Process for regenerating catalyst in a fluid catalytic cracking unit
One exemplary embodiment can be a process for regenerating catalyst in a fluid catalytic cracking unit. Generally, the process includes providing a feed to a riser of a reaction vessel, and providing a stream to a distributor positioned within a void proximate to an inlet receiving unregenerated catalyst in a regenerator. The feed can include at least one of a gas oil, a vacuum gas oil, an atmospheric gas oil, a coker gas oil, a hydrotreated gas oil, a hydrocracker unconverted oil, and an atmospheric residue.
1. A process for regenerating catalyst in a fluid catalytic cracking unit, comprising:
A) providing a feed comprising at least one of a gas oil, a vacuum gas oil, an atmospheric gas oil, a coker gas oil, a hydrotreated gas oil, a hydrocracker unconverted oil, and an atmospheric residue to a riser of a reaction vessel; and
B) introducing an uncombusted stream, which comprises a first stream comprising oxygen and a second stream comprising at least one of a hydrocarbon and hydrogen, proximate to an inlet receiving unregenerated catalyst for a regenerator;
wherein the first and second streams are mixed together in a heater before introducing, and the heater does not ignite at least one of the hydrocarbon and hydrogen.
2. The process according to claim 1 , wherein the heater is a direct fired heater.
3. The process according to claim 1 , wherein the hydrocarbon comprises one or more C1-C5 hydrocarbons.
4. The process according to claim 1 , wherein the hydrocarbon comprises one or more C2-C5 hydrocarbons, and the total volume of hydrocarbon is no more than about 3%, by volume, based on the volume of the uncombusted stream.
5. The process according to claim 1 , wherein the hydrocarbon comprises methane, and the total volume of methane is no more than about 5%, by volume, based on the volume of the uncombusted stream.
6. The process according to claim 1 , wherein the uncombusted stream comprises hydrogen, and the total volume of hydrogen is no more than about 4%, by volume, based on the volume of the uncombusted stream.
7. The process according to claim 1 , wherein the uncombusted stream comprises no more than about 3%, by volume, of the total amount of the hydrocarbon and hydrogen based on the volume of the uncombusted stream.
8. The process according to claim 1 , wherein the regenerator comprises a separator and a combustor.
9. The process according to claim 8 , wherein the separator substantially encloses a distributing device and one or more cyclone separators.
10. A process for regenerating catalyst in a fluid catalytic cracking unit, comprising:
A) providing a feed comprising at least one of a gas oil, a vacuum gas oil, an atmospheric gas oil, a coker gas oil, a hydrotreated gas oil, a hydrocracker unconverted oil, and an atmospheric residue to a riser of a reaction vessel;
B) mixing a first stream comprising air and a second stream comprising at least one of a hydrocarbon and hydrogen in a direct fired heater to form an uncombusted stream exiting the direct fired heater; and
C) introducing the uncombusted stream proximate to an inlet receiving unregenerated catalyst for a regenerator.