Combustion system comprising an annular shroud burner
A carbon sequestration system includes a furnace having an oxy-combustion burner, a mill configured to receive a fuel and to provide the fuel to the oxy-combustion burner, a waste heat recovery exchanger configured to receive a flue gas from the furnace, the flue gas ultimately supplied to one or more of an overfire air port of the furnace, the oxy-combustion burner, the mill, and a CO 2 purification unit, the CO 2 purification unit configured to produce a purified CO 2 stream.
1. A carbon sequestration system, comprising:
a furnace having an oxy-combustion burner;
a mill configured to receive a fuel and to provide the fuel to the oxy-combustion burner;
a waste heat recovery exchanger configured to receive a flue gas from the furnace;
an electrostatic precipitator configured to receive the flue gas from the waste heat recovery exchanger;
a direct contact cooler/polishing scrubber configured to receive the flue gas downstream of the waste heat recovery exchanger and to exhaust the flue gas as a cooled flue gas;
a first cooled flue gas recycle supply stream configured to supply the cooled flue gas to
a first flue gas recycle supply stream, the first flue gas recycle supply stream configured for input to a flue gas recycle heater and for output from the flue gas recycle heater as a heated flue gas recycle supply stream configured for input to at least one of an overfire air port of the furnace or the oxy-combustion burner as a secondary flue gas recycle stream, and
a second flue gas recycle supply stream, the second flue gas recycle supply stream configured for input to the mill; and
a second cooled flue gas recycle supply stream configured to supply the cooled flue gas to a CO 2 purification unit, the CO 2 purification unit configured to produce a purified CO 2 stream from the second cooled flue gas recycle stream for sequestration.
2. The carbon sequestration system of claim 1 , further comprising a flue gas desulfurizer in fluid communication with the electrostatic precipitator and the direct contact cooler/polishing scrubber.
3. The carbon sequestration system of claim 2 , wherein the flue gas recycle heater is configured to receive the flue gas from the furnace to heat the first flue gas recycle supply stream to produce the heated flue gas recycle supply stream.
4. The carbon sequestration system of claim 3 , wherein the heated flue gas recycle supply stream is configured to be provided to the mill as a primary flue gas recycle stream.
5. The carbon sequestration system of claim 4 , further comprising a flow temperature control valve configured to mix a portion of the second flue gas recycle supply stream and the heated flue gas recycle supply stream to produce a cooled primary flue gas recycle stream.
6. The carbon sequestration system of claim 5 , wherein the heated flue gas recycle supply stream is configured to be received by both the overfire air port of the furnace and the oxy-combustion burner as the secondary flue gas recycle stream.
7. The carbon sequestration system of claim 6 , wherein the primary flue gas recycle stream is mixed or the cooled primary flue gas recycle stream is diluted with an oxidant.
8. The carbon sequestration system of claim 1 , wherein the oxy-combustion burner is an annular shroud burner, comprising:
a quarl, the quarl having a diverging conical shape that is positioned to extend along a central axis and defining a combustion zone radially inward and downstream of a radially inner surface of the quarl, the quarl extending from a burner face to a furnace interior wall;
a first conduit, the first conduit positioned to extend along the central axis and configured to provide a first stream of oxygen into the combustion zone at the burner face;
a second conduit, the second conduit positioned to extend along the central axis, radially outward of the first conduit, and configured to provide a mixed stream of a fuel and a carrier to the combustion zone at the burner face;
a third conduit, the third conduit positioned to extend along the central axis, radially outward of the second conduit, and configured to provide a second stream of oxygen to the combustion zone at the burner face; and
a fourth conduit, the fourth conduit positioned to extend along the central axis, radially outward of the third conduit, and configured to provide a stream of recycled flue gas in a form of a conical shroud that extends along the inner surface of the quarl, from the burner face to the furnace interior wall, the stream of recycled flue gas surrounding a peak flame temperature region within the combustion zone.
