Article ID | Journal | Published Year | Pages | File Type |
---|---|---|---|---|
620409 | Chemical Engineering Research and Design | 2015 | 6 Pages |
Abstract
Results are presented of total reflux distillation experiments carried out with Montz-Pak B1-350MN in a 1.22Â m internal diameter column at Fractionation Research Inc. using two tests systems at two operating pressures, i.e. cyclohexane/n-heptane, at 0.31 and 1.62Â bar, and paraxylene/orthoxylene at 0.1 and 1Â bar, respectively. In all cases an impressive packing efficiency was achieved, ranging from five stages- at low to four stages per unit bed height at high vapour loads. Comparison with data obtained earlier with B1-250MN under similar conditions indicates a relatively higher maximum useful capacity of B1-350MN, while the relative efficiency and pressure drop are close to the ratio of installed specific geometric areas. The Delft model captures observed packing geometry related effects quite well qualitatively. Quantitatively, the efficiency and pressure drop predictions are on the safe side.
Keywords
Related Topics
Physical Sciences and Engineering
Chemical Engineering
Filtration and Separation
Authors
Ž. OlujiÄ, T. Rietfort, H. Jansen, E. Zich,