N.V. Sidenko & B.L Sherriff
Objective:
Understand major factors controlling metal mobility
concentrations and pH.
Predict changes in pH and metal concentration using
equilibrium calculations
Outline:
Equilibrium
pH, neutralization/acidification
Complexation in the solution
Solubility of metal solids
Ksp, IAP and saturation index,
System, closed, open, components, phases, species.
Modeling:
Active treatment (lime use)
Rb
H2O <--> H+ + OH-
reactant Rf products
EQ when Rf =Rb
EQ constant , K = activity of products/activity of
reactant
In diluted solutions, activity is equal to
concentration measured in mole per liter (mole/L or M)
Molar concentrations is input for most software
Law of mass action
K = KW (water
dissociation) = [H+][
a H2O = ?
KW = [H+][OH-]/[H2O]=
10-14, in neutral solution [H+]=[OH-]= 10-? M
pH = -Log[H+],
in neutral solution pH = -Log10-? = ?
M
What is [H+]
in stream with pH=3?
Answer:
Lime slurry has
pH=10, what is [
Answer:
Acidification -when H+ is produced or
In AMD, acid is produced
1) by
sulfide oxidation,
FeCuS2(chalcopyrite) + 7/2O2 +H2O
-> Fe2+ + Cu2+ +2SO42- + 2H+
then one H+ is consumed (left side of the
reaction) by Fe oxidation
Fe2+ + 1/4O2 + H+ -> Fe3+
+1/2H2O
2) by
complexation and precipitation, when some
Fe3+ + 2H2O -> Fe(OH)2+(aqueous
complex with OH-) +2H+
Fe3+ + 3H2O -> Fe(OH)3(Fe-hydroxide
precipitate) +3H+
Neutralization – when H+ is consumed or
When:
Ca2+ + 2OH- (slaked lime) + 2H+ -> Ca2+ + 2H2O
(hydroxide addition)
H++ CaCO3(calcite) -> Ca +
HCO3- (aqueous complex with H+) , or reaction
with salt of strong base and weak acid)
Q; Find
examples of minerals which are salts of strong base and weak acid
How much grams of calcite do we need to neutralize 1
liter of solution from ph 3 to pH 7.
a)Moles acid to be neutralized = 10-3 - 10-7
(very small copared to 10-3) ~ 10-3 M (moles/L)
b) 1 mole of calcite neutralizes 1 mole of acid (see
reaction above) means ~ 10-3 moles of calcite (M CaCO3 =
100 g/mole)
c) convert moles to grams
Metal complexes in the solution:
in solution, ions of opposite charge tend to associate
and form complexes:
Fe(OH)2+, Al(OH)3oaq,
PbSO4 oaq, HSO4-, FeHSO4+2
Dissolution/precipitation of metal solids. pH
dependence:
Dissolution of metal hydroxides is key factor
controlling metal migration and concentration during the treatment.
We assume that all metals (consider Zn as example)
during lime treatment will precipitate in form of hydroxide. Metal hydroxides
are considered in equilibrium with solution.
At what pH
solubility of c is lowest, meaning lowest Zn concentrations.
Write Zn(OH)2(solid) solubility
equation
|
Zn(OH)2(solid) + 2H+
-> Zn + 2H2O; |
K = [Zn2+]/[H+]2 =
1011.5; |
LgK=11.5 |
Take log of the law of mass action: LgK=Lg[Zn2+]
– 2log[H+]= Lg[Zn2+] + 2pH
Rearrange for Lg[Zn2+]:
|
Lg[Zn2+] = LgK- 2pH =
11.5 - 2pH |
(a) |
Plot this line in coordinates pH- Log[Zn2+]
At pH 4 [Zn2+] = 103.5M; at pH 8
[Zn2+] = 10-4.5M
However it will be concentration of free Zn ion or Zn2+,
which is not the same as total Zn, which is measured (and regulated in most
cases). Reason is formation of complexes. Hydroxide complexes can be suspected
at first because reaction occurs in the water.
|
Zn+2 + H2O = ZnOH+
+ H+; |
K = [H+][ZnOH+]/[Zn2+]
= 10-9; |
LgK=-9.0 |
Take log of the law of mass action:
LgK= Lg[H+] + Lg[ZnOH+]
- Lg[Zn2+]
= - pH + Lg[ZnOH+] -
Lg[Zn2+]
Solve for Lg[ZnOH+]; Lg[ZnOH+] =
pH + Lg[Zn2+] + LgK
|
Lg[ZnOH+] = Lg[Zn2+]
+ pH -9.0 |
(b0) |
Zn+2
concentrations are controlled by equilibrium with Zn(OH)2(solid).
Therefore, substitute for Lg[Zn2+] right side of equation (a)
|
Lg[ZnOH+] = 11.5 - 2pH
+ pH -9.0 |
(b1) |
|
Lg[ZnOH+] = 2.5 - pH |
(b2) |
Plot concentration of complex vs pH,
At pH 4 [ZnOH+] = 10-1.5M; at pH
8 [ZnOH+] = 10-5.5M, in both cases [ZnOH+]
lower than [Zn2+]
Another complex can have one more
hydroxide:
|
Zn+2 + 2H2O
= Zn(OH)2oaq + 2H+; |
K = [H+]2[Zn(OH)2o]/[Zn2+]
= 10-17.0; |
Take log law of mass action LgK= 2Lg[H+] +
Lg[Zn(OH)2o] - Lg[Zn2+]
Solve for Lg[Zn(OH)2o];
Lg[Zn(OH)2o] = Lg[Zn2+] - 2Lg[H+] +
lgK
|
Lg[Zn(OH)2 o]
= Lg[Zn2+] + 2pH -17.0 |
(c0) |
substitute for Lg[Zn2+] right side of
equation (a)
|
Lg[Zn(OH)2o]
= -5.5 |
(c1) |
Concentration of Zn(OH)2oaq
= 10-5.5M and does not depend on pH and this line will be parallel
to pH axis
at pH > 8.5, [Zn(OH)2oaq]
> [Zn2+]
(10-5.5M). Thus, pH just above
8.5 will require minimum use of lime for neutralization and achieve MINIMUM
total concentration of Zn 10-5.5M.
