diff --git a/include/cantera/kinetics/BlowersMaselRate.h b/include/cantera/kinetics/BlowersMaselRate.h index 238dd28958..b359ead54e 100644 --- a/include/cantera/kinetics/BlowersMaselRate.h +++ b/include/cantera/kinetics/BlowersMaselRate.h @@ -40,7 +40,7 @@ struct BlowersMaselData : public ReactionData //! Blowers Masel reaction rate type depends on the enthalpy of reaction /** - * The Blowers Masel approximation \cite blowers2004 adjusts the activation energy + * The Blowers Masel approximation @cite blowers2004 adjusts the activation energy * based on enthalpy change of a reaction: * * \f{eqnarray*}{ diff --git a/include/cantera/kinetics/Falloff.h b/include/cantera/kinetics/Falloff.h index c6e35be0a9..8c43f9c7f6 100644 --- a/include/cantera/kinetics/Falloff.h +++ b/include/cantera/kinetics/Falloff.h @@ -508,9 +508,9 @@ class SriRate final : public FalloffRate * * References: * * Example of reaction database developed by Tsang utilizing this format - * \cite tsang1991 + * @cite tsang1991 * * Example of Chemkin implementation of Tsang format (supplemental materials) - * \cite lucassen2011 + * @cite lucassen2011 * * @ingroup falloffGroup */ diff --git a/include/cantera/kinetics/InterfaceRate.h b/include/cantera/kinetics/InterfaceRate.h index 7df0270865..a342bc04c5 100644 --- a/include/cantera/kinetics/InterfaceRate.h +++ b/include/cantera/kinetics/InterfaceRate.h @@ -63,7 +63,7 @@ struct InterfaceData : public BlowersMaselData //! Base class for rate parameterizations that involve interfaces /** * Rate expressions defined for interfaces may include coverage dependent terms, - * where an example is given by Kee, et al. \cite kee2003, Eq 11.113. + * where an example is given by Kee, et al. @cite kee2003, Eq 11.113. * Using %Cantera nomenclature, this expression can be rewritten as * \f[ * k_f = A T^b \exp \left( - \frac{E_a}{RT} \right) diff --git a/include/cantera/thermo/PlasmaPhase.h b/include/cantera/thermo/PlasmaPhase.h index 2494b588c9..8dbe7cebb9 100644 --- a/include/cantera/thermo/PlasmaPhase.h +++ b/include/cantera/thermo/PlasmaPhase.h @@ -45,7 +45,7 @@ namespace Cantera * where \f$ i \f$ is the index of energy levels. * * For references, see Gudmundsson @cite gudmundsson2001; Khalilpour and Foroutan - * @cite khalilpour2020; and Hagelaar and Pitchford @cite hagelaar2005. + * @cite khalilpour2020; Hagelaar and Pitchford @cite hagelaar2005, and BOLOS * @cite BOLOS. * * @warning This class is an experimental part of %Cantera and may be diff --git a/include/cantera/thermo/WaterPropsIAPWSphi.h b/include/cantera/thermo/WaterPropsIAPWSphi.h index ee028c69cc..5b2da13dff 100644 --- a/include/cantera/thermo/WaterPropsIAPWSphi.h +++ b/include/cantera/thermo/WaterPropsIAPWSphi.h @@ -25,7 +25,7 @@ namespace Cantera * and classes \link Cantera::WaterSSTP WaterSSTP\endlink and * \link Cantera::PDSS_Water PDSS_Water\endlink). * - * The reference is Wagner and Pruss \cite wagner2002. + * The reference is Wagner and Pruss @cite wagner2002. * * Units Note: This class works with reduced units exclusively. */ diff --git a/include/cantera/transport/GasTransport.h b/include/cantera/transport/GasTransport.h index b6f83958c2..34666fd4cd 100644 --- a/include/cantera/transport/GasTransport.h +++ b/include/cantera/transport/GasTransport.h @@ -19,7 +19,7 @@ class MMCollisionInt; //! Class GasTransport implements some functions and properties that are //! shared by the MixTransport and MultiTransport classes. //! -//! For details, see Kee, et al. \cite kee2003 and \cite kee2017. +//! For details, see Kee, et al. @cite kee2003 and @cite kee2017. //! //! @ingroup tranprops class GasTransport : public Transport diff --git a/include/cantera/transport/IonGasTransport.h b/include/cantera/transport/IonGasTransport.h index c0fee918fb..0780e98b38 100644 --- a/include/cantera/transport/IonGasTransport.h +++ b/include/cantera/transport/IonGasTransport.h @@ -27,7 +27,7 @@ namespace Cantera * due to resonant charge transfer. Therefore, an experimental collision * data is used instead. * - * Data taken from \cite prager2005. + * Data taken from @cite prager2005. * * @ingroup tranprops */ diff --git a/include/cantera/transport/MixTransport.h b/include/cantera/transport/MixTransport.h index c4e36da012..bfee27295e 100644 --- a/include/cantera/transport/MixTransport.h +++ b/include/cantera/transport/MixTransport.h @@ -19,7 +19,7 @@ namespace Cantera //! Class MixTransport implements mixture-averaged transport properties for //! ideal gas mixtures. /*! - * The model is based on that described in Kee, et al. \cite kee2003. + * The model is based on that described in Kee, et al. @cite kee2003. * * The viscosity is computed using the Wilke mixture rule (kg /m /s) * diff --git a/include/cantera/transport/MultiTransport.h b/include/cantera/transport/MultiTransport.h index 1fe17397eb..b89d1658c0 100644 --- a/include/cantera/transport/MultiTransport.h +++ b/include/cantera/transport/MultiTransport.h @@ -18,7 +18,7 @@ namespace Cantera //! ideal gas mixtures. /*! * The implementation generally follows the procedure outlined in Kee, et al. - * \cite kee2003. + * @cite kee2003. * * @ingroup tranprops */ diff --git a/include/cantera/transport/WaterTransport.h b/include/cantera/transport/WaterTransport.h index a3e2c82cb6..bb85b447bb 100644 --- a/include/cantera/transport/WaterTransport.h +++ b/include/cantera/transport/WaterTransport.h @@ -40,7 +40,7 @@ class WaterTransport : public Transport * This function calculates the value of the viscosity of pure water at the * current T and P. * - * The formulas used are from Sengers and Watson \cite sengers1986. + * The formulas used are from Sengers and Watson @cite sengers1986. * * The formulation is accurate for all temperatures and pressures, for steam * and for water, even near the critical point. Pressures above 500 MPa and @@ -58,7 +58,7 @@ class WaterTransport : public Transport * This function calculates the value of the thermal conductivity of water * at the current T and P. * - * The formulas used are from Sengers and Watson \cite sengers1986. + * The formulas used are from Sengers and Watson @cite sengers1986. * * The formulation is accurate for all temperatures and pressures, for steam * and for water, even near the critical point. Pressures above 500 MPa and