Workbook Copper
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Transcript of Workbook Copper
HYDROMETALLURGY
Theory and Practice
Copper Course Workbook
Fundamentals
H-1,+1-259-253
1.0079
1
Hydrogen
Li+1181
1347
6.941
3
Lithium
Na+198
883
22.990
11
Sodium
K+164
774
39.098
19
Potassium
Rb+139
688
85.468
37
Rubidium
Cs+128
678
132.91
55
Cesium
Fr+127
677
223.02*
87
Francium
Be+2
12782970
9.0122
4
Beryllium
Mg+2649
1090
24.305
12
Magnesium
Ca+2839
1484
40.078
20
Calcium
Sr+2769
1384
87.62
38
Strontium
Ba+2725
1640
137.33
56
Barium
Ra+2700
1140
226.03*
88
Radium
Sc+3
15412831
44.956
21
Scandium
Y+3
15413338
88.906
39
Yttrium
La+3
9213457
138.91
57
Lanthanum
Ac+3
10503200
227.03*
89
Actinium
Ti+3,416603287
47.88
22
Titanium
Zr+4
18524377
91.224
40
Zirconium
Hf+4
22274602
178.49
72
Hafnium
V+2,3,4,5
18903380
50.942
23
Vanadium
Nb+3,524684742
92.906
41
Niobium
Ta+5
29965425
180.95
73
Tantalum
Cr+2,3,6
18572672
51.996
24
Chromium
Unq261*
104*
UnnilquadiumUnp
262*
105#
UnnilpentiumUnh
263*
106
UnnilhexiumUns
262*
107
Unnilseptium
108
Une266*
109
Unnilennium
Mo+2,3,4,5,6
18572672
95.94
42
Molybdenum
W+2,3,4,5,6
34105660
183.85
74
Tungsten
Mn+2,3,4,6,7
12441962
54.938
25
Manganese
Tc+7
21724877
98.906*
43
Technicium
Re+2,4,7
31805627
186.2
75
Rhenium
Fe+2,3,6
15352750
55.847
26
Iron
Ru+3,4,8
23103900
101.07
44
Ruthenium
Os+2,3,4,6,8
30455027
190.2
76
Osmium
Co+2,315352750
58.933
27
CobaltNi
+2,315352750
58.69
28
Nickel
Rh+1,2,3,4
19663727
102.91
45
Rhodium
Ir+1,2,3,4,6
24104130
192.22
77
Iridium
Pd+2,415523140
106.42
46
Palladium
Pt+2,417723827
195.08
78
Platinum
Cu+1,210832567
63.546
29
Copper
Ag+1,2962
2212
107.87
47
Silver
Au+1,310642807
196.97
79
Gold
Zn+2420907
65.39
30
Zinc
Cd+2321765
112.41
48
Cadmium
Hg+1,2-38.8357
200.59
80
Mercury
Al+3660
2467
26.982
13
Aluminium
B+3
20792550
10.811
5
BoronC
-4,+2,433674827
12.011
6
CarbonN
-3,+2,3,4,1-210-196
14.007
7
NitrogenO
-2,-1-218-183
15.999
8
OxygenF
-1-220-188
18.998
9
FluorineNe
0-249-246
20.179
10
Neon
He0
-272-269
4.0026
2
Helium
Si+4
14102355
28.086
14
Silicon
Ga+330
2403
69.723
31
GalliumGe
+4937
2830
72.61
32
Germanium
In+3157
2080
114.82
49
IndiumSn
+2,4232
2270
118.71
50
Tin
Tl+1,3157
2080
204.38
81
ThalliumPb
+2,4328
1740
207.2
82
Lead
P-3,+3,5
44280
30.974
15
Phosphorus
As-3,+3,5
817613
74.922
33
Arsenic
Sb-3,+3,5
6311750
121.75
51
Antimony
Bi+3,5271
1560
208.98
83
Bismuth
S-2,+2,4,6
113445
32.066
16
Sulphur
Se-2,+4,6
217685
78.96
34
Selenium
Te-2,+4,6
450990
127.60
52
Tellurium
Po+2,4,6
254962
208.98*
84
Polonium
Cl-1,+1,3,5,7
-101-35
35.453
17
Chlorine
Br-1,+1,3,5,7
-7.259
79.904
35
Bromine
I-1,+1,3,5,7
114184
126.90
53
Iodine
At-1,+1,3,5,7
302337
209.99*
85
Astatine
Kr+2,4-157-152
83.80
36
Krypton
Ar0
-189-186
39.948
18
Argon
Xe+2,4,6
-112-107
131.29
54
Xenon
Rn+2-71-62
222.02*
86
Radon
Ce+3,4799
3426
140.12
58
CeriumPr
+3,4931
3512
140.91
59
PraseodymiumNd
+310213068
144.24
60
NeodymiumPm
+311682460
146.92*
61
PromethiumSm
+2,310771791
150.36
62
SamariumEu
+2,3822
1597
151.97
63
EuropiumGd
+313133266
157.25
64
GadoliniumTb
+3,413563123
158.93
65
TerbiumDy
+314122562
162.50
66
