CN103966028B - The manufacture craft of a kind of circulating san-mou oil production equipment and san-mou oil - Google Patents
The manufacture craft of a kind of circulating san-mou oil production equipment and san-mou oil Download PDFInfo
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- CN103966028B CN103966028B CN201410243673.XA CN201410243673A CN103966028B CN 103966028 B CN103966028 B CN 103966028B CN 201410243673 A CN201410243673 A CN 201410243673A CN 103966028 B CN103966028 B CN 103966028B
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Abstract
A kind of circulating san-mou oil production equipment, comprise steam generating device, san-mou oil extraction element, condenser pipe device, oily-water seperating equipment and san-mou oil gathering-device, san-mou oil extraction element comprises san-mou oil extractor, san-mou oil extractor comprises extraction pot and external chuck, external chuck is enclosed to form an accommodation space jointly with extraction outer wall of wall, extract pot and comprise main dispersion steam pipe and complex root aid dispersion steam pipe, one end of every root aid dispersion steam pipe is all communicated in described accommodation space, and the other end converges and is communicated on main dispersion steam pipe, the bottom of described main dispersion steam pipe offers air-vent.The present invention also comprises use the said equipment and prepares the technique of san-mou oil and obtained san-mou oil.The present invention can guarantee the san-mou oil that is attached on steam and external heat source is completely isolated comes, and guarantees that san-mou oil there will not be temperature too high, thus avoids occurring that san-mou oil burns situation, effectively ensure that the quality of san-mou oil.
Description
Technical field
The present invention relates to san-mou oil production field, refer in particular to the manufacture craft of a kind of circulating san-mou oil production equipment and san-mou oil.
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, handling ease, does not stick up and does not split, corrosion resistant insect protected, and wearability is strong, and has aromatic odor, is therefore widely used in the aspects such as building, bridge, vessel, electric pole, furniture.Current Chinese fir root-bark and processing waste are not well utilized, or stay in mountain forest and leave to rot, or are used as the low value-added utilization such as burning, cause the serious waste of resource.
A large amount of data show, containing a large amount of fir essential oils in China fir, and Chinese fir root-bark is the position that in whole Chinese fir, essential oil content is the highest.The main component of fir essential oil is cedar wood alcohol, eneα-cedar, β-cedrene, thujopsene, australene and alpha-terpineol etc., from primary chemical composition and fragrance all closely cedar wood oil, so alternative Cypress ethereal oil can be used for completely for perfume industry.Cedar wood oil has strong woody-musky-ambergris fragrance, is mainly used in cosmetics class cosmetics and the soap classes such as talcum powder, muffin, kermes, is also applicable to and allocates in illusion type essence.Cedar wood oil is one of large essential oil in the world ten, being in great demand of market.Because the growth cycle of cypress is very long, within about 60 years, just can become a useful person, so cause cypress scarcity of resources, thus have a strong impact on the development of China's cedar wood oil industry.China fir has the feature of growth fast, and a large amount of tree root resources stayed after the felling of its trees can be used for the production of fir essential oil, and substitutes cedar wood oil in perfume industry.
By san-mou oil isolated obtain cedrol, cedrene can directly as spices use, also can carry out deep processing synthesis high added value spices.The synthetic perfume of cypress series mainly contains: cedrol methyl ether, vertofix coeur, cedryl acetate, epoxycedrane, cedralone and cypress olefine aldehydr etc., be all widely used in essence and flavoring agent industry.
The extraction of current san-mou oil mainly adopts steam distillation, solvent extraction and cracking process.The fir essential oil fragrance adopting steam method to extract is pure, substantially meet blending requirement, but yield is very low; Comparatively steam is high for the fir essential oil yield of extract by solvents, but needs a large amount of solvents, and subsequent treatment is complicated, there is energy consumption high, the problem of dissolvent residual; It is high that cracking process extracts yield, can obtain the products such as pyrolkigneous liquid, charcoal, wood tar and fuel gas, but empyreumatic oil contains the materials such as a large amount of tar, phenol, aldehyde and ketone, has a strong impact on the quality of san-mou oil simultaneously.Thick empyreumatic oil has to pass through burnt deodorization process of dispelling, and could substantially meet blending requirement.
