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PBasic not used here. Will compare to this. git-svn-id: svn://136.177.114.72/svn_GW/phreeqcpp/branches/ErrorHandling@5748 1feff8c3-07ed-0310-ac33-dd36852eb9cd
2894 lines
93 KiB
Plaintext
2894 lines
93 KiB
Plaintext
Input file: ../examples/ex11
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Output file: ex11.out
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Database file: ../database/phreeqc.dat
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------------------
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Reading data base.
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------------------
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SOLUTION_MASTER_SPECIES
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SOLUTION_SPECIES
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PHASES
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EXCHANGE_MASTER_SPECIES
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EXCHANGE_SPECIES
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SURFACE_MASTER_SPECIES
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SURFACE_SPECIES
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RATES
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END
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------------------------------------
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Reading input data for simulation 1.
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------------------------------------
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PRINT
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TITLE Example 11.--Transport and ion exchange.
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SOLUTION 0 CaCl2
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units mmol/kgw
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temp 25.0
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pH 7.0 charge
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pe 12.5 O2(g) -0.68
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Ca 0.6
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Cl 1.2
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SOLUTION 1-40 Initial solution for column
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units mmol/kgw
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temp 25.0
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pH 7.0 charge
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pe 12.5 O2(g) -0.68
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Na 1.0
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K 0.2
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N(5) 1.2
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EXCHANGE 1-40
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equilibrate 1
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X 0.0011
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ADVECTION
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cells 40
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shifts 120
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punch_cells 40
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punch_frequency 1
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print_cells 40
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print_frequency 20
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SELECTED_OUTPUT
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file ex11adv.sel
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reset false
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step
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totals Na Cl K Ca
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USER_PUNCH
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heading Pore_vol
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10 PUNCH (STEP_NO + .5) / 40.
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END
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-----
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TITLE
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-----
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Example 11.--Transport and ion exchange.
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-------------------------------------------
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Beginning of initial solution calculations.
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-------------------------------------------
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Initial solution 0. CaCl2
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-----------------------------Solution composition------------------------------
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Elements Molality Moles
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Ca 6.000e-04 6.000e-04
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Cl 1.200e-03 1.200e-03
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----------------------------Description of solution----------------------------
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pH = 6.997 Charge balance
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pe = 13.630 Equilibrium with O2(g)
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Specific Conductance (uS/cm, 25 oC) = 155
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Density (g/cm3) = 0.99711
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Activity of water = 1.000
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Ionic strength = 1.800e-03
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Mass of water (kg) = 1.000e+00
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Total alkalinity (eq/kg) = 1.156e-19
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Total carbon (mol/kg) = 0.000e+00
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Total CO2 (mol/kg) = 0.000e+00
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Temperature (deg C) = 25.000
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Electrical balance (eq) = 4.099e-18
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Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
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Iterations = 4
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Total H = 1.110124e+02
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Total O = 5.550675e+01
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----------------------------Distribution of species----------------------------
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Log Log Log
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Species Molality Activity Molality Activity Gamma
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H+ 1.052e-07 1.006e-07 -6.978 -6.997 -0.019
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OH- 1.043e-07 9.948e-08 -6.982 -7.002 -0.021
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H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
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Ca 6.000e-04
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Ca+2 6.000e-04 4.985e-04 -3.222 -3.302 -0.081
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CaOH+ 8.617e-10 8.221e-10 -9.065 -9.085 -0.020
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Cl 1.200e-03
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Cl- 1.200e-03 1.144e-03 -2.921 -2.941 -0.021
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H(0) 0.000e+00
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H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
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O(0) 5.352e-04
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O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
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------------------------------Saturation indices-------------------------------
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Phase SI log IAP log KT
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H2(g) -41.25 -44.40 -3.15 H2
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H2O(g) -1.51 -0.00 1.51 H2O
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O2(g) -0.68 -3.57 -2.89 O2
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Initial solution 1. Initial solution for column
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-----------------------------Solution composition------------------------------
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Elements Molality Moles
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K 2.000e-04 2.000e-04
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N(5) 1.200e-03 1.200e-03
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Na 1.000e-03 1.000e-03
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----------------------------Description of solution----------------------------
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pH = 6.999 Charge balance
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pe = 13.628 Equilibrium with O2(g)
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Specific Conductance (uS/cm, 25 oC) = 146
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Density (g/cm3) = 0.99706
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Activity of water = 1.000
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Ionic strength = 1.200e-03
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Mass of water (kg) = 1.000e+00
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Total alkalinity (eq/kg) = -9.547e-19
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Total carbon (mol/kg) = 0.000e+00
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Total CO2 (mol/kg) = 0.000e+00
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Temperature (deg C) = 25.000
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Electrical balance (eq) = -8.377e-17
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Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
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Iterations = 3
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Total H = 1.110124e+02
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Total O = 5.551035e+01
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----------------------------Distribution of species----------------------------
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Log Log Log
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Species Molality Activity Molality Activity Gamma
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H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
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OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
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H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
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H(0) 0.000e+00
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H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
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K 2.000e-04
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K+ 2.000e-04 1.923e-04 -3.699 -3.716 -0.017
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KOH 6.654e-12 6.656e-12 -11.177 -11.177 0.000
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N(5) 1.200e-03
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NO3- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017
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Na 1.000e-03
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Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017
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NaOH 6.342e-11 6.344e-11 -10.198 -10.198 0.000
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O(0) 5.352e-04
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O2 2.676e-04 2.677e-04 -3.572 -3.572 0.000
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------------------------------Saturation indices-------------------------------
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Phase SI log IAP log KT
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H2(g) -41.25 -44.40 -3.15 H2
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H2O(g) -1.51 -0.00 1.51 H2O
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O2(g) -0.68 -3.57 -2.89 O2
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-------------------------------------------------------
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Beginning of initial exchange-composition calculations.
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-------------------------------------------------------
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Exchange 1.
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X 1.100e-03 mol
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Equiv- Equivalent Log
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Species Moles alents Fraction Gamma
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KX 5.507e-04 5.507e-04 5.006e-01 -0.017
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NaX 5.493e-04 5.493e-04 4.994e-01 -0.017
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-----------------------------------------
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Beginning of batch-reaction calculations.
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-----------------------------------------
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Reaction step 1.
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Using solution 0. CaCl2
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Using exchange 1. Exchange assemblage after simulation 1.
