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ProMine 23.-25. April 2013, Levi 1
ProMine - Nano-particle products from new mineral resources in Europe
Products from schwertmannite
G.E.O.S. Ingenieurgesellschaft mbH
WOLA Chemisch-technische Erzeugnisse GmbH Bangor University
Vattenfall Europe Mining AG
UBIG GmbH
ProMine 23.-25. April 2013, Levi 2
Pigments from schwertmannite
G.E.O.S. Ingenieurgesellschaft mbH
WOLA Chemisch-technische Erzeugnisse GmbH
Vattenfall Europe Mining AG
Iron in mine water - a resource?
River „Kleine Spree „, (29.09.2008)
Iron in mine water – a resource?
4
Nochten – modelsite for schwertmannite products
• Open cast mine Nochten: 18 Mio t/year lignite • Waterlift: ~ 120 Mio. m³/year
Watertreatment plant Tzschelln: 20 Mio. m³/a mine water
5
Flowsheet - pilot scale schwertmannite production
Schwertmannite
Microbial iron oxidation
25-35 g/m3*h
Mine water
Air
Fe2+ + MO + O2 + CO2 → Fe 3+ + biomass
16Fe3+ + 3,5 SO42- + 25 H2O → Fe16O16(OH)9(SO4)3,5 + 41 H+
Fe3+ + 3 H2O → Fe(OH)3 + 3 H+
Max. throughput
Amount of recovered Schwertmannite
Reactor volume
5 m³/h 5 t/year 10.5 m³
Schwertmannite from Lignite mine water
Parameter Unit Mean
Analysis-water (106°C) % by wt 9.8
Fe % by wt 48.8
SO42- (acid-soluble) % by wt 16.6
Aluminium % by wt 0.1
Silicium % by wt 0.5
NH4+ (CaCI2-extract) mg/kg 6.6
Potassium mg/kg 118
Sodium mg/kg 46
Calcium mg/kg 506
Magnesium mg/kg 180
Arsenic mg/kg 106
Nickel mg/kg <2
Zinc mg/kg 11
Manganese mg/kg 10
Phosphorous mg/kg 228
7
Pigment production from schwertmannite
Laboratory scale optimization of pigment production: - optimization of drying, calcination and sieving conditions - testing of various mechanical and chemical pelletizing processes
Mechanical drainage of schwertmannite
Pre-shredding of the dried sludge
Thermal drying
Grinding Screen and stream grading
high temperature
roasting
Solid separation Washing water, H2SO4
Filter
water water
Red Pigment
gas treatment
8
Pigment specification…
Parameter Requirements with regard to group and category
Red pigment Yellow pigment
A B C D A B C D
Total content of Fe2O3 determined after drying at 105°C [min. % by wt] 95 70 50 10 83 70 50 10
Volatile matter at 105°C [max % by wt] 1 1.5 2.5 2.5 1 2.5 2.5 2.5
Water soluble fraction [% by wt] (hot extraction)
Type I ≤ 0.3 -
Type II ≥ 0.3 and ≤ 1 ≤ 1
Type III > 1 and ≤ 5
Water soluble chloride and sulfate as Cl- and SO42-
[% by wt] Type 1 ≤ 0.1 -
Sieve residue (45 µm) [% by wt] Grade 1 ≤0.01
Grade 2 >0.01 and ≤0.1
Grade 3 >0.1 and ≤1
Acidity or Alcalinity of the aqueous extract [max. ml 0.1 mol/l solution] 20
Presence of lead chromate unverifiable
Total content of CaO, after drying at 105°C [max. % by wt] class a 0.3
class b, c 5
class d as agreed between contracting parties
Presence of organic colourants unverifiable
Technical scale production tests
9
Calcination Grinding
Result: • 300 kg iron
oxide after calcination
• 120 kg pigment
Technical quality of developed iron oxide pigments
10
Iron oxide pigment (IOP) DIN-Norm Nochten Ochre Nochten Red (33) Bayferrox Rot Bayferrox Rot Rudner IOP Yellow pigment Red pigment type 130 type 222
Application in concrete stones coatins, stains,
ceramics, engobes concrete stones stains, engobes, glazes ferrite
Colour ochre brick-red brick-red brick-red brick-red
Volatile matter, 105°C % EN ISO 787-2 <1 <0.5 <0.5 <0.5 <0.5
Fe2O3 % EN ISO 1248 75-80 99 95-97 90...96 > 99
SiO2+Al2O3 % 55913 0.1 0.1 3 max. 4.0 <0.20 Water-soluble percentage, hot extraction % EN ISO 787-3 ~10 <0.1 0.3 0.5 <0.15 pH EN ISO 787-9 2…3 3...5 6.0 4...8
Tapped density g/cm³ EN ISO 787-
11 0.9-1.1 0.6 0.9 1.4...1.8
Theoretical density g/cm³ EN ISO 787-
10 ~5 5.22 5.0 5
oil adsorption g/100
g EN ISO 787-5 50-55 24-33 26 15 Sieve residue <45 µm % EN ISO 787-7 <0.1 <0.1 0.05 max. 0.1 Specific surface m²/g 12…15 12...15 3.8-4.8
ProMine 23.-25. April 2013, Levi
Application of pigments in coatings
Investigation Description Scale Result Partner
Specific pigment tests
Analysis of pigments for application in coatings
L Pigments are suitable for application in colour and coatings
WOLA
Production of base coatings