DysprosiumHo
+314742695
164.93
67
HolmiumEr
+314972900
167.26
68
ErbiumTm
+2,315451947
168.93
69
ThuliumYb
+2,3819
1194
173.04
70
YtterbiumLu
+316633395
174.97
71
Lutetium
Th+4
17504790
232.04*
90
ThoriumPa
+4,51600
231.04*
91
ProtactiniumU
+3,4,5,611323818
238.03*
92
UraniumNp
+3,4,5,6640
3902
237.05*
93
NeptiniumPu
+3,4,5,6641
3232
244.06*
94
PlutoniumAm
+3,4,5,6994
2607
243.06*
95
AmericiumCm
+3,41340
247.07*
96
CuriumBk
+3,4
247.07*
97
BerkeliumCf
+3,4
251.08*
98
CaliforniumEs
+3
252.08*
99
EinsteinumFm
+3
257.10*
100
FermiumMd
+3
258.10*
101
MendeleviumNo
+2,3
259.10*
102
NobeliumLr
+3
260.11*
103
Lawrencium
IA 1
IIA2
IIIB3
IVB4
VB5
VIB6
VIIB7
VIII8 9 10
IB11
IIB12
IIIA13
IVA14
VA15
VIA16
VIIA17
0 18
Co
+2,315352750
58.933
27
Cobalt
AtomicNumber
Symbol
Relative AtomicMass
Oxidation StatesMelting Point °CBoiling Point °C
Non-MetalsAlkaline Earth Metals
Noble gasesAlkali Metals
Platinum Group Metals Other Metals
Magnetic Metals
Transition Metals Lanthanides
Actinides
Lanthanides
Actinides
*Hahnium (USA)Kurchatovium (USSR)
#Rutherfordium (USA)Nielsbohrium (USSR)
Values of Useful Constants
Absolute zero temperature -273.2 oC Acceleration due gravity 9.8067 m s-2 Avogadro constant 6.022 x 1023 mol-1 Boltzmann constant 1.381 x 10-23 J K-1 Faraday constant, F 96490 C mol-1 Molar gas constant , R 8.315 J K-1 mol-1 Molar Volume of ideal gas (1 bar) 0.022712 m3 mol-1 Standard atmosphere 1.013 x 105 Pa
2.303RT/F = 0.0591 V at 298K
Useful Thermodynamic Formulae
G = H – T.S
G = -RT.lnK
G = -nF.E
E = Eo – RT/(nF). ln {[Red]/[Ox]}
= Eo -0.0591/n . log {[Red]/[Ox]} at 25oC
HTo = H298
o + 298T Cp
o dt
GoT = Ho
298 -TSo298 +(T-298) Cp
o]T298 - T Cp
o]T298 ln(T/298).
4
Class and Workshop Problems
Class Problems
Class Problem 1 An ore contains chalcopyrite, covellite and chalcocite as the only minerals of copper, iron and sulfur. Chemical analysis gives 0.60% Cu, 0.137% Fe and 0.312% S. Calculate the % of each of the minerals in the ore. Check your answer using the Mineralogy option in HSC. How much copper (tonnes/a) could be produced in a plant treating 10000t/d of the ore if the recovery of copper is 45% from chalcopyrite, 75% from covellite and 95% from chalcocite ?
5
Class Problem 2 An ore consists of 80% quartz, 10% Cu2O and 10% chalcopyrite. If 1 kg of ore is reacted with 1 L of 1 M HCl in the absence of dissolved oxygen only the Cu2O dissolves. The pH is maintained by addition of 10 M HCl (density 1.18 g/cm3). You can assume an initial and final solution density of 1.02 and 1.08 g/cm3 respectively.
Determine
1) the minimum volume of 10M HCl required.
2) the final concentrations of dissolved species
3) a mass balance
6
Class Problem 3 Consider the hydrolysis equilibrium:
Fe3+ + H2O = Fe(OH)2+ + H+ : K1 = 10-2.2
Show that
pH = pK1 + log {[Fe(OH)2+]/[Fe3+]}
Plot the variation of [Fe(OH)2+] and [Fe3+] as a function of pH in the range pH 0-3 and total [Fe(III)] = 0.1M
7
Class Problem 4 What is the fraction of copper(I) present as CuCl2
- in a 1M chloride solution containing 0.01M of total copper(I). Use HSC to obtain the relevant stability constants.
