A system-level model combining heat and mass transport and chemical reaction is developed to study siliconcarbide-based uranium ceramic material processing. This process is based on pyrolysis and synthesis of a mixture of preceramic polymers and uranium oxide particles. Three key steps for polymer pyrolysis and one key reaction for uranium oxide and silicon carbide interaction are established for the processing. The mechanism of vapor species transport is described by introducing a driving force induced by both natural and forced convection. The effects of geometry of sample, driving force, and particle size and volume fraction of filler, uranium oxide, on the porosity evolution, species uniformity, and reaction rate of the sample are investigated. Nomenclature C p = specific heat at constant pressure, J=kg K d p = equivalent average particle diameter, m d = particle diameter, m E a = activation energy, J=mol f = volume fraction K = permeability, m 2 k = thermal conductivity, W=m K M = mass, kg n = ratio of diameter of large particles and small particles P = pressure, Pa q 00 = heat flux, W=m 2 _ R = reaction rate R = universal gas constant, 8.314 J=mol K r = radial coordinate T = temperature, K T" = tortuosity t = time, s u = velocity vector u r = radial velocity, m=s u z = axial velocity, m=s V = volume, m 3 Y = species mass fraction Z = preexponential H = heat of reaction, J=mol P 1 = driving force induced by natural convection, Pa P 2 = driving force induced by forced convection, Pa Z = elevation difference, m " m = emissivity " = porosity = viscosity, kg=m s = density, kg=m 3 Subscripts eff = effective g = gas r = radial direction s = mixed solid side = side surface top = top surface total = total 1 = surrounding 0 = reference 1 = first reaction, uranium oxide 2 = second reaction, polymer 3 = third reaction