This study focuses on an optimization of start-up operating conditions of a
rapid pressure swing adsorption (RPSA) process, which is operated in a cyc
lic pressure variation mode. The objective function is defined not only to
reduce the operating power but also to shorten the time to reach the cyclic
steady state (CSS), as well as to increase the purity of the desired produ
ct at CSS. A general mathematical model considering the dynamic variation a
nd spatial distribution of properties within the bed has been formulated an
d described by a set of integrated partial differential algebraic equations
(IPDAE). The number of variables for optimization is 16 825 and both the s
ingle discretization of a spatial domain and the double discretization of s
patial/time domains have been used for the numerical integration. As the co
mputation result the optimal cycle time is 14.46 s and the optimal feed pre
ssure is 597 kPa. Under the optimal condition the purity of desired product
at CSS is calculated as 96.42% and the CSS convergence rime is 5857 s. (C)
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