CN104946396A - Method for preparing aquilaria essential oil - Google Patents
Method for preparing aquilaria essential oil Download PDFInfo
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- CN104946396A CN104946396A CN201510300459.8A CN201510300459A CN104946396A CN 104946396 A CN104946396 A CN 104946396A CN 201510300459 A CN201510300459 A CN 201510300459A CN 104946396 A CN104946396 A CN 104946396A
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- distillation tower
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Abstract
The invention discloses a method for preparing the aquilaria essential oil, and belongs to the technical field of manufacturing and extracting essential oils, which comprises a steam distillation column and a vacuum control distillation column. The feed port of the steam distillation column is connected with crushed agarwood and water. The reaction discharging port of the steam distillation column is connected with an oil-water separator. The distilled water and the distilled oil are separated. The distilled water is circularly fed into the steam distillation column and the distilled oil is fed into the vacuum control distillation column. The distillation column of the vacuum control distillation column is placed in a heating jacket and two pipes are led out of the pylon of the column, wherein the lower pipe serves as an essential oil outflow pipe and the upper pipe serves as a vacuum control pipe. A set of condensers is arranged between the ports of the two pipes. The vacuum control pipe is provided with a vacuum valve and the end portion thereof is connected with a vacuum device. A condenser is arranged in the essential oil outflow pipe. According to the invention, the vacuum distillation technology is combined with the vapor distillation technology, so that the refined aquilaria essential oil can be extracted. The extraction time is greatly shortened and the thermal stability of the extraction process is ensured. The components of the essential oil are less susceptible to damage and volatile loss, and the flowability of the aquilaria essential oil is improved. Meanwhile, the product quality of the aquilaria essential oil is improved.
Description
Technical field
The present invention relates to acetals spices manufacture technology field, be specially a kind of agilawood essential oil preparation method.
Background technology
Agalloch eaglewood has causing resuscitation with aromatic drugs, pain relieving, the meridian dredging, calms the nerves, relieving convulsion, convergence is dispeled the wind, good effect is had to calm, the adjustment of nervus centralis, in traditional Chinese medical science drug effect, it is the purging medicine of fragrant strengthening the spleen and stomach, controlling the circulation of vital energy in the wrong direction breathes heavily effective in especially retention of urine, nervous vomiting, stomachache, dysthymic uncomfortable in chest, stomach colic, liver depression is not relaxed, stenocardia etc. is all effective.
Most of agalloch eaglewood almost can't smell fragrance under normal conditions, then give off a strong fragrance when smouldering, other smell can be covered, and fragrance remaining time is very long, be the high-grade spices manufacturing volatile oil and natural perfumes, agalloch eaglewood is higher containing the amount of volatile oil, has strong fragrance, be the main component of agalloch eaglewood volatility drug effect, its amount containing volatile oil is directly relevant to the quality of medicinal material.
Steam distillation method is the common method extracting agalloch eaglewood ethereal oil at present, and not only the time is long, and in leaching process, easily cause destruction and the volatilization loss of thermally labile and oxidizable composition, has destruction to fractions.
Vacuum environment can reduce the boiling point of liquid, is more easily separated compatible substances.
Summary of the invention
The technical problem that the present invention mainly solves is to provide a kind of agilawood essential oil preparation method, vacuum distilling control techniques and steam distillation method combine by it, refinement agilawood essential oil can be refined, not only substantially reduce extraction time, and leaching process is thermally-stabilised, make the survivable and volatilization loss of derived essential oil, improve the mobility of agilawood essential oil, improve the quality of agilawood essential oil finished product.
Technical solution problem of the present invention adopts following technical scheme:
A kind of agilawood essential oil preparation method is provided, it comprises vapor distillation tower and vacuum control distillation tower, it is characterized in that: described vapor distillation tower opening for feed is connected to pulverizes agalloch eaglewood and water, reaction discharge port is connected to water-and-oil separator, water-and-oil separator isolates distilled water and distilled oil, in water needed for distilled water circulation access vapor distillation tower, vacuum control distillation tower described in distilled oil access, described vacuum control distillation tower, its distillation tower is placed in heating jacket, the king-post of distillation tower draws two pipelines, what be positioned at lower end is essential oil outlet pipe, what be positioned at upper end is vacuum control pipe, one group of condenser is installed between two pipeline opening, described vacuum control pipe is provided with vacuum valve, end connects vacuum unit, in described essential oil outflow conduit, one group of condenser is installed.
