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Fundamentals of mineral processing and recycling
Ted Nuorivaara Dept. of Chemical and Metallurgical Engineering Fall 2017
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Applying what we have learned on this course in real life examples
Week 5 Applying what we have learned on this course in real life examples
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Case: Experimental flotation studies
Common topics in this course and experimental flotation studies: Composition Mineral composition Chemical composition Particle properties Particle size distribution Density Properties of the separation process Slurry properties Mass pull Recovery Grade Separation efficiency Kinetics
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Case: Experimental flotation studies
Additional properties to be taken into account: Chemical system Includes the type of chemical and their corresponding concentrations Operating conditions Air flow rate Imppeller speed Special conditions
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Introduction to research
What is research? A detailed study of a subject in order to discover new information or reach a new understanding Sustainable chemicals Cellulose derivatives Cellulose is a rigid polymer whose properties can be varied Certain cellulose derivatives have similar attribute as surfactants Their macromolecular size affects their behavior
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Experimental design Experiment No Chemicals pH Re-grinding 1
NF240 50ppm 5,5 No 2 HPMC 50ppm 3 NF240 30ppm + HPMC 16ppm 4 10 5 6 7 ZnSO4Β 100 g/t SIBX 100 g/t NF ppm 8 HPMC 50 ppm 9 NF ppm + HPMC 16ppm Yes 11 12 13 14 15 16 17 18
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Total volume of suspension
Experimental design Parameter Value Air flow rate 4 l/min Impeller speed 1300 rpm Flotation time 30 min Solid content 33 w-% Amount of solids 600 g Amount of water 1200 g Total volume of suspension 1,5 l This and the previous slide combined is called the experimental design
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Case: Experimental flotation studies
What properties can be measured? Mass of fractions Concentration of elements (grade) Particle size distribution What properties can be calculated? Mass pull Recovery Kinetic constant Separation Efficiency Median particle size (a.k.a. d50)
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Mathematical relations vs. real life
Recovery πΉπππππππ= πͺπ ππ βπππ % C = mass of concentrate c = fraction of valuable mineral in the concentrate F = mass of feed f = fraction of valuable mineral in the feed Mass pull π΄πππ ππππ= πͺ π βπππ %
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Mathematical relations vs. real life
Β Test Fraction 0-3min 3-6min 6-10min 10-14min 14-20min 20-30min Tailings Total Tot. 0-30min 2 Β Mass (g) - Measured 203,7 16,9 2,6 0,4 0,2 360,4 584,6 224,2 Mass pull of froth fractions (%) - Calculated 34,84 2,89 0,44 0,07 0,03 38,35 Grade of Cu (%)Β - Measured 0,020 0,042 0,063 0,000 0,110 0,08 Cc (Ff) - Calculated 0,041 0,007 0,0016 0,396 (0,45) 0,049 Recovery - Calculated 9,14 % 1,57 % 0,37 % 0,00 % 88,92 % 11,08 %
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Mathematical relations vs. real life
Kinetics πΉ= πΉ πππ [πβ πππ βππ ] R = total recovery at a time t Rmax = maximum theoretical recovery k = kinetic constant t = time This is called the first order kinetic equation
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Mathematical relations vs. real life
Β Test Fraction 0-3min 3-6min 6-10min 10-14min 14-20min 20-30min k (s^-1) Rmax (%) Diff^2 2 t (min) 3 6 10 14 20 30 Β Recovery 9,1 % 10,7 % 11,1 % 0,57845 11,08 0,00002 % Modelled recovery 9,13 % 10,74 % 11,05 % 11,08 % βThis is how you experimentally calculate the value for kβ βby applying the first order kinetic equation to the experimental data we are able to determine the famous k, you used in your assignmentsβ Solved wΓth MS-Excel βSolverβ πΉ= πΉ πππ [πβ πππ βππ ] This value is minimized in the solver function
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Mathematical relations vs. real life
Separation efficiency ππΈ= π
π β π
π = 100 πΆ π (πβπ) πβπ π SE = separation efficiency Rm = % recovery of the valuable mineral Rg = % recovery of the gangue into the concentrate C = the fraction of total feed weight that reports to the concentrate f = % of metal in the feed c = % of metal in the concentrate m = % of valuable element in the mineral πΆ= π
ππππ£πππ¦ βπΉπππ πΊππππ πππππ’ππ‘ πΊππππ β 100 %
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Mathematical relations vs. real life
Test Cummulative Recovery of Cu at t = 30 min (%) Cumulative grade of Cu at t = 30 min (%) Feed Grade - Cu (%) 11 35,6 % 0,293 % 0,096% C Cu content in Chalcopyrite (%) Separation Efficiency β in relation to Cu (%) 0,116 34,63 24,03
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Particle size distribution
One of the most common ways to determine the particle size distribution of the sample is to use laser diffraction
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Particle size distribution β Raw data
Frequency Undersize Size Classes (ΞΌm) Volume Density (%) 0,259261 0,313977 0,294563 6,51E-05 0,35673 0,000653 0,334671 0,007234 0,405303 0,066636 0,380241 0,073965 0,46049 0,146005 0,432016 0,095575 0,523192 0,242499 0,490841 0,116317 0,594431 0,361877 0,557675 0,1439 0,675371 0,511252 0,63361 0,18 0,767332 0,698918 0,719884 0,226027 0,871814 0,934148 0,817906 0,283131 0,990523 1,226744
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Particle size distribution β Working with the data
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Particle size distribution β Working with the data
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What do you do with all this data?
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Behavorial tendencies from graphs
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Behavorial tendencies from graphs
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Behavorial tendencies from graphs
SE = 10 % SE = 20 %
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Behavorial tendencies from graphs
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Thank you!
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