Agricola Research Center –
Multicomponent Mineral Systems
(ARC-MMS, “ARC-2”):
Partikelteknologi inom gruvindustriella
processer – växelverkan i mineralsystem
med flera komponenter
Prof. Oleg N. Antzutkin (coordinator)
Division of Chemical Engineering, Luleå University of Technology, Luleå, SE-97187, Sweden
Historisk backgrund:
ARC-”1”
(finansierer: SSF, STINT och gruvföretag, 2002-2007
Koordinator:
Prof. Willis Forsling
)
Sustainability is the issue of survival!
- China commissions two new coal-fired power stations each week!
- China overtakes US as leading CO2(g) emitter: (In 2006 China emitted 6.2 billion tonnes of CO2(g) compared to 5.8 billion tonnes emitted by the US)
- Atmospheric CO2(g) increased from 284 ppm (in
1832) to 383 ppm (in 2007) => Climate change!
- Only the UK alone discards 27 million tonnes of waste a year => severe ecological issues!
OUR COMMON TASKS:
- ALTERNATIVE ENERGY SOURCES
- IMPROVING OF PROCESSES (to minimize CO2(g) emission)
- NEW TECHNOLOGIES (to minimize CO2(g) emission)
Agricola Research Center - Multicomponent Mineral Systems ARC-MMS (2008 - 2012)
Total: 14.6 Mkr
VINNOVA: 7.3 Mkr (50%)
New Boliden AB: 2.8 Mkr (19.2 %) LKAB: 2.5 Mkr (17.1 %)
Lundin Mining: 2.0 Mkr (13.7 %)
ARC-MMS program coordinator:
Prof. O.N. Antzutkin,
The Division of Chemiical Eng.
New Boliden and Lundin Mining LKAB
Project I
Recycling of process water and influence of its chemistry on sulphide flotation and flotation selectivity
Objectives: To provide remedies
to selectively regulate surface properties of sulfides, which are affected by recycled process water
Research coordinator:
Prof. H. Rao, The Division of Mineral Processing
Project II
Molecular scale approach towards dithiophosphate (DTP) behaviour on sulphide surfaces Objectives: To utilize understanding of adsorption mechanisms of collectors in improving selectivity and recovery of the valuable sulfide minerals
Research coordinator:
Dr A.-C. Larsson,
The Division of Chemical Eng.
Project III
3D data for iron ore pellets
Objectives: To supply a new type
of 3-D data for water, air bubbles, flotation reagents and particles in wet iron ore pellets. Remedies for air-bubble inclusion
Research coordinator:
Prof. J. Hedlund, The Division of Chemical Engineering
The central goal of the program: Understanding of mineral-aqueous interface chemistry and affinities within multi-component mineral systems for development of new surface related mineral processing technologies
ARC-MMS-1
Ions in
the process
water
ARC-MMS-3
3D-distrib.
in iron oxide
pellets
ARC-MMS-2
DTP,xan on
MeS
Johanne Mouzon Jonas Hedlund Anna-Carin Larsson Lars Gunneriusson Allan Holmgren Fatai IkumapayiIftekhar Uddin Bhuniyan
Hanumantha Rao Sven Öberg
New
Boliden
Björn JohanssonLunding Mining
Mikael SchaumanZinkgruvan AB
Bengt-Arne BergströmLKAB
Seija ForsmoNew Boliden
VINNOVA
Oleg Antzutkin Lena SvendsenHLRC
Iron oxides fluorapatite, waterglass, bentonite, dolomite, olivine, ssNMR/DNP on TiPSi adsorbents Nanoparticles with modified surfaces Collaboration:Yinan University, China IWRI, Australia
Aarhus University, Denmark The University of Warwick, UK Kola Science center, Russia
Blagoveszhensk University, Russia Budapest University, Hungary Kazan’ University, Russia Umeå University
At LTU:
Mathematics Dept. Dept. Mechanical Eng. Div. of Physics
Dept. Of Health Sc.
