Burner apparatus and method of combustion
10914468 ยท 2021-02-09
Assignee
Inventors
- Izaak Risseeuw (Zoetermeer, NL)
- Jeffrey Kloosterman (Allentown, PA, US)
- Xianming Jimmy Li (Orefield, PA)
- Robert Gregory Wolf (Hackettstown, NJ, US)
- Reed Jacob Hendershot (Orefield, PA, US)
- Franciscus Arnoldus Maria Jeunink (Delfgauw, NL)
Cpc classification
F23C6/047
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23C2201/20
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23C2201/30
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23C2900/06043
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23D14/70
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
F23C6/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23D14/70
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
A burner apparatus (10) includes a fluid-based flame stabilizer for discharging a stabilized flame therefrom, a burner tile (44), and fuel lances associated with the burner tile. Each of the fuel lances has a discharge nozzle (40). A Coanda feature (34) having a Coanda surface directs a portion of the stabilized flame from the passage defined by the burner tile at the discharge end of a primary flow passage (32) toward at least one first fuel lance of the plurality of fuel lances to cross light the at least one first fuel lance. In another embodiment, a method of combustion includes supplying a first gaseous fuel to fuel lances of a burner apparatus and igniting and sustaining combustion of a gaseous fuel by cross lighting at the discharge nozzles of the fuel lances by flow from the fluid-based flame stabilizer along a Coanda surface of a Coanda feature toward the discharge nozzles.
Claims
1. A burner apparatus comprising: a fluid-based flame stabilizer for discharging a stabilized flame therefrom; a burner tile defining a primary flow passage therein, the primary flow passage having an inlet end, a discharge end, and a wall connecting the inlet end to the discharge end and surrounding the primary flow passage, wherein the fluid-based flame stabilizer is operatively disposed to direct the stabilized flame into the primary flow passage of the burner tile; and a plurality of fuel lances associated with the burner tile, each of the plurality of fuel lances having a discharge nozzle, the discharge nozzles of the plurality of fuel lances being positioned proximate the discharge end of the primary flow passage of the burner tile and spaced to distribute a first gaseous fuel proximate the discharge end of the primary flow passage of the burner tile; wherein a first Coanda feature having a Coanda surface directs a portion of the stabilized flame from the primary flow passage defined by the burner tile at the discharge end of the primary flow passage toward at least one first fuel lance of the plurality of fuel lances to cross light the at least one first fuel lance; wherein the first Coanda feature having a Coanda surface protrudes into the primary flow passage.
2. A burner apparatus according to claim 1, wherein the discharge nozzles are located within 10 cm (3.94 inches) of the discharge end of the primary flow passage of the burner tile.
3. A burner apparatus according to claim 1, wherein the fluid-based flame stabilizer comprises: a first duct having an inlet end, a discharge end, and a wall extending from the inlet end of the first duct to the discharge end of the first duct, the wall thereby defining a first passage for passing a first oxygen-containing gas therethrough; a second duct having an inlet end, a discharge end, and a wall extending from the inlet end of the second duct to the discharge end of the second duct, the first duct disposed partially within the second duct thereby defining a second passage between the external surface of the first duct and the internal surface of the second duct for passing a second gaseous fuel therethrough, wherein the discharge end of the first duct is recessed from the discharge end of the second duct; and a third duct having an inlet end, a discharge end, and a wall extending from the inlet end of the third duct to the discharge end of the third duct, the second duct disposed partially within the third duct thereby defining a third passage between the external surface of the second duct and the internal surface of the third duct for passing a second oxygen-containing gas therethrough, wherein the discharge end of the second duct is recessed from the discharge end of the third duct.
4. A burner apparatus according to claim 3, wherein the first gaseous fuel and the second gaseous fuel have the same composition.
5. A burner apparatus according to claim 3, wherein the first oxygen-containing gas and the second oxygen-containing gas have the same composition.
6. A burner apparatus according to claim 5 further comprising an oxygen-containing gas source operatively disposed to direct the oxygen-containing gas to the first duct and the third duct.
7. A burner apparatus according to claim 1 further comprising a fuel source operatively connected to the plurality of fuel lances.
8. A burner apparatus according to claim 1, wherein the plurality of fuel lances pass through the burner tile.
9. A burner apparatus according to claim 1, wherein the discharge end of the primary flow passage of the burner tile has a circular cross-section.
