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Periodic cycling of distillation columns using a new tray design

Journal Article · · A.E.Ch.E. J.; (United States)
Computer simulations of periodically cycled columns predicted improvements in column performance of greater than 200% for systems with nonlinear equilibrium curves. Experiments distilling methanol-water mixtures have verified those predictions for periodic cycling with a single plate. The extension of the theory to multiple-plate columns fails in usual distillation apparatus due to liquid mixing during the liquid flow period. To overcome this problem a new tray design consisting of a sieve plate and inclined surfaces has introduced an effective liquid time delay. Although the predicted efficiencies of 200% were not realized due to vapor movement hindering the tray action, a wide range of operating conditions provided good overall column efficiencies of 140%.
Research Organization:
Department of Chemical Engineering, University of Sydney, NSW
OSTI ID:
6314498
Journal Information:
A.E.Ch.E. J.; (United States), Journal Name: A.E.Ch.E. J.; (United States) Vol. 31:11; ISSN AICEA
Country of Publication:
United States
Language:
English