Synthesis of nano γ- AlOOH from aluminate solutions for catalytic applications
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Transcript of Synthesis of nano γ- AlOOH from aluminate solutions for catalytic applications
Prof. Panias DimitriosProf. Panias DimitriosKrestou Athina, MSc Krestou Athina, MSc
22/04/23SLM 2008, Belgrade National Technical University of
Athens
22/04/23 SLM 2008, Belgrade National Technical University
of Athens
BauxitBauxitee
AluminaAlumina
22/04/23 SLM 2008, Belgrade National Technical University
of Athens
BAYER PROCESSBAYER PROCESS to lower the SiOto lower the SiO22 concentration and concentration and control the level of control the level of phosphates phosphates
may contain may contain Al(OH)Al(OH)33 or or AlOOHAlOOH
for the extraction for the extraction of all of the Alof all of the Al22OO3 3 in bauxite in bauxite
Al(OH)3 Calcination above 1380KCalcination above 1380K
2Al(OH)2Al(OH)33 α-α-AlAl22OO33 +3H+3H22OO
22/04/23 SLM 2008, Belgrade National Technical University
of Athens
(energy saving,(energy saving, topotactictopotactic
transformation into transformation into γ-γ-AlAl22OO33))
22/04/23 SLM 2008, Belgrade National Technical University
of Athens
22/04/23 SLM 2008, Belgrade National Technical University
of Athens
22/04/23 SLM 2008, Belgrade National Technical University
of Athens
PropertiesProperties ApplicationsApplications
MicrostructureMicrostructure
22/04/23 SLM 2008, Belgrade National Technical University
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ApplicationsApplications
(catalysis, (catalysis, adsorption)adsorption)
MicrostructureMicrostructure (homogeneous, defect-free)(homogeneous, defect-free)
PropertiesProperties(high surface area, mesoporosity,(high surface area, mesoporosity,
proper crystallite size) proper crystallite size)
22/04/23 SLM 2008, Belgrade National Technical University
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Applications of Applications of γγ- Al- Al22OO33• catalyst or catalyst support in heterogeneous catalysiscatalyst or catalyst support in heterogeneous catalysis• adsorbent in purification and bleaching processesadsorbent in purification and bleaching processes• composite reinforcementcomposite reinforcement• membrane in separation processes of industrial waste streams membrane in separation processes of industrial waste streams and foodand food• in biomedical and chemical processes in biomedical and chemical processes
absence of defectsabsence of defectsEnhanced performance: homogeneous Enhanced performance: homogeneous microstructure microstructure uniform size uniform size distributiondistributionNANO-METER or SUB-MICROMETERNANO-METER or SUB-MICROMETER sized sized particlesparticles
Previous research in the Laboratory of Metallurgy (NTUA)Previous research in the Laboratory of Metallurgy (NTUA) Synthetic Bayer liquor (SSA)Synthetic Bayer liquor (SSA) Boehmite seedsBoehmite seeds T<100T<100ooCC precipitation of coarse precipitation of coarse γ-γ-AlOOH particles by decreasing the AlOOH particles by decreasing the free NaOHfree NaOH
More information:More information:D. Panias, A. Asimidis, I. Paspaliaris, Hydrometallurgy D. Panias, A. Asimidis, I. Paspaliaris, Hydrometallurgy 15-2915-29 (2001) 59. (2001) 59.C.Skoufadis, D.Panias, I Papsaliaris, Hydrometallurgy C.Skoufadis, D.Panias, I Papsaliaris, Hydrometallurgy 5757 (2003) 68. (2003) 68.D. Panias, Hydrometallurgy D. Panias, Hydrometallurgy 203203 (2004) 74. (2004) 74.D. Panias, A. Krestou, Powder Technology D. Panias, A. Krestou, Powder Technology 163-173163-173 (2007) 175. (2007) 175.
