Modeling of in-line low-NOx calciners - a parametric study

Ion Iliuta, Kim Dam-Johansen, Anker Jensen, Lars Skaarup Jensen

Research output: Contribution to journalJournal articleResearchpeer-review

Abstract

Simulations with a heterogeneous model of an in-line low-NOx calciner, based on non-isothermal diffusion-reaction models for char combustion and limestone calcination combined with a kinetic model for NO formation and reduction, are reported. The analysis shows that the most important hydrodynamic parameter is the mixing rate of preheated combustion air into the sub-stoichiometric suspension leaving the reducing zone and the most important combustion parameter is the char reactivity. Also, the calcination rate modifies very much the temperature in the calciner, char and limestone conversion and NO emission. Carbon monoxide is a key component for the reduction of NO and reliable data for the kinetics of NO reduction by CO over CaO are very important for the prediction of the NO emission. The internal surface area of char and limestone particles influences the combustion and calcination rates and thereby the char and limestone conversion and the NO emission. (C) 2002 Elsevier Science Ltd. All rights reserved.
Original languageEnglish
JournalChemical Engineering Science
Volume57
Issue number5
Pages (from-to)789-803
ISSN0009-2509
Publication statusPublished - 2002

Cite this