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Temperature Range Typical Sources of Waste Heat Typical Uses Type of Heat Exchange (Gas Gas, Gas Liquid, etc.) Recovers Moisture Large Temperature Differentials Permitted No Cross Contamination Corrosive Gases Permitted with Special Construction Recovery Method Radiation Recuperator Soaking or annealing ovens, melting H furnaces, incinerators, radianttube Combustion air preheat GG Combustion air preheat GG X X X Convection Recuperator Soaking or annealing ovens, melting MH furnaces, incinerators, radianttube X X X Metallic Heat Wheel Hygroscopic Heat Wheel Ceramic Heat Wheel burners, reheat furnace LM Boiler exhaust, curing and drying Combustion air preheat, GG b space heat Combustion air preheat, GG X space heat c x c X X Platetype Heat Exchanger Exhaust from boilers, incinerators, L,M & turbines Combustion air preheat, space heat GG, LL X X Heat Pipe LH furnaces (secondary recovery) Drying, curing & baking ovens d X X Finnedtube Heat Exchanger L,M Boiler exhaust Boiler feedwater GL preheat X X e Wasteheat Boilers Exhaust from gas turbines, LH reciprocating engines, incinerators, Hot water or steam generation GL X e Tube Shelland Tube Exchanger L,M waste steam distillation condensates, coolants from engines, air compressors, bearings & lubricants Liquid feed flows GL, LL requiring heating X X burners, reheat furnace Table 8 Comparison of Heat Recovery Technologies a ovens M Boiler exhaust, curing and drying ovens MH Large boilers, incinerator exhaust, Combustion air preheat, GG X melting furnaces Drying, curing, and baking ovens Waste steam, air dryers, kilns (secondary recovery), reverberatory Combustion air preheat, boiler makeup water preheat, domestic hot GG,GL water, space heat furnaces Refrigeration condensates, waste steam distillation condensates, a. Sources: W. Turner. Energy Management Handbook, 2007; PG&E Energy Efficiency Information “Industrial Heat Recovery Strategies,” 1997 b. claimed by some vendors c. with a purge section added, crosscontamination can be limited to less than 1% by mass d. allowable temperatures and temperature differential limited by the phase equilibrium properties of the internal fluid e. can be constructed from corrosionresistant materials, but consider possible extensive damage to equipment caused by leaks or tube rupturesPDF Image | Waste Heat to Energy Tech Opportunities in US Industry
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