To
evaluate and optimize a developed two-stage entrained flow bed
gasifier when it is used for the coal hydrogasification (CHG) process,
a series of comprehensive three-dimensional numerical simulations
designed with the orthogonal method are carried out. The effects of
different operating conditions, including the reaction pressure p, H2/coal mass ratio R
h/c, and O2/H2 mass ratio R
o/h on the fields and the evolution histories of the gasification
parameters as well as the carbon conversion rate (CCR), the CH4 mole fraction (MMF), and the cold gas efficiency (CGE) are
analyzed, and meaningful conclusions are obtained. The hydrogasifier
proposed in this work performs well. Counter flow can be detected
in the gasifier and is beneficial for char conversion. The gas temperature
and MMF increase with the height of the gasifier, while the hydrogen
mole fraction (HMF) decreases. The water mole fraction (WMF) increases
with the height of the gasifier if the gasification temperature is
high; otherwise, it will decreases slightly. The distribution of CH4 in the top zone of the reductor tends to be homogeneous with
the increase of R
o/h. Ranked in descending
order, the effect degrees of the operating conditions on CCR, MMF,
and CGE are R
o/h > p > R
h/c, p > R
h/c > R
o/h, and R
h/c > R
o/h = p, respectively. The optimum combinations of the operating
conditions
for CCR, MMF, and CGE are p = 7 MPa, R
h/c = 0.7, and R
o/h = 1.5; p = 7 MPa, R
h/c = 0.3, and R
o/h = 1.5; and p = 3 MPa (p = 5 MPa), R
h/c = 0.7, and R
o/h = 1.25, respectively. After comprehensive
analyses, a synthetically optimal combination of the operating condition
is proposed. With this condition, CCR can reach 96.78%, MMF can reach
17.42%, and CGE can reach 76.4%.