Oxy-boost control in furnaces

• US 6,454,562 B1
• Filed: 04/20/2000
• Issued: 09/24/2002
• Est. Priority Date: 04/20/2000
• Status: Expired due to Term

• Current Assignee: L'Air Liquide SA
• Original Assignee: American Air Liquide Incorporated (L'Air Liquide SA), L'Air Liquide SA
• Inventors: Joshi, Mahendra L., Marin, Ovidiu
• Primary Examiner(s): Lu, Jiping
• Application Number:
  US09/553,418
• Time in Patent Office: 887 Days
• Field of Search: 432/159, 432/17, 432/19, 432/24, 432/36, 432/37, 432/146, 432/149, 432/47, 65/292.1, 651/61, 651/62, 65D/IG.13
• US Class Current: 432/17
• CPC Class Codes: C03B 5/2353 by combustion with pure oxygen or oxygen-enriched air, e.g. using oxy-fuel burners or oxygen lances
• CPC Class Codes: C03B 5/24 Automatically regulating the melting process
• CPC Class Codes: Y02P 40/50 Glass production, e.g. reusing waste heat during processing or shaping
• CPC Class Codes: Y02P 40/57 Improving the yield, e-g- reduction of reject rates
• CPC Class Codes: Y10S 65/13 Computer control

Abstract

A process controls oxy-boost firing and air-fuel burner firing in furnaces, including large glass furnaces such as float furnaces. The large side-fired regenerative float furnaces use oxy-boost firing for a variety of reasons, including production increase, improved glass quality, lowering of superstructure temperatures, and reduction of emissions. An adaptive controller receives input data from process parameter sensors throughout the furnace, and adjusts its control logic for controlling both the oxy-boost burners and the air-fuel port burners.

Claims

1. A process of operating a furnace, comprising the steps of:

firing an oxy-fuel burner into the furnace to heat a load;

firing an air-fuel burner into the furnace to heat the load;

measuring a furnace process parameter;

inputting the measured process parameter into a model-free controller; and

controlling both the firing of the oxy-burner and the firing of the air-fuel burner with the controller based on the measured process parameter.

2. A process in accordance with claim 1, wherein the furnace process parameter is selected from the group consisting of crown temperature, bottom temperature, furnace exhaust gas composition, furnace exhaust gas temperature, processed load quality, refractory condition, regenerator pressure, furnace pressure, and pull rate when glass is disposed within the furnace.

6. A system in accordance with claim 2, wherein the at least one furnace condition input device comprises an input device adapted for communicating data to the controller indicative of glass quality when glass is disposed within the furnace.

7. A system in accordance with claim 2, wherein the at least one furnace condition input device comprises an input device adapted for communicating data to the controller indicative of batch line location in the furnace when glass is disposed within the furnace.

8. A system in accordance with claim 2, wherein the at least one furnace condition input device comprises an input device adapted for communicating data to the controller indicative of furnace pull rate.

3. A system useful for heating a product, comprising:

a furnace having a sidewall and an interior space;

at least one oxy-fuel burner positioned to direct a flame into the furnace interior space;

a source of an oxidant in fluid communication with the at least one oxy-fuel burner, the oxidant comprising oxygen, oxygen enriched gas, or combinations thereof;

a source of fuel in fluid communication with the at least one oxy-fuel burner;

a first valve set interposed between the oxy-fuel burner and the sources of fuel and oxidant, the first valve set operable to control the flow of oxidant and fuel to the at least one oxy-fuel burner;

at least one air-fuel burner positioned to direct a flame into the furnace interior space;

a source of air in fluid communication with the at least one air-fuel burner;

a source of fuel in fluid communication with the at least one air-fuel burner;

a second valve set interposed between the air-fuel burner and the sources of fuel and air, the second valve set operable to control the flow of air and fuel to the at least one air-fuel burner;

at least one furnace condition input device generating at least one output signal; and

a model-free controller in communication with the at least one furnace condition input device to receive the at least one furnace condition input device output signal, the controller having a setpoint value for the at least one furnace value, the controller generating at least one control signal based on a comparison of the input and setpoint values, the controller being in communication with the first valve set to communicate the at least one control signal to the first valve set to set the flow rates of oxidant and fuel through the first valve set and to the oxy-fuel burner, and the controller being in communication with the second valve set to communicate the at least one control signal to the second valve set to set the flow rates of air and fuel through the second valve set and to the air-fuel burner.

4. A system in accordance with claim 3, wherein the at least one furnace condition input device comprises at least one sensor positioned to sense at least one condition of the furnace.

5. A system in accordance with claim 4, wherein the furnace has a crown and a bottom, and the at least one sensor is selected from the group consisting of a temperature sensor in the furnace crown, a temperature sensor in the furnace bottom, a pressure sensor in fluid communication with the furnace interior, an exhaust gas sensor in fluid communication with the furnace interior, and a temperature sensor for sensing the temperature of the furnace exhaust gas.

9. A system in accordance with claim 3, wherein the at least one control signal comprises a first control signal set and a second control signal set, the controller being in communication with the first valve set to communicate the first control signal set to the first valve set to set the flow rates of oxidant and fuel through the first valve set and to the oxy-fuel burner, the controller being in communication with the second valve set to communicate the second control signal set to the second valve set to set the flow rates of oxidant and fuel through the second valve set and to the port burner.