Class GasTransport implements some functions and properties that are shared by the MixTransport and MultiTransport classes. More...
#include <GasTransport.h>
Class GasTransport implements some functions and properties that are shared by the MixTransport and MultiTransport classes.
For details, see Kee, et al. [20] and [21].
Definition at line 25 of file GasTransport.h.
Public Member Functions | |
| double | viscosity () override |
| Get the viscosity [Pa·s] of the mixture. | |
| void | getSpeciesViscosities (span< double > visc) override |
| Get the pure-species viscosities [Pa·s]. | |
| void | getBinaryDiffCoeffs (const size_t ld, span< double > d) override |
| Returns the matrix of binary diffusion coefficients [m²/s]. | |
| void | getMixDiffCoeffs (span< double > d) override |
| Returns the Mixture-averaged diffusion coefficients [m²/s]. | |
| void | getMixDiffCoeffsMole (span< double > d) override |
| Returns the mixture-averaged diffusion coefficients [m²/s]. | |
| void | getMixDiffCoeffsMass (span< double > d) override |
| Returns the mixture-averaged diffusion coefficients [m²/s]. | |
| void | getViscosityPolynomial (size_t i, span< double > coeffs) const override |
Return the polynomial fits to the viscosity of species i. | |
| void | getConductivityPolynomial (size_t i, span< double > coeffs) const override |
Return the temperature fits of the heat conductivity of species i. | |
| void | getBinDiffusivityPolynomial (size_t i, size_t j, span< double > coeffs) const override |
| Return the polynomial fits to the binary diffusivity of species pair (i, j) | |
| void | getCollisionIntegralPolynomial (size_t i, size_t j, span< double > astar_coeffs, span< double > bstar_coeffs, span< double > cstar_coeffs) const override |
| Return the polynomial fits to the collision integral of species pair (i, j) | |
| void | setViscosityPolynomial (size_t i, span< double > coeffs) override |
Modify the polynomial fits to the viscosity of species i | |
| void | setConductivityPolynomial (size_t i, span< double > coeffs) override |
Modify the temperature fits of the heat conductivity of species i | |
| void | setBinDiffusivityPolynomial (size_t i, size_t j, span< double > coeffs) override |
| Modify the polynomial fits to the binary diffusivity of species pair (i, j) | |
| void | setCollisionIntegralPolynomial (size_t i, size_t j, span< double > astar_coeffs, span< double > bstar_coeffs, span< double > cstar_coeffs, bool actualT) override |
| Modify the polynomial fits to the collision integral of species pair (i, j) | |
| void | init (shared_ptr< ThermoPhase > thermo, int mode=0) override |
| Initialize a transport manager. | |
| bool | CKMode () const override |
| Boolean indicating the form of the transport properties polynomial fits. | |
| void | invalidateCache () override |
| Invalidate any cached values which are normally updated only when a change in state is detected. | |
Public Member Functions inherited from Transport | |
| Transport ()=default | |
| Constructor. | |
| Transport (const Transport &)=delete | |
| Transport & | operator= (const Transport &)=delete |
| shared_ptr< Transport > | clone (shared_ptr< ThermoPhase > thermo) const |
| Create a new Transport object using the same transport model and species transport properties as this one. | |
| virtual string | transportModel () const |
| Identifies the model represented by this Transport object. | |
| ThermoPhase & | thermo () |
| Phase object. | |
| size_t | checkSpeciesIndex (size_t k) const |
| Check that the specified species index is in range. | |
| virtual void | getSpeciesFluxes (size_t ndim, span< const double > grad_T, size_t ldx, span< const double > grad_X, size_t ldf, span< double > fluxes) |
| Get the species diffusive mass fluxes [kg/m²/s] with respect to the specified solution averaged velocity, given the mole fraction and temperature gradients. | |
| virtual void | getMolarFluxes (span< const double > state1, span< const double > state2, const double delta, span< double > cfluxes) |
| Get the molar fluxes [kmol/m²/s], given the thermodynamic state at two nearby points. | |
| virtual void | getMassFluxes (span< const double > state1, span< const double > state2, double delta, span< double > mfluxes) |
| Get the mass fluxes [kg/m²/s], given the thermodynamic state at two nearby points. | |
| virtual void | getThermalDiffCoeffs (span< double > dt) |
| Return a vector of thermal diffusion coefficients [kg/m/s]. | |
