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Viscosity #76

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14 changes: 8 additions & 6 deletions database/Amm.dat
Original file line number Diff line number Diff line change
Expand Up @@ -213,7 +213,7 @@ H2O = OH- + H+
-analytic 293.29227 0.1360833 -10576.913 -123.73158 0 -6.996455e-5
-gamma 3.5 0
-Vm -9.66 28.5 80 -22.9 1.89 0 1.09 0 0 1
-viscosity -1.02e-1 0.189 9.4e-3 -4e-5 0 3.281 -2.053 # < 5 M Li,Na,KOH
-viscosity -2.26e-2 0.106 2.184e-2 -3.2e-3 0 0.4082 -1.634 # < 5 M Li,Na,KOH
-dw 5.27e-9 478 0.8695
2 H2O = O2 + 4 H+ + 4 e-
-log_k -86.08
Expand Down Expand Up @@ -243,11 +243,13 @@ CO3-2 + 2 H+ = CO2 + H2O
-analytic 464.1965 0.09344813 -26986.16 -165.75951 2248628.9
-Vm 7.29 0.92 2.07 -1.23 -1.6 # McBride et al. 2015, JCED 60, 171
-gamma 0 0.066 # Rumpf et al. 1994, J. Sol. Chem. 23, 431
-viscosity 6.8e-3 9.03e-2 3.27e-2 0 0 0 0.18
-dw 1.92e-9 -120 # TK dependence from Cadogan et al. 2014, , JCED 59, 519
2 CO2 = (CO2)2 # activity correction for CO2 solubility at high P, T
-log_k -1.8
-analytical_expression 8.68 -0.0103 -2190
-Vm 14.58 1.84 4.14 -2.46 -3.2
-viscosity 1.36e-2 0.1806 3.27e-2 0 0 0 0.36
-dw 1.92e-9 -120 # TK dependence from Cadogan et al. 2014, , JCED 59, 519
CO3-2 + 10 H+ + 8 e- = CH4 + 3 H2O
-log_k 41.071
Expand Down Expand Up @@ -446,8 +448,8 @@ Mg+2 + F- = MgF+
-delta_h 3.2 kcal
-gamma 4.5 0
-Vm .6494 -6.1958 8.1852 -2.5229 .9706 4.5 # supcrt
Na+ + OH- = NaOH
-log_k -10 # remove this complex
# Na+ + OH- = NaOH
# -log_k -14.7 # remove this complex
Na+ + HCO3- = NaHCO3
-log_k -0.06; -delta_h 21 kJ
-gamma 0 0.2
Expand Down Expand Up @@ -1938,15 +1940,15 @@ END
# For details, consult ref. 1.
# =============================================================================================
# The viscosity is calculated with a (modified) Jones-Dole equation:
# viscos / viscos_0 = 1 + A Sum(0.5 z_i m_i) + fan (B_i m_i + D_i m_i n_i)
# viscos / viscos_0 = 1 + A * Sum(0.5 z_i m_i) + fan * Sum(B_i m_i + D_i m_i n_i)
# Parameters are for calculating the B and D terms:
# -viscosity 9.35e-2 -8.31e-2 2.487e-2 4.49e-4 2.01e-2 1.570 0
# # b0 b1 b2 d1 d2 d3 tan
# z_i is absolute charge number, m_i is molality of i
# B_i = b0 + b1 exp(-b2 * tc)
# fan = (2 - tan V_i / V_Cl-), corrects for the volume of anions
# D_i = d1 + exp(-d2 tc)
# n_i = ((1 + fI)^d3 + ((z_i^2 + z_i) / 2 � m_i)d^3 / (2 + fI), fI is an ionic strength term.
# D_i = d1 * exp(-d2 tc)
# n_i = (I^d3 * (1 + fI) + ((z_i^2 + z_i) / 2 � m_i)^d3) / (2 + fI), fI is an ionic strength term.
# For details, consult ref. 4.
#
# ref. 1: Appelo, Parkhurst and Post, 2014. Geochim. Cosmochim. Acta 125, 49�67.
Expand Down
