In this work it presents an procedure for to simulate the behavior of a ideal binary mixture in a batch column with rectification in the mode of operation of a constant reflux.

In this work we show an analysis of the operation of inverted batch distillation column for ideal binary systems at constant reboil ratio.

In this work it presents an procedure for to simulate the behavior of a ideal binary mixture in a batch column with rectification in the mode of operation of a constant reflux.

In this work we show an analysis of the operation of inverted batch distillation column for ideal binary systems at constant reboil ratio.

It was prepared a bimetallic palladium–iron catalyst with support in carbon by the method of impregnation, following of drying and calcinations. The catalyst was characterized by DRX, Hydrogen DTP, TPR, BET and TEM. The test of the activity was made with the reaction of the hydrogenation of cronotaldehyde, obtained a selectivity to butanol of 23,65%.

It was prepared a bimetallic palladium–iron catalyst with support in carbon by the method of impregnation, following of drying and calcinations. The catalyst was characterized by DRX, Hydrogen DTP, TPR, BET and TEM. The test of the activity was made with the reaction of the hydrogenation of cronotaldehyde, obtained a selectivity to butanol of 23,65%.