Influence of Viscosity and Surface Tension on Performance of Gas-Liqid Contactors with Ejector Type Gas Distributor.

Kód výsledku v IS VaVaI

<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F67985858%3A_____%2F02%3A27020249" target="_blank" >RIV/67985858:_____/02:27020249 - isvavai.cz</a>

Výsledek na webu

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DOI - Digital Object Identifier

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Jazyk výsledku

angličtina

Název v původním jazyce

Influence of Viscosity and Surface Tension on Performance of Gas-Liqid Contactors with Ejector Type Gas Distributor.

Popis výsledku v původním jazyce

Effect of the liquid phase viscosity (0.7 to 25 mPa s) and surface tension (33 to 65 mN m-1) on hydraulic and mass transfer characteristics in a bubble column with an up-flow ejector-type gas distributor was studied. The coalescent character of the aqueous batches was changed by addition of a polymeric thickener, sucrose and an alcoholic foam breaker. Mass transfer was studied using steady-state physical absorption of air. Better performance of the ejector with swirl body for all tested liquid batches was achieved. Gas hold-up in the bubble column increased with increasing viscosity and surface tension in all batches. Mass transfer coefficient in the ejector decreased with increasing viscosity by 60% maximally in the maximum viscous coalescent batch. It was correlated within +_10% using the gas monodispersion model. Mass transfer coefficient in the column decreased with increasing viscosity by 30% maximally in the same coalescent viscous batch. It was correlated with large relative err

Název v anglickém jazyce

Influence of Viscosity and Surface Tension on Performance of Gas-Liqid Contactors with Ejector Type Gas Distributor.

Popis výsledku anglicky

Effect of the liquid phase viscosity (0.7 to 25 mPa s) and surface tension (33 to 65 mN m-1) on hydraulic and mass transfer characteristics in a bubble column with an up-flow ejector-type gas distributor was studied. The coalescent character of the aqueous batches was changed by addition of a polymeric thickener, sucrose and an alcoholic foam breaker. Mass transfer was studied using steady-state physical absorption of air. Better performance of the ejector with swirl body for all tested liquid batches was achieved. Gas hold-up in the bubble column increased with increasing viscosity and surface tension in all batches. Mass transfer coefficient in the ejector decreased with increasing viscosity by 60% maximally in the maximum viscous coalescent batch. It was correlated within +_10% using the gas monodispersion model. Mass transfer coefficient in the column decreased with increasing viscosity by 30% maximally in the same coalescent viscous batch. It was correlated with large relative err

Druh

J_x - Nezařazeno - Článek v odborném periodiku (Jimp, Jsc a Jost)

CEP obor

CI - Průmyslová chemie a chemické inženýrství

OECD FORD obor

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Projekt

<a href="/cs/project/GA104%2F97%2F1170" target="_blank" >GA104/97/1170: Vliv fyzikálních vlastností kapalné fáze na přenos hmoty mezi plynem a kapalinou v reaktorech s ejektorovými distributory</a><br>

Návaznosti

P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)<br>Z - Vyzkumny zamer (s odkazem do CEZ)

Rok uplatnění

2002

Kód důvěrnosti údajů

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

Název periodika

Chemical Engineering Science

ISSN

0009-2509

e-ISSN

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Svazek periodika

57

Číslo periodika v rámci svazku

15

Stát vydavatele periodika

GB - Spojené království Velké Británie a Severního Irska

Počet stran výsledku

8

Strana od-do

2987-2994

Kód UT WoS článku

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EID výsledku v databázi Scopus

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