Input file: H:\ntc\03\Tuesday\feldspar.pqi
  Output file: H:\ntc\03\Tuesday\feldspar.pqo
Database file: C:\Program Files\USGS\Phreeqc Interactive 2.7\phreeqc.dat

------------------
Reading data base.
------------------

	SOLUTION_MASTER_SPECIES
	SOLUTION_SPECIES
	PHASES
	EXCHANGE_MASTER_SPECIES
	EXCHANGE_SPECIES
	SURFACE_MASTER_SPECIES
	SURFACE_SPECIES
	RATES
	END
------------------------------------
Reading input data for simulation 1.
------------------------------------

	DATABASE C:\Program Files\USGS\Phreeqc Interactive 2.7\phreeqc.dat
	SOLUTION 1
	END
-------------------------------------------
Beginning of initial solution calculations.
-------------------------------------------

Initial solution 1.	

-----------------------------Solution composition------------------------------

	Elements           Molality       Moles

	Pure water
    
----------------------------Description of solution----------------------------

                                       pH  =   7.000    
                                       pe  =   4.000    
                        Activity of water  =   1.000
                           Ionic strength  =  1.001e-007
                       Mass of water (kg)  =  1.000e+000
                 Total alkalinity (eq/kg)  =  1.082e-010
                    Total carbon (mol/kg)  =  0.000e+000
                       Total CO2 (mol/kg)  =  0.000e+000
                      Temperature (deg C)  =  25.000
                  Electrical balance (eq)  = -1.082e-010
 Percent error, 100*(Cat-|An|)/(Cat+|An|)  =  -0.05
                               Iterations  =   0
                                  Total H  = 1.110124e+002
                                  Total O  = 5.550622e+001

----------------------------Distribution of species----------------------------

	                                           Log       Log         Log 
	Species            Molality    Activity  Molality  Activity     Gamma

	OH-              1.002e-007  1.001e-007    -6.999    -6.999    -0.000
	H+               1.001e-007  1.000e-007    -7.000    -7.000    -0.000
	H2O              5.551e+001  1.000e+000     1.744     0.000     0.000
H(0)            1.416e-025
	H2               7.079e-026  7.079e-026   -25.150   -25.150     0.000
O(0)            0.000e+000
	O2               0.000e+000  0.000e+000   -42.080   -42.080     0.000

------------------------------Saturation indices-------------------------------

	Phase               SI log IAP  log KT

	H2(g)           -22.00  -22.00    0.00  H2
	H2O(g)           -1.51    0.00    1.51  H2O
	O2(g)           -39.12   44.00   83.12  O2

------------------
End of simulation.
------------------

------------------------------------
Reading input data for simulation 2.
------------------------------------

	USE solution 1
	EQUILIBRIUM_PHASES 1
	    Gibbsite  0 KAlSi3O8  10
	END
-----------------------------------------
Beginning of batch-reaction calculations.
-----------------------------------------

Reaction step 1.

Using solution 1.	
Using pure phase assemblage 1.	

-------------------------------Phase assemblage--------------------------------

                                                     Moles in assemblage
	Phase               SI log IAP  log KT    Initial      Final      Delta

	Gibbsite          0.00    8.11    8.11
		KAlSi3O8        is reactant    1.000e+001 1.000e+001-3.081e-008

-----------------------------Solution composition------------------------------

	Elements           Molality       Moles

	Al               3.081e-008  3.081e-008
	K                3.081e-008  3.081e-008
	Si               9.243e-008  9.243e-008

----------------------------Description of solution----------------------------

                                       pH  =   7.007      Charge balance
                                       pe  =  10.956      Adjusted to redox equilibrium
                        Activity of water  =   1.000
                           Ionic strength  =  1.303e-007
                       Mass of water (kg)  =  1.000e+000
                 Total alkalinity (eq/kg)  =  1.234e-007
                    Total carbon (mol/kg)  =  0.000e+000
                       Total CO2 (mol/kg)  =  0.000e+000
                      Temperature (deg C)  =  25.000
                  Electrical balance (eq)  = -1.082e-010
 Percent error, 100*(Cat-|An|)/(Cat+|An|)  =  -0.04
                               Iterations  =   9
                                  Total H  = 1.110124e+002
                                  Total O  = 5.550622e+001