| virtual void | getBinaryDiffCoeffs (const size_t ld, span< double > d) |
| Returns the matrix of binary diffusion coefficients [m²/s]. | |
| virtual void | getMultiDiffCoeffs (const size_t ld, span< double > d) |
| Return the multicomponent diffusion coefficients [m²/s]. | |
| virtual void | getMixDiffCoeffs (span< double > d) |
| Return a vector of mixture averaged diffusion coefficients [m²/s]. | |
| virtual void | getMixDiffCoeffsMole (span< double > d) |
| Returns a vector of mixture averaged diffusion coefficients [m²/s]. | |
| virtual void | getMixDiffCoeffsMass (span< double > d) |
| Returns a vector of mixture averaged diffusion coefficients [m²/s]. | |
| virtual void | getViscosityPolynomial (size_t i, span< double > coeffs) const |
Return the polynomial fits to the viscosity of species i. | |
| virtual void | getConductivityPolynomial (size_t i, span< double > coeffs) const |
Return the temperature fits of the heat conductivity of species i. | |
| virtual void | getBinDiffusivityPolynomial (size_t i, size_t j, span< double > coeffs) const |
| Return the polynomial fits to the binary diffusivity of species pair (i, j) | |
| virtual void | getCollisionIntegralPolynomial (size_t i, size_t j, span< double > astar_coeffs, span< double > bstar_coeffs, span< double > cstar_coeffs) const |
| Return the polynomial fits to the collision integral of species pair (i, j) | |
| virtual void | setViscosityPolynomial (size_t i, span< double > coeffs) |
Modify the polynomial fits to the viscosity of species i | |
| virtual void | setConductivityPolynomial (size_t i, span< double > coeffs) |
Modify the temperature fits of the heat conductivity of species i | |
| virtual void | setBinDiffusivityPolynomial (size_t i, size_t j, span< double > coeffs) |
| Modify the polynomial fits to the binary diffusivity of species pair (i, j) | |
| virtual void | setCollisionIntegralPolynomial (size_t i, size_t j, span< double > astar_coeffs, span< double > bstar_coeffs, span< double > cstar_coeffs, bool flag) |
| Modify the polynomial fits to the collision integral of species pair (i, j) | |
| AnyMap | parameters () const |
| Return the parameters for a phase definition which are needed to reconstruct an identical object using the newTransport() function. | |
| AnyMap | fittingErrors () const |
| Get error metrics about any functional fits calculated for pure species transport properties. | |
| virtual void | invalidateCache () |
| Invalidate any cached values which are normally updated only when a change in state is detected. | |
| virtual double | bulkViscosity () |
| The bulk viscosity [Pa·s]. | |
| virtual double | thermalConductivity () |
| Get the mixture thermal conductivity [W/m/K]. | |
| virtual double | electricalConductivity () |
| Get the electrical conductivity [siemens/m]. | |
| virtual void | getMobilities (span< double > mobil_e) |
| Get the electrical mobilities [m²/V/s]. | |
Protected Member Functions | |
| virtual void | update_T () |
| virtual void | update_C ()=0 |
| virtual void | updateViscosity_T () |
| Update the temperature-dependent viscosity terms. | |
| virtual void | updateSpeciesViscosities () |
| Update the pure-species viscosities. | |
| virtual void | updateDiff_T () |
| Update the binary diffusion coefficients. | |
Initialization | |
| virtual void | setupCollisionParameters () |
| Setup parameters for a new kinetic-theory-based transport manager for low-density gases. | |
| void | setupCollisionIntegral () |
| Setup range for polynomial fits to collision integrals of Monchick & Mason [31]. | |
| virtual void | getTransportData () |
| Read the transport database. | |
| void | makePolarCorrections (size_t i, size_t j, double &f_eps, double &f_sigma) |
| Corrections for polar-nonpolar binary diffusion coefficients. | |
| void | fitCollisionIntegrals (MMCollisionInt &integrals) |
| Generate polynomial fits to collision integrals. | |
| virtual void | fitProperties (MMCollisionInt &integrals) |
| Generate polynomial fits to the viscosity \( \eta \) and conductivity \( \lambda \). | |
| virtual void | fitDiffCoeffs (MMCollisionInt &integrals) |
| Generate polynomial fits to the binary diffusion coefficients. | |
| void | getBinDiffCorrection (double t, MMCollisionInt &integrals, size_t k, size_t j, double xk, double xj, double &fkj, double &fjk) |
| Second-order correction to the binary diffusion coefficients. | |
Protected Attributes | |
| vector< double > | m_molefracs |
