Doxygen update
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2 changed files with 123 additions and 38 deletions
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@ -54,11 +54,9 @@ namespace Cantera {
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m_cond(0),
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m_molefracs(0),
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m_poly(0),
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m_astar_poly(0),
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m_bstar_poly(0),
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m_cstar_poly(0),
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m_om22_poly(0),
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m_astar(0, 0),
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m_bstar(0, 0),
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m_cstar(0, 0),
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m_om22(0, 0),
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@ -116,11 +114,9 @@ namespace Cantera {
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m_cond(0),
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m_molefracs(0),
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m_poly(0),
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m_astar_poly(0),
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m_bstar_poly(0),
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m_cstar_poly(0),
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m_om22_poly(0),
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m_astar(0, 0),
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m_bstar(0, 0),
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m_cstar(0, 0),
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m_om22(0, 0),
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@ -191,11 +187,9 @@ namespace Cantera {
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m_cond = right.m_cond;
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m_molefracs = right.m_molefracs;
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m_poly = right.m_poly;
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m_astar_poly = right.m_astar_poly;
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m_bstar_poly = right.m_bstar_poly;
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m_cstar_poly = right.m_cstar_poly;
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m_om22_poly = right.m_om22_poly;
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m_astar = right.m_astar;
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m_bstar = right.m_bstar;
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m_cstar = right.m_cstar;
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m_om22 = right.m_om22;
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@ -425,6 +419,7 @@ namespace Cantera {
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sum2 += m_molefracs[k] / m_cond[k];
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}
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m_lambda = 0.5*(sum1 + 1.0/sum2);
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m_condmix_ok = true;
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}
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return m_lambda;
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}
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@ -443,14 +438,30 @@ namespace Cantera {
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}
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}
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//===================================================================================================================
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/**
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* @param ndim The number of spatial dimensions (1, 2, or 3).
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* @param grad_T The temperature gradient (ignored in this model).
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* @param ldx Leading dimension of the grad_X array.
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// Get the species diffusive mass fluxes wrt to the mass averaged velocity,
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// given the gradients in mole fraction and temperature
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/*
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* Units for the returned fluxes are kg m-2 s-1.
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*
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*
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* The diffusive mass flux of species \e k is computed from
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* \f[
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* \vec{j}_k = -n M_k D_k \nabla X_k.
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* \vec{j}_k = -n M_k D_k \nabla X_k.
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* \f]
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*
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* @param ndim Number of dimensions in the flux expressions
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* @param grad_T Gradient of the temperature
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* (length = ndim)
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* @param ldx Leading dimension of the grad_X array
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* (usually equal to m_nsp but not always)
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* @param grad_X Gradients of the mole fraction
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* Flat vector with the m_nsp in the inner loop.
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* length = ldx * ndim
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* @param ldf Leading dimension of the fluxes array
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* (usually equal to m_nsp but not always)
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* @param fluxes Output of the diffusive mass fluxes
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* Flat vector with the m_nsp in the inner loop.
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* length = ldx * ndim
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*/
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void MixTransport::getSpeciesFluxes(int ndim,
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const doublereal* grad_T, int ldx, const doublereal* grad_X,
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@ -608,7 +619,7 @@ namespace Cantera {
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}
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else {
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for (k = 0; k < m_nsp; k++) {
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m_cond[k] = m_sqrt_t*dot5(m_polytempvec, m_condcoeffs[k]);
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m_cond[k] = m_sqrt_t * dot5(m_polytempvec, m_condcoeffs[k]);
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}
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}
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m_spcond_ok = true;
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@ -653,7 +664,6 @@ namespace Cantera {
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* Update the pure-species viscosities.
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*/
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void MixTransport::updateSpeciesViscosities() {
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int k;
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if (m_mode == CK_Mode) {
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for (k = 0; k < m_nsp; k++) {
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@ -664,13 +674,12 @@ namespace Cantera {
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else {
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for (k = 0; k < m_nsp; k++) {
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// the polynomial fit is done for sqrt(visc/sqrt(T))
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m_sqvisc[k] = m_t14*dot5(m_polytempvec, m_visccoeffs[k]);
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m_visc[k] = (m_sqvisc[k]*m_sqvisc[k]);
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m_sqvisc[k] = m_t14 * dot5(m_polytempvec, m_visccoeffs[k]);
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m_visc[k] = (m_sqvisc[k] * m_sqvisc[k]);
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}
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}
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m_spvisc_ok = true;
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}
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//====================================================================================================================
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/*
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* Update the temperature-dependent viscosity terms.
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@ -37,11 +37,44 @@ namespace Cantera {
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class GasTransportParams;
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/**
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* Class MixTransport implements mixture-averaged transport
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* properties for ideal gas mixtures. The model is based on that
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* described by Kee, Coltrin, and Glarborg, "Theoretical and
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* Practical Aspects of Chemically Reacting Flow Modeling."
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//! Class MixTransport implements mixture-averaged transport properties for ideal gas mixtures.
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/*!
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* The model is based on that described by Kee, Coltrin, and Glarborg, "Theoretical and
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* Practical Aspects of Chemically Reacting Flow Modeling."
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*
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*
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* The viscosity is computed using the Wilke mixture rule (kg /m /s)
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*
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* \f[
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* \mu = \sum_k \frac{\mu_k X_k}{\sum_j \Phi_{k,j} X_j}.
