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INPUT_FC17.TXT
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TITLE: Ethane-Propane Titan model parameters
1, FREEZE(1) OR EVAPORATION(2) OR PRESSURE(3) SCENARIO ? CALLED PATH BELOW.
2, EQUILIBRIUM(1) OR FRACTIONAL(2) CRYSTALLIZATION?
0, WANT SEAWATER SALINITY(Sp) TO GOVERN THE CALCULATIONS,Y=1,N=0.
0.0, IF YES ABOVE, ENTER SEAWATER PRACTICAL SALINITY(Sp) OR 0.0.
0, WANT SEAWATER CARBONATE SUPERSATURATION TO BE CONSIDERED? Y=1,N=0.
0.00 SODIUM(M/KG).
0.00, POTASSIUM(M/KG).
0.00, CALCIUM(M/KG
0.00, MAGNESIUM(M/KG)
0.00, STRONTIUM(M/KG).
0.00, FERROUS IRON(M/KG).
0.00, FERRIC IRON (M/KG).
0.00, ALUMINUM(M/KG).
0.00, SILICA (M/KG).
3.00, AMMONIUM(M/KG).
FOR FE,AL, SI, AND ALKALINE CHEMISTRIES,DO YOU WANT ACIDITY
IGNORED(1),OR FIXED BY PH(2), OR ACIDITY(3), OR
ALKALINITY(4)? IF YES, THEN ENTER NUM. NOTE THAT OPTIONS 3
AND 4 REQUIRE A FURTHER SPECIFICATION BELOW. OPTIONS 2-4
WILL ADJUST SOLUTION-PHASE CHARGE BALANCE AS AL, FE, OR SI
REACTIONS PRODUCE ACIDITY BY ASSUMING H+ REACTS WITH ROCKS
TO RELEASE NA,K,CA,MG,OR FE(II) IONS. SOME OF THE LATTER
IONS MUST BE PRESENT AS INPUT TO SERVE AS AN ION SINK/SOURCE.
FOR NH3(AQ) + NH4(AQ) CASE, SET OPTION = 2, WITH PH = 10.0.
2, SPECIFY ABOVE ACIDITY OPTION
10.00, SPECIFY INITIAL PH.
1.00, CHLORIDE(M/KG).
0.00, BROMIDE(M/KG).
0.00, PERCHLORATE(M/KG).
1.00, SULFATE(M/KG).
0.00, NITRATE(M/KG).
0.00, CARBON ALKALINITY(EQUIVALENTS/KG).
0.00, SULFITE ALKALINITY(EQUIVALENTS/KG).
0.00, SULFIDE ACIDITY(EQUIVALENTS/KG).
0.00, ACIDITY(EQUIVALENTS/KG).
0.00, IF YOU WANT TO SPECIFY HCL(BARS), ENTER VALUE HERE.
0.00, IF YOU WANT TO SPECIFY HNO3(BARS), ENTER VALUE HERE.
0.00, IF YOU WANT TO SPECIFY H2SO4(BARS), ENTER VALUE HERE.
0.00, BORON (M/KG).
0.00, FLUORIDE(M/KG).
1.467, INITIAL TOTAL PRESSURE(BARS).
0.00, INITIAL CO2(BARS).
0.00, ENTER MOLE FRACTION OF CO2, 0=FIXED CO2, 1=PURE CO2.
0.00, INITIAL O2(BARS).
0.0829, INITIAL CH4(BARS).
0.00, ENTER MOLE FRACTION OF CH4, 0=FIXED CH4, 1=PURE CH4.
0.00, CONSIDER A MIXED CO2-CH4 GAS HYDRATE,MIX(YES=1, NO=0)?
0.00, INITIAL NH3(G)(BARS), DO NOT INCLUDE BOTH NH3 INPUTS.
10.00, INITIAL NH3(AQ)(M/KG), DO NOT INCLUDE BOTH NH3 INPUTS.
1.3825, INITIAL N2(BARS)
0.00, ENTER MOLE FRACTION OF N2, 0=FIXED N2, 1=PURE N2.
1, CONSIDER A MIXED N2-CH4 GAS HYDRATE,MIX2(YES=1, NO=0)?
0, CONSIDER A MIXED N2-C02 GAS HYDRATE,MIX3(YES=1, NO=0)?
0.000056, INITIAL C2H6(BARS)
0.00, ENTER MOLE FRACTION OF C2H6, 0=FIXED C2H6, 1=PURE C2H6.
0.000005, INITIAL C3H8(BARS)
0.00, ENTER MOLE FRACTION OF C3H8, 0=FIXED C3H8, 1=PURE C3H8.
0, CONSIDER A MIXED C2H6-C3H8 GAS HYDRATE,MIX4 (YES=1, NO=0)?
0, CONSIDER A MIXED C2H6-CH4 GAS HYDRATE,MIX5(YES=1, NO=0)?
0, CONSIDER A MIXED C3H8-CH4 GAS HYDRATE,MIX6(YES=1, NO=0)?
1, CONSIDER A MIXED C2H6-N2 GAS HYDRATE,MIX7(YES=1, NO=0)?
1, CONSIDER A MIXED C3H8-N2 GAS HYDRATE,MIX8(YES=1, NO=0)?
0, CONSIDER A MIXED C2H6-CO2 GAS HYDRATE,MIX9(YES=1, NO=0)?
0, CONSIDER A MIXED C3H8-CO2 GAS HYDRATE,MIX10(YES=1, NO=0)?
0, MOLAR TO MOLAL CONVERSION? YES=1,NO=0.
0.00 IF YES ABOVE, ENTER SALINITY(G)/LITER.
273.15, INITIAL TEMPERATURE(K).
173.15, FINAL TEMPERATURE(K), IF PATH =1, OTHERWISE, SET = 0.
5.00, TEMPERATURE DECREMENT(K), IF PATH = 1, OTHERWISE, SET = 0.
1000, INITIAL WATER(G), IF PATH = 2, OTHERWISE, SET = 1000.
0.00, FINAL WATER (G), IF PATH = 2, OTHERWISE, SET = 0.
0.00, WATER DECREMENT(K), IF PATH = 2, OTHERWISE, SET = 0.
1.467, FINAL PRESSURE(BARS), IF PATH = 3, OTHERWISE, SET = 0.
0.00, PRESSURE INCREMENT(BARS), IF PATH = 3, OTHERWISE, SET = 0.