Fixed sulfur petroleum coke fuel and method for its production

Claim 2

A process of producing a fixed-sulfur petroleum coke fuel which comprises coking a heavy petroleum coker feedstock in the presence of an added alkaline earth metal oxide or precursor thereof, the amount of added alkaline earth metal oxide being within the range from about 1 to 10 times the amount theoretically necessary to completely fix the sulfur contained in the coke produced from the petroleum coker feedstock, and recovering coker products including a fixed-sulfur petroleum coke fuel byproduct comprising coke and about 3 to 30 weight percent ash (calculated as calcium oxide) derived from the alkaline earth additive.

Claim 3

The method of claim 1 wherein the heavy petroleum coker feedstock contains from about 0.5 to 6 weight percent sulfur.

Claim 4

The method of claim 2 wherein the fixed-sulfur petroleum coke fuel byproduct comprises coke and about 5 to 15 weight percent ash derived from the alkaline earth additive.

Claim 5

The method of claim 2 wherein the fixed-sulfur petroleum coke fuel byproduct comprises coke and about 10 weight percent ash derived from the alkaline earth additive.

Claim 6

The method of claim 1 wherein the coking process employed is delayed coking.

Claim 7

The process of claim 1 wherein the added alkaline earth metal oxide or precursor thereof is selected from the group consisting of lime, limestone, dolomite, and mixtures thereof.

Claim 8

The process of claim 1 wherein the added alkaline earth metal oxide comprises calcium oxide.

Claim 9

In a continuous process of coking a heavy petroleum coker feedstock wherein at least a portion of the coke produced in the coking zone is burned to raise its temperature above the coking zone temperature and is then recycled to the coking zone to provide heat for the coking reactions, the improvement which comprises: a. coking the heavy petroleum coker feedstock in the presence of an added alkaline earth metal oxide or precursor thereof, the amount of added alkaline earth metal oxide being within the range of about 1 to 10 times the stoichiometric amount necessary to completely fix the sulfur contained in the coke produced from the petroleum coker feedstock; b. recovering normally liquid and gaseous hydrocarbons and solid particles comprising coke and about 3 to 30 weight percent ash (calculated as calcium oxide) derived from the alkaline earth additive from the coking zone; c. partially combusting at least a portion of said particles to raise the temperature thereof above the coking zone temperature, the heated solid particles comprising coke and about 4 to 40 weight percent ash (calculated as calcium oxide) derived from the alkaline earth additive from the coking zone; and returning said heated solids to the coking zone; and d. recovering the remaining solid particles as a fixed-sulfur petroleum coke fuel byproduct.

Claim 10

In a continuous process of coking a heavy petroleum coker feedstock wherein at least a portion of the coke produced in the coking zone is burned to raise its temperature above the coking zone temperature and is then recycled to the coking zone to provide heat for the coking reactions, the improvement which comprises: a. coking the heavy petroleum coker feedstock in the presence of an added alkaline earth metal oxide or precursor thereof, the amount of added alkaline earth metal oxide being within the range of about 1 to 10 times the stoichiometric amount necessary to completely fix the sulfur contained in the coke produced from the petroleum coker feedstock; b. recovering normally liquid and gaseous hydrocarbons and solid particles comprising coke and about 3 to 30 weight percent ash (calculated as calcium oxide) derived from the alkaline earth additive from the coking zone; c. partially combusting at least a portion of said particles to raise the temperature thereof above the coking zone temperature, the heated solid particles comprising coke and about 4 to 40 weight percent ash (calculated as calcium oxide) derived from the alkaline earth additive from the coking zone; and returning said heated solids to the coking zone; and d. recovering the remaining solid particles as a fixed-sulfur petroleum coke fuel byproduct.

Claim 11

The method of claim 8 wherein the fixed-sulfur petroleum coke fuel byproduct is a portion of the solid particles recovered in step b.

Claim 12

The method of claim 9 wherein the ratio of solids recovered as byproduct to solids combusted and returned to the coking zone is adjusted such that from about 10 to 40 weight percent of the carbonaceous deposit on the solid particles passing to the combustion zone will be burned therein to raise the temperature of the resulting particles to about 1000° to 1750° F. for return to the coking zone.

Claim 13

The method of claim 10 wherein the heavy petroleum coker feedstock contains from about 0.5 to 6 weight percent sulfur.

Claim 14

The method of claim 11 wherein the solid particles recovered in step b. comprise coke and from about 5 to 15 weight percent ash derived from the alkaline earth additive and the heated solid particles returned to the coking zone comprise coke and from about 4 to 25 weight percent ash derived from the alkaline earth additive.

Claim 15

The method of claim 12 wherein the solid particles returned to the coking zone comprise coke and from about 6 to 18 weight percent ash derived from the alkaline earth additive.

Claim 16

The process of claim 8 wherein the coking zone contains a fluidized bed of solids.

Claim 17

The process of claim 8 wherein the coking zone contains a moving bed of solids.

Claim 18

The process of claim 8 wherein the added alkaline earth metal oxide or precursor thereof is selected from the group consisting of lime, limestone, dolomite and mixtures thereof.

Claim 19

The process of claim 8 wherein the added alkaline earth metal oxide comprises calcium oxide.