Underground coal
gasification (UCG) has its own reaction characteristics with the growth
of the combustion cavity because the coal seam is fixed while the
gasification face moves. The theoretical understanding of UCG requires
continuous and deep research. In order to explain the UCG mechanism
by means of simulation calculation, based on the analysis of the reaction
process of UCG, radial and axial reaction models are established.
The comprehensive heat transfer coefficient of the coal seam is determined
by comparing the calculation results with the field test results.
The differential method is used to calculate variations in the composition
of the outlet gas, the temperature field distribution in the channel,
the thickness of the radial reaction zone, and the influence of the
oxygen fraction on the length of the oxidation zone. The results indicate
that in one gasification cycle, the changes of gas composition is
close to that of the field test, which initially increases and then
decreases with increasing gasification time. The radial expansion
of the coal seam mainly occurs in the high-temperature zone, consistent
with the trend of the channel temperature field. The radial expansion
thickness in the coal seam is between 0.2 and 0.8 m. The higher the
oxygen fraction in the gasifying agent is, the shorter the range of
the oxygen distribution along the axial direction will be, that is,
the shorter the length of the oxidation zone.