Production of 1,6-hexanediol
The present invention refers to a process for hydrogenation of caprolactone and/or its oligomers or polymers to 1,6-hexanediol. The process is performed in liquid phase at a pressure between 100 and 350 bar and is performed in the presence of a catalytically effective amount of at least one catalyst comprising Cu, Mn, Al, Cr, Zn, Ba and/or Zr.
1. A process for hydrogenation of caprolactone and/or its oligomers or polymers to 1,6-hexanediol characterized in that said process is performed in liquid phase at a pressure between 220 and 310 bar and a temperature between 180-240° C., and that said process is performed in the presence of a catalytically effective amount of at least one catalyst comprising Cu, Mn, Al, Cr, Zn, Ba and/or Zr and in the presence of at least one of the solvents methanol, isobutanol and/or 1,6-hexanediol.
2. A process according to claim 1 , characterised in that said process is performed in a single reactor.
3. A process according to claim 1 , characterised in that said catalyst is present as one or more oxides.
4. A process according to claim 1 , characterised in that said catalyst is present as one or more elemental metals.
5. A process according to claim 1 , characterised in that said catalyst is present as a combination of one or more oxides and one or more elemental metals.
6. A process according to claim 1 , characterised in that said catalyst further comprises a promoter.
7. A process to claim 6 , characterised in that said promoter is MnO 2 , BaO, ZnO, FeO, Fe 2 O 3 , Fe 3 O 4 and/or a mixture thereof.
8. A process according to claim 1 , characterised in that said catalyst is supported on a carrier containing Al 2 O 3 , SiO 2 , TiO 2 , activated carbon, Cr 2 O 3 and/or ZnO and/or CaO.