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Advances in life cycle costs of Flotation machines
Kari Föhr
Symphos 11 Conference
Marrakech, May 11th, 2011
Starting point
Flotation machine life-cycle energy cost is
significant compared to initial investment
There are both economical and environmental
reasons to concentrate on energy efficiency
Factors Affecting Energy Usage
Choice of Technology
• Size matters!
• Mechanism rpm
Electric system
Power transmission
Factors Affecting Energy Usage
Choice of Technology
• Forced Air Outotec TankCell® 300
including Mixer AND Blower
• 0.49 kW/m3 - water only,
• 0.67 kW/m3 - operating at pulp density of 1,35 kg/dm3
• Source: Press release published by Outotec and Codelco
• Self Aspirating 257 m3:
• 0.88 kW/m3 - water only,
• 1.09 kW/m3 – estimated with pulp of 1,35 kg/dm3.
• Source: A Weber, L MacNamara, H Scheiber, 2008
In a Real Case
Outotec "Self Aspirated" Outotec "Self Aspirated"
Cell Volume, m3 300 257 300 257
Energy consumption in Mechanism, kW 160 280 160 280
Energy consumption in Blower, kW 40 0 40 0
Energy consumption in Total, kW 200 280 200 280
Specific energy, kW/m3 0,67 1,09 0,67 1,09
Hours / year 8 300 8 300 8 300 8 300
Total energy consumption / cell / year, kW 1 328 000 2 324 000 1 328 000 2 324 000
Energy cost, US$/kWh $0,05 $0,05 $0,10 $0,10
Energy cost US$/year x cell $66 400 $116 200 $132 800 $232 400
Number of Cells 12 14 12 14
Total Volume 3600 3598 3600 3598
Cost of Total Energy , US$/year $796 800 $1 626 800 $1 593 600 $3 253 600
Comparison per Year $830 000 $1 660 000
a) Energy cost $0,05 / kWh b) Energy cost $0,10 / kWh
6
Size matters!
1800 m3 flotation volume – the options
Consider a plant requiring 1800 m3 of
rougher/scavenger volume.
Three possible scenarios for this volume
can be:
a) 18 x 100 m3 cells in 2 rows of 9.
b) 12 x 150 m3 cells in 2 rows of 6.
c) 9 x 200 m3 cells in 1 row of 9.
d) 6 x 300 m3 cells in 1 row of 6
7
Size matters 1800 m3 flotation volume
From the table we can see that the use of 300 m3 cells leads to a
1. Reduction in capital equipment cost of 50 %
when compared to using 100 m3.
2. A decrease in plant footprint area of 54 %
3. Savings of 28% and 50 % for power and air requirements
4. Savings in maintenance: 6 shafts instead of 18 – equal time per shaft
means 67% reduction in maintenance time!!
Factors Affecting Energy Usage
P = drawn Power
rho = density
k = power factor (efficiency of the mechanism)
n = shaft / rotor speed
D = rotor diameter
53 *** DnkP
Factors Affecting Energy Usage
10% reduction in the Speed equals
30 % reduction in Energy
~ 20% reduction in Wear Rate
53 *** DnkP
Can you reduce the speed?
YES, if
• There is enough mixing to avoid sanding
• The air dispersion is good enough
• There is enough torque to start after
blackout
• The drive type allows adjustment
• V-belts
• If the transmission ratio allows. Practical limit is 1:8
• Variable Frequency Drive (Converter)
• Only if you have low voltage motors (max 690 V)
In a Real Case
Outotec Outotec Outotec Outotec
Cell Volume, m3 300 300 300 300
Speed Nominal -5 % -10 % -15 %
Energy consumption in Mechanism, kW 160 137 117 98
Energy consumption in Blower, kW 40 40 40 40
Energy consumption in Total, kW 200 177 157 138
Specific energy, kW/m3 0,67 0,59 0,52 0,46
Hours / year 8 300 8 300 8 300 8 300
1 328 000 1 138 594 968 112 815 558
Energy cost, US$/kWh $0,10 $0,10 $0,10 $0,10
Energy cost US$/year x cell $132 800 $113 859 $96 811 $81 556
Number of Cells 12 12 12 12
Cost of Total Energy , US$/year $1 593 600 $1 366 313 $1 161 734 $978 670
Comparison per Year -$227 287 -$431 866 -$614 930
Case 2 - TankCell 300 with Optimized Speed
• Note:
– TankCell® 300 at Chuquicamata at specific power of
0,49 kW/m3 produced over 5% better recovery than
TankCell® 160 at higher sp. Power.
Metallurgy?
Can rotor speed be reduced without sacrificing the metallurgy?
