iphreeqc/ex22
David L Parkhurst f06bcb47e5 Minor changes for manual.
git-svn-id: svn://136.177.114.72/svn_GW/phreeqc3/trunk@6626 1feff8c3-07ed-0310-ac33-dd36852eb9cd
2012-06-01 22:36:20 +00:00

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TITLE Compare experimental CO2 solubilities at high CO2 pressure with
Peng-Robinson calc'ns with fixed-volume gas_phase, 25, 50, 75, 100 oC.
SOLUTION 1
GAS_PHASE 1
-fixed_volume
CO2(g) 0
H2O(g) 0
REACTION
CO2 1; 0 27*1
INCREMENTAL_REACTIONS true
USER_GRAPH 1 Example 22, CO2 solubility at high pressures, 25 - 100 oC
-plot_tsv_file co2.tsv
-axis_titles "PRESSURE, IN ATMOSPHERES" "CO2 CONCENTRATION, IN MOLES PER KILOGRAM WATER"
-axis_scale x_axis 0 500
-axis_scale y_axis 0 2
-connect_simulations false
10 graph_x PR_P("CO2(g)")
20 graph_y TOT("C(4)")
-end
USER_GRAPH 2 Example 22, P-Vm of CO2 gas, 25 - 100 oC
-headings 25.oC
-axis_titles "MOLAR VOLUME OF CO2 GAS, IN LITERS PER MOLE" "CO2 PRESSURE, IN ATMOSPHERES"
-axis_scale x_axis 0 1
-axis_scale y_axis 0 500
-connect_simulations false
10 plot_xy gas_vm, gas_p symbol = None
-end
END
USE solution 1
USE gas_phase 1
USE reaction 1
REACTION_TEMPERATURE 2
50
USER_GRAPH 2
-headings 50.oC
END
USE solution 1
USE gas_phase 1
USE reaction 1
REACTION_TEMPERATURE 3
75
USER_GRAPH 2
-headings 75.oC
END
USE solution 1
USE gas_phase 1
USE reaction 1
REACTION_TEMPERATURE 4
100
USER_GRAPH 2
-headings 100oC
END