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-----------------------------Exchange composition------------------------------
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X 1.100e-03 mol
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Equiv- Equivalent Log
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Species Moles alents Fraction Gamma
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CaX2 4.933e-04 9.866e-04 8.969e-01 -0.069
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KX 9.224e-05 9.224e-05 8.385e-02 -0.018
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NaX 2.120e-05 2.120e-05 1.928e-02 -0.017
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-----------------------------Solution composition------------------------------
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Elements Molality Moles
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Ca 1.067e-04 1.067e-04
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Cl 1.200e-03 1.200e-03
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K 4.584e-04 4.584e-04
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Na 5.281e-04 5.281e-04
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----------------------------Description of solution----------------------------
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pH = 6.999 Charge balance
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pe = 13.628 Adjusted to redox equilibrium
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Specific Conductance (uS/cm, 25 oC) = 159
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Density (g/cm3) = 0.99711
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Activity of water = 1.000
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Ionic strength = 1.307e-03
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Mass of water (kg) = 1.000e+00
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Total alkalinity (eq/kg) = 3.103e-19
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Total carbon (mol/kg) = 0.000e+00
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Total CO2 (mol/kg) = 0.000e+00
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Temperature (deg C) = 25.000
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Electrical balance (eq) = 9.601e-14
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Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
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Iterations = 8
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Total H = 1.110124e+02
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Total O = 5.550675e+01
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----------------------------Distribution of species----------------------------
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Log Log Log
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Species Molality Activity Molality Activity Gamma
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H+ 1.042e-07 1.003e-07 -6.982 -6.999 -0.017
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OH- 1.040e-07 9.983e-08 -6.983 -7.001 -0.018
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H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
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Ca 1.067e-04
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Ca+2 1.067e-04 9.098e-05 -3.972 -4.041 -0.069
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CaOH+ 1.568e-10 1.506e-10 -9.805 -9.822 -0.018
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Cl 1.200e-03
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Cl- 1.200e-03 1.152e-03 -2.921 -2.938 -0.018
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H(0) 0.000e+00
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H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
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K 4.584e-04
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K+ 4.584e-04 4.402e-04 -3.339 -3.356 -0.018
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KOH 1.522e-11 1.522e-11 -10.818 -10.818 0.000
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Na 5.281e-04
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Na+ 5.281e-04 5.073e-04 -3.277 -3.295 -0.017
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NaOH 3.342e-11 3.343e-11 -10.476 -10.476 0.000
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O(0) 5.352e-04
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O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
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------------------------------Saturation indices-------------------------------
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Phase SI log IAP log KT
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H2(g) -41.25 -44.40 -3.15 H2
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H2O(g) -1.51 -0.00 1.51 H2O
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Halite -7.82 -6.23 1.58 NaCl
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O2(g) -0.68 -3.57 -2.89 O2
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------------------------------------
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Beginning of advection calculations.
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------------------------------------
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Beginning of advection time step 1, cumulative pore volumes 0.025000.
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Beginning of advection time step 2, cumulative pore volumes 0.050000.
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Beginning of advection time step 3, cumulative pore volumes 0.075000.
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Beginning of advection time step 4, cumulative pore volumes 0.100000.
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Beginning of advection time step 5, cumulative pore volumes 0.125000.
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Beginning of advection time step 6, cumulative pore volumes 0.150000.
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Beginning of advection time step 7, cumulative pore volumes 0.175000.
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Beginning of advection time step 8, cumulative pore volumes 0.200000.
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Beginning of advection time step 9, cumulative pore volumes 0.225000.
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Beginning of advection time step 10, cumulative pore volumes 0.250000.
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Beginning of advection time step 11, cumulative pore volumes 0.275000.
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Beginning of advection time step 12, cumulative pore volumes 0.300000.
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Beginning of advection time step 13, cumulative pore volumes 0.325000.
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Beginning of advection time step 14, cumulative pore volumes 0.350000.
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Beginning of advection time step 15, cumulative pore volumes 0.375000.
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Beginning of advection time step 16, cumulative pore volumes 0.400000.
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Beginning of advection time step 17, cumulative pore volumes 0.425000.
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Beginning of advection time step 18, cumulative pore volumes 0.450000.
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Beginning of advection time step 19, cumulative pore volumes 0.475000.
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Beginning of advection time step 20, cumulative pore volumes 0.500000.
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Cell 40.
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Using solution 40. Solution after simulation 1.
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Using exchange 40. Exchange assemblage after simulation 1.
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-----------------------------Exchange composition------------------------------
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X 1.100e-03 mol
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Equiv- Equivalent Log
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Species Moles alents Fraction Gamma
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KX 5.507e-04 5.507e-04 5.006e-01 -0.017
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NaX 5.493e-04 5.493e-04 4.994e-01 -0.017
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NH4X 3.038e-63 3.038e-63 2.761e-60 -0.017
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-----------------------------Solution composition------------------------------
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Elements Molality Moles
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K 2.000e-04 2.000e-04
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N 1.200e-03 1.200e-03
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Na 1.000e-03 1.000e-03
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----------------------------Description of solution----------------------------
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pH = 6.999 Charge balance
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pe = 13.628 Adjusted to redox equilibrium
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Specific Conductance (uS/cm, 25 oC) = 146
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Density (g/cm3) = 0.99706
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Activity of water = 1.000
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Ionic strength = 1.200e-03
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Mass of water (kg) = 1.000e+00
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Total alkalinity (eq/kg) = -9.547e-19
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Total carbon (mol/kg) = 0.000e+00
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Total CO2 (mol/kg) = 0.000e+00
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Temperature (deg C) = 25.000
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Electrical balance (eq) = -3.321e-16
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Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
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Iterations = 0
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Total H = 1.110124e+02
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Total O = 5.551035e+01
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----------------------------Distribution of species----------------------------
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Log Log Log
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Species Molality Activity Molality Activity Gamma
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H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
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OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
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H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
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H(0) 0.000e+00
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H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
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K 2.000e-04
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K+ 2.000e-04 1.923e-04 -3.699 -3.716 -0.017
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KOH 6.654e-12 6.656e-12 -11.177 -11.177 0.000
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N(-3) 0.000e+00
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NH4+ 0.000e+00 0.000e+00 -62.857 -62.874 -0.017
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NH3 0.000e+00 0.000e+00 -65.120 -65.120 0.000
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N(0) 1.729e-19
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N2 8.645e-20 8.647e-20 -19.063 -19.063 0.000
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N(3) 2.485e-16
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NO2- 2.485e-16 2.389e-16 -15.605 -15.622 -0.017
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N(5) 1.200e-03
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NO3- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017
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Na 1.000e-03
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Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017
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NaOH 6.342e-11 6.344e-11 -10.198 -10.198 0.000
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O(0) 5.352e-04
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O2 2.676e-04 2.677e-04 -3.572 -3.572 0.000
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------------------------------Saturation indices-------------------------------
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Phase SI log IAP log KT
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H2(g) -41.25 -44.40 -3.15 H2
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H2O(g) -1.51 -0.00 1.51 H2O
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N2(g) -15.80 -19.06 -3.26 N2
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NH3(g) -66.89 -65.12 1.77 NH3
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O2(g) -0.68 -3.57 -2.89 O2
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Beginning of advection time step 21, cumulative pore volumes 0.525000.
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Beginning of advection time step 22, cumulative pore volumes 0.550000.
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Beginning of advection time step 23, cumulative pore volumes 0.575000.
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Beginning of advection time step 24, cumulative pore volumes 0.600000.
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Beginning of advection time step 25, cumulative pore volumes 0.625000.
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Beginning of advection time step 26, cumulative pore volumes 0.650000.
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Beginning of advection time step 27, cumulative pore volumes 0.675000.
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Beginning of advection time step 28, cumulative pore volumes 0.700000.
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Beginning of advection time step 29, cumulative pore volumes 0.725000.
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Beginning of advection time step 30, cumulative pore volumes 0.750000.
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Beginning of advection time step 31, cumulative pore volumes 0.775000.
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Beginning of advection time step 32, cumulative pore volumes 0.800000.
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Beginning of advection time step 33, cumulative pore volumes 0.825000.
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Beginning of advection time step 34, cumulative pore volumes 0.850000.
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Beginning of advection time step 35, cumulative pore volumes 0.875000.
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Beginning of advection time step 36, cumulative pore volumes 0.900000.
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Beginning of advection time step 37, cumulative pore volumes 0.925000.
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Beginning of advection time step 38, cumulative pore volumes 0.950000.
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Beginning of advection time step 39, cumulative pore volumes 0.975000.
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Beginning of advection time step 40, cumulative pore volumes 1.000000.
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Cell 40.
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Using solution 40. Solution after simulation 1.
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Using exchange 40. Exchange assemblage after simulation 1.
