Oxidation process in fluidised bed reactor
View Patent ↗A process for reacting in a fluid bed reactor at least one oxidisable reactant with molecular oxygen in the presence of a catalytically active fluidised bed of solid particles. In the process a molecular oxygen-containing gas having an oxygen concentration greater than that of air is introduced into the fluidised bed whilst the fluidised bed is maintained in a turbulent regime. The process is suitable for oxidation, ammoxidation and carboxylation processes, including the production of maleic anhydride, acrylonitrile, ethylene, acetic acid and vinyl acetate.
1. A process for reacting in a fluid bed reactor, at least one oxidisable hydrocarbon reactant which is not ethane or ethylene or propylene with molecular oxygen in the presence of a catalytically active fluidised bed of solid particles, which process comprises introducing a molecular oxygen-containing gas having an oxygen concentration greater than that of air into said fluidised bed whilst said fluidised bed is maintained in a turbulent regime, wherein the turbulent regime has the ratio of transition velocity (U k ):terminal velocity (U t ) in the range 0.1:1 to 25:1.
2. A process according to claim 1 wherein the hydrocarbon is a C 4 hydrocarbon and the C 4 hydrocarbon is reacted with molecular oxygen to produce maleic anhydride.
3. A process according to claim 1 wherein the hydrocarbon is reacted with molecular oxygen and ammonia.
4. A process according to claim 3 wherein the hydrocarbon is propane, and the hydrocarbon is reacted with molecular oxygen and ammonia to produce acrylonitrile.
5. A process according to claim 1 wherein the solid particles have a particle diameter in the range 20 to 300 microns.
6. A process according to claim 3 wherein the particle diameter size distribution is at least 20 microns.
7. A process according to claim 1 wherein the fluidised bed comprises solid particles having sizes according to one or more of the following independent criteria: (i) at least 65% of the particles have particle diameters in the range 20-120 microns; (ii) less than 15% of the particles have a particle diameter less than 45 microns; and (iii) less than 5% of the particles have a particle diameter greater than 105 microns.
8. A process according to claim 1 wherein the concentration of oxygen in the molecular oxygen-containing gas is in the range 50 to 100% by volume.
9. A process according to claim 1 wherein the at least one oxidisable reactant is introduced into the fluidised bed as a gas and/or liquid through one or more inlets.
10. A process according to claim 9 wherein the at least one oxidisable reactant is introduced into the fluidised bed as a gas and is a component of the fluidising gas.
11. A process according to claim 1 wherein the fluidised bed has a particle density of at least 0.6 g/cm 3 .
12. A process according to claim 1 wherein the fluidised bed has a settled bed density of at least 0.4 g/cm 3 .
13. A process according to claim 1 wherein the solid particles comprise a support.
14. A process according to claim 13 wherein the support is selected from the group consisting of silica, alumina, silica/alumina, titania, silica/titania, zirconia and mixtures thereof.
15. A process according to claim 1 wherein the particle density of the solid particles is modified by the use of a densifier during the preparation of the particles.
16. A process according to claim 15 wherein the densifier is used during preparation of the support.
17. A process according to claim 16 wherein the densifier is an inert oxide.
18. A process according to claim 17 wherein the inert oxide is tin oxide.
19. A process according to claim 16 wherein the particle density is modified by substitution of at least one metal of the solid particles by at least one metal having a higher atomic weight.
20. A process according to claim 19 wherein the at least one substituting metal is chemically equivalent to the at least one substituted metal.
21. A process according to claim 20 wherein the solid particles comprise at least one of Mo, V and Nb, and the particle density of the particles is modified by substituting at least one of Mo, V, Nb by at least one of Sn, Te, La, Ta, W, Re, Pb, Bi, Ce, Pr, Gd and Yb.
22. A process according to claim 1 wherein the particle density of the solid particles is modified by the use of a fluidising gas.