CN1181415A - Euclyptus oil continuous rectificating technique - Google Patents
Euclyptus oil continuous rectificating technique Download PDFInfo
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- CN1181415A CN1181415A CN 96117155 CN96117155A CN1181415A CN 1181415 A CN1181415 A CN 1181415A CN 96117155 CN96117155 CN 96117155 CN 96117155 A CN96117155 A CN 96117155A CN 1181415 A CN1181415 A CN 1181415A
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- eucalyptus
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Abstract
A continuous rectification process for eucalyptus oil includes pre-treating raw eucalyptus oi lby treating agent and continuous rectification through two rectifying towers with integral stainless steel filler corrugated to obtin medicine-grade or perfume-grade eucalyptus oil.
Description
The present invention relates to a kind of volatile oil extracted from eucalyptus' leaves or twigs purification techniques, specifically a kind of with the processing method of thick volatile oil extracted from eucalyptus' leaves or twigs through continuous rectification processed finished products oil.
Volatile oil extracted from eucalyptus' leaves or twigs extracts from eucalyptus leaves, and eucalyptus is an aiphyllium, contains perfume oil in the leaf, and the main component of volatile oil extracted from eucalyptus' leaves or twigs is a cineole 1.8, and it is having been widely used aspect medicine industry and the perfume industry.
In the present prior art, refining volatile oil extracted from eucalyptus' leaves or twigs majority is to adopt the rectifying of Raschig ring packing tower, batch production technology, and 1500 kilograms of still chargings, the processing cycle is 100 hours, throughput is low.The thick volatile oil extracted from eucalyptus' leaves or twigs of raw material is unprocessed, and Raschig ring is bonded to piece because of the throw out that produces in the rectifying, not only influences rectification effect, and cleans very difficulty, and labour intensity is big.
The object of the present invention is to provide a kind of volatile oil extracted from eucalyptus' leaves or twigs quality product that improves, the continuous rectificating technique of enhancing productivity.
The object of the present invention is achieved like this: earlier the thick volatile oil extracted from eucalyptus' leaves or twigs of raw material is carried out pre-treatment, generate sedimentary white mass in the rectifying easily to remove, prevent that these throw outs from stopping up filler, the steps include: the thick volatile oil extracted from eucalyptus' leaves or twigs of raw material is squeezed in the autoclave pressure, and add a certain amount of treatment agent, and as: water vapor, N
2, CO
2Rare gas element.Thick volatile oil extracted from eucalyptus' leaves or twigs is heated to 100～250 ℃, is 2～10kg/cm at pressure
2State kept 1～5 hour down, and cooling then after filtration or sedimentary method, is removed white depositions.
To carry out rectifying by two continuous rectifying towers through pretreated volatile oil extracted from eucalyptus' leaves or twigs.Rectifying tower (I) is for being equipped with the continuous rectifying tower of the whole filler of stainless steel ripple, and decompression is operated down, and reboiler is adopted the thermal siphon natural circulation and risen cineole 1.8 content＜1.0% in film reboiler, the rectifying requirement overhead distillate; Bottom product consists of cineole 1.8 content 〉=58%, and with this raw material as rectifying tower (II).Rectifying tower (II) also is the continuous rectifying tower that the whole filler of stainless steel ripple is housed, operation under reduced pressure, reboiler adopts the pump circulation falling-film evaporator, regulate the operational condition of rectifying tower (II), can obtain pharmaceutical grade or the spices level volatile oil extracted from eucalyptus' leaves or twigs that content is respectively 70% or 80% cineole 1.8 from tower (II) distillate.
The thick volatile oil extracted from eucalyptus' leaves or twigs of raw material that the present invention is used, wherein the quality of cineole 1.8 is 34～40%.