9. The carbon sequestration system of claim 8 , wherein the first stream of oxygen and the second stream of oxygen of the annular shroud burner comprise undiluted oxygen.
10. The carbon sequestration system of claim 9 , wherein the first stream of oxygen and the second stream of oxygen of the annular shroud burner comprise an oxygen content of at least about 90%.
11. The carbon sequestration system of claim 10 , wherein the carrier comprises a recycled flue gas.
12. The carbon sequestration system of claim 11 , wherein the recycled flue gas comprises at least a portion of the secondary flue gas recycle supply stream.
13. The carbon sequestration system of claim 12 , wherein the stream of recycled flue gas surrounding the peak flame temperature region within the combustion zone comprises at least a portion of the heated flue gas recycle supply stream.
14. A method for generating purified carbon dioxide for sequestration using a system comprising a furnace having an oxy-combustion burner, a mill configured to receive a fuel and to provide the fuel to the oxy-combustion burner, a waste heat recovery exchanger configured to receive a flue gas from the furnace, an electrostatic precipitator configured to receive the flue gas from the waste heat recovery exchanger, and a direct contact cooler/polishing scrubber configured to receive the flue gas downstream of the waste heat recovery exchanger and to exhaust the flue gas as a cooled flue gas, the method comprising:
supplying the cooled flue gas via a first cooled flue gas recycle supply stream to
a first flue gas recycle supply stream, the first flue gas recycle supply stream configured to for input to a flue gas recycle heater and for output from the flue gas recycle heater as a heated flue gas recycle supply stream configured for input to at least one of an overfire air port of the furnace or the oxy-combustion burner as a secondary flue gas recycle stream, and
a second flue gas recycle supply stream, the second flue gas recycle supply stream configured for input to the mill; and
supplying the cooled flue gas via a second cooled flue gas recycle supply stream to a CO 2 purification unit, the CO 2 purification unit configured to produce a purified CO 2 stream from the second cooled flue gas recycle stream for sequestration.
15. The method of claim 14 , wherein the oxy-combustion burner includes an annular shroud burner having a quarl, the quarl having a diverging conical shape that is positioned to extend along a central axis and defining a combustion zone radially inward and downstream of a radially inner surface of the quarl, the quarl extending from a burner face to a furnace interior wall, the method further comprising:
providing a first stream of oxygen into the combustion zone via a first conduit, the first conduit positioned to extend along the central axis and configured to open into the quarl at the burner face;
providing a mixed stream of the fuel and a carrier to the combustion zone via a second conduit, the second conduit positioned to extend along the central axis, radially outward of the first conduit, and configured to open into the quarl at the burner face;
providing a second stream of oxygen to the combustion zone via a third conduit, the third conduit positioned to extend along the central axis, radially outward of the second conduit, and configured to open into the quarl at the burner face; and
providing a stream of recycled flue gas, that surrounds a portion of the combustion zone, via a fourth conduit, the fourth conduit positioned to extend along the central axis, radially outward of the third conduit, and configured to provide the stream of recycled flue gas in a form of a conical shroud that extends along the inner surface of the quarl, from the burner face to the furnace interior wall, the stream of recycled flue gas surrounding a peak flame temperature area within the combustion zone.
16. The method of claim 15 , wherein the first stream of oxygen and the second stream of oxygen of the annular shroud burner comprise undiluted oxygen.
17. The method of claim 16 , wherein the first stream of oxygen and the second stream of oxygen of the annular shroud burner comprise an oxygen content of at least about 90%.
18. The method of claim 17 , wherein the carrier comprises a recycled flue gas.
19. The method of claim 18 , wherein the recycled flue gas comprises at least a portion of the secondary flue gas recycle supply stream.
20. The method of claim 19 , wherein the stream of recycled flue gas surrounding the peak flame temperature region within the combustion zone comprises at least a portion of the heated flue gas recycle supply stream.