m_comp_co2::eos Namespace Reference

Functions
double	poly_logK0 (const double c[5], double T_C)
double	co2_saturation_pressure_bar (double T_C)
bool	co2_is_liquid (double T_C, double P_bar)
int	solve_cubic_real (double b, double c, double d, double r[3])
double	rk_molar_volume (double T_C, double P_bar, bool liquid)
double	ln_phi (double T_C, double P_bar, double V, double b_k, double sum_aik)
void	spycher_pruess_solubility (double T_C, double P_bar, double, double &x_CO2, double &y_H2O)
double	co2_rich_molar_density (double T_C, double P_bar)
double	pure_water_density_gcc (double T_C)
double	brine_molar_density (double T_C, double P_bar, double x_CO2)

Variables
constexpr double	R_CM3_BAR = 83.1446
constexpr double	P0_BAR = 1.0
constexpr double	M_PER_KG_H2O = 55.508
constexpr double	A_CO2_0 = 7.54e7
constexpr double	A_CO2_1 = 4.02e4
constexpr double	A_H2O_CO2 = 7.89e7
constexpr double	B_CO2 = 27.80
constexpr double	B_H2O = 18.10
constexpr double	V_H2O = 18.5
constexpr double	V_CO2 = 32.1
constexpr double	C_F_BRINE = 4.5e-10
constexpr double	P_REF_BRINE = 1.01325e5
constexpr double	M_CO2_KG = 0.04401
constexpr double	M_H2O_KG = 0.018015
constexpr double	K0_H2O [5] = {-2.215, 3.162e-2, -1.294e-4, 4.187e-7, -7.331e-10}
constexpr double	K0_CO2_G [5] = { 1.188, 1.307e-2, -5.445e-5, 0.0, 0.0}
constexpr double	K0_CO2_L [5] = { 1.168, 1.361e-2, -5.135e-5, 0.0, 0.0}
constexpr double	TC_CO2_K = 304.1282
constexpr double	PC_CO2_BAR = 73.773
constexpr double	SW_A [4] = {-7.0602087, 1.9391218, -1.6463597, -3.2995634}

Function Documentation

brine_molar_density()

double m_comp_co2::eos::brine_molar_density ( double T_C, double P_bar, double x_CO2 )

inline

Definition at line 154 of file co2_brine_eos.h.

co2_is_liquid()

bool m_comp_co2::eos::co2_is_liquid ( double T_C, double P_bar )

inline

Definition at line 59 of file co2_brine_eos.h.

co2_rich_molar_density()

double m_comp_co2::eos::co2_rich_molar_density ( double T_C, double P_bar )

inline

Definition at line 143 of file co2_brine_eos.h.

co2_saturation_pressure_bar()

double m_comp_co2::eos::co2_saturation_pressure_bar ( double T_C )

inline

Definition at line 50 of file co2_brine_eos.h.

ln_phi()

double m_comp_co2::eos::ln_phi ( double T_C, double P_bar, double V, double b_k, double sum_aik )

inline

Definition at line 112 of file co2_brine_eos.h.

poly_logK0()

double m_comp_co2::eos::poly_logK0 ( const double c[5], double T_C )

inline

Definition at line 46 of file co2_brine_eos.h.

pure_water_density_gcc()

double m_comp_co2::eos::pure_water_density_gcc ( double T_C )

inline

Definition at line 147 of file co2_brine_eos.h.

rk_molar_volume()

double m_comp_co2::eos::rk_molar_volume ( double T_C, double P_bar, bool liquid )

inline

Definition at line 90 of file co2_brine_eos.h.

solve_cubic_real()

int m_comp_co2::eos::solve_cubic_real ( double b, double c, double d, double r[3] )

inline

Definition at line 65 of file co2_brine_eos.h.

spycher_pruess_solubility()

void m_comp_co2::eos::spycher_pruess_solubility ( double T_C, double P_bar, double , double & x_CO2, double & y_H2O )

inline

Definition at line 127 of file co2_brine_eos.h.

Variable Documentation

A_CO2_0

double m_comp_co2::eos::A_CO2_0 = 7.54e7

constexpr

Definition at line 21 of file co2_brine_eos.h.

A_CO2_1

double m_comp_co2::eos::A_CO2_1 = 4.02e4

constexpr

Definition at line 22 of file co2_brine_eos.h.

A_H2O_CO2

double m_comp_co2::eos::A_H2O_CO2 = 7.89e7

constexpr

Definition at line 23 of file co2_brine_eos.h.

B_CO2

double m_comp_co2::eos::B_CO2 = 27.80

constexpr

Definition at line 24 of file co2_brine_eos.h.

B_H2O

double m_comp_co2::eos::B_H2O = 18.10

constexpr

Definition at line 25 of file co2_brine_eos.h.

C_F_BRINE

double m_comp_co2::eos::C_F_BRINE = 4.5e-10

constexpr

Definition at line 32 of file co2_brine_eos.h.

K0_CO2_G

double m_comp_co2::eos::K0_CO2_G[5] = { 1.188, 1.307e-2, -5.445e-5, 0.0, 0.0}

constexpr

Definition at line 40 of file co2_brine_eos.h.

K0_CO2_L

double m_comp_co2::eos::K0_CO2_L[5] = { 1.168, 1.361e-2, -5.135e-5, 0.0, 0.0}

constexpr

Definition at line 41 of file co2_brine_eos.h.

K0_H2O

double m_comp_co2::eos::K0_H2O[5] = {-2.215, 3.162e-2, -1.294e-4, 4.187e-7, -7.331e-10}

constexpr

Definition at line 39 of file co2_brine_eos.h.

M_CO2_KG

double m_comp_co2::eos::M_CO2_KG = 0.04401

constexpr

Definition at line 35 of file co2_brine_eos.h.

M_H2O_KG

double m_comp_co2::eos::M_H2O_KG = 0.018015

constexpr

Definition at line 36 of file co2_brine_eos.h.

M_PER_KG_H2O

double m_comp_co2::eos::M_PER_KG_H2O = 55.508

constexpr

Definition at line 19 of file co2_brine_eos.h.

P0_BAR

double m_comp_co2::eos::P0_BAR = 1.0

constexpr

Definition at line 18 of file co2_brine_eos.h.

P_REF_BRINE

double m_comp_co2::eos::P_REF_BRINE = 1.01325e5

constexpr

Definition at line 33 of file co2_brine_eos.h.

PC_CO2_BAR

double m_comp_co2::eos::PC_CO2_BAR = 73.773

Definition at line 43 of file co2_brine_eos.h.

R_CM3_BAR

double m_comp_co2::eos::R_CM3_BAR = 83.1446

constexpr

Definition at line 17 of file co2_brine_eos.h.

SW_A

double m_comp_co2::eos::SW_A[4] = {-7.0602087, 1.9391218, -1.6463597, -3.2995634}

constexpr

Definition at line 44 of file co2_brine_eos.h.

TC_CO2_K

double m_comp_co2::eos::TC_CO2_K = 304.1282

constexpr

Definition at line 43 of file co2_brine_eos.h.

V_CO2

double m_comp_co2::eos::V_CO2 = 32.1

Definition at line 27 of file co2_brine_eos.h.

V_H2O

double m_comp_co2::eos::V_H2O = 18.5

constexpr

Definition at line 27 of file co2_brine_eos.h.