Heat and Mass Balance on a Curing Oven
Aguey-Zinsou, Gilchrist
Promoteur(s) :
Toye, Dominique
Date de soutenance : 26-jan-2026 • URL permanente : http://hdl.handle.net/2268.2/25223
Détails
| Titre : | Heat and Mass Balance on a Curing Oven |
| Titre traduit : | [fr] Bilan de masse et de chaleur sur un four de cuisson |
| Auteur : | Aguey-Zinsou, Gilchrist
|
| Date de soutenance : | 26-jan-2026 |
| Promoteur(s) : | Toye, Dominique
|
| Membre(s) du jury : | Léonard, Angélique
Léonard, Grégoire
Niessen, Sébastien |
| Langue : | Anglais |
| Nombre de pages : | 148 |
| Mots-clés : | [en] Heat, Mass, transport phenomena |
| Discipline(s) : | Ingénierie, informatique & technologie > Ingénierie civile |
| Institution(s) : | Université de Liège, Liège, Belgique |
| Diplôme : | Master : ingénieur civil en chimie et science des matériaux, à finalité spécialisée en Chemical Engineering |
| Faculté : | Mémoires de la Faculté des Sciences appliquées |
Résumé
[en] Glass wool manufacturing requires simultaneous drying and curing of an impregnated glass wool
mat in a multi-zone conveyor oven.
This work develops a lumped-capacity model that couples heat and mass transfer mechanisms
with curing kinetics to predict the temperature profile and conversion level throughout the process.
The model uses a Number of Transfer Units formulation to model the cross-flow drying
process and implements an isoconversional kinetic model using Differential Scanning Calorimetry
data.
Heat transfer coefficients were computed from two years of production data and show discrepancies
that reflect the physical configuration of the oven. Simulations on 60 production runs showed
that the model captures the global temperature profile of the product by identifying three main
periods: preheating, constant-rate drying, and falling-rate periods where curing predominantly
occurs. Additionally, a sensitivity analysis of the most important parameters was performed to
assess and understand their impact on the drying process and the temperature profile of the mat.
When the outlet gas temperature is fixed from process data, the model achieves good agreement
with experimental observations. The conversion profile also shows physically consistent
behaviour as the final conversion increases with residence time under favourable temperature
conditions.
Several limitations were encountered, including the estimation of initial and critical moisture
content, the inability to capture internal diffusion that leads to thermal and material gradients
along the mat thickness, and uncertainty regarding the accuracy of the computed heat transfer
coefficients. To tackle one of these limitations, the critical moisture content was defined to
produce a transition between the constant drying rate period and the falling rate period that
matches the measured temperature profile.
Future work should focus on experimental determination of characteristic drying curves and development
of appropriate correlations that will enable accurate computation of transport properties.
Validation experiments in controlled pilot-scale equipment would also strengthen model predictions.
Finally, the lumped assumption can be relaxed by taking into account both heat and mass
transfer limitations along the mat thickness.
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