The invention relates to burners for appliances such as furnaces and, in particular, relates to an ultra-low oxides of nitrogen (NOx) burner that provides flame carryover to accommodate multiple heat exchanger tubes in residential and commercial gas-fired furnaces.
Recently, new NOx emission requirements for residential gas-fired central furnaces have been implemented in an effort to reduce the environmental impact of their use. A few types of burners used on different types of gas-fired appliances are capable of meeting the specified NOx level. None, however, have been successfully applied to a residential gas-fired furnace of the type to which this invention pertains, for several reasons. In particular, the current burners are designed to fire into a single heat exchange chamber. Current residential furnace designs, however, have heat exchangers made with multiple tubes, clamshell or drum sections with separate burners firing into each tube or section. The cost of applying current single ULN system burner technologies to multiple section heat exchangers would be prohibitively expensive due to the cost of requiring multiple ULN system burners.
In one example, a burner for use with an igniter for firing a flame into a heat-exchanger includes a body having a sidewall that defines an interior chamber. A first opening in the body receives a pre-mixed mixture of air and fuel. A second opening in the body is in fluid communication with the first opening. A distributor is connected to the body and closes the second opening. The distributor includes a first portion and at least one curved second portion provided on the first portion. Each second portion includes a plurality of first perforations in fluid communication with the first opening in the body. The first perforations of one second portion are positioned adjacent to the igniter such that ignition of the pre-mix mixture flowing through the first perforations results in a flame through the second portion. A flange extends around the first portion and includes second perforations.
In another example, a device for mixing air and fuel for a burner includes a mixing wheel having circumferentially arranged openings for receiving air. A nozzle is connected to the mixing wheel and includes a longitudinal passage for receiving fuel. Radial openings extend from the longitudinal passage and upstream of the mixing wheel for delivering the fuel upstream of the mixing wheel. A restrictor plate is positioned upstream of the nozzle and includes circumferentially arranged openings for helping to mix the air and fuel for delivery to the burner.
Other objects and advantages and a fuller understanding of the invention will be had from the following detailed description of the preferred embodiments and the accompanying drawings.
The invention relates to burners for appliances and, in particular, relates to an ultra-low-NOx burner that provides flame carryover to accommodate multiple heat exchanger sections in residential and commercial gas-fired furnaces. Alternative appliances in which the burner of the present invention may be used include, for example, water heaters and, ovens.
In
A gas valve 40 and manifold or tube 42 cooperate to supply fuel to the burner 10. To this end, the gas valve 40 supplies fuel to the tube 42 in the manner A2. The controller 110 is connected to the gas valve 40 for controlling operation thereof. The tube 42 is fluidly connected to an upstream side of the mixer 60. The mixer 60 mixes the incoming air (provided by the blower 856) and fuel (provided by the gas valve 40) and directs a pre-mixed mixture to the burner 10 in the manner A3.
As shown in
In another example shown in
The adaptor 52 is inserted into the second passage 67 such that the adaptor and gas flow regulation device 56a are threaded together. Consequently, the first end 44 of the tube 42, the adaptor 54, the gas flow regulation device 56a, and the gas valve 40 are connected together in a sealed, fluid-tight manner. The projection 69 and passages 65, 67 are sized and shaped to help control or regulate the flow of gas from the gas valve 40 to the tube 42.
Referring to
A support bracket 80 is connected to the second end 46 of the tube 42 and secured to the interior of the tube 62 for helping to stabilize and center the tube 42. To this end, the support bracket 80 includes a centrally located opening 82 for receiving the tube 42.
A mixing wheel 90 is provided in the passage 68 and has a lip 95 extending into a first recess 76 in the tube 62. The first recess 76 extends circumferentially about the centerline 64. The mixing wheel 90 includes openings 92 arranged in an annular pattern about the centerline 63. In one example, the openings 98 are wedge-shaped or triangular and advantageously allow for more airflow through the mixing wheel 90 compared to circular openings. The mixing wheel 90 includes a central opening 94 that receives the second end 46 of the gas tube 42.
A nozzle 84 extends into the second end 46 of the gas tube 42 and upstream of the mixing wheel 90. The nozzle 84 includes a longitudinal passage 86 for receiving the incoming gas A2 from the tube 42. Openings 88 extend radially outward from the passage 86 to positions upstream of the mixing wheel 90.
A flow restrictor plate 96 is provided in the passage 68 downstream of both the mixing wheel 90 and the radial openings 88 in the nozzle 84. The flow restrictor plate 96 extends into a second recess 78 in the tube 62 that encircles the centerline 63. The flow restrictor plate 96 includes openings 98 symmetrically arranged in an annular pattern about the centerline 63. In one example, the openings 98 are circular. Regardless, the openings 98 improve fuel/air mixing and help eliminate combustor noise.
