Impacts of TGA furnace parameters for prediction of long-term thermal stability of ionic liquids

The concept of maximum operation temperature is established for the prediction of the time dependent thermal stability of ionic liquids based on kinetic evaluation of thermogravimetric analysis. The influence of the furnace control parameters on the maximum operation temperature (MOT) is shown using the example of 1-methyl-3-propylimidazolium iodide ([C(3)C(1)im]I) with respect to three different parameter sets of a programmed proportional integral derivative (PID) controller of the TGA. Kinetics of thermal decomposition of [[C(3)C(1)im]I have been investigated with the implementation of an improved kinetic model. The activation energy obtained using the Kissinger-Akahira-Sunose equation showed variations apparently due to the decomposition degree. The model compound is decomposed by a one-step kinetics, which results from pseudo zero order relationship of the activation energy to the conversion rate. The activation energy, pre-exponential factor, and the activation energy are strongly dependent on the parameters of TGA furnace controller.

Automated summary

By conducting kinetic evaluation through thermogravimetric analysis, the concept of maximum operation temperature has been successfully established for predicting the thermal stability of ionic liquids. The influence of furnace control parameters on thermal decomposition kinetics of 1-methyl-3-propylimidazolium iodide has been studied, showing variations in activation energy based on the degree of decomposition. The activation energy, pre-exponential factor, and the activation energy are highly dependent on the parameters of the TGA furnace controller.