Pressure swing adsorption is commercially used for the separation of air as
an alternative to the conventional cryogenic separation process. A zeolite
based process, in which the adsorbent shows preferential adsorption of nit
rogen over oxygen under equilibrium conditions, is used for the production
of oxygen. On the other hand, the separation of air for the production of n
itrogen is carried out by pressure swing adsorption over a carbon molecular
sieve. The separation is kinetically based, since the equilibrium adsorpti
on of both oxygen and nitrogen is very similar, but the oxygen is adsorbed
faster. In conventional pressure swing adsorption systems, both the product
ivity and yield decrease significantly as nitrogen purities are increased b
eyond 99.9 %. Although higher nitrogen purities were achievable, product fl
ows were so low that it was not an economically viable process. Only recent
ly, through both improvements in the manufacture of carbon molecular sieves
and new cycle developments, higher performance is achieved in the high pur
ity region. A theoretical dynamic model developed for the kinetic separatio
n of nitrogen from air is presented, and the effect of the different proces
s variables and cycle steps on the process performance is analyzed. A compa
rison between the experimental performance and the model predictions is dis
cussed.