Although the yield of extraction by steam distillation san-mou oil is come low than solvent extraction method, its cost is comparatively cheap, and without the need to the treatment process of follow-up complexity, thus most domestic producer adopts steam distillation to extract san-mou oil at present.Existing san-mou oil production equipment is generally produce steam by steam generating device, and steam is passed in the retort being stacked with China fir or China fir tree root, by carrying out continuous heating to retort, to allow steam constantly penetrate in China fir or China fir tree root, thus to take away san-mou oil.Existing san-mou oil production equipment is because the direct outer wall in retort is with heating, occur burning with the san-mou oil be attached on steam is easy to because retort inwall local temperature is too high, so not only govern the yield extracting san-mou oil, a large amount of tar or other unfavorable materials can be contained in the san-mou oil extracted, the quality of san-mou oil can be had a strong impact on like this, this just equally also inevitable requirement through dispelling burnt deodorization process, could substantially meet blending requirement.
Summary of the invention
The invention provides the manufacture craft of a kind of circulating san-mou oil production equipment and san-mou oil, its main purpose is the defect that san-mou oil yield is low, product contains a large amount of tar overcoming the existence of existing san-mou oil production equipment.
For solving the problems of the technologies described above, the present invention adopts following technical scheme:
A kind of circulating san-mou oil production equipment, comprise steam generating device, san-mou oil extraction element, condenser pipe device, oily-water seperating equipment and san-mou oil gathering-device, the outlet of described steam generating device is in the import of described san-mou oil extraction element, described san-mou oil extraction element outlet is in the import of described condenser pipe device, the outlet of described condenser pipe device is 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 device, and another is communicated in described san-mou oil gathering-device, described san-mou oil extraction element comprises at least one san-mou oil extractor, described san-mou oil extractor comprises the external chuck extracting 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, described extraction pot comprises and axially extends to the main dispersion steam pipe at top and complex root by the aid dispersion steam pipe extracting pot sidewall and extend to obliquely described main dispersion steam pipe by bottom centre position, one end of every root aid dispersion steam 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 air-vent.
Further, described san-mou oil extraction element includes two san-mou oil extractors, be respectively the first san-mou oil extractor and the second san-mou oil extractor, wherein the described external chuck of the first san-mou oil extractor is enclosed to form one first accommodation space jointly with extraction outer wall of wall, arranges the second accommodation space in the extraction pot of the first san-mou oil extractor; The described external chuck of the second san-mou oil extractor is enclosed to form one the 3rd accommodation space jointly with extraction outer wall of wall, 4th accommodation space is set in the extraction pot of the second san-mou oil extractor, described first accommodation space is connected with the 3rd accommodation space, the outlet of described second accommodation space is in described 4th accommodation space, the inlet communication of described 3rd accommodation space is in the outlet of described steam generating device, and the outlet of described 4th accommodation space is in the import of described condenser pipe device.
Further, the equal unilaterally connected in entrance one end of every root aid dispersion steam pipe is in described first/three accommodation space, and the outlet of each aid dispersion steam pipe is all converged and is communicated in described main dispersion steam pipe.
Further, the outlet of described second accommodation space goes back unilaterally connected in the below of the air-vent of the bottom of the described main dispersion steam pipe of the second san-mou oil extractor.
Further, described complex root aid dispersion steam pipe is that at least one row ground is arranged, aid dispersion steam pipe often on row is consistent with the junction height of described main dispersion steam pipe, aid dispersion steam pipe equally often on row is also consistent with the junction height of described extraction pot sidewall, and often row's aid dispersion steam pipe entirety is radially arranged.
