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Pritii Tam, Chiara Cardenia, Buhle Xakalashe,

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Presentation on theme: "Pritii Tam, Chiara Cardenia, Buhle Xakalashe,"— Presentation transcript:

1 Conceptual Flowsheets for Combined Recovery of Fe and Al from Bauxite Residue
Pritii Tam, Chiara Cardenia, Buhle Xakalashe, Vicky Vassiliadou, Dimitrios Panias, Bernd Friedrich

2 The Bayer Process BAUXITE RESIDUE (RED MUD) Digestion Bauxite ores
Aluminium of Greece (AoG) bauxite residue waste storage at Agios Nikolaos site, Greece. Image by Evangelos Mouchos©. Digestion BAUXITE RESIDUE (RED MUD) Bauxite ores Clarification Precipitation Calcination Production: 150 x 106 Mt/year Stock: 4 x 109 Mt Alumina

3 Katoite - Ca3Al2(SiO3)(OH)10 Cancrinite - Na6Ca2(AlSiO4)6(CO3)2 (H2O)2
Major Components Chemical Composition Mineralogical Phases Hematite - Fe2O3 Goethite - Fe2O3·H2O Gibbsite - Al2O3·3H2O Boehmite – AlOOH Diaspore – AlOOH Katoite - Ca3Al2(SiO3)(OH)10 Cancrinite - Na6Ca2(AlSiO4)6(CO3)2 (H2O)2 Calcite - CaCO3 Perovskite- CaTiO3 Anatase - TiO2 Rutile - TiO2 Quartz - SiO2 Composition of Greek Bauxite Residue XRF Glass Disc (Chemical Analysis) and XRD (Mineralogical Analysis)

4 Iron in Bauxite Residue
5%<Fe2O3<60% Hematite (Fe2O3) Goethite (FeO(OH)) Magnetite (Fe3O4) Fe2O3>Fe3O4>FeO>Fe Evans (2015)

5 Fe Fe Targeting Iron… BR Flux C BR C Reductive Smelting Smelting
High Temperatures Reduction to Metallic Fe Form (Pig Iron) Fe BR Smelting Flux Molten Slag C Reductive Roasting Reducing Hematite into Magnetic (Magnetic) Fe Roasting Reduction Magnetic Separation BR C Residue (Non-Magnetic)

6 Targeting Dielectric Phases using Electromagnetic Energy
Microwave Reduction Microwave Reduction Targeting Dielectric Phases using Electromagnetic Energy (Combination) Fe Microwave Reduction BR Electric Arc Furnace, Blast Furnace Slag for downstream recovery, building materials, mineral wool. Sinter Residue C Completing in a fraction of time compared to traditional smelting or roasting furnaces Roasting Furnaces: Smaller Tube Furnaces and scaling up to Rotary Kilns Smelting Furnaces: Electric Arc Furnace, Blast Furnace Other Types: Microwave

7 Targeting Iron… PROCESSES AUTHORS Fe Recovery %
Soda ash/lime roasting process prior to magnetic separation of Fe, and alkaline leaching for Al and Na Liu et al. Mishra et al. Cardenia et al. 51.2% 94% metallization 99% metallization Smelting using calcite or dolomite as fluxes followed by further downstream processing Kaussen et al. Borra et al. Erçağ and Apak. Tam et al. Gharda. Balomenos et al. Alkan et al. Dobos et al. 93% 98% 95% 97% 97.3% Microwave reductive roasting technique followed by wet magnetic separation Samouhos et al. 63.3% metallization

8 Aluminium in Bauxite Residue
5%<Al2O3<30% Simple Al-based Diaspore, Gibbsite, Boehmite DSP-based Cancrinite, Sodalite, Ca-based Grossular Products Leachable Sodium Aluminate Evans (2015)

9 Combined Soda Sinter Process Combined Smelting Process
Targeting Aluminium… Combined Soda Sinter Process Conversion of Al-mineral Phases to Leachable NaAlO2 (Leachable) Al,Na BR Roasting Alkaline Leaching C Leached Residue Na2CO3 Combined Smelting Process Fe Recovery and Conditioning Slag to Leachable Calcium Aluminates (Leachable) Al,Na Smelting, Calcium Aluminate Conditioning Alkaline Leaching BR Flux Leached Residue C Fe

