Hydroconversion with group IA, IIA metal compounds

• US 4,127,470 A
• Filed: 08/01/1977
• Issued: 11/28/1978
• 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., Ledford, Thomas H.
• Primary Examiner(s): Gantz, Delbert E.
• Assistant Examiner(s): Schmitkons, G. E.
• Application Number:
  US05/820,859
• Time in Patent Office: 484 Days
• Field of Search: 208/58, 208/108, 208/212
• US Class Current: 208/58
• CPC Class Codes: C10G 45/04 characterised by the catalyst used
• CPC Class Codes: C10G 65/04 including only refining steps

Abstract

Processes for the treating of sulfur-containing petroleum oil feedstocks employing alkali metal compounds, alkaline earth metal compounds, and mixtures thereof are disclosed. Specifically, processes for hydrotreating feedstocks which have been previously partially desulfurized using conventional hydrodesulfurization catalysts by contacting such feedstocks with alkali metal compounds, alkaline earth metal compounds, and mixtures thereof, are disclosed. Preferably, the products of such a treatment are employed as feeds for catalytic cracking processes. In addition, processes for the combined hydrotreating and hydroconversion of various sulfur-containing petroleum oil feeds are disclosed, employing at least two hydroconversion agents selected from the group consisting of the alkali metal compounds and alkaline earth metal compounds, in the presence of added hydrogen, and at elevated temperatures. The reaction products formed thereby include a substantially desulfurized and demetallized, as well as a significantly upgraded petroleum product. The latter is demonstrated by a reduced Conradson carbon content and an increased API gravity.

Claims

1. A process for hydrotreating a partially desulfurized petroleum oil feedstock in a reaction zone at a temperature ranging from about 500°

to about 1500°

F. in the presence of sufficient added hydrogen to produce a hydrogen partial pressure of from about 500 to 5000 psi, which comprises;

contacting said feedstock in said reaction zone with a reagent consisting essentially of a compound selected from the group consisting of (a) at least one alkali metal compound selected from the group consisting of alkali metal oxides, alkali metal sulfides, alkali metal hydrosulfides, alkali metal amides, alkali metal carbonates, alkali metal carboxylates, and alkali metal alkoxides;

(b) at least one compound selected from the group consisting of alkaline earth metal hydroxides, alkaline earth metal sulfides, alkaline earth metal hydrosulfides, alkaline earth metal amides, alkaline earth metal carbonates, alkaline earth metal alkoxides, and (c) a mixture of at least one alkali metal compound and at least one alkaline earth metal compound, said alkali metal compound being selected from the group consisting of alkali metal oxides, alkali metal hydroxides, alkali metal sulfides, alkali metal hydrosulfides, alkali metal amides, alkali metal carbonates, alkali metal carboxylates, alkali metal alkoxides and, wherein said alkaline earth metal compound is selected from the group consisting of alkaline earth metal oxides, alkaline earth metal hydroxides, alkaline earth metal sulfides, alkaline earth metal hydrosulfides, alkaline earth metal carboxylates and alkaline earth metal alkoxides.

2. The process of claim 1 wherein the alkali metal constituent of said alkali metal compound is selected from the group consisting of sodium, potassium and cesium.

3. The process of claim 1 wherein the alkaline earth metal constituent of said alkaline earth metal compound is selected from the group consisting of calcium, barium and magnesium.

4. The process of claim 1 wherein said alkaline earth metal compound is an alkaline earth oxide.

5. The process of claim 1 wherein said reagent is a mixture of at least one alkali metal compound and at least one alkaline earth metal compound of group (c).

6. The process of claim 1 wherein said reagent is present in said reaction zone in an amount ranging from about 1 to about 15 weight percent.

7. The process of claim 1 wherein prior to said hydrotreating stage, a sulfur-containing pertroleum oil is subjected to catalytic desulfurization in a reaction zone maintained at a temperature ranging from about 500°

to about 2000°

F. in the presence of a sufficient amount of added hydrogen to provide a hydrogen pressure ranging from about 500 to about 2500 psi and thereby produce said partially desulfurized feedstock which is subsequently hydrotreated.