Patent Number: 053352521
Section: claims

1. In a vapor generator heat removal system for a nuclear power plant reactor, which produces required inlet vapor conditions for the main nuclear power plant turbine and for the nuclear power plant reheat turbine, while diverting a portion of superheated vapor to plant feed system heaters, one or more reheater tube bundles comprising a plurality of parallel heat transfer tube circuits located inside of a nuclear pressure vessel, said nuclear pressure vessel also containing a nuclear reactor core, and external to said nuclear pressure vessel a finishing superheater tube bundle comprising a plurality of parallel heat transfer tube circuits contained in a finishing superheater pressure vessel and an intermediate superheater tube bundle comprising a plurality of parallel heat transfer tube circuits contained in an intermediate superheater pressure vessel, such that said reheater tube bundles absorb heat from the reactor primary coolant into a secondary vapor medium flowing inside of the heat transfer tubes of said reheater tube bundles, said heat being sufficient in quantity and at sufficiently high temperature to increase the temperature of superheated vapor flowing inside of the heat transfer tubes of said finishing superheater tube bundle and said intermediate superheater tube bundle by the flow of said secondary vapor medium first through the shell side of said finishing superheater tube bundle and then through the shell side of said intermediate superheater tube bundle, to meet the vapor temperature, pressure and flow requirements of said main nuclear power plant turbine, while said reheat secondary vapor medium retains sufficient heat to meet the vapor temperature, pressure and flow requirements of said nuclear power plant reheat turbine. 2. The apparatus of claim 1 wherein the pressure of said secondary fluid medium is higher than the pressure of said reactor primary coolant thereby preventing leakage of radioactive materials into said secondary vapor medium. 3. The apparatus of claim 1 wherein the differential pressure across said reheater heat transfer tubes and other pressure bearing parts is sufficiently low to reduce creep stresses in said reheater heat transfer tubes to acceptable levels, thereby increasing the design temperature limits and the heat absorption capabilities of said reheater tube bundles. 4. The apparatus of claim 1 wherein materials having high temperature capability such as graphite, ceramics or alloy steels are used for said heat transfer tubes, other pressure bearing parts and structural components of said reheaters. 5. The apparatus of claim 1 wherein a portion of the superheated vapor flowing from the tube side outlet of the initial superheater tube bundle stage to the tube side inlet of said intermediate superheater tube bundle can be diverted to plant feed system heaters to increase the ratio of said secondary vapor medium flowing inside the heat transfer tubes of said reheaters to said superheated vapor flow entering the tube side of said intermediate superheater tube bundle, thereby reducing the maximum temperature requirement for vapor exiting from the tube side outlet of said reheater tube bundles. 6. The apparatus of claim 1 wherein a bypass system comprised of a pressure reducing valve, flash tank and other appropriate flow control components receives flow from the tube side inlet of said intermediate superheater tube bundle during start-up operation of the plant, separates said flow into vapor and liquid, and delivers said vapor flow to the tube side inlet of said reheater tube bundles, to be raised in temperature in said reheater tube bundles, while said liquid flow is drained from said flash tank to other plant systems. 7. In a vapor generator heat removal system for a nuclear power plant reactor, which produces required inlet vapor conditions for the main nuclear power plant turbine and for the nuclear power plant reheat turbine, while diverting a portion of superheated vapor to plant feed system heaters, one of more reheater tube bundles comprising a plurality of parallel heat transfer tube circuits, an initial superheater tube bundle stage comprising a plurality of parallel heat transfer tube circuits, and an economizer/evaporator tube bundle stage comprising a plurality of parallel heat transfer tube circuits, located within a nuclear pressure vessel, said nuclear pressure vessel also containing a nuclear reactor core, wherein the tube side inlets of said initial superheater tube bundle stage are connected in series to said economizer/evaporator tube bundle stage, while the tube side outlet of said initial superheater tube bundle stage is connected in series to the tube side inlet of an intermediate superheater tube bundle having a plurality of parallel heat transfer tube circuits contained in an intermediate superheater pressure vessel located outside of said nuclear pressure vessel, the tube side outlet of which is connected to the tube side inlet of a finishing superheater tube bundle having a plurality of parallel heat transfer tube circuits contained in a finishing superheater pressure vessel also located outside of said nuclear pressure vessel , such that the heat transfer tube surface area of said initial superheater tube bundle can be sized relative to the heat transfer tube surface area of said intermediate superheater tube bundle, thereby providing for the production of desired vapor conditions of flow, temperature and pressure at the tube side outlet of said reheater tube bundles, the heat transfer tube surface area of which is dependant upon the temperature of superheated vapor emerging from said initial superheater tube bundle stage. 