All the experimental data required for the source terms calculations. More...

Variables
double	Pr = 101325.0
	initial/final pressure of the mixture, Pa

double	Temp0 = 297
	initial temperature, K

double	A_OH = 1965.0
	pre-exponential factor for the gelling reaction, 1/s

double	E_OH = 5.487e4
	activation energy for the gelling reaction, J/mol

double	OH_0 = 3765.0
	Initial concentration of polyol OH groups in the mixutre, mol/m3.

double	NCO_0 = 3765.0
	Initial concentration of isocianate NCO groups in the mixutre, mol/m3.

double	W_0 = -1.0
	Initial concentration of water in the mixture, mol/m3.

double	catalyst

double	polyol1_ini

double	polyol2_ini

double	amine_ini

double	isocyanate1_ini

double	isocyanate2_ini

double	isocyanate3_ini

double	A_W = 1.385e3
	pre-exponential factor for the blowing reaction, 1/s

double	E_W = 3.266e4
	activation energy for the blowing reaction, J/mol

double	RR = 8.3145
	ideal gas constant, J/mol K

double	rhoPoly = 1100.0
	density of the liquid polymer, kg/m3

double	rhoBL = 1467.0
	density of the blowing agent, kg/m3

double	DH_OH = -7.49e4
	Reaction heat for the gelling reaction, J/mol.

double	DH_W = -8.6e4
	Reaction heat for the blowing reaction, J/mol.

double	C_Poly = 1800.0

double	C_CO2 = 836.6
	CO2 specific heat, J/kg K.

double	C_BG = 593.0
	Specific heat of the physical blowing agent in gas phase, J/kg K.

double	C_BL = 870.0
	Specific heat of the physical blowing agent in liquid phase, J/kg K.

double	lambda = 2.0e5
	Latent heat of blowing agent, J/kg.

double	C_TOT
	Total specifc heat of the mixture.

int	phBL = 1
	type of physical blowing agent 1 = pentane, 2 = R-11

int	denMod
	density mode, 1 = modena, 2 = constant

int	kinMod = 2
	kinetics model, 1 = Baser, 2 = Baser with R(x) More...

bool	dilution = true
	use dilution effect

double	X_gel

double	M_CO2 = 44.0
	Molecular mass of carbon dioxide, kg/kmol.

double	M_B = 137.37
	Molecular mass of blowing agent, kg/kmol.

double	M_NCO = 615.0
	Molecular weight of NCO, kg/kmol.

double	M_air = 29.0
	Molecular weight of air, kg/kmol.

double	L0 = 0.155
	Initial weight fraction of blowing agent in the liquid, -.

double	CO2_0 = 0.0
	Initial weight fraction of CO2 in the liquid, -.

double	surfaceTension = 25e-3
	required for the computation of partial pressure

double	sig = 1e-1
	correlated to variance of initial distribution

double	init_size = 2.0e-6
	initial mean bubble diameter, m

double	NN = 0.138e12
	correlated to number of initial bubbles in m^3

double	air_g
	air weight fraction

double	abs_err = 1e-6
	absolute error

double	rel_err = 1e-6
	relative error

double	dt = 1e0
	time step, s

double	tend = 200
	end time, s

bool	realizabilityCheck = false

std::string	bubbleMode

bool	apparentViscosity

Detailed Description

All the experimental data required for the source terms calculations.

Definition in file experimentalInputs.h.

Variable Documentation

◆ kinMod

int kinMod = 2

kinetics model, 1 = Baser, 2 = Baser with R(x)

See also: http://onlinelibrary.wiley.com/doi/10.1002/pen.760340804/abstract

Definition at line 125 of file experimentalInputs.h.

Variables

Detailed Description

Variable Documentation

◆ kinMod