Hydroconversion of residua with potassium sulfide

• US 4,119,528 A
• Filed: 08/01/1977
• Issued: 10/10/1978
• Est. Priority Date: 08/01/1977
• Status: Expired due to Term

• Current Assignee: Exxon Research and Engineering Company (Exxon Mobil Corporation)
• Original Assignee: Exxon Research and Engineering Company (Exxon Mobil Corporation)
• Inventors: Bearden, Roby Jr., Baird, William C. Jr.
• Primary Examiner(s): Gantz, Delbert E.
• Assistant Examiner(s): Schmitkons, G. E.
• Application Number:
  US05/820,820
• Time in Patent Office: 435 Days
• Field of Search: 208/108
• US Class Current: 208/108
• CPC Class Codes: C10G 29/10 Sulfides
• CPC Class Codes: C10G 45/00 Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
• CPC Class Codes: C10G 47/00 Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions C10G15/00 takes precedence; destructive hydrogenation of non-melting solid carbonaceous or similar materials C10G1/06
• CPC Class Codes: Y10S 423/12 Molten media

Abstract

A process for the simultaneous desulfurization and hydroconversion of heavy carbonaceous feeds, including various sulfur-containing heavy petroleum oils, is disclosed. These feedstocks are contacted with potassium sulfide in a conversion zone maintained at elevated temperatures and in the presence of added hydrogen. In this manner, the feeds are substantially desulfurized, and significant upgrading of these feeds is also obtained as demonstrated by decreased Conradson carbon, increased API gravity, and the conversion of substantial portion of the 1,050° F.+ portion of these feeds. In a preferred embodiment, such a process is disclosed employing a combination of potassium sulfide and sodium sulfide, and in particular these processes include procedures for the regeneration of the sulfides and their recycle to the conversion zone.

Claims

1. A process for the combined desulfurization and hydroconversion of a heavy hydrocarbon feedstock, which comprises contacting said heavy hydrocarbon feedstock without pretreatment with potassium sulfide in a conversion zone in the presence of a sufficient amount of added hydrogen to produce a hydrogen pressure of from about 500 to 5000 psi, in a conversion zone maintained at an elevated temperature between 500°

and 2000°

F., so that said heavy hydrocarbon feedstock is converted to lower boiling hydrocarbon products and is substantially desulfurized.

2. The process of claim 1 wherein said potassium sulfide is present in said conversion zone in an amount ranging from about 1 to 50 weight percent based on said hydrocarbon feedstock.

3. The process of claim 1 wherein said potassium sulfide is employed in a slurry with said heavy hydrocarbon feedstock in said conversion zone.

4. The process of claim 1 wherein said hydrogen pressure ranges from about 1500 to 3000 psi.

5. The process of claim 1 wherein said heavy hydrocarbon feedstock includes at least about 10 weight percent of components boiling above about 1050°

F., and wherein at least about 50 percent of said components boiling above about 1050°

F. are converted therein.

6. The process of claim 5 wherein said elevated temperature is greater than about 750°

F.

7. The process of claim 1 wherein less than about 50 weight percent of potassium hydrosulfide is formed in said conversion zone, and wherein said potassium hydrosulfide is converted to potassium sulfide, and said potassium sulfide is recycled to said conversion zone.

8. The process of claim 7 wherein said potassium hydrosulfide is converted to said potassium sulfide by high temperature steaming of said potassium hydrosulfide to form potassium hydroxide, and said potassium hydroxide is contacted with hydrogen sulfide to produce said potassium sulfide.

9. The process of claim 1 wherein sodium sulfide is present in said conversion zone.

10. The process of claim 9 wherein the ratio of said potassium sulfide to said sodium sulfide is between about 50:

1 and 1;

50.

11. The process of claim 9 wherein said elevated temperature is between about 500°

and 2000°

F.

12. The process of claim 9 wherein said heavy hydrocarbon feedstock includes at least about 10 weight percent of components boiling above about 1050°

F., and at least about 50 percent of said components boiling above about 1050°

F. are converted to lower boiling products in said conversion zone.

13. The process of claim 9 wherein sodium hydrosulfide is produced in said conversion zone, and said sodium hydrosulfide is converted to said sodium sulfide by contacting said sodium hydrosulfide in a stripping zone maintained at a temperature between about 200°

and 700°

F.