Commit 25269a4e authored by Sina Ackermann's avatar Sina Ackermann Committed by Simon Emmert

[doxygen] Add missing citations in tests and handbook.bib

parent f3b086d4
......@@ -1772,3 +1772,68 @@ url = {http://www.sciencedirect.com/science/article/pii/0094454874901507},
doi = {10.2514/6.1992-439},
url = {http://dx.doi.org/10.2514/6.1992-439}
}
@book{Donea2003,
title={Finite element methods for flow problems},
author={Donea, Jean and Huerta, Antonio},
year={2003},
publisher={John Wiley \& Sons}
}
@inproceedings{Angeli2017,
title={FVCA8 Benchmark for the Stokes and Navier--Stokes Equations with the TrioCFD Code—Benchmark Session},
author={Angeli, P-E and Puscas, M-A and Fauchet, G and Cartalade, A},
booktitle={International Conference on Finite Volumes for Complex Applications},
pages={181--202},
year={2017},
organization={Springer}
}
@InProceedings{Kovasznay1948,
author = {Kovasznay, L. I. G.},
title = {Laminar flow behind a two-dimensional grid},
booktitle = {Mathematical Proceedings of the Cambridge Philosophical Society},
year = {1948},
volume = {44},
pages = {58--62},
organization = {Cambridge Univ Press},
}
@PHDTHESIS{Class2001,
author = {H. Class},
title = {{Theorie und numerische Modellierung nichtisothermer Mehrphasenprozesse in NAPL-kontaminierten por"osen Medien}},
school = {Universit\"at Stuttgart},
year = {2001}
}
@Article{Shi2011,
author={Shi, J. X. and Wang, J. H.},
title={A Numerical Investigation of Transpiration Cooling with Liquid Coolant Phase Change},
journal={Transport in Porous Media},
year={2011},
volume={87},
number={3},
pages={703--716},
doi={10.1007/s11242-010-9710-9},
url={https://doi.org/10.1007/s11242-010-9710-9}
}
@article{nagel2014,
title={The influence of gas--solid reaction kinetics in models of thermochemical heat storage under monotonic and cyclic loading},
author={Nagel, T and Shao, H and Ro{\ss}kopf, C and Linder, M and W{\"o}rner, A and Kolditz, O},
journal={Applied Energy},
volume={136},
pages={289--302},
year={2014},
publisher={Elsevier}
}
@article{shao2013,
title={{Non-equilibrium thermo-chemical heat storage in porous media: Part 2--A 1D computational model for a calcium hydroxide reaction system}},
author={Shao, H and Nagel, T and Ro{\ss}kopf, C and Linder, M and W{\"o}rner, A and Kolditz, O},
journal={Energy},
volume={60},
pages={271--282},
year={2013},
publisher={Elsevier}
}
......@@ -19,7 +19,8 @@
/*!
* \file
* \ingroup NavierStokesTests
* \brief Test for the instationary staggered grid Navier-Stokes model with analytical solution (Angeli et al., 2017).
* \brief Test for the instationary staggered grid Navier-Stokes model
* with analytical solution (Angeli et al. 2017, \cite Angeli2017).
*/
#include <config.h>
......
......@@ -19,7 +19,8 @@
/*!
* \file
* \ingroup NavierStokesTests
* \brief Test for the instationary staggered grid Navier-Stokes model with analytical solution (Angeli et al., 2017)
* \brief Test for the instationary staggered grid Navier-Stokes model
* with analytical solution (Angeli et al. 2017, \cite Angeli2017).
*/
#ifndef DUMUX_ANGELI_TEST_PROBLEM_HH
......@@ -74,7 +75,7 @@ struct EnableGridVolumeVariablesCache<TypeTag, TTag::AngeliTest> { static conste
/*!
* \ingroup NavierStokesTests
* \brief Test problem for the staggered grid (Angeli 1947).
* \brief Test problem for the staggered grid (Angeli et al. 2017, \cite Angeli2017).
*
* The unsteady, 2D, incompressible Navier-Stokes equations for a zero source and a Newtonian
* flow is solved and compared to an analytical solution (sums/products of trigonometric functions).
......
