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Replace \log by \ln

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This commit is contained in:
Ingmar Schoegl 2023-08-06 08:46:45 -05:00
parent d951bd5ee6
commit 38b76a0476
6 changed files with 10 additions and 10 deletions
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2
include/cantera/equil/vcs_solve.h
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@ -820,7 +820,7 @@ private:
* We are checking the equation:
*
* sum_u = sum_j_comp [ sigma_i_j * u_j ]
* = u_i_O + \log((AC_i * W_i)/m_tPhaseMoles_old)
* = u_i_O + \ln((AC_i * W_i)/m_tPhaseMoles_old)
*
* by first evaluating:
*

4
include/cantera/thermo/DebyeHuckel.h
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@ -443,7 +443,7 @@ public:
* pure species phases which exhibit zero volume expansivity:
* @f[
* \hat s(T, P, X_k) = \sum_k X_k \hat s^0_k(T)
* - \hat R \sum_k X_k \log(X_k)
* - \hat R \sum_k X_k \ln(X_k)
* @f]
* The reference-state pure-species entropies
* @f$ \hat s^0_k(T,p_{ref}) @f$ are computed by the
@ -575,7 +575,7 @@ public:
* For this phase, the partial molar entropies are equal to the SS species
* entropies plus the ideal solution contribution:
* @f[
* \bar s_k(T,P) = \hat s^0_k(T) - R \log(M0 * molality[k])
* \bar s_k(T,P) = \hat s^0_k(T) - R \ln(M0 * molality[k])
* @f]
* @f[
* \bar s_{solvent}(T,P) = \hat s^0_{solvent}(T)

2
include/cantera/thermo/HMWSoln.h
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@ -835,7 +835,7 @@ public:
* exhibit zero volume expansivity:
* @f[
* \hat s(T, P, X_k) = \sum_k X_k \hat s^0_k(T)
* - \hat R \sum_k X_k \log(X_k)
* - \hat R \sum_k X_k \ln(X_k)
* @f]
* The reference-state pure-species entropies @f$ \hat s^0_k(T,p_{ref}) @f$
* are computed by the species thermodynamic property manager. The pure

6
include/cantera/thermo/IdealSolidSolnPhase.h
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@ -89,7 +89,7 @@ public:
* partial molar volume solution mixture with pure species phases which
* exhibit zero volume expansivity:
* @f[
* \hat s(T, P, X_k) = \sum_k X_k \hat s^0_k(T) - \hat R \sum_k X_k \log(X_k)
* \hat s(T, P, X_k) = \sum_k X_k \hat s^0_k(T) - \hat R \sum_k X_k \ln(X_k)
* @f]
* The reference-state pure-species entropies
* @f$ \hat s^0_k(T,p_{ref}) @f$ are computed by the species thermodynamic
@ -104,7 +104,7 @@ public:
* constant partial molar volume solution mixture with pure species phases
* which exhibit zero volume expansivity:
* @f[
* \hat g(T, P) = \sum_k X_k \hat g^0_k(T,P) + \hat R T \sum_k X_k \log(X_k)
* \hat g(T, P) = \sum_k X_k \hat g^0_k(T,P) + \hat R T \sum_k X_k \ln(X_k)
* @f]
* The reference-state pure-species Gibbs free energies
* @f$ \hat g^0_k(T) @f$ are computed by the species thermodynamic
@ -338,7 +338,7 @@ public:
* are equal to the pure species entropies plus the ideal solution
* contribution.
* @f[
* \bar s_k(T,P) = \hat s^0_k(T) - R \log(X_k)
* \bar s_k(T,P) = \hat s^0_k(T) - R \ln(X_k)
* @f]
* The reference-state pure-species entropies,@f$ \hat s^{ref}_k(T) @f$, at
* the reference pressure, @f$ P_{ref} @f$, are computed by the species

4
include/cantera/thermo/LatticePhase.h
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@ -227,7 +227,7 @@ public:
* For an ideal, constant partial molar volume solution mixture with
* pure species phases which exhibit zero volume expansivity:
* @f[
* \hat s(T, P, X_k) = \sum_k X_k \hat s^0_k(T) - \hat R \sum_k X_k \log(X_k)
* \hat s(T, P, X_k) = \sum_k X_k \hat s^0_k(T) - \hat R \sum_k X_k \ln(X_k)
* @f]
* The reference-state pure-species entropies @f$ \hat s^0_k(T,p_{ref}) @f$
* are computed by the species thermodynamic property manager. The pure
@ -395,7 +395,7 @@ public:
* are equal to the pure species entropies plus the ideal solution
* contribution.
* @f[
* \bar s_k(T,P) = \hat s^0_k(T) - R \log(X_k)
* \bar s_k(T,P) = \hat s^0_k(T) - R \ln(X_k)
* @f]
* The reference-state pure-species entropies,@f$ \hat s^{ref}_k(T) @f$, at
* the reference pressure, @f$ P_{ref} @f$, are computed by the species

2
include/cantera/thermo/LatticeSolidPhase.h
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@ -364,7 +364,7 @@ public:
* are equal to the pure species entropies plus the ideal solution
* contribution.
* @f[
* \bar s_k(T,P) = \hat s^0_k(T) - R \log(X_k)
* \bar s_k(T,P) = \hat s^0_k(T) - R \ln(X_k)
* @f]
* The reference-state pure-species entropies,@f$ \hat s^{ref}_k(T) @f$, at
* the reference pressure, @f$ P_{ref} @f$, are computed by the species