14 changes: 8 additions & 6 deletions database/phreeqc.dat
Original file line number Diff line number Diff line change
Expand Up @@ -213,7 +213,7 @@ H2O = OH- + H+
-analytic 293.29227 0.1360833 -10576.913 -123.73158 0 -6.996455e-5
-gamma 3.5 0
-Vm -9.66 28.5 80 -22.9 1.89 0 1.09 0 0 1
-viscosity -1.02e-1 0.189 9.4e-3 -4e-5 0 3.281 -2.053 # < 5 M Li,Na,KOH
-viscosity -2.26e-2 0.106 2.184e-2 -3.2e-3 0 0.4082 -1.634 # < 5 M Li,Na,KOH
-dw 5.27e-9 478 0.8695
2 H2O = O2 + 4 H+ + 4 e-
-log_k -86.08
Expand Down Expand Up @@ -243,11 +243,13 @@ CO3-2 + 2 H+ = CO2 + H2O
-analytic 464.1965 0.09344813 -26986.16 -165.75951 2248628.9
-Vm 7.29 0.92 2.07 -1.23 -1.6 # McBride et al. 2015, JCED 60, 171
-gamma 0 0.066 # Rumpf et al. 1994, J. Sol. Chem. 23, 431
-viscosity 6.8e-3 9.03e-2 3.27e-2 0 0 0 0.18
-dw 1.92e-9 -120 # TK dependence from Cadogan et al. 2014, , JCED 59, 519
2 CO2 = (CO2)2 # activity correction for CO2 solubility at high P, T
-log_k -1.8
-analytical_expression 8.68 -0.0103 -2190
-Vm 14.58 1.84 4.14 -2.46 -3.2
-viscosity 1.36e-2 0.1806 3.27e-2 0 0 0 0.36
-dw 1.92e-9 -120 # TK dependence from Cadogan et al. 2014, , JCED 59, 519
CO3-2 + 10 H+ + 8 e- = CH4 + 3 H2O
-log_k 41.071
Expand Down Expand Up @@ -446,8 +448,8 @@ Mg+2 + F- = MgF+
-delta_h 3.2 kcal
-gamma 4.5 0
-Vm .6494 -6.1958 8.1852 -2.5229 .9706 4.5 # supcrt
Na+ + OH- = NaOH
-log_k -10 # remove this complex
# Na+ + OH- = NaOH
# -log_k -14.7 # remove this complex
Na+ + HCO3- = NaHCO3
-log_k -0.06; -delta_h 21 kJ
-gamma 0 0.2
Expand Down Expand Up @@ -1938,15 +1940,15 @@ END
# For details, consult ref. 1.
# =============================================================================================
# The viscosity is calculated with a (modified) Jones-Dole equation:
# viscos / viscos_0 = 1 + A Sum(0.5 z_i m_i) + fan (B_i m_i + D_i m_i n_i)
# viscos / viscos_0 = 1 + A * Sum(0.5 z_i m_i) + fan * Sum(B_i m_i + D_i m_i n_i)
# Parameters are for calculating the B and D terms:
# -viscosity 9.35e-2 -8.31e-2 2.487e-2 4.49e-4 2.01e-2 1.570 0
# # b0 b1 b2 d1 d2 d3 tan
# z_i is absolute charge number, m_i is molality of i
# B_i = b0 + b1 exp(-b2 * tc)
# fan = (2 - tan V_i / V_Cl-), corrects for the volume of anions
# D_i = d1 + exp(-d2 tc)
# n_i = ((1 + fI)^d3 + ((z_i^2 + z_i) / 2 � m_i)d^3 / (2 + fI), fI is an ionic strength term.
# D_i = d1 * exp(-d2 tc)
# n_i = (I^d3 * (1 + fI) + ((z_i^2 + z_i) / 2 � m_i)^d3) / (2 + fI), fI is an ionic strength term.
# For details, consult ref. 4.
#
# ref. 1: Appelo, Parkhurst and Post, 2014. Geochim. Cosmochim. Acta 125, 49�67.
Expand Down
14 changes: 8 additions & 6 deletions database/phreeqc_rates.dat
Original file line number Diff line number Diff line change
Expand Up @@ -213,7 +213,7 @@ H2O = OH- + H+
