Using solution 22. Using reaction 22. Reaction 22. 1.000e+00 moles of the following reaction have been added: Relative Reactant moles H2SO4 0.31034 Relative Element moles H 0.62069 O 1.24138 S 0.31034-----------------------------Solution composition------------------------------ Elements Molality Moles S 3.103e-01 3.103e-01----------------------------Description of solution---------------------------- pH = 0.527 Charge balance pe = 4.000 Adjusted to redox equilibrium Specific Conductance (?S/cm, 25?C) = 128016 Density (g/cm?) = 1.01619 Volume (L) = 1.01402 Activity of water = 0.989 Ionic strength (mol/kgw) = 4.495e-01 Mass of water (kg) = 1.000e+00 Total alkalinity (eq/kg) = -6.207e-01 Temperature (?C) = 25.00 Electrical balance (eq) = 1.488e-11 Percent error, 100*(Cat-|An|)/(Cat+|An|) = 0.00 Iterations = 22 Gamma iterations = 5 Osmotic coefficient = 0.90158 Density of water = 0.99704 Total H = 1.116331e+02 Total O = 5.674760e+01----------------------------Distribution of species---------------------------- MacInnes MacInnes MacInnes Log Log Log mole V Species Molality Activity Molality Activity Gamma cm?/mol H+ 3.799e-01 2.968e-01 -0.420 -0.527 -0.107 0.00 OH- 6.497e-14 3.372e-14 -13.187 -13.472 -0.285 -3.02 H2O 5.551e+01 9.889e-01 1.744 -0.005 0.000 18.07S(6) 3.103e-01 HSO4- 2.408e-01 1.757e-01 -0.618 -0.755 -0.137 40.84 SO4-2 6.958e-02 6.213e-03 -1.158 -2.207 -1.049 17.61------------------------------Saturation indices------------------------------- Phase SI** log IAP log K(298 K, 1 atm) H2O(g) -1.51 -0.00 1.50 H2O**For a gas, SI = log10(fugacity). Fugacity = pressure * phi / 1 atm. For ideal gases, phi = 1.------------------End of simulation.------------------
SELECTED_OUTPUT-file output.xls-ph true-molalities H+ END
SELECTED_OUTPUT 1-reset false-file output.tsv-pH true-molalites H+-activities H+-totals S(6)