CN104926610A - Preparation method of dihydromyrcenol - Google Patents

Preparation method of dihydromyrcenol Download PDF

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Publication number
CN104926610A
CN104926610A CN201510276832.0A CN201510276832A CN104926610A CN 104926610 A CN104926610 A CN 104926610A CN 201510276832 A CN201510276832 A CN 201510276832A CN 104926610 A CN104926610 A CN 104926610A
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Prior art keywords
parts
dihydromyrcenol
preparation
hours
reactor
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CN201510276832.0A
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CN104926610B (en
Inventor
陈伟强
陈键泉
苏炳连
李战
冯玲
董俊
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GUANGXI WUSONGLIN CHEMICAL GROUP Co Ltd
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GUANGXI WUSONGLIN CHEMICAL GROUP Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/03Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2
    • C07C29/04Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by addition of hydroxy groups to unsaturated carbon-to-carbon bonds, e.g. with the aid of H2O2 by hydration of carbon-to-carbon double bonds

Abstract

The invention discloses a preparation method of dihydromyrcenol, belonging to the technical field of forestry chemical product preparation. The method comprises the following steps: according to a certain ratio, putting 36% of acetic acid and water into a reaction kettle, mixing evenly, and then heating to 80 DEG C to 120 DEG C; adding a catalyst into the reaction kettle, and keeping the material temperature in the kettle within the range of 80 DEG C to 120 DEG C; adding 100 parts of dihydromyrcenol preheated to 80 DEG C to 120 DEG C in advance into the reaction kettle, keeping the material temperature in the kettle within the range of 80 DEG C to 120 DEG C, and performing thermostatic reaction for one hour to 3 hours; performing filtering, standing layering and reduced pressure distillation on a product obtained by the reaction, thus obtaining the dihydromyrcenol. According to the preparation method of the dihydromyrcenol, by adopting the home-made catalyst and matching with the corresponding raw material ratio, the production cycle of the product dihydromyrcenol is shortened, and the yield of the dihydromyrcenol is improved.