Another complex can have one more
hydroxide in alkaline conditions:
|
Zn+2 + 3H2O = Zn(OH)3-
+ 3H+; |
K = [H+]3[Zn(OH)3-]/[Zn2+]
= 10-28.4; |
Take log law of mass action LgK= 3Lg[H+] +
Lg[Zn(OH)3-] - Lg[Zn2+]
Solve for Lg[Zn(OH)3-];
Lg[Zn(OH)3-] = Lg[Zn2+] - 3Lg[H+] +
lgK
|
Lg[Zn(OH)2o]
= Lg[Zn2+] + 3pH - 28.4=11.5 - 2pH3pH - 28.4 |
(c0) |
substitute for Lg[Zn2+] right side of
equation (a)
|
Lg[Zn(OH) 3-]
= pH - 17.9 |
(c1) |
complex concentration increases with pH,
over pH 12.4, [Zn(OH) 3-] >
Zn(OH)2o (10-5.5M), this means that if we
increase pH further solubility of Zn(OH)2 solid will increase.
Thus, reaction Zn(OH)2oaq <=>
Zn(OH)2(solid) will control MINIMUM total
concentration of Zn 10-5.5M = 3.1x10-6M What is that in mg/l?
This reaction will dominate between pH 8.5 and 12.4.
Ksp, IAP and saturation index
If we know concentration of ions in the solution we
can predict possible metal solids which can be in equilibrium with solution
(not always 100%). Consider solution is in equilibrium with anglesite
PbSO4 (solid, anglesite) <->Pb2+
+ SO42-
Activity of PbSO4 solid?
K=Ksp
(solubility product) = [Pb2+][SO42-]=10-7.79
= tabulated value; LogKsp =-7.79
Your solution has 10-1M of [SO42-]
and 10-6.8 M of [Pb2+],
Ion Activity Product (IAP)= [Pb2+][SO42-]=10-1
x 10-8 = 10-7.8; LogIAP =-7.8
Saturation Index (SI) is comparison of tabulated solubility to ion
concentrations in the solution.
SI anglesite = Log (IAP/Ksp); if
IAP= Ksp then SI= 0
Log (IAP/Ksp) = Log(IAP) – LogKsp=-9 – (-7.79)
= -1.21.
Solution is undersaturated with respect to anglesite
(it cannot precipitate). Normally, if saturation index is 0±0.5, solid is
considered in equilibrium in the solution.
System: volume surrounded by boundaries:
Closed
system – maintain initial mass (confined groundwater)
Open system – open to mass transfer
trough boundary.(surface water)
AMD normally open to atmosphere PO2
= 0.2 PCO2 = 10-2.5
Phases :solid, gases and solution.
Species: forms of the element (in soulution in our case) ions or
complexes.
Fe2+,Fe3+,
FeSO4-, Fe(OH)20
Figure:
concentration of aqueous Zn species at different pH in equilibrium with
solid Zn(OH)2.

Assignment,
class &home:
1) Open file Sat_ind.phrq. Solution represents
seepage at toe of tailings.
Change database to wateq4f.dat.
a)
Run the program, identify, and list the most significant aqueous
complexes for Fe, Al, Cu, Zn, Ni and Pb.
b)
List minerals of Fe, Al, Cu, Zn, Ni and Pb, which might be in
equilibrium with solution.
2) Open file Lime_tr.phrq. We need to estimate
how much lime (Ca(OH)2 or Portlandite) should be added to reach saturation of
a) Al(OH)3(a), b) Cu(OH)2, c) Zn(OH)2-g, c)
Ni(OH)2, d) Pb(OH)2 (consider 0<SI<1)? Vary amount
of lime (Ca(OH)2 or Portlandite) and see how SI of the metal hydroxides will
change. System open to atmosphere during the treatment, therefore pressures of
gases are fixed, Fe(OH)3 and gypsum are minerals which expected to
precipitate. Therefore, all these phases are in equilibrium with solution.
Indicate pH at saturation of every hydroxide (a to d).
What pH should be reached to treat all these metals?
e) List the most significant aqueous complexes for Fe,
Al, Cu, Zn, Ni and Pb when the mental hydroxides precpitate.
Home
assignment.
3) Construct diagram solubility of Al(OH)3
solid in coordinates pH – lg[Al form in solution] using following data:
|
Al(OH)3(solid) + 3H+
= Al+3 + 3H2O |
log_k 10.8 |
|
Al+3 + H2O = AlOH+2
+ H+ |
log_k -5.0 |
|
Al+3 + 2H2O = Al(OH)2+
+ 2H+ |
log_k -10.1 |
|
Al+3 + 3H2O
= Al(OH)30aq + 3H+ |
log_k -16.9 |
|
Al+3 + 4H2O = Al(OH)4-
+ 4H+ |
log_k -22.7 |
Define lowest pH at lowest concentration of Al in the
solution in equilibrium with Al(OH)3.