Process for hydrodesulfurizing or hydrogenating a hydrocarbon distillate

Claim 2

A process for desulfurizing a sulfurous hydrocarbon distillate containing mono-olefinic hydrocarbons and aromatics hydrocarbons which process comprises reacting said distillate with hydrogen in contact with a catalytic composite of from about 4 to about 30 weight percent Group VI-B metal, from about 0.1 to about 30 percent Group VIII metal and a refractory inorganic oxide carrier material which is prepared in the following manner: (a) dry mixing a finely divided Group VI-B metal compound, a Group VIII metal compound and a refractory inorganic oxide, said metal compound being utilized in an amount to provide from about 25 to about 90% of the Group VI-B metal component of the final catalytic composite, and from about 25 to about 90% of the Group VIII metal component; (b) peptizing the mixture and forming an extrudable dough; (c) extruding said dough and calcining the extrudate; (d) impregnating the calcined extrudate with a Group VI-B metal compound and a Group VIII metal compound, said metal compound being utilized in an amount to provide a final catalytic composite containing from about 4 to about 30 weight percent Group VI-B metal and from about 0.1 to about 10 weight percent Group VIII metal; and, (e) calcining the resulting composite in an oxidizing atmosphere.

Claim 3

A process for hydrogenating a coke-forming hydrocarbon distillate containing di-olefinic, mono-olefinic and aromatic hydrocarbons to hydrogenate di-olefinic hydrocarbons to monoolefinic hydrocarbons which process comprises reacting said distillate with hydrogen at a temperature below about 500° F. in contact with a catalytic composite of from about 4 to about 30 weight percent Group VI-B metal, from about 0.1 to about 30 weight percent Group VIII metal and a refractory inorganic oxide carrier material which is prepared in the following manner: (a) dry mixing a finely divided Group VI-B compound, a Group VIII metal compound and a refractory inorganic oxide, said metal compound being utilized in an amount to provide from about 25 to about 90% of the Group VI-B metal component of the final catalytic composite, and from about 25 to about 90% of the Group VIII metal component; (b) peptizing the mixture and forming an extrudable dough; (c) extruding said dough and calcining the extrudate; (d) impregnating the calcined extrudate with a Group VI-B metal compound and a Group VIII metal compound, said metal compound being utilized in an amount to provide a final catalytic composite containing from about 4 to about 30 weight percent Group VI-B metal and from about 0.1 to about 10 weight percent Group VIII metal; and, (e) calcining the resulting composite in an oxidizing atmosphere.

Claim 4

A process for hydrogenating a coke-forming hydrocarbon distillate containing di-olefinic, mono-olefinic and aromatic hydrocarbons to hydrogenate di-olefinic hydrocarbons to monoolefinic hydrocarbons which process comprises reacting said distillate with hydrogen at a temperature below about 500° F. in contact with a catalytic composite of from about 4 to about 30 weight percent Group VI-B metal, from about 0.1 to about 30 weight percent Group VIII metal and a refractory inorganic oxide carrier material which is prepared in the following manner: (a) dry mixing a finely divided Group VI-B compound, a Group VIII metal compound and a refractory inorganic oxide, said metal compound being utilized in an amount to provide from about 25 to about 90% of the Group VI-B metal component of the final catalytic composite, and from about 25 to about 90% of the Group VIII metal component; (b) peptizing the mixture and forming an extrudable dough; (c) extruding said dough and calcining the extrudate; (d) impregnating the calcined extrudate with a Group VI-B metal compound and a Group VIII metal compound, said metal compound being utilized in an amount to provide a final catalytic composite containing from about 4 to about 30 weight percent Group VI-B metal and from about 0.1 to about 10 weight percent Group VIII metal; and, (e) calcining the resulting composite in an oxidizing atmosphere.

Claim 5

A process for improving the jet fuel characteristics of a sulfurous kerosene boiling range fraction by reducing the sulfur content of said fraction which process comprises reacting said kerosene fraction and hydrogen at a maximum catalyst temperature of about 750° F. in a catalytic reaction zone containing a catalytic composite of from about 4 to about 30 weight percent Group VI-B metal, from about 0.1 to about 30 weight percent Group VIII metal and a refractory inorganic oxide carrier material which is prepared in the following manner: (a) dry mixing a finely divided Group VI-B metal compound, a Group VIII metal compound and a refractory inorganic oxide, said metal compound being utilized in an amount to provide from about 25 to about 90% of the Group VI-B metal component of the final catalytic composite, and from about 25 to about 90% of the Group VIII metal component; (b) peptizing the mixture and forming an extrudable dough; (c) extruding said dough and calcining the extrudate; (d) impregnating the calcined extrudate with a Group VI-B metal compound and a Group VIII metal compound, said metal compound being utilized in an amount to provide a final catalytic composite containing from about 4 to about 30 weight percent Group VI-B metal and from about 0.1 to about 10 weight percent Group VIII metal; and, (e) calcining the resulting composite in an oxidizing atmosphere.

Claim 6

A process for improving the jet fuel characteristics of a sulfurous kerosene boiling range fraction by reducing the sulfur content of said fraction which process comprises reacting said kerosene fraction and hydrogen at a maximum catalyst temperature of about 750° F. in a catalytic reaction zone containing a catalytic composite of from about 4 to about 30 weight percent Group VI-B metal, from about 0.1 to about 30 weight percent Group VIII metal and a refractory inorganic oxide carrier material which is prepared in the following manner: (a) dry mixing a finely divided Group VI-B metal compound, a Group VIII metal compound and a refractory inorganic oxide, said metal compound being utilized in an amount to provide from about 25 to about 90% of the Group VI-B metal component of the final catalytic composite, and from about 25 to about 90% of the Group VIII metal component; (b) peptizing the mixture and forming an extrudable dough; (c) extruding said dough and calcining the extrudate; (d) impregnating the calcined extrudate with a Group VI-B metal compound and a Group VIII metal compound, said metal compound being utilized in an amount to provide a final catalytic composite containing from about 4 to about 30 weight percent Group VI-B metal and from about 0.1 to about 10 weight percent Group VIII metal; and, (e) calcining the resulting composite in an oxidizing atmosphere.