초록 ▼

A liquid hydrocarbonaceous feedstock containing asphaltenes and optionally solids is hydroprocessed by passing the feedstock through a catalytic reaction zone in the presence of a catalyst bed containing a solid hydroprocessing catalyst under hydroprocessing conditions to produce a hydrocarbonaceous

A liquid hydrocarbonaceous feedstock containing asphaltenes and optionally solids is hydroprocessed by passing the feedstock through a catalytic reaction zone in the presence of a catalyst bed containing a solid hydroprocessing catalyst under hydroprocessing conditions to produce a hydrocarbonaceous effluent containing solids. Plugging of the catalyst bed is avoided by controlling the severity of the hydroprocessing conditions in the catalytic reaction zone to maintain the aliphatic hydrogen concentration of the liquid effluent sufficiently low to prevent substantial precipitation of asphaltenes within the catalytic reaction zone.

대표청구항 ▼

1. A process for avoiding catalyst bed plugging during the liquefaction of coal comprising the steps of: (a) passing a slurry comprising a hydrocarbonaceous liquid and particulate coal or coal-derived particles with hydrogen upwardly through a catalytic reaction zone in the presence of a packed b

1. A process for avoiding catalyst bed plugging during the liquefaction of coal comprising the steps of: (a) passing a slurry comprising a hydrocarbonaceous liquid and particulate coal or coal-derived particles with hydrogen upwardly through a catalytic reaction zone in the presence of a packed bed containing a solid hydroprocessing catalyst under hydroprocessing conditions to produce a hydrocarbonaceous liquid effluent containing insoluble solids; and (b) controlling the severity of the hydroprocessing conditions in said catalytic reaction zone to maintain the aliphatic hydrogen concentration of said hydrocarbonaceous liquid effluent sufficiently low to prevent substantial precipitation of n-heptane insoluble asphaltenes within said catalytic reaction zone. 2. A process according to claim 1 wherein substantially all of the slurry feed to said catalytic reaction zone is passed upwardly through said packed bed. 3. A process according to claim 1 wherein said packed bed is a fixed bed. 4. A process according to claim 3 wherein said packed bed is a moving bed. 5. A process according to claim 1, 2, 3, or 4 further comprising the step of measuring the aliphatic hydrogen concentration of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 6. A process according to claim 1, 2, 3 or 4 further comprising the step of measuring the hydrogen/carbon atomic ratio of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 7. A process according to claim 1, 2, 3, or 4 further comprising the step of measuring the n-heptane-insoluble asphaltene content of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 8. A process according to claim 1, 2, 3, or 4 further comprising the step of measuring the density of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 9. A process of claim 1, 2, 3, or 4 further comprising the step of measuring the viscosity of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 10. A process for avoiding catalyst bed plugging during the liquefaction of coal and the hydroprocessing of a heavy petroleum oil comprising the steps of: (a) passing a carbonaceous slurry comprising (1) heavy petroleum or heavy petroleum derived-oil, and (2) particulate coal or coal-derived particles with hydrogen upwardly through a catalytic reaction zone in the presence of a packed bed containing a solid hydroprocessing catalyst under hydroprocessing conditions to produce a hydrocarbonaceous liquid effluent containing insoluble solids; and (b) controlling the severity of the hydroprocessing conditions in said catalytic reaction zone to maintain the aliphatic hydrogen concentration of said hydrocarbonaceous liquid effluent sufficiently low to prevent substantial precipitation of n-heptane-insoluble asphaltenes within said catalytic hydrogenation zone. 11. A process according to claim 10 wherein substantially all of the carbonaceous slurry feed to said catalytic reaction zone is passed upwardly through said packed bed. 12. A process according to claim 10 wherein said packed bed is a fixed bed. 13. A process according to claim 10 wherein said packed bed is a moving bed. 14. A process according to claim 10, 11, 12, or 13 further comprising the step of measuring the aliphatic hydrogen concentration of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 15. A process according to claim 10, 11, 12, or 13 further comprising the step of measuring the hydrogen/carbon atomic ratio of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 16. A process according to claim 10, 11, 12, or 13 further comprising the step of measuring the n-heptane-insoluble asphaltene content of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 17. A process according to claim 10, 11, 12, or 13 further comprising the step of measuring the density of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step. 18. A process according to claim 10, 11, 12, or 13 further comprising the step of measuring the viscosity of said hydrocarbonaceous liquid effluent to provide a parameter for said controlling step.