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Biomass gasification with steam in fluidized bed: Effectiveness of CaO, MgO, and CaO-MgO for hot raw gas cleaning

Journal Article · · Industrial and Engineering Chemistry Research
DOI:https://doi.org/10.1021/ie960273w· OSTI ID:509348
;  [1];  [2]
  1. Univ. of Saragossa (Spain). Dept. of Chemical and Environmental Engineering
  2. Univ. Complutense of Madrid (Spain). Dept. of Chemical Engineering
The upgrading of the raw hot gas from a bubbling fluidized bed biomass gasifier is studied using cheap calcined minerals or rocks downstream from the gasifier. Biomass gasification is made with steam (not air) at 750--780 C and about 0.5--1.0 kg of biomass/h. Calcined solids used are dolomite (MgO-CaO), pure calcite (CaO), and pure magnesite (MgO). Variables studied have been temperature of the secondary bed (780--910 C), time of contact or space-time of the gas (0.08--0.32 kg{center_dot}h/m{sup 3}n), and particle diameter (1--4 mm) and type of mineral. Their effects on tar conversion, tar amount in the exit gas, product distribution, and gas composition are presented. Using a macrokinetic model for the tar disappearance network, the activities of the stones are expressed by their apparent kinetic constant. Apparent energies of activation for tar elimination (42--47 kJ/mol) and preexponential and effectiveness factors are given for all tested solids of which the most active is the calcined dolomite.
Sponsoring Organization:
DGICyT (Spain)
OSTI ID:
509348
Journal Information:
Industrial and Engineering Chemistry Research, Journal Name: Industrial and Engineering Chemistry Research Journal Issue: 5 Vol. 36; ISSN IECRED; ISSN 0888-5885
Country of Publication:
United States
Language:
English

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