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-----------------------------Exchange composition------------------------------
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X 1.100e-03 mol
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Equiv- Equivalent Log
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Species Moles alents Fraction Gamma
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|
|
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KX 5.507e-04 5.507e-04 5.006e-01 -0.017
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NaX 5.493e-04 5.493e-04 4.994e-01 -0.017
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-----------------------------Solution composition------------------------------
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Elements Molality Moles
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Cl 1.200e-03 1.200e-03
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K 2.000e-04 2.000e-04
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Na 1.000e-03 1.000e-03
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----------------------------Description of solution----------------------------
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pH = 6.999 Charge balance
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pe = 13.628 Adjusted to redox equilibrium
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Specific Conductance (uS/cm, 25 oC) = 152
|
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Density (g/cm3) = 0.99710
|
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Activity of water = 1.000
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Ionic strength = 1.200e-03
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Mass of water (kg) = 1.000e+00
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Total alkalinity (eq/kg) = -3.748e-20
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Total carbon (mol/kg) = 0.000e+00
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Total CO2 (mol/kg) = 0.000e+00
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Temperature (deg C) = 25.000
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Electrical balance (eq) = 2.960e-12
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Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
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Iterations = 0
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Total H = 1.110124e+02
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Total O = 5.550675e+01
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|
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----------------------------Distribution of species----------------------------
|
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|
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Log Log Log
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Species Molality Activity Molality Activity Gamma
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|
|
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H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
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OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
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H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
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Cl 1.200e-03
|
|
Cl- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 2.000e-04
|
|
K+ 2.000e-04 1.923e-04 -3.699 -3.716 -0.017
|
|
KOH 6.654e-12 6.656e-12 -11.177 -11.177 0.000
|
|
Na 1.000e-03
|
|
Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017
|
|
NaOH 6.342e-11 6.344e-11 -10.198 -10.198 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -7.54 -5.95 1.58 NaCl
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
Beginning of advection time step 41, cumulative pore volumes 1.025000.
|
|
Beginning of advection time step 42, cumulative pore volumes 1.050000.
|
|
Beginning of advection time step 43, cumulative pore volumes 1.075000.
|
|
Beginning of advection time step 44, cumulative pore volumes 1.100000.
|
|
Beginning of advection time step 45, cumulative pore volumes 1.125000.
|
|
Beginning of advection time step 46, cumulative pore volumes 1.150000.
|
|
Beginning of advection time step 47, cumulative pore volumes 1.175000.
|
|
Beginning of advection time step 48, cumulative pore volumes 1.200000.
|
|
Beginning of advection time step 49, cumulative pore volumes 1.225000.
|
|
Beginning of advection time step 50, cumulative pore volumes 1.250000.
|
|
Beginning of advection time step 51, cumulative pore volumes 1.275000.
|
|
Beginning of advection time step 52, cumulative pore volumes 1.300000.
|
|
Beginning of advection time step 53, cumulative pore volumes 1.325000.
|
|
Beginning of advection time step 54, cumulative pore volumes 1.350000.
|
|
Beginning of advection time step 55, cumulative pore volumes 1.375000.
|
|
Beginning of advection time step 56, cumulative pore volumes 1.400000.
|
|
Beginning of advection time step 57, cumulative pore volumes 1.425000.
|
|
Beginning of advection time step 58, cumulative pore volumes 1.450000.
|
|
Beginning of advection time step 59, cumulative pore volumes 1.475000.
|
|
Beginning of advection time step 60, cumulative pore volumes 1.500000.
|
|
|
|
Cell 40.
|
|
|
|
Using solution 40. Solution after simulation 1.
|
|
Using exchange 40. Exchange assemblage after simulation 1.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
X 1.100e-03 mol
|
|
|
|
Equiv- Equivalent Log
|
|
Species Moles alents Fraction Gamma
|
|
|
|
KX 7.000e-04 7.000e-04 6.363e-01 -0.017
|
|
NaX 4.000e-04 4.000e-04 3.637e-01 -0.017
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Cl 1.200e-03 1.200e-03
|
|
K 3.105e-04 3.105e-04
|
|
Na 8.895e-04 8.895e-04
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.999 Charge balance
|
|
pe = 13.628 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 155
|
|
Density (g/cm3) = 0.99710
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.200e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = -1.003e-18
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 3.548e-12
|
|
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
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
|
|
OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Cl 1.200e-03
|
|
Cl- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 3.105e-04
|
|
K+ 3.105e-04 2.986e-04 -3.508 -3.525 -0.017
|
|
KOH 1.033e-11 1.033e-11 -10.986 -10.986 0.000
|
|
Na 8.895e-04
|
|
Na+ 8.895e-04 8.558e-04 -3.051 -3.068 -0.017
|
|
NaOH 5.641e-11 5.643e-11 -10.249 -10.249 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -7.59 -6.01 1.58 NaCl
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
Beginning of advection time step 61, cumulative pore volumes 1.525000.
|
|
Beginning of advection time step 62, cumulative pore volumes 1.550000.
|
|
Beginning of advection time step 63, cumulative pore volumes 1.575000.
|
|
Beginning of advection time step 64, cumulative pore volumes 1.600000.
|
|
Beginning of advection time step 65, cumulative pore volumes 1.625000.
|
|
Beginning of advection time step 66, cumulative pore volumes 1.650000.
|
|
Beginning of advection time step 67, cumulative pore volumes 1.675000.
|
|
Beginning of advection time step 68, cumulative pore volumes 1.700000.
|
|
Beginning of advection time step 69, cumulative pore volumes 1.725000.
|
|
Beginning of advection time step 70, cumulative pore volumes 1.750000.
|
|
Beginning of advection time step 71, cumulative pore volumes 1.775000.
|
|
Beginning of advection time step 72, cumulative pore volumes 1.800000.
|
|
Beginning of advection time step 73, cumulative pore volumes 1.825000.
|
|
Beginning of advection time step 74, cumulative pore volumes 1.850000.
|
|
Beginning of advection time step 75, cumulative pore volumes 1.875000.
|
|
Beginning of advection time step 76, cumulative pore volumes 1.900000.
|
|
Beginning of advection time step 77, cumulative pore volumes 1.925000.
|
|
Beginning of advection time step 78, cumulative pore volumes 1.950000.
|
|
Beginning of advection time step 79, cumulative pore volumes 1.975000.
|
|
Beginning of advection time step 80, cumulative pore volumes 2.000000.
|
|
|
|
Cell 40.
|
|
|
|
Using solution 40. Solution after simulation 1.
|
|
Using exchange 40. Exchange assemblage after simulation 1.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
X 1.100e-03 mol
|
|
|
|
Equiv- Equivalent Log
|
|
Species Moles alents Fraction Gamma
|
|
|
|
CaX2 5.500e-04 1.100e-03 1.000e+00 -0.081
|
|
KX 6.870e-09 6.870e-09 6.246e-06 -0.021
|
|
NaX 2.513e-21 2.513e-21 2.285e-18 -0.020
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Ca 6.000e-04 6.000e-04
|
|
Cl 1.200e-03 1.200e-03
|
|
K 7.667e-08 7.667e-08
|
|
Na 1.406e-19 1.406e-19
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.997 Charge balance
|
|
pe = 13.630 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 155
|
|
Density (g/cm3) = 0.99711
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.800e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = 7.069e-19
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 3.087e-18
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 6
|
|
Total H = 1.110124e+02
|
|
Total O = 5.550675e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.052e-07 1.006e-07 -6.978 -6.997 -0.019
|
|
OH- 1.043e-07 9.948e-08 -6.982 -7.002 -0.021
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Ca 6.000e-04
|
|
Ca+2 6.000e-04 4.984e-04 -3.222 -3.302 -0.081
|
|
CaOH+ 8.617e-10 8.220e-10 -9.065 -9.085 -0.020
|
|
Cl 1.200e-03
|
|
Cl- 1.200e-03 1.144e-03 -2.921 -2.941 -0.021
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 7.667e-08
|
|
K+ 7.667e-08 7.312e-08 -7.115 -7.136 -0.021
|
|
KOH 2.519e-15 2.520e-15 -14.599 -14.599 0.000
|
|
Na 1.406e-19
|
|
Na+ 1.406e-19 1.341e-19 -18.852 -18.872 -0.020
|
|
NaOH 8.804e-27 8.807e-27 -26.055 -26.055 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -23.40 -21.81 1.58 NaCl
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
Beginning of advection time step 81, cumulative pore volumes 2.025000.