Use above-mentioned circulating san-mou oil production equipment to make a technique for san-mou oil, comprise the following steps:
A, described first san-mou oil extractor and the second san-mou oil extractor are placed in thermal source heat;
B, heat described steam generating device, produce steam by this steam generating device and be passed in described 3rd accommodation space in the second san-mou oil extractor,
C, a steam part in 3rd accommodation space flows in the first accommodation space, another part flows to the aid dispersion steam pipe of the second san-mou oil extractor, steam in the aid dispersion steam pipe of above-mentioned second san-mou oil extractor converges on described main dispersion steam pipe, flow downward and come out by the air-vent of main dispersion steam pipe, upwards flow and be fully combined with the China fir raw material extracting middle part and bottom position in pot, take away the san-mou oil of this China fir raw material, after fully in conjunction with extraction, flow into the import of described condenser pipe device from the outlet at the second san-mou oil extractor top with the steam of san-mou oil,
Steam in d, the first accommodation space all flows to the aid dispersion steam pipe of the first san-mou oil extractor, steam in the aid dispersion steam pipe of above-mentioned first san-mou oil extractor converges on described main dispersion steam pipe, flow downward and come out by the air-vent of main dispersion steam pipe and be fully combined with the China fir raw material extracting middle part and bottom position in pot, taking away the san-mou oil of this China fir raw material; After fully in conjunction with extraction, flow into the bottom of described main dispersion steam pipe with the steam of san-mou oil from the outlet at the first san-mou oil extractor top, then repeat step c, until the import of described condenser pipe device should be flowed into steam of san-mou oil;
E, flow into described condenser pipe device with the steam of san-mou oil import after, cool through described condenser pipe device thus form moisture san-mou oil, then pass into oily-water seperating equipment san-mou oil is separated with water, san-mou oil passes into described san-mou oil gathering-device after being separated, and water passes into described steam generating device after being separated.
Compared to the prior art, the beneficial effect that the present invention produces is:
1, reasonable in design of the present invention, san-mou oil extraction efficiency is high and fir essential oil fragrance is pure, by san-mou oil extractor being arranged to the structure be made up of extraction pot and external chuck, described extraction pot just does not directly carry out contacting with external heat source and heats, but first the steam in accommodation space is heated by external heat source, and then utilize steam to enter into and extract in pot and carry out heat trnasfer, thus the san-mou oil that is attached on steam can be guaranteed and external heat source is completely isolated comes, guarantee that san-mou oil there will not be temperature too high, thus avoid occurring that san-mou oil burns situation, effectively ensure that the quality of san-mou oil.
2, in the present invention, by external chuck entirety is placed in external heat source, make the steam passed into become superheated vapor under the effect of external heat source, use superheated vapor is conducive to the extraction to san-mou oil composition on China fir, and can improve the quality extracting rear san-mou oil.
3, in invention, by arranging the first san-mou oil extractor and the second san-mou oil extractor, and by steam pass into be 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, substantially can stop to be attached to the situation that directly contacting appears in san-mou oil on steam and external heat source like this, adopt two san-mou oil extractor series connection to carry out extraction and can save the energy, the extraction solubility improving san-mou oil and san-mou oil quality, by being also conducive to the san-mou oil oil yield improving Board Lot China fir raw material.
4, in invention, the aqueous phase produced in oily-water seperating equipment directly can be drained in steam generating device and recycle, the whole process of thus inventing production there is no the externally any waste water of discharge, contaminated wastewater can not be caused to environment, also the loss not being separated san-mou oil of part in aqueous phase can be avoided, thus by the production that repeatedly circulates, in invention, the san-mou oil oil yield of Board Lot China fir raw material can effectively be promoted.
5, in the present invention, by arranging described main dispersion steam pipe and aid dispersion steam pipe, the China fir raw material of each position in whole extraction pot can be made can both to act on mutually with steam fully and steam can be kept comparatively stable temperature, steam can be made to be uniformly distributed in extract in pot, and then ensure that san-mou oil extracts stability and the uniformity of product quality.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention.
Fig. 2 is the enlarged diagram at A place in the present invention.
Fig. 3 is the structural representation of the first san-mou oil extractor described in the present invention.
Fig. 4 is the generalized section of Fig. 3 along B-B place.
Detailed description of the invention
With reference to the accompanying drawings the specific embodiment of the present invention is described.
