The aim of this paper is to study of the thermal degradation of Tunisian olive stones by non-isothermal thermogravimetric analysis (TGA) device, under nitrogen atmosphere. Thermogravimetric analysis of different particles sizes (0.63-2.5mm) was evaluated. The effect of heating rates has been performed. Results showed that particles sizes don't have any effect on the pyrolysis of olive stones whereas the decomposition process is shifted to higher temperature zone with heating rate increasing. Three different kinetic models, the iso-conversional; kissinger-Akahira-Sunose, Ozawa-Flynn-Wall methods and Coats Redfern model were applied on TGA data of olive stones (OS) to calculate the kinetic parameters including activation energy, pre-exponential factor and reaction order. Simulation of olive stones pyrolysis using data obtained from TGA analysis showed good agreement with experimental data for all models. The dependence of the apparent activation energy determined using kissinger-Akahira-Sunose (KAS) and Ozawa-Flynn-Wall (OFW) methods, on the conversion degree reveals that pyrolysis progress rather through multi-steps kinetics.

A three-dimensional model with the COMSOL Multiphysics software was used to simulate the flow behavior in straight rectangular microchannels of 500

The conversion of sulfur dioxide into sulfur trioxide is a reaction which interests not only the industry of sulfuric acid production but also the processes of pollution control of certain gas effluents containing SO2. This exothermic reaction needs a very good control of temperature, that's why it is led in the industry in a multistage converter with intermediate heat exchangers. Microreactors represent a good alternative for such reaction due to their intensification of mass and heat transfer and enhancement of temperature control. In this study, this reaction was conducted in a stainless steel tubular (4mm ID) packed bed reactor using particles of vanadium pentoxide as catalyst at atmospheric pressure. Experiments were performed with different inlet SO2 concentration in 3-9% range and reaction temperature between 685-833K. We noticed that the conversion decreases with the amount of SO2 and increases with the temperature until an optimum, above this value the conversion drop according to the shape of the equilibrium curve. Controlling rate mechanism is studied by varying temperature. Pseudohomogeneous perfect plug flow is used to describe this small tubular reactor. Numerical simulations with MATLAB were performed to validate the experimental results. Good agreement between the model predictions and the experimental results is achieved. Fluid flow description inside the packed bed reactor was performed by using the free fluid and porous media flow model. This model was solved by the commercial software COMSOL Multiphysics. Velocity profile inside the reactor is theoretically obtained.