-analytic 293.29227 0.1360833 -10576.913 -123.73158 0 -6.996455e-5
-gamma 3.5 0
-Vm -9.66 28.5 80 -22.9 1.89 0 1.09 0 0 1
-viscosity -1.02e-1 0.189 9.4e-3 -4e-5 0 3.281 -2.053 # < 5 M Li,Na,KOH
-viscosity -2.26e-2 0.106 2.184e-2 -3.2e-3 0 0.4082 -1.634 # < 5 M Li,Na,KOH
-dw 5.27e-9 478 0.8695
2 H2O = O2 + 4 H+ + 4 e-
-log_k -86.08
Expand Down Expand Up @@ -243,11 +243,13 @@ CO3-2 + 2 H+ = CO2 + H2O
-analytic 464.1965 0.09344813 -26986.16 -165.75951 2248628.9
-Vm 7.29 0.92 2.07 -1.23 -1.6 # McBride et al. 2015, JCED 60, 171
-gamma 0 0.066 # Rumpf et al. 1994, J. Sol. Chem. 23, 431
-viscosity 6.8e-3 9.03e-2 3.27e-2 0 0 0 0.18
-dw 1.92e-9 -120 # TK dependence from Cadogan et al. 2014, , JCED 59, 519
2 CO2 = (CO2)2 # activity correction for CO2 solubility at high P, T
-log_k -1.8
-analytical_expression 8.68 -0.0103 -2190
-Vm 14.58 1.84 4.14 -2.46 -3.2
-viscosity 1.36e-2 0.1806 3.27e-2 0 0 0 0.36
-dw 1.92e-9 -120 # TK dependence from Cadogan et al. 2014, , JCED 59, 519
CO3-2 + 10 H+ + 8 e- = CH4 + 3 H2O
-log_k 41.071
Expand Down Expand Up @@ -446,8 +448,8 @@ Mg+2 + F- = MgF+
-delta_h 3.2 kcal
-gamma 4.5 0
-Vm .6494 -6.1958 8.1852 -2.5229 .9706 4.5 # supcrt
Na+ + OH- = NaOH
-log_k -10 # remove this complex
# Na+ + OH- = NaOH
# -log_k -14.7 # remove this complex
Na+ + HCO3- = NaHCO3
-log_k -0.06; -delta_h 21 kJ
-gamma 0 0.2
Expand Down Expand Up @@ -3128,15 +3130,15 @@ Wollastonite -6.97 700 56 0.4 0 0
# For details, consult ref. 1.
# =============================================================================================
# The viscosity is calculated with a (modified) Jones-Dole equation:
# viscos / viscos_0 = 1 + A Sum(0.5 z_i m_i) + fan (B_i m_i + D_i m_i n_i)
# viscos / viscos_0 = 1 + A * Sum(0.5 z_i m_i) + fan * Sum(B_i m_i + D_i m_i n_i)
# Parameters are for calculating the B and D terms:
# -viscosity 9.35e-2 -8.31e-2 2.487e-2 4.49e-4 2.01e-2 1.570 0
# # b0 b1 b2 d1 d2 d3 tan
# z_i is absolute charge number, m_i is molality of i
# B_i = b0 + b1 exp(-b2 * tc)
# fan = (2 - tan V_i / V_Cl-), corrects for the volume of anions
# D_i = d1 + exp(-d2 tc)
# n_i = ((1 + fI)^d3 + ((z_i^2 + z_i) / 2 � m_i)d^3 / (2 + fI), fI is an ionic strength term.
# D_i = d1 * exp(-d2 tc)
# n_i = (I^d3 * (1 + fI) + ((z_i^2 + z_i) / 2 � m_i)^d3) / (2 + fI), fI is an ionic strength term.
# For details, consult ref. 4.
#
# ref. 1: Appelo, Parkhurst and Post, 2014. Geochim. Cosmochim. Acta 125, 49�67.
Expand Down
11 changes: 6 additions & 5 deletions database/pitzer.dat
Original file line number Diff line number Diff line change
Expand Up @@ -132,7 +132,7 @@ H2Sg = H2Sg # H2S
H2O = OH- + H+
-analytic 293.29227 0.1360833 -10576.913 -123.73158 0 -6.996455e-5