22/04/23 SLM 2008, Belgrade National Technical University
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This study: This study: Precipitation of pure nano-Precipitation of pure nano-boehmite by the destabilization of SSA boehmite by the destabilization of SSA through neutralization at atmospheric through neutralization at atmospheric conditions conditions
without without γ-γ-AlOOH seed additionAlOOH seed addition
22/04/23 SLM 2008, Belgrade National Technical University
of Athens
22/04/23 SLM 2008, Belgrade National Technical University
of Athens
SSA SSA (solution A)(solution A)
Acid Acid (solution B)(solution B)
ReagentReagentss
HNO3, HCl, H2SO4, HNO3, HCl, H2SO4, H3PO4, CH3COOHH3PO4, CH3COOH
BABA
ABAB
Mode Mode of of
mixingmixing 30<T<10030<T<100ooCC
5<pH<13,5<pH<13,66
ParameterParameters Studieds Studied
0<t0<tagag<2weeks<2weeks
addition rateaddition rate
calcination Tcalcination T
Characterization Characterization of precipitatesof precipitates
XRDXRD
TGTG
ssa, ps, pv, psdssa, ps, pv, psdby Nby N22 adsorption adsorption
/desorption/desorption
SEM, TEMSEM, TEM
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Precipitates: well crystallised gibbsite Precipitates: well crystallised gibbsite gibbsite/bayerite mixturesgibbsite/bayerite mixtures gibbsite/bayerite/boehmite gibbsite/bayerite/boehmite mixturesmixtures
NO PURE γ-AlOOH with the BA experiments
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PURE nano-crystallite PURE nano-crystallite γ-γ-AlOOH AlOOH
with the AB experimentswith the AB experiments
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Effect of Temperature and Effect of Temperature and pHpH
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Effect of ageing timeEffect of ageing timeT60-pH7
0
20
40
60
80
100
120
140
160
180
200
5 10 15 20 25 30 35 40 45 50 55 60
2θ
cps
020120
140
131
051200
220 151
t=0t=2
t=24
t=48
t=144t=168
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Effect of different acidsEffect of different acidsT60°C- pH7- t24h
050
100150200250300350400450500550600650
5 10 15 20 25 30 35 40 45 50 55 60
2θ
cps
HNO3
HCl
H2SO4
CH3COOH
020120
140 200
020 120 140,031 051,020HNO3 3,10 3,97 4,33 7,03HCl 3,00 4,39 3,50 5,84H2SO4 - 3,30 3,40 5,27CH3COOH - 2,89 2,68 3,52
crystallite size (nm)
22/04/23 SLM 2008, Belgrade National Technical University
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Effect of different acids (T90-Effect of different acids (T90-pH7-t24h)pH7-t24h)
Region Ι
Region ΙΙ Region ΙΙΙ
Crystallites<50nm
Transformation to γ-AlOOH of higher crystallinity
Transformation of γ-AlOOH to γ-Al2O3
Transformations
SLM 2008, Belgrade National Technical University of Athens
acids Calcination Temperature, (°C) 390 450 650 900 1100
HNO3 Precip. phase
γ-AlOOH
η-Al2O3
η-Al2O3
η-Al2O3
η/α/θ-Al2O3
ssa (m2/g) 98,44 220,59 186,78 102,78 38,08 pore size (Å) 56,26 54,07 71,92 116,66 216,5 ads. isotherm Type II Type II Type II Type II Type II
HCl Precip. phase
γ-AlOOH
η/ γ- Al2O3
η/ γ- Al2O3
η/ γ- Al2O3
α/δ-Al2O3