----------------------------Distribution of species----------------------------

	                                           Log       Log         Log 
	Species            Molality    Activity  Molality  Activity     Gamma

	OH-              1.018e-007  1.018e-007    -6.992    -6.992    -0.000
	H+               9.838e-008  9.834e-008    -7.007    -7.007    -0.000
	H2O              5.551e+001  1.000e+000     1.744    -0.000     0.000
Al              3.081e-008
	Al(OH)4-         2.833e-008  2.832e-008    -7.548    -7.548    -0.000
	Al(OH)3          1.478e-009  1.478e-009    -8.830    -8.830     0.000
	Al(OH)2+         9.867e-010  9.863e-010    -9.006    -9.006    -0.000
	AlOH+2           1.240e-011  1.238e-011   -10.907   -10.907    -0.001
	Al+3             1.230e-013  1.225e-013   -12.910   -12.912    -0.002
H(0)            1.677e-039
	H2               8.385e-040  8.385e-040   -39.077   -39.077     0.000
K               3.081e-008
	K+               3.081e-008  3.080e-008    -7.511    -7.511    -0.000
	KOH              1.086e-015  1.086e-015   -14.964   -14.964     0.000
O(0)            1.186e-014
	O2               5.930e-015  5.930e-015   -14.227   -14.227     0.000
Si              9.243e-008
	H4SiO4           9.229e-008  9.229e-008    -7.035    -7.035     0.000
	H3SiO4-          1.384e-010  1.384e-010    -9.859    -9.859    -0.000
	H2SiO4-2         9.588e-017  9.572e-017   -16.018   -16.019    -0.001

------------------------------Saturation indices-------------------------------

	Phase               SI log IAP  log KT

	Al(OH)3(a)       -2.69    8.11   10.80  Al(OH)3
	Chalcedony       -3.48   -7.03   -3.55  SiO2
	Gibbsite          0.00    8.11    8.11  Al(OH)3
	H2(g)           -35.93  -35.93    0.00  H2
	H2O(g)           -1.51   -0.00    1.51  H2O
	K-feldspar      -15.59  -13.50    2.09  KAlSi3O8
	K-mica           -9.98    2.72   12.70  KAl3Si3O10(OH)2
	Kaolinite        -5.28    2.15    7.43  Al2Si2O5(OH)4
	O2(g)           -11.27   71.85   83.12  O2
	Quartz           -3.05   -7.03   -3.98  SiO2
	SiO2(a)          -4.32   -7.03   -2.71  SiO2

------------------
End of simulation.
------------------

------------------------------------
Reading input data for simulation 3.
------------------------------------

	USE solution 1
	EQUILIBRIUM_PHASES 1
	    Kaolinite 0 KAlSi3O8  10
	END
-----------------------------------------
Beginning of batch-reaction calculations.
-----------------------------------------

Reaction step 1.

Using solution 1.	
Using pure phase assemblage 1.	

-------------------------------Phase assemblage--------------------------------

                                                     Moles in assemblage
	Phase               SI log IAP  log KT    Initial      Final      Delta

	Kaolinite        -0.00    7.43    7.43
		KAlSi3O8        is reactant    1.000e+001 1.000e+001-7.214e-007

-----------------------------Solution composition------------------------------

	Elements           Molality       Moles

	Al               7.214e-007  7.214e-007
	K                7.214e-007  7.214e-007
	Si               2.164e-006  2.164e-006