-Vm -9.66 28.5 80 -22.9 1.89 0 1.09 0 0 1
-viscosity -5.45e-2 0.142 1.45e-2 -3e-5 0 3.231 -1.791 # < 5 M Li,Na,KOH
-viscosity -2.26e-2 0.106 2.184e-2 -3.2e-3 0 0.4082 -1.634 # < 5 M Li,Na,KOH
-dw 5.27e-9 491 1.851 0 0.3256
CO3-2 + H+ = HCO3-
log_k 10.3393; delta_h -3.561 kcal
Expand All @@ -145,6 +145,7 @@ CO3-2 + 2 H+ = CO2 + H2O
delta_h -5.738 kcal
-analytic 464.1965 0.09344813 -26986.16 -165.75951 2248628.9
-Vm 7.29 0.92 2.07 -1.23 -1.6 # McBride et al. 2015, JCED 60, 171
-viscosity 1.15e-2 9.82e-2 3.59e-2 0 0 0 0.266
-dw 1.92e-9 -120 # TK dependence from Cadogan et al. 2014, , JCED 59, 519
SO4-2 + H+ = HSO4-
-log_k 1.988; -delta_h 3.85 kcal
Expand Down Expand Up @@ -1011,15 +1012,15 @@ END
# For details, consult ref. 1.
# =============================================================================================
# The viscosity is calculated with a (modified) Jones-Dole equation:
# viscos / viscos_0 = 1 + A Sum(0.5 z_i m_i) + fan (B_i m_i + D_i m_i n_i)
# viscos / viscos_0 = 1 + A * Sum(0.5 z_i m_i) + fan * Sum(B_i m_i + D_i m_i n_i)
# Parameters are for calculating the B and D terms:
# -viscosity 9.35e-2 -8.31e-2 2.487e-2 4.49e-4 2.01e-2 1.570 0
# # b0 b1 b2 d1 d2 d3 tan
# # b0 b1 b2 d1 d2 d3 tan
# z_i is absolute charge number, m_i is molality of i
# B_i = b0 + b1 exp(-b2 * tc)
# fan = (2 - tan V_i / V_Cl-), corrects for the volume of anions
# D_i = d1 + exp(-d2 tc)
# n_i = ((1 + fI)^d3 + ((z_i^2 + z_i) / 2 � m_i)d^3 / (2 + fI), fI is an ionic strength term.
# D_i = d1 * exp(-d2 tc)
# n_i = (I^d3 * (1 + fI) + ((z_i^2 + z_i) / 2 � m_i)^d3) / (2 + fI), fI is an ionic strength term.
# For details, consult ref. 5.
#
# ref. 1: Appelo, Parkhurst and Post, 2014. Geochim. Cosmochim. Acta 125, 49�67.
Expand Down
3 changes: 1 addition & 2 deletions examples/ex1.out
Original file line number Diff line number Diff line change
Expand Up @@ -124,7 +124,7 @@ Initial solution 1. SEAWATER FROM NORDSTROM AND OTHERS (1979)
Specific Conductance (µS/cm, 25°C) = 52856
Density (g/cm³) = 1.02328
Volume (L) = 1.01278
Viscosity (mPa s) = 0.96029
Viscosity (mPa s) = 0.96030
Activity of water = 0.981
Ionic strength (mol/kgw) = 6.704e-01
Mass of water (kg) = 1.000e+00
Expand Down Expand Up @@ -248,7 +248,6 @@ Na 4.854e-01
Na+ 4.712e-01 3.381e-01 -0.327 -0.471 -0.144 -0.51
NaSO4- 1.396e-02 9.473e-03 -1.855 -2.024 -0.168 8.22
NaHCO3 2.252e-04 3.066e-04 -3.647 -3.513 0.134 31.73
NaOH 4.773e-17 5.570e-17 -16.321 -16.254 0.067 (0)
O(0) 4.381e-04
O2 2.190e-04 2.556e-04 -3.659 -3.592 0.067 30.40
S(6) 2.926e-02
Expand Down
6 changes: 3 additions & 3 deletions examples/ex10.out
Original file line number Diff line number Diff line change
Expand Up @@ -123,7 +123,7 @@ Initial solution 1.