......@@ -19,7 +19,7 @@
/*!
* \file
* \ingroup NavierStokesTests
* \brief Test for the staggered grid Navier-Stokes model (Kovasznay 1947).
* \brief Test for the staggered grid Navier-Stokes model (Donea 2003, \cite Donea2003).
*/
#include <config.h>
......
......@@ -19,7 +19,7 @@
/*!
* \file
* \ingroup NavierStokesTests
* \brief Stationary test for the staggered grid Navier-Stokes model (Kovasznay 1947).
* \brief Stationary test for the staggered grid Navier-Stokes model (Kovasznay 1948, \cite Kovasznay1948).
*/
#include <config.h>
......
......@@ -37,7 +37,7 @@ namespace Components {
*
* This class uses a different CaO density. It is to be used for calculating the
* chemical reaction of CaO to Ca(OH)2 without considering the porosity change
* according to See Shao et al. (2013).
* according to Shao et al. (2013) \cite shao2013.
*/
template <class Scalar>
class ModifiedCaO : public Components::CaO<Scalar>
......@@ -46,11 +46,14 @@ public:
/*!
* \brief The corrected mass density \f$\mathrm{[kg/m^3]}\f$ of CaO.
*
* This density is to be used for calculating the chemical reaction
* of CaO to Ca(OH)2 without considering the solid volume change.
* See Shao et al. (2013) \cite shao2013.
*/
static Scalar solidDensity(Scalar temperature)
{
return 1656;
// This density is to be used for calculating the chemical reaction of CaO to Ca(OH)2 without considering the solid volume change. See Shao et al. (2013)
}
};
......
......@@ -21,7 +21,7 @@
* \ingroup OnePNCMinTests
* \brief Class for the evaluation of the reaction rate of Calciumoxide to Halciumhydroxide
*
* It contains simple and advanced reaction kinetics according to Nagel et al. (2014).
* It contains simple and advanced reaction kinetics according to Nagel et al. (2014) \cite nagel2014.
*/
#ifndef DUMUX_THERMOCHEM_REACTION_HH
......@@ -33,13 +33,13 @@ namespace Dumux {
* \ingroup OnePNCMinTests
* \brief Class for the evaluation of the reaction rate of Calciumoxide to Halciumhydroxide
*
* It contains simple and advanced reaction kinetics according to Nagel et al. (2014).
* It contains simple and advanced reaction kinetics according to Nagel et al. (2014) \cite nagel2014.
*/
class ThermoChemReaction {
public:
/*!
* \brief Evaluates the reaction kinetics (see Nagel et al. 2014)
* \brief Evaluates the reaction kinetics (see Nagel et al. 2014 \cite nagel2014).
*/
template<class VolumeVariables>
typename VolumeVariables::PrimaryVariables::value_type
......@@ -239,6 +239,6 @@ public:
};
} // namespace Dumux
} // end namespace Dumux
#endif
......@@ -96,13 +96,10 @@ struct FluidSystem<TypeTag, TTag::Kuevette>
* for the mass components and the enthalpy), aimed at remediating an initial
* NAPL (Non-Aquoeus Phase Liquid) contamination in the heterogeneous domain.
* The contamination is initially placed partly into the coarse sand
* and partly into a fine sand lense.
* and partly into a fine sand lens.
*
* This simulation can be varied through assigning different boundary conditions
* at the left boundary as described in Class (2001):
* Theorie und numerische Modellierung nichtisothermer Mehrphasenprozesse in
* NAPL-kontaminierten por"osen Medien, Dissertation, Eigenverlag des Instituts
* f"ur Wasserbau
* at the left boundary as described in \cite Class2001.
*
* This problem uses the \ref ThreePThreeCModel and \ref NIModel model.
*
......
......@@ -44,8 +44,7 @@ namespace FluidSystems {
*
* \brief A two-phase fluid system with water as sole component.
*
* Values are taken from Shi & Wang, A numerical investigation of transpiration
* cooling with liquid coolant phase change, Transport in Porous Media, 2011
* Values are taken from Shi and Wang, 2011 \cite Shi2011.
*/
template <class Scalar>
class CombustionFluidsystem
......
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