| Vector of species mole fractions. | |
| double | m_viscmix = 0.0 |
| Internal storage for the viscosity of the mixture [Pa·s]. | |
| bool | m_visc_ok = false |
| Update boolean for mixture rule for the mixture viscosity. | |
| bool | m_viscwt_ok = false |
| Update boolean for the weighting factors for the mixture viscosity. | |
| bool | m_spvisc_ok = false |
| Update boolean for the species viscosities. | |
| bool | m_bindiff_ok = false |
| Update boolean for the binary diffusivities at unit pressure. | |
| int | m_mode = 0 |
| Type of the polynomial fits to temperature. | |
| DenseMatrix | m_phi |
| Viscosity weighting function. size = m_nsp * m_nsp. | |
| vector< double > | m_spwork |
| work space length = m_nsp | |
| vector< double > | m_visc |
| vector of species viscosities [Pa·s]. | |
| vector< vector< double > > | m_visccoeffs |
| Polynomial fits to the viscosity of each species. | |
| vector< double > | m_mw |
| Local copy of the species molecular weights. | |
| DenseMatrix | m_wratjk |
| Holds square roots of molecular weight ratios. | |
| DenseMatrix | m_wratkj1 |
| Holds square roots of molecular weight ratios. | |
| vector< double > | m_sqvisc |
| vector of square root of species viscosities. | |
| vector< double > | m_polytempvec |
| Powers of the ln temperature, up to fourth order. | |
| double | m_temp = -1.0 |
| Current value of the temperature [K] at which the properties in this object are calculated. | |
| double | m_kbt = 0.0 |
| Current value of Boltzmann constant times the temperature [J]. | |
| double | m_sqrt_t = 0.0 |
| current value of temperature to 1/2 power | |
| double | m_logt = 0.0 |
| Current value of the log of the temperature. | |
| double | m_t14 = 0.0 |
| Current value of temperature to 1/4 power. | |
| vector< vector< double > > | m_diffcoeffs |
| Polynomial fits to the binary diffusivity of each species. | |
| DenseMatrix | m_bdiff |
| Matrix of binary diffusion coefficients at the reference pressure and the current temperature Size is m_nsp x m_nsp. | |
| vector< vector< double > > | m_condcoeffs |
| temperature fits of the heat conduction | |
| vector< vector< int > > | m_poly |
| Indices for the (i,j) interaction in collision integral fits. | |
| vector< vector< double > > | m_omega22_poly |
| Fit for omega22 collision integral. | |
| vector< vector< int > > | m_star_poly_uses_actualT |
| Flag to indicate for which (i,j) interaction pairs the actual temperature is used instead of the reduced temperature. | |
| vector< vector< double > > | m_astar_poly |
| Fit for astar collision integral. | |
| vector< vector< double > > | m_bstar_poly |
| Fit for bstar collision integral. | |
| vector< vector< double > > | m_cstar_poly |
| Fit for cstar collision integral. | |
| vector< double > | m_zrot |
| Rotational relaxation number for each species. | |
| vector< double > | m_crot |
| Dimensionless rotational heat capacity of each species. | |
| vector< bool > | m_polar |
| Vector of booleans indicating whether a species is a polar molecule. | |
| vector< double > | m_alpha |
| Polarizability [m³] of each species in the phase. | |
| vector< double > | m_eps |
| Lennard-Jones well-depth [J] of the species in the current phase. | |
| vector< double > | m_sigma |
| Lennard-Jones diameter [m] of the species in the current phase. | |
| DenseMatrix | m_reducedMass |
| This is the reduced mass [kg] of the interaction between species i and j. | |
| DenseMatrix | m_diam |
| hard-sphere diameter [m] for (i,j) collision | |
| DenseMatrix | m_epsilon |
| The effective well depth [J] for (i,j) collisions. | |
| DenseMatrix | m_dipole |
| The effective dipole moment [Coulomb·m] for (i,j) collisions. | |
| DenseMatrix | m_delta |
| Reduced dipole moment of the interaction between two species. | |
| vector< double > | m_w_ac |
| Pitzer acentric factor [dimensionless]. | |
| vector< double > | m_disp |
| Dispersion coefficient normalized by the square of the elementary charge [m⁵]. | |
| vector< double > | m_quad_polar |
| Quadrupole polarizability. | |
Protected Attributes inherited from Transport | |
| shared_ptr< ThermoPhase > | m_thermo |
| pointer to the object representing the phase | |
| size_t | m_nsp = 0 |
| Number of species in the phase. | |
| AnyMap | m_fittingErrors |
| Maximum errors associated with fitting pure species transport properties. | |
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protected |
Definition at line 23 of file GasTransport.cpp.
