Process for the regeneration of a catalyst
Process for the regeneration of an at least partially coked molecular sieve catalyst comprising introducing the at least partially coked catalyst into a regenerator; introducing into the regenerator an oxygen-containing gas to regenerate at least part of the at least partially coked catalyst, thereby producing a gaseous mixture and at least partially regenerated catalyst; separating at least partially regenerated catalyst and at least part of the gaseous mixture; and analyzing the composition of the gaseous mixture to control the burning rate of the coke present on the at least partially coked catalyst in the regenerator by adjusting the mass flow rate of the oxygen-containing gas on the basis of the analysis of the gaseous mixture.
1. Process for the regeneration of an at least partially coked molecular sieve catalyst, which process comprises the steps of:
(a) introducing the at least partially coked catalyst into a regenerator;
(b) introducing into the regenerator an oxygen-containing gas to regenerate at least part of the at least partially coked catalyst by removing between 0.01-5 wt % of the coke present on the at least partially coked catalyst, thereby producing a gaseous mixture and at least partially regenerated catalyst;
(c) separating at least partially regenerated catalyst and at least part of the gaseous mixture as obtained in step (b); and
(d) analysing the composition of the gaseous mixture as obtained in step (b) to control the burning rate of the coke present on the at least partially coked catalyst in the regenerator by adjusting the mass flow rate of the oxygen-containing gas as introduced in step (b) on the basis of the analysis of the gaseous mixture.
2. Process according to claim 1 , wherein the molecular sieve catalyst comprises one or more zeolite catalysts and/or one or more SAPO, ALPO and/or MeALPO catalysts.
3. Process according to claim 1 , wherein the regeneration in step (b) is carried out at a temperature in the range of from 580-800° C. and a pressure in the range of from 1-5 bar(a) (absolute).
4. Process according to claim 1 , wherein in the analysis in step (d) the concentration of carbon monoxide present in the gaseous mixture is determined and the burning rate of the coke present on the at least partially coked catalyst is controlled by adjusting the mass flow rate of the oxygen-containing gas as introduced in step (b) on the basis of the concentration of carbon monoxide present in the analysed gaseous mixture.
5. Process according to claim 1 , wherein in the analysis in step (d) the concentration of oxygen present in the gaseous mixture is determined and the burning rate of the coke present on the at least partially coked catalyst is controlled by adjusting the mass flow rate of the oxygen-containing gas as introduced in step (b) on the basis of the concentration of oxygen present in the analysed gaseous mixture.
6. Process according to claim 1 , wherein the mass flow rate of the oxygen-containing gas as introduced in step (b) is automatically adjusted on the basis of the analysis of the gaseous mixture.
7. Process according to claim 1 , wherein the residence time of the catalyst in the regenerator is in the range of from 1-60 minutes.
8. Process according to claim 1 , wherein the volume of oxygen in the oxygen-containing gas as introduced in step (b) is 15-50 mol-%, based on total volume of the oxygen-containing gas.
9. Process according to claim 1 , wherein the at least partially coked catalyst introduced in step (a) in the regenerator is an at least partially coked molecular sieve catalyst which has been used in an oxygenate-to-olefins process or an olefin cracking process.
10. Process according to claim 9 , wherein at least part of the at least partially regenerated catalyst as obtained in step (c) is recycled to the oxygenate-to-olefins process or the olefin cracking process.