According to the present invention, the technology specific embodiments of above-mentioned continuous rectification is further described.The operational condition of tower (I): inlet amount is 100～200 liters/hour, 80～90 ℃ of cat head service temperatures; The cat head working pressure is-0.01～0～0.015Mpa; 40～70 liters/hour of cat head liquid outlet quantity, cineole 1.8 content＜1.0%, cineole 1.8 content are about 60% in the bottom product, the operational condition of tower (II), inlet amount is 60～120 liters/hour, 80～100 ℃ of cat head service temperatures, and cat head working pressure-0.006～-0.01Mpa, cat head distillates the finished product volatile oil extracted from eucalyptus' leaves or twigs, cineole 1.8 content 70～83%.
The present invention is owing to carried out pre-treatment to the thick volatile oil extracted from eucalyptus' leaves or twigs of raw material, solved and occurred the problem that throw out stops up filler after volatile oil extracted from eucalyptus' leaves or twigs is heated, because production technique is simple and easy, operational condition is looser, mass transfer effect is good during operation, and the material treatment capacity is big, conserve energy, thereby the cost of product is low, the quality homogeneous, the yield rate height.
The specific embodiments of the invention reaction conditions sees Table 1.
Table 1 embodiment reaction conditions
| Tower is other | Pressure Mpa | Temperature ℃ | The inlet amount liter/hour |
| ???(I) | Cat head tower still-0.013-0.0155 | Cat head tower still 84 115.5 | ???????185 |
| ??(II) | Cat head tower still-0.0087-0.0125 | Cat head tower still 95 114 | ????????90 |
| Tower is other | The liquid outlet quantity liter/hour | Cineole 1.8 content % | |
| ???(I) | Cat head tower still 55 125 | Cat head tower still 0.1 59 | |
| ??(II) | Cat head tower still 50 40 | Cat head 80.80 |
Claims (5)
1. one kind is applicable to the Euclyptus oil continuous rectificating technique of processing thick volatile oil extracted from eucalyptus' leaves or twigs, it is characterized in that:
(1) earlier the thick volatile oil extracted from eucalyptus' leaves or twigs of raw material is carried out pre-treatment, the steps include:
A. the thick volatile oil extracted from eucalyptus' leaves or twigs of raw material is squeezed in the autoclave pressure, and added a certain amount of treatment agent, as water vapor, N
2, CO
2Rare gas element;
B. thick volatile oil extracted from eucalyptus' leaves or twigs is heated to 100～250 ℃, pressure is 2～10kg/cm
2Under the state, kept 1～5 hour, then the cooling, after filtration or the precipitation, remove white depositions;
(2) will by tower (I) and two continuous rectifying towers of tower (II) of the whole filler of stainless steel ripple are housed, carry out rectifying through pretreated volatile oil extracted from eucalyptus' leaves or twigs.
2. continuous rectificating technique according to claim 1, it is characterized in that: rectifying tower (I) inlet amount is 100～200 liters/hour, the cat head service temperature is 80～90 ℃, the cat head working pressure is-0.01～-0.015MPa, the cat head liquid outlet quantity is 40～70 liters/hour, and bottom product consists of cineole 1.8 content 〉=58%.
3. continuous rectificating technique according to claim 1, it is characterized in that: rectifying tower (I) bottom product is as the raw material of rectifying tower (II), its inlet amount is 60～120 liters/hour, the cat head service temperature is 80～100 ℃, the cat head working pressure is-0.006～-0.01MPa, cat head distillates the finished product volatile oil extracted from eucalyptus' leaves or twigs; Cineole 1.8 content are 70～83%.
4. continuous rectificating technique according to claim 1 is characterized in that: the rectifying tower (I) at decompression operation adopts the thermal siphon natural circulation to rise the film reboiler, and rectifying tower (II) reboiler adopts the pump circulation falling-film evaporator.