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Get the viscosity [Pa·s] of the mixture.
The viscosity is computed using the Wilke mixture rule, as given in Poling et al. [38], Eqs. (9-5.13 and 9-5.14):
\[ \eta = \sum_k \frac{\eta_k X_k}{\sum_j \Phi_{k,j} X_j}. \]
Here, \( \eta_k \) is the viscosity of pure species k and the weighting function \( \Phi_{k,j} \) is:
\[ \Phi_{k,j} = \frac{ \left[ 1 + \left( \eta_k / \eta_j \right)^{1/2} \left( M_j / M_k \right)^{1/4} \right]^2 } {\left[ 8 \left( 1 + M_k / M_j \right) \right]^{1/2}} \]
Reimplemented from Transport.
Reimplemented in HighPressureGasTransport, and IonGasTransport.
Definition at line 60 of file GasTransport.cpp.
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Get the pure-species viscosities [Pa·s].
Reimplemented from Transport.
Definition at line 48 of file GasTransport.h.
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Returns the matrix of binary diffusion coefficients [m²/s].
| [in] | ld | Leading dimension of the flattened array d used to store the diffusion coefficient matrix; usually equal to the number of species. |
| [out] | d | Diffusion coefficient matrix stored in column-major (Fortran) order, such that \( \mathcal{D}_{ij} = \tt{d[ld*j + i]} \); must be at least ld times the number of species in length. |
Reimplemented from Transport.
Reimplemented in HighPressureGasTransportBase.
Definition at line 149 of file GasTransport.cpp.
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Returns the Mixture-averaged diffusion coefficients [m²/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"
\[ D_{km}' = \frac{\left( \bar{M} - X_k M_k \right)}{ \bar{\qquad M \qquad } } {\left( \sum_{j \ne k} \frac{X_j}{\mathcal{D}_{kj}} \right) }^{-1} \]
| [out] | d | Vector of mixture diffusion coefficients, \( D_{km}' \) , for each species; length is the number of species. |
Reimplemented from Transport.
Reimplemented in HighPressureGasTransportBase, IonGasTransport, and UnityLewisTransport.
Definition at line 168 of file GasTransport.cpp.
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Returns the mixture-averaged diffusion coefficients [m²/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.
Reimplemented in HighPressureGasTransportBase, and UnityLewisTransport.
Definition at line 200 of file GasTransport.cpp.
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Returns the mixture-averaged diffusion coefficients [m²/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.
Reimplemented in HighPressureGasTransportBase, and UnityLewisTransport.
Definition at line 231 of file GasTransport.cpp.
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Return the polynomial fits to the viscosity of species i.
Reimplemented from Transport.
Definition at line 758 of file GasTransport.cpp.
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Return the temperature fits of the heat conductivity of species i.
Reimplemented from Transport.
Definition at line 768 of file GasTransport.cpp.
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Return the polynomial fits to the binary diffusivity of species pair (i, j)
Reimplemented from Transport.
Definition at line 778 of file GasTransport.cpp.
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Return the polynomial fits to the collision integral of species pair (i, j)
Reimplemented from Transport.
Definition at line 797 of file GasTransport.cpp.
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Modify the polynomial fits to the viscosity of species i
Reimplemented from Transport.
Definition at line 818 of file GasTransport.cpp.
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Modify the temperature fits of the heat conductivity of species i
Reimplemented from Transport.
Definition at line 829 of file GasTransport.cpp.
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Modify the polynomial fits to the binary diffusivity of species pair (i, j)
Reimplemented from Transport.
Definition at line 840 of file GasTransport.cpp.
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Modify the polynomial fits to the collision integral of species pair (i, j)
Reimplemented from Transport.
