Process for the treatment of waste water
The invention provides a process for treating waste water from an industrial process for producing propylene oxide, which process comprises subjecting the waste water to a catalytic wet oxidation treatment in the presence of a catalyst comprising metal nanoparticles-doped porous carbon beads.
1. A process for treating waste water from an industrial process for producing propylene oxide, which process comprises subjecting the waste water to a catalytic wet oxidation treatment in the presence of a catalyst comprising metal nanoparticles-doped porous carbon beads, wherein the metal nanoparticles are incorporated within the beads.
2. The process according to claim 1 , wherein the metal is selected from one or more of aluminium, iron, nickel, copper, silver, cobalt, molybdenum, gold and platinum.
3. The process according to claim 1 , wherein the metal is selected from one or more of iron, nickel, copper and cobalt.
4. The process according claim 1 , wherein the catalyst further comprises carbon nanofibers.
5. The process according to claim 1 , wherein the catalyst has been prepared by a method comprising:
(i) preparing a mixture of one or more aromatic alcohol monomers and/or non-aromatic monomers, solvent, polymerization catalyst, crosslinking agent, suspension stabilizing agent and one or more metal salts, under conditions sufficient to produce polymeric beads doped with one or more metals or salts thereof; and
(ii) carbonizing, activating and then reducing the polymeric beads produced in step (i) to produce metal nanoparticles-doped porous carbon beads.
6. The process according to claim 5 , wherein the catalyst has been prepared by a method further comprising:
(iii) subjecting the metal nanoparticles-doped porous carbon beads to chemical vapour deposition in the presence of a carbon source to produce metal nanoparticles-doped porous carbon beads which comprise carbon nanofibers.
7. The process according to claim 6 , wherein the carbon source is selected from acetylene, benzene, xylene and toluene.
8. The process according to claim 5 , wherein the aromatic alcohol monomers and non-aromatic monomers are selected from one or more of phenol, vinyl benzyl alcohol, cresol, butylphenol and methyl methacrylate (MMA).
9. The process according to claim 5 , wherein the suspension stabilising agent is selected from one or more of poly vinyl alcohol (PVA), gum acacia powder (GAP) and poly vinyl pyrodinone.
10. The process according claim 1 , wherein the waste water treatment is carried out at a temperature in the range of from 120 to 300° C. and a pressure in the range of from 2 to 15 MPa.