Selective oxy-fuel boost burner system and method for a regenerative furnace

Patent metadata

Field	Value
Publication number	US-9657945-B2
Application number	US-201514721297-A
Country	US
Kind code	B2
Filing date	May 26, 2015
Priority date	May 26, 2015
Publication date	May 23, 2017
Grant date	May 23, 2017

Abstract

An oxy-fuel boost burner for a regenerative furnace having a pair of regenerator ports configured to alternately fire into and exhaust from the furnace, including at least one burner element corresponding to each of the regenerator ports by being positioned to fire into a complimentary region of the furnace, each burner element including a selective distribution nozzle configured to flow a first reactant and a proportional distribution nozzle configured to flow a second reactant, and a controller programmed to identify which regenerator port is currently firing and which is currently exhausting and to independently control the first reactant flow to each selective distribution nozzle such that the at least one burner element corresponding to the currently firing regenerator port has a greater than average first reactant flow and the at least one burner element corresponding to the currently exhausting regenerator port as a less than average first reactant flow.

First claim

The invention claimed is:

1. An oxy-fuel boost burner for a regenerative furnace having a pair of regenerator ports configured to alternately fire into and exhaust from the furnace, the boost burner comprising:
at least two burner elements, wherein at least one of the burner elements corresponds to each of the regenerator ports such that a regenerator port and its corresponding at least one burner element are positioned to fire into complimentary regions of the furnace, each burner element comprising:
a selective distribution nozzle configured to flow a first reactant; and
a proportional distribution nozzle configured to flow a second reactant; and
a controller programmed:
to identify which regenerator port is currently firing and which regenerator port is currently exhausting;
to control the second reactant flow to be substantially proportionally distributed to the proportional distribution nozzles; and
to independently control the first reactant flow to each selective distribution nozzle such that the at least one burner element corresponding to the currently firing regenerator port is active and the at least one burner element corresponding to the currently exhausting regenerator port is passive, wherein first reactant flow in the selective distribution nozzle of an active burner element is greater than an average first reactant flow to the selective distribution nozzles and first reactant flow in the selective distribution nozzle of a passive burner element is less than the average first reactant flow to the selective distribution nozzles;

wherein the second reactant is substantially proportionally distributed to the proportional distribution nozzles; and
wherein the first reactant is one of a fuel and an oxidant and wherein the second reactant is the other of a fuel and an oxidant.

2. The boost burner of claim 1 , wherein the proportional distribution nozzle is an annular nozzle surrounding the selective distribution nozzle.

3. The boost burner of claim 1 , wherein the first reactant is a fuel and the second reactant is an oxidant.

4. The boost burner of claim 3 , further comprising:
at least one staging nozzle spaced apart from each of the burner elements and configured to flow a secondary oxidant;
wherein the controller is further programmed to control a staging ratio to be less than or equal to about 75%, wherein the staging ratio is the ratio of the oxygen contained in the secondary oxidant flow to the sum of the oxidant flowed through the proportional distribution nozzles and the staging nozzle.

5. The boost burner of claim 1 , wherein the regenerator ports are mounted in an end wall of the furnace, and wherein the boost burner is mounted in an opposite end wall of the furnace.

6. The boost burner of claim 1 , wherein the regenerator ports are positioned in opposite sidewalls near an end wall of the furnace, each regenerator port being at a non-perpendicular angle to its respective sidewall, and wherein the boost burner is mounted in an opposite end wall of the furnace.

7. The boost burner of claim 1 , wherein the regenerator ports are positioned in opposite sidewalls near an end wall of the furnace, each regenerator port being at a non-perpendicular angle to its respective sidewall, and wherein the boost burner is mounted in a roof of the furnace.

8. The boost burner of claim 1 , wherein the burner elements are mounted in the same housing.

9. The boost burner of claim 1 , wherein at least one of the burner elements is mounted in a separate housing from at least one other of the burner elements.

10. The boost burner of claim 1 , wherein the controller is programmed to control first reactant flow to a passive selective distribution nozzle to be greater than zero and less than or equal to half the first reactant flow rate of an active selective distribution nozzle.

11. The boost burner of claim 1 ,
wherein the oxidant flowing through the burner elements has an oxygen concentration of equal to or greater than about 23%.

12. The boost burner of claim 1 ,
wherein the selective distribution nozzle of an active burner element has an active jet flow rate and wherein the selective distribution nozzle of a passive burner element has a passive jet flow rate; and
wherein the controller is programmed to control the ratio of the active jet flow rate to the passive jet flow rate to be from about 5 to about 40.

13. The boost burner of claim 1 , wherein a passive burner element has an equivalence ratio of from about 0.2 to about 1, and wherein an active burner element has an equivalence ratio of from about 1 to about 10, wherein the equivalence ratio is the ratio of theoretical stoichiometric oxidant flow required to combust the actual fuel flow through the burner element to actual oxidant flow through the burner element.

14. A method of operating the boost burner of claim 1 in a regenerative furnace having a pair of regenerator ports configured to alternately fire into and exhaust from the furnace, the method comprising:
flowing a second reactant at a second reactant flow rate through each of the proportional distribution nozzles;
identifying which regenerator port is currently firing and which regenerator port is current exhausting;
selecting at least one of the selective distribution nozzles to be active and at least one of the selective distribution nozzles to be passive, the at least one active distribution nozzle having a flame zone that is complimentary to a flame zone of the regenerator port currently firing;
flowing the second reactant substantially proportionally to each of the proportional distribution nozzles;
flowing the first reactant at an active jet flow rate through the at least one active selective distribution nozzle; and
flowing the first reactant at a passive jet flow rate through the at least one passive selective distribution nozzle;
wherein the active jet flow rate is greater than an average flow rate through the selective distribution nozzles and the passive jet flow rate is less than the average flow rate through the selective distribution nozzles.

Assignees

• Air Prod & Chem

Inventors

• Gangoli Shailesh Pradeep
• Hewertson Russell James
• Sane Anup Vasant
• Palazzolo John C
• He Xiaoyi

Classifications

• F23D14/48

  Nozzles · CPC title

• F23D14/32

  using a mixture of gaseous fuel and pure oxygen or oxygen-enriched air (F23D14/38 takes precedence) · CPC title

• F23C2900/05081

  Disposition of burners relative to each other creating specific heat patterns · CPC title

• F27B7/34 Primary

  Arrangements of heating devices · CPC title

• F23C5/08

  Disposition of burners · CPC title