초록 ▼

Desulfurization, denitrogenation, deoxygenation and CCR reduction of highly aromatic petroleum and coal derived liquids are conducted with hydrogen and with a refractory base catalyst incorporating at least one Group VIA metal and at least one Group VIII metal. The catalyst has a surface area of bet

Desulfurization, denitrogenation, deoxygenation and CCR reduction of highly aromatic petroleum and coal derived liquids are conducted with hydrogen and with a refractory base catalyst incorporating at least one Group VIA metal and at least one Group VIII metal. The catalyst has a surface area of between about 100 and 300 m2/g and a total pore volume of between about 0.3 and 1.0 cc/g and is further characterized as follows: ________________________________ - Pore Volume Distribution, Volume % in Pores of ________________________________ 0-150 Angstroms diameter 20-40 150-200 Angstroms diameter 40-60 200+Angstroms diameter 10-30 ________________________________

대표청구항 ▼

A catalyst for the upgrading of a highly aromatic petroleum or coal derived liquid comprising at least one Group VIII metal or its oxides or sulfides and at least one additional member selected from the group consisting of chromium, molybdenum, tungsten, oxides thereof and sulfides thereof on a refr

A catalyst for the upgrading of a highly aromatic petroleum or coal derived liquid comprising at least one Group VIII metal or its oxides or sulfides and at least one additional member selected from the group consisting of chromium, molybdenum, tungsten, oxides thereof and sulfides thereof on a refractory support, said catalyst having a surface area of between about 110 and about 175 m2/g and a total pore volume of between about 0.5 and about 0.8 cc/g and being further characterized as follows: ________________________________ -Pore Volume Distribution, Volume % in Pores of ________________________________ 0-150 Angstroms diameter 25-35 150-200 Angstroms diameter 45-55 200+Angstroms diameter 10-30 ________________________________