghamiae lanceolatae extraction element, prolong device, oily-water seperating equipment and oleum Cunninghamiae lanceolatae collection device, the outlet of described steam-generating installation is communicated in the import of described oleum Cunninghamiae lanceolatae extraction element, described oleum Cunninghamiae lanceolatae extraction element outlet is communicated in the import of described prolong device, the outlet of described prolong device is communicated in the import of described oily-water seperating equipment, described oily-water seperating equipment is provided with two outlets, one is communicated in described steam-generating installation, another is communicated in described oleum Cunninghamiae lanceolatae collection device, described oleum Cunninghamiae lanceolatae extraction element comprises at least one oleum Cunninghamiae lanceolatae extractor, described oleum Cunninghamiae lanceolatae extractor comprises the external chuck that extracts pot and be coated on this extraction outer wall of wall, described external chuck is enclosed to form an accommodation space jointly with extraction outer wall of wall, the described pot that extracts comprises by bottom centre position and extending axially to the main dispersion steam pipe at top and complex root by the aid dispersion vapour pipe that extracts pot sidewall and tiltedly extend downward described main dispersion steam pipe, one end of every aid dispersion vapour pipe is all communicated in described accommodation space, and the other end converges and is communicated on described main dispersion steam pipe, the bottom of described main dispersion steam pipe offers breather hole.
2. circulating oleum Cunninghamiae lanceolatae production unit as claimed in claim 1, it is characterized in that: described oleum Cunninghamiae lanceolatae extraction element includes two oleum Cunninghamiae lanceolatae extractors, be respectively the first oleum Cunninghamiae lanceolatae extractor and the second oleum Cunninghamiae lanceolatae extractor, wherein the described external chuck of the first oleum Cunninghamiae lanceolatae extractor is enclosed to form one first accommodation space jointly with extracting outer wall of wall, in the extraction pot of the first oleum Cunninghamiae lanceolatae extractor, the second accommodation space is set; The described external chuck of the second oleum Cunninghamiae lanceolatae extractor is enclosed to form one the 3rd accommodation space jointly with extraction outer wall of wall, the 4th accommodation space is set in the extraction pot of the second oleum Cunninghamiae lanceolatae extractor, described the first accommodation space and the 3rd accommodation space are connected, the outlet of described the second accommodation space is communicated in described the 4th accommodation space, the import of described the 3rd accommodation space is communicated in the outlet of described steam-generating installation, and the outlet of described the 4th accommodation space is communicated in the import of described prolong device.
3. circulating oleum Cunninghamiae lanceolatae production unit as claimed in claim 2, it is characterized in that: the equal unilaterally connected in entrance one end of every aid dispersion vapour pipe is in described the first/three accommodation space, and described main dispersion steam pipe is all converged and is communicated in the outlet of each aid dispersion vapour pipe.
4. circulating oleum Cunninghamiae lanceolatae production unit as claimed in claim 3, is characterized in that: the outlet of described the second accommodation space is gone back unilaterally connected in the below of the breather hole of the bottom of the described main dispersion steam pipe of the second oleum Cunninghamiae lanceolatae extractor.
5. circulating oleum Cunninghamiae lanceolatae production unit as claimed in claim 4, it is characterized in that: described complex root aid dispersion vapour pipe is at least one row and arranges, aid dispersion vapour pipe on every row is consistent with the junction height of described main dispersion steam pipe, aid dispersion vapour pipe on same every row is also consistent with the junction height of described extraction pot sidewall, and every row's aid dispersion vapour pipe integral body is radial arrangement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420292818.0U CN203866274U (en) | 2014-06-04 | 2014-06-04 | Circulating cedar oil production equipment |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420292818.0U CN203866274U (en) | 2014-06-04 | 2014-06-04 | Circulating cedar oil production equipment |
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| CN203866274U true CN203866274U (en) | 2014-10-08 |
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| CN201420292818.0U Withdrawn - After Issue CN203866274U (en) | 2014-06-04 | 2014-06-04 | Circulating cedar oil production equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103966028A (en) * | 2014-06-04 | 2014-08-06 | 罗成木 | Circulating sanmon oil production equipment and process for preparing sanmon oil |
-
2014
- 2014-06-04 CN CN201420292818.0U patent/CN203866274U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103966028A (en) * | 2014-06-04 | 2014-08-06 | 罗成木 | Circulating sanmon oil production equipment and process for preparing sanmon oil |
| CN103966028B (en) * | 2014-06-04 | 2016-01-27 | 将乐县新利达生物科技有限公司 | The manufacture craft of a kind of circulating san-mou oil production equipment and san-mou oil |
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| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: JIANGLE COUNTY XINLIDA BIOTECHNOLOGY LIMITED CO., Free format text: FORMER OWNER: LUO CHENGMU Effective date: 20150327 |
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| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 366000 SANMING, FUJIAN PROVINCE TO: 353304 SANMING, FUJIAN PROVINCE |
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| TR01 | Transfer of patent right |
Effective date of registration: 20150327 Address after: 353304 Sanming City county will be Fujian Province South Xiang Fu Linggan Industrial Zone Patentee after: Jiangle Xinlida Biotechnology Co., Ltd. Address before: Sanming City 366000 Fujian city of Yongan province Nanpu Yan Village No. 32 Patentee before: Luo Chengmu |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20141008 Effective date of abandoning: 20160127 |
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| C25 | Abandonment of patent right or utility model to avoid double patenting |