A pulsed
fluidized bed system was established, targeting the analysis
of the drying and separation characteristics of fine lignite. Experiments,
involving factors of air velocity, pulsating frequency, and bed height
were conducted under room temperature to analyze the influence of
each factor on the separation characteristics of −6 + 3 mm
lignite and −3 + 1 mm lignite in a pulsed fluidized bed, respectively.
The combustible recovery and standard deviation of ash content were
implemented to evaluate the separation efficiency. Results show three
factors have a significant impact on the separation efficiency of
fine lignite. Afterward, the thermal energy characterized by inlet
temperature was imported into the pulsed fluidized bed system to study
the influence of inlet temperature, air velocity, pulsating frequency,
and bed height on the separation efficiency of fine lignite under
thermal conditions. Results show that the ash content of the top layer
product decreases significantly from 14.44% to 9.82% and from 15.52%
to 7.31% when the pulsating frequency increases from 0 Hz to 3.93 Hz under room temperature and thermal conditions
for −6 + 3 mm lignite, respectively. For −3 + 1 mm lignite,
the ash content of the top layer product decreases from 17.22% to
10.25% and from 16.77% to 10.01% under room temperature and thermal
conditions, respectively. Optimal operation parameters were determined.
With the air velocity of 1.09 m/s, inlet temperature of 80 °C, pulsating frequency of 3.93 Hz, and bed height of 120 mm, the optimal separation efficiency
was achieved for −6 + 3 mm lignite. For −3 + 1 mm lignite,
the optimal is achieved when air velocity, inlet temperature, pulsating
frequency, and bed height are 0.55 m/s, 100 °C, 3.49 Hz, and 80 mm. The separation
efficiency of lignite with a pulsed fluidized bed was dramatically
improved.