๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Liquid phase mass transfer resistance in a small scale packed distillation column

โœ Scribed by K.J. Arwikar; O.C. Sandall

Publisher
Elsevier Science
Year
1980
Tongue
English
Weight
701 KB
Volume
35
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.

โœฆ Synopsis

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 column It was shown in both cases that end-effects can be effecbvely removed by usmg a "dtierenhal height" technique It was observed in the dlstdlatlon expenments that the hqmd phase was saturated, mdlcatmg a neghsble resistance to mass transfer m the hqmd Results from the absorption expenments indicate that this resistance IS small but not neghgtble

๐Ÿ“œ SIMILAR VOLUMES

Simultaneous heat and mass transfer in a
Simultaneous heat and mass transfer in a packed binary distillation column
โœ Alain Honorat; Orville C. Sandall ๐Ÿ“‚ Article ๐Ÿ“… 1978 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 638 KB

A simultaneous heat and mass transfer model was applied to a binary system m a 3-m dtstdlatlon column packed with i m Raschlg Rings Mass transfer coefficients were obtained by measunng composmons and temperatures as functions of column height through use of the "dlfferentlal height" technique The ex

Effectiveness of mass transfer in a pack
Effectiveness of mass transfer in a packed distillation column in relation to surface tension gradients
โœ W.B. Patberg; A. Koers; W.D.E. Steenge; A.A.H. Drinkenburg ๐Ÿ“‚ Article ๐Ÿ“… 1983 ๐Ÿ› Elsevier Science ๐ŸŒ English โš– 582 KB

## Ah&act -In packed columns large differences occur in the wetting of the particles and especially in the refreshing of the liquid 011 the wetted particles due to gradients in surface tension of the liquid/gas interface. Mass transfer rates may die, with a factor 2. In a column packed with Berl s

CFD Simulation of Mass Transfer Efficien
CFD Simulation of Mass Transfer Efficiency and Pressure Drop in a Structured Packed Distillation Column
โœ M. Haghshenas Fard; M. Zivdar; R. Rahimi; M. Nasr Esfahani; A. Afacan; K. Nandak ๐Ÿ“‚ Article ๐Ÿ“… 2007 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 363 KB ๐Ÿ‘ 2 views

## Abstract The pressure drop and mass transfer efficiency for twoโ€phase flow in a structured packed column were simulated using a commercial CFD package, CFX version 10. The distillation of the methanol/isopropanol system was carried out in a 0.073โ€‰m diameter column, with an element composed of a