A steam turbine power plant utilizing high temperature high efficiency industrial heat pumps (IHP) to preheat boiler feedwater is disclosed. The typical extraction steam feedwater preheater is replaced by a plurality of series connected heat pumps that produce boiler feedwater by preheating pressurized condensate from a feedwater pump attached to a condensate receiver. A stack economizer extracts waste heat from boiler flue gas to provide a closed loop of hot source water to the heat pumps. The Heat Rate of the power plant will be reduced by approximately 7%. By using leaving condenser water as source water for the lower temperature stage heat pumps, some of the liberated high temperature source water can be diverted to a new boiler combustion air preheater. The combination of feedwater preheating heat pumps plus a boiler combustion air preheater will reduce the Heat Rate of the power plant by approximately 12%.

A method for starting a vertical forced-flow steam generator in a waste-heat steam generator, wherein feed water is fed to the forced-flow steam generator as working fluid, and there flows firstly through a feed-water preheater and then through an evaporator and is at least partly evaporated, wherein the partly evaporated working fluid is fed to a water separation system, in which non-evaporated working fluid is separated from evaporated working fluid and is collected, in which at least part of the non-evaporated working fluid is fed geodetically to the evaporator and, beginning from a certain quantity of accumulating non-evaporated working fluid, a remaining part is automatically removed from the water separation system. A corresponding device is for starting a vertical forced-flow steam generator according to the method.

A condensate and feedwater system includes: a deaerator circulation pump that returns condensate water flowing out from a deaerator to a part of a condensate line between a heater and the deaerator; an apparatus to be supplied with part of the condensate water flowing from the heater toward the deaerator, through a supply line branched from the condensate line; a supply line shutoff valve that switches between communication and interruption of the supply line; and a controller that controls opening/closing of the supply line shutoff valve and driving/stopping of the deaerator circulation pump. The controller closes the supply line shutoff valve from an open state at normal operation and at least temporarily drives the deaerator circulation pump from a stopped state at normal operation, in condenser throttling in which supply of extraction steam of a steam turbine to the heater and the deaerator is reduced as compared to that at normal operation and a deaerator water level control valve is closed.

An all-condition auxiliary denitration system and an operation method thereof are provided. The system includes a heat-storage medium heater, a low-temperature reheater, an economizer, and an SCR denitration device which are successively interconnected, and further including a heat-storage medium tank and a heat-storage medium and feedwater heat exchanger. A flow of a cold heat-storage medium entering the heat-storage medium heater is regulated, so that heat absorption of the heat-storage medium is matched with a boiler load. Flows of hot heat-storage medium and feedwater, which enter the heat-storage medium and feedwater heat exchanger, are regulated through a feedwater regulating valve and a hot heat-storage medium outlet regulating valve. A total feedwater flow is regulated with assistance of a bypass feedwater regulating valve, so that a temperature of flue gas entering the SCR denitration device is kept in an optimal operation range under different boiler loads, and denitration efficiency is ensured.

An evaporator system for an industrial boiler, containing a heat transfer system, a separator for separating water and steam and a dryer for drying the separated wet steam. A horizontal vessel contains a required minimum amount of water, a relatively small steam volume and internals for the separation of water and wet-steam. A vertical vessel contains internals for drying the wet steam to predetermined values by separating liquid from the wet-steam. The horizontal vessel and the vertical vessel are connected to each other by wet-steam piping through which separated wet-steam is transported from the horizontal vessel to the vertical vessel. The vertical vessel has a connection to dry-steam piping for discharging dried steam. The vertical vessel has a connection to a liquid drain piping for transporting liquid from the vertical vessel back to the inlet conduits of the evaporator heat transfer section.

An all-condition auxiliary denitration system and an operation method. thereof are provided. The system includes a heat-storage medium heater, a low-temperature reheater, an economizer, and an SCR denitration device which are successively interconnected, and further including a heat-storage medium tank and a heat-storage medium and feedwater heat exchanger. A flow of a cold heat-storage medium entering the heat-storage medium heater is regulated, so that heat absorption of the heat-storage medium is matched with a boiler load. Flows of hot heat-storage medium and feedwater, which enter the heat-storage medium and feedwater heat exchanger, are regulated through a feedwater regulating valve and a hot heat-storage medium outlet regulating valve. A total feedwater flow is regulated with assistance of a bypass feedwater regulating valve, so that a temperature of flue gas entering the SCR denitration device is kept in an optimal operation range under different boiler loads, and denitration efficiency is ensured.

There is provided a steam power plant which has a plurality of units and improves turbine plant efficiency in partial-load operation of the plurality of units in total. The steam power plant includes a first steam power plant having a boiler which generates steam, a high-pressure turbine which is driven with the steam that the boiler generates, a first reheat line which supplies the steam which is exhausted or extracted from the high-pressure turbine to the boiler, a first feed water heater to which part of the steam which is exhausted or extracted from the high-pressure turbine is supplied, and a high-pressure extraction steam line which supplies the part of the steam which is exhausted or extracted from the high-pressure turbine to the first feed water heater; a second steam power plant having a boiler which generates steam, a high-pressure turbine which is driven with the steam that the boiler generates, a first reheat line which supplies the steam which is exhausted or extracted from the high-pressure turbine to the boiler, a first feed water heater to which part of the steam which is exhausted or extracted from the high-pressure turbine is supplied, and a high-pressure extraction steam line which supplies the part of the steam which is exhausted or extracted from the high-pressure turbine to the first feed water heater; and an inter-unit connected extraction steam line which connects the high-pressure extraction steam line of the first steam power plant with the high-pressure extraction steam line of the second steam power plant.

A thermal energy recovery device includes a circulation flow path for circulating a working fluid, a thermal fluid circulation flow path for circulating hot water, an evaporator for evaporating the working fluid flowing in the circulation flow path by heat of the hot water flowing in the thermal fluid circulation flow path, a preheater for heating the working fluid before flowing into the evaporator by the heat of the hot water flowing in the thermal fluid circulation flow path, and a control unit for controlling a startup operation of the thermal energy recovery device. The control unit executes a suppression control for suppressing a temperature difference between the hot water and the working fluid in the preheater.

A thermal energy recovery device includes a circulation flow path for circulating a working fluid, a thermal fluid circulation flow path for circulating hot water, an evaporator for evaporating the working fluid flowing in the circulation flow path by heat of the hot water flowing in the thermal fluid circulation flow path, a preheater for heating the working fluid before flowing into the evaporator by the heat of the hot water flowing in the thermal fluid circulation flow path, and a control unit for controlling a startup operation of the thermal energy recovery device. The control unit executes a suppression control for suppressing a temperature difference between the hot water and the working fluid in the preheater.

A solar thermal power generation system is provided with a low-temperature heat collection device; a steam separator; a first hot water line that feeds water separated by a steam separator to the low-temperature heat collection device; a low-temperature heat storage device provided in the first hot water line; a high-temperature heat collection device; a steam turbine; a first main steam line that feeds superheated steam to the steam turbine; a second main steam line that branches from the first main steam line and joins with the first main steam line; a high-temperature heat storage device provided in the second main steam line; a low-temperature bypass line that bypasses the low-temperature heat collection device and; and a high-temperature bypass line that bypasses the high-temperature heat collection device and connects a steam outlet-side of the steam separator to an inlet-side of the high-temperature heat storage device.