“…Depending on the atmospheric conditions in the off-gas treatment system, iron or iron oxide particles can be returned to the EAF. Thermodynamically, this treatment step drastically outperforms any HTMR natural gas RHF [5][6][7][8][9] 1250-1300°C Rotary hearth furnace Coke, binder, CZO, DRI/HBI Commercial* 200 (high Zn EAFD) natural gas Primus 10,11 1000-1100°C Multiple hearth Coal, air CZO, pig iron Commercial 100 furnace + EAF Ausmelt [12][13][14] 1250-1300°C Top Submerged Coal, CZO, Fe-slag Commercial 100 Lance furnace O 2 -enriched air (waste) ESRF 15,16 1300-1500°C EAF Binder, air, CZO, Pig iron, Commercial 36 electricity and slag Submerged 1300-1400°C Submerged plasma Coke, natural gas, CZO, Fe-slag (waste) Commercial 40 -60 Plasma [17][18][19] reactor fluxes, air, electricity PIZO [20][21][22] 1300-1500°C Induction furnace Coal, air, electricity CZO, pig iron Commercial 50 OxiCup 23 1500-1600°C Shaft furnace Coke, scrap, bricks CZO, molten Commercial 200 (dust (waste + cement + C) metal, and slag and sludge) Coke Packed Bed 24,25 1500-1600°C Shaft furnace Coke, fluxes, CZO, molten metal, Pilot Plant 10 O 2 -enriched air and slag LAMS 26,27 900-1100°C -CaCO 3 + heat CZO, Ca 2 Fe 2 O 5 for Lab-scale use in blast furnace EAFD+PVC pellets 28,29 800°C -PVC + heat ZnCl 2 , Fe+C pellets Lab-scale -* First large proof-of-concept plant is still ramping up to full production.…”