With reference to Fig. 1-Fig. 4.A kind of circulating san-mou oil production equipment, comprise steam generating device 1, san-mou oil extraction element 2, condenser pipe device 3, oily-water seperating equipment 4 and san-mou oil gathering-device 5, the outlet of described steam generating device 1 is in the import of described san-mou oil extraction element 2, described san-mou oil extraction element 2 outlet is in the import of described condenser pipe device 3, the outlet of described condenser pipe device 3 is 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 device 1, another is communicated in described san-mou oil gathering-device 5, described san-mou oil extraction element 2 comprises at least one san-mou oil extractor 20, described san-mou oil extractor 20 comprises the external chuck 22 extracting pot 21 and be coated on this extraction pot 21 outer wall, described external chuck 22 is enclosed to form an accommodation space jointly with extraction pot 21 outer wall, described extraction pot 21 comprises and axially extends to the main dispersion steam pipe 23 at top and complex root by the aid dispersion steam pipe 24 extracting pot 21 sidewall and extend to obliquely described main dispersion steam pipe 23 by bottom centre position, one end of every root aid dispersion steam 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 air-vent.The present embodiment reasonable in design, san-mou oil extraction efficiency is high and fir essential oil fragrance is pure, by san-mou oil extractor 20 being arranged to the structure be made up of extraction pot 21 and external chuck 22, described extraction pot 21 just does not directly carry out contacting with external heat source and heats, but first the steam in accommodation space is heated by external heat source, and then utilize steam to enter into and extract in pot 21 and carry out heat trnasfer, thus the san-mou oil that is attached on steam can be guaranteed and external heat source is completely isolated comes, guarantee that san-mou oil there will not be temperature too high, thus avoid occurring that san-mou oil burns situation, effectively ensure that the quality of san-mou oil.In addition, the present embodiment is by being placed in external heat source by external chuck 22 entirety, make the steam passed into become superheated vapor under the effect of external heat source, use superheated vapor is conducive to the extraction to san-mou oil composition on China fir, and can improve the quality extracting rear san-mou oil.
With reference to Fig. 1-Fig. 4.As the preferred version of the present embodiment, described san-mou oil extraction element 2 includes two san-mou oil extractors 20, be respectively the first san-mou oil extractor 201 and the second san-mou oil extractor 2022, in described external chuck 22 and the extraction pot 21 extracting pot 21 outer wall and be jointly enclosed to form one first accommodation space 251, first san-mou oil extractor 201 of wherein the first san-mou oil extractor 201, the second accommodation space 252 is set; The described external chuck 22 of the second san-mou oil extractor 202 is enclosed to form one the 3rd accommodation space 253 jointly with extraction pot 21 outer wall, 4th accommodation space 254 is set in the extraction pot 21 of the second san-mou oil extractor 202, described first accommodation space 251 is connected with the 3rd accommodation space 253, the outlet of described second accommodation space 252 is in described 4th accommodation space 254, the inlet communication of described 3rd accommodation space 253 is in the outlet of described steam generating device 1, and the outlet of described 4th accommodation space 254 is in the import of described condenser pipe device 3.In the present invention, by arranging the first san-mou oil extractor 201 and the second san-mou oil extractor 202, and by steam pass into be arranged to successively by the 3rd accommodation space 253 to the first accommodation space 251 again to the second accommodation space 252 finally to the mode of the 4th accommodation space 254, substantially can stop to be attached to the situation that directly contacting appears in san-mou oil on steam and external heat source like this, adopt two san-mou oil extractor 20 series connection to carry out extraction and can save the energy, improve extraction solubility and the san-mou oil quality of san-mou oil, by being also conducive to the san-mou oil oil yield improving Board Lot China fir raw material.
With reference to Fig. 1-Fig. 4.The equal unilaterally connected in entrance one end of every root aid dispersion steam pipe 24 is in described first/three accommodation space 253, and the outlet of each aid dispersion steam pipe 24 is all converged and is communicated in described main dispersion steam pipe 23.The outlet of described second accommodation space 252 goes back unilaterally connected on the entrance of the described dispersion steam pipe of the second san-mou oil extractor 202 or the described main dispersion steam pipe 23 of the second san-mou oil extractor 202.Described complex root aid dispersion steam pipe 24 is arranged at least one row ground, aid dispersion steam pipe 24 often on row is consistent with the junction height of described main dispersion steam pipe 23, aid dispersion steam pipe 24 equally often on row is also consistent with the junction height of described extraction pot 21 sidewall, and often row's aid dispersion steam pipe 24 entirety is radially arranged.In the present embodiment, by arranging described main dispersion steam pipe 23 and aid dispersion steam pipe 24, the China fir raw material of each position in whole extraction pot 21 can be made can both to act on mutually with steam fully and steam can be kept comparatively stable temperature, steam can be made to be uniformly distributed in extract in pot 21, and then ensure that san-mou oil extracts stability and the uniformity of product quality.
