A method for producing a diesel fuel and a Group III base stock, comprising: providing a feed stock comprising a vacuum gas oil feed having a solvent dewaxed oil feed viscosity index of 60 to 150; hydrotreating the feed stock under first effective hydrotreating conditions to produce a first hydrotreated effluent; hydrotreating the first hydrotreated effluent under second effective hydrotreating conditions to produce a second hydrotreated effluent; fractionating the second hydrotreated effluent to produce at least a first diesel product fraction and a bottoms fraction; hydrocracking the bottoms fraction under effective hydrocracking conditions to produce a hydrocracked effluent; dewaxing the hydrocracked effluent under effective catalytic dewaxing conditions to produce a dewaxed effluent, the dewaxing catalyst including at least one non-dealuminated, unidimensional, 10-member ring pore zeolite, and at least one Group VI metal, Group VIII metal or combination thereof; hydrotreating the dewaxed effluent under third effective hydrotreating conditions to produce a third hydrotreated effluent; and fractionating the third hydrotreated effluent to form at least a second diesel product fraction and the Group III base stock product fraction, wherein - the Group III lubricant base stock product fraction includes 32 wt.% to 70 wt.% paraffins, greater than or equal to 90 wt. % saturates, a kinematic viscosity at 100°C between 5cSt and 7 cSt, a ratio of multi-ring naphthenes to single ring naphthenes (2R+N/1RN) of less than 0.52 and a ratio of branched carbons to straight chain (BC/SC) carbons less than or equal to 0.21; - the effective hydrotreating conditions include a temperature of 300°C. to 450° C., hydrogen partial pressure of 1500 psi to 5000 psi (10.3 MPa to 34.6 MPa), a liquid hourly space velocity of 0.2 hr-1 to 10 hr-1, and a hydrogen circulation rate of 35.6 m 3 /m 3 to 1781 m 3 /m 3 (200 scf/B to 10,000 scf/B).and - the effective hydrocracking conditions include a temperature of 280°C to 450°C, a hydrogen partial pressure of 1000 psig to 5000 psig (6.9 MPa to 34.6 MPa), a liquid hourly space velocity of 0.5 h -1 to 10 h -1, and a hydrogen treat gas rate of 35.6 m 3 /m 3 to 1781 m 3 /m 3 (200 scf/B to 10,000 scf/B). providing a feed stock comprising a vacuum gas oil feed having a solvent dewaxed oil feed viscosity index of 60 to 150; hydrotreating the feed stock under first effective hydrotreating conditions to produce a first hydrotreated effluent; hydrotreating the first hydrotreated effluent under second effective hydrotreating conditions to produce a second hydrotreated effluent; fractionating the second hydrotreated effluent to produce at least a first diesel product fraction and a bottoms fraction; hydrocracking the bottoms fraction under effective hydrocracking conditions to produce a hydrocracked effluent; dewaxing the hydrocracked effluent under effective catalytic dewaxing conditions to produce a dewaxed effluent, the dewaxing catalyst including at least one non-dealuminated, unidimensional, 10-member ring pore zeolite, and at least one Group VI metal, Group VIII metal or combination thereof; hydrotreating the dewaxed effluent under third effective hydrotreating conditions to produce a third hydrotreated effluent; and fractionating the third hydrotreated effluent to form at least a second diesel product fraction and the Group III base stock product fraction, wherein - the Group III lubricant base stock product fraction includes 32 wt.% to 70 wt.% paraffins, greater than or equal to 90 wt. % saturates, a kinematic viscosity at 100°C between 5cSt and 7 cSt, a ratio of multi-ring naphthenes to single ring naphthenes (2R+N/1RN) of less than 0.52 and a ratio of branched carbons to straight chain (BC/SC) carbons less than or equal to 0.21; - the effective hydrotreating conditions include a temperature of 300°C. to 450° C., hydrogen partial pressure of 1500 psi to 5000 psi (10.3 MPa to 34.6 MPa), a liquid hourly space velocity of 0.2 hr-1 to 10 hr-1, and a hydrogen circulation rate of 35.6 m 3 /m 3 to 1781 m 3 /m 3 (200 scf/B to 10,000 scf/B).and - the effective hydrocracking conditions include a temperature of 280°C to 450°C, a hydrogen partial pressure of 1000 psig to 5000 psig (6.9 MPa to 34.6 MPa), a liquid hourly space velocity of 0.5 h -1 to 10 h -1, and a hydrogen treat gas rate of 35.6 m 3 /m 3 to 1781 m 3 /m 3 (200 scf/B to 10,000 scf/B). - the Group III lubricant base stock product fraction includes 32 wt.% to 70 wt.% paraffins, greater than or equal to 90 wt. % saturates, a kinematic viscosity at 100°C between 5cSt and 7 cSt, a ratio of multi-ring naphthenes to single ring naphthenes (2R+N/1RN) of less than 0.52 and a ratio of branched carbons to straight chain (BC/SC) carbons less than or equal to 0.21; - the effective hydrotreating conditions include a temperature of 300°C. to 450° C., hydrogen partial pressure of 1500 psi to 5000 psi (10.3 MPa to 34.6 MPa), a liquid hourly space velocity of 0.2 hr-1 to 10 hr-1, and a hydrogen circulation rate of 35.6 m 3 /m 3 to 1781 m 3 /m 3 (200 scf/B to 10,000 scf/B).and - the effective hydrocracking conditions include a temperature of 280°C to 450°C, a hydrogen partial pressure of 1000 psig to 5000 psig (6.9 MPa to 34.6 MPa), a liquid hourly space velocity of 0.5 h -1 to 10 h -1, and a hydrogen treat gas rate of 35.6 m 3 /m 3 to 1781 m 3 /m 3 (200 scf/B to 10,000 scf/B).