|
|
Beginning of advection time step 82, cumulative pore volumes 2.050000.
|
|
Beginning of advection time step 83, cumulative pore volumes 2.075000.
|
|
Beginning of advection time step 84, cumulative pore volumes 2.100000.
|
|
Beginning of advection time step 85, cumulative pore volumes 2.125000.
|
|
Beginning of advection time step 86, cumulative pore volumes 2.150000.
|
|
Beginning of advection time step 87, cumulative pore volumes 2.175000.
|
|
Beginning of advection time step 88, cumulative pore volumes 2.200000.
|
|
Beginning of advection time step 89, cumulative pore volumes 2.225000.
|
|
Beginning of advection time step 90, cumulative pore volumes 2.250000.
|
|
Beginning of advection time step 91, cumulative pore volumes 2.275000.
|
|
Beginning of advection time step 92, cumulative pore volumes 2.300000.
|
|
Beginning of advection time step 93, cumulative pore volumes 2.325000.
|
|
Beginning of advection time step 94, cumulative pore volumes 2.350000.
|
|
Beginning of advection time step 95, cumulative pore volumes 2.375000.
|
|
Beginning of advection time step 96, cumulative pore volumes 2.400000.
|
|
Beginning of advection time step 97, cumulative pore volumes 2.425000.
|
|
Beginning of advection time step 98, cumulative pore volumes 2.450000.
|
|
Beginning of advection time step 99, cumulative pore volumes 2.475000.
|
|
Beginning of advection time step 100, cumulative pore volumes 2.500000.
|
|
|
|
Cell 40.
|
|
|
|
Using solution 40. Solution after simulation 1.
|
|
Using exchange 40. Exchange assemblage after simulation 1.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
X 1.100e-03 mol
|
|
|
|
Equiv- Equivalent Log
|
|
Species Moles alents Fraction Gamma
|
|
|
|
CaX2 5.500e-04 1.100e-03 1.000e+00 -0.081
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Ca 6.000e-04 6.000e-04
|
|
Cl 1.200e-03 1.200e-03
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.997 Charge balance
|
|
pe = 13.630 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 155
|
|
Density (g/cm3) = 0.99711
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.800e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = 1.156e-19
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 4.099e-18
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 0
|
|
Total H = 1.110124e+02
|
|
Total O = 5.550675e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.052e-07 1.006e-07 -6.978 -6.997 -0.019
|
|
OH- 1.043e-07 9.948e-08 -6.982 -7.002 -0.021
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Ca 6.000e-04
|
|
Ca+2 6.000e-04 4.985e-04 -3.222 -3.302 -0.081
|
|
CaOH+ 8.617e-10 8.221e-10 -9.065 -9.085 -0.020
|
|
Cl 1.200e-03
|
|
Cl- 1.200e-03 1.144e-03 -2.921 -2.941 -0.021
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
Beginning of advection time step 101, cumulative pore volumes 2.525000.
|
|
Beginning of advection time step 102, cumulative pore volumes 2.550000.
|
|
Beginning of advection time step 103, cumulative pore volumes 2.575000.
|
|
Beginning of advection time step 104, cumulative pore volumes 2.600000.
|
|
Beginning of advection time step 105, cumulative pore volumes 2.625000.
|
|
Beginning of advection time step 106, cumulative pore volumes 2.650000.
|
|
Beginning of advection time step 107, cumulative pore volumes 2.675000.
|
|
Beginning of advection time step 108, cumulative pore volumes 2.700000.
|
|
Beginning of advection time step 109, cumulative pore volumes 2.725000.
|
|
Beginning of advection time step 110, cumulative pore volumes 2.750000.
|
|
Beginning of advection time step 111, cumulative pore volumes 2.775000.
|
|
Beginning of advection time step 112, cumulative pore volumes 2.800000.
|
|
Beginning of advection time step 113, cumulative pore volumes 2.825000.
|
|
Beginning of advection time step 114, cumulative pore volumes 2.850000.
|
|
Beginning of advection time step 115, cumulative pore volumes 2.875000.
|
|
Beginning of advection time step 116, cumulative pore volumes 2.900000.
|
|
Beginning of advection time step 117, cumulative pore volumes 2.925000.
|
|
Beginning of advection time step 118, cumulative pore volumes 2.950000.
|
|
Beginning of advection time step 119, cumulative pore volumes 2.975000.
|
|
Beginning of advection time step 120, cumulative pore volumes 3.000000.
|
|
|
|
Cell 40.
|
|
|
|
Using solution 40. Solution after simulation 1.
|
|
Using exchange 40. Exchange assemblage after simulation 1.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
X 1.100e-03 mol
|
|
|
|
Equiv- Equivalent Log
|
|
Species Moles alents Fraction Gamma
|
|
|
|
CaX2 5.500e-04 1.100e-03 1.000e+00 -0.081
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Ca 6.000e-04 6.000e-04
|
|
Cl 1.200e-03 1.200e-03
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.997 Charge balance
|
|
pe = 13.630 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 155
|
|
Density (g/cm3) = 0.99711
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.800e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = 1.156e-19
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 4.099e-18
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 0
|
|
Total H = 1.110124e+02
|
|
Total O = 5.550675e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.052e-07 1.006e-07 -6.978 -6.997 -0.019
|
|
OH- 1.043e-07 9.948e-08 -6.982 -7.002 -0.021
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Ca 6.000e-04
|
|
Ca+2 6.000e-04 4.985e-04 -3.222 -3.302 -0.081
|
|
CaOH+ 8.617e-10 8.221e-10 -9.065 -9.085 -0.020
|
|
Cl 1.200e-03
|
|
Cl- 1.200e-03 1.144e-03 -2.921 -2.941 -0.021
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
------------------
|
|
End of simulation.
|
|
------------------
|
|
|
|
------------------------------------
|
|
Reading input data for simulation 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
|
|
EXCHANGE 1-40
|
|
equilibrate 1
|
|
X 0.0011
|
|
TRANSPORT
|
|
cells 40
|
|
length 0.002
|
|
shifts 120
|
|
time_step 720.0
|
|
flow_direction forward
|
|
boundary_conditions flux flux
|
|
diffc 0.0e-9
|
|
dispersivity 0.002
|
|
correct_disp true
|
|
punch 40
|
|
punch_frequency 1
|
|
print 40
|
|
print_frequency 20
|
|
SELECTED_OUTPUT
|
|
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.
|
|
file ex11trn.sel
|
|
reset false
|
|
step
|
|
totals Na Cl K Ca
|
|
END
|
|
-------------------------------------------
|
|
Beginning of initial solution calculations.