10. A burner apparatus according to claim 1 further comprising a second Coanda feature extending from the burner tile, the second Coanda feature having a Coanda surface extending into the primary flow passage of the burner tile at the discharge end of the primary flow passage adjacent a second fuel lance of the plurality of fuel lances to deflect a portion of the stabilized flame toward the discharge nozzle of the second of the plurality of fuel lances.
11. A burner apparatus according to claim 1, wherein the or each Coanda surface extends into the primary flow passage around only a portion of the perimeter of the discharge end of the primary flow passage.
12. A burner apparatus according to claim 1, wherein said apparatus is devoid of separate or secondary passages for redirecting the stabilized flame.
13. A method of combustion comprising: supplying a first gaseous fuel to a plurality of fuel lances of a burner apparatus, the burner apparatus comprising: a fluid-based flame stabilizer for discharging a stabilized flame therefrom; a burner tile defining a primary flow passage therein, the primary flow passage having an inlet end, a discharge end, and a wall connecting the inlet end to the discharge end and surrounding the primary flow passage, wherein the fluid-based flame stabilizer is operatively disposed to direct the stabilized flame into the primary flow passage of the burner tile; and the plurality of fuel lances associated with the burner tile, each of the plurality of fuel lances having a discharge nozzle, the discharge nozzles of the plurality of fuel lances being positioned proximate the discharge end of the primary flow passage of the burner tile and spaced to distribute the first gaseous fuel proximate the discharge end of the primary flow passage of the burner tile; wherein a first Coanda feature having a Coanda surface directs a portion of the stabilized flame from the primary flow passage defined by the burner tile at the discharge end of the primary flow passage toward at least one first fuel lance of the plurality of fuel lances to cross light the at least one first fuel lance; and igniting and sustaining combustion of the first gaseous fuel by cross lighting at the discharge nozzles by flow from the fluid-based flame stabilizer along the Coanda surface toward the discharge nozzles; wherein the first Coanda feature having a Coanda surface protrudes into the primary flow passage.
14. A method according to claim 13, wherein the discharge nozzles are located within 10 cm (3.94 inches) of the discharge end of the primary flow passage of the burner tile.
15. A method according to claim 13, wherein the fluid-based flame stabilizer comprises: a first duct having an inlet end, a discharge end, and a wall extending from the inlet end of the first duct to the discharge end of the first duct, the wall thereby defining a first passage for passing a first oxygen-containing gas therethrough; a second duct having an inlet end, a discharge end, and a wall extending from the inlet end of the second duct to the discharge end of the second duct, the first duct disposed partially within the second duct thereby defining a second passage between the external surface of the first duct and the internal surface of the second duct for passing a second gaseous fuel therethrough, wherein the discharge end of the first duct is recessed from the discharge end of the second duct; and a third duct having an inlet end, a discharge end, and a wall extending from the inlet end of the third duct to the discharge end of the third duct, the second duct disposed partially within the third duct thereby defining a third passage between the external surface of the second duct and the internal surface of the third duct for passing a second oxygen-containing gas therethrough, wherein the discharge end of the second duct is recessed from the discharge end of the third duct.
Description
(1) Preferred embodiments of the present invention will now be described with reference to the drawings in which:
(2)
(3)
(4)
(5)
(6)
(7) Referring now to the drawings, there is shown in
(8) A stabilizing structure includes a primary flow passage 32 surrounded by a Coanda feature 34 having an internal Coanda surface 36. The primary flow passage 32 is a singular passage in which a stabilized flame is capable of being supported. In systems having multiple flow passages, the primary flow passage 32 is the passage having the greater cross-section or supports the largest volume of flame. In one embodiment, the combustion apparatus 10 includes only a singular, unitary passage to support the stabilized flame, the singular, unitary passage being the primary flow passage 32. In another embodiment, the combustion apparatus 10 is devoid of and does not include separate or secondary passages for redirecting the stabilized flame. The Coanda feature 34 directs a portion of the fluid flow from the primary flow passage 32 toward at least one fuel stage tip discharge nozzle 40 of a fuel lance 42 in a burner tile 44 arranged annularly around the discharge end 46 of the combustion apparatus 10. The Coanda feature 34 may extend as an annulus around the entire discharge end 46 of the combustion apparatus 10 or alternatively may extending only around a portion of the discharge end 46 of the combustion apparatus 10, where the combustion apparatus may include one or more additional Coanda features 34, as shown in
(9) The end view of
(10) Next, there is shown in
(11) As with
(12) The symmetric design of the device of the first embodiment 10 provides for a lower pressure drop than the asymmetric second embodiment 50 and eliminates direct flame impingement on a burner and uneven furnace heating inherent to the asymmetric design. The relatively low temperatures experienced by either embodiment of the present invention allow construction using common, inexpensive materials.
