A method for making lubricant base stock, comprising: performing solvent deasphalting using a C 3 solvent under effective solvent deasphalting conditions on a feedstock having a T5 boiling point of at least 400°C to produce deasphalted oil and rock, a yield of deasphalted oil being 40 wt% or less; hydroprocessing at least a portion of the deasphalted oil under first effective hydroprocessing conditions to form a hydroprocessed effluent, the at least a portion of the deasphalted oil having a kinematic viscosity at 100°C of at least 30 cSt, the hydroprocessed effluent having a sulfur content of 50 wppm or less and a nitrogen content of 20 wppm or less, the first effective hydroprocessing conditions comprising first hydrotreating conditions, first hydrocracking conditions and first aromatic saturation conditions, and comprising a first amount of conversion of the at least a portion of the deasphalted oil relative to 370°C, the first amount of conversion being 7 wt% to 25 wt%; separating the hydroprocessed effluent to form at least a fraction comprising fuels boiling range portion and a hydroprocessed bottoms fraction; and hydroprocessing at least a portion of the hydroprocessed bottoms fraction under second effective hydroprocessing conditions to form a catalytically dewaxed effluent, the second effective hydroprocessing conditions comprising second catalytic hydrotreating conditions, catalytic dewaxing conditions and second catalytic aromatic saturation conditions, and further comprising a second amount of conversion of the at least a portion of the hydroprocessed bottoms fraction relative to 370°C, the second amount of conversion being 10 wt% to 20 wt%, a yield of a 370°C+ portion of the catalytically dewaxed effluent being at least 50 wt% relative to the at least a portion of the deasphalted oil, wherein the 370°C+ portion of the catalytically dewaxed effluent comprises a VI of at least 100, a pour point of -10°C or less, and a kinematic viscosity at 100°C of 8 cSt to 20 cSt. performing solvent deasphalting using a C 3 solvent under effective solvent deasphalting conditions on a feedstock having a T5 boiling point of at least 400°C to produce deasphalted oil and rock, a yield of deasphalted oil being 40 wt% or less; hydroprocessing at least a portion of the deasphalted oil under first effective hydroprocessing conditions to form a hydroprocessed effluent, the at least a portion of the deasphalted oil having a kinematic viscosity at 100°C of at least 30 cSt, the hydroprocessed effluent having a sulfur content of 50 wppm or less and a nitrogen content of 20 wppm or less, the first effective hydroprocessing conditions comprising first hydrotreating conditions, first hydrocracking conditions and first aromatic saturation conditions, and comprising a first amount of conversion of the at least a portion of the deasphalted oil relative to 370°C, the first amount of conversion being 7 wt% to 25 wt%; separating the hydroprocessed effluent to form at least a fraction comprising fuels boiling range portion and a hydroprocessed bottoms fraction; and hydroprocessing at least a portion of the hydroprocessed bottoms fraction under second effective hydroprocessing conditions to form a catalytically dewaxed effluent, the second effective hydroprocessing conditions comprising second catalytic hydrotreating conditions, catalytic dewaxing conditions and second catalytic aromatic saturation conditions, and further comprising a second amount of conversion of the at least a portion of the hydroprocessed bottoms fraction relative to 370°C, the second amount of conversion being 10 wt% to 20 wt%, a yield of a 370°C+ portion of the catalytically dewaxed effluent being at least 50 wt% relative to the at least a portion of the deasphalted oil, wherein the 370°C+ portion of the catalytically dewaxed effluent comprises a VI of at least 100, a pour point of -10°C or less, and a kinematic viscosity at 100°C of 8 cSt to 20 cSt.