In operation, air A1 is received through the opening 70 in the tube 62 (see
A flange 254 extends from the sidewall 250 along the front side 238 of the body 232. The flange 254 has a rectangular shape and includes an opening 256 in fluid communication with the interior chamber 252. The opening 256 in the flange 254 receives a distributor 280.
A baffle 253 is provided in the interior chamber 252 to direct the incoming pre-mix mixture A3 to particular locations within the body 232, e.g., outwards toward the first and second ends 234, 236. The baffle 253 includes a base 242 positioned generally at the center of the body 232 and a pair of tapered legs 244 extending outward from the base in opposite directions. The base 242 can be, for example, U-shaped. The baffle 253 can extend the entire width of the interior chamber 252 between the ends 234, 236.
One or more openings 255 can extend through the legs 244. Alternatively, the openings 255 can be omitted (not shown). The openings 255 can be the same size or different sizes from one another. The presence of the openings 255 and/or the positioning of the baffle 253 relative to the distributor 280 and incoming pre-mix mixture A3 can help improve the operating range of the burner 10 and dampen noise during burner operation.
Referring to
The distributor 280 has an elongated shape, e.g., rectangular, that mimics the shape of the opening 256 in the flange 254. When the distributor 280 is secured to the flange 254 the first end 282 of the distributor is positioned at the first end 234 of the body 232 and the second end 284 of the flange is positioned at the second end 236 of the body. The distributor 280 and baffle 253 are separated by a gap 283 (see
The distributor 280 is formed from a thin, durable, and heat-resistant material, such as metal, metal screen or expanded metal. The distributor 280 includes a first portion 288 and at least one dimple or second portion 290 formed or provided on the first portion. The number, size, and spacing of the second portions 290 coincides with the number, size, and spacing of downstream heat exchanger sections (not shown) used in the furnace in which the burner 10 is used. In particular, each second portion 290 is aligned with an open end of an associated heat exchanger section such that the end of each section is in fluid communication with each second portion. Each second portion 290 is configured to provide a desired flame characteristic or profile from the burner 10 to the respective heat exchanger section.
In one example, the first portion 288 has a planar configuration and each second portion 290 is curved or dimple-shaped, e.g., rounded, concave or convex. Every second portion 290 may have the same configuration or different configurations from one another. A concave second portion 290 will provide a narrow, long or elongated flame while a convex second portion will provide a wider, more dispersed flame. Each second portion 290 may exhibit any circular or polygonal shape such as triangular, square or the like.
As shown in
A series of perforations 292 is formed in each concave portion 290 and extends entirely through the material of the distributor 280. The perforations 292 may exhibit any shape, e.g., circular, square, triangular, etc., and may be randomly spaced about the concave portion 290 or may have predetermined spacing. Each concave portion 90 can have substantially the same perforation 292 configuration. The perforations 292 cooperate with the concave portions 290 to produce an elongated flame for each concave portion that extends into the corresponding heat exchanger section (not shown) during use of the burner 10.
The perforations 292 and/or concave portions 290 may be individually or collectively tailored to provide a series of flames that have particular positions, sizes, and shapes. In one example, the perforations 292 can extend at angles through the concave portions 290 such that the pre-mixed mixture flow therethrough is directed to a common point downstream of the particular concave portion. This adds to flame stability and helps to focus the flame produced at each concave portion 290 towards the center of the respective heat exchanger section (not shown).
Alternatively or additionally, the first perforations 292 may have different sizes within the same concave portion 290. For example, the size of the first perforations 292 may increase in a direction extending towards the center of the concave portion 290 to maximize the flow area through the middle of the concave portion. Accordingly, the largest first perforation 292 may be located near or at the center of the concave portion 290. Consequently, the flame provided by that concave portion 290 is substantially aligned with the center of the respective heat exchanger section. In other words, the flame is concentrated at the center of the concave portion 290—where the largest flow area is located—and is minimized around the periphery of the concave portion—where the smallest flow area is located.
A series of carryover perforations 294 may also extend through the planar portion 288 of the distributor 280. The carryover perforations 294 may be similar, identical or different than the perforations 292 in the concave portions 290. As shown in
A portion 287 of the flange 285 extends substantially perpendicular to the first portion 288 and forms a perimeter around/surrounds the first portion. As shown, the portion 287 is rectangular. A series of openings 289 extend entirely through the portion 287 such that collectively the openings extends entirely around the first portion 289. The openings 289 are positioned downstream of the first and second portions 288, 290 and can vary in size and/or shape. The openings 289 help to achieve an intended burner surface pressure drop, which helps manage flame stability, prevent burner noise, and provide cooling for the distributor 280.