----------------------------Description of solution----------------------------

                                       pH  =   7.114      Charge balance
                                       pe  =  10.638      Adjusted to redox equilibrium
                        Activity of water  =   1.000
                           Ionic strength  =  8.135e-007
                       Mass of water (kg)  =  1.000e+000
                 Total alkalinity (eq/kg)  =  2.886e-006
                    Total carbon (mol/kg)  =  0.000e+000
                       Total CO2 (mol/kg)  =  0.000e+000
                      Temperature (deg C)  =  25.000
                  Electrical balance (eq)  = -1.082e-010
 Percent error, 100*(Cat-|An|)/(Cat+|An|)  =  -0.01
                               Iterations  =  10
                                  Total H  = 1.110124e+002
                                  Total O  = 5.550622e+001

----------------------------Distribution of species----------------------------

	                                           Log       Log         Log 
	Species            Molality    Activity  Molality  Activity     Gamma

	OH-              1.302e-007  1.300e-007    -6.885    -6.886    -0.000
	H+               7.707e-008  7.699e-008    -7.113    -7.114    -0.000
	H2O              5.551e+001  1.000e+000     1.744    -0.000     0.000
Al              7.214e-007
	Al(OH)4-         6.791e-007  6.783e-007    -6.168    -6.169    -0.000
	Al(OH)3          2.771e-008  2.771e-008    -7.557    -7.557     0.000
	Al(OH)2+         1.449e-008  1.448e-008    -7.839    -7.839    -0.000
	AlOH+2           1.428e-010  1.422e-010    -9.845    -9.847    -0.002
	Al+3             1.113e-012  1.102e-012   -11.954   -11.958    -0.004
H(0)            4.453e-039
	H2               2.227e-039  2.227e-039   -38.652   -38.652     0.000
K               7.214e-007
	K+               7.214e-007  7.206e-007    -6.142    -6.142    -0.000
	KOH              3.246e-014  3.246e-014   -13.489   -13.489     0.000
O(0)            1.681e-015
	O2               8.407e-016  8.407e-016   -15.075   -15.075     0.000
Si              2.164e-006
	H4SiO4           2.160e-006  2.160e-006    -5.666    -5.666     0.000
	H3SiO4-          4.141e-009  4.137e-009    -8.383    -8.383    -0.000
	H2SiO4-2         3.671e-015  3.655e-015   -14.435   -14.437    -0.002

------------------------------Saturation indices-------------------------------

	Phase               SI log IAP  log KT

	Al(OH)3(a)       -1.42    9.38   10.80  Al(OH)3
	Chalcedony       -2.11   -5.67   -3.55  SiO2
	Gibbsite          1.27    9.38    8.11  Al(OH)3
	H2(g)           -35.50  -35.50    0.00  H2
	H2O(g)           -1.51   -0.00    1.51  H2O
	K-feldspar       -8.73   -6.64    2.09  KAlSi3O8
	K-mica           -0.58   12.12   12.70  KAl3Si3O10(OH)2
	Kaolinite        -0.00    7.43    7.43  Al2Si2O5(OH)4
	O2(g)           -12.12   71.00   83.12  O2
	Quartz           -1.69   -5.67   -3.98  SiO2
	SiO2(a)          -2.95   -5.67   -2.71  SiO2

------------------
End of simulation.
------------------

------------------------------------
Reading input data for simulation 4.
------------------------------------

	USE solution 1
	EQUILIBRIUM_PHASES 1
	    K-mica    0 KAlSi3O8  10
	END
-----------------------------------------
Beginning of batch-reaction calculations.
-----------------------------------------

Reaction step 1.

Using solution 1.	
Using pure phase assemblage 1.	

