To study the temperature distribution
characteristics and evolution
law of underground lignite gasifiers, a three-dimensional heat conduction
model of underground lignite gasification was constructed. Moreover,
the effects of different coal thicknesses, advance speeds of the flame
working face, and surrounding rock types on the gasifier were analyzed.
The results show that with the increase in the coal thickness, the
transfer range and distance of temperature in the roof, floor, and
coal seam gradually increase, as does the coal quantity in the three
zones. The heat loss rate of the gasifier decreased gradually with
the coal seam thickness. When the advance speed of the flame working
face is 0.5 m/d, the ideal gasification coal thickness range of lignite
is 2.5–17.5 m. With the increase in the gasification rate,
the maximum transfer distance of temperature to the roof and floor,
the average temperature of the gasifier, and the coal quantity of
the three zones gradually increase. Conversely, the coal thickness
corresponding to the intersection of the coal quantity of the oxidation
and reduction zones and the heat loss rate of the gasifier gradually
decrease. When the coal seam below 2.5 m is gasified, the gasification
rate can be increased appropriately. When the coal seam is above 13
m, increasing the gasification rate will make the coal quantity in
the oxidation zone close to or even higher than that in the reduction
zone. Regarding the surrounding rock types comprising a combination
of siltstone, mudstone, sandy mudstone, and fine sandstone, the most
favorable roof and floor type for underground coal gasification is
the combination of fine sandstone and sandy mudstone (without considering
the sealing and mechanical properties). These results provide important
theoretical support for the industrialization of underground coal
gasification.