Deactivation model for dry desulphurization of simulated flue gas with calcined limestone in a fluidized-bed reactor

Suyadal Y., Erol M., Oguz H.

FUEL, vol.84, no.12-13, pp.1705-1712, 2005 (SCI-Expanded) identifier identifier

  • Publication Type: Article / Article
  • Volume: 84 Issue: 12-13
  • Publication Date: 2005
  • Doi Number: 10.1016/j.fuel.2005.03.003
  • Journal Name: FUEL
  • Journal Indexes: Science Citation Index Expanded (SCI-EXPANDED), Scopus
  • Page Numbers: pp.1705-1712
  • Keywords: flue gas desulphurization, deactivation model, fluidized bed, SOLID REACTIONS, PORE STRUCTURE, SIZE MODEL, SO2, TEMPERATURE, ADSORPTION, DIFFUSION, KINETICS, SINGLE
  • Ankara University Affiliated: No

Abstract

In this work, dry desulphurization of simulated flue gas was investigated in a laboratory-scale stainless steel fluidized-bed reactor (46 X 500 rum 2) by using calcium-containing local Turkish limestone (Karaagach/MUS) which was calcined at 900 degrees C with 5% H2O vapour. The fluidized-bed reactor (FBR) was operated batchwise with a single charge of (15 g) particles for obtaining SO2 breakthrough curves. Experiments were carried out at different temperatures (600 <= T <= 900 C) and SO2 feedstock concentration (1000 <= C <= 6000 ppmSO(2)) within the range of space velocity (10,000 <= v <= 30,000 h(-1)). In addition, the effects of other components (O-2, CO2, H2O) in flue gas were investigated on the SO2 breakthrough curves. The deactivation model (DM) was tested for these curves by using the analogy between calcined limestone sulphation and the deactivation of catalyst particles. Observed surface reaction rate constant (k(S)) and first order deactivation rate constant (k(d)) were obtained from the model. It was found that the DM allows a good description of the experimental breakthrough curves without having to resort to prohibitively lengthy computer calculations compared to the so-called grain model (GM) and random pore model (RPM). (c) 2005 Elsevier Ltd. All rights reserved.