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Country Scale of the study Source Exhaust temperatu re (oC) TES material material amount Storage capacity (MWh) Heat sink Distance (km) Savings Ref. n.a. N Steelworks n.a. (1) PCM (2) Zeolite n.a. n.a. Utility plant 30 n.a. [62] Germany N Aluminium factory / Incineration n.a. (1) Sodium acetate trihydrate (2) Zeolite 15t (1) 2.4 (2) 3.4 Industrial drying, air conditioning and swimming pools n.a. DH network (1) 10 (2) 7 Energy costs drop to [67] 15 €/MWh Sweden Sweden N N n.a. n.a. n.a. n.a. Erythritol n.a. n.a. n.a. n.a. 10 – 50 48 n.a. [68] Japan N Sludge 70–350 58oC) n.a. 2 Civic 2.5 gymnasium 68-95% [71] CO2 emissions: 71-93 Japan N 200 Erythritol 17.5 t 1.5 Hot and cold water 20 88-92.3 % [72] CO2 emissions: 73.4- [73] Sweden N Steelworks 250 Sodium hydroxide 17.5 t 2.3 Chemical 10 plant 91.4 % [74] CO2 emissions: 82.5 Japan Sweden N N Steelworks CHP plant 250 Sodium carbonate / Sodium hydroxide 17.5 t n.a. 1.9 Chemical 10 plant % Energy consumption: 90.5 % CO2 emissions: 81.4 % n.a. [76] [77] Table 9. Summary of the M-TES systems for off-site IWH reuse IWH source TES system TES Heat demand incinerator n.a. (2) PCM (melting at 118 oC) % Energy consumption: Erythritol (1) PCM (melting at n.a. [70] Energy consumption: n.a. Erythritol 224 DH network 20 79.8 % Energy consumption: 32PDF Image | Thermal Energy Storage TES Industrial Waste Heat Recovery
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