Abstract

During the spray drying of detergent formulations, powder can accumulate on the inner walls of the spray drying tower. Under certain conditions, when the accumulations are large enough, self-heating can occur. This leads to unwanted charring and in severe cases to thermal runaway. In this study, basket heating methods, namely the steady-state approach and cross-point temperature method, were used to estimate the zero-order kinetics of the self-heating reaction of a typical detergent formulation. It was found that the resulting kinetics of these two methods were not in agreement, with this being attributed to the cross-point temperature method’s sensitivity to errors. The estimated kinetics were used in a 2D-axisymmetric transient model of heat transfer within an oven heated basket of detergent powder. Temperature-time profiles, and critical ambient temperatures, predicted by the model agreed well with experimental measurements. The model was also used to explore the value of using nth-order kinetics that were estimated using a thermogravimetric measurement technique. Theses kinetic showed no benefit over the zero-order kinetics and introduced unnecessary complexity. Future work will see this model and the insights gained applied to the problem of modeling self-heating in spray dryer wall accumulations.

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