Specific Conductance (µS/cm, 25°C) = 701
Density (g/cm³) = 0.99755
Volume (L) = 1.00310
Viscosity (mPa s) = 0.89435
Viscosity (mPa s) = 0.89463
Activity of water = 1.000
Ionic strength (mol/kgw) = 1.134e-02
Mass of water (kg) = 1.000e+00
Expand Down Expand Up @@ -206,10 +206,10 @@ CO2(g) -0.01 -1.48 -1.47 1.000e+01 9.961e+00 -3.875e-02

pH = 6.058 Charge balance
pe = 11.902 Adjusted to redox equilibrium
Specific Conductance (µS/cm, 25°C) = 1708
Specific Conductance (µS/cm, 25°C) = 1684
Density (g/cm³) = 0.99860
Volume (L) = 1.00434
Viscosity (mPa s) = 0.89962
Viscosity (mPa s) = 0.92188
Activity of water = 0.999
Ionic strength (mol/kgw) = 2.900e-02
Mass of water (kg) = 9.999e-01
Expand Down
3 changes: 1 addition & 2 deletions examples/ex11.out
Original file line number Diff line number Diff line change
Expand Up @@ -126,7 +126,7 @@ Initial solution 1. Initial solution for column
Activity of water = 1.000
Ionic strength (mol/kgw) = 1.200e-03
Mass of water (kg) = 1.000e+00
Total alkalinity (eq/kg) = -1.017e-18
Total alkalinity (eq/kg) = -1.027e-18
Temperature (°C) = 25.00
Electrical balance (eq) = -9.088e-17
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Expand All @@ -150,7 +150,6 @@ N(5) 1.200e-03
NO3- 1.200e-03 1.154e-03 -2.921 -2.938 -0.017 29.49
Na 1.000e-03
Na+ 1.000e-03 9.621e-04 -3.000 -3.017 -0.017 -1.47
NaOH 9.666e-21 9.668e-21 -20.015 -20.015 0.000 (0)
O(0) 5.351e-04
O2 2.676e-04 2.676e-04 -3.573 -3.572 0.000 30.40

Expand Down
38 changes: 19 additions & 19 deletions examples/ex11trn.sel
Original file line number Diff line number Diff line change
Expand Up @@ -57,27 +57,27 @@
55 8.344533301406e-04 1.131625845338e-03 3.655466698441e-04 0.000000000000e+00 1.387500000000e+00
56 7.847919650475e-04 1.142020362045e-03 4.152080349369e-04 0.000000000000e+00 1.412500000000e+00
57 7.284538372959e-04 1.150973656035e-03 4.715461626881e-04 3.531139650212e-28 1.437500000000e+00
58 6.674661295231e-04 1.158656441394e-03 5.325338704605e-04 4.216133178351e-26 1.462500000000e+00
58 6.674661295231e-04 1.158656441394e-03 5.325338704605e-04 4.216133178352e-26 1.462500000000e+00
59 6.042301758578e-04 1.165225432017e-03 5.957698241254e-04 2.112623929847e-24 1.487500000000e+00
60 5.410707042902e-04 1.170823053923e-03 6.589292956926e-04 9.154192241146e-23 1.512500000000e+00
60 5.410707042902e-04 1.170823053923e-03 6.589292956926e-04 9.154192241147e-23 1.512500000000e+00
61 4.799177066706e-04 1.175577598779e-03 7.200822933118e-04 3.514353871101e-21 1.537500000000e+00
62 4.221746364521e-04 1.179603706071e-03 7.778253635299e-04 1.207213754641e-19 1.562500000000e+00
63 3.687296865690e-04 1.183003078326e-03 8.312703134126e-04 3.694071268300e-18 1.587500000000e+00
64 3.200378094467e-04 1.185865350144e-03 8.799621905343e-04 1.035721724513e-16 1.612500000000e+00
65 2.762284431584e-04 1.188269047043e-03 9.237715568171e-04 2.657316487699e-15 1.637500000000e+00
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70 1.223834694923e-04 1.195504582884e-03 1.077593516927e-03 1.150677988346e-08 1.762500000000e+00
