Burner panels, submerged combustion melters, and methods
a technology of combustion melters and burner panels, which is applied in the direction of combustion types, lighting and heating apparatuses, manufacturing tools, etc., can solve the problems of high turbulence and foaming, rapid melting of glass batches or other feedstocks, and it is not economically feasible to fabricate the entire burner using these materials. , to achieve the effect of reducing or eliminating problems
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embodiment 300
[0037]Referring again to FIG. 1A, fuel and oxidant conduits 4, 6, may extend above first major surface 8 by heights h1 and h2 respectively, which may be the same or different. Referring to embodiment 300 illustrated in FIG. 1C, fuel conduit 4 includes a distal end 28 and a proximal end 30, while oxidant conduit 6 includes a distal end 32 and a proximal end 34. Heights h1 and h2 of distal ends 28 and 32 may each range from about 0 (in other words, flush with major surface 8 or body panel 2), or in the alternative, the heights h1 and h2 may have a magnitude in the range of at least 5 cm or greater; or in the alternative, the heights h1 and h2 may have a magnitude in the range of at least 15 cm or greater; or in the alternative, the heights h1 and h2 may have a magnitude in the range of at least 25 cm or greater; or in the alternative, the heights h1 and h2 may have a magnitude in the range of at least 30 cm or greater. Theoretically the magnitude of heights h1 and h2 are limited only ...
embodiment 200
[0038]FIG. 1B illustrates schematically embodiment 200, where fuel conduit 4 and oxidant conduit 6 are angled toward each other at angles θ1 and θ2, which may be the same or different, and each may independently range from about 20 to about 90 degrees. All individual values and subranges from about 20 to about 90 degrees are included herein and disclosed herein. For example, the angles used can be from a lower limit of about 20, 21, 23, 25, 27, 29, 31, 33, 35, or 40 to an upper limit of 50, 52, 54, 56,58, 60, 75, 80, 85, or about 90 degrees. For example, the angles θ1 and θ2 may be in the range of from about 30 to about 80 degrees, or in the alternative, the angles θ1 and θ2 may be in the range of from about 40 to about 70 degrees, or in the alternative, the angles θ1 and θ2 may be in the range of from about 40 to about 50 degrees.
[0039]FIG. 1B also illustrates diameters d2 and d3 of fuel and oxidant conduits, respectively. Fuel and oxidant conduits 4 and 6 may be round or other cro...
embodiment 800
[0045]FIG. 3 illustrates schematically, embodiment 800, wherein fuel and oxidant are injected at the same point but may be injected at different times through a single conduit 36 connected fluidly at 38 to a “T” connection 40, and to an oxidant supply conduit 42 and associated valve or flow oscillator 46, and to a fuel supply conduit 44 and associated valve or flow oscillator 48. For example, a burner flowing only oxygen for 1 second and then only fuel for 1 second; thus, the oxygen and fuel would mix above the burner tip keeping most combustion away from the burner tip.
[0046]Other options are to use one or more slot nozzles for the introduction of the oxidant or fuel with small radial nozzles inside the oxidant or fuel slot for the introduction of the fuel or oxidant. This would change the glass and burner flows relationship relative to thermal stress and these designs are also easily scaled in size by increasing the length of the slot. Another version of this is replacing the radi...
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