Cantera
2.2.1
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Class GasTransport implements some functions and properties that are shared by the MixTransport and MultiTransport classes. More...
#include <GasTransport.h>
Public Member Functions | |
GasTransport (const GasTransport &right) | |
GasTransport & | operator= (const GasTransport &right) |
virtual doublereal | viscosity () |
Viscosity of the mixture (kg /m /s) More... | |
virtual void | getSpeciesViscosities (doublereal *const visc) |
Get the pure-species viscosities. More... | |
virtual void | getBinaryDiffCoeffs (const size_t ld, doublereal *const d) |
Returns the matrix of binary diffusion coefficients. More... | |
virtual void | getMixDiffCoeffs (doublereal *const d) |
Returns the Mixture-averaged diffusion coefficients [m^2/s]. More... | |
virtual void | getMixDiffCoeffsMole (doublereal *const d) |
Returns the mixture-averaged diffusion coefficients [m^2/s]. More... | |
virtual void | getMixDiffCoeffsMass (doublereal *const d) |
Returns the mixture-averaged diffusion coefficients [m^2/s]. More... | |
virtual void | init (thermo_t *thermo, int mode=0, int log_level=0) |
Initialize a transport manager. More... | |
Public Member Functions inherited from Transport | |
Transport (thermo_t *thermo=0, size_t ndim=1) | |
Constructor. More... | |
Transport (const Transport &right) | |
Transport & | operator= (const Transport &right) |
virtual Transport * | duplMyselfAsTransport () const |
Duplication routine for objects which inherit from Transport. More... | |
virtual int | model () const |
Transport model. More... | |
thermo_t & | thermo () |
bool | ready () |
void | setNDim (const int ndim) |
Set the number of dimensions to be expected in flux expressions. More... | |
size_t | nDim () const |
Return the number of dimensions in flux expressions. More... | |
void | checkSpeciesIndex (size_t k) const |
Check that the specified species index is in range Throws an exception if k is greater than nSpecies() More... | |
void | checkSpeciesArraySize (size_t kk) const |
Check that an array size is at least nSpecies() Throws an exception if kk is less than nSpecies(). More... | |
virtual doublereal | getElectricConduct () |
Compute the mixture electrical conductivity (S m-1) at the current conditions of the phase (Siemens m-1) More... | |
virtual void | getElectricCurrent (int ndim, const doublereal *grad_T, int ldx, const doublereal *grad_X, int ldf, const doublereal *grad_V, doublereal *current) |
Compute the electric current density in A/m^2. More... | |
virtual void | getSpeciesFluxes (size_t ndim, const doublereal *const grad_T, size_t ldx, const doublereal *const grad_X, size_t ldf, doublereal *const fluxes) |
Get the species diffusive mass fluxes wrt to the specified solution averaged velocity, given the gradients in mole fraction and temperature. More... | |
virtual void | getSpeciesFluxesES (size_t ndim, const doublereal *grad_T, size_t ldx, const doublereal *grad_X, size_t ldf, const doublereal *grad_Phi, doublereal *fluxes) |
Get the species diffusive mass fluxes wrt to the mass averaged velocity, given the gradients in mole fraction, temperature and electrostatic potential. More... | |
virtual void | getSpeciesVdiff (size_t ndim, const doublereal *grad_T, int ldx, const doublereal *grad_X, int ldf, doublereal *Vdiff) |
Get the species diffusive velocities wrt to the mass averaged velocity, given the gradients in mole fraction and temperature. More... | |
virtual void | getSpeciesVdiffES (size_t ndim, const doublereal *grad_T, int ldx, const doublereal *grad_X, int ldf, const doublereal *grad_Phi, doublereal *Vdiff) |
Get the species diffusive velocities wrt to the mass averaged velocity, given the gradients in mole fraction, temperature, and electrostatic potential. More... | |
virtual void | getMolarFluxes (const doublereal *const state1, const doublereal *const state2, const doublereal delta, doublereal *const cfluxes) |
Get the molar fluxes [kmol/m^2/s], given the thermodynamic state at two nearby points. More... | |
virtual void | getMassFluxes (const doublereal *state1, const doublereal *state2, doublereal delta, doublereal *mfluxes) |
