Thermal power generation system and control method for same

1. A thermal power generation system, comprising:

a coal burning or oil burning boiler including at least one internal heat exchanger that includes an economizer being disposed in a circulation passage through which water is circulatable, and being capable of generating steam through heat exchange between the water and exhaust gas produced by burning coal or heavily oil as a fuel;

at least one steam turbine being disposed in the circulation passage and being capable of outputting power by utilizing the steam;

a generator capable of generating electric power by utilizing the power outputted from the steam turbine;

a condenser capable of condensing the steam discharged from the steam turbine;

at least one low-pressure feed water heater being disposed in a feed water path forming a part of the circulation passage, extending from the condenser to the at least one internal heat exchanger, and being capable of heating the water condensed by the condenser by utilizing steam extracted from the at least one steam turbine;

a high-pressure feed water pump being disposed in the feed water path of the circulation passage so as to be positioned downstream of the at least one low-pressure feed water heater, and being capable of increasing a pressure of the water heated by the at least one low-pressure feed water heater and pumping the water;

at least one high-pressure feed water heater being disposed in the feed water path of the circulation passage so as to be positioned between the high-pressure feed water pump and the at least one internal heat exchanger, and being capable of heating the water pumped by the high-pressure feed water pump by utilizing steam extracted from the at least one steam turbine;

a catalyst device being disposed in an exhaust path of the exhaust gas extending from the boiler, and including at least one kind of catalyst capable of promoting reduction reaction of nitrogen oxide and oxidation reaction of metallic mercury, the nitrogen oxide and the metallic mercury both being contained in the exhaust gas;

at least one mercuric oxide removing device being disposed in the exhaust path so as to be positioned downstream of the catalyst device, and being capable of removing mercuric oxide produced by the oxidation reaction of the metallic mercury from the exhaust gas;

an exhaust gas temperature adjustment device capable of adjusting a temperature of the exhaust gas at the catalyst device to be not higher than 420° C., by adjusting heating of the water by the at least one high-pressure feed water heater; and

a bypass duct which brings a flue gas duct of an upstream side of the economizer and a flue gas duct of a downstream side of the economizer into communication,

wherein the bypass duct allows at least a part of the exhaust gas to bypass the economizer during startup of the boiler or during part load of the boiler and the exhaust gas is prevented from passing through the bypass duct while not in starting up of the boiler nor in part load of the boiler after starting the boiler, and

wherein the exhaust gas temperature adjustment device includes:

an exhaust gas temperature sensor capable of measuring the temperature of the exhaust gas at the catalyst device;

at least one extraction valve disposed in at least one extraction passage extending between the at least one steam turbine and the at least one high-pressure feed water heater, and being capable of adjusting a flow rate of steam extracted from the at least one steam turbine; and

a control device adjusting an opening degree of the at least one extraction valve on the basis of a measurement result of the exhaust gas temperature sensor.

2. The thermal power generation system according to claim 1 ,

wherein the exhaust gas temperature adjustment device includes:

at least one bypass passage disposed parallel to the feed water path so as to be capable of bypassing at least one of the at least one high-pressure feed water heater;

at least one bypass valve capable of adjusting a flow rate of the water in the at least one bypass passage; and

a control device adjusting an opening degree of the at least one bypass valve on the basis of a measurement result of the exhaust gas temperature sensor.

3. The thermal power generation system according to claim 1 ,

wherein the fuel is lignite.

4. The thermal power generation system according to claim 1 ,

wherein the exhaust gas temperature adjustment device adjusts the temperature of the exhaust gas at the catalyst device to be not lower than 290° C.

5. The thermal power generation system according to claim 1 , further comprising an oxidizing agent supply device capable of supplying halogen to be used in the oxidation reaction of the metallic mercury to the catalyst device.

6. A method of controlling a thermal power generation system according to claim 1 ,

wherein the method comprises:

adjusting a temperature of the exhaust gas at the catalyst device to be not higher than 420° C. by the exhaust gas temperature adjustment device adjusting heating of the water by the at least one high-pressure feed water heater; and allowing at least a part of the exhaust gas to bypass the economizer by the bypass duct during startup of the boiler or during part load of the boiler and preventing the exhaust gas from passing through the bypass duct while not in starting up of the boiler, nor in part load of the boiler after staring the boiler.

7. A thermal power generation system comprising:

a coal burning or oil burning boiler including at least one internal heat exchanger that includes an economizer being disposed in a circulation passage through which water is circulatable, and being capable of generating steam through heat exchange between the water and exhaust gas produced by burning coal or heavily oil as a fuel;

at least one steam turbine being disposed in the circulation passage and being capable of outputting power by utilizing the steam;

a generator capable of generating electric power by utilizing the power outputted from the steam turbine;

a condenser capable of condensing the steam discharged from the steam turbine;

at least one low-pressure feed water heater being disposed in a feed water path forming a part of the circulation passage, extending from the condenser to the at least one internal heat exchanger, and being capable of heating the water condensed by the condenser by utilizing steam extracted from the at least one steam turbine;

a high-pressure feed water pump being disposed in the feed water path of the circulation passage so as to be positioned downstream of the at least one low-pressure feed water heater, and being capable of increasing a pressure of the water heated by the at least one low-pressure feed water heater and pumping the water;

at least one high-pressure feed water heater being disposed in the feed water path of the circulation passage so as to be positioned between the high-pressure feed water pump and the at least one internal heat exchanger, and being capable of heating the water pumped by the high-pressure feed water pump by utilizing steam extracted from the at least one steam turbine;

a catalyst device being disposed in an exhaust path of the exhaust gas extending from the boiler, and including at least one kind of catalyst capable of promoting reduction reaction of nitrogen oxide and oxidation reaction of metallic mercury, the nitrogen oxide and the metallic mercury both being contained in the exhaust gas;

at least one mercuric oxide removing device being disposed in the exhaust path so as to be positioned downstream of the catalyst device, and being capable of removing mercuric oxide produced by the oxidation reaction of the metallic mercury from the exhaust gas;

an exhaust gas temperature adjustment device capable of adjusting a temperature of the exhaust gas at the catalyst device to be not higher than 420° C., by adjusting heating of the water by the at least one high-pressure feed water heater; and

a bypass duct which brings a flue gas duct of an upstream side of the economizer and a flue gas duct of a downstream side of the economizer into communication,

wherein the bypass duct allows at least a part of the exhaust gas to bypass the economizer during startup of the boiler or during part load of the boiler and the exhaust gas is prevented from passing through the bypass duct while not in starting up of the boiler nor in part load of the boiler after starting the boiler,

wherein the exhaust gas temperature adjustment device comprises:

an exhaust gas temperature sensor capable of measuring the temperature of the exhaust gas at the catalyst device; and

a feed water temperature sensor capable of measuring the temperature of the water to be supplied to the at least one internal heat exchanger, and

wherein the exhaust gas temperature adjustment device adjusts heating of the water by the at least one high-pressure feed water heater on the basis of the detecting results of the exhaust gas temperature sensor and the feed water temperature sensor.