|
|
-------------------------------------------
|
|
|
|
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 = 6.999 Charge balance
|
|
pe = 13.628 Equilibrium with O2(g)
|
|
Specific Conductance (uS/cm, 25 oC) = 146
|
|
Density (g/cm3) = 0.99706
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.200e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = -9.547e-19
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = -8.377e-17
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
|
|
Iterations = 3
|
|
Total H = 1.110124e+02
|
|
Total O = 5.551035e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
|
|
OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 2.000e-04
|
|
K+ 2.000e-04 1.923e-04 -3.699 -3.716 -0.017
|
|
KOH 6.654e-12 6.656e-12 -11.177 -11.177 0.000
|
|
N(5) 1.200e-03
|
|
NO3- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017
|
|
Na 1.000e-03
|
|
Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017
|
|
NaOH 6.342e-11 6.344e-11 -10.198 -10.198 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.572 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
-------------------------------------------------------
|
|
Beginning of initial exchange-composition calculations.
|
|
-------------------------------------------------------
|
|
|
|
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
|
|
|
|
-----------------------------------------
|
|
Beginning of batch-reaction calculations.
|
|
-----------------------------------------
|
|
|
|
Reaction step 1.
|
|
|
|
Using solution 1. Initial solution for column
|
|
Using exchange 1. Exchange assemblage after simulation 2.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
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
|
|
NH4X 3.038e-63 3.038e-63 2.761e-60 -0.017
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
K 2.000e-04 2.000e-04
|
|
N 1.200e-03 1.200e-03
|
|
Na 1.000e-03 1.000e-03
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.999 Charge balance
|
|
pe = 13.628 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 146
|
|
Density (g/cm3) = 0.99706
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.200e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = -9.547e-19
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = -3.325e-16
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
|
|
Iterations = 0
|
|
Total H = 1.110124e+02
|
|
Total O = 5.551035e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
|
|
OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 2.000e-04
|
|
K+ 2.000e-04 1.923e-04 -3.699 -3.716 -0.017
|
|
KOH 6.654e-12 6.656e-12 -11.177 -11.177 0.000
|
|
N(-3) 0.000e+00
|
|
NH4+ 0.000e+00 0.000e+00 -62.857 -62.874 -0.017
|
|
NH3 0.000e+00 0.000e+00 -65.120 -65.120 0.000
|
|
N(0) 1.729e-19
|
|
N2 8.645e-20 8.647e-20 -19.063 -19.063 0.000
|
|
N(3) 2.485e-16
|
|
NO2- 2.485e-16 2.389e-16 -15.605 -15.622 -0.017
|
|
N(5) 1.200e-03
|
|
NO3- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017
|
|
Na 1.000e-03
|
|
Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017
|
|
NaOH 6.342e-11 6.344e-11 -10.198 -10.198 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.572 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
N2(g) -15.80 -19.06 -3.26 N2
|
|
NH3(g) -66.89 -65.12 1.77 NH3
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
------------------------------------
|
|
Beginning of transport calculations.
|
|
------------------------------------
|
|
|
|
-------------------------------
|
|
Equilibrating initial solutions
|
|
-------------------------------
|
|
|
|
Using solution 40. Initial solution for column
|
|
Using exchange 40. Exchanger defined in simulation 2.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
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
|
|
NH4X 3.038e-63 3.038e-63 2.761e-60 -0.017
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
K 2.000e-04 2.000e-04
|
|
N 1.200e-03 1.200e-03
|
|
Na 1.000e-03 1.000e-03
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.999 Charge balance
|
|
pe = 13.628 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 146
|
|
Density (g/cm3) = 0.99706
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.200e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = -9.547e-19
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = -3.325e-16
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
|
|
Iterations = 0
|
|
Total H = 1.110124e+02
|
|
Total O = 5.551035e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
|
|
OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 2.000e-04
|
|
K+ 2.000e-04 1.923e-04 -3.699 -3.716 -0.017
|
|
KOH 6.654e-12 6.656e-12 -11.177 -11.177 0.000
|
|
N(-3) 0.000e+00
|
|
NH4+ 0.000e+00 0.000e+00 -62.857 -62.874 -0.017
|
|
NH3 0.000e+00 0.000e+00 -65.120 -65.120 0.000
|
|
N(0) 1.729e-19
|
|
N2 8.645e-20 8.647e-20 -19.063 -19.063 0.000
|
|
N(3) 2.485e-16
|
|
NO2- 2.485e-16 2.389e-16 -15.605 -15.622 -0.017
|
|
N(5) 1.200e-03
|
|
NO3- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017
|
|
Na 1.000e-03
|
|
Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017
|
|
NaOH 6.342e-11 6.344e-11 -10.198 -10.198 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.572 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
N2(g) -15.80 -19.06 -3.26 N2
|
|
NH3(g) -66.89 -65.12 1.77 NH3
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
Transport step 1.
|
|
|
|
Transport step 1. Mixrun 1.
|
|
|
|
Transport step 1. Mixrun 2.
|
|
|
|
Transport step 1. Mixrun 3.
|
|
|
|
Transport step 1. Mixrun 4.
|
|
|
|
Transport step 2.
|
|
|
|
Transport step 2. Mixrun 1.
|
|
|
|
Transport step 2. Mixrun 2.
|
|
|
|
Transport step 2. Mixrun 3.
|
|
|
|
Transport step 2. Mixrun 4.
|
|
|
|
Transport step 3.
|
|
|
|
Transport step 3. Mixrun 1.
|
|
|
|
Transport step 3. Mixrun 2.
|
|
|
|
Transport step 3. Mixrun 3.
|
|
|
|
Transport step 3. Mixrun 4.
|
|
|
|
Transport step 4.
|
|
|
|
Transport step 4. Mixrun 1.
|
|
|
|
Transport step 4. Mixrun 2.
|
|
|
|
Transport step 4. Mixrun 3.
|
|
|
|
Transport step 4. Mixrun 4.
|
|
|
|
Transport step 5.
|
|
|
|
Transport step 5. Mixrun 1.
|
|
|
|
Transport step 5. Mixrun 2.
|
|
|
|
Transport step 5. Mixrun 3.
|
|
|
|
Transport step 5. Mixrun 4.
|
|
|
|
Transport step 6.
|
|
|
|
Transport step 6. Mixrun 1.
|
|
|
|
Transport step 6. Mixrun 2.
|
|
|
|
Transport step 6. Mixrun 3.
|
|
|
|
Transport step 6. Mixrun 4.
|
|
|
|
Transport step 7.
|
|
|
|
Transport step 7. Mixrun 1.
|
|
|
|
Transport step 7. Mixrun 2.
|
|
|
|
Transport step 7. Mixrun 3.
|
|
|
|
Transport step 7. Mixrun 4.
|
|
|
|
Transport step 8.
|
|
|
|
Transport step 8. Mixrun 1.
|
|
|
|
Transport step 8. Mixrun 2.
|
|
|
|
Transport step 8. Mixrun 3.
|
|
|
|
Transport step 8. Mixrun 4.
|
|
|
|
Transport step 9.
|
|
|
|
Transport step 9. Mixrun 1.
|
|
|
|
Transport step 9. Mixrun 2.
|
|
|
|
Transport step 9. Mixrun 3.
|
|
|
|
Transport step 9. Mixrun 4.
|
|
|
|
Transport step 10.
|
|
|
|
Transport step 10. Mixrun 1.
|
|
|
|
Transport step 10. Mixrun 2.
|
|
|
|
Transport step 10. Mixrun 3.
|
|
|
|
Transport step 10. Mixrun 4.
|
|
|
|
Transport step 11.
|
|
|
|
Transport step 11. Mixrun 1.
|
|
|
|
Transport step 11. Mixrun 2.
|
|
|
|
Transport step 11. Mixrun 3.
|
|
|
|
Transport step 11. Mixrun 4.
|
|
|
|
Transport step 12.
|
|
|
|
Transport step 12. Mixrun 1.
|
|
|
|
Transport step 12. Mixrun 2.
