Oil
sludge (OS) pyrolysis was conducted with a tube furnace reactor.
Production distributions and compositions were investigated under
different conditions of pyrolysis temperature, heating mode, and atmosphere
(N2/CO2). Little change was detected with the
product yields of char, oil, and gas when the final temperature exceeded
600 °C. Compared with slow pyrolysis, oil and char yields decreased
and gas yield increased in fast pyrolysis. CO2 could promote
OS pyrolysis, resulting in a reduction of char yield. SEM images showed
that the surface of OS was smooth with a dense texture while the surface
of OS char was rough with a well-developed pore structure that formed
after pyrolysis. Simulated distillation results showed that light
fractions from OS pyrolysis were more than 30% higher than those of
oil from OS extraction. With the increase of pyrolysis temperature,
light fractions (gasoline, diesel, and jet fuel) in pyrolysis oil
decreased. During fast pyrolysis, the heavy fractions produced can
be cracked into light fractions. The content of light fractions was
46% compared with 34% for oil from slow pyrolysis. It did not differ
much with the oil product distributions from pyrolysis in inert (N2) and CO2 atmosphere. The yields of C4–6 and C6 were higher than those of CH4 in slow
pyrolysis between 500 and 700 °C. Fast pyrolysis and CO2 atmosphere favored the conversion of stable macromolecules to short
chain methyl compounds, resulting in a higher CH4 yield.