iphreeqc/ex22
David L Parkhurst a9d21427db Updated for manual, mostly case for axes.
git-svn-id: svn://136.177.114.72/svn_GW/phreeqc3/trunk@7125 1feff8c3-07ed-0310-ac33-dd36852eb9cd
2012-11-29 19:04:23 +00:00

59 lines
1.2 KiB
Plaintext

TITLE Example 22.--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 - 100C
-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 - 100C
-headings 25C
-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 50C
END
USE solution 1
USE gas_phase 1
USE reaction 1
REACTION_TEMPERATURE 3
75
USER_GRAPH 2
-headings 75C
END
USE solution 1
USE gas_phase 1
USE reaction 1
REACTION_TEMPERATURE 4
100
USER_GRAPH 2
-headings 100C
END