Reverse flow regenerative apparatus and method
View Patent ↗An exemplary embodiment provides a regenerative burner apparatus. The apparatus includes a burner housing having a gas channel and a single-stage heat regenerator equipped with a housing enclosing a fluid-porous heat regenerative media bed. A first gas passageway in the housing directly interconnects the gas channel and the lower surface of the media bed. A second gas passageway in the housing interconnects an opening in the housing communicating with the exterior and the upper surface of the media bed. This arrangement allows hot waste combustion gases to pass upwardly through the media bed so that any condensable contaminant in the gases condenses to a liquid and flows out of the bed under gravity before becoming solid and clogging the bed. The liquid contaminant may then be removed from the regenerator from a position below the media bed.
1. A regenerative burner apparatus, comprising:
a burner housing having a gas channel extending therethrough;
a single-stage heat regenerator provided with a housing enclosing a fluid-porous heat regenerative media bed having an upper surface and a lower surface, said housing having an opening communicating with an exterior of said apparatus;
a first gas passageway in said housing directly interconnecting said gas channel of said burner housing and said lower surface of said heat regenerative media bed; and
a second gas passageway in said housing interconnecting said opening in said housing communicating with said exterior and said upper surface of said heat regenerative media bed, said first and second gas passageways being in communication with each other substantially only through said heat regenerative media bed,
wherein said heat regenerative media bed is supported on a porous support within said burner housing and wherein the porous support is held above a bottom surface of said housing by a plurality of generally upright struts.
2. The apparatus of claim 1 , wherein said housing includes a liquid collection chamber directly beneath said lower surface of the heat regenerative media bed.
3. The apparatus of claim 2 , wherein said liquid collection chamber includes a sump in a bottom wall thereof.
4. The apparatus of claim 3 , wherein said sump has a perforated cover plate covering said sump.
5. The apparatus of claim 3 , wherein said sump has a liquid-removal outlet provided therein.
6. The apparatus of claim 2 , wherein said liquid collection chamber has a liquid-removal outlet provided therein.
7. The apparatus of claim 6 , wherein said liquid removal outlet includes a closure element removably positioned therein.
8. The apparatus of claim 6 , wherein said liquid removal outlet is connected to an open liquid drain tube.
9. The apparatus of claim 1 , wherein said heat regenerative media bed comprises a packed bed of discrete particles of refractory material.
10. The apparatus of claim 9 , wherein said discrete particles are spheres.
11. The apparatus of claim 10 , wherein said spheres have a diameter in a range of 1-1.5 inch.
12. The apparatus of claim 1 , wherein the generally upright struts are mutually spaced.
13. The apparatus of claim 1 , wherein said porous support is a grating having an upper surface supporting the media bed comprising openings separated by solid portions.
14. The apparatus of claim 13 , wherein said openings of said grating have a combined area at said upper surface within a range of 30-90% of a total area of the grating.
15. The apparatus of claim 13 , wherein said openings of said grating have a combined area at said upper surface within a range of 40-70% of the total area of the grating.
16. The apparatus of claim 13 , wherein said openings are elongated, having a width and a length, said width being smaller than said length.
17. The apparatus of claim 16 , wherein said width of said openings is in a range of 0.75 to 0.88 inch.
18. The apparatus of claim 13 , wherein said grating comprises an array of grating tiles of smaller upper surface area than said grating.
19. The apparatus of claim 1 , wherein said housing is in two parts comprising a lower part retaining said heat regenerative media bed and an upper part detachable from said lower part.
20. The apparatus of claim 19 , wherein said upper part and said lower part are joined by at least one hinge at one side of said housing.
21. The apparatus of claim 1 , wherein said housing has a layer of heat insulating refractory material lining said first passageway.
22. The apparatus of claim 1 , including a combustible-fuel burner housed in said burner housing.
23. A single stage regenerator for a regenerative burner apparatus, said regenerator comprising:
a housing enclosing a fluid-porous heat regenerative media bed having an upper surface and a lower surface, said housing having an opening communicating with an exterior of said apparatus and a port adapted for connection with a burner housing;
a first gas passageway in said housing directly interconnecting said port and said lower surface of said heat regenerative media bed; and
a second gas passageway in said housing interconnecting said opening in said housing communicating with said exterior and said upper surface of said heat regenerative media bed,
said first and second gas passageways being in communication with each other substantially only through said heat regenerative media bed,
wherein said heat regenerative media bed is supported on a porous support within said housing and wherein the porous support is held above a bottom surface of the housing by a plurality of generally upright struts.
24. A method of heating a furnace containing a charge to be heated and a vaporizable contaminant, wherein at least two regenerative burner apparatuses are used alternately to introduce heated combustion gases into the furnace and to recover heat from waste combustion gases vented from the furnace, and wherein said at least two regenerative burner apparatuses each employ a single stage heat regenerative burner bed having an upper surface and a lower surface, which method comprises alternately passing hot combustion gases from said furnace and then external combustion air through said heat regenerative media beds, wherein said hot combustion gases from said furnace are passed upwardly through at least one of said beds from said lower surface to said upper surface thereof, and said external combustion air is passed downwardly through said at least one of said heat regenerative beds from said upper surface to said lower surface thereof; wherein said contaminant in liquid form is removed from at least one of said apparatuses beneath said heat regenerative media beds thereof, and wherein said hot combustion gases are passed upwardly through said heat regenerative media beds at a constant rate of flow, except for a period of time during which said rate of flow is reduced to facilitate drainage of said contaminant in liquid form to drain from said bed.
25. The method of claim 24 , wherein said hot combustion gases are passed upwardly through said heat regenerative media beds at a rate of flow in a range of 100-2,000 feet per minute.
26. The method of claim 24 , wherein said hot combustion gases are passed upwardly through said heat regenerative media beds at a rate of flow in a range of 800-1,300 feet per minute.
27. The method of claim 24 , wherein said period of time is in a range of 2 to 8 minutes for every hour of operation of each regenerative burner apparatus.