The Expanded Fluid (EF) viscosity model for Newtonian fluids is extended to crude oils characterized as mixtures of defined components and pseudo components The EF models take the fluid density, dilute gas viscosity, pressure, and fluid composition as inputs and requires three fluid specific parameters, c(2), c(3), and rho(s)degrees, for the fluid or its components. Generally, experimental viscosity data are required to determine these values for each component In this study, an internally consistent estimation method was developed to predict the fluid specific parameters of the model for hydrocarbons when no experimental viscosity data are available. The method uses n-paraffins as the reference system and correlates the fluid specific parameters for hydrocarbons as departures from the reference system. The method was evaluated against viscosity data of over 250 pure hydrocarbon compounds and petroleum distillation cuts. The model predictions were within the same order of magnitude of the measurements, with an overall average absolute relative deviation of 31%. The method was then used to calculate the correlation parameters for the pseudo-components of nine dead and live oils characterized on the basis of their gas chromatography (GC) assays. The viscosities of the crude oils were predicted within a factor of 3 of the measured values using the measured density of the oils as the input. The applicability of the EF model was also demonstrated using the densities determined with the Peng-Robinson equation of state. A simple method was proposed to tune the model to available viscosity data using a single multiplier to the c(2) parameter (and also to c(3) and rho(s)degrees if necessary) of the pseudo-components. Single-parameter tuning of the model improved the viscosity prediction for the characterized oils to within 30% of the measured values.