Continuous dialysis of hydrochloric acid and sodium chloride mixture

Kód výsledku v IS VaVaI

<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F00216275%3A25310%2F17%3A39911297" target="_blank" >RIV/00216275:25310/17:39911297 - isvavai.cz</a>

Výsledek na webu

<a href="http://dx.doi.org/10.1080/01496395.2017.1363230" target="_blank" >http://dx.doi.org/10.1080/01496395.2017.1363230</a>

DOI - Digital Object Identifier

<a href="http://dx.doi.org/10.1080/01496395.2017.1363230" target="_blank" >10.1080/01496395.2017.1363230</a>

Jazyk výsledku

angličtina

Název v původním jazyce

Continuous dialysis of hydrochloric acid and sodium chloride mixture

Popis výsledku v původním jazyce

Using a two-compartment counter-current dialyzer with single passes, the simultaneous transport of hydrochloric acid and sodium chloride through an anion-exchange membrane Neosepta-AFN was studied at steady state. The diffusion dialysis process was quantified by four membrane mass transfer coefficients, which were correlated with the hydrochloric acid and sodium chloride concentrations in the feed. These characteristics were calculated from the experimental data on dialysis using a two-step procedure combining the numerical integration of the basic differential equations and a multivariable optimization. The second step of this procedure ensured the best agreement between the experimental and calculated data.

Název v anglickém jazyce

Continuous dialysis of hydrochloric acid and sodium chloride mixture

Popis výsledku anglicky

Using a two-compartment counter-current dialyzer with single passes, the simultaneous transport of hydrochloric acid and sodium chloride through an anion-exchange membrane Neosepta-AFN was studied at steady state. The diffusion dialysis process was quantified by four membrane mass transfer coefficients, which were correlated with the hydrochloric acid and sodium chloride concentrations in the feed. These characteristics were calculated from the experimental data on dialysis using a two-step procedure combining the numerical integration of the basic differential equations and a multivariable optimization. The second step of this procedure ensured the best agreement between the experimental and calculated data.

Druh

J_imp - Článek v periodiku v databázi Web of Science

CEP obor

—

OECD FORD obor

20402 - Chemical process engineering

Projekt

—

Návaznosti

I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace

Rok uplatnění

2017

Kód důvěrnosti údajů

S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Název periodika

Separation Science and Technology

ISSN

0149-6395

e-ISSN

—

Svazek periodika

52

Číslo periodika v rámci svazku

16

Stát vydavatele periodika

US - Spojené státy americké

Počet stran výsledku

11

Strana od-do

2611-2621

Kód UT WoS článku

000415729400012

EID výsledku v databázi Scopus

—