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Energy Efficient Process Heating. Energy Balance on Furnace. Energy Saving Opportunities From Energy Balance. Reduce opening losses: radiation and air exchange Reduce cooling losses Reduce conveyance losses Reduce storage losses Reduce wall losses Reduce flue losses
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Energy Saving Opportunities From Energy Balance • Reduce opening losses: radiation and air exchange • Reduce cooling losses • Reduce conveyance losses • Reduce storage losses • Reduce wall losses • Reduce flue losses • Improve internal heat transfer • Reduce air leakage into furnace • Control combustion air / oxygen • Reclaim heat • Pre-heat combustion air • Pre-heat load • Cascade heat to lower temperature processes
Cover Charge Wells • 2 ft x 4 ft open charge well radiates and convects heat • Cover charge well with mineral fiber insulation 75% of time • Savings = $1,500 /yr
Reducing Air Exchange in Continuous Ovens By Modifying Entrance/Exit
Reduce Conveyance Losses • Slow conveyor • Brazing oven at 1,900 F • Conveyor runs at 0.7 ft/min • Conveyor loaded 30% of time • Slow conveyor to 0.3 ft/min when unloaded • Reduces conveyor losses by 40%
Reduce Conveyance Losses Lighter conveyance fixtures reduce energy carryout losses
Reduce Storage Losses Larger batch sizes to reduce number of loads in heat treat ovens
Reduce Storage Losses Reduce bricks (thermal mass) on transport cars
Reduce Storage Losses Increase batch sizes in arc furnaces
Insulate Hot Surfaces • Insulate four lids at 400 F • Induction furnace efficiency = 51% • Savings = $17,0000 /yr
Flue Losses • Flue losses increase with: • Temperature • Flow
Reduce Flue Losses • Reduce Temperature • Improve internal heat transfer • Reduce Flow • Reduce air leakage into furnace • Combustion air control • Use O2 instead of ambient air for combustion
Counter Flow Heat Transfer Reduces Exhaust Temperature T Q Parallel Flow x T Q Counter Flow x
Convert Batch Cross Flow Processesto Continuous Counter Flow Batch crucible melting Counter-flow cupola melting
Replace Reverb (Cross Flow) with Stack (Counter Flow) Furnace and Pre-heat Charge Reverb Furnace Stack Furnace
Lead Melt Furnace: Place Scrap on Top and Drain Molten Lead From Bottom
Relocate Exhaust Portsto Increase Counter-flow Within Zones Increases convection heat transfer by 83% Contact length = 2 x (5 + 4 + 3 + 2 + 1) = 30 feet Contact length = (10 + 9 + 8 + 7 + 6 + 5 + 4 + 3 + 2 + 1) = 55 feet
Set Exhaust Dampers to Increase Counter Flow in Dry Off Oven Product In Product Out 100% open 75% open 50% open 25% open 12% open
Set Exhaust Dampers to Increase Counter Flow in Tile Kiln Tile Exit Tile Entrance
Reduce Air Leakage Heat in Flue Gases Negative Pressure Combustion Air Air Leaks Fuel
Seal Furnace Openings Seal opening around lid with mineral fiber blanket
Flue damper Counterweight Hydraulic cylinder Hydraulic power unit Controller Compensating line Pressure tap (not in line with opposing burner) Use Draft Control to Balance Pressure
Combustion with Air Minimum Combustion Air (Stoichiometric): CH4 + 2 (O2 + 3.8 N2) CO2 + 2 H2O + 7.6 N2 Excess Combustion Air: CH4+ 4 (O2 + 3.8 N2) CO2 + 2 H2O + 15.2 N2 + 2 O2
Excess Combustion AirDecreases Flame Temperature and Efficiency Air Preheat temperature) % Available Heat % Excess Air (% O2) in flue gases Flue gas temperature)
Combustion with Oxygen Eliminates Unnecessary Nitrogen • Combustion with Air • CH4 + 2 (O2 + 3.8 N2) > CO2 + 2 H2O + 7.6 N2 • Mair / Mfuel= [ (4 x 16) + (4 x 3.8 x 14) ] / (12 + 4) • Mair / Mfuel= 17.6 • Combustion with O2 • CH4 + 2 O2 > CO2 + 2 H2O • Mo2 / Mfuel = (4 x 16) / (12 + 4) • Mo2/ Mfuel= 4.0
Combustion with Oxygen Increases Efficiency
Reclaim Heat • Preheat combustion air • Preheat load/charge • Cascade to lower temperature process
ex. gas out Th2 = 950 F comb. air out Tc2 = 615 F comb. air in Tc1 = 95 F ex. gas in Th1 = 1,465 F Preheat Combustion Air with External Recuperator