Model of Laakkonen et al. (2006). The total breakup rate is calculated by. More...

Inheritance diagram for LaakkonenAlopaeusAittamaa:

Collaboration diagram for LaakkonenAlopaeusAittamaa:

Public Member Functions
	TypeName ("LaakkonenAlopaeusAittamaa")

	LaakkonenAlopaeusAittamaa (const populationBalanceModel &popBal, const dictionary &dict)

virtual	~LaakkonenAlopaeusAittamaa ()=default

virtual void	setBreakupRate (volScalarField &breakupRate, const label i)

Public Member Functions inherited from breakupModel
	TypeName ("breakupModel")

	declareRunTimeSelectionTable (autoPtr, breakupModel, dictionary,(const populationBalanceModel &popBal, const dictionary &dict),(popBal, dict))

	breakupModel (const populationBalanceModel &popBal, const dictionary &dict)

autoPtr< breakupModel >	clone () const

virtual	~breakupModel ()=default

const populationBalanceModel &	popBal () const

const autoPtr< daughterSizeDistributionModel > &	dsdPtr () const

autoPtr< daughterSizeDistributionModel > &	dsdPtr ()

virtual void	correct ()

Additional Inherited Members
Static Public Member Functions inherited from breakupModel
static autoPtr< breakupModel >	New (const word &modelType, const populationBalanceModel &popBal, const dictionary &dict)

Protected Attributes inherited from breakupModel
const populationBalanceModel &	popBal_

dictionary	dict_

autoPtr< daughterSizeDistributionModel >	dsd_

Detailed Description

Model of Laakkonen et al. (2006). The total breakup rate is calculated by.

$C_1 \epsilon_c^{1/3} \mathrm{erfc} \left( \sqrt { C_2 \frac{\sigma}{\rho_c \epsilon_c^{2/3} (6v_i/\pi)^{5/9}} + C_3 \frac{\mu_c}{\sqrt{\rho_c \rho_d} \epsilon_c^{1/3} (6v_i/\pi)^{4/9}} } \right)$

where

$\sigma$	=	Surface tension [N/m]
	=	Volume of mother bubble i [m]
$\epsilon_c$	=	Turbulent dissipation rate of continuous phase [m2/s3]
$\mu_c$	=	Molecular dynamic viscosity of liquid phase [Pa s]
$\rho_c$	=	Density of continuous phase [kg/m3]
$\rho_d$	=	Density of disperse phase [kg/m3]

References:

        Laakkonen, M., Alopaeus, V., & Aittamaa, J. (2006).
        Validation of bubble breakage, coalescence and mass transfer models for
        gas-liquid dispersion in agitated vessel.
        Chemical engineering science, 61(1), 218-228.
        Eq. 2-3, p. 220.

Usage

Property	Description	Required	Default value
`C1`	coefficient C1	no	6.0
`C2`	coefficient C2	no	0.04
`C3`	coefficient C3	no	0.01
`daughterSizeDistributionModel`	inh. from breakupModel	inherited

Source files

Definition at line 141 of file LaakkonenAlopaeusAittamaa.H.

Constructor & Destructor Documentation

◆ LaakkonenAlopaeusAittamaa()

LaakkonenAlopaeusAittamaa	(	const populationBalanceModel &	popBal,
		const dictionary &	dict
	)

Definition at line 50 of file LaakkonenAlopaeusAittamaa.C.

◆ ~LaakkonenAlopaeusAittamaa()

virtual ~LaakkonenAlopaeusAittamaa ( )

virtualdefault

Member Function Documentation

◆ TypeName()

TypeName ( "LaakkonenAlopaeusAittamaa" )

◆ setBreakupRate()

void setBreakupRate	(	volScalarField &	breakupRate,
		const label	i
	)

virtual

Implements breakupModel.

Definition at line 75 of file LaakkonenAlopaeusAittamaa.C.

References Foam::cbrt(), sizeGroup::d(), Foam::erfc(), phaseModel::mu(), sizeGroup::phase(), Foam::pow(), phaseModel::rho(), and Foam::sqrt().

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The documentation for this class was generated from the following files:

src/phaseSystemModels/reactingEuler/multiphaseSystem/populationBalanceModel/breakupModels/LaakkonenAlopaeusAittamaa/LaakkonenAlopaeusAittamaa.H
src/phaseSystemModels/reactingEuler/multiphaseSystem/populationBalanceModel/breakupModels/LaakkonenAlopaeusAittamaa/LaakkonenAlopaeusAittamaa.C

Public Member Functions