Characterization of Foam Catalysts as Packing for Tubular Reactors.

Kód výsledku v IS VaVaI

<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F67985858%3A_____%2F16%3A00458697" target="_blank" >RIV/67985858:_____/16:00458697 - isvavai.cz</a>

Výsledek na webu

<a href="http://dx.doi.org/10.1016/j.cep.2016.04.001" target="_blank" >http://dx.doi.org/10.1016/j.cep.2016.04.001</a>

DOI - Digital Object Identifier

<a href="http://dx.doi.org/10.1016/j.cep.2016.04.001" target="_blank" >10.1016/j.cep.2016.04.001</a>

Jazyk výsledku

angličtina

Název v původním jazyce

Characterization of Foam Catalysts as Packing for Tubular Reactors.

Popis výsledku v původním jazyce

This study deals with the characterization of catalytically active foams as packing for continuous tubular reactors in terms of reactor performance and overall mass transfer. The tubular reactor was operated in a vertical direction such that gas and liquid entered the reactor in co-current upward flow. The hydrogenation reaction of α-methylstyrene was applied for characterization of the Pd/Al2O3 foam catalysts with a bed length of 50 cm and a diameter of 1.8 cm. Two pore densities for foams namely 30 and 45 PPI were investigated. The foam catalyst showed an overall mass transfer rate that ranged between 0.2 and 14 s-1 for 30 PPI and 0.3 to 18 s-1 for 45 PPI foam catalyst, whereas the energy dissipation was below 1 Wm-3.

Název v anglickém jazyce

Characterization of Foam Catalysts as Packing for Tubular Reactors.

Popis výsledku anglicky

This study deals with the characterization of catalytically active foams as packing for continuous tubular reactors in terms of reactor performance and overall mass transfer. The tubular reactor was operated in a vertical direction such that gas and liquid entered the reactor in co-current upward flow. The hydrogenation reaction of α-methylstyrene was applied for characterization of the Pd/Al2O3 foam catalysts with a bed length of 50 cm and a diameter of 1.8 cm. Two pore densities for foams namely 30 and 45 PPI were investigated. The foam catalyst showed an overall mass transfer rate that ranged between 0.2 and 14 s-1 for 30 PPI and 0.3 to 18 s-1 for 45 PPI foam catalyst, whereas the energy dissipation was below 1 Wm-3.

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

2016

Kód důvěrnosti údajů

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

Název periodika

Chemical Engineering and Processing: Process Intensification

ISSN

0255-2701

e-ISSN

—

Svazek periodika

105

Číslo periodika v rámci svazku

JUL 2016

Stát vydavatele periodika

CH - Švýcarská konfederace

Počet stran výsledku

9

Strana od-do

1-9

Kód UT WoS článku

000378366100001

EID výsledku v databázi Scopus

2-s2.0-85015607102