Get the mass fluxes [kg/m^2/s], given the thermodynamic state at two nearby points. More... | |
virtual void | getThermalDiffCoeffs (doublereal *const dt) |
Return a vector of Thermal diffusion coefficients [kg/m/sec]. More... | |
virtual void | getMultiDiffCoeffs (const size_t ld, doublereal *const d) |
Return the Multicomponent diffusion coefficients. Units: [m^2/s]. More... | |
virtual void | setParameters (const int type, const int k, const doublereal *const p) |
Set model parameters for derived classes. More... | |
void | setVelocityBasis (VelocityBasis ivb) |
Sets the velocity basis. More... | |
VelocityBasis | getVelocityBasis () const |
Gets the velocity basis. More... | |
virtual doublereal | bulkViscosity () |
The bulk viscosity in Pa-s. More... | |
virtual doublereal | ionConductivity () |
The ionic conductivity in 1/ohm/m. More... | |
virtual void | getSpeciesIonConductivity (doublereal *const ionCond) |
Returns the pure species ionic conductivity. More... | |
virtual void | mobilityRatio (double *mobRat) |
Returns the pointer to the mobility ratios of the species in the phase. More... | |
virtual void | getSpeciesMobilityRatio (double **mobRat) |
Returns the pure species limit of the mobility ratios. More... | |
virtual void | selfDiffusion (doublereal *const selfDiff) |
Returns the self diffusion coefficients of the species in the phase. More... | |
virtual void | getSpeciesSelfDiffusion (double **selfDiff) |
Returns the pure species self diffusion in solution of each species. More... | |
virtual doublereal | thermalConductivity () |
Returns the mixture thermal conductivity in W/m/K. More... | |
virtual doublereal | electricalConductivity () |
virtual void | getMobilities (doublereal *const mobil_e) |
Get the Electrical mobilities (m^2/V/s). More... | |
virtual void | getFluidMobilities (doublereal *const mobil_f) |
Get the fluid mobilities (s kmol/kg). More... | |
virtual bool | initLiquid (LiquidTransportParams &tr) |
Called by TransportFactory to set parameters. More... | |
virtual bool | initSolid (SolidTransportData &tr) |
Called by TransportFactory to set parameters. More... | |
virtual void | setThermo (thermo_t &thermo) |
Specifies the ThermoPhase object. More... | |
Protected Member Functions | |
GasTransport (ThermoPhase *thermo=0) | |
virtual void | update_T () |
virtual void | update_C ()=0 |
virtual void | updateViscosity_T () |
Update the temperature-dependent viscosity terms. More... | |
virtual void | updateSpeciesViscosities () |
Update the pure-species viscosities. More... | |
virtual void | updateDiff_T () |
Update the binary diffusion coefficients. More... | |
Initialization | |
void | setupMM () |
Prepare to build a new kinetic-theory-based transport manager for low-density gases. More... | |
void | getTransportData () |
Read the transport database. More... | |
void | makePolarCorrections (size_t i, size_t j, doublereal &f_eps, doublereal &f_sigma) |
Corrections for polar-nonpolar binary diffusion coefficients. More... | |
void | fitCollisionIntegrals (MMCollisionInt &integrals) |
Generate polynomial fits to collision integrals. More... | |
void | fitProperties (MMCollisionInt &integrals) |
Generate polynomial fits to the viscosity, conductivity, and the binary diffusion coefficients. More... | |
void | getBinDiffCorrection (doublereal t, MMCollisionInt &integrals, size_t k, size_t j, doublereal xk, doublereal xj, doublereal &fkj, doublereal &fjk) |
Second-order correction to the binary diffusion coefficients. More... | |
Protected Member Functions inherited from Transport | |
void | finalize () |
Enable the transport object for use. More... | |
Protected Attributes | |
vector_fp | m_molefracs |
Vector of species mole fractions. More... | |
doublereal | m_viscmix |
Internal storage for the viscosity of the mixture (kg /m /s) More... | |
bool | m_visc_ok |
Update boolean for mixture rule for the mixture viscosity. More... | |
bool | m_viscwt_ok |
Update boolean for the weighting factors for the mixture viscosity. More... | |
bool | m_spvisc_ok |