8. The apparatus of claim 7 wherein a recirculation system comprised of a recirculation pump, inlet heat exchanger and other appropriate flow control components is provided to recirculate fluid from the tube side outlet of said initial superheater tube bundle stage to the tube side inlet of said economizer/evaporator tube bundle stage, wherein said recirculated fluid is mixed with incoming liquid flow from the plant feed system to said tube side inlet of said economizer/evaporator tube bundle stage, such that said recirculation system may be operated during low load and start-up operation of the plant and said recirculation system may be isolated during continuous operation of said plant at normal load to allow once-through flow through the tube side of said economizer/evaporator tube bundle stage, said initial superheater tube bundle stage, said intermediate superheater tube bundle, and said finishing superheater tube bundle. 9. The apparatus of claim 7 wherein a pipe connects the tube side outlet of said initial superheater tube bundle stage with the tube side inlet of said intermediate superheater tube bundle, said pipe producing mixing of flow emerging from said tube side outlet of said initial superheater tube bundle stage, thereby delivering flow at uniform temperature through said pipe to said tube side inlet of said intermediate superheater tube bundle. 10. The apparatus of claim 7 wherein said initial superheater tube bundle stage, said economizer/evaporator tube bundle stage, said intermediate superheater tube bundle, and said finishing superheater tube bundle are designed for internal pressure exceeding the critical pressure of the fluid being circulated through the tube side of said initial superheater and said economizer/evaporator tube bundle stages and through the tube side of said intermediate superheater and said finishing superheater tube bundles, critical pressure being defined as that pressure at which the phase change from liquid to vapor is temperature dependant and occurs without a change in density. 11. The apparatus of claim 7 wherein a portion of the superheated vapor flowing from the tube side outlet of said initial superheater tube bundle stage to the tube side inlet of said intermediate superheater tube bundle can be diverted to said plant feed system heaters to increase the ratio of reheat vapor flow to said superheated vapor flow entering the tube side of said intermediate superheater tube bundle, thereby reducing the maximum temperature requirement for vapor exiting from the tube side outlet of said reheater tube bundles. 12. In a vapor generator heat removal system for a nuclear power plant reactor, which produces required inlet vapor conditions for the main nuclear power plant turbine and for the nuclear power plant reheat turbine, one or more reheater tube bundles comprising a plurality of parallel heat transfer tube circuits, an economizer/evaporator tube bundle stage comprising a plurality of heat transfer tube circuits, and an initial superheater tube bundle stage located inside of a nuclear pressure vessel, said nuclear pressure vessel also containing a nuclear reactor core, and external to said nuclear pressure vessel an intermediate superheater tube bundle comprising a plurality of heat transfer tubes arranged in parallel tube circuits contained in an intermediate superheater pressure vessel, and a finishing superheater tube bundle comprising a plurality of heat transfer tubes arranged in parallel tube circuits contained in a finishing superheater pressure vessel, such that the tube side inlet of said intermediate superheater pressure vessel is connected to the tube side outlet of said initial superheater, the shell side inlet of said finishing superheater is connected to the tube side outlet of said reheater tube bundles, the tube side outlet of said intermediate superheater pressure vessel is connected to the tube side inlet of said finishing superheater pressure vessel, and the shell side outlet of said finishing superheater pressure vessel is connected to the shell side inlet of said intermediate superheater pressure vessel, such that the tube side of said intermediate superheater tube bundle and the tube side of said finishing superheater tube bundle comprise a series flow arrangement from the tube side outlet of said initial superheater tube bundle to the inlet of said plant main turbine, and the shell side of said finishing superheater tube bundle, and the shell side of said intermediate superheater tube bundle comprise a series flow arrangement from the tube side outlet of said reheater tube bundle to the inlet of said plant reheat turbine. 13. The apparatus of claim 12 wherein a pipe connects the tube side outlet penetration of said intermediate superheater pressure vessel with the tube side inlet of said finishing superheater pressure vessel, said pipe producing mixing of flow emerging from the tube side outlet of said intermediate superheater tube bundle, thereby delivering flow at uniform temperature through said pipe to the tube side inlet of said finishing superheater pressure vessel. 14. The apparatus of claim 12 wherein the tube material of said finishing superheater tube bundle is upgraded from the tube material of said intermediate superheater tube bundle to a material having higher allowable and design stress capability, said tube material change being effected by the placement of a bi-metallic weld at a location between the tube side outlet of said intermediate superheater tube bundle and the tube side inlet of said finishing superheater tube bundle. 15. The apparatus of claim 12 wherein said intermediate superheater pressure vessel and said finishing superheater pressure vessel, and said intermediate superheater tube bundle and said finishing superheater tube bundle, are designed for replacement of failed tubes and designed for in-service inspection and maintenance of heat transfer tubes and other components.