With reference to Fig. 1-Fig. 4.Use above-mentioned circulating san-mou oil production equipment to make the technique of san-mou oil in the present invention, comprise the following steps:
The first step: described first san-mou oil extractor 201 and the second san-mou oil extractor 202 are placed in thermal source and heat;
Second step: heat described steam generating device 1, produces steam by this steam generating device 1 and is passed in described 3rd accommodation space 253 in the second san-mou oil extractor 202,
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 steam pipe 24 of the second san-mou oil extractor 202, steam in the aid dispersion steam pipe 24 of above-mentioned second san-mou oil extractor 202 converges on described main dispersion steam pipe 23, flow downward and come out by the air-vent of main dispersion steam pipe 23, upwards spread and be fully combined with the China fir raw material extracting middle part and bottom position in pot 21, take away the san-mou oil of this China fir raw material, after fully in conjunction with extraction, flow into the import of described condenser pipe device 3 from the outlet at the second san-mou oil extractor 202 top with the steam of san-mou oil,
4th step: the steam in the first accommodation space 251 all flows to the aid dispersion steam pipe 24 of the first san-mou oil extractor 201, steam in the aid dispersion steam pipe 24 of above-mentioned first san-mou oil extractor 201 converges on described main dispersion steam pipe 23, flow downward and come out by the air-vent of main dispersion steam pipe 23, upwards diffusion and with extract in the middle part of in pot 21 and the China fir raw material of bottom position is fully combined, take away the san-mou oil of this China fir raw material; After fully in conjunction with extraction, flow into the below of the air-vent of the described main dispersion steam pipe 23 of described first san-mou oil extractor 201 from the outlet at the first san-mou oil extractor 201 top with the steam of san-mou oil, then step c is repeated, until the import of described condenser pipe device 3 should be flowed into the steam of san-mou oil;
5th step: after flowing into the import of described condenser pipe device 3 with the steam of san-mou oil, cool through described condenser pipe device 3 thus form moisture san-mou oil, then pass into oily-water seperating equipment 4 san-mou oil is separated with water, san-mou oil passes into described san-mou oil gathering-device 5 after being separated, and water passes into described steam generating device 1 after being separated.
In sum, in an embodiment, the aqueous phase produced in oily-water seperating equipment 4 directly can be drained in steam generating device and recycle, the whole process of thus inventing production there is no the externally any waste water of discharge, contaminated wastewater can not be caused to environment, also can avoid the loss not being separated san-mou oil of part in aqueous phase, thus by the production that repeatedly circulates, in invention, the san-mou oil oil yield of Board Lot China fir raw material can effectively be promoted.
Above are only the specific embodiment of the present invention, but design concept of the present invention is not limited thereto, all changes utilizing this design the present invention to be carried out to unsubstantiality, all should belong to the behavior of invading scope.
Claims (6)
1. a circulating san-mou oil production equipment, it is characterized in that: comprise steam generating device, san-mou oil extraction element, condenser pipe device, oily-water seperating equipment and san-mou oil gathering-device, the outlet of described steam generating device is in the import of described san-mou oil extraction element, described san-mou oil extraction element outlet is in the import of described condenser pipe device, the outlet of described condenser pipe device is 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 device, another is communicated in described san-mou oil gathering-device, described san-mou oil extraction element comprises at least one san-mou oil extractor, described san-mou oil extractor comprises the external chuck extracting 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, described extraction pot comprises and axially extends to the main dispersion steam pipe at top and complex root by the aid dispersion steam pipe extracting pot sidewall and extend to obliquely described main dispersion steam pipe by bottom centre position, one end of every root aid dispersion steam 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 air-vent.
2. circulating san-mou oil production equipment as claimed in claim 1, it is characterized in that: described san-mou oil extraction element includes two san-mou oil extractors, be respectively the first san-mou oil extractor and the second san-mou oil extractor, wherein the described external chuck of the first san-mou oil extractor is enclosed to form one first accommodation space jointly with extraction outer wall of wall, arranges the second accommodation space in the extraction pot of the first san-mou oil extractor; The described external chuck of the second san-mou oil extractor is enclosed to form one the 3rd accommodation space jointly with extraction outer wall of wall, 4th accommodation space is set in the extraction pot of the second san-mou oil extractor, described first accommodation space is connected with the 3rd accommodation space, the outlet of described second accommodation space is in described 4th accommodation space, the inlet communication of described 3rd accommodation space is in the outlet of described steam generating device, and the outlet of described 4th accommodation space is in the import of described condenser pipe device.
