Towards Red mud Valorisation:

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Presentation transcript:

Towards Red mud Valorisation: Slag Valorisation Symposium Mechelen 02. April. 2019 Towards Red mud Valorisation: EAF Smelting process for iron recovery and slag design for use as precursor in the construction industry B. Xakalashe, B. Friedrich

Bayer Process – Generation of Red Mud Digestion Clarification Bauxite ores 30-54% Al2O3 Precipitation Production: >150 x 106 Mt/year Stock: 4 x 109 Mt Calcination Alumina

Red Mud – Resource and Challenges Potential resource of valuable elements Challenges: Generation of residue during extraction Low reactivity Leaching of heavy metals UP Components Fe2O3 Al2O3 CaO SiO2 TiO2 Na2O Typical range (wt.%) 5- 60 5-30 2-14 3-50 0.3-15 1-10 Trace elements: As, Be, Cd, Cr, Cu, Ga, Hg, K, Mn, Pb, REEs, Sc, Th, U, V, Zn, REEs

Zero Waste Valorisation of Red Mud IME Alumina Horizon 2020: MSCA–ETN Redmud “European Training Network for Zero-waste Valorisation of Bauxite Residue (Red Mud)“ http://etn.redmud.org/

EAF Smelting Process Red Mud (MYTILINEOS Aluminium of Greece) Component Fe2O3 Al2O3 CaO SiO2 TiO2 Na2O Cr2O3 V2O5 Wt.% 43.5 24.0 10.2 5.5 5.6 2 0.4 0.1 3C + Fe2O3 = 2Fe + 3CO Fe recovery to metal phase High melting slag Fluxing Lower operating temperatures Fluid slag Silica sand: aluminosilicate, vitreous slag (Inorganic polymer) Lime: calcium aluminate, crystalline slag (cement clinker) Silica fluxing lime fluxing RM

Experimental Procedure – EAF Smelting 100 kW DC furnace Operated (3-6kW) Batch mass:1.5kg Red Mud Lignite Coke: 0.1 x Red Mud (Reducing agent) Silica sand: 0.2 x Red Mud Lime: 0.4 x Red Mud Operating Temperature: 1500 – 1550oC Holding Time: 1 hour Slag cooling: Slow - 30oC/min UP slag Pig Iron (Fe)

Silica Fluxed Slag Fe removal achieved Vitreous slag achieved UP Components Fe2O3 Al2O3 CaO SiO2 TiO2 Na2O RM (wt.%) 43.5 24.0 10.2 5.5 5.6 1.8 Slag (wt.%) 1.2 36.8 15.3 38.0 7.3 2.4 Silica fluxed slag Intensity (A.U.) Red Mud

Lime Fluxed Slag Fe removal achieved Crystalline slag achieved UP Components Fe2O3 Al2O3 CaO SiO2 TiO2 Na2O RM (wt.%) 43.5 24.0 10.2 5.5 5.6 1.8 Slag (wt.%) 0.6 31.5 53.9 8.9 6.2 0.5 Silica fluxed slag Intensity (A.U.) Red Mud

Metal Analysis High recovery of Fe, Cr, V achieved (cleaning) Low Si and Ti recovery Pig iron can be used in secondary steel making Pig iron caUP Component Fe C Si Ti Cr V P S Silica fluxed 91.8 5 1.7 0.3 0.5 0.2 0.1 0.03 Recovery high - low Lime fluxed 93 5.1 0.01

Synergistic Waste Treatment with Red Mud MSWI BA: Municipal Solid Waste Incineration bottom ash Waste produce around all EU 20 million tonnes/year It’s a SiO2-CaO-Al2O3 acid slag (rich in silica ~50%) BOF: Basic Oxygen Furnace Slag (from Steel making) Waste produce around all EU 10 million tonnes/year It’s mainly CaO-FeO basic slag (rich in CaO ~40%)

Synergistic waste treatment with Red Mud Vitrified MSWI Bottom Ash Amorphous Low melting point MSWIBA Highly amorphous Acidic slags Highly crystalline Low melting point and low viscosity Combined recovery of Iron (BOF+RM) BOF RM Basic slags

Production of a vitreous slag under silica fluxing was achieved Conclusions Red mud was successfully smelted for iron recovery and conditioning of slag Cleaning of the mineral phase (slag) was achieved Production of a vitreous slag under silica fluxing was achieved Production of a crystalline slag enriched in calcium aluminate phases was demostrated Utilisation of the produced mineral phase in the construction industry could lead to zero waste valorisation of red mud UP