Using a hydrogen/oxygen steam generator it is possible to carry out many st
eam mixing re-heatings without increasing the complexity of a traditional s
team power-plant: steam is not required to re-enter the boiler for each re-
heating. An isothermal expansion could thus be approached by means of sever
al adiabatic expansions and several steam mixing re-heatings. A theoretical
investigation showed that an isothermal expansion could achieve high effic
iency (up to 70% of HHV) when the waste heat at the turbine outlet is recov
ered for pre-heating water, hydrogen and oxygen. In a real plant the number
of re-heatings that can be carried out, although high, is limited and we c
an therefore expect an efficiency drop which varies as a function of the nu
mber of re-hearings, the re-heating temperature and the maximum pressure. I
n order to evaluate real cycle performance, a numerical code. specifically
created, was implemented. (C) 2001 International Association for Hydrogen E
nergy. Published by Elsevier Science Ltd. All rights reserved.