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Textile Fiber Total Table A2.2 - Estimated Exhaust Gas Waste Heat Losses from Glass Melting Furnaces Glass Flat Glass Container Glass Pressed and Blown Glass Insulation Fiber Electric Melter Recuperative Melter Oxy-Fuel Recuperative Melter Oxy-Fuel % Fuel % Fuel input lost input lost as waste as waste heata heata 77°F 300°F Reference Reference 29% 12% 29% 12% 29% 12% 29% 12% 36% 23% 29% 12% 74% 57% 36% 23% 56% 40% 36% 23% 56% 40% 36% 23% Waste Heat Waste Heat Loss Loss (TBtu/Year)b (TBtu/Year)b 77°F 300°F Reference Reference 11.00 4.74 0.82 0.35 3.10 1.34 7.77 3.35 2.78 1.79 1.02 0.44 7.48 5.82 1.13 0.73 1.58 1.12 0.16 0.10 6.05 4.28 0.09 0.06 42.99 24.11 Maximum Carnot Work Efficiency Potential (TBtu/Year)c 77°F Reference 57% 6.31 57% 0.47 57% 1.78 57% 4.46 82% 2.29 57% 0.59 81% 6.08 82% 0.93 76% 1.20 82% 0.13 76% 4.62 82% 0.08 28.94 Regenerative Electric Boost Regenerative Electric Boost Oxy-Fuel Electric Melter Regenerative Direct Melter Oxy-Fuel Electric Melter a. Based on calculations described in section A.1. Percentage is reported as a percent total energy input. b. Based on fuel consumption reported in Table A 1. c. Maximum work obtainable from a heat engine operating between the combustion exhaust temperature and ambient temperature (77°F) A-7 of natural gas input, notPDF Image | Waste Heat to Energy Tech Opportunities in US Industry
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