Coking process

Claim 2

A process for coking hydrocarbon oils which comprises the following steps in combination: (a) preheating a hydrocarbon oil feedstock in a preheating zone to a temperature lower than the cracking temperature of said feedstock; (b) directly contacting the preheated feedstock from step (a) in a combustion exhaust gas zone with combustion exhaust gas produced in the combustion gas generation zone of step (e), said gas being maintained at a temperature capable of heating the said feedstock to a temperature higher than its cracking temperature; (c) thereafter introducing said heated feedstock into a coking zone maintained at a temperature higher than the cracking temperature of said feedstock so as to coke at least a portion of said feedstock; (d) separating hot gaseous, liquid and solid products from said coking zones; (e) introducing at least a portion of said hot gaseous product to a combustion gas generation zone; and (f) introducing at least a portion of the combustion exhaust gas produced in said combustion gas generation zone to said combustion exhaust gas contact zone of step (b).

Claim 3

A process according to claim 1 wherein said combustion gas in step (b) is maintained at a temperature in the range from about 500° to about 1000° C.

Claim 4

A process according to claim 1 wherein said combustion gas in step (b) is maintained at a temperature in the range from about 700° to about 800° C.

Claim 5

A process according to claim 1 wherein said coking zone in step (c) is maintained at a temperature in the range from about 380° to about 550° C., a pressure in the range from atmospheric to about 50 kg/cm 2 G and for a residence time in the range from about 0.5 to about 20 hours.

Claim 6

A process according to claim 1 wherein said combustion exhaust gas contact zone of step (b) is maintained at an average liquid temperature in the range of 400° to 500° C., an average gas temperature in the range from about 500° to about 650° C., an average pressure of less than about 5 kg/cm 2 G, a gas to liquid volume ratio in the range from about 100 to about 160 and for a residence time in the range from about 0.1 to about 1 minute.

Claim 7

A process according to claim 1 wherein the hydrocarbon oil feedstock in said preheating zone of step (a) is heated to a temperature of about 15° to 40° C. lower than the cracking temperature of said feedstock.

Claim 8

A process according to claim 1 wherein the hydrocarbon oil feedstock has a specific gravity of between about 0.95 to about 1.10, a sulfur content in the range of about 1 to about 10 wt. %, a metal content of more than about 100 ppm, an asphaltene content of more than about 5 wt. %, and a Conradson Carbon residue of more than about 7 wt. %.

Claim 9

A process for coking hydrocarbon oil which comprises the following steps in combination: (a) preheating a hydrocarbon oil feedstock having a Conradson Carbon residue of more than about 7 wt. % and a specific gravity in the range from about 0.95 to about 1.10 in a preheating zone to a temperature in the range from about 340°-400° C.; (b) directly contacting the preheated feedstock from step (a) in a combustion exhaust gas contact zone with combustion exhaust gas produced in the combustion gas generation zone of step (e), said gas being maintained at a temperature in the range from about 500° to about 1000° C. for a residence time in the range from about 0.1 to about 1 minute; (c) thereafter, introducing said heated feedstock into a coking zone maintained at a temperature in the range from about 380° to about 550° C., a pressure in the range from atmospheric to about 50 kg/cm 2 G and for a residence time in the range from about 0.5 to about 20 hours. (d) separating hot gaseous, liquid and solid products from said coking zone; (e) introducing at least a portion of said hot gaseous products to a combustion gas generation zone; and (f) introducing at least a portion of the combustion exhaust gas produced in said combustion gas generation zone to said combustion exhaust gas contact zone of step (b).

Claim 10

A process for coking hydrocarbon oil which comprises the following steps in combination: (a) preheating a hydrocarbon oil feedstock having a Conradson Carbon residue of more than about 7 wt. % and a specific gravity in the range from about 0.95 to about 1.10 in a preheating zone to a temperature in the range from about 340°-400° C.; (b) directly contacting the preheated feedstock from step (a) in a combustion exhaust gas contact zone with combustion exhaust gas produced in the combustion gas generation zone of step (e), said gas being maintained at a temperature in the range from about 500° to about 1000° C. for a residence time in the range from about 0.1 to about 1 minute; (c) thereafter, introducing said heated feedstock into a coking zone maintained at a temperature in the range from about 380° to about 550° C., a pressure in the range from atmospheric to about 50 kg/cm 2 G and for a residence time in the range from about 0.5 to about 20 hours. (d) separating hot gaseous, liquid and solid products from said coking zone; (e) introducing at least a portion of said hot gaseous products to a combustion gas generation zone; and (f) introducing at least a portion of the combustion exhaust gas produced in said combustion gas generation zone to said combustion exhaust gas contact zone of step (b).

Claim 11

A process according to claim 8 wherein at least a portion of the hot gaseous product from the coking zone of step (c) is recycled back to the coking zone as an agitation gas.