Process for the production of cyclohexanone oxime
View Patent ↗The invention relates to a process for the production of cyclohexanone oxime in which a phosphate-containing aqueous reaction medium is cycled from a hydroxylammonium synthesis zone to a cyclohexanone oxime synthesis zone and back to the hydroxylammonium synthesis zone, in which hydroxylammonium synthesis zone hydroxylammonium is formed by catalytic reduction of nitrate with hydrogen, and in which cyclohexanone oxime synthesis zone hydroxylammonium is reacted with cyclohexanone to form cyclohexanone oxime, where the concentration hydroxylammonium in the aqueous reaction medium entering the cyclohexanone oxime synthesis zone is higher than 1.0 mol/l.
1. Process for the production of cyclohexanone oxime in which a phosphate-containing aqueous reaction medium is cycled from a hydroxylammonium synthesis zone to a cyclohexanone oxime synthesis zone and back to the hydroxylammonium synthesis zone, in which hydroxylammonium synthesis zone hydroxylammonium is formed by catalytic reduction of nitrate with hydrogen, and in which cyclohexanone oxime synthesis zone hydroxylammonium is reacted with cyclohexanone in the presence of an organic solvent to form cyclohexanone oxime, characterized in that the concentration hydroxylammonium in the aqueous reaction medium entering the cyclohexanone oxime synthesis zone is higher than 1.0 mol/l.
2. Process according to claim 1 , wherein the concentration hydroxylammonium in the aqueous reaction medium entering the cyclohexanone oxime synthesis zone is higher than 1.2 mol/l.
3. Process according to claim 1 , wherein the concentration hydroxylammonium in the aqueous reaction medium entering the cyclohexanone oxime synthesis zone is higher than 1.4 mol/l.
4. Process according to claim 1 , wherein the concentration hydroxylammonium in the aqueous reaction medium entering the cyclohexanone oxime synthesis zone is higher than 1.6 mol/l.
5. Process according to claim 1 , wherein the aqueous reaction medium and a stream comprising the cyclohexanone and the organic solvent are contacted in countercurrent flow.
6. Process according to claim 1 , wherein the organic solvent and cyclohexanone are fed to the cyclohexanone oxime synthesis zone, and an organic medium comprising the organic solvent and the cyclohexanone oxime are withdrawn from the cyclohexanone oxime synthesis zone, the cyclohexanone oxime concentration in the organic medium being higher than 5 wt. %.
7. Process according to claim 6 , wherein the cyclohexanone oxime concentration in the organic medium exiting the cyclohexanone oxime synthesis zone is higher than 25 wt. %.
8. Process according to claim 1 , wherein the organic solvent is selected from the group consisting of benzene, toluene, xylene, cyclohexane, and mixtures thereof.
9. Process according to claim 1 , wherein the concentration hydroxylammonium in the aqueous reaction medium exiting the cyclohexanone oxime synthesis zone is less than 0.1 mol/l.
10. Process according to claim 9 , wherein the concentration hydroxylammonium in the aqueous reaction medium exiting the cyclohexanone oxime synthesis zone is between 0.01 and 0.05 mol/l.