As shown in
The burner surface 300 can be contoured to match the contour of the distributor 280. That said, the burner surface 300 can include a planar portion 302, dimples or rounded portion(s) 304 extending from the planar portion, and a flange portion 306 extending entirely around the planar portion. The burner surface 300 can alternatively be planar across its entire length and therefore be planar overlying the second portions 290 (not shown). A cover retainer (not shown) can be secured to the flange 283 of the distributor 280 to secure the fiber mesh burner surface 300 thereto.
In operation, and referring back to
Alternatively, the igniter could be positioned adjacent to any other concave portion 290. In any case, when the igniter is activated, the air and fuel mixture A3 is ignited to produce a flame, indicated generally by arrow F1 in
Referring further to
The flame F1 in the leftmost concave portion 290 carries over or propagates across the planar portion 282 via the carryover perforations 294 and ignites the pre-mix mixture A3 flowing through the adjacent concave portion. The flame through this concave portion 290 likewise has a desired size and shape for the associated heat exchanger section (not shown). The flame propagation is repeated to each successive concave portion 290 via the corresponding carryover perforations 294 until a flame F1 is produced in the rightmost concave portion of the distributor 280 (as viewed in
A flame sensor (not shown) may be positioned adjacent to the rightmost concave portion 290 that produces the flame Fn in order to provide proof of ignition and propagation. Due to the repeatability and simplicity of the carryover perforations 294, the distributor 280 can be configured to provide a low-NOx flame to any number of similar or different heat exchanger sections in an efficient, reliable manner. Moreover, since all the concave portions 290 are fluidly connected via the carryover perforations 294, the igniter and flame sensor can be placed adjacent to any concave portion(s) and the low-NOx flame F1 will reliably propagate to all other concave portions.
In particular, the furnace 820 includes a furnace cabinet 822, a primary heat exchanger 824 that comprises a plurality of serpentine tubes 824a, a secondary, condensing heat exchanger 826, and a circulating air blower 828. Alternatively, the primary heat exchanger 824 may have a clamshell design (not shown) known in the art. Further detail about the construction of the furnace 820 is detailed in U.S. application Ser. No. 14/763,362, the entirety of which is incorporated by reference herein.
Referring also to
The secondary heat exchanger 826 (
The burner assembly 10 is attached to the vest panel 836a and is received in a rectangular opening 842 (
The distributor 280 is clamped between the body 232 and the exterior of the vest panel 836a. A combustion chamber defining cover 844 (
The combustion chamber cover 844 includes a plurality of openings (not shown) each aligned with one of the burner portions 90′ defined in the distributor 80′. The openings each receive an associated inlet side 846 of an associated heat exchange section 824a (
The flame of each portion 290 extends through the associated opening 844a of the cover 844 and into the inlet side 846 of the associated heat exchange section 824a. The flames are tailored such that the tip of each flame terminates at or adjacent to the inlet side 846 of each section 824a, i.e., the flames may barely extend into the interior of each tube.
As best seen in
Although the furnace 820 is shown and described as a condensing type furnace it should be noted that the burner 10 and/or mixer 60 shown and described herein can be used in a non-condensing type furnace. Typically, in this type of furnace, the secondary heat exchanger 826 would be eliminated. In addition, the burner assembly 10 would be mounted in alignment with a horizontal slot (not shown) that would be located in a lower section of the vest panel 836 nearer the horizontal segment 835a.
In this configuration, the sections 824a would have their inlet sides 846 join burner assembly 10 near the bottom of the vest panel 836. The upper or discharge ends 847 of the heat exchange sections 824a would be connected to a collection chamber located at the top of the vest panel 836 and in fluid communication with the induced draft blower 856.
The burner assembly 10 may advantageously be configured for use in high-efficiency residential furnaces. More specifically, by using both the first and secondary heat exchangers 824, 826 the condensing furnace 820 is capable of about 90% or greater efficiency. Using only the primary heat exchanger 824 produces a non-condensing furnace 820 capable of about 80-83% efficiency.
The preferred embodiments of the invention have been illustrated and described in detail. However, the present invention is not to be considered limited to the precise construction disclosed. Various adaptations, modifications and uses of the invention may occur to those skilled in the art to which the invention relates and the intention is to cover hereby all such adaptations, modifications, and uses which fall within the spirit or scope of the appended claims.
This applications claims priority to U.S. Provisional Application Ser. No. 62/977,541, filed Feb. 17, 2020, the entirety of which is incorporated herein by reference.
Number | Date | Country | |
---|---|---|---|
62977541 | Feb 2020 | US |