Description

The preparation method of dihydromyrcenol
Technical field
The invention belongs to silvichemical preparing technical field, particularly relate to a kind of preparation method of dihydromyrcenol.
Background technology
Dihydromyrcenol, chemical name 2,6-dimethyl-7-octen-2-ol, there is the fresh fragrance of a flower, limette sample fruital, be mainly used in Harmony and the satisfactory stability of fragrances fragrance, the consumption in essence can reach about 20%, is the kind of large usage quantity in turps synthetic perfume.
The indirect hydration method of current industrial conventional dihydromyrcene and formic acid esterification, saponification is produced.There is the shortcoming of low conversion rate, production cycle length in this technique.
Summary of the invention
The invention provides a kind of preparation method of dihydromyrcenol, the method can solve the problem that the existing reparation technology of dihydroterpineol exists low conversion rate, production cycle length.
In order to solve the problems of the technologies described above, the technical solution adopted in the present invention is:
It comprises the following steps:
A, by weight, first 80 parts ~ 90 part 36% acetic acid and 50 parts ~ 60 parts water are put into reactor and mix, be then heated to 80 DEG C ~ 120 DEG C;
B, after step A, in this reactor, add 5 parts ~ 8 parts catalyzer, and to keep in still temperature of charge in the scope of 80 DEG C ~ 120 DEG C;
C, after step B, in this reactor, add the dihydromyrcene that 100 parts are preheated to 80 DEG C ~ 120 DEG C in advance, and to keep in still temperature of charge in the scope of 80 DEG C ~ 120 DEG C, isothermal reaction 1 hour ~ 3 hours;
D, after step C, by be obtained by reacting product filtration, stratification, underpressure distillation, obtained;
Wherein, the preparation method of step B used catalyst is as follows:
20 parts of particle diameters are that 200 order ~ 240 object niobic acids put into 60% nitric acid, normal temperature acidifying 2 hours by A, by weight, and then washing is to neutral;
B, the material obtained after step A process is put into 28% ammoniacal liquor, normal temperature alkalizes 2 hours, and then washing is to neutral;
C, the material obtained after step B process to be mixed with Magnesium Stearate, calcine 3 hours at being then placed in 1200 DEG C, obtained.
In technique scheme, technical scheme is more specifically: 36% acetic acid 85 parts and 60 parts, water, catalyzer 5 parts, dihydromyrcene 100 parts.
Owing to adopting technique scheme, the beneficial effect that the present invention obtains is:
The present invention by adopting homemade catalyzer and coordinating the corresponding proportioning raw materials of the present invention, thus shortens the production cycle of product dihydromyrcenol, improves its yield.
Embodiment
Below in conjunction with specific embodiment, the invention will be further described, and protection scope of the present invention is not only confined to following examples.
Embodiment 1
The preparation method of this dihydromyrcenol comprises the following steps:
A, first 85 part of 36% acetic acid and 60 parts of water are put into reactor and mix, be then heated to 80 DEG C;
B, after step A, in this reactor, add 5 parts of catalyzer, and to keep in still temperature of charge in the scope of 80 DEG C DEG C;
C, after step B, in this reactor, add the dihydromyrcene that 100 parts are preheated to 80 DEG C in advance, and keep temperature of charge in still to be 80 DEG C, isothermal reaction 3 hours;
D, after step C, by be obtained by reacting product filtration, stratification, underpressure distillation, obtained;
Wherein, the preparation method of step B used catalyst is as follows:
A, be that 200 object niobic acids put into 60% nitric acid by 20 parts of particle diameters, normal temperature acidifying 2 hours, then washing is to neutral;
B, the material obtained after step A process is put into 28% ammoniacal liquor, normal temperature alkalizes 2 hours, and then washing is to neutral;
C, the material obtained after step B process to be mixed with Magnesium Stearate, calcine 3 hours at being then placed in 1200 DEG C, obtained.
Relative to the preparation technology of existing dihydromyrcenol, the production cycle of the present embodiment dihydroterpineol shortens 50%, and yield is 99%.
Embodiment 2
The preparation method of this dihydromyrcenol comprises the following steps:
A, first 80 part of 36% acetic acid and 50 parts of water are put into reactor and mix, be then heated to 120 DEG C;
B, after step A, in this reactor, add 8 parts of catalyzer, and to keep in still temperature of charge in the scope of 120 DEG C;
C, after step B, in this reactor, add the dihydromyrcene that 100 parts are preheated to 120 DEG C in advance, and keep temperature of charge in still to be 120 DEG C, isothermal reaction 1 hour;
D, after step C, by be obtained by reacting product filtration, stratification, underpressure distillation, obtained;
Wherein, the preparation method of step B used catalyst is as follows:
A, be that 240 object niobic acids put into 60% nitric acid by 20 parts of particle diameters, normal temperature acidifying 2 hours, then washing is to neutral;
B, the material obtained after step A process is put into 28% ammoniacal liquor, normal temperature alkalizes 2 hours, and then washing is to neutral;
C, the material obtained after step B process to be mixed with Magnesium Stearate, calcine 3 hours at being then placed in 1200 DEG C, obtained.
Relative to the preparation technology of existing dihydromyrcenol, the production cycle of the present embodiment dihydroterpineol shortens 50%, and yield is 99.5%.
Embodiment 3
The preparation method of this dihydromyrcenol comprises the following steps:
A, first 90 part of 36% acetic acid and 55 parts of water are put into reactor and mix, be then heated to 100 DEG C;
B, after step A, in this reactor, add 7 parts of catalyzer, and to keep in still temperature of charge in the scope of 100 DEG C;
C, after step B, in this reactor, add the dihydromyrcene that 100 parts are preheated to 100 DEG C in advance, and keep temperature of charge in still to be 100 DEG C, isothermal reaction 2 hours;
D, after step C, by be obtained by reacting product filtration, stratification, underpressure distillation, obtained;
Wherein, the preparation method of step B used catalyst is as follows:
A, be that 230 object niobic acids put into 60% nitric acid by 20 parts of particle diameters, normal temperature acidifying 2 hours, then washing is to neutral;
B, the material obtained after step A process is put into 28% ammoniacal liquor, normal temperature alkalizes 2 hours, and then washing is to neutral;
C, the material obtained after step B process to be mixed with Magnesium Stearate, calcine 3 hours at being then placed in 1200 DEG C, obtained.
Relative to the preparation technology of existing dihydromyrcenol, the production cycle of the present embodiment dihydroterpineol shortens 50%, and yield is 99.4%.