Update boolean for the species viscosities. More... | |
bool | m_bindiff_ok |
Update boolean for the binary diffusivities at unit pressure. More... | |
int | m_mode |
Type of the polynomial fits to temperature. More... | |
DenseMatrix | m_phi |
m_phi is a Viscosity Weighting Function. size = m_nsp * n_nsp More... | |
vector_fp | m_spwork |
work space length = m_kk More... | |
vector_fp | m_visc |
vector of species viscosities (kg /m /s). More... | |
std::vector< vector_fp > | m_visccoeffs |
Polynomial fits to the viscosity of each species. More... | |
vector_fp | m_mw |
Local copy of the species molecular weights. More... | |
DenseMatrix | m_wratjk |
Holds square roots of molecular weight ratios. More... | |
DenseMatrix | m_wratkj1 |
Holds square roots of molecular weight ratios. More... | |
vector_fp | m_sqvisc |
vector of square root of species viscosities sqrt(kg /m /s). More... | |
vector_fp | m_polytempvec |
Powers of the ln temperature, up to fourth order. More... | |
doublereal | m_temp |
Current value of the temperature at which the properties in this object are calculated (Kelvin). More... | |
doublereal | m_kbt |
Current value of Boltzmann constant times the temperature (Joules) More... | |
doublereal | m_sqrt_kbt |
current value of Boltzmann constant times the temperature. More... | |
doublereal | m_sqrt_t |
current value of temperature to 1/2 power More... | |
doublereal | m_logt |
Current value of the log of the temperature. More... | |
doublereal | m_t14 |
Current value of temperature to 1/4 power. More... | |
doublereal | m_t32 |
Current value of temperature to the 3/2 power. More... | |
std::vector< vector_fp > | m_diffcoeffs |
Polynomial fits to the binary diffusivity of each species. More... | |
DenseMatrix | m_bdiff |
Matrix of binary diffusion coefficients at the reference pressure and the current temperature Size is nsp x nsp. More... | |
std::vector< vector_fp > | m_condcoeffs |
temperature fits of the heat conduction More... | |
std::vector< vector_int > | m_poly |
Indices for the (i,j) interaction in collision integral fits. More... | |
std::vector< vector_fp > | m_omega22_poly |
Fit for omega22 collision integral. More... | |
std::vector< vector_fp > | m_astar_poly |
Fit for astar collision integral. More... | |
std::vector< vector_fp > | m_bstar_poly |
Fit for bstar collision integral. More... | |
std::vector< vector_fp > | m_cstar_poly |
Fit for cstar collision integral. More... | |
vector_fp | m_zrot |
Rotational relaxation number for each species. More... | |
vector_fp | m_crot |
Dimensionless rotational heat capacity of each species. More... | |
std::vector< bool > | m_polar |
Vector of booleans indicating whether a species is a polar molecule. More... | |
vector_fp | m_alpha |
Polarizability of each species in the phase. More... | |
vector_fp | m_eps |
Lennard-Jones well-depth of the species in the current phase. More... | |
vector_fp | m_sigma |
Lennard-Jones diameter of the species in the current phase. More... | |
DenseMatrix | m_reducedMass |
This is the reduced mass of the interaction between species i and j. More... | |
DenseMatrix | m_diam |
hard-sphere diameter for (i,j) collision More... | |
DenseMatrix | m_epsilon |
The effective well depth for (i,j) collisions. More... | |
DenseMatrix | m_dipole |
The effective dipole moment for (i,j) collisions. More... | |
DenseMatrix | m_delta |
Reduced dipole moment of the interaction between two species. More... | |
vector_fp | m_w_ac |
Pitzer acentric factor. More... | |
int | m_log_level |
Level of verbose printing during initialization. More... | |
Protected Attributes inherited from Transport | |
thermo_t * | m_thermo |
pointer to the object representing the phase More... | |
bool | m_ready |
true if finalize has been called More... | |
size_t | m_nsp |
Number of species. More... | |
size_t | m_nDim |
Number of dimensions used in flux expressions. More... | |
int | m_velocityBasis |
Velocity basis from which diffusion velocities are computed. More... | |
Class GasTransport implements some functions and properties that are shared by the MixTransport and MultiTransport classes.
