Fluid catalytic cracking (FCC) is an industrial process to convert heavy petroleum cuts into light products, such as gasoline and light olefins. In this research, a steady state one dimensional model of FCC riser using a four-lump kinetic model was presented. Equations for mass, momentum, and energy balances were written and coded by MATLAB. It is assumed that the catalyst particles in the riser are moving upward as clusters. Using the model, product yield, temperature profile in the riser, gas and solid velocity and catalyst decay rate along the riser were investigated. Obtained results are in good agreement with published industrial data.