Nonlinear dynamics of a membrane reactor for hydrogen production: Multiplicity of equilibrium solutions and inhibition effects

Membrane reactors for the production of hydrogen are interesting devices that allow for the decentralized production of pure hydrogen while reducing the energy cost of the traditional steam reforming process. The performance of these systems is strongly dependent on the permeability and selectivity of the membrane employed for the separation of the produced hydrogen. Several studies have shown that the actual rate of hydrogen permeation is lower than the one that would be expected based on studies of membrane permeability carried out with pure hydrogen. This difference has been attributed to the competitive adsorption of other species, specifically CO, on the membrane surface. Here we show that this phenomenon could also lead to steady state multiplicity and analyze the dynamics of membrane reactors in the presence of competitive adsorption by CO. Emphasis has been placed on the effect of temperature and gas composition on possible multistable behavior. The results have been interpreted in terms of a transition between kinetics- and permeation-controlled regimes, in which the behavior of the reactor is limited, respectively, by the rate of the chemical reactions or the rate of hydrogen permeation. • Dynamics of membrane reactors in the presence of permeance inhibition were analyzed. • Effect of gas composition and temperature on multistable behavior was investigated. • Relationship between observed multistability and membrane inhibition was assessed. • Multistability due to competition between rate of H 2 production and permeation is observed.