Definition at line 19 of file GasTransport.h.
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Viscosity of the mixture (kg /m /s)
The viscosity is computed using the Wilke mixture rule (kg /m /s)
\[ \mu = \sum_k \frac{\mu_k X_k}{\sum_j \Phi_{k,j} X_j}. \]
Here \( \mu_k \) is the viscosity of pure species k, and
\[ \Phi_{k,j} = \frac{\left[1 + \sqrt{\left(\frac{\mu_k}{\mu_j}\sqrt{\frac{M_j}{M_k}}\right)}\right]^2} {\sqrt{8}\sqrt{1 + M_k/M_j}} \]
Reimplemented from Transport.
Reimplemented in HighPressureGasTransport.
Definition at line 131 of file GasTransport.cpp.
References DATA_PTR, and Cantera::multiply().
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Get the pure-species viscosities.
Reimplemented from Transport.
Definition at line 48 of file GasTransport.h.
References GasTransport::m_visc, and GasTransport::updateViscosity_T().
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Returns the matrix of binary diffusion coefficients.
d[ld*j + i] = rp * m_bdiff(i,j);
ld | offset of rows in the storage |
d | output vector of diffusion coefficients. Units of m**2 / s |
Reimplemented from Transport.
Reimplemented in HighPressureGasTransport.
Definition at line 222 of file GasTransport.cpp.
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Returns the Mixture-averaged diffusion coefficients [m^2/s].
Returns the mixture averaged diffusion coefficients for a gas, appropriate for calculating the mass averaged diffusive flux with respect to the mass averaged velocity using gradients of the mole fraction. Note, for the single species case or the pure fluid case the routine returns the self-diffusion coefficient. This is needed to avoid a Nan result in the formula below.
This is Eqn. 12.180 from "Chemically Reacting Flow"
\[ D_{km}' = \frac{\left( \bar{M} - X_k M_k \right)}{ \bar{\qquad M \qquad } } {\left( \sum_{j \ne k} \frac{X_j}{D_{kj}} \right) }^{-1} \]
[out] | d | Vector of mixture diffusion coefficients, \( D_{km}' \) , for each species (m^2/s). length m_nsp |
Reimplemented from Transport.
Definition at line 239 of file GasTransport.cpp.
Referenced by MixTransport::getMobilities(), and MixTransport::getSpeciesFluxes().
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Returns the mixture-averaged diffusion coefficients [m^2/s].
These are the coefficients for calculating the molar diffusive fluxes from the species mole fraction gradients, computed according to Eq. 12.176 in "Chemically Reacting Flow":
\[ D_{km}^* = \frac{1-X_k}{\sum_{j \ne k}^K X_j/\mathcal{D}_{kj}} \]
[out] | d | vector of mixture-averaged diffusion coefficients for each species, length m_nsp. |
Reimplemented from Transport.
Definition at line 274 of file GasTransport.cpp.
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Returns the mixture-averaged diffusion coefficients [m^2/s].
These are the coefficients for calculating the diffusive mass fluxes from the species mass fraction gradients, computed according to Eq. 12.178 in "Chemically Reacting Flow":
\[ \frac{1}{D_{km}} = \sum_{j \ne k}^K \frac{X_j}{\mathcal{D}_{kj}} + \frac{X_k}{1-Y_k} \sum_{j \ne k}^K \frac{Y_j}{\mathcal{D}_{kj}} \]
[out] | d | vector of mixture-averaged diffusion coefficients for each species, length m_nsp. |
Reimplemented from Transport.
Definition at line 304 of file GasTransport.cpp.
