An existing side-fired steam reformer is simulated using a rigorous model w
ith proven reaction kinetics, incorporating aspects of heat transfer in the
furnace and diffusion in the catalyst pellet. Thereafter, "optimal" condit
ions, which could lead to an improvement in its performance, are obtained.
An adaptation of the nondominated sorting genetic algorithm is employed to
perform a multiobjective optimization. For a fixed production rate of hydro
gen from the unit, the simultaneous minimization of the methane feed rate a
nd the maximization of the flow rate of carbon monoxide in the syngas are c
hosen as the two objective functions, keeping in mind the processing requir
ements, heat integration, and economics. For the design configuration consi
dered in this study, sets of Pareto-optimal operating conditions are obtain
ed. The results are expected to enable the engineer to gain useful insights
into the process and guide him/her in operating the reformer to minimize p
rocessing costs and to maximize profits.