A method for hydroprocessing deasphalted oil, comprising: performing solvent deasphalting with a C 4 solvent, a C 5 solvent, or a combination thereof, under effective solvent deasphalting conditions on a feedstock having a T5 boiling point of at least 400°C to form a first fraction comprising deasphalted oil and a solvent and a second fraction comprising deasphalter rock and the solvent, the effective solvent deasphalting conditions producing a yield of deasphalted oil of at least 50 wt% of the feedstock; recovering solvent from at least one of the first fraction and the second fraction, the recovering comprising generating heat for the recovering by combustion of a solvent recovery fuel comprising H 2; gasifying at least a portion of the deasphalter rock to form synthesis gas, the solvent recovery fuel comprising at least a portion of the synthesis gas; desulfurizing at least a portion of the synthesis gas; separating at least a portion of the desulfurized synthesis gas to form an H 2 -enriched stream; and hydroprocessing at least a portion of the deasphalted oil under first effective hydroprocessing conditions in the presence of an H 2 -containing gas to form a hydroprocessed effluent comprising a sulfur content of 500 wppm or less, the H 2 -containing gas comprising at least a portion of the H 2 -enriched stream separating the hydroprocessed effluent to form at least a fuels boiling range fraction and a bottoms fraction; hydroprocessing at least a portion of the hydroprocessed bottoms fraction under second effective hydroprocessing conditions, the second effective hydroprocessing conditions comprising hydrocracking conditions and catalytic dewaxing conditions, to form a catalytically dewaxed effluent comprising a 950°F+ (510°C+) portion having a VI of at least 80 and a pour point of -6°C or less; and at least one of: a) solvent extracting at least a portion of the catalytically dewaxed effluent to form a solvent processed effluent, and b) solvent dewaxing at least a portion of the catalytically dewaxed effluent to form a solvent processed effluent, wherein the catalytically dewaxed effluent is underdewaxed; wherein the solvent processed effluent comprising a cloud point of -2°C or less. performing solvent deasphalting with a C 4 solvent, a C 5 solvent, or a combination thereof, under effective solvent deasphalting conditions on a feedstock having a T5 boiling point of at least 400°C to form a first fraction comprising deasphalted oil and a solvent and a second fraction comprising deasphalter rock and the solvent, the effective solvent deasphalting conditions producing a yield of deasphalted oil of at least 50 wt% of the feedstock; recovering solvent from at least one of the first fraction and the second fraction, the recovering comprising generating heat for the recovering by combustion of a solvent recovery fuel comprising H 2; gasifying at least a portion of the deasphalter rock to form synthesis gas, the solvent recovery fuel comprising at least a portion of the synthesis gas; desulfurizing at least a portion of the synthesis gas; separating at least a portion of the desulfurized synthesis gas to form an H 2 -enriched stream; and hydroprocessing at least a portion of the deasphalted oil under first effective hydroprocessing conditions in the presence of an H 2 -containing gas to form a hydroprocessed effluent comprising a sulfur content of 500 wppm or less, the H 2 -containing gas comprising at least a portion of the H 2 -enriched stream separating the hydroprocessed effluent to form at least a fuels boiling range fraction and a bottoms fraction; hydroprocessing at least a portion of the hydroprocessed bottoms fraction under second effective hydroprocessing conditions, the second effective hydroprocessing conditions comprising hydrocracking conditions and catalytic dewaxing conditions, to form a catalytically dewaxed effluent comprising a 950°F+ (510°C+) portion having a VI of at least 80 and a pour point of -6°C or less; and at least one of: a) solvent extracting at least a portion of the catalytically dewaxed effluent to form a solvent processed effluent, and b) solvent dewaxing at least a portion of the catalytically dewaxed effluent to form a solvent processed effluent, wherein the catalytically dewaxed effluent is underdewaxed; a) solvent extracting at least a portion of the catalytically dewaxed effluent to form a solvent processed effluent, and b) solvent dewaxing at least a portion of the catalytically dewaxed effluent to form a solvent processed effluent, wherein the catalytically dewaxed effluent is underdewaxed; wherein the solvent processed effluent comprising a cloud point of -2°C or less.