Journal
APPLIED CATALYSIS A-GENERAL
Volume 303, Issue 1, Pages 131-137Publisher
ELSEVIER SCIENCE BV
DOI: 10.1016/j.apcata.2006.02.015
Keywords
hydrogen production; natural gas; sorbent enhanced steam reforming; dolomite; nickel catalyst; fluidized bed reactor
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High hydrogen yields can be obtained by sorbent enhanced steam reforming (SESR) of methane at temperatures below 600 degrees C by using calcined dolomite as internal sorbent together with a Ni/NiAl2O4 catalyst in a fluidized bed reactor. Effluent gas compositions containing > 90 mole.% H-2 are obtained, indicating that the sorbent acts efficiently after an induction period with low methane conversion. XRD examination of the catalyst/sorbent powder after different times-on-stream shows that during the induction period, CaO of the calcined dolomite reacts with water vapor to form Ca(OH)(2). The induction period is directly proportional to the time the catalyst/sorbent mixture is in contact with steam at temperatures below 600 degrees C where Ca(OH)(2) is thermodynamically stable. The catalyst/sorbent mixture can be regenerated at temperatures above 800 degrees C in H-2/N-2/H2O atmosphere. (c) 2006 Elsevier B.V. All rights reserved.
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