초록 ▼

The present invention is an improved regenerated catalyst bend assembly for a fluid catalytic cracking unit. In a preferred embodiment, the reduced elevation (“RE-bend” or “REL-bend”) regenerated catalyst return line assembly of the present invention has an outlet elevation that is lower than the in

The present invention is an improved regenerated catalyst bend assembly for a fluid catalytic cracking unit. In a preferred embodiment, the reduced elevation (“RE-bend” or “REL-bend”) regenerated catalyst return line assembly of the present invention has an outlet elevation that is lower than the inlet elevation of the RE-bend or REL-bend regenerated catalyst return line assembly, and a process for utilizing the assembly in a fluid catalytic cracking unit. The present invention is especially useful in the modification of existing fluid catalytic cracking units to lower the elevation of the outlet of the regenerated catalyst return line assembly, thereby providing needed space to increase the fluid catalytic cracking reactor riser length.

대표청구항 ▼

1. A regenerated catalyst conduit for fluidly connecting a regenerator standpipe to a reactor riser of a fluid catalytic cracking unit, comprising: a) a first bend with a bend radius, R1, and an inlet end and an outlet end; andb) a second bend with a bend radius, R2, and an inlet end and an outlet e

1. A regenerated catalyst conduit for fluidly connecting a regenerator standpipe to a reactor riser of a fluid catalytic cracking unit, comprising: a) a first bend with a bend radius, R1, and an inlet end and an outlet end; andb) a second bend with a bend radius, R2, and an inlet end and an outlet end;wherein the inlet end of the first bend is physically connected to the outlet end of the regenerator standpipe, the outlet end of the first bend is physically connected, without an intervening structure, to the inlet end of the second bend, the outlet end of the second bend is physically connected to the inlet end of the reactor riser, andR1 is not equal to R2. 2. The conduit of claim 1, wherein the outlet end of second bend is at a lower elevation than the inlet end of the first bend. 3. The conduit of claim 2, wherein regenerator standpipe and the reactor riser have a substantially vertical section above the regenerated catalyst conduit. 4. The conduit of claim 2, wherein R1 is greater than R2. 5. The conduit of claim 2, wherein the internal angle of the first bend, α1, is greater than the internal angle of the second bend, α2. 6. The conduit of claim 4, wherein the internal angle of the first bend, α1, is greater than the internal angle of the second bend, α2. 7. The conduit of claim 4, wherein the centerline of the regenerator standpipe at the point where it connects to the inlet end of the first bend is substantially concurrent with the centerline of the inlet end of the first bend. 8. The conduit of claim 4, wherein the centerline of the reactor riser at the point where it connects to the outlet end of the second bend is substantially concurrent with the centerline of the outlet end of the second bend. 9. The conduit of claim 7, wherein the centerline of the reactor riser at the point where it connects to the outlet end of the second bend is substantially concurrent with the centerline of the outlet end of the second bend. 10. The conduit of claim 7, wherein the sum of the internal angle of the first bend, α1, and the internal angle of the second bend, u2 is substantially 180°. 11. A fluid catalytic cracking process, comprising: a) catalytically cracking a hydrocarbon-containing feedstream in a reactor riser the presence of a fluidized catalyst to form a mixture of a cracked hydrocarbon product stream and a spent catalyst;b) separating the cracked hydrocarbon product stream from the spent catalyst, wherein the spent catalyst comprises hydrocarbon residue;c) regenerating at least a portion of the spent catalyst in a regenerator by combusting at least a portion of the hydrocarbon residue in an oxygen-containing atmosphere to produce a regenerated catalyst;d) conducting at least a portion of the regenerated catalyst from the regenerator to a regenerated catalyst conduit through a regenerator standpipe; ande) transporting at least a portion of the regenerated catalyst to the reactor riser through the regenerated catalyst conduit;wherein the regenerated catalyst conduit fluidly connects the regenerator standpipe to the reactor riser and is comprised of a first bend with a bend radius, R1, and an inlet end and an outlet end; and a second bend with a bend radius, R2, and an inlet end and an outlet end; wherein the inlet end of the first bend is physically connected to the outlet end of the regenerator standpipe, the outlet end of the first bend is physically connected, without an intervening structure, to the inlet end of the second bend, the outlet end of the second bend is physically connected to the inlet end of the reactor riser, and R1 is not equal to R2. 12. The process of claim 11, wherein the outlet end of second bend is at a lower elevation than the inlet end of the first bend. 13. The process of claim 12, wherein the hydrocarbon-containing feedstream is comprised of hydrocarbonaceous oils boiling in the range of about 430° F. to about 1050° F. (221 to 566° C.). 14. The process of claim 13, catalyst is comprised of a medium pore zeolite selected from the group consisting of ZSM-5, ZSM-11, ZSM-12, ZSM-22, ZSM-23, ZSM-35, ZSM-48, ZSM-57, SH-3 and MCM-22, and combinations thereof. 15. The process of claim 14, wherein the hydrocarbon-containing feedstream is contacted with the regenerated catalyst in the reactor riser for less than about 5 seconds. 16. The process of claim 13, wherein the short-contact time conditions include riser outlet temperatures from about 900° F. to about 1200° F. (482 to 649° C.) and pressures from about 0 to about 100 psig (0 to 690 kPa). 17. The process of claim 16, wherein R1 is greater than R2, and the internal angle of the first bend, α1, is greater than the internal angle of the second bend, α2.