Gas separation performance of carbon dioxide-selective poly(vinyl alcohol)-ionic liquid blend membranes: The effect of temperature, feed pressure and humidity.

Kód výsledku v IS VaVaI

<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F67985858%3A_____%2F21%3A00552480" target="_blank" >RIV/67985858:_____/21:00552480 - isvavai.cz</a>

Nalezeny alternativní kódy

RIV/60461373:22310/21:43923353 RIV/60461373:22340/21:43923353

Výsledek na webu

<a href="http://hdl.handle.net/11104/0327596" target="_blank" >http://hdl.handle.net/11104/0327596</a>

DOI - Digital Object Identifier

<a href="http://dx.doi.org/10.1016/j.seppur.2021.118812" target="_blank" >10.1016/j.seppur.2021.118812</a>

Jazyk výsledku

angličtina

Název v původním jazyce

Gas separation performance of carbon dioxide-selective poly(vinyl alcohol)-ionic liquid blend membranes: The effect of temperature, feed pressure and humidity.

Popis výsledku v původním jazyce

Membrane separation technology is rapidly emerging as an alternative to traditional gas separation processes, and increasingly challenging separations require a constant search for new and better-performing materials. This paper reports the gas separation performance of a poly (vinyl alcohol) (PVA) membrane blended with 53 wt% of the ionic liquid 1-ethyl-3-methyl-imidazolium dicyanamide ([EMIM][DCA]), known from our previous work as highly CO2/H-2 reverse-selective material, under different experimental conditions. The material properties of the solution-cast membranes are discussed and compared with the neat PVA polymer. Pure gas permeation measurements show a drastic increase of permeability for all gases (H-2, He, O-2, N-2, CH4, and CO2) compared to the neat polymer, with a change from diffusion-selective to sorption-selective behaviour. The gas permeability further increases over the temperature range from 25 degrees C to 55 degrees C and is accompanied by a decrease in selectivity for most gas pairs, in particular, CO2/N-2 and CO2/CH4, except for the H-2/CO2 gas pair. Mixed gas permeation measurements with the CO2/CH4 mixture show a beneficial effect of humidity on permeability and selectivity. This is supported by vapour sorption measurements, which show the high affinity of the membrane for water vapour and the vapour of lower alcohols.

Název v anglickém jazyce

Gas separation performance of carbon dioxide-selective poly(vinyl alcohol)-ionic liquid blend membranes: The effect of temperature, feed pressure and humidity.

Popis výsledku anglicky

Membrane separation technology is rapidly emerging as an alternative to traditional gas separation processes, and increasingly challenging separations require a constant search for new and better-performing materials. This paper reports the gas separation performance of a poly (vinyl alcohol) (PVA) membrane blended with 53 wt% of the ionic liquid 1-ethyl-3-methyl-imidazolium dicyanamide ([EMIM][DCA]), known from our previous work as highly CO2/H-2 reverse-selective material, under different experimental conditions. The material properties of the solution-cast membranes are discussed and compared with the neat PVA polymer. Pure gas permeation measurements show a drastic increase of permeability for all gases (H-2, He, O-2, N-2, CH4, and CO2) compared to the neat polymer, with a change from diffusion-selective to sorption-selective behaviour. The gas permeability further increases over the temperature range from 25 degrees C to 55 degrees C and is accompanied by a decrease in selectivity for most gas pairs, in particular, CO2/N-2 and CO2/CH4, except for the H-2/CO2 gas pair. Mixed gas permeation measurements with the CO2/CH4 mixture show a beneficial effect of humidity on permeability and selectivity. This is supported by vapour sorption measurements, which show the high affinity of the membrane for water vapour and the vapour of lower alcohols.

Druh

J_imp - Článek v periodiku v databázi Web of Science

CEP obor

—

OECD FORD obor

20402 - Chemical process engineering

Projekt

Výsledek vznikl pri realizaci vícero projektů. Více informací v záložce Projekty.

Návaznosti

P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)

Rok uplatnění

2021

Kód důvěrnosti údajů

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

Název periodika

Separation and Purification Technology

ISSN

1383-5866

e-ISSN

1873-3794

Svazek periodika

270

Číslo periodika v rámci svazku

SEP 1

Stát vydavatele periodika

GB - Spojené království Velké Británie a Severního Irska

Počet stran výsledku

9

Strana od-do

118812

Kód UT WoS článku

000652642100006

EID výsledku v databázi Scopus

2-s2.0-85106297238