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The median composition of the Askola groundwater is given in table 1:
Table 1. Median composition of the Askola ground water (GTK 2008)
|
mg/L
|
HCO3-
|
128
|
SIO2
|
11.7
|
Na+
|
34.05
|
K+
|
2.36
|
Ca2+
|
14.05
|
Mg2+
|
6.33
|
Sr2+
|
0.13
|
B3+
|
0.05
|
SO42-
|
17.85
|
Cl-
|
25.6
|
F-
|
0.38
|
Br-
|
0.02
|
I-
|
0.02
|
The pH of the water is 7.7, temperature 10 centigrade and the uranium concentration 340 μg/l. In oxic conditions the Eh of the water is 500 mV and the density of water 1.0 kg/l.
where R is the gas constant, T temperature and F the Faraday constant
R = 8.3145 J K
-1 mol
-1 F = 96485.3 C/mol
Modify the given .phrg input file (below) based on data given above and do the following exercises using PHREEQC:
1. Calculate the prevailing uranium species at pH range 2-12 using llnl.dat database. Create a "selected output" file with most relevant prevailing uranium species. Open your .txt file with excel or another relevant program and produce a figure of uranium species as a function of pH. What uranium species are most prevailing in oxic conditions? Save your output file as a text file for the next exercise.
2. Open your output file, and from ”Saturation indices” block look at the SI-values. Write in your input file a command line for the SI values of the most relevant solid uranium phases and produce a figure representing the SI values as a function of pH.
3. If we assume that a uranium-bearing groundwater attains equilibrium with a strongly reducing mineral, such as FeS, how will pH, pe, uranium species and SI values of solid uranium phases change?
Input file for modification based on given data:
SOLUTION 1 Speciation exercise #use llnl-database
#write the correct values, calculate pe based on Eh:
-temp
-pH
-pe
-units
- write the water composition here:
SAVE SOLUTION 1
END
USE SOLUTION 1
#SELECTED_OUTPUT
#-RESET false
#-file #here the name of the file
#-PH
#-TOTALS #here the oxidation states of uranium
#-molalities #here the species of interest
#-SATURATION_INDICES #here satiration indices
PHASES
Fix_H+
H+ = H+
log_k 0.0
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -2.0 HCl 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -3 HCl 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -4 HCl 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -5 HCl 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -6 HCl 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -7 HCl 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -8 NaOH 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -9 NaOH 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -10 NaOH 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -11 NaOH 10.0
END
USE solution 1
EQUILIBRIUM_PHASES 1
Fix_H+ -12 NaOH 10.0
END