Fix miscellaneous spelling errors

This commit is contained in:
Ray Speth 2016-12-28 00:14:13 -05:00
parent 3014b7af89
commit 4669b9cf5a
4 changed files with 8 additions and 8 deletions

View file

@ -374,7 +374,7 @@ public:
* \f[
* \vec{i} = \sum_{i} z_i F \rho \vec{V_i} / W_i
* \f]
* where \f$ z_i \f$ is the charge on species i, \f$ F \f$ is Faradays
* where \f$ z_i \f$ is the charge on species i, \f$ F \f$ is Faraday's
* constant, \f$ \rho \f$ is the density, \f$ W_i \f$ is the molecular mass
* of species i. The conductance, \f$ \kappa \f$ is obtained from
* \f[
@ -391,7 +391,7 @@ public:
* \f[
* \vec{i} = \sum_{i} z_i F \rho \vec{V_i} / W_i
* \f]
* where \f$ z_i \f$ is the charge on species i, \f$ F \f$ is Faradays
* where \f$ z_i \f$ is the charge on species i, \f$ F \f$ is Faraday's
* constant, \f$ \rho \f$ is the density, \f$ W_i \f$ is the molecular mass
* of species \c i.
*

View file

@ -442,7 +442,7 @@ int ChemEquil::equilibrate(thermo_t& s, const char* XYstr,
// first get the property values at the upper and lower temperature
// limits. Since p1 (h, s, or u) is monotonic in T, these values
// determine the upper and lower bounnds (phigh, plow) for p1.
// determine the upper and lower bounds (phigh, plow) for p1.
s.setTemperature(tmax);
setInitialMoles(s, elMolesGoal, loglevel - 1);
@ -517,7 +517,7 @@ int ChemEquil::equilibrate(thermo_t& s, const char* XYstr,
}
} else {
// Calculate initial estimates of the element potentials. This algorithm
// uese the MultiPhaseEquil object's initialization capabilities to
// uses the MultiPhaseEquil object's initialization capabilities to
// calculate an initial estimate of the mole fractions for a set of
// linearly independent component species. Then, the element potentials
// are solved for based on the chemical potentials of the component

View file

@ -110,7 +110,7 @@ DebyeHuckel& DebyeHuckel::operator=(const DebyeHuckel& b)
// This is an internal shallow copy of the PDSS_Water pointer
m_waterSS = dynamic_cast<PDSS_Water*>(providePDSS(0));
if (!m_waterSS) {
throw CanteraError("DebyHuckel::operator=()", "Dynamic cast to waterPDSS failed");
throw CanteraError("DebyeHuckel::operator=()", "Dynamic cast to waterPDSS failed");
}
m_densWaterSS = b.m_densWaterSS;

View file

@ -4,7 +4,7 @@
*
* Transport parameters are calculated using corresponding states models:
* Binary diffusion coefficients use the generalized chart described by
* Takahashi, et al. and viscosity calcualtions use the Lucas method.
* Takahashi, et al. and viscosity calculations use the Lucas method.
* All methods are described in Reid, Prausnitz, and Polling, "The Properties
* of Gases and Liquids, 4th ed., 1987 (viscosity in Ch. 9, Thermal
* conductivity in Ch. 10, and Diffusion coefficients in Ch. 11).
@ -247,7 +247,7 @@ void HighPressureGasTransport::getMultiDiffCoeffs(const size_t ld, doublereal* c
m_bindiff_ok = false; // m_bdiff is overwritten by the above routine.
// Having corrected m_bdiff for pressure and concentration effects, the
// routine now procedes the same as in the low-pressure case:
// routine now proceeds the same as in the low-pressure case:
// evaluate L0000 if the temperature or concentrations have
// changed since it was last evaluated.
@ -324,7 +324,7 @@ doublereal HighPressureGasTransport::viscosity()
// Calculate contribution to quantum correction term.
// SCD Note: This assumes the species of interest (He, H2, and D2) have
// been named in this specific way. They are perhaps the most obvious
// names, butit would of course be preferred to have a more general
// names, but it would of course be preferred to have a more general
// approach, here.
std::vector<std::string> spnames = m_thermo->speciesNames();
if (spnames[i] == "He") {