In this paper we perform a formal asymptotic analysis on a kinetic model for reactive mixtures in order to derive a reaction-diffusion system of Maxwell-Stefan type. More specifically, we start from the kinetic model of simple reacting spheres for a quaternary mixture of monatomic ideal gases that undergoes a reversible chemical reaction of bimolecular type. Then, we consider a scaling describing a physical situation in which mechanical collisions play a dominant role in the evolution process, while chemical reactions are slow, and compute explicitly the production terms associated to the concentration and momentum balance equations for each species in the reactive mixture. Finally, we prove that, under isothermal assumptions, the limit equations for the scaled kinetic model is the reaction diffusion system of Maxwell-Stefan type. 1 2. The continuum reaction-diffusion system of Maxwell-Stefan type In this section, we introduce a mathematical model for a reactive multi-species gaseous mixture in the context of continuum mechanics. The mixture is influenced by two processes, namely the diffusion, which causes the species to spread in space, and a chemical reaction, which results in the transformation of the species into each other. The model equations consist of the concentration balance equations for the reactive species in the mixture coupled with the MS equations for the momentum of the species. These equations describe how both processes affect the evolution of the mixture and will be referred to as the reaction-diffusion system of MS type.Let Ω ⊂ R 3 be a bounded domain with boundary denoted by ∂Ω and outward normal vector at each point x of the boundary given by ν(x). We consider a mixture of four species, say A 1 ,A 2 ,A 3 and A 4 , that participate in a chemical reaction of type(2.1)This means that species A 1 ,A 2 react to produce species A 3 ,A 4 and conversely, species A 3 ,A 4 also react to produce species A 1 ,A 2 . We say that A 1 ,A 2 and A 3 ,A 4 are the reactive species (or the reactive pairs), more specifically A 1 ,A 2 are reactants and A 3 ,A 4 are products of the forward chemical reaction. For each species A i , with i = 1,2,3,4, let ̺ i (t,x) ≥ 0 be the mass density, u i (t,x) the mean velocity and r i (t,x) the production rate of mass density due to the chemical reaction, where x ∈ Ω and t > 0.