In the present research work, numerical simulations were performed to investigate the effects of structural parameters on fluid flow and heat transfer under unsteady state conditions in aluminium foams, with various physical specifications such as different porosities (76-96%), pores diameter (100-500m) and tortuosity (1.024-1.14), by meshing computed micro-tomography images. In all the simulated cases, the fluid was considered as air with a temperature of 500K and different superficial velocities (1-6m/s) entered the foam with a temperature of 300K. Calculation of the pressure gradient based on a generic formula P/L=v+v(2) shows that by increasing porosity and pore diameter, coefficients and decrease. Moreover, heat transfer analysis shows that the average convection heat transfer coefficient (h(ave)) depends on the geometrical parameters of the foam and also on the superficial velocity of the fluid. In fact, the minor changes in the pore diameter can greatly affect h(ave) (e.g. the variation of h(ave) for samples with 86% porosity at inlet velocity of 5m/s and different pore diameters from 500 to 100m: 250 to 600J/m(2)sK). However, the porosity variations do not have significant effects on h(ave). On the other hand, by using the nonlinear least square fitting technique and also including the structural factor (F-s, function of the foam geometrical parameters) to the Nu correlation, the equation Nu=0.0305Re(0.77)F(s) [where F-s=((1-epsilon)/)(-0.27) (d(p)/d(t))(-5.108)] for determining the Nu in the different foams has been proposed. The equation and simulated results are agreed with each other very well and additionally are similar to the previous studies. Therefore, it's expected that this equation can be used in design and performance evaluation of porous heat exchangers and porous catalysts.