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Think fixed volume P-R gases are working correctly with

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numerical derivatives.

There is a problem with CO2_conc_PR_EQ related to gas.dat.

Am going to remove -reset false from some of the gas
problems so that testing is better.




git-svn-id: svn://136.177.114.72/svn_GW/phreeqcpp/branches/ErrorHandling@5902 1feff8c3-07ed-0310-ac33-dd36852eb9cd
This commit is contained in:
David L Parkhurst 2011-12-16 01:04:53 +00:00
parent 470bf54cd9
commit a6e74f7680
1 changed files with 11 additions and 11 deletions
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22
ex7.out
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@ -1711,7 +1711,7 @@ N2(g) -4.45 3.548e-05 0.000e+00 3.363e-05 3.363e-05
Total alkalinity (eq/kg) = 5.007e-03
Total CO2 (mol/kg) = 6.090e-03
Temperature (deg C) = 25.00
Pressure (atm) = 0.06
Pressure (atm) = 0.07
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 9
@ -1825,7 +1825,7 @@ N2(g) -4.15 7.118e-05 0.000e+00 6.746e-05 6.746e-05
Total alkalinity (eq/kg) = 5.009e-03
Total CO2 (mol/kg) = 6.109e-03
Temperature (deg C) = 25.00
Pressure (atm) = 0.06
Pressure (atm) = 0.07
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 9
@ -2167,7 +2167,7 @@ N2(g) -3.54 2.859e-04 0.000e+00 2.710e-04 2.710e-04
Total alkalinity (eq/kg) = 5.022e-03
Total CO2 (mol/kg) = 6.220e-03
Temperature (deg C) = 25.00
Pressure (atm) = 0.07
Pressure (atm) = 0.09
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 7
@ -2281,7 +2281,7 @@ N2(g) -3.24 5.723e-04 0.000e+00 5.424e-04 5.424e-04
Total alkalinity (eq/kg) = 5.039e-03
Total CO2 (mol/kg) = 6.368e-03
Temperature (deg C) = 25.00
Pressure (atm) = 0.08
Pressure (atm) = 0.09
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 7
@ -2509,7 +2509,7 @@ N2(g) -2.64 2.282e-03 0.000e+00 2.163e-03 2.163e-03
Total alkalinity (eq/kg) = 5.155e-03
Total CO2 (mol/kg) = 7.271e-03
Temperature (deg C) = 25.00
Pressure (atm) = 0.13
Pressure (atm) = 0.14
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 11
@ -2623,7 +2623,7 @@ N2(g) -2.35 4.438e-03 0.000e+00 4.206e-03 4.206e-03
Total alkalinity (eq/kg) = 5.336e-03
Total CO2 (mol/kg) = 8.450e-03
Temperature (deg C) = 25.00
Pressure (atm) = 0.20
Pressure (atm) = 0.25
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 16
@ -2737,7 +2737,7 @@ N2(g) -2.05 8.819e-03 0.000e+00 8.359e-03 8.359e-03
Total alkalinity (eq/kg) = 5.775e-03
Total CO2 (mol/kg) = 1.093e-02
Temperature (deg C) = 25.00
Pressure (atm) = 0.33
Pressure (atm) = 0.39
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 15
@ -2851,7 +2851,7 @@ N2(g) -1.76 1.753e-02 0.000e+00 1.661e-02 1.661e-02
Total alkalinity (eq/kg) = 6.754e-03
Total CO2 (mol/kg) = 1.598e-02
Temperature (deg C) = 25.00
Pressure (atm) = 0.60
Pressure (atm) = 0.61
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 10
@ -2965,10 +2965,10 @@ N2(g) -1.46 3.493e-02 0.000e+00 3.311e-02 3.311e-02
Total alkalinity (eq/kg) = 8.740e-03
Total CO2 (mol/kg) = 2.612e-02
Temperature (deg C) = 25.00
Pressure (atm) = 1.13
Electrical balance (eq) = -1.567e-10
Pressure (atm) = 1.25
Electrical balance (eq) = -1.075e-10
Percent error, 100*(Cat-|An|)/(Cat+|An|) = -0.00
Iterations = 11
Iterations = 12
Total H = 1.111261e+02
Total O = 5.561070e+01