In
this work, the thermal cracking process of seventeen (17) vacuum
residues from Colombian crude oils is studied. Cracking tests are
carried out in a batch microreactor at 390, 410, 420, and 430 °C,
during 60 min of reaction and in an inert atmosphere with nitrogen.
The quality of the vacuum residues and its products, obtained under
thermal cracking conditions, is determined by thermogravimetric analysis
and proton nuclear magnetic resonance (1H NMR) spectroscopy,
whereas the yield of liquid products is calculated via simulated distillation
following the ASTM D7169 standard. The thermogram trends show three
zones, one in the range of 100–300 °C, where few chemical
changes are observed, one between 300 and 550 °C, where the greatest
formation of volatile compounds occurs, and the third, in the range
of 550–900 °C, where the mass loss decreases to a constant
average weight of 14.8% (±6.3%). In contrast, the fractional
conversion curves show two reactivity zones corresponding to the vaporization
and thermal cracking stages, with activation energies ranging between
53.9–97.7 and 132.2–192.5 kJ/mol, respectively. It is
observed that the activation energy in the cracking zone increases
as the vacuum residues become heavier. The tendency of the distillation
curves for the liquid products shows a significant increase in the
525 °C fraction yield from each vacuum residue, with the increasing
reactivity temperature of the thermal cracking. The analysis of the
average molecular parameters via 1H NMR confirms that the
reactivity and product yield vary according to the complexity of the
molecular structure in the vacuum residues. On the other hand, the
results of this research contribute to the development of a methodology
of reactivity and compositional characterization by using 1H NMR spectroscopy and multivariate models to evaluate the thermal
cracking effect of vacuum residues on a laboratory scale.