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Input file: ../examples/ex11
Output file: ex11.out
Database file: ../database/phreeqc.dat
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Reading data base.
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SOLUTION_MASTER_SPECIES
SOLUTION_SPECIES
PHASES
GAS_BINARY_PARAMETERS
EXCHANGE_MASTER_SPECIES
EXCHANGE_SPECIES
SURFACE_MASTER_SPECIES
SURFACE_SPECIES
MEAN_GAMMAS
RATES
END
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Reading input data for simulation 1.
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TITLE Example 11.--Transport and cation exchange.
SOLUTION 0 CaCl2
units mmol/kgw
temp 25.0
pH 7.0 charge
pe 12.5 O2(g) -0.68
Ca 0.6
Cl 1.2
SOLUTION 1-40 Initial solution for column
units mmol/kgw
temp 25.0
pH 7.0 charge
pe 12.5 O2(g) -0.68
Na 1.0
K 0.2
N(5) 1.2
END
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TITLE
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Example 11.--Transport and cation exchange.
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Beginning of initial solution calculations.
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Initial solution 0. CaCl2
-----------------------------Solution composition------------------------------
Elements Molality Moles
Ca 6.000e-04 6.000e-04
Cl 1.200e-03 1.200e-03
----------------------------Description of solution----------------------------
pH = 6.995 Charge balance
pe = 13.632 Equilibrium with O2(g)
Specific Conductance (µS/cm, 25°C) = 155
Density (g/cm³) = 0.99710
Volume (L) = 1.00298
Viscosity (mPa s) = 0.89067
Activity of water = 1.000
Ionic strength (mol/kgw) = 1.800e-03
Mass of water (kg) = 1.000e+00
Total alkalinity (eq/kg) = -1.854e-20
Temperature (°C) = 25.00
Electrical balance (eq) = 2.979e-18
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
Iterations = 4
Total H = 1.110124e+02
Total O = 5.550675e+01
----------------------------Distribution of species----------------------------
Log Log Log mole V
Species Molality Activity Molality Activity Gamma cm³/mol
H+ 1.057e-07 1.012e-07 -6.976 -6.995 -0.019 0.00
OH- 1.049e-07 1.001e-07 -6.979 -7.000 -0.021 -4.10
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000 18.07
Ca 6.000e-04
Ca+2 6.000e-04 4.983e-04 -3.222 -3.302 -0.081 -18.10
CaOH+ 8.570e-10 8.175e-10 -9.067 -9.087 -0.020 (0)
Cl 1.200e-03
Cl- 1.200e-03 1.144e-03 -2.921 -2.941 -0.021 18.08
HCl 3.981e-11 3.988e-11 -10.400 -10.399 0.001 (0)
H(0) 0.000e+00
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000 28.61
O(0) 5.351e-04
O2 2.675e-04 2.676e-04 -3.573 -3.572 0.000 30.40
------------------------------Saturation indices-------------------------------
Phase SI** log IAP log K(298 K, 1 atm)
H2(g) -41.30 -44.40 -3.10 H2
H2O(g) -1.50 -0.00 1.50 H2O
O2(g) -0.68 -3.57 -2.89 O2 Pressure 0.2 atm, phi 1.000
**For a gas, SI = log10(fugacity). Fugacity = pressure * phi / 1 atm.
For ideal gases, phi = 1.
Initial solution 1. Initial solution for column
-----------------------------Solution composition------------------------------
Elements Molality Moles
K 2.000e-04 2.000e-04
N(5) 1.200e-03 1.200e-03
Na 1.000e-03 1.000e-03
----------------------------Description of solution----------------------------
pH = 6.997 Charge balance
pe = 13.630 Equilibrium with O2(g)
Specific Conductance (µS/cm, 25°C) = 145
Density (g/cm³) = 0.99711
Volume (L) = 1.00301
Viscosity (mPa s) = 0.89020
Activity of water = 1.000
Ionic strength (mol/kgw) = 1.200e-03
Mass of water (kg) = 1.000e+00
Total alkalinity (eq/kg) = -1.027e-18
Temperature (°C) = 25.00
Electrical balance (eq) = -9.088e-17
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 3 (7 overall)
Total H = 1.110124e+02
Total O = 5.551035e+01
----------------------------Distribution of species----------------------------
Log Log Log mole V
Species Molality Activity Molality Activity Gamma cm³/mol
H+ 1.045e-07 1.007e-07 -6.981 -6.997 -0.016 0.00
OH- 1.045e-07 1.005e-07 -6.981 -6.998 -0.017 -4.10
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000 18.07
H(0) 0.000e+00
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000 28.61
K 2.000e-04
K+ 2.000e-04 1.923e-04 -3.699 -3.716 -0.017 9.01
N(5) 1.200e-03
NO3- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017 29.49
Na 1.000e-03
Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017 -1.47
O(0) 5.351e-04
O2 2.676e-04 2.676e-04 -3.573 -3.572 0.000 30.40
------------------------------Saturation indices-------------------------------
Phase SI** log IAP log K(298 K, 1 atm)
H2(g) -41.30 -44.40 -3.10 H2
H2O(g) -1.50 -0.00 1.50 H2O
O2(g) -0.68 -3.57 -2.89 O2 Pressure 0.2 atm, phi 1.000
**For a gas, SI = log10(fugacity). Fugacity = pressure * phi / 1 atm.
For ideal gases, phi = 1.
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End of simulation.
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Reading input data for simulation 2.
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EXCHANGE 1-40
equilibrate 1
X 0.0011
COPY cell 1 101
END
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Beginning of initial exchange-composition calculations.
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Exchange 1.
X 1.100e-03 mol
Equiv- Equivalent Log
Species Moles alents Fraction Gamma
KX 5.507e-04 5.507e-04 5.006e-01 -0.017
NaX 5.493e-04 5.493e-04 4.994e-01 -0.017
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End of simulation.
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Reading input data for simulation 3.
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ADVECTION
cells 40
shifts 100
punch_cells 40
punch_frequency 1
print_cells 40
print_frequency 20
PRINT
reset false
WARNING: Cell-lengths were read for 1 cells. Last value is used till cell 40.
WARNING: Dispersivities were read for 1 cells. Last value is used till cell 40.
WARNING:
Calculating transport: 40 (mobile) cells, 100 shifts, 4 mixruns...