CO2 capture via catalytic hydrogenation to methanol: Thermodynamic limit vs. 'kinetic limit

Catalysis Today

Volumn 172, Issue 1, 2011, Pages 158-165

  Fornero, Esteban L ^a   Chiavassa, Dante L ^a   Bonivardi, Adrian L ^a   Baltanás, Miguel A ^a  

^a Instituto de Desarrollo Tecnologico para la Industria Quimica   (Argentina)

Author keywords

Capture; Carbon dioxide; Fixed bed catalytic reactors; Methanol

Indexed keywords

ASYMPTOTIC RESPONSE; CAPTURE; CAPTURE CAPABILITY; CARBON OXIDE; CATALYTIC HYDROGENATION; FEED COMPOSITIONS; FEED FLOW RATE; FIXED-BED; FIXED-BED REACTORS; INDUSTRIAL CONDITIONS; NON-CONDENSABLE GAS; REACTING SYSTEM; RECYCLE RATIOS; SPECIFIC PRODUCTIVITY; THERMODYNAMIC EQUILIBRIA; THERMODYNAMIC LIMITS;

CATALYST ACTIVITY; CATALYST SELECTIVITY; CHEMICAL REACTORS; GALLIUM; HYDROGENATION; METHANOL; PRODUCTIVITY; RECYCLING; SILICON COMPOUNDS;

CARBON DIOXIDE;

EID: 80052263535     PISSN: 09205861     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cattod.2011.02.036     Document Type: Conference Paper

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