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Initialize a transport manager.
This routine sets up a transport manager. It calculates the collision integrals and populates species-dependent data structures.
thermo | Pointer to the ThermoPhase object |
mode | Chemkin compatible mode or not. This alters the specification of the collision integrals. defaults to no. |
log_level | Defaults to zero, no logging |
Reimplemented from Transport.
Reimplemented in MixTransport, and MultiTransport.
Definition at line 337 of file GasTransport.cpp.
References Phase::nSpecies().
Referenced by MultiTransport::init(), and MixTransport::init().
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Update the temperature-dependent viscosity terms.
Updates the array of pure species viscosities, and the weighting functions in the viscosity mixture rule. The flag m_visc_ok is set to true.
The formula for the weighting function is from Poling and Prausnitz, Eq. (9-5.14):
\[ \phi_{ij} = \frac{ \left[ 1 + \left( \mu_i / \mu_j \right)^{1/2} \left( M_j / M_i \right)^{1/4} \right]^2 } {\left[ 8 \left( 1 + M_i / M_j \right) \right]^{1/2}} \]
Definition at line 155 of file GasTransport.cpp.
Referenced by GasTransport::getSpeciesViscosities().
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Update the pure-species viscosities.
These are evaluated from the polynomial fits of the temperature and are assumed to be independent of pressure.
Definition at line 178 of file GasTransport.cpp.
References Cantera::dot4(), and Cantera::dot5().
Referenced by MultiTransport::updateThermal_T().
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Update the binary diffusion coefficients.
These are evaluated from the polynomial fits of the temperature at the unit pressure of 1 Pa.
Definition at line 196 of file GasTransport.cpp.
References Cantera::dot4(), and Cantera::dot5().
Referenced by HighPressureGasTransport::getBinaryDiffCoeffs(), MultiTransport::getMassFluxes(), HighPressureGasTransport::getMultiDiffCoeffs(), MultiTransport::getSpeciesFluxes(), and MultiTransport::updateThermal_T().
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Prepare to build a new kinetic-theory-based transport manager for low-density gases.
Uses polynomial fits to Monchick & Mason collision integrals.
Definition at line 374 of file GasTransport.cpp.
References Cantera::Avogadro, Cantera::Boltzmann, Cantera::epsilon_0, MMCollisionInt::init(), Cantera::Pi, and Cantera::writelog().
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Read the transport database.
Read transport property data from a file for a list of species. Given the name of a file containing transport property parameters and a list of species names.
Definition at line 464 of file GasTransport.cpp.
References GasTransportData::acentric_factor, GasTransportData::diameter, GasTransportData::dipole, GasTransportData::geometry, GasTransportData::polarizability, GasTransportData::rotational_relaxation, and GasTransportData::well_depth.
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Corrections for polar-nonpolar binary diffusion coefficients.
Calculate corrections to the well depth parameter and the diameter for use in computing the binary diffusion coefficient of polar-nonpolar pairs. For more information about this correction, see Dixon-Lewis, Proc. Royal Society (1968).
i | Species one - this is a bimolecular correction routine |
j | species two - this is a bimolecular correction routine |
f_eps | Multiplicative correction factor to be applied to epsilon(i,j) |
f_sigma | Multiplicative correction factor to be applied to diam(i,j) |
Definition at line 493 of file GasTransport.cpp.
References Cantera::epsilon_0, and Cantera::Pi.
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Generate polynomial fits to collision integrals.
integrals | interpolator for the collision integrals |
Definition at line 520 of file GasTransport.cpp.
References COLL_INT_POLY_DEGREE, DATA_PTR, and Cantera::writelog().
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Generate polynomial fits to the viscosity, conductivity, and the binary diffusion coefficients.
If CK_mode, then the fits are of the form
\[ \log(\eta(i)) = \sum_{n = 0}^3 a_n(i) (\log T)^n \]
and
\[ \log(D(i,j)) = \sum_{n = 0}^3 a_n(i,j) (\log T)^n \]
Otherwise the fits are of the form
\[ \eta(i)/sqrt(k_BT) = \sum_{n = 0}^4 a_n(i) (\log T)^n \]
and
\[ D(i,j)/sqrt(k_BT)) = \sum_{n = 0}^4 a_n(i,j) (\log T)^n \]
integrals | interpolator for the collision integrals |
Definition at line 574 of file GasTransport.cpp.