71 1.019262303182e-04 1.196307568531e-03 1.097657241059e-03 2.082643005568e-07 1.787500000000e+00
72 8.381480436917e-05 1.196971656899e-03 1.109525476375e-03 3.329859617448e-06 1.812500000000e+00
73 6.668225222783e-05 1.197519877322e-03 1.024937206784e-03 5.419027048446e-05 1.837500000000e+00
74 5.053198367604e-05 1.197971659937e-03 7.350507107061e-04 2.072086528030e-04 1.862500000000e+00
75 3.879701357395e-05 1.198343349753e-03 5.356918142768e-04 3.127555860708e-04 1.887500000000e+00
75 3.879701357395e-05 1.198343349753e-03 5.356918142767e-04 3.127555860708e-04 1.887500000000e+00
76 3.007678322722e-05 1.198648658204e-03 4.021188008094e-04 3.839022079790e-04 1.912500000000e+00
77 2.344463549483e-05 1.198899057198e-03 3.068522371412e-04 4.348515636801e-04 1.937500000000e+00
78 1.834047972307e-05 1.199104120993e-03 2.366187847945e-04 4.725203677398e-04 1.962500000000e+00
77 2.344463549483e-05 1.198899057198e-03 3.068522371411e-04 4.348515636801e-04 1.937500000000e+00
78 1.834047972307e-05 1.199104120993e-03 2.366187847944e-04 4.725203677398e-04 1.962500000000e+00
79 1.438416333582e-05 1.199271821253e-03 1.838015689086e-04 5.009071338768e-04 1.987500000000e+00
80 1.130287552755e-05 1.199408780437e-03 1.435541337153e-04 5.225714953778e-04 2.012500000000e+00
81 8.894854154099e-06 1.199520488471e-03 1.125953626079e-04 5.392548916185e-04 2.037500000000e+00
Expand All @@ -86,13 +86,13 @@
84 4.362237388672e-06 1.199745698858e-03 5.532050326743e-05 5.701586296717e-04 2.112500000000e+00
85 3.445231625616e-06 1.199794545990e-03 4.384740222256e-05 5.763536830758e-04 2.137500000000e+00
86 2.722483623513e-06 1.199834157394e-03 3.481279241283e-05 5.812323619826e-04 2.162500000000e+00
87 2.152343734153e-06 1.199866246232e-03 2.768046312193e-05 5.850835965725e-04 2.187500000000e+00
87 2.152343734153e-06 1.199866246232e-03 2.768046312192e-05 5.850835965725e-04 2.187500000000e+00
88 1.702259902002e-06 1.199892215323e-03 2.203774543638e-05 5.881299973317e-04 2.212500000000e+00
89 1.346733078607e-06 1.199913211686e-03 1.756522033724e-05 5.905440232928e-04 2.237500000000e+00
90 1.065752199293e-06 1.199930171882e-03 1.401446577327e-05 5.924598910143e-04 2.262500000000e+00
91 8.435890597776e-07 1.199943859609e-03 1.119149963194e-05 5.939824556550e-04 2.287500000000e+00
92 6.678659094764e-07 1.199954896813e-03 8.944331673377e-06 5.951939012093e-04 2.312500000000e+00
93 5.288312745990e-07 1.199963789378e-03 7.153523668295e-06 5.961588225292e-04 2.337500000000e+00
92 6.678659094763e-07 1.199954896813e-03 8.944331673377e-06 5.951939012093e-04 2.312500000000e+00
93 5.288312745990e-07 1.199963789378e-03 7.153523668294e-06 5.961588225292e-04 2.337500000000e+00
94 4.187957414427e-07 1.199970948301e-03 5.724978921457e-06 5.969281126691e-04 2.362500000000e+00
95 3.316912256408e-07 1.199976707113e-03 4.584400974714e-06 5.975419539002e-04 2.387500000000e+00
96 2.627259549757e-07 1.199981336185e-03 3.673012861562e-06 5.980321305921e-04 2.412500000000e+00
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