As preferred embodiment, do not have water in the distillation tower of described vacuum control distillation tower, described distilled oil directly accesses in distillation tower.
As preferred embodiment, described vapor distillation tower carries out steam distillation when having an output distilled oil, the vacuum valve of immediate unlock vacuum control distillation tower, and starts to heat to heating jacket.
The present invention is compared with existing, its beneficial effect is: vacuum distilling control techniques and steam distillation method combine, refinement agilawood essential oil can be refined, not only substantially reduce extraction time, and leaching process is thermally-stabilised, make the survivable and volatilization loss of derived essential oil, improve the mobility of agilawood essential oil, improve the quality of agilawood essential oil finished product.
Accompanying drawing explanation
Fig. 1 is the schematic flow sheet of a kind of agilawood essential oil preparation method of the present invention.
Embodiment
Structural representation below in conjunction with a specific embodiment of the present invention is specifically described the present invention.
A kind of agilawood essential oil preparation method, it comprises vapor distillation tower and vacuum control distillation tower, it is characterized in that: described vapor distillation tower opening for feed is connected to pulverizes agalloch eaglewood and water, reaction discharge port is connected to water-and-oil separator, water-and-oil separator isolates distilled water and distilled oil, in water needed for distilled water circulation access vapor distillation tower, vacuum control distillation tower described in distilled oil access, described vacuum control distillation tower, its distillation tower is placed in heating jacket, the king-post of distillation tower draws two pipelines, what be positioned at lower end is essential oil outlet pipe, what be positioned at upper end is vacuum control pipe, one group of condenser is installed between two pipeline opening, described vacuum control pipe is provided with vacuum valve, end connects vacuum unit, in described essential oil outflow conduit, one group of condenser is installed.
Do not have water in the distillation tower of vacuum control distillation tower, distilled oil directly accesses in distillation tower.
Vapor distillation tower carries out steam distillation when having an output distilled oil, the vacuum valve of immediate unlock vacuum control distillation tower, and starts to heat to heating jacket.
During preparation agilawood essential oil, first vapor distillation tower is opened, pulverizing agalloch eaglewood and water add, the product generated through steam distillation carries out being separated into distilled water and distilled oil through water-and-oil separator, in distilled water circulation access steam distillation water, open the vacuum valve of vacuum control distillation tower and start to carry out heating jacket heating, distilled oil flows in the distillation tower of vacuum control distillation tower, through the heating of heating jacket, start to carry out magazins' layout, refining essential oil is flowed out by essential oil outflow conduit, and flowed out by essential oil outlet after condenser cooling, thus obtained required refining agilawood essential oil.
More than show and describe ultimate principle of the present invention, principal character and advantage of the present invention.The technician of the industry should understand; the present invention is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications, and these changes and improvements all fall in the claimed scope of the invention.Application claims protection domain is defined by appending claims and equivalent thereof.
Claims (3)
1. an agilawood essential oil preparation method, it comprises vapor distillation tower and vacuum control distillation tower, it is characterized in that: described vapor distillation tower opening for feed is connected to pulverizes agalloch eaglewood and water, reaction discharge port is connected to water-and-oil separator, water-and-oil separator isolates distilled water and distilled oil, in water needed for distilled water circulation access vapor distillation tower, vacuum control distillation tower described in distilled oil access, described vacuum control distillation tower, its distillation tower is placed in heating jacket, the king-post of distillation tower draws two pipelines, what be positioned at lower end is essential oil outlet pipe, what be positioned at upper end is vacuum control pipe, one group of condenser is installed between two pipeline opening, described vacuum control pipe is provided with vacuum valve, end connects vacuum unit, in described essential oil outflow conduit, one group of condenser is installed.