Payman Roonasi Anuttam Patra Faiz Ullah Shah
Mattias Gran Allan Holmgren
Oleg Antzutkin
Marina Maslova, Daniela RusanovaOleg Antzutkin, Allan Holmgren
As adsorption on FexOy Ivan Carabante
S
urface
Mats Lindberg Allan HolmgrenC
hemistry
G
roup
Oleg Antzutkin VR09 appl. VINNOVA 2008-2011 VR09 appl. Kempe 2009•
Project I
Recycling of process water and influence of its
chemistry on sulphide flotation and flotation
selectivity
Ikumapayi Fatai Kolawole (Ph.D student)
Prof. Kota Hanumantha Rao (coordinator)
Collector-mineral interaction in the presence of flotation effluent components: adsorption, zeta potential and spectroscopic studies.
Influence of Ca2+ and SO
42- species: Bench scale flotation tests of complex
sulphide ore.
Influence of RSC species: Hallimond flotation response of pure minerals and bench scale flotation tests of complex sulphide ore.
Collective influence of process water components: Hallimond flotation response of pure minerals and bench scale flotation tests of complex sulphide ore.
Influence of pulp redox potential (controlled chemically and potentiometrically) on surface speciation and flotation selectivity.
Influence of Ca
2+ions in solution
Effect of calcium ions on sulphide flotation
0 10 20 30 40 50 60 70 80 90 0 100 200 300 400 500 600 700
Concentration of calcium ions mg/l
R eco ver y % PbS ZnS FeS2 CuFeS2
Influence of SO
42-ions in solution
Effects of sulphate ions on sulfide mineral flotation
0 10 20 30 40 50 60 70 80 90 100 0 200 400 600 800 1000 1200 1400 1600 1800
Concentration of sulphate ions mg/l
R eco ver y % PbS ZnS FeS2 CuFeS2
Some Conclusions (Project I)
•
Activation of pyrite is obvious at high calcium ion and
low to high sulphate ions concentrations in solution.
•
Depression of galena and chalcopyrite at low to high
concentration of sulphate in solution
•
Depression of galena and chalcopyrite at averagely low
concentration of sulphate and calcium ions combined in
solution.
•
Depression of sphalerite at low to high concentration of
sulphate and calcium ions combined in solution.
Flotation reagents behavior on
sulphide surfaces
Molecular scale approach towards DTP
behaviour on sulphide surfaces
Sub project II ARC-MMS
Dr Anna-Carin Larsson (project coordinator)
Prof. Sven Öberg
A.-C. Larsson, Z. Sun, M. Lindberg (UNPUBLISHED RESULTS)
Adsorption of Na-Amyl-Xanthate on ZnS
228 ppm: Precipitate CuX or CuX2 166 ppm: ? 226 ppm: Precipitate PbX2 150 ppm: Artifact 185 ppm: Monothiocarbonate? X2ca 210 ppm?
13C
enriched xanthates
Some interesting results -
13
C solid state
NMR: A powerful tool to study surface
adsorbed species
ZnS activated by 3 mM Pb2+ ZnS activated by 3 mM Cu2+ ZnS activated by 0.3 mM Pb2+ or Cu2+ (same result in both cases) No activation
Quantum Mechanical Calculations
(DFT)
•
ZnS+Xan
•
•
Computer simulations show how Heptyl-Xanthate
•
binds to clean ZnS surfaces
•
Adsorption energies, tilt angles and IR-data were
calculated.
•
Simulation of Cu-activation shows a stronger bond.
•
KBuDTP
A more refined interpretation of experimental data could be made due to the combination of experiment and computer simulations
Hellström, Larsson, Fredriksson, Holmgren, Öberg, J Phys Chem, 2008
Prof. Jonas Hedlund
Dr Johanne Mouzon
Iftekhar Uddin Bhuiyan
3D Data for Iron Ore Pellets
ARC-MMS Project 3
LKAB’s green pellets are complex arrangements of: • iron ore particles with a broad size distribution • a binder (e.g. bentonite)
• additives (e.g. olivine) • water
• porosity
It is this complex arrangement that determines the wet and dry strengths of the pellets and subsequently the final porosity for oxidization and reaction in blast furnaces ⇒ 3D data are valuable!
