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Waste Heat to Energy Tech Opportunities in US Industry

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Waste Heat to Energy Tech Opportunities in US Industry ( waste-heat-energy-tech-opportunities-us-industry )

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economizers in the industrial sector could extend to the commercial sector and facilitate further energy savings. 4.7 Ethylene Furnaces Ethylene is the largest volume petrochemical product in the United States and functions as a key building block for many other chemical products. Over 28.3 million tons of ethylene were produced in 2004145 requiring about 645 TBtu of energy input. A key component of the production process is the pyrolysis furnace (Figure 28), where hydrocarbon feedstocks are cracked at temperatures around 1400­1600°F [760­870°C].146 The energy intensity of ethylene production varies depending on the feedstocks used: it requires about 16.7 million Btu/ton to produce ethylene from ethane and around 27.4 million Btu/ton when produced from naphtha/gas oil feedstocks. Based on the mix of feedstocks used in the United States, the average energy intensity for ethylene production is about 22.8 million Btu/ton, corresponding to a total of 654 TBtu/yr. It is estimated that about 58% of energy consumption or about 374 TBtu is consumed in the ethylene furnace alone.147 Ethylene crackers rely on fired gas or oil to provide heat to the pyrolysis reaction. The furnace consists of both a radiant section and convection section. The radiant section contains reactor tubes where the pyrolysis reaction takes place. The convection section consists of several heat exchangers where heat is exchanged between flue gases and process fluids such as steam and reactor feed. The flue gases leaving the convection section are at relatively low temperatures. As with other systems such as conventional steam boilers, typical furnace exhaust temperatures are around 300°F [150°C].148 It is fairly common for furnaces to be designed for higher efficiencies via cooling of the exhaust gases to lower temperature. In this case fouling on the outside of the heat exchanger is cleaned by steam lancing, while fouling on the inside is addressed by burning.149 Based on an assumed average exhaust temperature of 300°F [150°C], the unrecovered waste heat from these ethylene cracking furnaces is about 60 TBtu/yr (Table 19). Table 19 ­ Unrecovered Waste Heat and Work Potential from Ethylene Furnaces Ethylene Furnace 374.0 300 149 60.5 ­ 29% 17.8 Note: Sources and assumptions in Appendix A: Documentation of Waste Heat Estimates Figure 28 ­ Ethylene Furnace (Source: Selas Fluid) Source Energy Consumption Waste Heat 77°F [25°C] Ref Waste Heat 300°F [150°C] Ref Work Potential Assumed Average Exhaust Temperature Carnot Efficiency TBtu/yr °F °C TBtu/yr TBtu/yr TBtu/yr 49 ­

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