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Restart of BF#2 Using Durfee Method
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Salient Features o Inner volume: 3,814 m3 o Working volume: 3,230 m3
o Number of tuyeres: 34 o Charging system: with belt conveyor and Paul Wurth Parallel hopper Bell Less Top®, o Cooling system o Under-hearth: water pipes o Hearth: cast-iron staves o Tuyere belt: cast iron staves o Bosh to lower Stack: copper staves o Middle Stack to Throat: cast iron staves o PCI design for 200 kg/thm o Top Gas Recovery Turbine 14 MW
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Chilled Hearth Condition
Start Up Situation Hot Metal and Slag Solidified Chilled Hearth Condition Unprepared Shut down for 162 days
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Major tasks of Recovery Process
Re-instate connection between Tap hole and Tuyeres Recover the Thermal Status Melting of Solidified Metal and Slag Stabilize the Process
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Process discussed for Revival Durfee Process
Blowing Hot Blast through Tap hole enriched with Oxygen Normally Used for Prepared shut downs Less aggressive on Refractory Oxy-Fuel Process Installing Oxy-fuel burners through Tap holes equipped with external fuel + Oxygen Can be used for severe chilled recoveries
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Process Selected for Revival
Durfee Process Reasons Furnace had coke O/C ratio 2.1 Extra Coke of around 90 T available in Lower Stack
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Durfee Process
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Time Line of Start Up Day-2 Day-3 Day-4 Day-5
Blast Introduced through Durfee No Blast flow observed Durfee removed and Tap Hole Lanced for 20 Hrs Day-2 Durfee Re-Introduced Blast Flow Average 7200m3/hr Blast Enriched with Oxygen Day-3 Cumulative Flow through Durfee ~ Nm3 4 Tuyere Opened above Tap Hole No 2 Durfee removed and First slag cast through Tap Hole No 2 Day-4 Hot Metal and Slag in Dry Pit Day-5 Hot Metal taken in Torpedo Ladle GCP Connected
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Tuyere Opening & Blast Volume Increase
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Sequence of Tuyere Opening
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Hot Metal Production Tons Per Day
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