Definition at line 860 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 | ThermoPhase object determining conditions for which to compute transport properties. |
| mode | Chemkin compatible mode or not. This alters the specification of the collision integrals. defaults to no. |
shared_ptr<ThermoPhase> in Cantera 3.2. Reimplemented from Transport.
Reimplemented in IonGasTransport, HighPressureGasTransport, MixTransport, and MultiTransport.
Definition at line 265 of file GasTransport.cpp.
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Boolean indicating the form of the transport properties polynomial fits.
Returns true if the Chemkin form is used.
Reimplemented from Transport.
Definition at line 143 of file GasTransport.h.
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Invalidate any cached values which are normally updated only when a change in state is detected.
Reimplemented from Transport.
Reimplemented in MultiTransport.
Definition at line 358 of file GasTransport.cpp.
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Reimplemented in MixTransport, and MultiTransport.
Definition at line 28 of file GasTransport.cpp.
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protectedpure virtual |
Implemented in MixTransport, and MultiTransport.
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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.
Definition at line 84 of file GasTransport.cpp.
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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 105 of file GasTransport.cpp.
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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 123 of file GasTransport.cpp.
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Setup parameters for a new kinetic-theory-based transport manager for low-density gases.
Definition at line 297 of file GasTransport.cpp.
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Setup range for polynomial fits to collision integrals of Monchick & Mason [31].
Definition at line 368 of file GasTransport.cpp.
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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.
Reimplemented in HighPressureGasTransportBase.
Definition at line 394 of file GasTransport.cpp.
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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 [7].
| 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 431 of file GasTransport.cpp.
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Generate polynomial fits to collision integrals.
| integrals | interpolator for the collision integrals |
Definition at line 456 of file GasTransport.cpp.
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Generate polynomial fits to the viscosity \( \eta \) and conductivity \( \lambda \).
If CKMode(), then the fits are of the form
\[ \ln \eta(i) = \sum_{n=0}^3 a_n(i) \, (\ln T)^n \]
and
\[ \ln \lambda(i) = \sum_{n=0}^3 b_n(i) \, (\ln T)^n \]
Otherwise the fits are of the form
\[ \left(\eta(i)\right)^{1/2} = T^{1/4} \sum_{n=0}^4 a_n(i) \, (\ln T)^n \]
and
\[ \lambda(i) = T^{1/2} \sum_{n=0}^4 b_n(i) \, (\ln T)^n \]
| integrals | interpolator for the collision integrals |
Definition at line 499 of file GasTransport.cpp.
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Generate polynomial fits to the binary diffusion coefficients.
If CKMode(), then the fits are of the form
\[ \ln \mathcal{D}(i,j) = \frac{1}{p} \sum_{n=0}^3 c_n(i,j) \, (\ln T)^n \]
Otherwise the fits are of the form
\[ \mathcal{D}(i,j) = \frac{T^{3/2}}{p} \sum_{n=0}^4 c_n(i,j) \, (\ln T)^n \]
| integrals | interpolator for the collision integrals |
Reimplemented in IonGasTransport.
Definition at line 635 of file GasTransport.cpp.
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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 [28].
| 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 706 of file GasTransport.cpp.
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Vector of species mole fractions.
These are processed so that all mole fractions are >= Tiny. Length = m_nsp.
Definition at line 283 of file GasTransport.h.
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Internal storage for the viscosity of the mixture [Pa·s].
Definition at line 286 of file GasTransport.h.
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Update boolean for mixture rule for the mixture viscosity.
Definition at line 289 of file GasTransport.h.
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Update boolean for the weighting factors for the mixture viscosity.
Definition at line 292 of file GasTransport.h.
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Update boolean for the species viscosities.
Definition at line 295 of file GasTransport.h.
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Update boolean for the binary diffusivities at unit pressure.
Definition at line 298 of file GasTransport.h.
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Type of the polynomial fits to temperature.
CK_Mode means Chemkin mode. Any other value means to use Cantera's preferred fitting functions.
Definition at line 302 of file GasTransport.h.
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Viscosity weighting function. size = m_nsp * m_nsp.
Definition at line 305 of file GasTransport.h.
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work space length = m_nsp
Definition at line 308 of file GasTransport.h.
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vector of species viscosities [Pa·s].
These are used in Wilke's rule to calculate the viscosity of the solution. length = m_nsp.
Definition at line 312 of file GasTransport.h.
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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 317 of file GasTransport.h.
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Local copy of the species molecular weights.
Definition at line 320 of file GasTransport.h.
