초록 ▼

A method of producing a crude product from a hydrocarbon feed is provided. A hydrocarbon feed is contacted with a catalyst containing a Col. 6-10 metal or compound thereof to produce the crude product, where the catalyst has a pore size distribution with a median pore diameter ranging from 105 Å to

A method of producing a crude product from a hydrocarbon feed is provided. A hydrocarbon feed is contacted with a catalyst containing a Col. 6-10 metal or compound thereof to produce the crude product, where the catalyst has a pore size distribution with a median pore diameter ranging from 105 Å to 150 Å, with 60% of the total number of pores in the pore size distribution having a pore diameter within 60 Å of the median pore diameter, with at least 50% of its pore volume in pores having a pore diameter of at most 600 Å, and between 5% and 25% of its pore volume in pores having a pore diameter between 1000 Å and 5000 Å.

대표청구항 ▼

1. A method of producing a crude product, comprising: contacting a hydrocarbon feed with a catalyst to produce a total product that includes the crude product, wherein the catalyst comprises a metal from Col. 6-10 of the Periodic Table, or a compound thereof, or a mixture of the metal and a compound

1. A method of producing a crude product, comprising: contacting a hydrocarbon feed with a catalyst to produce a total product that includes the crude product, wherein the catalyst comprises a metal from Col. 6-10 of the Periodic Table, or a compound thereof, or a mixture of the metal and a compound thereof; wherein the catalyst has a median pore diameter ranging from 105 Å to 150 Å with at least 60% of the total number of pores in the pore size distribution having a pore diameter within at least 60 Å of the median pore diameter, with at least 50% of its pore volume in pores having a pore diameter of at most 600 Å, and between 5% and 25% of its pore volume in pores having a pore diameter between 1000 Å and 5000 Å, wherein pore diameters and pore volumes are as measured by ASTM Method D4284. 2. The method of claim 1, wherein the crude product is a liquid mixture at 25° C. and 0.101 MPa. 3. The method of claim 1, wherein the hydrocarbon feed has a viscosity of at least 100 cSt at 37.8° C. and the crude product is a liquid mixture at 25° C. and 0.101 MPa, and the method further comprises controlling contacting conditions such that the crude product has a viscosity at 37.8° C. of at most 90% of the viscosity of the hydrocarbon feed at 37.8° C., wherein viscosity is as determined by ASTM Method D445. 4. The method of claim 1, further comprises controlling contacting conditions at a total pressure at most 5 MPa and a temperature of at least 200° C. 5. The method of claim 1, wherein the crude product has a sediment content of at most 0.01 gram per gram of crude product. 6. The method of claim 1, wherein the method further comprises fractionating the crude product into one or more distillate fractions, and producing transportation fuel from at least one of the distillate fractions. 7. The method of claim 1 wherein the pore volume in pores of the catalyst is from 0.3 cm3/g to 0.99 cm3/g. 8. The method of claim 1 wherein the catalyst has a surface area of at least 200 m2/g as determined by ASTM Method D3663. 9. The method of claim 1 wherein the catalyst is sulfided prior to contact with the hydrocarbon feed. 10. The method of claim 1 wherein the catalyst is sulfided by contact of the catalyst with the hydrocarbon feed. 11. The method of claim 1 wherein the catalyst is obtained by co-mulling the Col. 6-10 metal with a support selected from the group consisting of alumina, silica-alumina, titanium oxide, zirconium oxide, magnesium oxide, and mixtures thereof. 12. The method of claim 1 wherein the catalyst has a bimodal pore size distribution.