Abstract: An electrogenerating device comprises a steam boiler, a hydrogen plant for steam conversion of natural gas into hydrogen, an oxygen plant for production of oxygen from air, a high-temperature H2/O2 steam superheater, a steam turbine provided with an electric power generator and a condenser, and a heat recovery boiler. Inlets of the high-temperature steam superheater are connected to an outlet of the steam boiler and outlets of the hydrogen and oxygen plants at a ratio of hydrogen to oxygen flow rates close to a stoichiometric ratio. The total noncondensable gas impurities in hydrogen and oxygen are less than 0.5% by volume at a temperature of 20 to 100° C. An outlet of the high-temperature steam superheater is connected to an inlet of the steam turbine, an outlet of the hydrogen plant is exhaust-gas connected to a gas path of the heat recovery boiler. In addition, an outlet of the heat recovery boiler is steam connected to an intermediate inlet of the steam turbine.

Abstract: An electrogenerating device comprises a steam boiler, a hydrogen plant for steam conversion of natural gas into hydrogen, an oxygen plant for production of oxygen from air, a high-temperature H2/O2 steam superheater, a steam turbine provided with an electric power generator and a condenser, and a heat recovery boiler. Inlets of the high-temperature steam superheater are connected to an outlet of the steam boiler and outlets of the hydrogen and oxygen plants at a ratio of hydrogen to oxygen flow rates close to a stoichiometric ratio. The total noncondensable gas impurities in hydrogen and oxygen are less than 0.5% by volume at a temperature of 20 to 100° C. An outlet of the high-temperature steam superheater is connected to an inlet of the steam turbine, an outlet of the hydrogen plant is exhaust-gas connected to a gas path of the heat recovery boiler. In addition, an outlet of the heat recovery boiler is steam connected to an intermediate inlet of the steam turbine.