|
|
|
|
Transport step 12. Mixrun 3.
|
|
|
|
Transport step 12. Mixrun 4.
|
|
|
|
Transport step 13.
|
|
|
|
Transport step 13. Mixrun 1.
|
|
|
|
Transport step 13. Mixrun 2.
|
|
|
|
Transport step 13. Mixrun 3.
|
|
|
|
Transport step 13. Mixrun 4.
|
|
|
|
Transport step 14.
|
|
|
|
Transport step 14. Mixrun 1.
|
|
|
|
Transport step 14. Mixrun 2.
|
|
|
|
Transport step 14. Mixrun 3.
|
|
|
|
Transport step 14. Mixrun 4.
|
|
|
|
Transport step 15.
|
|
|
|
Transport step 15. Mixrun 1.
|
|
|
|
Transport step 15. Mixrun 2.
|
|
|
|
Transport step 15. Mixrun 3.
|
|
|
|
Transport step 15. Mixrun 4.
|
|
|
|
Transport step 16.
|
|
|
|
Transport step 16. Mixrun 1.
|
|
|
|
Transport step 16. Mixrun 2.
|
|
|
|
Transport step 16. Mixrun 3.
|
|
|
|
Transport step 16. Mixrun 4.
|
|
|
|
Transport step 17.
|
|
|
|
Transport step 17. Mixrun 1.
|
|
|
|
Transport step 17. Mixrun 2.
|
|
|
|
Transport step 17. Mixrun 3.
|
|
|
|
Transport step 17. Mixrun 4.
|
|
|
|
Transport step 18.
|
|
|
|
Transport step 18. Mixrun 1.
|
|
|
|
Transport step 18. Mixrun 2.
|
|
|
|
Transport step 18. Mixrun 3.
|
|
|
|
Transport step 18. Mixrun 4.
|
|
|
|
Transport step 19.
|
|
|
|
Transport step 19. Mixrun 1.
|
|
|
|
Transport step 19. Mixrun 2.
|
|
|
|
Transport step 19. Mixrun 3.
|
|
|
|
Transport step 19. Mixrun 4.
|
|
|
|
Transport step 20.
|
|
|
|
Transport step 20. Mixrun 1.
|
|
|
|
Transport step 20. Mixrun 2.
|
|
|
|
Transport step 20. Mixrun 3.
|
|
|
|
Transport step 20. Mixrun 4.
|
|
|
|
Using mix 40.
|
|
Using exchange 40. Exchange assemblage after simulation 2.
|
|
|
|
Mixture 40.
|
|
|
|
2.625e-01 Solution 39 Solution after simulation 2.
|
|
0.000e+00 Solution 41 Solution after simulation 2.
|
|
7.375e-01 Solution 40 Solution after simulation 2.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
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
|
|
NH4X 3.033e-63 3.033e-63 2.757e-60 -0.017
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Cl 1.848e-06 1.848e-06
|
|
K 2.000e-04 2.000e-04
|
|
N 1.198e-03 1.198e-03
|
|
Na 1.000e-03 1.000e-03
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.999 Charge balance
|
|
pe = 13.628 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 146
|
|
Density (g/cm3) = 0.99706
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.200e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = -7.546e-19
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 1.566e-14
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 2
|
|
Total H = 1.110124e+02
|
|
Total O = 5.551035e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
|
|
OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Cl 1.848e-06
|
|
Cl- 1.848e-06 1.777e-06 -5.733 -5.750 -0.017
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 2.000e-04
|
|
K+ 2.000e-04 1.923e-04 -3.699 -3.716 -0.017
|
|
KOH 6.654e-12 6.656e-12 -11.177 -11.177 0.000
|
|
N(-3) 0.000e+00
|
|
NH4+ 0.000e+00 0.000e+00 -62.858 -62.875 -0.017
|
|
NH3 0.000e+00 0.000e+00 -65.120 -65.120 0.000
|
|
N(0) 1.724e-19
|
|
N2 8.618e-20 8.620e-20 -19.065 -19.064 0.000
|
|
N(3) 2.481e-16
|
|
NO2- 2.481e-16 2.386e-16 -15.605 -15.622 -0.017
|
|
N(5) 1.198e-03
|
|
NO3- 1.198e-03 1.152e-03 -2.921 -2.939 -0.017
|
|
Na 1.000e-03
|
|
Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017
|
|
NaOH 6.342e-11 6.344e-11 -10.198 -10.198 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.572 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -10.35 -8.77 1.58 NaCl
|
|
N2(g) -15.80 -19.06 -3.26 N2
|
|
NH3(g) -66.89 -65.12 1.77 NH3
|
|
O2(g) -0.68 -3.57 -2.89 O2
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Using mix 40.
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Using exchange 40. Exchange assemblage after simulation 2.
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Mixture 40.
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2.625e-01 Solution 39 Solution after simulation 2.
|
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0.000e+00 Solution 41 Solution after simulation 2.
|
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7.375e-01 Solution 40 Solution after simulation 2.
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-----------------------------Exchange composition------------------------------
|
|
|
|
X 1.100e-03 mol
|
|
|
|
Equiv- Equivalent Log
|
|
Species Moles alents Fraction Gamma
|
|
|
|
KX 5.512e-04 5.512e-04 5.011e-01 -0.017
|
|
NaX 5.488e-04 5.488e-04 4.989e-01 -0.017
|
|
NH4X 1.315e-63 1.315e-63 1.196e-60 -0.017
|
|
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|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Cl 6.801e-04 6.801e-04
|
|
K 2.004e-04 2.004e-04
|
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N 5.199e-04 5.199e-04
|
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Na 9.996e-04 9.996e-04
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.999 Charge balance
|
|
pe = 13.628 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 150
|
|
Density (g/cm3) = 0.99709
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.200e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = 1.821e-18
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 8.884e-12
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 2
|
|
Total H = 1.110124e+02
|
|
Total O = 5.550831e+01
|
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|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
|
|
OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
|
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H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Cl 6.801e-04
|
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Cl- 6.801e-04 6.540e-04 -3.167 -3.184 -0.017
|
|
H(0) 0.000e+00
|
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H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 2.004e-04
|
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K+ 2.004e-04 1.927e-04 -3.698 -3.715 -0.017
|
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KOH 6.666e-12 6.668e-12 -11.176 -11.176 0.000
|
|
N(-3) 0.000e+00
|
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NH4+ 0.000e+00 0.000e+00 -63.220 -63.238 -0.017
|
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NH3 0.000e+00 0.000e+00 -65.483 -65.483 0.000
|
|
N(0) 3.246e-20
|
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N2 1.623e-20 1.624e-20 -19.790 -19.790 0.000
|
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N(3) 1.077e-16
|
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NO2- 1.077e-16 1.035e-16 -15.968 -15.985 -0.017
|
|
N(5) 5.199e-04
|
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NO3- 5.199e-04 4.999e-04 -3.284 -3.301 -0.017
|
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Na 9.996e-04
|
|
Na+ 9.996e-04 9.617e-04 -3.000 -3.017 -0.017
|
|
NaOH 6.340e-11 6.341e-11 -10.198 -10.198 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -7.78 -6.20 1.58 NaCl
|
|
N2(g) -16.53 -19.79 -3.26 N2
|
|
NH3(g) -67.25 -65.48 1.77 NH3
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
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Transport step 41.
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Transport step 41. Mixrun 1.
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Transport step 60. Mixrun 4.