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Holds square roots of molecular weight ratios.
Definition at line 329 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 335 of file GasTransport.h.
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vector of square root of species viscosities.
These are used in Wilke's rule to calculate the viscosity of the solution. length = m_nsp.
Definition at line 339 of file GasTransport.h.
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Powers of the ln temperature, up to fourth order.
Definition at line 342 of file GasTransport.h.
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Current value of the temperature [K] at which the properties in this object are calculated.
Definition at line 346 of file GasTransport.h.
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Current value of Boltzmann constant times the temperature [J].
Definition at line 349 of file GasTransport.h.
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current value of temperature to 1/2 power
Definition at line 352 of file GasTransport.h.
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Current value of the log of the temperature.
Definition at line 355 of file GasTransport.h.
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Current value of temperature to 1/4 power.
Definition at line 358 of file GasTransport.h.
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Polynomial fits to the binary diffusivity of each species.
m_diffcoeff[ic] is the vector of polynomial coefficients that fits the binary diffusion coefficient for species i and j. The relationship between i, j, and ic is determined from the following algorithm:
Definition at line 374 of file GasTransport.h.
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Matrix of binary diffusion coefficients at the reference pressure and the current temperature Size is m_nsp x m_nsp.
Definition at line 378 of file GasTransport.h.
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temperature fits of the heat conduction
Dimensions are number of species (m_nsp) and polynomial order of the collision integral fit (degree+1).
Definition at line 385 of file GasTransport.h.
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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 392 of file GasTransport.h.
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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 399 of file GasTransport.h.
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Flag to indicate for which (i,j) interaction pairs the actual temperature is used instead of the reduced temperature.
Definition at line 403 of file GasTransport.h.
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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 410 of file GasTransport.h.
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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 417 of file GasTransport.h.
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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 424 of file GasTransport.h.
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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 430 of file GasTransport.h.
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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 438 of file GasTransport.h.
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Vector of booleans indicating whether a species is a polar molecule.
Length is m_nsp.
Definition at line 444 of file GasTransport.h.
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Polarizability [m³] of each species in the phase.
Definition at line 447 of file GasTransport.h.
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Lennard-Jones well-depth [J] of the species in the current phase.
length is the number of species in the phase. Note this is not J/kmol; this is a per molecule amount.
Definition at line 454 of file GasTransport.h.
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Lennard-Jones diameter [m] of the species in the current phase.
Definition at line 457 of file GasTransport.h.
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This is the reduced mass [kg] of the interaction between species i and j.
\[ m_{ij} = \frac{M_i M_j}{N_A (M_i + M_j)} \]
Length m_nsp * m_nsp. This is a symmetric matrix
Definition at line 466 of file GasTransport.h.
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hard-sphere diameter [m] for (i,j) collision
\[ \sigma_{ij} = \frac{\sigma_i + \sigma_j}{2} \]
Length m_nsp * m_nsp. This is a symmetric matrix.
Definition at line 475 of file GasTransport.h.
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The effective well depth [J] for (i,j) collisions.
\[ \epsilon_{ij} = \sqrt{\epsilon_i \epsilon_j} \]
Length m_nsp * m_nsp. This is a symmetric matrix.
Definition at line 484 of file GasTransport.h.
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The effective dipole moment [Coulomb·m] for (i,j) collisions.
\[ \mu_{ij} = \sqrt{\mu_i \mu_j} \]
Dipole moments are conventionally given in Debye. The conversion factor to Coulomb·m is \( 10^{-21} / c \approx 3.335 \times 10^{-30} \).
Length m_nsp * m_nsp. This is a symmetric matrix.
Definition at line 497 of file GasTransport.h.
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Reduced dipole moment of the interaction between two species.
\[ \tilde{\delta}^*_{ij} = \frac{ \mu_{ij}^2 }{ 8 \pi \varepsilon_0 \epsilon_{ij} \sigma_{ij}^3 } \]
Length m_nsp * m_nsp. This is a symmetric matrix
Definition at line 507 of file GasTransport.h.
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Pitzer acentric factor [dimensionless].
Length is the number of species in the phase.
Definition at line 513 of file GasTransport.h.
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Dispersion coefficient normalized by the square of the elementary charge [m⁵].
Definition at line 516 of file GasTransport.h.
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Quadrupole polarizability.
Definition at line 519 of file GasTransport.h.