SU97080A1 - The method of converting citral to nerol - Google Patents
The method of converting citral to nerolInfo
- Publication number
- SU97080A1 SU97080A1 SU446778A SU446778A SU97080A1 SU 97080 A1 SU97080 A1 SU 97080A1 SU 446778 A SU446778 A SU 446778A SU 446778 A SU446778 A SU 446778A SU 97080 A1 SU97080 A1 SU 97080A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- citral
- nerol
- converting
- atm
- carried out
- Prior art date
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Обычно нерол-душистое вещество получают из масла гелихризум. Известен также способ получени его синтетическим путем из цитрал и нерал .Typically, a non-fragrant substance is obtained from helihrizum oil. There is also known a method for preparing it synthetically from citral and nonral.
Предметом изобретени вл етс способ перевода цитрал в нерол, при котором получают нерол с высокими выходами.The subject of the invention is a method for converting citral to nerol, in which nerol is obtained in high yields.
Особенность способа состоит в том, что гидрирование цитрал ведут под давлением .100-200 атм и при температу|зе 100-150° в присутствии медного ката.чнзатора, осажденного на носителе. Гид1)1фование может пропзводитьс в растворителе или без него.The peculiarity of this method is that the hydrogenation of citral is carried out under a pressure of .100-200 atm and at a temperature of 100-150 ° in the presence of a copper cathode deposited on the carrier. Hydro1) 1funding can be carried out in or without solvent.
Пример. 1000 г цитра.т гидрируютс в автоклаве в присхтсим-шExample. 1000 g of citra.t are hydrogenated in an autoclave in drying
50 г катализатора под давлением 100-200 атм и те.мпературе 100 150 до пог.тои1,ени иеобходимого ко.тичества водорода.50 g of catalyst at a pressure of 100–200 atm and a temperature of 100–150, up to 1 hour, of the required amount of hydrogen.
После отделени катализатора и nepeiOHKH в вакууме получают 980 г продукта, содержап1его около 90% перо.та и ЮА гераниол.а п Ц1ггро1ге ,1,тола.After separation of the catalyst and nepeiOHKH in vacuo, 980 g of product are obtained, containing about 90% of the pen. And SOA geraniol.
П р е д мет и з о б р е т е п и P p d e d m i s o b r e p e
Способ перевода цитрал в неро .т, о Т.1 и ч а ю III и и с тем. что, с ue.ibio 1 збирательного гидрировани , гидрирование ведут под давлением 100-200 атм и при температуре 100-150 в присутствиил едиого катализатора.The method of converting citral to nero. T, o T.1 and h III III and and so. that, with ue.ibio 1 selective hydrogenation, hydrogenation is carried out under a pressure of 100–200 atm and at a temperature of 100–150 in the presence of a single catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU446778A SU97080A1 (en) | 1953-04-27 | 1953-04-27 | The method of converting citral to nerol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU446778A SU97080A1 (en) | 1953-04-27 | 1953-04-27 | The method of converting citral to nerol |
Publications (1)
Publication Number | Publication Date |
---|---|
SU97080A1 true SU97080A1 (en) | 1953-11-30 |
Family
ID=48948970
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU446778A SU97080A1 (en) | 1953-04-27 | 1953-04-27 | The method of converting citral to nerol |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU97080A1 (en) |
-
1953
- 1953-04-27 SU SU446778A patent/SU97080A1/en active
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