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Using mix 40.
|
|
Using exchange 40. Exchange assemblage after simulation 2.
|
|
|
|
Mixture 40.
|
|
|
|
2.625e-01 Solution 39 Solution after simulation 2.
|
|
0.000e+00 Solution 41 Solution after simulation 2.
|
|
7.375e-01 Solution 40 Solution after simulation 2.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
X 1.100e-03 mol
|
|
|
|
Equiv- Equivalent Log
|
|
Species Moles alents Fraction Gamma
|
|
|
|
KX 9.451e-04 9.451e-04 8.592e-01 -0.017
|
|
NaX 1.549e-04 1.549e-04 1.408e-01 -0.017
|
|
CaX2 2.150e-20 4.300e-20 3.909e-17 -0.067
|
|
NH4X 3.848e-65 3.848e-65 3.498e-62 -0.017
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Ca 9.153e-23 9.153e-23
|
|
Cl 1.171e-03 1.171e-03
|
|
K 6.589e-04 6.589e-04
|
|
N 2.918e-05 2.918e-05
|
|
Na 5.411e-04 5.411e-04
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.999 Charge balance
|
|
pe = 13.628 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 163
|
|
Density (g/cm3) = 0.99711
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.200e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = 2.737e-18
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 3.043e-12
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 2
|
|
Total H = 1.110124e+02
|
|
Total O = 5.550684e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.040e-07 1.002e-07 -6.983 -6.999 -0.016
|
|
OH- 1.039e-07 9.991e-08 -6.983 -7.000 -0.017
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Ca 9.153e-23
|
|
Ca+2 9.153e-23 7.852e-23 -22.038 -22.105 -0.067
|
|
CaOH+ 1.352e-28 1.301e-28 -27.869 -27.886 -0.017
|
|
Cl 1.171e-03
|
|
Cl- 1.171e-03 1.126e-03 -2.932 -2.948 -0.017
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 6.589e-04
|
|
K+ 6.589e-04 6.337e-04 -3.181 -3.198 -0.017
|
|
KOH 2.192e-11 2.193e-11 -10.659 -10.659 0.000
|
|
N(-3) 0.000e+00
|
|
NH4+ 0.000e+00 0.000e+00 -64.471 -64.489 -0.017
|
|
NH3 0.000e+00 0.000e+00 -66.734 -66.734 0.000
|
|
N(0) 1.022e-22
|
|
N2 5.111e-23 5.113e-23 -22.291 -22.291 0.000
|
|
N(3) 6.043e-18
|
|
NO2- 6.043e-18 5.810e-18 -17.219 -17.236 -0.017
|
|
N(5) 2.918e-05
|
|
NO3- 2.918e-05 2.805e-05 -4.535 -4.552 -0.017
|
|
Na 5.411e-04
|
|
Na+ 5.411e-04 5.206e-04 -3.267 -3.284 -0.017
|
|
NaOH 3.432e-11 3.433e-11 -10.464 -10.464 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -7.81 -6.23 1.58 NaCl
|
|
N2(g) -19.03 -22.29 -3.26 N2
|
|
NH3(g) -68.50 -66.73 1.77 NH3
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
Transport step 61.
|
|
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|
Transport step 61. Mixrun 1.
|
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Transport step 61. Mixrun 2.
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Transport step 61. Mixrun 3.
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Transport step 64.
|
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Transport step 64. Mixrun 1.
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Using mix 40.
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Using exchange 40. Exchange assemblage after simulation 2.
|
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Mixture 40.
|
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|
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2.625e-01 Solution 39 Solution after simulation 2.
|
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0.000e+00 Solution 41 Solution after simulation 2.
|
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7.375e-01 Solution 40 Solution after simulation 2.
|
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|
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-----------------------------Exchange composition------------------------------
|
|
|
|
X 1.100e-03 mol
|
|
|
|
Equiv- Equivalent Log
|
|
Species Moles alents Fraction Gamma
|
|
|
|
CaX2 5.430e-04 1.086e-03 9.874e-01 -0.079
|
|
KX 1.370e-05 1.370e-05 1.245e-02 -0.020
|
|
NaX 2.152e-07 2.152e-07 1.956e-04 -0.020
|
|
NH4X 5.225e-68 5.225e-68 4.750e-65 -0.020
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Ca 5.226e-04 5.226e-04
|
|
Cl 1.199e-03 1.199e-03
|
|
K 1.436e-04 1.436e-04
|
|
N 5.912e-07 5.912e-07
|
|
Na 1.130e-05 1.130e-05
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.998 Charge balance
|
|
pe = 13.629 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 157
|
|
Density (g/cm3) = 0.99711
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.723e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = 7.177e-18
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 9.758e-12
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 2
|
|
Total H = 1.110124e+02
|
|
Total O = 5.550675e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.050e-07 1.006e-07 -6.979 -6.998 -0.019
|
|
OH- 1.043e-07 9.954e-08 -6.982 -7.002 -0.020
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Ca 5.226e-04
|
|
Ca+2 5.226e-04 4.358e-04 -3.282 -3.361 -0.079
|
|
CaOH+ 7.530e-10 7.191e-10 -9.123 -9.143 -0.020
|
|
Cl 1.199e-03
|
|
Cl- 1.199e-03 1.145e-03 -2.921 -2.941 -0.020
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 1.436e-04
|
|
K+ 1.436e-04 1.370e-04 -3.843 -3.863 -0.020
|
|
KOH 4.723e-12 4.725e-12 -11.326 -11.326 0.000
|
|
N(-3) 0.000e+00
|
|
NH4+ 0.000e+00 0.000e+00 -66.161 -66.182 -0.020
|
|
NH3 0.000e+00 0.000e+00 -68.429 -68.429 0.000
|
|
N(0) 4.165e-26
|
|
N2 2.083e-26 2.083e-26 -25.681 -25.681 0.000
|
|
N(3) 1.224e-19
|
|
NO2- 1.224e-19 1.168e-19 -18.912 -18.932 -0.020
|
|
N(5) 5.912e-07
|
|
NO3- 5.912e-07 5.642e-07 -6.228 -6.249 -0.020
|
|
Na 1.130e-05
|
|
Na+ 1.130e-05 1.080e-05 -4.947 -4.967 -0.020
|
|
NaOH 7.089e-13 7.092e-13 -12.149 -12.149 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -9.49 -7.91 1.58 NaCl
|
|
N2(g) -22.42 -25.68 -3.26 N2
|
|
NH3(g) -70.20 -68.43 1.77 NH3
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
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|
Transport step 81.
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Transport step 81. Mixrun 1.
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Transport step 100.
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Transport step 100. Mixrun 3.
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Transport step 100. Mixrun 4.
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Using mix 40.
|
|
Using exchange 40. Exchange assemblage after simulation 2.
|
|
|
|
Mixture 40.
|
|
|
|
2.625e-01 Solution 39 Solution after simulation 2.
|
|
0.000e+00 Solution 41 Solution after simulation 2.
|
|
7.375e-01 Solution 40 Solution after simulation 2.
