Comparison of dual fluidized bed steam gasification of biomass with and without selective transport of CO2

Chemical Engineering Science

Volumn 64, Issue 23, 2009, Pages 5073-5083

  Pfeifer, C ^a   Puchner, B ^a   Hofbauer, H ^a  

^a VIENNA UNIVERSITY OF TECHNOLOGY   (Austria)

Author keywords

Absorption; Biomass; Energy; Gasification; Hydrogen; Synthesis gas

Indexed keywords

BED MATERIALS; BIO-MASS ENERGY; DUAL FLUIDIZED BED GASIFICATION; ENERGY; EXPERIMENTAL DATA; FLUIDIZED BED REACTORS; FLUIDIZED BED TECHNOLOGY; GASIFIERS; HYDROGEN CONTENTS; OPERATION TEMPERATURE; PRODUCER GAS; RESIDUAL BIOMASS; SELECTIVE TRANSPORT; STEAM GASIFICATION; THERMODYNAMIC DATA;

BIOMASS; CARBON MONOXIDE; CHEMICAL REACTORS; FLUID CATALYTIC CRACKING; FLUID DYNAMICS; FLUIDIZATION; FLUIDIZED BED PROCESS; FLUIDIZED BEDS; GAS ABSORPTION; GAS GENERATORS; GASIFICATION; HIGH PRESSURE EFFECTS; HYDROGEN; OXYGEN; PILOT PLANTS; SYNTHESIS GAS;

FLUIDIZED BED COMBUSTION;

EID: 71549136190     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2009.08.014     Document Type: Article

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