-------------------------------Phase assemblage--------------------------------

                                                     Moles in assemblage
	Phase               SI log IAP  log KT    Initial      Final      Delta

	K-mica           -0.00   12.70   12.70
		KAlSi3O8        is reactant    1.000e+001 1.000e+001-8.813e-007

-----------------------------Solution composition------------------------------

	Elements           Molality       Moles

	Al               8.813e-007  8.813e-007
	K                8.813e-007  8.813e-007
	Si               2.644e-006  2.644e-006

----------------------------Description of solution----------------------------

                                       pH  =   7.130      Charge balance
                                       pe  =  10.620      Adjusted to redox equilibrium
                        Activity of water  =   1.000
                           Ionic strength  =  9.725e-007
                       Mass of water (kg)  =  1.000e+000
                 Total alkalinity (eq/kg)  =  3.525e-006
                    Total carbon (mol/kg)  =  0.000e+000
                       Total CO2 (mol/kg)  =  0.000e+000
                      Temperature (deg C)  =  25.000
                  Electrical balance (eq)  = -1.082e-010
 Percent error, 100*(Cat-|An|)/(Cat+|An|)  =  -0.01
                               Iterations  =  10
                                  Total H  = 1.110124e+002
                                  Total O  = 5.550622e+001

----------------------------Distribution of species----------------------------

	                                           Log       Log         Log 
	Species            Molality    Activity  Molality  Activity     Gamma

	OH-              1.352e-007  1.350e-007    -6.869    -6.870    -0.001
	H+               7.423e-008  7.414e-008    -7.129    -7.130    -0.001
	H2O              5.551e+001  1.000e+000     1.744    -0.000     0.000
Al              8.813e-007
	Al(OH)4-         8.319e-007  8.310e-007    -6.080    -6.080    -0.001
	Al(OH)3          3.269e-008  3.269e-008    -7.486    -7.486     0.000
	Al(OH)2+         1.647e-008  1.645e-008    -7.783    -7.784    -0.001
	AlOH+2           1.563e-010  1.556e-010    -9.806    -9.808    -0.002
	Al+3             1.174e-012  1.161e-012   -11.931   -11.935    -0.005
H(0)            4.469e-039
	H2               2.235e-039  2.235e-039   -38.651   -38.651     0.000
K               8.813e-007
	K+               8.813e-007  8.802e-007    -6.055    -6.055    -0.001
	KOH              4.117e-014  4.117e-014   -13.385   -13.385     0.000
O(0)            1.670e-015
	O2               8.349e-016  8.349e-016   -15.078   -15.078     0.000
Si              2.644e-006
	H4SiO4           2.638e-006  2.638e-006    -5.579    -5.579     0.000
	H3SiO4-          5.253e-009  5.247e-009    -8.280    -8.280    -0.001
	H2SiO4-2         4.837e-015  4.814e-015   -14.315   -14.317    -0.002

------------------------------Saturation indices-------------------------------

	Phase               SI log IAP  log KT

	Al(OH)3(a)       -1.35    9.45   10.80  Al(OH)3
	Chalcedony       -2.03   -5.58   -3.55  SiO2
	Gibbsite          1.34    9.45    8.11  Al(OH)3
	H2(g)           -35.50  -35.50    0.00  H2
	H2O(g)           -1.51   -0.00    1.51  H2O
	K-feldspar       -8.30   -6.21    2.09  KAlSi3O8
	K-mica           -0.00   12.70   12.70  KAl3Si3O10(OH)2
	Kaolinite         0.32    7.75    7.43  Al2Si2O5(OH)4
	O2(g)           -12.12   71.00   83.12  O2
	Quartz           -1.60   -5.58   -3.98  SiO2
	SiO2(a)          -2.87   -5.58   -2.71  SiO2

------------------
End of simulation.
------------------

------------------------------------
Reading input data for simulation 5.
------------------------------------

	USE solution 1
	EQUILIBRIUM_PHASES 1
	    K-feldspar 0 KAlSi3O8  10
	END
-----------------------------------------
Beginning of batch-reaction calculations.
-----------------------------------------

Reaction step 1.

Using solution 1.	
Using pure phase assemblage 1.	

