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A burner apparatus utilizes a reticulated member to promote mixing of a fuel and oxidizer mixture. A plurality of exit ports, disposed on a wall or surface encapsulating the reticulated member, defines exit streams of the mixture that produces flames upon combustion. The burner apparatus have high h

A burner apparatus utilizes a reticulated member to promote mixing of a fuel and oxidizer mixture. A plurality of exit ports, disposed on a wall or surface encapsulating the reticulated member, defines exit streams of the mixture that produces flames upon combustion. The burner apparatus have high heating rates and turndown ratios of at least about 18:1.

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What is claimed is: 1. A burner comprising: means for mixing fuel and oxidizer, comprising a porous member having a plurality of random flow paths; and a peripheral wall having a plurality of exit ports disposed therein positioned downstream of the means for mixing wherein the exit ports are constr

What is claimed is: 1. A burner comprising: means for mixing fuel and oxidizer, comprising a porous member having a plurality of random flow paths; and a peripheral wall having a plurality of exit ports disposed therein positioned downstream of the means for mixing wherein the exit ports are constructed and arranged to effect a minimum flow velocity of the mixture of fuel and oxidizer, wherein the porous member comprises an annular metal foam disposed adjacent an inner surface of the peripheral wall. 2. The burner of claim 1, wherein said porous member has a pore density in a range of about 10 pores per inch to about 60 pores per inch. 3. The burner of claim 1, wherein said plurality of exit ports define a port loading in a range of about 15,000 BTU/hr/in2 to about 60,000 BTU/hr/in2 during combustion of the mixture. 4. The burner of claim 1, wherein, said plurality of exit ports are sized to provide an exit stream velocity of the mixture that results in flame combustion. 5. The burner of claim 1, further comprising a venturi assembly disposed upstream of the means for mixing fluidly connecting the means for mixing and a fuel source. 6. The burner of claim 1, wherein the burner provides a maximum firing rate of at least about 12,700 BTU/hr during combustion of the mixture of fuel and oxidizer. 7. The burner of claim 6, wherein the burner provides a minimum firing rate of less than about 680 BTU/hr during combustion of the mixture of fuel and oxidizer. 8. The burner of claim 1, wherein the burner has a turndown ratio of at least about 18.7 to 1. 9. The burner of claim 1, wherein said annular metal foam has a pore density in a range of about 10 pores per inch to about 60 pores per inch. 10. The burner of claim 1, wherein the porous member is disposed in a burner cavity defined by the peripheral wall and a cap. 11. A burner apparatus comprising the burner of claim 1 disposed in a cooking appliance 12. The burner apparatus of claim 11, wherein the cooking appliance comprises a cooking utensil support assembly providing a separation distance of less than 2 inches between a heating surface of a cooking utensil and a top surface of the burner. 13. The burner apparatus of claim 11, wherein the cooking appliance does not comprise a forced air assembly. 14. A method of combustion comprising: introducing a naturally aspirated fuel/air mixture into a burner without using forced air; passing the fuel/air mixture through a member having a plurality of random flow paths, and a plurality of ports different from the member; and combusting the fuel/air mixture downstream of the plurality of exit ports. 15. The method of claim 14, wherein the member comprises a metal foam. 16. The method of claim 14, wherein the plurality of exit ports are disposed in a peripheral wall at least partially enclosing the member. 17. The method of claim 16, wherein the member comprises a porous ring disposed adjacent an inner surface of the peripheral wall. 18. The method of claim 14, wherein the plurality of ports are sized and spaced to provide a port loading in a range of about 15,000 BTU/hr/in2 to about 60,000 BTU/hr/in2 during combustion of the fuel/air mixture. 19. The method of claim 14, wherein the burner is capable of providing a maximum firing rate of at least about 12,700 BTU/hr during combustion of the fuel/air mixture. 20. The method of claim 19, wherein the burner has a nominal two-inch diameter and is capable of having a minimum firing rate of less than about 680 BTU/hr during combustion of the fuel/air mixture. 21. The method of claim 14, wherein the burner is capable of providing a minimum firing rate of less than about 680 BTU/hr during combustion of the fuel/air mixture. 22. The method of claim 14, wherein the burner is capable of providing a turndown ratio of at least about 18.7 to 1. 23. The method of claim 14, wherein the member comprises a reticulated structure. 24. The method of claim 14, wherein the burner is capable of having a Reynold's Number of greater than 13 at a peak velocity. 25. The method of claim 14, wherein the burner is capable of having a Reynold's Number of greater than 46 at a peak velocity. 26. The method of claim 14, wherein the member has a pore density in the range of about 10 pores per inch to about 60 pores per inch. 27. The method of claim 14, further comprising introducing the fuel/air mixture into a venturi assembly upstream of the member. 28. The method of claim 14, wherein the burner is disposed in a heating appliance. 29. The method of claim 14, wherein the burner is disposed in a cooking appliance. 30. The method of claim. 29, wherein the cooking appliance comprises a cooking utensil support assembly providing a separation distance of less than about 2 inches between a heating surface of a cooking utensil and a top surface of the burner. 31. The method of claim 14, wherein the burner is capable of providing a turndown ratio of least about 15 to 1. 32. The method of claim 14, further comprising inducing drawing of air into the burner. 33. The method of claim 14, wherein the burner, has a nominal two-inch diameter and is capable of having a maximum fixing rate of at least about 12,700 BTU/hr during combustion of the fuel/air mixture. 34. The method of claim 14, further comprising inhibiting or preventing flashback during combustion.