Magnetic removal of material from a mixture based on sulfided diluent in the mixture
View Patent ↗Methods and apparatus relate to processing of petroleum with a bed having a sorbent based diluent that the petroleum contacts upon passing through the bed. Magnetic properties of the sorbent and any other material, such as zeolite, used in the bed enable separation of such bed constituents based on a sulfided form of the sorbent being magnetic in contrast to a non-sulfided form of the sorbent being non-magnetic. Dividing the bed constituents into first and second portions by magnetic separation facilitates in selective replacing and/or regenerating the first portion independent of the second portion.
1. A method of processing petroleum, comprising:
contacting in a reactor a solid particulate mixture with a hydrocarbon-containing feed stream, wherein the solid particulate mixture comprises a sorbent impregnated with a nickel-containing material and a catalyst, wherein the sorbent adsorbs sulfur from the hydrocarbon-containing feed stream, wherein the catalyst comprises a zeolite and causes reactions that increase octane of the hydrocarbon-containing feed stream;
removing at least part of the solid particulate mixture from the reactor to provide a removed portion of the mixture;
separating the sorbent from the catalyst within the removed portion by magnetic separation; and
processing independent of one another the sorbent and the catalyst that are separated, wherein the solid particulate mixture within the reactor is replenished with at least one of the sorbent and the catalyst that is recycled from the removed portion.
2. The method according to claim 1 , wherein the processing includes replacing the catalyst from the removed portion with new material supplied to the reactor and recycling the sorbent from the removed portion back to the reactor.
3. The method according to claim 1 , wherein the processing includes replacing the sorbent from the removed portion with new material supplied to the reactor and recycling the catalyst from the removed portion back to the reactor.
4. The method according to claim 1 , wherein the catalyst is less magnetic than the sorbent.
5. The method according to claim 1 , wherein the sorbent further comprises zinc oxide.
6. The method according to claim 1 , wherein a sulfur unloaded form of the sorbent is less magnetic than a sulfided form of the sorbent.
7. The method according to claim 1 , further comprising regenerating the sorbent to remove sulfur-containing compounds from the sorbent.
8. The method according to claim 1 , further comprising regenerating the catalyst to remove coke from the catalyst.
9. The method according to claim 1 , further comprising regenerating the catalyst to remove coke from the catalyst and regenerating the sorbent to remove sulfur-containing compounds from the sorbent.
10. The method according to claim 1 , wherein a catalyst to sorbent ratio within the mixture is about 1:1.
11. The method according to claim 1 , wherein the zeolite comprises ZSM-5.
12. A system for processing petroleum, comprising:
a reactor containing a solid particulate mixture, wherein the solid particulate mixture comprises a sorbent and a catalyst, wherein the sorbent comprises a nickel-containing material impregnated thereon and is capable of adsorbing sulfur from a hydrocarbon-containing fluid, wherein the catalyst comprises a zeolite and is capable of catalyzing reactions that increase octane of the hydrocarbon-containing fluid;
a magnetic separator coupled to receive a portion of the solid particulate mixture and separate the sorbent from the catalyst within the portion; and
processing equipment to replenish the solid particulate mixture within the reactor with at least one of the sorbent and the catalyst that is recycled from the portion, wherein the processing equipment is coupled to the magnetic separator to process independent of one another the sorbent and the catalyst that are separated by the magnetic separator.
13. The system according to claim 12 , wherein the zeolite comprises ZSM-5.
14. The system according to claim 13 , wherein the sorbent further comprises zinc oxide.