10 Targeting Aluminium… PROCESSES AUTHORS Al Recovery %
Soda ash/lime roasting process prior to magnetic separation of Fe, and alkaline leaching for Al and Na Kaussen et al. Liu et al. Mishra et al. Borra et al. Hertel et al. 89% 75.7% 83.1% 75% 76% Smelting using calcite or dolomite as fluxes followed by further downstream processing <50% (Alkaline, below 200 gpl) 90% (High Alkaline, above 500 gpl) Erçağ and Apak. 85% (H2SO4 Acid) Tam et al. 43% (Caustic, below 300 gpl) Dobos et al. 84% (Nepheline, after smelting) 80% (Calcium Aluminate slag)

11 Flowsheet (I) + Two-step process of recovering firstly Al and
BR + Two-step process of recovering firstly Al and Na, followed by Fe + High throughput for the smelter + Reducing Na gaseous losses in smelting + Enriched and conditioned slag for downstream processing - Time, cost and energy intensive with introduction of leaching step before smelting C Soda Sintering Na2CO3 NaAlO2 Mild Alkaline Leaching Al, Na Recovery Metallic Fe Carbothermic Reductive Smelting C Fe Recovery Flux Leaching residue for Ti, Sc and REE recovery

12 Flowsheet (II) BR Carbothermic Reductive Smelting C Fe Recovery Flux
Conditioned Slag C Soda Sintering Caustic Leaching C Soda Sintering Na2CO3 Na2CO3 Cl Al, Na Recovery Mild Alkaline Leaching Al, Ti Recovery For electrolysis CaCO3 LR for Ti, Sc and REE recovery Al, Na Recovery LR for Ti, Sc and REE recovery LR for Sc and REE recovery

13 Flowsheet (II) + Enriched and conditioned slag assisting downstream
Carbothermic Reductive Smelting Flux C Fe Recovery BR Conditioned Slag + Enriched and conditioned slag assisting downstream recovery + Mild fluxing conditions optimising Fe removal and preparing for Al and Na recovery - Na losses in BR smelting - Excess CaO detrimental to downstream processing - High energy consumption due to two-step pyrometallurgical process Metallic Fe Caustic Leaching Na2CO3 Al, Na Recovery LR for Ti, Sc and REE recovery CaCO3 C Cl Soda Sintering Al, Ti Recovery For electrolysis LR for Sc and REE recovery NaAlSiO4, C2AS etc C Soda Sintering Na2CO3 NaAlO2 Mild Alkaline Leaching LR for Ti, Sc and REE recovery Al, Na Recovery

14 Flowsheet (II) + Single-step heat recovery process targeting Fe, Al
Carbothermic Reductive Smelting Flux C BR Conditioned Slag + Single-step heat recovery process targeting Fe, Al and Na through conditioning of slag + Downstream residue can be used for building materials - Proper conditioning of leachable calcium aluminates necessary - CaCO3 and CaTiO3 inhibit downstream recoveries LR for Ti, Sc and REE recovery Mild Alkaline Leaching C Na2CO3 Soda Sintering Al, Na Recovery LR for Ti, Sc and REE recovery Caustic Leaching Na2CO3 Al, Na Recovery CaCO3 C Cl Soda Sintering Al, Ti Recovery For electrolysis LR for Sc and REE recovery CA,C3A,C12A7,C2AS NaAlO2

15 Flowsheet (II) + Enriched slag targeting Al and Ti chlorides
Conditioned Slag Carbothermic Reductive Smelting Flux C Fe Recovery BR + Enriched slag targeting Al and Ti chlorides + AlCl3 easier to introduce into electrolysis, avoiding calcination step - Possible operational challenges in carbo- chlorination step - AlCl3 less favoured in electrolysis; corrosion problems and high maintenance costs - TiCl4 recovery only beneficial enriched LR for Ti, Sc and REE recovery Mild Alkaline Leaching C Na2CO3 Soda Sintering Caustic Leaching Al, Na Recovery CaCO3 C Cl Carbo-chlorination Al, Ti Recovery For electrolysis LR for Sc and REE recovery AlCl3, TiCl3

