Operating hydrogen plants efficiently is a critical issue, central to any e
nergy conservation exercise in petroleum refining and fertilizer industries
. To achieve this goal, "optimal" operating conditions for improved unit pe
rformance need to be identified. In this work, an entire industrial hydroge
n plant is simulated using rigorous process models for the steam reformer a
nd shift converters. An adaptation of the nondominated sorting genetic algo
rithm (NSGA) is then employed to perform a multi-objective optimization on
the unit performance. Simultaneous maximization of product hydrogen and exp
ort steam flow rates is considered as the two objective functions for a fix
ed feed rate of methane to the existing unit. For the specified plant confi
guration, Pareto-optimal sets of operating conditions are successfully obta
ined by NSGA for different process conditions. The results serve as a targe
t for the operator to aim at, in order to achieve cost effective operation
of hydrogen plants. (C) 2001 Elsevier Science Ltd. All rights reserved.