Hydroconversion process

Claim 2

In a slurry hydroconversion process wherein a carbonaceous chargestock containing a catalyst or catalyst precursor comprising a metal selected from the group consisting of vanadium, molybdenum and mixtures thereof, is reacted with a hydrogen-containing gas at hydroconversion conditions to produce a hydroconverted oil product comprising solids containing said metals, separating a heavy oil portion comprising said metal-containing solids from said hydroconverted oil; gasifying at least a portion of said separated heavy oil portion to produce a metal-containing ash, the improvement which comprises contacting said metal-containing ash with oxalic acid to extract said metal from said ash, and adding at least a portion of the resulting metal-containing oxalic acid extract to said carbonaceous chargestock as catalyst precursor.

Claim 3

The process of claim 1 wherein said metal-containing oxalic acid extract is added to said carbonaceous chargestock in an amount sufficient to provide from about 10 to 2000 wppm metal of said metals, calculated as elemental metal, based on said carbonaceous chargestock.

Claim 4

The process of claim 1 wherein said oxalic acid is used in at least a stoichiometric amount sufficient to form a metal oxalate of said metal.

Claim 5

The process of claim 1 wherein said oxalic acid is contacted with said metal-containing ash at a temperature ranging from 80° to 300 F. and a pressure ranging from 0 to 100 psig.

Claim 6

The process of claim 1 wherein said hydroconversion conditions include a temperature ranging from 650° to 1000° F. and a hydrogen partial pressure ranging from 500 to 5,000 psig.

Claim 7

The process of claim 1 wherein said gasification conditions include a temperature ranging from 800° to 2000° F. and a pressure ranging from 0 to 150 psig.

Claim 8

The process of claim 1 wherein at least a portion of said separated heavy oil is recycled to said hydroconversion zone.

Claim 9

The process of claim 1 wherein said carbonaceous chargestock comprises a hydrocarbonaceous oil.

Claim 10

The process of claim 1 wherein said carbonaceous chargestock comprises coal.

Claim 11

The process of claim 1 wherein said catalyst or catalyst precursor comprises vanadium.

Claim 12

The process of claim 1 wherein said catalyst has been prepared in situ in said feed from a catalyst precursor.

Claim 13

The process of claim 1 wherein said catalyst precursor comprises vanadyl oxalate.

Claim 14

A slurry hydroconversion process comprising the steps of: (a) adding an oxalic acid extract comprising a metal selected from the group consisting of vanadium, molybdenum and mixtures thereof recycled from step (f) as catalyst precursor to a carbonaceous chargestock to form a mixture; (b) reacting said mixture with a hydrogen-containing gas at hydroconversion conditions to produce a hydroconverted oil product comprising solids containing said metal; (c) separating a heavy oil portion comprising said metal-containing solids from said hydroconverted oil; (d) gasifying at least a portion of said separated heavy oil portion to produce a metal-containing ash; (e) contacting said metal-containing ash with oxalic acid to extract said metal from said ash, and (f) adding at least a portion of the resulting metal-containing acid extract to said carbonaceous chargestock as said catalyst precursor.

Claim 15

A slurry hydroconversion process comprising the steps of: (a) adding an oxalic acid extract comprising a metal selected from the group consisting of vanadium, molybdenum and mixtures thereof recycled from step (f) as catalyst precursor to a carbonaceous chargestock to form a mixture; (b) reacting said mixture with a hydrogen-containing gas at hydroconversion conditions to produce a hydroconverted oil product comprising solids containing said metal; (c) separating a heavy oil portion comprising said metal-containing solids from said hydroconverted oil; (d) gasifying at least a portion of said separated heavy oil portion to produce a metal-containing ash; (e) contacting said metal-containing ash with oxalic acid to extract said metal from said ash, and (f) adding at least a portion of the resulting metal-containing acid extract to said carbonaceous chargestock as said catalyst precursor.