(13) As shown in
(14) Although
(15) The Coanda surface 36 may be shaped and located in any manner such that it directs at least a portion of the stabilized flame from the primary flow passage 32 defined by the burner tile at the discharge end of the primary flow passage 32 toward at least one of the fuel lances to cross light that fuel lance. In some embodiments, the Coanda feature 34 is an integral part of the burner tile. In other embodiments, the Coanda feature 34 is attached to the burner tile. In yet other embodiments, the Coanda feature 34 is provided as part of an insert extending into the primary flow passage 32 such that the Coanda feature 34 is located adjacent the burner tile or contacting the burner tile but may or may not be physically attached to the burner tile.
(16) The LSV flame is preferably maintained extremely fuel-lean (e.g., phi=0.05, or 20 times the amount of air required for stoichiometric combustion, where phi is the stoichiometric ratio of fuel-to-air) and is anchored on the LSV fuel pipe. This flame gets more stable as the primary airflow through the relatively narrow outer oxidant annulus is increased. The LSV flame has a very low peak flame temperature (preferably less than 1093 C. (2000 F.) and produces very low NO.sub.x emissions. This is due to excellent mixing, avoidance of fuel-rich zones for prompt NO.sub.x formation (as observed in traditional flame holders) and completion of overall combustion under extremely fuel-lean conditions.
(17) In this method of fuel staging, the resulting combustion (above auto ignition temperature) is controlled by chemical kinetics and by fuel jet mixing with the furnace gases and oxidant. The carbon contained in the fuel molecule is drawn to complete oxidation with the diluted oxidant stream instead of the pyrolitic soot-forming reactions of a traditional flame front. It is assumed here that combustion takes place in two stages. In the first stage, fuel is converted to CO and H.sub.2 in diluted, fuel rich conditions. Here, the dilution suppresses the peak flame temperatures and formation of soot species, which would otherwise produce a luminous flame. In the second stage, CO and H.sub.2 react with diluted oxidant downstream to complete combustion and form CO.sub.2 and H.sub.2O. This space-based dilution and staged combustion leads to a space filling process where a much larger space surrounding flame is utilized to complete the overall combustion process.
(18) Preferably, the oxidant is air and natural gas is the fuel. However, any appropriate oxidant in combination with any appropriate fuel, as known in the art, may be used.
(19) In the LSV burner, the actual stabilized flame from the LSV extends outside the burner into the furnace slightly. Air flows over the internal Coanda surface 36, generating a lower pressure with flow from the flame causing the flame to propagate to cross light the fuel staging tips. Hence, the Coanda feature 34 propagates the flame. Start-up lances may be removed as a result of the presence of the Coanda feature 34. The Coanda feature 34 preferably does not actively disrupt the airflow within the primary flow passage 32.
(20) For the specific case of an oxidant as air and natural gas fuel, various optimal ranges for flow (e.g., V.sub.f=60.96-182.88 cm/sec (2-6 ft/sec); V.sub.pa=914.40-2,743.20 cm/sec (30-90 ft./sec).; V.sub.sa=457.2-1371.6 cm/sec (15-45 ft./sec.V.sub.f is fuel velocity, V.sub.pa is primary air velocity and the V.sub.sa is secondary air velocity) and non-dimensional geometric (e.g., length/diameter) parameters have been determined for a cylindrical design of the burner devices. It is noted that while use of cylindrical pipes operate properly in accordance with the present invention, numerous other shapes of pipes also operate properly so long as the relative speeds of the fuel and oxidants are supplied in accordance with the present invention.
(21) One or more curved surfaces of the Coanda feature 34 provide an exterior flow for the inner LSV flame to propagate from near the burner centerline across an air passage and to the fuel staging tips located some distance away from the centerline. The air passage does not contain fuel and therefore the flame must bridge fuel between the central LSV and the staged fuel tips in order to be effective. The addition of the Coanda feature 34 eliminates the need for a start-up lance and lowers the fuel requirement of the LSV to achieve the same stable flame, even in a cold furnace environment.
(22) The surface of the Coanda feature 34 preferably only has a slight curvature, which induces a lower pressure at the surface, causing the flame to remain on the surface and propagate outward. If the curvature is too great, the fuel and flame detach from the surface and no longer perform its function. The surface creates a waterfall-like flame that appears to flow outward towards the staged fuel lances. In some embodiments, the Coanda surface 36 has the convex cross section of at least a portion of a circle or the convex shape of at least a portion of a cylinder. In other embodiments, the Coanda surface 36 has a convex elliptical cross sectional shape. In some embodiments, the Coanda feature 34 has a width of about 10.16 cm. (4 inches).
