Circulating fluidized bed boiler with a loopseal heat exchanger
US-11603989-B2 · Mar 14, 2023 · US
US12510241B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12510241-B2 |
| Application number | US-202118251811-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 2, 2021 |
| Priority date | Nov 19, 2020 |
| Publication date | Dec 30, 2025 |
| Grant date | Dec 30, 2025 |
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A method for heating a heat exchange medium in a fluidized bed boiler ( 100 ), the method comprising burning first fuel ( 165 ) in a first furnace ( 162 ) of the fluidized bed boiler ( 100 ) to produce first flue gas ( 163 ); recovering heat from the first flue gas ( 163 ) to a heat exchange medium using a first heat exchanger ( 310 ); conveying the heat exchange medium from the first heat exchanger ( 310 ) to a second heat exchanger ( 320 ), of which at least a part is arranged in contact with a fluidized bed of the fluidized bed boiler ( 100 ); burning second fuel ( 175 ) in a second furnace ( 172 ) of the fluidized bed boiler ( 100 ) to produce second flue gas ( 173 ); conveying the heat exchange medium from the second heat exchanger ( 320 ) to a third heat exchanger ( 330 ); and recovering heat from the second flue gas ( 173 ) to the heat exchange medium using the third heat exchanger ( 330 ). A fluidized bed boiler ( 100 ) for performing the method. A loopseal heat exchanger ( 400 ) that is, when installed in a loopseal of a circulating fluidized bed boiler, configured to burn second fuel ( 175 ) in a second furnace ( 172 ) of the loopseal heat exchanger ( 400 ) to produce second flue gas ( 173 ); convey the heat exchange medium from the second heat exchanger ( 320 ) to a third heat exchanger ( 330 ); and recover heat from the second flue gas ( 173 ) to the heat exchange medium using the third heat exchanger ( 330 ).
Opening claim text (preview).
The invention claimed is: 1 . A method for heating a heat exchange medium in a fluidized bed boiler, the method comprising, at a first period of time, the steps of: burning first fuel in a first furnace of the fluidized bed boiler to produce first flue gas, recovering heat from the first flue gas to a heat exchange medium using a first heat exchanger, conveying the heat exchange medium from the first heat exchanger to a second heat exchanger, of which at least a part is arranged in contact with a fluidized bed of the fluidized bed boiler, burning second fuel in a second furnace of the fluidized bed boiler to produce second flue gas, conveying the heat exchange medium from the second heat exchanger to a third heat exchanger, and recovering heat from the second flue gas to the heat exchange medium using the third heat exchanger, wherein: the third heat exchanger is not in contact with a fluidized bed of the fluidized bed boiler, and the second flue gas comprises less alkali and halogen than the first flue gas and/or the second fuel comprises less alkali and halogen than the first fuel. 2 . The method of claim 1 , wherein the third heat exchanger is not in contact with the first flue gases. 3 . The method of claim 1 , further comprising, at a second period of time, the steps of: recovering heat from the fluidized bed of the fluidized bed boiler to the heat exchange medium using the second heat exchanger, and conveying the heat exchange medium from the second heat exchanger to the third heat exchanger, and either: [A] not burning the second fuel in the second furnace during the second period of time, or [B] burning less second fuel in the second furnace during the second period of time than during the first period of time. 4 . The method of claim 3 , further comprising, at the second period of time, conveying the heat exchange medium through the third heat exchanger. 5 . The method of claim 3 , wherein: during the second period of time, a load of the fluidized boiler is more than a load of the fluidized bed boiler during the first period of time; for example, during the first period of time, a load of the fluidized boiler is less than a threshold and during the second period of time, a load of the fluidized boiler is at least equal to the threshold. 6 . The method of claim 1 , wherein at least one of the second fuel is liquid or gas, such as a gas comprising natural gas or a liquid comprising oil, or the first fuel comprises solid material, such as biomass and/or residue derived fuel. 7 . The method of claim 1 , further comprising the step of circulating bed material from the first furnace to a cyclone, from the cyclone to a loopseal, and from the loopseal to the first furnace, wherein the second heat exchanger is arranged in the loopseal of the of the fluidized bed boiler. 8 . The method of claim 7 , wherein: a first side of a wall of a loopseal heat exchanger limits a first chamber, the first side or an opposite second side of the wall of the loopseal heat exchanger limits a second chamber, the second heat exchanger is arranged in the first chamber or in a wall limiting the first chamber, and the third heat exchanger is arranged in the second chamber or in a wall limiting the second chamber. 9 . The method of claim 1 , further comprising fluidizing a fluidized bed within the fluidized bed boiler using fluidizing gas that comprises at least some of the second flue gas. 10 . A fluidized bed boiler, comprising: a first furnace for burning first fuel comprising solid material to produce first flue gas, a first heat exchanger for recovering heat from the first flue gas to a heat exchange medium, a second heat exchanger arranged in such a location of the fluidized bed boiler that in use, a fluidized bed comprising bed material is configured to contact the second heat exchanger, a first pipeline for conveying the heat exchange medium from the first heat exchanger to the second heat exchanger, a second furnace for burning second fuel to produce second flue gas, a burner arranged in the second furnace, and a third heat exchanger for recovering heat from the second flue gas to the heat exchange medium received from the second heat exchanger, wherein: the third heat exchanger is configured not to be in contact with a fluidized bed of the fluidized bed boiler, and the burner is configured to burn second fuel, which is liquid or gas, and the second flue gas comprises less alkali and halogen than the first flue gas and/or the second fuel comprises less alkali and halogen than the first fuel. 11 . The fluidized bed boiler of claim 10 , further comprising: a cyclone, and a loopseal, wherein bed material is configured to circulate from the first furnace through the cyclone to the loopseal and from the loopseal to the first furnace. 12 . The fluidized bed boiler of claim 11 , wherein: the fluidized bed boiler comprises a loopseal heat exchanger arranged in the loopseal, the loopseal heat exchanger comprises a first chamber and a second chamber, the second heat exchanger is arranged in the first chamber or in a wall that limits the first chamber, the third heat exchanger is arranged in the second chamber or in a wall that limits the second chamber, a first side of a wall limits the first chamber, and the first side of the wall or an opposite second side of the wall limits the second chamber. 13 . The fluidized bed boiler of claim 10 , further comprising a channel for conveying at least some of the second flue gas to such a part of the fluidized bed boiler, wherein a fluidized bed is configured to form in use. 14 . A power plant, comprising: the fluidized bed boiler of claim 10 , a steam turbine, a pipeline configured to convey heat exchange medium from the third heat exchanger to the steam turbine, and an electricity generator arranged in a mechanical connection with the steam turbine.
structurally associated with turbines or similar engines · CPC title
Heat-exchange apparatus using a fluidised bed · CPC title
the separation apparatus being located outside the combustion chamber · CPC title
in parallel arrangement · CPC title
an electrical generator · CPC title
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