This paper presents an experimental investigation for an improved process of sorption-enhanced steam reforming of methane in an admixture fixed bed reactor. A highly active Rh/Ce alpha Zr1-alpha O2 catalyst and K2CO3-promoted hydrotalcite are utilized as novel catalyst/sorbent materials for an efficient H-2 production with in situ CO2 capture at low temperature (450-500 degrees C). The process performance is demonstrated in response to temperature (400-500 degrees C), pressure (1.5-6.0 bar), and steam/carbon ratio (3-6). Thus, direct production of high H-2 purity and fuel conversion >99% is achieved with low level of carbon oxides impurities (<100 ppm). A maximum enhancement of 162% in CH4 conversion is obtained at a temperature of 450 degrees C and a pressure of 6 bar using a steam/carbon molar ratio of 4. The high catalyst activity of Rh yields an enhanced CH4 conversion using much lower catalyst/sorbent bed composition and much smaller reactor size than Ni-based sorption enhanced processes at low temperature. The cyclic stability of the process is demonstrated over a series of 30 sorption/desorption cycles. The sorbent exhibited a stable performance in terms of the CO2 working sorption capacity and the corresponding CH4 conversion obtained in the sorption enhanced process. The process showed a good thermal stability in the temperature range of 400-500 degrees C. The effects of the sorbent regeneration time and the purge stream humidity on the achieved CH4 conversion are also studied. Using steam purge is beneficial for high degree of CO2 recovery from the sorbent. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.