Liquid phase axial mixing in distillation column packed with structured packing: Effect on column performance
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F60461373%3A22340%2F19%3A43918683" target="_blank" >RIV/60461373:22340/19:43918683 - isvavai.cz</a>
Výsledek na webu
<a href="https://www.sciencedirect.com/science/article/pii/S0263876219302400?via%3Dihub" target="_blank" >https://www.sciencedirect.com/science/article/pii/S0263876219302400?via%3Dihub</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1016/j.cherd.2019.05.030" target="_blank" >10.1016/j.cherd.2019.05.030</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
Liquid phase axial mixing in distillation column packed with structured packing: Effect on column performance
Popis výsledku v původním jazyce
We present values of the Bodenstein number, Bo(L), characterizing liquid phase axial mixing, for the atmospheric distillation of three binary mixtures of primary alcohols and a mixture of cyclohexane/n-heptane, all of which were distilled in a column packed with Mellapak 250.Y or Mellapak 452.Y. In addition, volumetric mass transfer coefficients (k(L)a, k(G)a) were evaluated from the experimental composition profiles along the distillation column. To describe the distillation process, axial mixing in the phases was considered and modelled as axial dispersion. The results of our modelling call for a reassessment of the relative importance of the process-affecting phenomena. In particular, while vapour phase mass transfer resistance was confirmed as most important, liquid phase axial mixing is shown to have a significant impact under all conditions. For the C-6/C-7 mixture on Mellapak 452.Y, liquid phase mass transfer resistance was negligible when axial mixing was taken into account. Conversely, non-zero liquid phase mass transfer resistance was found for the alcohol mixtures in all cases. However, our investigation revealed that this is most likely a relic of the usage of the simplistic plug flow model. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
Název v anglickém jazyce
Liquid phase axial mixing in distillation column packed with structured packing: Effect on column performance
Popis výsledku anglicky
We present values of the Bodenstein number, Bo(L), characterizing liquid phase axial mixing, for the atmospheric distillation of three binary mixtures of primary alcohols and a mixture of cyclohexane/n-heptane, all of which were distilled in a column packed with Mellapak 250.Y or Mellapak 452.Y. In addition, volumetric mass transfer coefficients (k(L)a, k(G)a) were evaluated from the experimental composition profiles along the distillation column. To describe the distillation process, axial mixing in the phases was considered and modelled as axial dispersion. The results of our modelling call for a reassessment of the relative importance of the process-affecting phenomena. In particular, while vapour phase mass transfer resistance was confirmed as most important, liquid phase axial mixing is shown to have a significant impact under all conditions. For the C-6/C-7 mixture on Mellapak 452.Y, liquid phase mass transfer resistance was negligible when axial mixing was taken into account. Conversely, non-zero liquid phase mass transfer resistance was found for the alcohol mixtures in all cases. However, our investigation revealed that this is most likely a relic of the usage of the simplistic plug flow model. (C) 2019 Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
Klasifikace
Druh
J<sub>imp</sub> - Článek v periodiku v databázi Web of Science
CEP obor
—
OECD FORD obor
20401 - Chemical engineering (plants, products)
Návaznosti výsledku
Projekt
—
Návaznosti
S - Specificky vyzkum na vysokych skolach
Ostatní
Rok uplatnění
2019
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název periodika
Chemical Engineering Research and Design
ISSN
0263-8762
e-ISSN
—
Svazek periodika
148
Číslo periodika v rámci svazku
August
Stát vydavatele periodika
SG - Singapurská republika
Počet stran výsledku
13
Strana od-do
129-141
Kód UT WoS článku
000480374700011
EID výsledku v databázi Scopus
2-s2.0-85067386036