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A slurry hydroprocessing process for upgrading a hydrocarbon feedstock containing nitrogen and sulfur using bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals wherein the ratio of Group VIB metal to Group VIII metal is about 10:1 to abo

A slurry hydroprocessing process for upgrading a hydrocarbon feedstock containing nitrogen and sulfur using bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals wherein the ratio of Group VIB metal to Group VIII metal is about 10:1 to about 1:10.

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1. A slurry hydroprocessinig process which comprises hydroprocessing a hydrocarbon feedstock selected from the group comprising distillate and residual feedstocks containing nitrogen and sulfur, under effective slurry hydrotreating conditions, in the presence of a hydrogen containing treat gas and o

1. A slurry hydroprocessinig process which comprises hydroprocessing a hydrocarbon feedstock selected from the group comprising distillate and residual feedstocks containing nitrogen and sulfur, under effective slurry hydrotreating conditions, in the presence of a hydrogen containing treat gas and of a bulk multimetallic catalyst for upgrading said hydrocarbon feedstock, wherein said bulk multimetallic catalyst comprises of at least one Group VIII non-noble metal and at least two Group VIB metals and wherein the ratio of said at least two Group VIB metals to said at least one Group VIII non-noble metal is from about 10:1 to about 1:10. 2. The process of claim 1, wherein said bulk multimetallic catalyst is represented by the formula: (X)b(Mo)c(W)dOZ wherein X is a Group VIII non-noble metal, and the molar ratio of b: (c+d) is 0.5/1 to 3/1. 3. The process of claim 1, wherein said at least one Group VIII non-noble metal is selected from Ni and Co. 4. The process of claim 2, wherein said at least one Group VIII metal is Ni, and said bulk multimetallic catalyst has an X-ray diffraction pattern essentially amorphous with crystalline peaks at d=2.53 Angstroms and d=1.70 Angstroms. 5. The process of claim 1, wherein said bulk multimetallic catalyst is represented by the formula: (X)b(Mo)c(W)dOz wherein X is a Group VIII non-noble metal, and the molar ratio of b: (c+d) is 0.75/1 to 1.5/1 and the molar ratio of c:d is 1/10 to 10/1. 6. The process of claim 1 wherein said hydrocarbon feedstock is a distillate selected from the group consisting of a product of a petroleum, synfuel, coal, shale oil, bitumen, or a tar sand conversion process. 7. The process of claim 1, wherein said hydrocarbon feedstock is a distillate boiling range feedstock boiling in the range of about 175° to about 400° C. 8. The process of claim 1, wherein said slurry hydrotreating conditions include a temperature in the range of about 290 to 370° C., pressures from about 300 to 1200 psig, and hydrogen treat rates of about 200 to 2000 standard cubic feet per hour.