8
Class Problem 5 Estimate the enthalpy (per mole Cu produced) associated with the electrowinning of copper at 298K and 1 atmosphere pressure by the reaction CuSO4(a) + H2O(l) = Cu + H2SO4(a) + 1/2O2
9
Class Problem 6 Sketch the curve for the ratio of NH4
+/NH3 as a function of pH.
10
Class Problem 7
Copper(I) and (II) ions both form strong complexes with ammonia. Calculate the formal potential of the Cu(II)/Cu(I) couple in 1M ammonia solution using the data in Table 3.3 and Table 3.5 of Module 3.
11
Class Problem 8 The measured pH of 2 mol/L HCl at 298 K is –0.63. Calculate aH
+, γH+ and
aOH- of the solution.
12
Class Problem 9 An ore contains CuO and Al2O3. On leaching the ore, an equilibrium [Cu2+] of 0.1 mol/dm3 is obtained at 25oC. What is the pH in the leach and the equilibrium [Al3+]?
Class Problem 10 Assuming that the pH and the dissolved oxygen concentration are maintained at 2.0 and 1 mM respectively, calculate the half-life of a solution containing 0.1 M Fe2+ at 25oC using the rate equation below with k = 0.015 min-1.75 .
13
-d[Fe2+]/dt = k [Fe2+]2.[O2]/[H+]0.25
If the activation energy for the reaction is 80kJ/mol, calculate the half life of the reaction at 90oC. Assume the same parameters as the above problem but allow for the lower solubility (0.40 of solubility at 25oC) of oxygen at the higher temperature.
Convert the above equation to one for the rate of disappearance of oxygen and calculate the pseudo-1st order rate constant for [Fe(II)] = 0.1M and pH 2.
Class Problem 11 Using the data provided in relevant table in the notes, calculate the overpotential you would expect for the reduction of Cu ions (1M) at current densities of 200 and 300 A m-2. Use the “high field” approximation.
14
Do the same for the evolution of oxygen on the lead anode at the same current densities assuming the high field approximation.
What would be the actual potentials(versus SHE) at the anode and cathode for a solution with unit activity copper and hydrogen ions for each current density?
Class Problem 12 Calculate the initial rate(g s-1) of dissolution of copper from a suspended spherical 100m particle of CuS in a 0.01M ferric solution assuming that the rate is controlled by the mass transport of ferric ions to the surface and that the product is Cu2S.
15
Class Problem 13
Calculate the cell voltage for the EW of copper using the results (anode and cathode potentials) of Class Problem 4 i.e. a cell operating with an electrolyte
16
containing 40 g/L CuSO4 and 175 g/L H2SO4 at 300A/m2 . Assume an anode/cathode spacing of 50mm.
Class Problem 14 Copper can be dissolved in aerated acidic aqueous solutions by the reaction
Cu + O2 + H+ Cu2+ + H2O
17
The rate of reaction is controlled by mass transport of dissolved oxygen from the gas phase into the solution. Estimate the maximum rate of dissolution (in g copper h-1) of copper powder suspended in a stirred reactor with an air/solution interfacial area of 1m2. The aqueous phase mass transfer coefficient for oxygen is 1 x 10-3 cm s-1 and the solubility of oxygen in equilibrium with air is 2.5 x 10-4 M.
18
Workshop Problems
Workshop Problem 1 Species Distribution
You are required to derive the species distribution using HSC for a solution containing 0.1M FeSO4 + 0.05M Fe2(SO4)3 at pH values between 3.0 and 1.0 at 80oC by adding increasing amounts of H2SO4 to the above solution. Repeat the calculation for an initial solution containing 1M H2SO4 to which is added increasing amounts of Na2SO4 up to 2M.
Workshop Problem 2 Species Distribution and Electrochemical Potentials
You are required to derive the species distribution using HSC for a solution containing 0.1M Cu(II) and 0.1M Cu(I) as a function of the concentration of chloride from 0.5M to 5M at 25oC. Export the relevant results to Excel and calculate the formal potential of the copper(II)/copper(I) couple as a function of chloride concentration (Use HSC to obtain the standard potential for the couple Cu2+ + e = Cu+) Calculate the potential for the reduction of Cu(I) in the presence of sulfur to produce covellite(CuS) as a function of the chloride concentration assuming a concentration of 0.1M Cu(I). Thence calculate the equilibrium constant for the dissolution of covellite (CuS) by the oxidation reaction
CuS + Cu(II) = 2Cu(I) + S
as a function of chloride of concentration. What conclusions can you draw about the viability of this as a leaching process for covellite?