|
|
|
|
-----------------------------Exchange composition------------------------------
|
|
|
|
X 1.100e-03 mol
|
|
|
|
Equiv- Equivalent Log
|
|
Species Moles alents Fraction Gamma
|
|
|
|
CaX2 5.499e-04 1.100e-03 9.999e-01 -0.080
|
|
KX 1.363e-07 1.363e-07 1.239e-04 -0.021
|
|
NaX 1.851e-09 1.851e-09 1.683e-06 -0.020
|
|
NH4X 6.359e-70 6.359e-70 5.781e-67 -0.021
|
|
|
|
-----------------------------Solution composition------------------------------
|
|
|
|
Elements Molality Moles
|
|
|
|
Ca 5.992e-04 5.992e-04
|
|
Cl 1.200e-03 1.200e-03
|
|
K 1.520e-06 1.520e-06
|
|
N 7.648e-09 7.648e-09
|
|
Na 1.035e-07 1.035e-07
|
|
|
|
----------------------------Description of solution----------------------------
|
|
|
|
pH = 6.997 Charge balance
|
|
pe = 13.630 Adjusted to redox equilibrium
|
|
Specific Conductance (uS/cm, 25 oC) = 155
|
|
Density (g/cm3) = 0.99711
|
|
Activity of water = 1.000
|
|
Ionic strength = 1.799e-03
|
|
Mass of water (kg) = 1.000e+00
|
|
Total alkalinity (eq/kg) = -1.989e-18
|
|
Total carbon (mol/kg) = 0.000e+00
|
|
Total CO2 (mol/kg) = 0.000e+00
|
|
Temperature (deg C) = 25.000
|
|
Electrical balance (eq) = 7.774e-14
|
|
Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 2
|
|
Total H = 1.110124e+02
|
|
Total O = 5.550675e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
|
|
|
Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.052e-07 1.006e-07 -6.978 -6.997 -0.019
|
|
OH- 1.043e-07 9.948e-08 -6.982 -7.002 -0.021
|
|
H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
|
Ca 5.992e-04
|
|
Ca+2 5.992e-04 4.978e-04 -3.222 -3.303 -0.080
|
|
CaOH+ 8.606e-10 8.210e-10 -9.065 -9.086 -0.020
|
|
Cl 1.200e-03
|
|
Cl- 1.200e-03 1.144e-03 -2.921 -2.941 -0.021
|
|
H(0) 0.000e+00
|
|
H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 1.520e-06
|
|
K+ 1.520e-06 1.450e-06 -5.818 -5.839 -0.021
|
|
KOH 4.994e-14 4.996e-14 -13.302 -13.301 0.000
|
|
N(-3) 0.000e+00
|
|
NH4+ 0.000e+00 0.000e+00 -68.049 -68.070 -0.021
|
|
NH3 0.000e+00 0.000e+00 -70.317 -70.317 0.000
|
|
N(0) 6.963e-30
|
|
N2 3.481e-30 3.483e-30 -29.458 -29.458 0.000
|
|
N(3) 1.584e-21
|
|
NO2- 1.584e-21 1.510e-21 -20.800 -20.821 -0.021
|
|
N(5) 7.648e-09
|
|
NO3- 7.648e-09 7.291e-09 -8.116 -8.137 -0.021
|
|
Na 1.035e-07
|
|
Na+ 1.035e-07 9.874e-08 -6.985 -7.006 -0.020
|
|
NaOH 6.480e-15 6.483e-15 -14.188 -14.188 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -11.53 -9.95 1.58 NaCl
|
|
N2(g) -26.20 -29.46 -3.26 N2
|
|
NH3(g) -72.09 -70.32 1.77 NH3
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
|
|
|
Transport step 101.
|
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Transport step 101. Mixrun 1.
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Transport step 101. Mixrun 2.
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Transport step 113.
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Transport step 114.
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Using mix 40.
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Using exchange 40. Exchange assemblage after simulation 2.
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Mixture 40.
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2.625e-01 Solution 39 Solution after simulation 2.
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0.000e+00 Solution 41 Solution after simulation 2.
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7.375e-01 Solution 40 Solution after simulation 2.
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-----------------------------Exchange composition------------------------------
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X 1.100e-03 mol
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Equiv- Equivalent Log
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Species Moles alents Fraction Gamma
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CaX2 5.500e-04 1.100e-03 1.000e+00 -0.081
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KX 1.753e-09 1.753e-09 1.593e-06 -0.021
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NaX 1.743e-11 1.743e-11 1.585e-08 -0.020
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NH4X 6.565e-72 6.565e-72 5.969e-69 -0.021
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-----------------------------Solution composition------------------------------
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Elements Molality Moles
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Ca 6.000e-04 6.000e-04
|
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Cl 1.200e-03 1.200e-03
|
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K 1.956e-08 1.956e-08
|
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N 7.901e-11 7.901e-11
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Na 9.751e-10 9.751e-10
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----------------------------Description of solution----------------------------
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pH = 6.997 Charge balance
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pe = 13.630 Adjusted to redox equilibrium
|
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Specific Conductance (uS/cm, 25 oC) = 155
|
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Density (g/cm3) = 0.99711
|
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Activity of water = 1.000
|
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Ionic strength = 1.800e-03
|
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Mass of water (kg) = 1.000e+00
|
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Total alkalinity (eq/kg) = 2.194e-19
|
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Total carbon (mol/kg) = 0.000e+00
|
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Total CO2 (mol/kg) = 0.000e+00
|
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Temperature (deg C) = 25.000
|
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Electrical balance (eq) = 1.160e-15
|
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Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00
|
|
Iterations = 2
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Total H = 1.110124e+02
|
|
Total O = 5.550675e+01
|
|
|
|
----------------------------Distribution of species----------------------------
|
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Log Log Log
|
|
Species Molality Activity Molality Activity Gamma
|
|
|
|
H+ 1.052e-07 1.006e-07 -6.978 -6.997 -0.019
|
|
OH- 1.043e-07 9.948e-08 -6.982 -7.002 -0.021
|
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H2O 5.551e+01 1.000e+00 1.744 -0.000 0.000
|
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Ca 6.000e-04
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Ca+2 6.000e-04 4.985e-04 -3.222 -3.302 -0.081
|
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CaOH+ 8.617e-10 8.221e-10 -9.065 -9.085 -0.020
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Cl 1.200e-03
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Cl- 1.200e-03 1.144e-03 -2.921 -2.941 -0.021
|
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H(0) 0.000e+00
|
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H2 0.000e+00 0.000e+00 -44.404 -44.404 0.000
|
|
K 1.956e-08
|
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K+ 1.956e-08 1.865e-08 -7.709 -7.729 -0.021
|
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KOH 6.425e-16 6.428e-16 -15.192 -15.192 0.000
|
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N(-3) 0.000e+00
|
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NH4+ 0.000e+00 0.000e+00 -70.035 -70.056 -0.021
|
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NH3 0.000e+00 0.000e+00 -72.303 -72.303 0.000
|
|
N(0) 7.431e-34
|
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N2 3.716e-34 3.717e-34 -33.430 -33.430 0.000
|
|
N(3) 1.636e-23
|
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NO2- 1.636e-23 1.560e-23 -22.786 -22.807 -0.021
|
|
N(5) 7.901e-11
|
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NO3- 7.901e-11 7.532e-11 -10.102 -10.123 -0.021
|
|
Na 9.751e-10
|
|
Na+ 9.751e-10 9.305e-10 -9.011 -9.031 -0.020
|
|
NaOH 6.107e-17 6.109e-17 -16.214 -16.214 0.000
|
|
O(0) 5.352e-04
|
|
O2 2.676e-04 2.677e-04 -3.573 -3.572 0.000
|
|
|
|
------------------------------Saturation indices-------------------------------
|
|
|
|
Phase SI log IAP log KT
|
|
|
|
H2(g) -41.25 -44.40 -3.15 H2
|
|
H2O(g) -1.51 -0.00 1.51 H2O
|
|
Halite -13.55 -11.97 1.58 NaCl
|
|
N2(g) -30.17 -33.43 -3.26 N2
|
|
NH3(g) -74.07 -72.30 1.77 NH3
|
|
O2(g) -0.68 -3.57 -2.89 O2
|
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|
------------------
|
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End of simulation.
|
|
------------------
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------------------------------------
|
|
Reading input data for simulation 3.
|
|
------------------------------------
|
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-----------
|
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End of run.
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-----------
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