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or to be transformed into electricity. The authors estimated in 370 kWh per ton of liquid steel. However, only up to 24% of the energy existing in the exhaust gas could be recovered to generate process steam or electricity for on-site use. Therefore, energy consumption could be reduced between 60 and 80 kWh per ton of liquid steel, and CO2 emissions could be reduced by up to 45 kg per ton of liquid steel. Later on, a test rig using 1500 kg of molten salts at 430 °C [31] was designed (Figure 5, left) and implemented (Figure 5, right) to experimentally test the concept proposed by Steinparzer et al. [30]. So far, there are not published results about its performance. Figure 5. Schematic view of the design of the pilot plant [30] (left); and picture of the real molten salt tank [31] (right) Recently, Raine et al. [32] investigated the potential uses of intermittent IWH (0.5 PJ/y) from three steelmaking industries in the United Kingdom using a thermal energy steam accumulator as TES system to be further reused for various processes on-site by means of an internal district heating (DH) network. Four IWH sources at a temperature range of 600-1500 °C were identified: steam from arc furnace flue gas, hot water from arc furnace flue gas, hot water recovered from reheat furnace flue gas and cooling water. High pressure steam accumulators and regenerator ceramic materials were proposed as TES system. The estimated annual CO2 savings as a result of implementing these TES systems were 22482 tCO2. Finally, from the point of view of recovering IWH from metal molten slags, Barati et al. [33] estimated a worldwide amount of IWH recovered from the slags at temperatures in the range of 1200-1600 °C of 792 PJ/y. Moreover, they reported the possibility of using the molten slags both as heat carrier and TES medium. 9PDF Image | Thermal Energy Storage TES Industrial Waste Heat Recovery
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