Lube base oil were produced by catalytic dewaxing from hydrocracking tail oil of the Mao Ming Petrochemical Corporation in fixed catalytic bed reactor using NKC-7 as the dewaxing catalyst. The effects of reaction temperature (340~400 ℃) and space velocity( 1~8 h
-1) on the product distribution, solidifying point and liquid yield were studied. The results show that good product distribution and higher yield of lube base oil (61.4 % ) can be obtained at 380 ℃ and a space velocity of 2 h
-1, the solidifying point of lube base oil can reach -24 ℃.