Waste heat recovery device, gas turbine plant provided with same, and waste heat recovery method
US-2017074164-A1 · Mar 16, 2017 · US
US10227900B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10227900-B2 |
| Application number | US-201515329685-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 2, 2015 |
| Priority date | Sep 26, 2014 |
| Publication date | Mar 12, 2019 |
| Grant date | Mar 12, 2019 |
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The purpose of the present invention is to decrease the loss of energy of flue gas when superheated steam is cooled and prevent heat efficiency from being decreased. A boiler is provided with: economizers (a medium-pressure economizer (13) and a high-pressure secondary economizer (18)) which heat water supplied by water supply pumps (a medium-pressure water supply pump (27) and a high-pressure water supply pump (28)); evaporators (a medium-pressure evaporator (16) and a high-pressure evaporator (21)) which evaporate the water that is heated by the economizers; and cooling devices (a medium-pressure system and a high-pressure system) which mix water, as a coolant, which has passed through the economizers via the water supply pumps with steam.
Opening claim text (preview).
The invention claimed is: 1. A boiler comprising: a water supply pump; a first economizer for heating water supplied by the water supply pump; a first evaporator for evaporating first water that is the water heated by the first economizer; a second economizer for receiving second water that is a part of the first water passed through the first economizer, wherein the second economizer heats the second water provided from the first economizer; a second evaporator for evaporating a part of the second water heated by the second economizer; a first cooling device for mixing a part of the second water, as a coolant, that has passed through the second economizer via the water supply pump with steam from the second evaporator; a third economizer for receiving third water, which is a part of the first water passed through the first economizer and pressurized at higher pressure than the second water, wherein the third economizer heats the third water; a third evaporator for evaporating a part of the third water heated by the third economizer, and a second cooling device for mixing a part of the third water, as a coolant, which has passed through the third economizer via the water supply pump with steam from the third evaporator. 2. The boiler according to claim 1 , further comprising: a drum for receiving the part of the second water heated by the second economizer, the drum being connected to the second evaporator, wherein the first cooling device extracts the coolant from a connection line connecting the second economizer and the drum to each other. 3. The boiler according to claim 2 , wherein a flow regulation valve is provided in the connection line, and the first cooling device extracts the coolant from a portion of the connection line located between the second economizer and the flow regulation valve. 4. The boiler according to claim 1 , further comprising: a superheater for superheating the steam delivered from the second evaporator to generate superheated steam, and wherein the first cooling device supplies the coolant to an inlet side of the superheater. 5. The boiler according to claim 4 , wherein the superheater includes a first superheater for superheating the steam delivered from the second evaporator, and a second superheater for further superheating the superheated steam delivered from the first superheater, and the first cooling device supplies the coolant to a portion between the first superheater and the second superheater. 6. A combined cycle plant comprising: a gas turbine; the boiler according to claim 1 having a flue gas discharged from the gas turbine as a heat source; a steam turbine driven by steam generated by the boiler; a condenser for condensing steam via the steam turbine; and a condensate pump for supplying the condensate from the condenser to the boiler. 7. A steam cooling method for a boiler including: a first economizer for heating water supplied by a water supply pump; a first evaporator for evaporating first water that is the water heated by the first economizer; a second economizer for receiving second water that is a part of the first water passed through the first economizer, wherein the second economizer heats the second water provided; a second evaporator for evaporating a part of the second water heated by the second economizer; a first cooling device for mixing a part of the second water; a third economizer for receiving third water, which is a part of the first water passed through the first economizer and pressurized at higher pressure than the second water, wherein the third economizer heats the third water; a third evaporator for evaporating a part of the third water heated by the third economizer; and a second cooling device for mixing a part of the third water, as a coolant, which has passed through the third economizer via the water supply pump with steam from the third evaporator, the steam cooling method comprising: extracting the part of the second water having passed through the second economizer via the water supply pump; and mixing, in the first cooling device, the part of the second water, as a coolant, that has passed through the second economizer with steam from the second evaporator.
Regulating means specially adapted therefor · CPC title
Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT] · CPC title
with water evaporated or preheated at different pressures in exhaust boiler · CPC title
using the waste heat of gas-turbine plants outside the plants themselves, e.g. gas-turbine power heat plants (using waste heat as source of energy for refrigeration plants F25B27/02; using the waste heat of a gasturbine for steam generation or in a steam cycle see F01K23/10) · CPC title
by attemperating the superheated steam, e.g. by injected water sprays · CPC title
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