Bentonite bridges between iron oxide (and olivine) particles in pellets
SEM
Dr Johanne Mouzon and
Iftekhar U. Bhuiyan
Image Processing
Image analysis
Spherical Porosity Distribution
HLRC
Iron oxides fluorapatite, waterglass, bentonite, dolomite, olivine, ssNMR/DNP on TiPSi adsorbents Nanoparticles with modified surfaces Collaboration:Yinan University, China IWRI, Australia
Aarhus University, Denmark The University of Warwick, UK Kola Science center, Russia
Blagoveszhensk University, Russia Budapest University, Hungary Kazan’ University, Russia Umeå University
At LTU:
Mathematics Dept. Dept. Mechanical Eng. Div. of Physics
Dept. Of Health Sc.
Payman Roonasi Anuttam Patra Faiz Ullah Shah
Mattias Gran Allan Holmgren
Oleg Antzutkin
Marina Maslova, Daniela RusanovaOleg Antzutkin, Allan Holmgren
As adsorption on FexOy Ivan Carabante
S
urface
Mats Lindberg Allan HolmgrenC
hemistry
G
roup
Oleg Antzutkin VR09 appl. VINNOVA 2008-2011 VR09 appl. Kempe 20091. RF patent 2235685. A method for sphene concentrate processing. Maslova M.V, Gerasimova L.G BI 25 2004.
2. RF patent 2207980 A method for titanium-containing concentrate processing. Maslova M.V, Gerasimova L.G BI 19, 2003.
Adsorption of Metal Ions on Titanium Phosphate
> 800 million tonnes of apatite tailings (Kola Region, Russia), ca 5 % of tailings is sphene, CaTiSiO5
- Titanium Phosphate adsorbents are produced from sphene by decomposition with H2SO4 and treatment with H3PO4
SEM
sphene
Ref. 2: Maslova et.al, J. S. S. Chem. 2008
sphene
Ti(HPO4)2.H2O Ti(HPO4)2.H2O
TiP + sphene
Ti(OH)1.36(HPO4)1.32.2.3H2O
ssNMR/DNP on TiPSi
adsorbents
Co-applicant:
Prof. Mark E. Smith (University of Warwick) Oleg Antzutkin (10%) Allan Holmgren (10%) (Marina Maslova 15%) a PhD student (80%) “Vetenskapsrådet” 2009 application Applicants:
“Development of novel solid-state NMR
methods for studies of surface and metal ion
adsorption on new types of sorbents”
Fig. left: 145.72 MHz 31P MAS NMR spectra of polycrystalline titanium phosphates (TiP) before
(bottom) and after (top) of adsorption of 50 mL 0.4 g/L Cu+2(aq) on 0.25 g of the sorbent. Assignment of P-resonances is suggested in the figure. right: inversion recovery profiles, which point at the differential T1 of different P-sites in the sorbent: Those with directly bound Cu(II) have T1 ca. 7 ms (fast recovery of the signals), while the free P-sites have T1 ca. 70 ms (slower recovery). UNPUBLISHED RESULTS.
ARC-MMS-1
Ions in
the process
water
ARC-MMS-3
3D-distrib.
in iron oxide
pellets
ARC-MMS-2
DTP,xan on
MeS
Johanne Mouzon Jonas Hedlund Anna-Carin Larsson Lars Gunneriusson Allan Holmgren Fatai IkumapayiIftekhar Uddin Bhuniyan
Hanumantha Rao Sven Öberg
New
Boliden
Björn Johansson(Lunding Mining)
Mikael Schauman(Zinkgruvan AB)
Bengt-Arne BergströmLKAB
Seija ForsmoNew Boliden
VINNOVA
Oleg Antzutkin Lena Svendsen Unfortunately, leaving ARC-MMS from Sep.09WELCOME to join ARC-MMS!