Regeneration of oxidative dehydrogenation catalyst in a reactor
View Patent ↗Disclosed herein is a process for the regeneration of oxidative dehydrogenation (OXO-D) catalyst in an alternate or separate regeneration reactor by employing controlled steam:air and time/pressure/temperature conditions. The process avoids destruction of the catalyst, and wear/tear on an OXO-D reactor. The regenerated catalyst is an iron based oxide catalyst which can be zinc or zinc-free. The iron based oxide catalyst is regenerated in the regeneration reactor by feeding an air/steam stream over a set amount of time, preferably about 6 days to yield a regenerated OXO-D catalyst. The regenerated catalyst is activated and re-utilized to produce butadienes.
1. A process for regenerating an iron-based spent oxidative dehydrogenation catalyst in a fixed bed reactor, the process comprising:
passing a stream containing steam and air in a controlled fashion, together with an oxygen-containing gaseous mixture having O 2 to HC ratio is in the range of 0.2-1, and the steam to HC ratio is in the range of 10-15 over a spent iron-based oxidative dehydrogenation catalyst containing carbonaceous compounds in the fixed bed reactor; wherein the steam to air ratio is less than 20 moles; and,
heating the carbonaceous compounds deposited on the spent iron-based oxidative dehydrogenation catalyst at a pressure of 0-150 psig and a temperature less than 705° C., (1300° F.), wherein the temperature is maintained substantially constant for a period less than 144 hours (6 days) in the fixed bed reactor, and thereby regenerating the spent iron-based oxidative dehydrogenation catalyst in the fixed bed reactor.
2. The process of claim 1 wherein the O 2 to HC ratio is 0.55 and the steam to HC ratio is 12.
3. The process of claim 1 wherein the steam to air ratio is less than 10 moles.
4. The process of claim 1 wherein the temperature in the range of 340-650° C.
5. The process of claim 1 wherein the reaction temperature is raised by adjusting steam rate at no more than about 10 MT/hour.
6. The process of claim 1 , wherein the iron-based oxidative dehydrogenation catalyst is a composite of iron-based oxide and zinc.
7. The process of claim 4 wherein zinc is monitored while removal of carbonaceous compounds are occurring and the addition of air and steam is controlled to ensure temperatures of about 594° C. (1100° F.).
8. The process of claim 4 wherein a top layer and a bottom layer of catalyst are present and the temperature of the top catalyst bed is about 345° C. (650° F.) and the temperature of the bottom catalyst bed is in range of about 345-595° C. (650-1100° F.).
9. The process of claim 6 wherein the reaction is continued until a balance is substantially reached between the iron and ferrite content of the catalyst.
10. The process of claim 1 , wherein the iron-based oxidative dehydrogenation catalyst is free of zinc.
11. The process of claim 1 , wherein the carbonaceous compound is at least one of coke, charcoal, and soot.
12. The process of claim 1 , wherein the oxygen-containing gaseous mixture is a combination of oxygen and at least one of steam, hydrocarbons, hydrogen, nitrogen and natural gases.
13. The process of claim 1 wherein the stream of steam and air is an oxygen enriched gas mixture having a combination of steam, air, oxygen, hydrocarbons, nitrogen and natural gases.
14. A process for regenerating an iron based oxidative dehydrogenation catalyst using multiple reactors, the process comprising:
allowing oxidative dehydrogenation reaction for conversion of butene to butadiene in first and second reactors; and
regenerating spent iron-based oxidative dehydrogenation catalyst in a third reactor, wherein steps for regenerating the spent iron-based oxidative dehydrogenation catalyst comprise:
passing a stream containing steam:air in a controlled fashion, together with an oxygen-containing gaseous mixture over the spent iron-based oxidative dehydrogenation catalyst; and,
heating a carbonaceous compound deposited on the spent iron-based oxidative dehydrogenation catalyst at a pressure of 0-150 psig and a temperature less than 705° C. (1300° F.), for a period less than 144 hours (6 days), and thereby regenerating the spent oxidative dehydrogenation catalyst in the third reactor;
and, wherein the first and second reactors are online when the third reactor is offline, thereby regenerating the iron based oxidative dehydrogenation catalyst in the third reactor.
15. The process of claim 14 , wherein the first, second, and third reactors are at least one of fixed and fluidized beds.
16. The process of claim 14 , wherein the online is operation condition and the offline is non-operation condition of the first, second, and third reactors.
17. The process of claim 14 , wherein the iron-based oxidative dehydrogenation catalyst is a composite of iron-based oxide and zinc.
18. The process of claim 14 , wherein the iron-based oxidative dehydrogenation catalyst is free of zinc.
19. The process of claim 14 , wherein the carbonaceous compound is at least one of coke, charcoal, and soot.
20. The process of claim 14 , wherein the oxygen-containing gaseous mixture is a combination of oxygen and at least one of steam, hydrocarbons, hydrogen, and natural gases.