A proposal for a 100% use of bauxite residue: The process, results - - PowerPoint PPT Presentation
A proposal for a 100% use of bauxite residue: The process, results - - PowerPoint PPT Presentation
A proposal for a 100% use of bauxite residue: The process, results on the novel Fe-rich binder and how this can take place within the alumina refinery T. Hertel, L. Arnout, A. Peys, L. Pandelaers, B. Blanpain, Y. Pontikes 06/10/2015 The dirty
A proposal for a 100% use
- f bauxite residue:
The process, results on the novel Fe-rich binder and how this can take place within the alumina refinery
- T. Hertel, L. Arnout, A. Peys, L. Pandelaers, B. Blanpain, Y. Pontikes
06/10/2015
The dirty by-product of the Bayer process…
Stade, Germany1
1https://en.wikipedia.org/
- production: > 140 Mt of BR/yr
- landfilled: > 2.7 Bt
Kolontar, Hungary2
2http://i.dailymail.co.uk/
Imagine…
Stade, Germany1
2adapted from http://blogs.uni-siegen.de/ 1https://en.wikipedia.org/
2
Imagine…
100 % use of BR
Stade, Germany1
1adapted from ttps://en.wikipedia.org/ 2adapted from http://blogs.uni-siegen.de/
2
- Al- and Si-rich cementitious amorphous binder
- polymerisation of an alkali activated precursor
- alternative to OPC
Inorganic polymers (IP)
http://www.geopolymer.org/
- Al- and Si-rich cementitious amorphous binder
- polymerisation of an alkali activated precursor
- alternative to OPC
Inorganic polymers (IP)
http://www.geopolymer.org/
- Al- and Si-rich cementitious amorphous binder
- polymerisation of an alkali activated precursor
- alternative to OPC
Inorganic polymers (IP)
http://www.geopolymer.org/
- Al- and Si-rich cementitious amorphous binder
- polymerisation of an alkali activated precursor
- alternative to OPC
Inorganic polymers (IP)
The market is already there …
- Fe-rich precursors such as copper, lead, ferro-nickel slags
- Partially vitrified
- Iron in oxidation state +II
Inorganic polymers (IP)
Cu slag1
1http://www.istgrup.com/
Goal
Phase diagrams BR insoluble in alkaline media
Modification into Fe-rich precursor
Reduction of iron: Fe+III Fe+II Support formation of liquid phase
Inspiration by Fe-rich precursors
- Partially vitrified
- Iron in oxidation state +II
Thermal treatment
Goal
FeO SiO2 Al2O3 SiO2 CaO FeO
1083 °C 1093 °C
How to increase liquid phase formation?
Goal
FeO SiO2 Al2O3 SiO2 CaO FeO
1083 °C 1093 °C
How to increase liquid phase formation?
Aim of present work
IP BR
Development of near zero-waste process for the synthesis of IP
partially vitrified Fe-rich precursor Synthesis High temperature processing
Synthesis of inorganic polymers High temperature processing Characterisation of Bauxite Residue
thermodynamic calculations XRD
Overview of work
I II III
XRF XRD SEM strength
XRF
Characterisation of BR
Oxides wt.% Fe2O3 47.9 Al2O3 18.9 CaO 11.0 SiO2 9.6 TiO2 6.5 Na2O 4.0
20 30 40 50 60 G Goethite I Ca-Al-Fe-Si-Hydroxide P Perovskite R Rutile Q Quartz Z Zincite H G I Cc D I D I Cc Q G H P G I I G A Q R C P C Cc H H H H Z
Intensity [a.u.] °2ϑ CuKα
H Z Z Z Z A Gibbsite C Cancrinite Cc Calcite D Diaspore H Hematite
XRD
(Internal standard)
High temperature processing
0,4 0,8 1,2 1,6 2,0 2,4 10 20 30 40 50 60 70 80 90 100
wt.% wt.% C
FactSage calculation 1100 °C – Carbon addition
Ti-Spinel Ca(Al,Fe)6O10 Ca2(Al,Fe)8SiO16 Corundum Fe FeO Mellilite NaAlO2 Nepheline Perovskite Liquid phase Spinel Gas
High temperature processing
0,4 0,8 1,2 1,6 2,0 2,4 10 20 30 40 50 60 70 80 90 100
wt.% wt.% C
FactSage calculation 1100 °C – Carbon addition
Ti-Spinel Ca(Al,Fe)6O10 Ca2(Al,Fe)8SiO16 Corundum Fe FeO Mellilite NaAlO2 Nepheline Perovskite Liquid phase Spinel Gas
High temperature processing
FactSage calculation 1100 °C – Carbon + silica addition
High temperature processing
19 FactSage calculation 1100 °C – Carbon + silica
High temperature processing
20 FactSage calculation 1100 °C – Carbon + silica
100BR 98.4BR_1.6C 88.6BR_1.4C_10S
High temperature processing
Transformation of BR
- Induction furnace: 1100 ± 10 °C – 1 hour
- closed iron crucible, gas inlet/outlet
- inert atmosphere – Argon 99.995 %
Aim:
semi-vitrified material precursor for IP
20 30 40 50 60
M
a) b) c)
M N G f N H MS H S S H G c G H H,G G,S Zc c f m M G,c Q P N,f Z N Z,P Z Z Z S f P P W S G c,N H,G S P S S M Z Z,P Z Z Z Z G,S S G G Z,P Z Q G H,P PG N,f I S W Z S S Z G
Intensity (a.u.)
