“…However, industrial devices such as furnaces with surfaces which permit emitted as well as incident radiation require convective-radiation effect coupled with a nonlocal boundary condition. 2,11,18 The constitutive law of the stress-tensor for the class of non-Newtonian fluids considered here as dependent on the temperature is σ = −πI + ν(·, θ)τ (D(u)), (1.1) where π denotes the pressure, I the identity matrix, ν the viscosity, θ the temperature, u the velocity of the fluid and D(u) = 1 2 (∇u+ ∇u T ) the symmetrized velocity gradient, and τ is the deviator stress-tensor defined such that τ : M n×n sym → M n×n sym is a continuous function which satisfies the conditions of p-coercivity…”