References Cantera::Avogadro, Cantera::Boltzmann, DATA_PTR, Cantera::Pi, Cantera::poly3(), Cantera::poly4(), Cantera::polyfit(), Cantera::vec2str(), Cantera::writelog(), and Cantera::writelogf().
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Second-order correction to the binary diffusion coefficients.
Calculate second-order corrections to binary diffusion coefficient pair (dkj, djk). At first order, the binary diffusion coefficients are independent of composition, and d(k,j) = d(j,k). But at second order, there is a weak dependence on composition, with the result that d(k,j) != d(j,k). This method computes the multiplier by which the first-order binary diffusion coefficient should be multiplied to produce the value correct to second order. The expressions here are taken from Marerro and Mason, J. Phys. Chem. Ref. Data, vol. 1, p. 3 (1972).
t | Temperature (K) |
integrals | interpolator for the collision integrals |
k | index of first species |
j | index of second species |
xk | Mole fraction of species k |
xj | Mole fraction of species j |
fkj | multiplier for d(k,j) |
fjk | multiplier for d(j,k) |
Definition at line 813 of file GasTransport.cpp.
References Cantera::Boltzmann.
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Vector of species mole fractions.
These are processed so that all mole fractions are >= Tiny. Length = m_kk.
Definition at line 237 of file GasTransport.h.
Referenced by MultiTransport::getMassFluxes(), MultiTransport::getMultiDiffCoeffs(), MultiTransport::getSpeciesFluxes(), MultiTransport::getThermalDiffCoeffs(), MixTransport::thermalConductivity(), MultiTransport::update_C(), and MixTransport::update_C().
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Internal storage for the viscosity of the mixture (kg /m /s)
Definition at line 240 of file GasTransport.h.
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Update boolean for mixture rule for the mixture viscosity.
Definition at line 243 of file GasTransport.h.
Referenced by MixTransport::update_C().
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Update boolean for the weighting factors for the mixture viscosity.
Definition at line 246 of file GasTransport.h.
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Update boolean for the species viscosities.
Definition at line 249 of file GasTransport.h.
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Update boolean for the binary diffusivities at unit pressure.
Definition at line 252 of file GasTransport.h.
Referenced by HighPressureGasTransport::getMultiDiffCoeffs(), and MixTransport::update_T().
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Type of the polynomial fits to temperature.
CK_Mode means Chemkin mode. Currently CA_Mode is used which are different types of fits to temperature.
Definition at line 256 of file GasTransport.h.
Referenced by MultiTransport::model(), HighPressureGasTransport::model(), MixTransport::updateCond_T(), and MultiTransport::updateThermal_T().
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m_phi is a Viscosity Weighting Function. size = m_nsp * n_nsp
Definition at line 259 of file GasTransport.h.
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work space length = m_kk
Definition at line 262 of file GasTransport.h.
Referenced by MultiTransport::getMassFluxes(), MixTransport::getMobilities(), MultiTransport::getSpeciesFluxes(), and MixTransport::getSpeciesFluxes().
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vector of species viscosities (kg /m /s).
These are used in Wilke's rule to calculate the viscosity of the solution. length = m_kk.
Definition at line 266 of file GasTransport.h.
Referenced by GasTransport::getSpeciesViscosities(), and MultiTransport::updateThermal_T().
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Polynomial fits to the viscosity of each species.
m_visccoeffs[k] is the vector of polynomial coefficients for species k that fits the viscosity as a function of temperature.
Definition at line 271 of file GasTransport.h.
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Local copy of the species molecular weights.
Definition at line 274 of file GasTransport.h.
