Simultaneous heat and mass transfer in a packed binary distillation column
β Scribed by Alain Honorat; Orville C. Sandall
- Publisher
- Elsevier Science
- Year
- 1978
- Tongue
- English
- Weight
- 638 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
β¦ Synopsis
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 experiments carried out with the toluene-tnchloroethylene system show that the hquld phase IS saturated indicating no resistance to mass transfer in the lquid phase Mass transfer coefficients obtained from the dlsullatlon experiments show agreement with mass transfer coefficients predicted from correlations of gas absorption data Bmary dlstlllatlon m contmuous contact equipment was modeled as a simultaneous heat and mass transfer
π SIMILAR VOLUMES
A theoretlcal study of sunultaneous heat and mass transfer m bmary dlstdlation has shown that heat and mass transfer coefficients can be appropnately evaluated If hqud phase temperatures and compositions are measured as funcuons of herght m a column In tlus study, the expenments were camed out m a w
AbstractBinary distillation in continuous contact equipment is modeled as a simultaneous heat and mass transfer process. In order to account for the interactions between heat and mass transfer between the two phases, the equations developed from enthalpy and material balances are analyzed simultaneo
A sunultaneous heat and mass transfer model was apphed to multlcomponent datdlatlon m a wetted-wall column Experunents were carried out. usmg the benzene-toluene-ethylbenzene ternary system, m a wetted-wall column of 2 2 cm I d and 100 cm long equipped with specml probes designed for simultaneous hq
## 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