-------------------------------Phase assemblage--------------------------------

                                                     Moles in assemblage
	Phase               SI log IAP  log KT    Initial      Final      Delta

	K-feldspar       -0.00    2.09    2.09
		KAlSi3O8        is reactant    1.000e+001 1.000e+001-4.012e-005

-----------------------------Solution composition------------------------------

	Elements           Molality       Moles

	Al               4.012e-005  4.012e-005
	K                4.012e-005  4.012e-005
	Si               1.204e-004  1.204e-004

----------------------------Description of solution----------------------------

                                       pH  =   7.519      Charge balance
                                       pe  =  10.230      Adjusted to redox equilibrium
                        Activity of water  =   1.000
                           Ionic strength  =  4.028e-005
                       Mass of water (kg)  =  1.000e+000
                 Total alkalinity (eq/kg)  =  1.605e-004
                    Total carbon (mol/kg)  =  0.000e+000
                       Total CO2 (mol/kg)  =  0.000e+000
                      Temperature (deg C)  =  25.000
                  Electrical balance (eq)  = -1.082e-010
 Percent error, 100*(Cat-|An|)/(Cat+|An|)  =  -0.00
                               Iterations  =  11
                                  Total H  = 1.110124e+002
                                  Total O  = 5.550654e+001

----------------------------Distribution of species----------------------------

	                                           Log       Log         Log 
	Species            Molality    Activity  Molality  Activity     Gamma

	OH-              3.329e-007  3.305e-007    -6.478    -6.481    -0.003
	H+               3.051e-008  3.029e-008    -7.515    -7.519    -0.003
	H2O              5.551e+001  1.000e+000     1.744    -0.000     0.000
Al              4.012e-005
	Al(OH)4-         3.936e-005  3.907e-005    -4.405    -4.408    -0.003
	Al(OH)3          6.279e-007  6.279e-007    -6.202    -6.202     0.000
	Al(OH)2+         1.301e-007  1.291e-007    -6.886    -6.889    -0.003
	AlOH+2           5.139e-010  4.990e-010    -9.289    -9.302    -0.013
	Al+3             1.625e-012  1.522e-012   -11.789   -11.818    -0.029
H(0)            4.496e-039
	H2               2.248e-039  2.248e-039   -38.648   -38.648     0.000
K               4.012e-005
	K+               4.012e-005  3.982e-005    -4.397    -4.400    -0.003
	KOH              4.558e-012  4.558e-012   -11.341   -11.341     0.000
O(0)            1.650e-015
	O2               8.249e-016  8.249e-016   -15.084   -15.084     0.000
Si              1.204e-004
	H4SiO4           1.198e-004  1.198e-004    -3.922    -3.922     0.000
	H3SiO4-          5.873e-007  5.830e-007    -6.231    -6.234    -0.003
	H2SiO4-2         1.348e-012  1.309e-012   -11.870   -11.883    -0.013

------------------------------Saturation indices-------------------------------

	Phase               SI log IAP  log KT

	Al(OH)3(a)       -0.06   10.74   10.80  Al(OH)3
	Chalcedony       -0.37   -3.92   -3.55  SiO2
	Gibbsite          2.63   10.74    8.11  Al(OH)3
	H2(g)           -35.50  -35.50    0.00  H2
	H2O(g)           -1.51   -0.00    1.51  H2O
	K-feldspar       -0.00    2.09    2.09  KAlSi3O8
	K-mica           10.87   23.57   12.70  KAl3Si3O10(OH)2
	Kaolinite         6.20   13.63    7.43  Al2Si2O5(OH)4
	O2(g)           -12.12   71.00   83.12  O2
	Quartz            0.06   -3.92   -3.98  SiO2
	SiO2(a)          -1.21   -3.92   -2.71  SiO2

------------------
End of simulation.
------------------

------------------------------------
Reading input data for simulation 6.
------------------------------------

-----------
End of run.
-----------