The effects of temperature and rotating speed of a feeding screw
on the key performance parameters (mass yield, energy yield, and energy
densification index) of torrefaction in a stationary reactor with
a feeding screw were studied. A comparative experiment of sorghum
straw pellet torrefaction was performed on a fixed tube furnace. The
results obtained from torrefaction in two reactors indicated that
the increase in temperature resulted in a decrease in mass yield and
energy yield. As the temperature increased, the volatile content in
the solid products decreased and the fixed carbon content increased,
indicating that the increase in temperature leads to a deeper degree
of biomass thermal degradation. The thermal degradation characteristics
of sorghum straw were supplemented by thermogravimetric experimental
results measured at 2.5, 5, 10, 20, 40, and 60 °C/min. Compared
with the fixed tube furnace, the pellets torrefied in the stationary
reactor with a feeding screw were heated more uniformly due to the
mechanical rotation of the feeding screw. The effect of the feeding
screw on the heat transfer mechanism in the stationary reactor was
analyzed based on the results of the torrefaction tests in the two
reactors. The temperature distribution in the stationary reactor with
a feeding screw was measured by five thermocouple measuring rods,
which were evenly installed at 0.05 m to the inner pipe wall along
the screw axis. It can be seen from the measured temperature profiles
that the heating rate of the pellets heated in the stationary reactor
with the feeding screw was variable. For the stationary reactor with
the feeding screw loaded with biomass pellets, the optimal rotating
speed of the feeding screw for torrefaction in the stationary reactor
can be estimated by temperature and the theoretical average heating
rate (HRestimation). Comparing the results obtained from
the torrefaction tests and thermogravimetric experiments, it can be
concluded that the optimal theoretical average heating rate is 4–4.5
°C/min.