2. a kind of agilawood essential oil preparation method according to claim 1, is characterized in that: do not have water in the distillation tower of described vacuum control distillation tower, described distilled oil directly accesses in distillation tower.
3. a kind of agilawood essential oil preparation method according to claim 1, is characterized in that: described vapor distillation tower carries out steam distillation when having an output distilled oil, the vacuum valve of immediate unlock vacuum control distillation tower, and starts to heat to heating jacket.
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Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105733813A (en) * | 2016-04-07 | 2016-07-06 | 广西贵港市宏利生物能源科技有限公司 | Distillation production method and device of agilawood essential oil |
CN107057857A (en) * | 2017-03-29 | 2017-08-18 | 刘文龙 | Agilawood essential oil equipment and process are extracted in a kind of efficiently distillation |
CN107525356A (en) * | 2017-08-11 | 2017-12-29 | 中南林业科技大学 | The steam drying of camphorwood vaporization water and essential oil and waste-heat recovery device and application method |
CN107760443A (en) * | 2017-10-13 | 2018-03-06 | 广东贡品沉香产业投资有限公司 | A kind of agilawood essential oil vacuum fractionation method |
CN112137925A (en) * | 2020-09-01 | 2020-12-29 | 梁勇 | Preparation method of agilawood distilled water |
CN112159722A (en) * | 2020-09-01 | 2021-01-01 | 梁勇 | Preparation method of agilawood essential oil |
CN112795430A (en) * | 2020-12-25 | 2021-05-14 | 海南黎药堂生物科技开发有限公司 | Extraction method for extracting Kyara agilawood essential oil |
CN114276868A (en) * | 2021-12-21 | 2022-04-05 | 广西壮族自治区亚热带作物研究所(广西亚热带农产品加工研究所) | Aquilaria agallocha essential oil refining device |
CN114307218A (en) * | 2022-01-05 | 2022-04-12 | 吉安市中香天然植物有限公司 | Continuous rectification production control system for spices |
CN115251448A (en) * | 2022-08-22 | 2022-11-01 | 江西中烟工业有限责任公司 | Efficient tobacco essential oil extraction equipment and method thereof |
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Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105733813A (en) * | 2016-04-07 | 2016-07-06 | 广西贵港市宏利生物能源科技有限公司 | Distillation production method and device of agilawood essential oil |
CN107057857A (en) * | 2017-03-29 | 2017-08-18 | 刘文龙 | Agilawood essential oil equipment and process are extracted in a kind of efficiently distillation |
CN107525356A (en) * | 2017-08-11 | 2017-12-29 | 中南林业科技大学 | The steam drying of camphorwood vaporization water and essential oil and waste-heat recovery device and application method |
CN107760443A (en) * | 2017-10-13 | 2018-03-06 | 广东贡品沉香产业投资有限公司 | A kind of agilawood essential oil vacuum fractionation method |
CN112137925A (en) * | 2020-09-01 | 2020-12-29 | 梁勇 | Preparation method of agilawood distilled water |
CN112159722A (en) * | 2020-09-01 | 2021-01-01 | 梁勇 | Preparation method of agilawood essential oil |
CN112795430A (en) * | 2020-12-25 | 2021-05-14 | 海南黎药堂生物科技开发有限公司 | Extraction method for extracting Kyara agilawood essential oil |
CN114276868A (en) * | 2021-12-21 | 2022-04-05 | 广西壮族自治区亚热带作物研究所(广西亚热带农产品加工研究所) | Aquilaria agallocha essential oil refining device |
CN114307218A (en) * | 2022-01-05 | 2022-04-12 | 吉安市中香天然植物有限公司 | Continuous rectification production control system for spices |
CN115251448A (en) * | 2022-08-22 | 2022-11-01 | 江西中烟工业有限责任公司 | Efficient tobacco essential oil extraction equipment and method thereof |
CN115251448B (en) * | 2022-08-22 | 2023-06-16 | 江西中烟工业有限责任公司 | Efficient tobacco essential oil extraction equipment and method thereof |
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