Claims (2)

1. a preparation method for dihydromyrcenol, is characterized in that:
A, by weight, first 80 parts ~ 90 part 36% acetic acid and 50 parts ~ 60 parts water are put into reactor and mix, be then heated to 80 DEG C ~ 120 DEG C;
B, after step A, in this reactor, add 5 parts ~ 8 parts catalyzer, and to keep in still temperature of charge in the scope of 80 DEG C ~ 120 DEG C;
C, after step B, in this reactor, add the dihydromyrcene that 100 parts are preheated to 80 DEG C ~ 120 DEG C in advance, and to keep in still temperature of charge in the scope of 80 DEG C ~ 120 DEG C, isothermal reaction 1 hour ~ 3 hours;
D, after step C, by be obtained by reacting product filtration, stratification, underpressure distillation, obtained;
Wherein, the preparation method of step B used catalyst is as follows:
20 parts of particle diameters are that 200 order ~ 240 object niobic acids put into 60% nitric acid, normal temperature acidifying 2 hours by A, by weight, and then washing is to neutral;
B, the material obtained after step A process is put into 28% ammoniacal liquor, normal temperature alkalizes 2 hours, and then washing is to neutral;
C, the material obtained after step B process to be mixed with Magnesium Stearate, calcine 3 hours at being then placed in 1200 DEG C, obtained.
2. to go the preparation method of the dihydromyrcenol described in 1 according to right, it is characterized in that: 36% acetic acid 85 parts and 60 parts, water, catalyzer 5 parts, dihydromyrcene 100 parts.
CN201510276832.0A 2015-05-27 2015-05-27 The preparation method of dihydromyrcenol Expired - Fee Related CN104926610B (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106924224A (en) * 2017-03-09 2017-07-07 新乡医学院 A kind of pharmaceutical composition for treating craniocerebral injury caused by mental disorder and its application
US11008271B2 (en) 2016-09-08 2021-05-18 P2 Science, Inc. Methods for the continuous alkoxylation and derivatization of terpenes

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5013910A (en) * 1973-06-08 1975-02-13
US4652544A (en) * 1984-08-21 1987-03-24 Cbmm Internacional Ltda. Solid acid catalyst of acid-treated hydrated niobium oxide and method for its preparation
CN1463960A (en) * 2002-06-12 2003-12-31 中国石油化工股份有限公司 Process for preparing ethandiol by catalyzing epoxyethane hydration
CN101921176A (en) * 2010-08-10 2010-12-22 福州大学 Novel method for producing dihydromyrcenol
WO2012017447A2 (en) * 2010-08-04 2012-02-09 Vijay Kumar Doppalapudi Method for selective hydration of aroma olefins to alcohols in continuous solid catalyst column reactor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5013910A (en) * 1973-06-08 1975-02-13
US4652544A (en) * 1984-08-21 1987-03-24 Cbmm Internacional Ltda. Solid acid catalyst of acid-treated hydrated niobium oxide and method for its preparation
CN1463960A (en) * 2002-06-12 2003-12-31 中国石油化工股份有限公司 Process for preparing ethandiol by catalyzing epoxyethane hydration
WO2012017447A2 (en) * 2010-08-04 2012-02-09 Vijay Kumar Doppalapudi Method for selective hydration of aroma olefins to alcohols in continuous solid catalyst column reactor
CN101921176A (en) * 2010-08-10 2010-12-22 福州大学 Novel method for producing dihydromyrcenol

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
俞忠华等: "二氢月桂烯水合制备二氢月桂烯醇的研究进展", 《江西科学》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11008271B2 (en) 2016-09-08 2021-05-18 P2 Science, Inc. Methods for the continuous alkoxylation and derivatization of terpenes
CN106924224A (en) * 2017-03-09 2017-07-07 新乡医学院 A kind of pharmaceutical composition for treating craniocerebral injury caused by mental disorder and its application

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