ARXIM: tests of thermodynamic database and related calculations

cubic equations of state for gases

cubic equations of state (eos) for CO2

Redlich-Kwong, Soave, Peng-Robinson)

(
script= inn/a2_carbonate_tp.inn
SYSTEM
  TDGC 25.
  PBAR 1.013
  NA  MOLE  NA+    0.600
  CL  MOLE  CL-    0.600
  C   PK    CO2(G) 0.00
END SYSTEM
SOLVENT
  MODEL DAV_1
END SOLVENT
  
INCLUDE  dtb\elements.dtb
INCLUDE  dtb\thr_twq_gas.dtb
INCLUDE  dtb\hkf_aqu.dtb
INCLUDE  dtb\hkf_min.dtb

TP.GRID !defines the T,P grid for calculation
  TDGC INITIAL 0.0 FINAL 200.0  DELTA 5.0
  PBAR INITIAL 1.0 FINAL 1200.0 RATIO 1.2
END TP.GRID
  

extract from database file used for gases (dtb\thr_twq_gas.dtb) :

the format here is derived from that used by R. Berman or C. de Capitani
= lines beginning with & ST, &  C1, or & C2 contain the standard state properties and heat capacity function of the "ideal gas"
= lines beginning with & keyword give parameters specific to the eos model pointed by keyword

CO2(G)               C(1)O(2)                           
& ST             0.00     -393510.00       213.6770
& C1         81.61970       -710.477     972938.000
& C2         -4103.83      -0.001761
CO2(G)REDKWON        C(1)O(2)
& ST       -394342.00     -393510.01       213.6770
& REDKWON 8.051633E+07 -4.982372E+04   2.720863E+01 3.069069E-03
& C1         93.00000      -1340.900     123800.000
& C2          6336.20      -0.002876
CO2(G)SOAVE          C(1)O(2)
!-> CO2(G)SOAVE is the name to address the model in SYSTEM
& ST       -394342.00     -393510.01       213.6770
& SOAVE       304.136         73.773          0.225
! model       Tcrit°C       PcritBar       acentric
!-> SOAVE is a keyword for the eos calculation program
!-> PENGROB, REDKWON, PRSV are also keywords for the eos calculation 
& C1         93.00000      -1340.900     123800.000
& C2          6336.20      -0.002876
CO2(G)PENG           C(1)O(2)
& ST       -394342.00     -393510.01       213.6770
& PENGROB     304.136         73.773          0.225
! model       Tcrit°C       PcritBar       acentric
& C1         93.00000      -1340.900     123800.000
& C2          6336.20      -0.002876
H2O(G)PRSV           H(2)O(1)
& ST             0.00     -285830.00        69.9150
& C1        135.36930      -4816.884   -4076072.000
& C2         66876.15      -0.000452
& PRSV         647.29          220.9         0.3438    -0.06635
  

!! for detailed view,  right-click on image -> View Image !!

>density of pure CO2, Peng-Robinson EoS
>density of pure CO2, Soave EoS
a2tp_density_co2_pengrob_1
a2tp_density_co2_soave_1

fugacity coefficient of pure CO2, Peng-Robinson EoS fugacity coefficient of pure CO2, Soave EoS
a2tp_fugcoef_co2_pengrob_1 a2tp_fugcoef_co2_soave_1
same as above, detailed same as above, detailed
a2tp_fugcoef_co2_pengrob_1 a2tp_fugcoef_co2_soave_1

cubic equations of state (eos) for CH4

(Redlich-Kwong, Soave, Peng-Robinson,...)

standard state thermodynamic properties of aqeous species (HKF model) at (T,P)

Na and Cl species: NaCl°, NaOH°, HCl°

logK of association reaction Na+ + Cl- >> NaCl°
a2tp_aq_nacl_logk.png
a2tp_aq_nacl_logk_2

logK of association reaction Na+ + OH- >> NaOH°
a2tp_aq_naoh_logk.png
a2tp_aq_naoh_logk_2
logK of association reaction H+ + Cl- >> HCl°
a2tp_aq_hcl_logk.png
a2tp_aq_hcl_logk_2

carbonate species: CO2,aq - HCO3-, CO3-2

>
>>> call DTBGRID
>
SYSTEM
TDGC 25.
PBAR 1.013
NA MOLE NA+ 0.600
CL MOLE CL- 0.600
C PK CO2(G) 0.00
END SYSTEM
>
INCLUDE  dtb\elements.dtb
INCLUDE dtb\hkf_aqu.dtb

TP.GRID !defines the T,P grid for calculation
TDGC INITIAL 0.0 FINAL 200.0 DELTA 5.0
PBAR INITIAL 1.0 FINAL 1200.0 RATIO 1.2
END TP.GRID

logK of acid-base reaction H2O + CO2,aq == HCO3- + H+ pK for same reaction
a2tp_carbonate_logk1_1 a2tp_carbonate_logk1_2

logK of acid-base reaction HCO3- == CO3-2 + H+
pK for same reaction
a2tp_carbonate_logk2_1 a2tp_carbonate_logk2_2