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* \f]
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*
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* Here \f$ \mu_k \f$ is the viscosity of pure species \e k, and
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*
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* \f[
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* \Phi_{k,j} = \frac{\left[1
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* + \sqrt{\left(\frac{\mu_k}{\mu_j}\sqrt{\frac{M_j}{M_k}}\right)}\right]^2}
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* {\sqrt{8}\sqrt{1 + M_k/M_j}}
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* \f]
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*
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*
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* The thermal conductivity is computed from the following mixture rule:
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* \f[
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* \lambda = 0.5 \left( \sum_k X_k \lambda_k + \frac{1}{\sum_k X_k/\lambda_k} \right)
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* \f]
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*
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* It's used to compute the flux of energy due to a thermal gradient
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*
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* \f[
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* j_T = - \lambda \nabla T
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* \f]
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*
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* The flux of energy has units of energy (kg m2 /s2) per second per area.
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*
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* The units of lambda are W / m K which is equivalent to kg m / s^3 K.
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*
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*
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*/
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class MixTransport : public Transport {
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@ -53,6 +86,7 @@ namespace Cantera {
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MixTransport();
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public:
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//!Copy Constructor for the %MixTransport object.
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/*!
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* @param right %LiquidTransport to be copied
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@ -92,9 +126,25 @@ namespace Cantera {
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return cMixtureAveraged;
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}
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//! Viscosity of the mixture
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//! Viscosity of the mixture (kg /m /s)
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/*!
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* The viscosity is computed using the Wilke mixture rule (kg /m /s)
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*
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* \f[
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* \mu = \sum_k \frac{\mu_k X_k}{\sum_j \Phi_{k,j} X_j}.
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* \f]
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*
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* Here \f$ \mu_k \f$ is the viscosity of pure species \e k, and
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*
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* \f[
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* \Phi_{k,j} = \frac{\left[1
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* + \sqrt{\left(\frac{\mu_k}{\mu_j}\sqrt{\frac{M_j}{M_k}}\right)}\right]^2}
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* {\sqrt{8}\sqrt{1 + M_k/M_j}}
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* \f]
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*
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* @return Returns the viscosity of the mixture ( units = Pa s = kg /m /s)
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*
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* @see updateViscosity_T();
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*/
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virtual doublereal viscosity();
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@ -161,20 +211,25 @@ namespace Cantera {
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virtual void update_T();
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virtual void update_C();
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//! Get the species diffusive mass fluxes wrt to
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//! the mass averaged velocity,
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//! Get the species diffusive mass fluxes wrt to the mass averaged velocity,
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//! given the gradients in mole fraction and temperature
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/*!
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* Units for the returned fluxes are kg m-2 s-1.
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*
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* @param ndim Number of dimensions in the flux expressions
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* @param grad_T Gradient of the temperature
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* (length = ndim)
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* @param ldx Leading dimension of the grad_X array
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* (usually equal to m_nsp but not always)
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* @param grad_X Gradients of the mole fraction
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* Flat vector with the m_nsp in the inner loop.
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* length = ldx * ndim
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*
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*
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* The diffusive mass flux of species \e k is computed from
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* \f[
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* \vec{j}_k = -n M_k D_k \nabla X_k.
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* \f]
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*
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* @param ndim Number of dimensions in the flux expressions
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* @param grad_T Gradient of the temperature
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* (length = ndim)
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* @param ldx Leading dimension of the grad_X array
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* (usually equal to m_nsp but not always)
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* @param grad_X Gradients of the mole fraction
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* Flat vector with the m_nsp in the inner loop.
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* length = ldx * ndim
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* @param ldf Leading dimension of the fluxes array
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* (usually equal to m_nsp but not always)
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* @param fluxes Output of the diffusive mass fluxes
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@ -250,20 +305,41 @@ namespace Cantera {
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// property values
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DenseMatrix m_bdiff;
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//! vector of species viscosities
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//! vector of species viscosities (kg /m /s)
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/*!
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* These are used in wilke's rule to calculate the viscosity of the solution
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* length = m_kk
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*/
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vector_fp m_visc;
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//! vector of square root of species viscosities sqrt(kg /m /s)
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/*!
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* These are used in wilke's rule to calculate the viscosity of the solution
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* length = m_kk
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*/
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vector_fp m_sqvisc;
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vector_fp m_cond;
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//! vector of species thermal conductivities (W/m /K)
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/*!
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* These are used in wilke's rule to calculate the viscosity of the solution
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* units = W /m /K = kg m /s^3 /K.
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* length = m_kk
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*/
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vector_fp m_cond;
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//! Vector of species molefractions
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array_fp m_molefracs;
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/*!
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* These are processed so that all mole fractions are >= MIN_X
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* Length = m_kk
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*/
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vector_fp m_molefracs;
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std::vector<std::vector<int> > m_poly;
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std::vector<vector_fp > m_astar_poly;
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std::vector<vector_fp > m_bstar_poly;
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std::vector<vector_fp > m_cstar_poly;
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std::vector<vector_fp > m_om22_poly;
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DenseMatrix m_astar;
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DenseMatrix m_bstar;
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DenseMatrix m_cstar;
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DenseMatrix m_om22;
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