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Model for Dynamic Liquid Hold-up in a Packed Distillation Column

✍ Scribed by Taiwo, Elijah A.; Fasesan, Samuel O.

Book ID
125974702
Publisher
American Chemical Society
Year
2004
Tongue
English
Weight
114 KB
Volume
43
Category
Article
ISSN
0888-5885

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πŸ“œ SIMILAR VOLUMES

Hold-up in packed liquid-liquid extracti
Hold-up in packed liquid-liquid extraction columns
✍ T. Sitaramayya; G.S. Laddha πŸ“‚ Article πŸ“… 1961 πŸ› Elsevier Science 🌐 English βš– 380 KB

A generalized correlation for hold-up of dispersed phase in packed liquid extraction columns has been derived and used to correlate the data of the present investigation in 2 in. column along with the reported data in 3 in. to 12 in. columns for a wide variety of liquid systems using different sizes

Hold-up prediction in packed columns for
Hold-up prediction in packed columns for co-current gasβ€”liquid downflow
✍ J.P. Reynier; J.C. Charpentier πŸ“‚ Article πŸ“… 1971 πŸ› Elsevier Science 🌐 English βš– 163 KB

Shorter Communications many authors, and the equation is identical to that derived by Lochiel and Calderbank [5]. For mass transfer to spherical drops or bubbles at high Reynolds number, the analysis of Moore [6] and Cheh and Tobias [7] can be applied to derive 2+3/~a/tLc l'45]t/~/.\_\_\_/bx.\_\_XlJ

Liquid phase mass transfer resistance in
Liquid phase mass transfer resistance in a small scale packed distillation column
✍ K.J. Arwikar; O.C. Sandall πŸ“‚ Article πŸ“… 1980 πŸ› Elsevier Science 🌐 English βš– 701 KB

## A&tract -Binary dlstdlatlon expenments usrng the toluen+tnchloroethylene system were conducted m a 3-m hameter column packed with 025m Raschlg rings In order to determine the hquld phase mass transfer charactenstlcs, gas absorption studies with COTwater system were also performed on the same co