Referenced by MultiTransport::eval_L0000(), MultiTransport::eval_L0010(), MultiTransport::getMolarFluxes(), MultiTransport::getMultiDiffCoeffs(), HighPressureGasTransport::getMultiDiffCoeffs(), MultiTransport::getThermalDiffCoeffs(), HighPressureGasTransport::thermalConductivity(), MultiTransport::updateThermal_T(), and HighPressureGasTransport::viscosity().
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Holds square roots of molecular weight ratios.
Definition at line 283 of file GasTransport.h.
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Holds square roots of molecular weight ratios.
m_wratjk1(j,k) = sqrt(1.0 + mw[k]/mw[j]) j < k
Definition at line 289 of file GasTransport.h.
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vector of square root of species viscosities sqrt(kg /m /s).
These are used in Wilke's rule to calculate the viscosity of the solution. length = m_kk.
Definition at line 294 of file GasTransport.h.
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Powers of the ln temperature, up to fourth order.
Definition at line 297 of file GasTransport.h.
Referenced by MixTransport::updateCond_T().
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Current value of the temperature at which the properties in this object are calculated (Kelvin).
Definition at line 301 of file GasTransport.h.
Referenced by MultiTransport::eval_L0000(), MultiTransport::eval_L0010(), HighPressureGasTransport::getBinaryDiffCoeffs(), MultiTransport::getMassFluxes(), MixTransport::getMobilities(), MultiTransport::getMultiDiffCoeffs(), HighPressureGasTransport::getMultiDiffCoeffs(), MultiTransport::getSpeciesFluxes(), HighPressureGasTransport::thermalConductivity(), MultiTransport::update_T(), MixTransport::update_T(), and MultiTransport::updateThermal_T().
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Current value of Boltzmann constant times the temperature (Joules)
Definition at line 304 of file GasTransport.h.
Referenced by MultiTransport::updateThermal_T().
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current value of Boltzmann constant times the temperature.
(Joules) to 1/2 power
Definition at line 308 of file GasTransport.h.
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current value of temperature to 1/2 power
Definition at line 311 of file GasTransport.h.
Referenced by MixTransport::updateCond_T(), and MultiTransport::updateThermal_T().
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Current value of the log of the temperature.
Definition at line 314 of file GasTransport.h.
Referenced by MultiTransport::updateThermal_T().
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Current value of temperature to 1/4 power.
Definition at line 317 of file GasTransport.h.
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Current value of temperature to the 3/2 power.
Definition at line 320 of file GasTransport.h.
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Polynomial fits to the binary diffusivity of each species.
m_diffcoeff[ic] is vector of polynomial coefficients for species i species j that fits the binary diffusion coefficient. The relationship between i j and ic is determined from the following algorithm:
int ic = 0; for (i = 0; i < m_nsp; i++) { for (j = i; j < m_nsp; j++) { ic++; }
Definition at line 335 of file GasTransport.h.
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Matrix of binary diffusion coefficients at the reference pressure and the current temperature Size is nsp x nsp.
Definition at line 339 of file GasTransport.h.
Referenced by MultiTransport::eval_L0000(), MultiTransport::eval_L0010(), HighPressureGasTransport::getBinaryDiffCoeffs(), MultiTransport::getMassFluxes(), HighPressureGasTransport::getMultiDiffCoeffs(), MultiTransport::getSpeciesFluxes(), and MultiTransport::updateThermal_T().
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temperature fits of the heat conduction
Dimensions are number of species (nsp) polynomial order of the collision integral fit (degree+1).
Definition at line 346 of file GasTransport.h.
Referenced by MixTransport::updateCond_T().
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Indices for the (i,j) interaction in collision integral fits.
m_poly[i][j] contains the index for (i,j) interactions in m_omega22_poly, m_astar_poly, m_bstar_poly, and m_cstar_poly.
Definition at line 353 of file GasTransport.h.
Referenced by MultiTransport::updateThermal_T().
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Fit for omega22 collision integral.
m_omega22_poly[m_poly[i][j]] is the vector of polynomial coefficients (length degree+1) for the collision integral fit for the species pair (i,j).
Definition at line 361 of file GasTransport.h.
Referenced by MultiTransport::updateThermal_T().