3. circulating san-mou oil production equipment as claimed in claim 2, it is characterized in that: the equal unilaterally connected in entrance one end of every root aid dispersion steam pipe is in described first/three accommodation space, and the outlet of each aid dispersion steam pipe is all converged and is communicated in described main dispersion steam pipe.
4. circulating san-mou oil production equipment as claimed in claim 3, is characterized in that: the outlet of described second accommodation space goes back unilaterally connected in the below of the air-vent of the bottom of the described main dispersion steam pipe of the second san-mou oil extractor.
5. circulating san-mou oil production equipment as claimed in claim 4, it is characterized in that: described complex root aid dispersion steam pipe is that at least one row ground is arranged, aid dispersion steam pipe often on row is consistent with the junction height of described main dispersion steam pipe, aid dispersion steam pipe equally often on row is also consistent with the junction height of described extraction pot sidewall, and often row's aid dispersion steam pipe entirety is radially arranged.
6. use as in claim 2-5, circulating san-mou oil production equipment as described in any one makes a technique for san-mou oil, it is characterized in that, comprise the following steps:
A, described first san-mou oil extractor and the second san-mou oil extractor are placed in thermal source heat;
B, heat described steam generating device, produce steam by this steam generating device and be passed in described 3rd accommodation space in the second san-mou oil extractor,
C, a steam part in 3rd accommodation space flows in the first accommodation space, another part flows to the aid dispersion steam pipe of the second san-mou oil extractor, steam in the aid dispersion steam pipe of above-mentioned second san-mou oil extractor converges on described main dispersion steam pipe, flow downward and come out by the air-vent of main dispersion steam pipe, upwards flow and be fully combined with the China fir raw material extracting middle part and bottom position in pot, take away the san-mou oil of this China fir raw material, after fully in conjunction with extraction, flow into the import of described condenser pipe device from the outlet at the second san-mou oil extractor top with the steam of san-mou oil,
Steam in d, the first accommodation space all flows to the aid dispersion steam pipe of the first san-mou oil extractor, steam in the aid dispersion steam pipe of above-mentioned first san-mou oil extractor converges on described main dispersion steam pipe, flow downward and come out by the air-vent of main dispersion steam pipe and be fully combined with the China fir raw material extracting middle part and bottom position in pot, taking away the san-mou oil of this China fir raw material; After fully in conjunction with extraction, flow into the bottom of described main dispersion steam pipe with the steam of san-mou oil from the outlet at the first san-mou oil extractor top, then repeat step c, until the import of described condenser pipe device should be flowed into steam of san-mou oil;
E, flow into described condenser pipe device with the steam of san-mou oil import after, cool through described condenser pipe device thus form moisture san-mou oil, then pass into oily-water seperating equipment san-mou oil is separated with water, san-mou oil passes into described san-mou oil gathering-device after being separated, and water passes into described steam generating device after being separated.
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| CN1431285A (en) * | 2003-01-23 | 2003-07-23 | 华南师范大学 | Segregator for extracting volatile oils and its usage |
| CN201634657U (en) * | 2009-08-01 | 2010-11-17 | 粟国江 | Sawdust steaming and oil distilling device |
| CN102250689A (en) * | 2011-05-30 | 2011-11-23 | 新疆大学 | Equipment and method for extracting perfume plant essential oil by reduced pressure steam distillation |
| CN203866274U (en) * | 2014-06-04 | 2014-10-08 | 罗成木 | Circulating cedar oil production equipment |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1431285A (en) * | 2003-01-23 | 2003-07-23 | 华南师范大学 | Segregator for extracting volatile oils and its usage |
| CN201634657U (en) * | 2009-08-01 | 2010-11-17 | 粟国江 | Sawdust steaming and oil distilling device |
| CN102250689A (en) * | 2011-05-30 | 2011-11-23 | 新疆大学 | Equipment and method for extracting perfume plant essential oil by reduced pressure steam distillation |
| CN203866274U (en) * | 2014-06-04 | 2014-10-08 | 罗成木 | Circulating cedar oil production equipment |
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