Primer coats with different organic binding agents
L & T Coats applied on metallic test panels
WOLA
Test of the coatings Salt spray test, weather resistence
T Nochten pigments can be used in anticorrosive primer coats
WOLA
ProMine 23.-25. April 2013, Levi 12
Corrosion resistant coatings
ProMine 23.-25. April 2013, Levi 13
Large scale application test
ProMine 23.-25. April 2013, Levi 14
Adsorbents from schwertmannite
G.E.O.S. Ingenieurgesellschaft mbH
and UBIG mbH
Adsorbent production from schwertmannite
• produced from the mineral schwertmannite
• adsorption of oxo anions (e. g. Arsenate) in industrial effluents, mine water
• very high sorption capacity for Arsenic and good sorption kinetics (similar or better than commercial products)
• maximum sorption capacity in unbuffered surroundings
• filterstable agglomerates for application in passive water treatment systems
• very low elution of As from the loaded material (Requirements for landfilling)
• cheaper than commercial products
• Patent was submitted in May 2012 (EP12167884.1)
15 15
Based on the results of the national project:
Technical quality of SHM agglomerates
16
adsorbent/ binder
test series
SHM-sorpX SHM-49 SHM-sorpP SHM-57
Organic
binder Organic binder Compaction
Organic binder and compaction
As(III) mg/g
buffered (pH qmax)
29.8 (pH 7.5)
35.7 (pH 7.5)
27.5 (pH 7.5)
36.8 (pH 7.5)
unbuffered (pH qmax)
64.8 (pH 6.6)
56.8 (pH 6.6)
42.0 (pH 6.7)
16.5 (pH 4.8)
As(V) mg/g
buffered (pH qmax)
50.7 (pH 7.5)
37.5 (pH 7.5)
25.6 (pH 7.5)
16.7 (pH 7.5)
unbuffered (pH qmax)
60.3 (pH 6.8)
55.8 (pH 6.7)
37.6 (pH 6.8)
21.4 (pH 5.9)
adsorbent
test series
Fe(OH)3 sludge
FerroSorp® Plus GEH® 104 Bayoxide®
E33 HCF
As(III) mg/g buffered to pH 7.5
22.6 28.9 18.6 18.3
As(V) mg/g − 40.1 33.2 21.1
Adsorption capacity for SHM granules
Comparison with commercial products 1 mm
Granula produced with organic binder
Adsorption kinetics: - better adsorption kinetics for
As(V) compared to commercial products:
Sorption
product SHM-Sorp
FerroSorp Plus GEH® 104 Bayoxide®
E33 HCF
Elimination of As(V) in days
5-8 17 6 9
Pilot plant for adsorbent production
chamber filter press
screw conveyor
ploughshare mixer
roll crusher
sieving plant
chamber dryer 1
chamber dryer 2
dissolver
conveyor belt
weighing /packaging
weighing machine
conveyor belt
stirrer tank
piston diaphragm pump
water water, binder
water, binder
air
M
M
Flow sheet: pilot plant for adsorbent production from schwertmannite
18
Individual processing steps
Mixing with binding agent Drying of the material Crushing and sieving
Products: filterstable schwertmannite pellets
1 cm
Testing the technically produced products
19
0
2
4
6
8
10
12
14
16
18
20
0 0.5 1 1.5 2 2.5 3 3.5 4 4.5
As-
sorp
tion
cap
acit
y [m
g/g]
equilibrium As-concenration in the liquid phase [mg/l]
experimental data
Langmuir
0
5
10
15
20
25
30
0 0.5 1 1.5 2 2.5 3A
s-so
rpti
on c
apac
ity
[mg/
g]
equilibrium As-concentration in the liquid phase [mg/l]
experimental data
Langmuir
Filterstable adsorbents with a maximum equilibrium sorption capacity of 35 mg/g As were produced
After ProMine: Pilot scale application tests in passive water treatment plants supported by various industrial partners and laboratory scale tests concerning further oxo anions and different water qualities
Estimation of the profitability of an industrial scale production
20
Production amount: 10,000 t SHM/a
Cost category Biosynthesis of SHM from mine watermine water
Capital costs 3,672,540 €Depreciation (10 years) 367,254 €/aOperating costs(energy, maintanace) 155,000 €/aTotal annual cost 522,254 €/a
Pigment production Adsorbent productionCapital costs 6,443,250 € 3,993,250 €Depreciation (10 years) 644,325 €/a 399,325 €/aOperating costs
Man power 108,000 €/a 108,000 €/aEnergy 900,000 €/a 300,000 €/aChemicals 500,000 €/aMaintenance 644,000 €/a 399,000 €/a
Total annual cost 2,818,579 €/a 2,228,579 €/a
Revenues from sales 3,410,000 €/a 5,600,000 €/a
Profit / loss 591,421 €/a 3,371,421 €/a
ProMine 23.-25. April 2013, Levi 21
Thank you! WOLA Chemisch-technische Erzeugnisse GmbH Bangor University
Vattenfall Europe Mining AG
UBIG GmbH