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Fit for astar collision integral.
m_astar_poly[m_poly[i][j]] is the vector of polynomial coefficients (length degree+1) for the collision integral fit for the species pair (i,j).
Definition at line 369 of file GasTransport.h.
Referenced by MultiTransport::updateThermal_T().
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Fit for bstar collision integral.
m_bstar_poly[m_poly[i][j]] is the vector of polynomial coefficients (length degree+1) for the collision integral fit for the species pair (i,j).
Definition at line 377 of file GasTransport.h.
Referenced by MultiTransport::updateThermal_T().
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Fit for cstar collision integral.
m_bstar_poly[m_poly[i][j]] is the vector of polynomial coefficients (length degree+1) for the collision integral fit for the species pair (i,j).
Definition at line 385 of file GasTransport.h.
Referenced by MultiTransport::updateThermal_T().
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Rotational relaxation number for each species.
length is the number of species in the phase. units are dimensionless
Definition at line 391 of file GasTransport.h.
Referenced by MultiTransport::updateThermal_T().
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Dimensionless rotational heat capacity of each species.
These values are 0, 1 and 1.5 for single-molecule, linear, and nonlinear species respectively length is the number of species in the phase. Dimensionless (Cr / R)
Definition at line 399 of file GasTransport.h.
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Vector of booleans indicating whether a species is a polar molecule.
Length is nsp
Definition at line 405 of file GasTransport.h.
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Polarizability of each species in the phase.
Length = nsp. Units = m^3
Definition at line 411 of file GasTransport.h.
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Lennard-Jones well-depth of the species in the current phase.
length is the number of species in the phase. Units are Joules (Note this is not Joules/kmol) (note, no kmol -> this is a per molecule amount)
Definition at line 418 of file GasTransport.h.
Referenced by MultiTransport::init(), and MultiTransport::updateThermal_T().
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Lennard-Jones diameter of the species in the current phase.
length is the number of species in the phase units are in meters.
Definition at line 425 of file GasTransport.h.
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This is the reduced mass of the interaction between species i and j.
reducedMass(i,j) = mw[i] * mw[j] / (Avogadro * (mw[i] + mw[j]));
Units are kg (note, no kmol -> this is a per molecule amount)
Length nsp * nsp. This is a symmetric matrix
Definition at line 435 of file GasTransport.h.
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hard-sphere diameter for (i,j) collision
diam(i,j) = 0.5*(sigma[i] + sigma[j]); Units are m (note, no kmol -> this is a per molecule amount)
Length nsp * nsp. This is a symmetric matrix.
Definition at line 444 of file GasTransport.h.
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The effective well depth for (i,j) collisions.
epsilon(i,j) = sqrt(eps[i]*eps[j]); Units are Joules (note, no kmol -> this is a per molecule amount)
Length nsp * nsp. This is a symmetric matrix.
Definition at line 453 of file GasTransport.h.
Referenced by MultiTransport::init().
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The effective dipole moment for (i,j) collisions.
Given dipoleMoment
in Debye (a Debye is 3.335e-30 C-m):
dipole(i,i) = 1.e-21 / lightSpeed * dipoleMoment; dipole(i,j) = sqrt(dipole(i,i) * dipole(j,j)); (note, no kmol -> this is a per molecule amount)
Length nsp * nsp. This is a symmetric matrix.
Definition at line 465 of file GasTransport.h.
Referenced by HighPressureGasTransport::viscosity().
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Reduced dipole moment of the interaction between two species.
This is the reduced dipole moment of the interaction between two species 0.5 * dipole(i,j)^2 / (4 * Pi * epsilon_0 * epsilon(i,j) * d^3);
Length nsp * nsp .This is a symmetric matrix
Definition at line 474 of file GasTransport.h.
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Pitzer acentric factor.
Length is the number of species in the phase. Dimensionless.
Definition at line 480 of file GasTransport.h.
Referenced by HighPressureGasTransport::thermalConductivity().
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Level of verbose printing during initialization.
Definition at line 483 of file GasTransport.h.