Sequential residue hydrodesulfurization and thermal cracking operations in a common reactor

Claim 2

A process comprising passing a first stream of residual oil containing metals and sulfur together with hydrogen downflow through a zone containing a packed bed of hydrodesulfurization catalyst comprising supported Group VI and Group VIII metals under hydrodesulfurization conditions including a space velocity between about 0.1 and 10 volumes of oil per volume of catalyst per hour, a hydrogen rate between about 500 and 10,000 SCF per barrel of oil and at a hydrogen pressure between about 50 to 5,000 psi, incrementally increasing the temperature in said zone within the range of about 690 to about 790° F. to compensate for loss of catalyst activity with age until said catalyst is deactivated for hydrodesulfurization, subsequently passing a second stream of residual oil and hydrogen upwardly through said zone containing said deactivated hydrodesulfurization catalyst under cracking conditions including a temperature above said hydrodesulfurization temperature up to 1,000° F. in the presence of hydrogen at a flow rate between about 500 to 10,000 SCF per barrel of oil, a hydrogen pressure between about 100 and 5,000 psi and an oil residence time between about 0.0014 and 5 hours to produce middle distillates.

Claim 3

The process of claim 1 wherein said oil residence time is between about 0.3 and 3 hours.

Claim 4

The process of claim 1 wherein said hydrodesulfurization catalyst contains a non-cracking support.

Claim 5

The process of claim 1 wherein said second stream of residual oil comprises hydrodesulfurized residual oil.

Claim 6

The process of claim 1 wherein the hydrogen pressure during the hydrodesulfurization step is above 1,000 psi and the hydrogen pressure during the hydrodesulfurization step is above the hydrogen pressure during the cracking step.

Claim 7

A process comprising passing residual oil containing metals and sulfur together with hydrogen downflow through a first zone containing a packed bed of hydrodesulfurization catalyst comprising supported Group VI and Group VIII metals under hydrodesulfurization conditions including a space velocity between about 0.1 and 10 volumes of oil per volume of catalyst per hour, a hydrogen rate between about 500 and 10,000 SCF per barrel of oil and a hydrogen pressure between about 50 and 5,000 psi, incrementally increasing the temperature in said first zone within the range of about 690° to 790° F. to compensate for loss of catalyst activity with age until said catalyst is deactivated for hydrodesulfurization, passing desulfurized effluent oil and hydrogen from said first zone upwardly through a second zone containing deactivated hydrodesulfurization catalyst comprising supported Group VI and Group VIII metals under cracking conditions including a temperature above the hydrodesulfurization temperature up to 1,000° F., a hydrogen pressure between about 100 and 5,000 psi, a hydrogen flow rate between about 500 and 10,000 SCF per barrel of oil and an oil residence time between about 0.0014 and 5 hours to produce middle distillates, continuing said process until the catalyst in said first zone becomes deactivated, thereupon replacing said second zone catalyst with fresh hydrodesulfurization catalyst without replacing the catalyst in said first zone, and reversing flow in said process so that said second zone is operated in downflow under said hydrodesulfurization conditions and so that said first zone is operated in upflow under said cracking conditions.

Claim 8

A process comprising passing residual oil containing metals and sulfur together with hydrogen downflow through a first zone containing a packed bed of hydrodesulfurization catalyst comprising supported Group VI and Group VIII metals under hydrodesulfurization conditions including a space velocity between about 0.1 and 10 volumes of oil per volume of catalyst per hour, a hydrogen rate between about 500 and 10,000 SCF per barrel of oil and a hydrogen pressure between about 50 and 5,000 psi, incrementally increasing the temperature in said first zone within the range of about 690° to 790° F. to compensate for loss of catalyst activity with age until said catalyst is deactivated for hydrodesulfurization, passing desulfurized effluent oil and hydrogen from said first zone upwardly through a second zone containing deactivated hydrodesulfurization catalyst comprising supported Group VI and Group VIII metals under cracking conditions including a temperature above the hydrodesulfurization temperature up to 1,000° F., a hydrogen pressure between about 100 and 5,000 psi, a hydrogen flow rate between about 500 and 10,000 SCF per barrel of oil and an oil residence time between about 0.0014 and 5 hours to produce middle distillates, continuing said process until the catalyst in said first zone becomes deactivated, thereupon replacing said second zone catalyst with fresh hydrodesulfurization catalyst without replacing the catalyst in said first zone, and reversing flow in said process so that said second zone is operated in downflow under said hydrodesulfurization conditions and so that said first zone is operated in upflow under said cracking conditions.

Claim 9

The process of claim 6 including a flashing step between said zones.

Claim 10

The process of claim 6 wherein the hydrodesulfurization catalyst contains a non-cracking support.

Claim 11

The process of claim 6 wherein said hydrodesulfurization conditions include a hydrogen pressure above 1,000 psi, and the hydrogen pressure in the hydrodesulfurization step is above the hydrogen pressure in the cracking step.

Claim 12

The process of claim 6 wherein said oil residence time is between about 0.3 and 3 hours.