In the work presented
herein, a joint experimental and theoretical
approach has been carried out to obtain an insight into the desulfurization
performance of an industrial molecular sieve (IMS), resembling a zeolitic
structure with a morphology of cubic crystallites and a high surface
area of 590 m
2
g
–1
, with a view to removing
H
2
S from biogas. The impact of temperature, H
2
S inlet concentration, gas matrix, and regeneration cycles on the
desulfurization performance of the IMS was thoroughly probed. The
adsorption equilibrium, sorption kinetics, and thermodynamics were
also examined. Experimental results showed that the relationship between
H
2
S uptake and temperature increase was inversely proportional.
Higher H
2
S initial concentrations led to lower breakpoints.
The presence of CO
2
negatively affected the desulfurization
performance. The IMS was fully regenerated after 15 adsorption/desorption
cycles. Theoretical studies revealed that the Langmuir isotherm better
described the sorption behavior, pore diffusion was the controlling
step of the process (Bangham model), and that the activation energy
was 42.7 kJ mol
–1
(physisorption). Finally, the
thermodynamic studies confirmed that physisorption predominated.