TY - JOUR
T1 - An analytical solution to equilibrium PSA cycles
AU - Chiang, Anthony S.T.
N1 - Funding Information:
Aknowledgement--This work has been supported in part by National Science Council of Taiwan, ROC through grant NSC-81-0402-E008-543.
PY - 1996
Y1 - 1996
N2 - A general pressure swing adsorption (PSA) cycle, involving pressure equalization, forward depressurization, incomplete purge, product backfill and feed pressurization steps, has been analyzed with an isothermal local equilibrium model assuming linear isotherms. The operation conditions of such a process could be characterized by the extents of feed, backfill and purge. Analytical expressions have been derived for the recovery ratio and the cycle throughput as a function of these extents. Critical conditions that ensure the formation of a simple shock and best utilization of column have also been identified. Product backfill plus pressure equalization steps were found the best policy when both recovery and throughput are important.
AB - A general pressure swing adsorption (PSA) cycle, involving pressure equalization, forward depressurization, incomplete purge, product backfill and feed pressurization steps, has been analyzed with an isothermal local equilibrium model assuming linear isotherms. The operation conditions of such a process could be characterized by the extents of feed, backfill and purge. Analytical expressions have been derived for the recovery ratio and the cycle throughput as a function of these extents. Critical conditions that ensure the formation of a simple shock and best utilization of column have also been identified. Product backfill plus pressure equalization steps were found the best policy when both recovery and throughput are important.
UR - http://www.scopus.com/inward/record.url?scp=0029731962&partnerID=8YFLogxK
U2 - 10.1016/0009-2509(95)00267-7
DO - 10.1016/0009-2509(95)00267-7
M3 - 期刊論文
AN - SCOPUS:0029731962
VL - 51
SP - 207
EP - 216
JO - Chemical Engineering Science
JF - Chemical Engineering Science
SN - 0009-2509
IS - 2
ER -