posted on 2020-03-13, 15:31authored byXiaohong Li, Pengju Huo, Yang Liu, Haiying Qi
The
load characteristics
of a large circulating
fluidized bed (CFB) coal gasifier were simulated by using the Eulerian–Eulerian
method with the generalized drag model, QC-EMMS. The simulations predicted
the gas–solid two-phase flows and coal gasification in a 60
m high CFB gasifier for 50, 80, and 100% loads. The results show that
the simulated pressure drop, temperatures, and syngas compositions
at the 50% load agree well with the field test data. The solid mass
circulation rate and the H2/CO ratio then increase linearly
with the increasing load. The average temperature in the riser decreases
slightly by 4% with the increasing load. The yield of effective syngas
per ton coal stabilizes at 465 Nm3/t for loads over 80%.
The study verifies that the QC-EMMS drag model can be used to accurately
simulate the complicated gas–solid reaction processes in a
large industrial CFB.