16 Flowsheet (III) + Microwave heating selectively focuses on
Microwave Reduction Water/Mild alkaline Leach Physical Treatment and Magnetic Separation C Na2CO3 BR(degassed) Al, Na Recovery Slag for Sc and REE recovery + Microwave heating selectively focuses on moderately absorptive (dielectrics) materials + Highly reduced time of reduction via microwave - Cost and size of microwave equipment, limited by maximum kWh - Magnetic separation of Fe fractions need several step processing - Degassing needed to avoid plasma NaAlO2 Magnetic phase Fe, Ti Recovery

17 Flowsheet (IV) + Stoichiometric C assist Al and Na recovery
Carbothermic Reductive Roasting Water/Mild alkaline Leach Magnetic Separation C Na2CO3 BR Al, Na Recovery Slag for Sc and REE recovery Fe, Ti Recovery + Stoichiometric C assist Al and Na recovery + Upscaling easier in industrial equipment + Minimal fluxing with lime aids downstream processing - Fe recovery from magnetic phase is lesser compared to metallic Fe recovery via smelting - Longer time needed compared to microwave process NaAlO2 Magnetic phase

18 Flowsheet (V) + Previous removal of Al and Na assists the Fe
BR + Previous removal of Al and Na assists the Fe metallisation + Short duration of microwave Fe recovery assists processing - Sintering and leaching step before microwave reduction costs energy and water. Soda Sintering Na2CO3 NaAlO2 Mild Alkaline Leaching Al, Na Recovery Microwave Reduction C Magnetic phase Physical Treatment and Magnetic Separation Fe, Ti Recovery Slag for Sc and REE recovery

19 Potential Valorisation of BR
Flexible pathways in the recovery of Fe and Al Dependent on input BR Composition and Mineralogy Important factors of consideration Energy Reagent/Flux(Downstream conditioning) Single step vs two-step conversion method Efficiency

20 Visit us at http://etn.redmud.org
Thank you! Visit us at

21 Additional References
Kaußen, F.M.; Friedrich, B. Reductive smelting of red mud for iron recovery. Chemie Ingenieur Technik 2015, 87, Kaußen, F.M.; Friedrich, B. In Soda sintering process for the mobilisation of aluminium and gallium in red mud Bauxite Residue Valorisation and Best Practices Conference (BR 2015) Leuven, Belgium 2015a; Pontikes, Y., Ed. ACCO: Leuven, Belgium pp Kaußen, F.M.; Sofras, I.; Friedrich, B. In Carbothermic reduction of red mud in an eaf and subsequent recovery of aluminum from the slag by pressure leaching in caustic solution, Bauxite Residue Valorisation and Best Practices (BR 2015), Leuven, Belgium 5-7 October 2015, 2015b; Pontikes, Y., Ed. ACCO: Leuven, Belgium pp Erçağ, E.; R. Apak, R. Furnace smelting and extractive metallurgy of red mud: Recovery of tio2, al2o3 and pig iron. J. Chem. Technol. Biotechnol. 1997, 70, Borra, C.R.; Blanpain, B.; Pontikes, Y.; Binnemans, K.; Van Gerven, T. Comparative analysis of processes for recovery of rare earths from bauxite residue. JOM 2016, 68, Borra, C.R.; Mermans, J.; Blanpain, B.; Pontikes, Y.; Binnemans, K.; Van Gerven, T. Selective recovery of rare earths from bauxite residue by combination of sulfation, roasting and leaching. Miner. Eng. 2016, 92, Mishra, B.; Gostu, S. Materials sustainability for environment: Red-mud treatment. Frontiers of Chemical Science and Engineering 2017, 11, Bruckard, W.J.; Calle, C.M.; R.H. Davidson, R.H.; Glenn, A.M.; Jahanshahi, S.; Somerville, M.A.; Sparrow, G.J.; Zhang, L. Smelting of bauxite residue to form a soluble sodium aluminium silicate phase to recover alumina and soda. Trans. Inst. Min. Metall., Sect. C 2010, 119,


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