Batch dialysis of phosphoric acid. Quantification of acid and water transport through Fumasep-FAD membrane
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F00216275%3A25310%2F19%3A39914862" target="_blank" >RIV/00216275:25310/19:39914862 - isvavai.cz</a>
Výsledek na webu
<a href="https://www.sciencedirect.com/science/article/pii/S1383586618334385?via%3Dihub" target="_blank" >https://www.sciencedirect.com/science/article/pii/S1383586618334385?via%3Dihub</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1016/j.seppur.2018.11.076" target="_blank" >10.1016/j.seppur.2018.11.076</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
Batch dialysis of phosphoric acid. Quantification of acid and water transport through Fumasep-FAD membrane
Popis výsledku v původním jazyce
Diffusion dialysis of model aqueous solutions of phosphoric acid was investigated in a two-compartment batch cell equipped with an anion-exchange membrane Fumasep-FAD. The transport of acid through the membrane was accompanied by a significant water transport in the same direction. In order to quantify both these phenomena, the permeability coefficient of the membrane for acid and proportionality coefficient between the flux of water and that of acid were determined from the experimental dependences of acid concentrations and liquid volumes in both the compartments upon time. This study proved that the membrane used is highly permeable for phosphoric acid, i.e., the permeability coefficient was found to be in the range from 0.67 x 10(-5) to 3.25 x 10(-5) m s(-1). Moreover, water transport can satisfactorily be quantified by only one proportionality coefficient with the value of 7.11.
Název v anglickém jazyce
Batch dialysis of phosphoric acid. Quantification of acid and water transport through Fumasep-FAD membrane
Popis výsledku anglicky
Diffusion dialysis of model aqueous solutions of phosphoric acid was investigated in a two-compartment batch cell equipped with an anion-exchange membrane Fumasep-FAD. The transport of acid through the membrane was accompanied by a significant water transport in the same direction. In order to quantify both these phenomena, the permeability coefficient of the membrane for acid and proportionality coefficient between the flux of water and that of acid were determined from the experimental dependences of acid concentrations and liquid volumes in both the compartments upon time. This study proved that the membrane used is highly permeable for phosphoric acid, i.e., the permeability coefficient was found to be in the range from 0.67 x 10(-5) to 3.25 x 10(-5) m s(-1). Moreover, water transport can satisfactorily be quantified by only one proportionality coefficient with the value of 7.11.
Klasifikace
Druh
J<sub>imp</sub> - Článek v periodiku v databázi Web of Science
CEP obor
—
OECD FORD obor
20402 - Chemical process engineering
Návaznosti výsledku
Projekt
—
Návaznosti
I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace
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
Separation and Purification Technology
ISSN
1383-5866
e-ISSN
—
Svazek periodika
212
Číslo periodika v rámci svazku
April
Stát vydavatele periodika
NL - Nizozemsko
Počet stran výsledku
6
Strana od-do
605-610
Kód UT WoS článku
000457814700068
EID výsledku v databázi Scopus
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