Sealpot and method for controlling a solids flow rate therethrough
View Patent ↗A sealpot for a combustion power plant includes a downcomer standpipe which receives solids of the combustion power plant, a bed including a first end and a second opposite end, the first end connected to the downcomer standpipe, a discharge standpipe disposed at the second opposite end of the bed, and an orifice plate disposed between the bed and the discharge standpipe separating the discharge standpipe from the bed. The orifice plate includes apertures disposed at a height above the bed which allow transport of fluidized solids and gas through the orifice plate.
1. A sealpot comprising:
a downcomer standpipe which receives solid particles from a combustion gas;
a bed having a first end and a second end, the first end being fluidly connected to the downcomer standpipe;
a discharge standpipe disposed at the second end of the bed; and
an orifice plate disposed between the bed and the discharge standpipe separating the discharge standpipe from the bed, the orifice plate having at least two rows of a plurality of apertures disposed above a weir height of the bed, wherein the at least two rows of apertures are vertically spaced a predetermined distance to reduce surging of the solid particles passing through the plurality of apertures of the orifice plate.
2. The sealpot according to claim 1 , wherein
the downcomer standpipe receives the solids from a solids separator,
the bed receives the solids from the downcomer standpipe at the first end of the bed, fluidizes the solids using a gas, and transports the fluidized solids and the gas through the orifice plate to the discharge standpipe at the second end of the bed, and
the discharge standpipe receives the fluidized solids and the gas from the bed through apertures of the plurality of apertures.
3. The sealpot according to claim 1 , wherein discharge standpipe provides the fluidized solid particles to a combustion power plant which comprises at least one of a fluidized bed combustion power plant, a circulating fluidized bed boiler, a bubbling fluidized bed boiler, a moving fluidized bed boiler and a chemical looping combustor.
4. The sealpot according to claim 1 , wherein the orifice plate includes at least one other aperture at least partially disposed above the maximum bed expansion height.
5. The sealpot according to claim 1 , wherein the at least two rows of the plurality of apertures is disposed below a maximum bed expansion height.
6. The sealpot according to claim 1 , wherein the orifice plate extends from a bottom portion defining the bed and extends to a height substantially above the bed.
7. The sealpot according to claim 1 , further comprising a fluidizing air source which fluidizes the solid particles in the bed to transport the fluidized solid particles from the first end to the second end of the bed and the orifice plate,
wherein a flow rate of the fluidized solids transported to the discharge standpipe is controlled based on at least one of a flow rate of the air supplied from the transport air source, a total number of the plurality of apertures, a diameter of an aperture of the plurality of apertures, a cross-sectional shape of an aperture of the plurality of apertures, an area of an aperture of the plurality of apertures and a height of an aperture of the plurality of apertures.
8. The sealpot according to claim 7 , wherein a flow rate of the fluidized solid particles transported to the discharge standpipe is controlled based on at least one of a flow rate of the air supplied from a transport air source, a total number of the plurality of apertures, a diameter of an aperture of the plurality of apertures, a cross-sectional shape of an aperture of the plurality of apertures, an area of an aperture of the plurality of apertures and a height of an aperture of the plurality of apertures.
9. The sealpot according to claim 7 , wherein the gas to from the fluidizing source is air.
10. The sealpot according to claim 1 , further comprising a solids control valve connected to the first end of the bed, wherein the solids control valve controls a flow rate of solids to the combustion power plant based on a flow rate of the fluidized solids and the gas delivered to the combustor through the discharge standpipe.
11. The sealpot according to claim 1 , wherein the orifice plate further comprising:
a third row of a plurality of apertures disposed above the third row of apertures, wherein the third row is disposed the at least two rows of apertures and vertically spaced a predetermined distance from the at least two rows to reduce surging of the solid particles passing through the plurality of apertures of the orifice plate.
12. The sealpot according to claim 1 , wherein the bed includes at least one of a fluidizing bed and a transport bed.
13. The sealpot according to claim 1 , further comprising a plurality of sealpots to enable the fluidized solids and gas from the downcomer standpipe to be transported to corresponding discharge standpipes of each of the sealpots.
14. A method of maintaining a seal between a solids separator and a vessel, the method comprising:
connecting fluidly a downcomer standpipe to the solids separator;
connecting fluidly a first end of a bed to the downcomer standpipe;
disposing a discharge standpipe at a second end of the bed; and
disposing an orifice plate between the bed and the discharge standpipe separating the discharge standpipe from the bed, the orifice plate having at least two rows of a plurality of apertures disposed above a weir height of the bed, wherein the at least two rows of apertures are vertically spaced a predetermined distance to reduce surging of the solid particles passing through the plurality of apertures of the orifice plate.
15. The method of claim 14 , further comprising:
receiving solids from the solids separator in the downcomer standpipe;
receiving the solids from the downcomer standpipe in the bed at the first end of the bed;
fluidizing the solids using a gas;
transporting the fluidized solids and the gas through the orifice plate to the discharge standpipe at the second end of the bed;
receiving the fluidized solids and the gas from the bed in the discharge standpipe through apertures of the plurality of apertures; and
delivering the fluidized solids and the gas to the vessel, wherein
a flow rate of the fluidized solids transported to the discharge standpipe is controlled based on at least one of a flow rate of the gas, a total number of the plurality of apertures, a diameter of an aperture of the plurality of apertures, a cross-sectional shape of an aperture of the plurality of apertures, an area of an aperture of the plurality of apertures and a height of an aperture of the plurality of apertures.
16. The method of claim 14 , wherein the vessel is a combustion chamber comprising at least one of a fluidized bed combustion power plant, a circulating fluidized bed boiler, a bubbling fluidized bed boiler, a moving fluidized bed boiler and a chemical looping combustor.
17. The method of claim 14 , wherein the at least two rows of the plurality of apertures is disposed below a maximum bed expansion height.
18. The method of claim 14 , wherein the orifice plate includes at least one gas aperture disposed above the maximum bed expansion height to pass primarily gas therethrough.
19. The method of claim 18 , wherein the bed includes at least one of a fluidizing bed and a transport bed.
20. A sealpot comprising:
a downcomer standpipe which receives solid particles from a combustion gas;
a bed having a first end and a second end, the first end being fluidly connected to the downcomer standpipe;
a discharge standpipe disposed at the second end of the bed; and an orifice plate disposed between the bed and the discharge standpipe separating the discharge standpipe from the bed, the orifice plate having at least two rows of a plurality of apertures disposed above a weir height of the bed and below a maximum solid expansion height and at least one other aperture at least partially disposed above the maximum solid expansion height.