Kinetic study of the chlorination of niobium oxide was carried out in a fix
ed-bed reactor under temperatures from 800 to 1000 degrees C and normal pre
ssure. Thermodynamic simulation was performed to analyze the reaction syste
m. Reactants introduced were niobium (V) oxide powder and gaseous chlorine
with carbon monoxide as reductant. The chlorination products were all in ga
seous phase under the temperatures and pressure studied. Reaction was of no
n-catalytic gas-solid nature and experimental data fitted the shrinking cor
e model. Rate expression and kinetic data were determined. (C) 1999 Elsevie
r Science S.A. All rights reserved.