G M G S G N,G G N P G G,M G S S M W M G M S S N NG QN N G M I
°2ϑ CuKα
XRD of precursor
c Calcium Iron Oxide, f Iron Calcium Silicate, G Gehlenite, H Hematite, I Iron, M Magnetite, m Maghemite, N Nepheline, P Perovskite, Q Quartz, S Spinel, W Wüstite, Z Zincite (internal standard)
100BR 98.4BR_1.6C 88.6BR_1.4C_10S
20 30 40 50 60
M
a) b) c)
M N G f N H MS H S S H G c G H H,G G,S Zc c f m M G,c Q P N,f Z N Z,P Z Z Z S f P P W S G c,N H,G S P S S M Z Z,P Z Z Z Z G,S S G G Z,P Z Q G H,P PG N,f I S W Z S S Z G
Intensity (a.u.)
G M G S G N,G G N P G G,M G S S M W M G M S S N NG QN N G M I
°2ϑ CuKα
XRD of precursor
100BR 98.4BR_1.6C 88.6BR_1.4C_10S
c Calcium Iron Oxide, f Iron Calcium Silicate, G Gehlenite, H Hematite, I Iron, M Magnetite, m Maghemite, N Nepheline, P Perovskite, Q Quartz, S Spinel, W Wüstite, Z Zincite (internal standard)
20 30 40 50 60
M
a) b) c)
M N G f N H MS H S S H G c G H H,G G,S Zc c f m M G,c Q P N,f Z N Z,P Z Z Z S f P P W S G c,N H,G S P S S M Z Z,P Z Z Z Z G,S S G G Z,P Z Q G H,P PG N,f I S W Z S S Z G
Intensity (a.u.)
G M G S G N,G G N P G G,M G S S M W M G M S S N NG QN N G M I
°2ϑ CuKα
XRD of precursor
100BR 98.4BR_1.6C 88.6BR_1.4C_10S
c Calcium Iron Oxide, f Iron Calcium Silicate, G Gehlenite, H Hematite, I Iron, M Magnetite, m Maghemite, N Nepheline, P Perovskite, Q Quartz, S Spinel, W Wüstite, Z Zincite (internal standard)
Synthesis of IP’s
- K-silicate activation solution, SiO2/K2O= 1.6, H2O/K2O = 16
- activation solution/solid ratio = 0.25
- Curing: 60 °C, 72 h
100BR 98.4BR_1.6C 88.6BR_1.4C_10S Steoroscope images
Microstructure – SEM (SE)
100BR 98.4BR_1.6C 88.6BR_1.4C_10S
denser microstructure less pores, cracks
SEM & strength (3d) of IPs
100BR 98.4BR_1.6C 88.6BR_1.4C_10S Compressive strength 13.4 ± 0.4 MPa 19.7 ± 1.1 MPa 43.5 ± 0.5 Mpa Flexural strength 4.2 MPa 5.5 MPa 9.8 MPa
Process within alumina refinery
Bayer process BR slurry C mixing filter press BR cake alkaline liquor
alkalis waterglass
firing precursor
Fe, Fe3O4
IP
SiO2
H2O
1http://img.tradeindia.com/ 2https://encrypted-tbn1.gstatic.com
1 2
Conclusion
- BR was transformed into suitable Fe-rich precursor
material for IP
- addition of C, SiO2
- heat treatment - 1100 °C
- Insoluble, dense IPs were sucessfully synthesised
- dense microstructure
- strength exceeding 40 MPa
Thank you for your kind attention!
To be continued …
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