Process for removing metals from crude

• US 4,645,589 A
• Filed: 10/18/1985
• Issued: 02/24/1987
• Est. Priority Date: 10/18/1985
• Status: Expired due to Fees

• Current Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Original Assignee: Mobil Oil Corporation (Exxon Mobil Corporation)
• Inventors: Lam, Chiu T., Krambeck, Frederick J., Schipper, Paul H.
• Primary Examiner(s): Metz, Andrew H.
• Assistant Examiner(s): Myers, Helane
• Application Number:
  US06/789,218
• Time in Patent Office: 494 Days
• Field of Search: 208/251 R, 208/252
• US Class Current: 208/251.00R
• CPC Class Codes: C10G 17/00 Refining of hydrocarbon oils in the absence of hydrogen, with acids, acid-forming compounds or acid-containing liquids, e.g. acid sludge
• CPC Class Codes: C10G 21/003 Solvent de-asphalting
• CPC Class Codes: C10G 21/24 Phosphorus-containing compounds
• CPC Class Codes: C10G 29/02 Non-metals

Abstract

A process for removing metal from a metal-containing hydrocarbon oil such as a heavy crude is disclosed which comprises:

(a) contacting a hydrocarbon oil phase containing at least one metal selected from the group consisting of vanadium and nickel with an aqueous phase of dissolved phosphorous compound capable of forming a compound or a complex with said metal, said aqueous phase containing a substantial quantity of water relative to the amount of liquid hydrocarbon contacted therewith, said contacting resulting in the removal of a substantial quantity of the metal from the hydrocarbon oil phase to the aqueous phase; and,

(b) separating the metal-containing aqueous phase from the demetalated hydrocarbon oil phase prior to subjecting the latter to downstream catalytic processing.

Claims

1. A process for removing metal from a metal-containing hydrocarbon oil which comprises:

(a) contacting a hydrocarbon oil phase containing at least one metal selected from the group consisting of vanadium and nickel with an aqueous phase of dissolved phosphorous compound capable of forming a compound or a complex with said metal, said aqueous phase containing from about 0.1 to about 20 parts by weight of water per part by weight of hydrocarbon oil contacted therewith, said contacting resulting in the removal of a substantial quantity of the metal from the hydrocarbon oil phase to the aqueous phase; and

,

(b) separating the metal-containing aqueous phase from the demetalated hydrocarbon oil phase prior to subjecting the latter to downstream catalytic processing.

2. The process of claim 1 wherein the hydrocarbon oil is a heavy crude oil containing from about 10 to about 1000 ppm vanadium and from about 5 to about 500 ppm nickel.

3. The process of claim 1 wherein the phosphorous compound is selected from the group consisting of P₂ O₅, H₃ PO₄, (NH₄)₃ PO₄, (NH₄)₂ HPO₄, (NH₄)H₂ PO₄, H₄ P₂ O₇, PSBr₃, H₃ PO₂, H₃ PO₃, (NH₄)H₂ P₂ O₇, phosphorylamide (PO(NH₂)₃), amino-tris(methanephosponic acid) and 1-hydroxyethyl di-phosphonic acid.

4. The process of claim 1 wherein the atomic ratio of atoms of phosphorus said phosphorous compound to atoms of vanadium and/or nickel present in the hydrocarbon oil is from about 0.01:

1 to about 3;

1.

5. The process of claim 1 wherein the atomic ratio of atoms of phosphorus in said phosphorous compound to atoms of vanadium and/or nickel present in the hydrocarbon oil is from about 0.03 to about 1:

1.

6. The process of claim 1 wherein the weight ratio of phosphorous compound to hydrocarbon oil is from about 1:

500 to about 1;

5.

7. The process of claim 1 wherein the weight ratio of phosphorous compound to hydrocarbon oil is from about 1:

200 to about 1;

10.

8. The process of claim 1 wherein the weight ratio of phosphorous compound to hydrocarbon oil is from about 1:

100 to about 1;

25.

9. The process of claim 1 wherein from about 0.1 to about 10 parts by weight of water per part by weight of hydrocarbon oil are employed.

10. The process of claim 1 wherein from about 0.2 to about 1 part by weight of water per part by weight of hydrocarbon oil are employed.

11. The process of claim 1 carried out at a temperature of from about 50°

to about 300°

C.

12. The process of claim 1 carried out at a temperature of from about 80°

to about 200°

C.

13. The process of claim 1 wherein the hydrocarbon oil is contacted with the aqueous phosphorous compound for from 5 minutes to about 60 minutes.

14. The process of claim 1 wherein the demetalated hydrocarbon is recycled to step (a).

15. The process of claim 1 employing batchwise counter current extraction.

16. The process of claim 1 employing continuous counter current extraction.