(23) One Coanda feature 34 may be used to promote the cross lighting of one to all of the fuel staging lances depending on the burner configuration. Multiple Coanda features 34 may alternatively be used to ensure the cross lighting takes place quickly, reducing the risk for uncombusted fuel entering the furnace. The spacing and size of the Coanda features 34 may include widths measured perpendicular to the fluid flow that provide the cross lighting of the fuel staging lances. For example, the width of the Coanda feature 34 may be from about 5.08 cm. (2 inches) to about 10.16 cm. (4 inches). Likewise, the spacing or placement of the Coanda features 34 along the surface of the primary flow passage 32 may vary. For example, the placement may be aligned with the fuel staging lances in the primary flow passage 32 or may be placed intermediate to the fuel staging lances in the primary flow passage 32 at distances sufficient to provide the cross lighting of the fuel staging lances.
(24) The Coanda surfaces 36 preferably have a curvature sufficient to maintain fluid flow and re-direct the flame flow to the burner tip but not curved beyond the limit at which the flame's flow departs from the curved surface. A preferred curvature maintains a laminar flow of the flame while avoiding conditions that would be considered to produce an aerodynamic stall. An optimal curvature may depend on the flow speed of the flame, the dimensions of the burner, and the desired amount of flame deflection. In one embodiment, particularly good cross-lighting and flame propagation results are obtained for a Coanda feature having Coanda surfaces having dimensions: length equal to the distance burner tile 76 exterior-to-LSV device 74 and width equal to the distance burner tile-to-LSV device (74).
(25) Most applications of a Coanda surface in relation to a flame in the art are seen in flares to promote premixing of uncombusted fuel and air prior to the ignition point. Such use usually requires a flame holder or other flame stabilization downstream of the surface. Also, when used to propagate a flame, the Coanda surface has been restricted to within the burner block structure itself and not exposed to the furnace environment as an external element of the burner. The Coanda feature 34, described herein on an LSV burner, reduces the NO.sub.x produced by the burner by lowering the fuel requirement of the LSV. The device also eliminates the capital and operating concerns of the start-up lance.
(26) Laboratory experiments were conducted as a proof of concept and computational fluid dynamics (CFD) analysis was used to visualize the effect of the surface on the flame and flow patterns. The results of that work are presented in the next section.
EXAMPLES
(27) The testing of two Coanda surfaces in an LSV burner with only 10% fuel to the LSV flame stabilizer over a range of fuels confirmed the surface increased cross lighting as well as light off in a cold furnace. Testing was performed with natural gas as the fuel and with propane as the fuel. Visual inspection clearly indicated the effect of the Coanda surface curving the flame toward the staged fuel tips. The cross lighting of the tips was confirmed with flamelets stabilized at less than 5.08 cm (2 inches) from the staged fuel tips. The device was found to be very effective in a cold furnace environment and provided low-NO.sub.x operation.
(28) In this initial testing, the Coanda feature was provided as part of a vane device made of carbon steel inserted in the burner air passage to form the surface used to stabilize the flame. A set of test points within the burner were monitored with an indication that they all were stable. The tested LSV burner was stable in low NO.sub.x mode up to a firing rate of 2 megawatts (MW) for propane and natural gas in a cold firebox. Burner light off and turndown was demonstrated at a firing rate of 200 kilowatts (kW) for propane and natural gas in a cold firebox at a draft combustion air flow rate of 124.5 Pa. (0.5 inch water-column (wc)). At a higher draft combustion air flow rate of 249.1 Pa (1 inch wc), the minimum firing rate was about 700 kW for propane and for natural gas.
(29) Computer Fluid Dynamics modeling confirmed the effect of the angle of the Coanda surface on its ability to direct flow up to a maximum angle of 90 degrees. The results clearly showed an increase in the bending of streamlines as the angle was reduced below 90 degrees.
(30) While the invention has been described with reference to certain aspects or embodiments, it will be understood by those skilled in the art that various changes may be made and equivalents may be substituted for elements thereof without departing from the scope of the invention. In addition, many modifications may be made to adapt the teachings of the invention without departing from the essential scope thereof. Therefore, it is intended that the invention not be limited to the particular embodiment disclosed as the best mode contemplated for carrying out this invention, but that the invention will include all embodiments falling within the scope of the appended claims.