In order to understand the mechanism
of in situ combustion, many
studies have investigated the characteristics and properties of oxidized
coke and pyrolyzed coke. However, in earlier research, the influence
of light hydrocarbon and other compounds always led to a calculation
error in the activation energy. In the work described here, we produced
and separated oxidized coke and pyrolyzed coke, respectively, first
to eliminate the influence of impurity and, second, to examine their
properties by means of the TG-DSC equipment. The kinetic parameters
were calculated by the Ozawa–Flynn–Wall model. The results
showed that the crude oil achieved two major mass losses in the 300–400
and 500–600 °C temperature ranges, while the oxidized
coke and the pyrolyzed coke released more heat than crude oil in the
same conditions. At 300 and 350 °C, the high temperature can
cause the thermal pyrolysis of the crude oil because the generation
of coke requires more energy. These temperature levels cannot trigger
the generation of coke and thus the pyrolyzed products stayed in one
phase. At 400 °C, the pyrolyzed product cracked into two products:
light oil and coke. The generated coke could only achieve major mass
loss over 500 °C, releasing more heat than both oxidized oil
and crude oil. According to the Ozawa–Flynn–Wall model,
the crude oil achieved higher instantaneous activation energy at each
conversion rate compared to results for oxidized coke and pyrolyzed
coke. With the increase in conversion rate, the activation energy
of oxidized coke rose while that of pyrolyzed coke decreased slightly.