The reversible dissociation of ammonia is one of the candidate reactions fo
r use in closed loop solar thermochemical energy storage systems. The major
determinant of achievable performance for such a system is the degree of t
hermodynamic irreversibility associated with the heat recovery process. Exe
rgy analysis of a semi realistic 30 MPa isobaric system has revealed that t
he major irreversibilities occur within the exothermic reactor and the coun
terflow heat exchanger between ingoing and outgoing reactants. In this stud
y, optimum reactor control yielded exergetic efficiencies up to 71%, which
should translate to overall solar to electric conversion efficiencies of ar
ound 20%. (C) 1999 Elsevier Science Ltd All rights reserved.