The endothermic decomposition of natural gas into a carbon-rich condensed p
hase and a hydrogen-rich gas phase, using concentrated solar energy as the
source of high-temperature process heat, is considered as a model reaction
for conducting a 2nd-law analysis of a solar decarbonization process in whi
ch carbon is removed from fossil fuels prior to their use for power generat
ion. The theoretical maximum closed-cycle exergy efficiency, defined as the
ratio of the Gibbs free energy change of the reaction to the solar power i
nput, can be as high as 35% for a black-body solar cavity-receiver/reactor
operating at 1500 K and under a mean solar flux concentration ratio of 1000
, and decreases to 21% if the products exiting the solar reactor are quench
ed without recovering their sensible heat. Four technically viable routes a
re examined for extracting power from the chemical products of the solar de
composition of CH4: (1) carbon is sequestered and only H-2 is used in a fue
l cell; (2) carbon is used to fuel a conventional Rankine cycle and H-2 is
used in a fuel cell; (3) carbon is steam-gasified to syngas in a solar gasi
fication process and the syngas further processed to H-2, which, together w
ith H-2 from the CH4-decomposition reaction, is used in a fuel cell; and (4
) carbon serves as a reducing agent of ZnO in a solar carbothermic process
for producing Zn and CO that are further converted via water-splitting and
water-shifting reactions to H-2 for use in a fuel cell, The open-cycle ener
gy efficiency, defined as the ratio of electric power output to the thermal
energy input (solar + heating value of reactants), exceeds 65% for the 3rd
and 4th power generation routes. Both of these routes offer a net gain of
40% in the electrical output and, consequently, an equal percent reduction
in the corresponding Specific CO2 emissions, vis-A-vis the direct use of CH
4 for fueling a 55%-efficient combined Brayton-Rankine cycle. For route nr.
1, the energy penalty for avoiding CO2 emissions amounts to 30% of the ele
ctrical output. (C) 2001 International Association for Hydrogen Energy. Pub
lished by Elsevier Science Ltd. All rights reserved.