Oxidation experiments on the carbon preform of a phenolic-impregnated carbon ablator were performed in a flow-tube reactor facility, at temperatures between 700 and 1300 K, under dry air gas at pressures between 1.6 × 10 3 and 6.0 × 10 4 Pa. Mass loss, volumetric recession and density changes were measured at different test conditions. An analysis of the diffusion/reaction competition within the porous material, based on the Thiele number, allows identification of low temperature and low-pressure conditions to be dominated by in-depth volume oxidation. Experiments above 1000 K were found at transition conditions, where diffusion and reaction occur at similar scales. The microscopic oxidation behavior of the fibers was characterized by scanning electron microscopy and energy dispersive x-ray analysis. The material was found to oxidize at specific sites, forming a pitting pattern distributed over the surface of the fibers. Calcium-and oxygen-rich residues from the oxidation reactions were observed at several locations. Nomenclature A = preexponential factor, m∕s D = tube diameter, m D = diffusion coefficient, m 2 ∕s D = binary diffusion coefficient, m 2 ∕s Da = Damköhler number d = fiber or pore diameter, m E = energy, J∕mol G = Gibbs free energy, J∕mol k = reactivity, m∕s k B = Boltzmann constant, 1.3806488 × 10 −23 J∕K L = characteristic length, m l = length, m m = mass (also atomic or molecular mass), kg _ m = mass flow, kg∕s n = number density, m −3 p = pressure, Pa Q = cross section, m 2 R = ideal gas constant, 8.314 J∕mol · K Re = Reynolds number s = specific surface, m 2 ∕m 3 T = temperature, K u = axial velocity, m∕s V = volume, m 3 v = mean molecular velocity (agitation), m∕s w = wall thickness, m x, y, z, t = space and time coordinates, m and s, respectively x = mole fraction Δ = variation δ = thickness, m ε = porosity η = tortuosity λ = mean free path, m μ = dynamic viscosity, mP ρ = density, kg∕m 3 Φ = Thiele number Superscripts 0 = standard (1,1) = diffusion Subscripts a = activation b = bulk end = end e = entrance eff = effective f = fiber g = gas i, j = relative to species i or j K = Knudsen p = pore r = reaction ref = reference s = surface 0 = initial