-> plant tests with Outotec FloatForce® Flotation mechanism
Site test results – case Harjavalta
TankCell® 50, slag copper, heavy material, slurry SG 1,8
• Two day test campaign, samples from 3-5 composites
Copper Recovery and Grade vs. Power Draw
0
10
20
30
40
50
60
70
80
90
0,60 0,75 0,85 1,00 1,10
Power Draw [kW/m3]
Reco
very
/Gra
de
[%]
.
Cu Recovery [%] Cu Grade [%]
Site test results – case Pyhäsalmi
TankCell® 60
• Left over zinc flotation from pyrite concentrate
• P80 80-90 μm, average slurry SG 1,7
• Several month test campaign
• Initial tests with several mechanism set-ups
• FloatForce-1050 with Jg 1,0 cm/s was selected to
further tests
• Several thousand samples taken to increase
statistical reliability
Site test results – case Pyhäsalmi
Zinc recoveries and grades of TankCell® 60
Zinc Recovery and Grade vs. Power Draw
0,0
10,0
20,0
30,0
40,0
50,0
60,0
70,0
0,6 1,1 1,6
Power Draw [kW/m3]
Re
co
ve
ry/G
rad
e [
%]
.
Zn Recovery [%] Zn Grade [%]
On Electric Systems
Frequency Converters have becomesignificantly cheaper
HOWEVER, they are only cheap for LOW VOLTAGE systems, < 690 V.
In a Real Case
Outotec Outotec Outotec Outotec
Cell Volume, m3 300 300 300 300
Speed Nominal -5 % -10 % -15 %
Energy consumption in Mechanism, kW 160 137 117 98
Energy consumption in Blower, kW 40 40 40 40
Energy consumption in Total, kW 200 177 157 138
Specific energy, kW/m3 0,67 0,59 0,52 0,46
Hours / year 8 300 8 300 8 300 8 300
1 328 000 1 138 594 968 112 815 558
Energy cost, US$/kWh $0,10 $0,10 $0,10 $0,10
Energy cost US$/year x cell $132 800 $113 859 $96 811 $81 556
Number of Cells 12 12 12 12
Cost of Total Energy , US$/year $1 593 600 $1 366 313 $1 161 734 $978 670
Comparison per Year -$227 287 -$431 866 -$614 930
Case 2 - TankCell 300 with Optimized Speed
• NOTE:– If VSD costs ~ USD 18 000 / unit
– With –5% speed decrease
– Pay-off in ONE YEAR!!
Power Transmission
Drive mechanism efficiency
Every drive component has its own efficiency
• Typical electric motors 95% (when selected correctly)
• Bearing unit 99%
• V-belts 90-98% (when aligned and tightened correctly)
• Two-stage gearbox 98% (when size is correct)
• Frequency converter 96-98%
Everything has to be installed properly
• E.g. incorrect belt alignment can cause significant losses
Case example!
Drive mechanism selection – case example
Energy cost comparison of different drive arrangements
• Cost of energy is considered to be 0,1 $/kWh
• Cost of capital is 6%
0
20 000
40 000
60 000
80 000
100 000
120 000
1 3 5 7 9 11 13 15 17 19
Ene
rgy
cost
[U
SD]
Years [a]
Energy cost comparison of industrial size flotation machine, agitator power consumption 100 kW
vDrive
vDrive (0,54 deg angle fault)
vDrive (1,08 deg angle fault)
eDrive
Gearbox+v-belt drive
V-belt drives
Feasible for the small cell sizes <70m3
Expensive Motors
• Low speed
• High bearing load
Low start-up torque
Tightening of belts
Changing of belts
Poor efficiency when (usually) misaligned
Noisy
The new TankCell® eDrive
Motor
• Standard Four Pole
(1500/1800 rpm)
• Flange mounted
No V-belts
Custom made Gearbox
Air feed through
Gearbox
The new TankCell® eDrive
High Efficiency
• No belts
Low Maintenance
• Standard mineral oil
One oil change /
year
• Synthetic oils
One oil change / 3
years
The new TankCell® eDrive
Compact
• Clean platforms
• Easy access
Conclusions
Flotation life cycle energy cost is significant
compared to initial investment
Energy consumption can be significantly
reduced via:
• Correct choice of technology enabling slower rotor
speed
• Using as big Flotation Cells as possible
• Correct selection of the Electric system
• Correct selection and maintenance of Power
transmission
Acknowledgements
Mr Antti Rinne, Mr Aleksi Peltola and Mr
Sami Grönstrand, Outotec
People at Boliden Harjavalta
People at Inmet Pyhäsalmi