REHEAT FURNACE UPGRADE

A top fired walking beam furnace rated at 75 t/hr was fitted with 12 Hauck SVG125 burners in the charge section of the furnace. Each burner was rated at nominal 1MBtu/hr each. The burners were fired with ambient temperature combustion air. The firing rate of the burner was controlled using a two position solenoid valve in the combustion air supply and each valve was fitted with a mechanically set low and high fire setting. The rising and falling pressure of the combustion air at the burner was used to control the amount of gas at the burner and each of the SVG burners was ignited using a spark electrode supplied with the burner.

IMPLEMENTATION

The modifications of the furnace included the installation of the new burner systems; the extension of the heating chamber of the furnace by six feet; and the replacement of the loading skids with water cooled skids. The high velocity burners were installed in prefabricated modules designed to accommodate two burners per module. The burners were fitted prior to installation of the module on the furnace. High Velocity Burners were also installed at the old baffle wall. These burners were completed in a similar fashion to the charge end modules. Only minor steel work modifications were required in this area.

CONCLUSION

This is a unique example of the technique of high intensity convective heating for generating significant material preheating which can be used to increase the production rate of a furnace. The mathematical developed for this application predicted a production increase of 17% and the furnace has now consistently demonstrated sustained production rates over 22% greater.

Oxidation rates will be gradually improved by the installation of Level II controls. There was also a small improvement in the specific fuel consumption of the furnace.

The static thermal model developed for this project is a reliable tool for the prediction of the performance of the modified furnace. The use of the high velocity burners in the mixing zone was an effective substitute for the customary baffle wall. In addition, the removal of the baffle wall removed the shadowing effect on the incoming load. The extra turbulence in the mixing zone also had a significant impact on the amount of heat removed from the POC as it is vented from the furnace.

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HOMEPAGE   -   CONTACT THERMIX   -   BURNERS   -   FURNACES   -   BIOMASS