ssa (m2/g) 170,56 219,27 - - 60,18 pore size (Å) 53,80 59,26 - - 191,56 ads. isotherm Type II Type II - - Type II
H2SO4 Precip. phase
γ-AlOOH
η-Al2O3
η-Al2O3
Al4(OH)10SO4*5H2O
η-Al2O3
Al4(OH)10SO4*5H2O
α/η-Al2O3
Al4(OH)10SO4*5H2O ssa (m2/g) 74,14 59,11 - - 9,02
pore size (Å) 65,07 47,11 - - 105,32 ads. isotherm Type II Type II - - Type II CH3COOH
Precip. phase
γ-AlOOH
η-Al2O3
η-Al2O3
η-Al2O3
α/η-Al2O3 ssa (m2/g) 302,99 329,30 - - 68,93
pore size (Å) 25,20 43,92 - - 157,01 ads. isotherm Type I Type II - - Type III
Effect of different acids (T90-Effect of different acids (T90-pH7-t24h)pH7-t24h)
SLM 2008, Belgrade National Technical University of Athens
Effect of addition rate(T90-ph7-Effect of addition rate(T90-ph7-t0)t0)
390 400 650 900 11001ml/minphase precipitated γ-AlOOH - - - - -ssa (m2/g) 85,25 - - - - -pore size (Å) 50,68 - - - - -ads. Isotherm type Type II - - - - -
3ml/minphase precipitated γ-AlOOH η/γ-Al2O3 η/γ-Al2O3 γ-Al2O3 α/δ-Al2O3
ssa (m2/g) 148,10 241,20 191,39 125,92 47,14pore size (Å) 47,55 54,56 73,02 113,22 191,19ads. Isotherm Type II Type II Type II Type II Type II
5ml/minphase precipitated γ-AlOOH γ-Al2O3 γ-Al2O3 γ-Al2O3 α-Al2O3
ssa (m2/g) 170,87 284,35 173,62 114,13 5,84pore size (Å) 33,47 45,01 66,16 77,91 -ads. Isotherm Type II Type IV Type IV Type IV Type III
7ml/minphase precipitated γ-AlOOH η/γ-Al2O3 η/γ-Al2O3 γ/δ-Al2O3 α/δ-Al2O3
ssa (m2/g) 144,52 - - - -pore size (Å) 41,18 - - - -ads. Isotherm Type II - - - -
10ml/minphase precipitated γ-AlOOH η/γ-Al2O3 η/γ-Al2O3 γ/δ-Al2O3 α/δ-Al2O3
ssa (m2/g) 118,31 - - - -pore size (Å) 44,45 - - - -ads. Isotherm Type II - - - -
abruptphase precipitated γ-AlOOH η/γ-Al2O3 γ/δ-Al2O3 γ/δ-Al2O3 α/δ/θ-Al2O3
ssa (m2/g) 104,25 206,43 157,27 110,08 11,99pore size (Å) 33,33 42,18 58,9 84,75 -ads. Isotherm type Type II Type IV Type IV Type IV Type III
Calcination Temperature (oC)Addition rate 90oC, pH7
rate (ml/min) d (020) d(100) d(001)1ml/min 2,764 4,519 5,833ml/min 2,769 4,476 5,4175ml/min 3,029 4,579 7,0587ml/min 2,970 4,984 6,49010ml/min 2,750 4,284 6,004abrupt 4,3801 4,9615
Ab. add.Ab. add.
10ml/10ml/minmin7ml/min7ml/min5ml/min5ml/min3ml/min3ml/min1ml/mi1ml/minn
Only the AB experiments resulted in Only the AB experiments resulted in γ-γ-AlOOH AlOOH precipitation : effect of Al-species precipitation : effect of Al-species
22/04/23 SLM 2008, Belgrade National Technical University
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0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
0 2 4 6 8 10 12 14
pH
%A
l
Al +3
Al(OH) +2
Al(OH)2 +1
Al(OH)3
AL(OH)4 -1
AL2(OH)2 +4
AL3(0H)4 +5
Al3(OH)4 5+ Al3+
Al2(OH)2 4+
Al(OH)3
Al(OH)4-
Al(OH)2+
Al(OH)2+
HCl : higher specific surface HCl : higher specific surface areaarea addition rate 5ml/min: most promising for the addition rate 5ml/min: most promising for the precipitation of nanocrystallite precipitation of nanocrystallite γ-γ-AlOOH and calcined AlOOH and calcined products for catalytic applicationsproducts for catalytic applications
T & pH: better crystallinity in less tT & pH: better crystallinity in less tageing ageing
22/04/23 SLM 2008, Belgrade