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Cantera · Jul 28, 2023 · becbad1 · becbad1
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Showing 10 changed files with 12 additions and 12 deletions.
diff --git 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
@@ -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
@@ -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
@@ -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
@@ -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
@@ -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
@@ -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
@@ -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
@@ -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
@@ -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