Effect of mass transfer on the reaction rate in a monolithic catalyst with porous walls

Catalysis Today

Volumn 144, Issue 3-4, 2009, Pages 258-264

  Klenov, O P ^a   Pokrovskaya, S A ^a,b   Chumakova, N A ^a,b   Pavlova, S N ^a   Sadykov, V A ^a,b   Noskov, A S ^a  

^a BORESKOV INSTITUTE OF CATALYSIS   (Russian Federation)

^b NOVOSIBIRSK STATE UNIVERSITY   (Russian Federation)

Author keywords

Computational fluid dynamics; Monolithic catalyst; Porous wall; Reaction rate

Indexed keywords

CATALYST VOLUME; CATALYTIC REACTIONS; CHANNEL INLETS; CHANNEL LENGTH; CHANNEL WALL; DEEP OXIDATION; EFFECTIVENESS FACTOR; EXCHANGE PROCESS; FEED COMPONENTS; FRONTAL SURFACE; GAS FLOWS; GAS STREAMS; HETEROGENEOUS REACTIONS; MODEL REACTIONS; MONOLITHIC CATALYST; MONOLITHIC CATALYSTS; ORDERS OF MAGNITUDE; POROUS MONOLITHS; POROUS WALL; POROUS WALLS; REACTING FLOWS; REACTING GAS; SPATIAL DISTRIBUTION; STEAM REFORMING OF METHANE; TRANSFER PROCESS; TRIANGULAR CHANNEL;

AERODYNAMICS; CATALYSIS; CATALYST ACTIVITY; COMPUTATIONAL FLUID DYNAMICS; FLOW OF GASES; FLUID DYNAMICS; GASES; MASS TRANSFER; METHANE; REFORMING REACTIONS; STEAM ENGINEERING;

REACTION RATES;

EID: 66349105139     PISSN: 09205861     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cattod.2008.11.014     Document Type: Article

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