Upgrading Slurry Oil Using Chromatographic Reactor Systems

• US 20100176029A1
• Filed: 01/09/2009
• Published: 07/15/2010
• Est. Priority Date: 01/09/2009
• Status: Abandoned Application

• Current Assignee: Phillips 66 Company
• Original Assignee: Conocophillips Company (ConocoPhillips)
• Inventors: Subbiah, Ayyappan, Choudhary, Tushar V.
• Application Number:
  US12/351,391
• Publication Number:
  US 20100176029A1
• Time in Patent Office: Days
• US Class Current: 208/91
• CPC Class Codes: B01D 15/08 Selective adsorption, e.g. chromatography
• CPC Class Codes: B01D 15/203 Equilibration or regeneration
• CPC Class Codes: B01J 20/103 comprising silica
• CPC Class Codes: B01J 20/283 based on silica
• CPC Class Codes: B01J 20/3433 of sorbents or filter aids other than those covered by B01J20/3408 - B01J20/3425
• CPC Class Codes: B01J 20/3475 in the liquid phase
• CPC Class Codes: C10B 57/045 containing mineral oils, bitumen, tar or the like or mixtures thereof
• CPC Class Codes: C10G 25/003 Specific sorbent material, not covered by C10G25/02 or C10G25/03

Abstract

Methods and apparatus relate to reducing content of nitrogen-containing compounds within slurry oil using a chromatographic based assembly, which may not affect aromatic content, prior to feeding the slurry oil into a coking system. The slurry oil passes through the chromatographic based assembly to upgrade the slurry oil and make the slurry oil suitable for feedstock in making needle coke. Further, a hydrotreater utilized in combination with the chromatographic based assembly may provide additional upgrading of the slurry oil.

Claims

1. A method of producing needle coke products, comprising:

passing a slurry oil mixture through a chromatographic based assembly to produce upgraded slurry oil, wherein nitrogen-containing compounds within the slurry oil mixture are adsorbed onto packing material of the chromatographic based assembly without affecting aromatic content of the slurry oil mixture; and

introducing the upgraded slurry oil into a coking system to make needle coke.

2. The method according to claim 1, further comprising reacting the upgraded slurry oil in presence of a catalyst to hydrogenate sulfur-containing compounds in the upgraded slurry oil.

3. The method according to claim 1, further comprising hydrotreating the upgraded slurry oil, wherein the hydrotreating generates hydrogen sulfide from sulfur-containing compounds in the upgraded slurry oil and strips the hydrogen sulfide from the upgraded slurry oil.

4. The method according to claim 1, wherein the nitrogen-containing compounds within the slurry oil mixture adsorb onto silica that forms the packing material.

5. The method according to claim 1, wherein the nitrogen-containing compounds within the slurry oil mixture adsorb onto modified silica that forms the packing material.

6. The method according to claim 1, wherein passing the slurry oil mixture through the chromatographic based assembly includes alternating between flowing the slurry oil mixture through a chromatographic first reactor and flowing the slurry oil mixture through a chromatographic second reactor.

7. The method according to claim 1, further comprising regenerating the packing material by passing a solvent through the chromatographic based assembly.

8. The method according to claim 1, further comprising regenerating the packing material by alternating between flowing a solvent through a chromatographic first reactor and flowing the solvent through a chromatographic second reactor, wherein passing the slurry oil mixture through the chromatographic based assembly alternates between flowing the slurry oil mixture through the first reactor and flowing the slurry oil mixture through the second reactor.

9. A system for producing needle coke products, comprising:

a supply for a slurry oil mixture;

a chromatographic based assembly having an inlet to receive the slurry oil mixture and an outlet, wherein the chromatographic based assembly includes packing material that is an adsorbent for nitrogen-containing compounds within the slurry oil mixture; and

a coking system configured to make needle coke, wherein a feedstock supply for the coking system is coupled to the outlet of the chromatographic based assembly such that the packing material of the chromatographic based assembly is disposed in a flow path of the slurry oil mixture between the supply for the slurry oil mixture and the coking system.

10. The system according to claim 9, further comprising a hydrotreater, wherein the flow path of the slurry oil mixture passes through the hydrotreater between the supply for the slurry oil mixture and the coking system.

11. The system according to claim 9, further comprising a hydrotreater, wherein the flow path of the slurry oil mixture passes through the hydrotreater between the chromatographic based assembly and the coking system.

12. The system according to claim 9, further comprising a hydrotreater having a catalyst of a reaction that hydrogenates sulfur-containing compounds in the slurry oil mixture, wherein the flow path of the slurry oil mixture passes through the hydrotreater.

13. The system according to claim 9, wherein the chromatographic based assembly includes first and second reactors each filled with the packing material.

14. The system according to claim 9, wherein the chromatographic based assembly includes first and second reactors each filled with the packing material and in alternate fluid communication with the supply for the slurry oil mixture and a solvent source.

15. The system according to claim 9, wherein the packing material comprises silica.

16. The system according to claim 9, wherein the packing material comprises modified silica.

17. A method of producing needle coke products, comprising:

removing nitrogen-containing compounds within a slurry oil by chromatography;

removing sulfur-containing compounds within the slurry oil by hydro-desulfurization; and

coking the slurry oil, which is output from the chromatography and the hydro-desulfurization, to make needle coke solids.

18. The method according to claim 17, wherein the chromatography occurs in multiple reactors operated in a cycle such that certain one or more of the reactors are regenerated by solvent washing while another one or more of the reactors are removing the nitrogen-containing compounds.

19. The method according to claim 17, wherein the chromatography reduces weight percent of the nitrogen-containing compounds in the slurry oil by at least 20%.

20. The method according to claim 17, further comprising preparing graphite electrodes with the needle coke solids.