5. continuous rectificating technique according to claim 1 is characterized in that: the thick volatile oil extracted from eucalyptus' leaves or twigs of used raw material, wherein cineole 1.8 content are 34～40%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96117155 CN1181415A (en) | 1996-11-04 | 1996-11-04 | Euclyptus oil continuous rectificating technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 96117155 CN1181415A (en) | 1996-11-04 | 1996-11-04 | Euclyptus oil continuous rectificating technique |
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| Publication Number | Publication Date |
|---|---|
| CN1181415A true CN1181415A (en) | 1998-05-13 |
Family
ID=5124090
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 96117155 Pending CN1181415A (en) | 1996-11-04 | 1996-11-04 | Euclyptus oil continuous rectificating technique |
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| CN (1) | CN1181415A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101899361A (en) * | 2010-08-04 | 2010-12-01 | 厦门百度科技开发有限公司 | Single-tower continuous rectification method of eucalyptus oil |
| CN102604735A (en) * | 2012-03-12 | 2012-07-25 | 国家***桉树研究开发中心 | Method for extracting unsaturated fatty acids from eucalyptus leaves |
| CN106554360A (en) * | 2016-11-21 | 2017-04-05 | 四川省林业科学研究院 | A kind of method of 1,8 Cineoles in purification yusho oil |
| CN106800496A (en) * | 2016-12-07 | 2017-06-06 | 广西灏源盛世生物科技有限公司 | It is a kind of to be continuously separated 1,8 cineoles and the dilute method of α pinanes in eucalyptus oil |
| CN108586199A (en) * | 2018-06-05 | 2018-09-28 | 云南国润香料制造有限公司 | The method of extraction separation terpinol from eucalyptus volatile oil |
| CN108864126A (en) * | 2018-06-05 | 2018-11-23 | 云南国润香料制造有限公司 | A kind of method of eucalyptus oil series classification rectifying |
| CN109293671A (en) * | 2018-09-04 | 2019-02-01 | 中粮德信行健康产业有限公司 | A kind of purification process of Cineole |
| USD862107S1 (en) | 2016-12-08 | 2019-10-08 | Hankscraft, Inc. | Dispenser cover |
-
1996
- 1996-11-04 CN CN 96117155 patent/CN1181415A/en active Pending
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101899361A (en) * | 2010-08-04 | 2010-12-01 | 厦门百度科技开发有限公司 | Single-tower continuous rectification method of eucalyptus oil |
| CN101899361B (en) * | 2010-08-04 | 2012-07-11 | 福建森美达生物科技有限公司 | Single-tower continuous rectification method of eucalyptus oil |
| CN102604735A (en) * | 2012-03-12 | 2012-07-25 | 国家***桉树研究开发中心 | Method for extracting unsaturated fatty acids from eucalyptus leaves |
| CN106554360A (en) * | 2016-11-21 | 2017-04-05 | 四川省林业科学研究院 | A kind of method of 1,8 Cineoles in purification yusho oil |
| CN106800496A (en) * | 2016-12-07 | 2017-06-06 | 广西灏源盛世生物科技有限公司 | It is a kind of to be continuously separated 1,8 cineoles and the dilute method of α pinanes in eucalyptus oil |
| USD862107S1 (en) | 2016-12-08 | 2019-10-08 | Hankscraft, Inc. | Dispenser cover |
| CN108586199A (en) * | 2018-06-05 | 2018-09-28 | 云南国润香料制造有限公司 | The method of extraction separation terpinol from eucalyptus volatile oil |
| CN108864126A (en) * | 2018-06-05 | 2018-11-23 | 云南国润香料制造有限公司 | A kind of method of eucalyptus oil series classification rectifying |
| CN108864126B (en) * | 2018-06-05 | 2021-06-04 | 云南国润香料制造有限公司 | Method for continuously and hierarchically rectifying eucalyptus oil |
| CN108586199B (en) * | 2018-06-05 | 2021-11-19 | 云南国润香料制造有限公司 | Method for extracting and separating terpineol from eucalyptus volatile oil |
| CN109293671A (en) * | 2018-09-04 | 2019-02-01 | 中粮德信行健康产业有限公司 | A kind of purification process of Cineole |
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