In this work, the effects of coal-fired flue gas components
(O
2
, CO
2
, SO
2
, and NO) on the Hg
0
removal by the promising mercury removal adsorbent mechanochemical
S-modified petroleum coke were characterized and analyzed in terms
of the Hg
0
removal efficiency, mercury adsorption capacity,
and mercury mass balance. The results show that the mechanochemical
S-modified petroleum coke with a theoretical sulfur content of 21%
(named TSC-21) is the best candidate for mercury removal based on
the Hg
0
removal efficiency, Hg
0
removal capacity,
and difference ratio of Hg
0
removal capacity (anti-interference
ability) in the basic and full-component simulated flue gas atmosphere
(N
2
+ O
2
+ CO
2
, N
2
+ O
2
+ CO
2
+ SO
2
+ NO). The maximum value
(MV) and stable value (SV) of the Hg
0
removal efficiency
of TSC-21 in the basic simulated flue gas atmosphere are 99.25% (MV)
and 91.17% (SV), respectively. O
2
, CO
2
, and
NO all promote the Hg
0
removal by the adsorbent, but they
benefit the Hg
0
oxidation while inhibiting the Hg
0
adsorption. The promoting effect of O
2
on the Hg
0
removal by TSC-21 is affected by the reaction time, which
is especially obvious after 1 min. The presence of SO
2
inhibits
the oxidation and adsorption of Hg
0
, which in turn reduces
the Hg
0
removal performance of the adsorbent. The improving
effects on the oxidative escape of Hg
0
by CO
2
is higher than that by NO and O
2
. TSC-21 acts more as
an oxidant than an adsorbent for Hg
0
removal.