The hydrogen production performance
of sorption-enhanced methane
steam reforming (SESMR) was investigated in this study. Three different
K2CO3-promoted hydrotalcites (HTCs), including
HTC A, industrial K2CO3-promoted HTC reported
in the work by Ding and Alpay (
Ding
Y.
Alpay
E.
Ding
Y.
Alpay
E.
Chem. Eng. Sci.20005534613474); HTC B, commercial HTC from SASOL impregnated with K2CO3 in the work by Oliveira et al. (
Oliveira
E. L. G.
Grande
C. A.
Rodrigues
A. E.
Oliveira
E. L. G.
Grande
C. A.
Rodrigues
A. E.
Sep. Purif. Technol.200862137147); and HTC C, commercial K2CO3-promoted
HTC from SASOL, were considered. A set of experiments was carried
out to measure CO2 adsorption on HTC C, and a one-dimensional
(1D) heterogeneous dynamic fixed-bed reactor mathematical model was
developed to simulate the performance of SEMSR. It was observed that
the CO2 adsorption characteristics were different among
the HTCs, resulting in different sorption-enhanced characteristic
curves. The reaction period that can be operated to produce the high-purity
hydrogen (99.99%) depends upon the sorbent type and operating conditions.
The increase of the steam/methane ratio leads to the increase of the
pre-breakthrough period. The increase of the operating pressure results
in the increase of the pre-breakthrough period when the S/C value
is high enough. The temperature of 863 K is suitable for the operation
at a low S/C value, while the temperature of 773 and 740 K is appropriate
for higher S/C values. The system using HTC B offers the best performance
with the pre-breakthrough period of 720 min at the following operating
conditions: F
tot, 0.73 mmol/min; T, 773 K; P, 0.2 MPa; S/C, 11.5; and catalyst/total
solid, 0.05, while the system with HTC A offers 126.67 min, which
is better than 20 min of HTC C.