Workshop Problem 3 Homogeneous Kinetics
The spreadsheet (Workshop Problem 3.xls) contains information on published data for the oxidation of ferrous ions to ferric ions in sulfate solutions. This is an important reaction in the leaching of most sulfide and some oxide minerals which require oxidation of the mineral by ferric ions. The low concentration of dissolved oxygen and the very slow direct oxidation kinetics by oxygen requires a catalyst or redox mediator such as the ferric/ferrous couple in order for these reactions to proceed at an acceptable rate. The re-oxidation of ferrous to ferric by dissolved oxygen is therefore important. The rate of this reaction can be increased by increasing the temperature and the oxygen concentration (by increasing the
19
pressure) as in the so-called pressure leach process. It can also be increased in the presence of suitable bacteria as in the bacterial oxidation or bio-leaching processes.
You are required to make a study of the kinetics of this reaction using the data given as well as other appropriate data that may be required.
Write a balanced chemical equation for the reaction.
Referring to the data in section (A) of the spreadsheet, establish the order of the reaction with respect to iron(II) and use Excel to make suitable plots from which you can derive appropriate rate constants for each run.
In a similar way, establish the reaction order with respect to oxygen by using the data in section (B) and derive rate constants.
Repeat (iii) using the data in section ( C) which shows the effect of added sulfate on the rate of oxidation.
Use the species distribution diagrams obtained in Workshop Problem 1 together with the data in (V) to explain the apparent effect of acid concentration on the rate as shown in section (A).
Derive an overall rate equation which can be used to calculate the rate of oxidation as a function of the various concentrations and the oxygen pressure at 353K. This rate equation can then be used in a linear regression of all the data to obtain a “best-fit” value for the rate constant.
Workshop Problem 4 Homogeneous and Heterogeneous Kinetics
Copper(I) in ammoniacal solutions forms the stable Cu(NH3)2
+ complex ion which is rapidly oxidized by dissolved oxygen to the Cu(NH3)4
2+ complex. The rate of the reaction can be conveniently measured by an amperometric technique which measures a current that is proportional to the concentration of copper(I). The following results (Workshop Problem 4.xls) were obtained in an experiment in which the initial concentrations are shown in the second row of Table 2 below. The dissolved oxygen concentration was maintained constant by sparging air into the solution.
20
Table 1. Results of a test with initial concentrations in 2nd row of Table 2
Time, s Current0.0 1.4720.5 1.2981.0 1.1261.5 0.9932.0 0.8682.5 0.7583.0 0.6664.0 0.5195.0 0.4026.0 0.3157.0 0.2438.0 0.194
10.0 0.12212.0 0.08014.0 0.05016.0 0.029
Table 2. Pseudo-First Order Rate Constants
[Cu(I)],M [NH4+], M [NH3], M [O2],M k1, sec-1
1.00E-04 0.01 0.01 2.50E-04 0.101
1.00E-04 0.025 0.025 2.50E-04 ???????
1.00E-04 0.05 0.05 2.50E-04 0.485
1.00E-04 0.025 0.025 2.50E-04 0.253
1.20E-04 0.025 0.025 2.50E-04 0.263
1.50E-04 0.025 0.025 2.50E-04 0.258
1.00E-04 0.01 0.01 1.00E-03 0.419
1. Write a balanced equation for the reaction. 2. Graphically or otherwise, demonstrate that the data in Table 1 is consistent
with a reaction which is first order in Cu(I). 3. Using the data in Table 2, derive the reaction orders with respect to
ammonia and dissolved oxygen. 4. Write the overall rate equation and calculate values for the overall rate
constant for each of the experimental runs in Table 2.
In a pilot plant, a solution of copper(I) initially containing 1x10-4mol/l of copper(I) and 0.01M ammonia/0.01M ammonium ions is oxidised by stirring the solution in an open reactor containing 1m3 of solution. The internal diameter of the tank is 1m.
Assuming that the rate of oxidation is controlled by mass transport of oxygen into the aqueous phase, calculate the rate of oxidation of copper(I) in mol l-1
21
min-1. The aqueous phase mass transfer coefficient for oxygen from the surface of the interface is 2 x 10-4 cm s-1 and the solubility of oxygen is 2.5 x 10-4 mol/l.
Sketch a graph of the concentration of copper(I) in solution as a function of time under these conditions.
Compare the rate of oxidation of copper(I) under these conditions with that calculated for the rate of the chemical reaction.