PrinceBlanch.H
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25
26Class
27 Foam::diameterModels::coalescenceModels::PrinceBlanch
28
29Description
30 Model of Prince and Blanch (1990). The coalescence rate is calculated by
31
32 \f[
33 \left( \theta_{ij}^{T} + \theta_{ij}^{B} + \theta_{ij}^{LS} \right)
34 \lambda_{ij}
35 \f]
36
37 with the coalescence efficiency
38
39 \f[
40 \lambda_{ij} =
41 \mathrm{exp}
42 \left(
43 - \sqrt{\frac{r_{ij}^3 \rho_c}{16 \sigma}}
44 \mathrm{ln} \left(\frac{h_0}{h_f}\right)
45 \epsilon_c^{1/3}/r_{ij}^{2/3}
46 \right)\;,
47 \f]
48
49 the turbulent collision rate
50
51 \f[
52 \theta_{ij}^{T} =
53 C_1 \pi (d_i + d_j)^{2} \epsilon_c^{1/3}
54 \sqrt{d_{i}^{2/3} + d_{j}^{2/3}}\;,
55 \f]
56
57 and the buoyancy-driven collision rate
58
59 \f[
60 \theta_{ij}^{B} = S_{ij} \left| u_{ri} - u_{rj} \right|\;,
61 \f]
62
63 where the rise velocity of bubble i is calculated by
64
65 \f[
66 u_{ri} = \sqrt{2.14 \sigma / \left(\rho_c d_i \right) + 0.505 g d_i}\;,
67 \f]
68
69 the equivalent radius by
70
71 \f[
72 r_{ij} = \left( \frac{1}{d_i} + \frac{1}{d_j} \right)^{-1}
73 \f]
74
75 and the collision cross sectional area by
76
77 \f[
78 S_{ij} = \frac{\pi}{4} \left(d_i + d_j\right)^{2}\;.
79 \f]
80
81 Note that in equation 2, the bubble radius has been substituted by the
82 bubble diameter. Also the expression for the equivalent radius r_ij
83 (equation 19 in the paper of Prince and Blanch (1990)) was corrected.
84 The collision rate contribution due to laminar shear in the continuous phase
85 is currently neglected.
86
87 \vartable
88 \theta_{ij}^{T} | Turbulent collision rate [m3/s]
89 \theta_{ij}^{B} | Buoyancy-driven collision rate [m3/s]
90 \theta_{ij}^{LS} | Laminar shear collision rate [m3/s]
91 \lambda_{ij} | Coalescence efficiency [-]
92 r_{ij} | Equivalent radius [m]
93 \rho_c | Density of continuous phase [kg/m3]
94 \sigma | Surface tension [N/m]
95 h_0 | Initial film thickness [m]
96 h_f | Critical film thickness [m]
97 \epsilon_c | Continuous phase turbulent dissipation rate [m2/s3]
98 d_i | Diameter of bubble i [m]
99 d_j | Diameter of bubble j [m]
100 u_{ri} | Rise velocity of bubble i [m/s]
101 S_{ij} | Collision cross sectional area [m2]
102 g | Gravitational constant [m/s2]
103 \endvartable
104
105 Reference:
106 \verbatim
107 Prince, M. J., & Blanch, H. W. (1990).
108 Bubble coalescence and break‐up in air‐sparged bubble columns.
109 AIChE journal, 36(10), 1485-1499.
110 \endverbatim
111
112Usage
113 \table
114 Property | Description | Required | Default value
115 C1 | coefficient C1 | no | 0.089
116 h0 | initial film thickness | no | 1e-4m
117 hf | critical film thickness | no | 1e-8m
118 turbulence | Switch for collisions due to turbulence | yes | none
119 buoyancy | Switch for collisions due to buoyancy | yes | none
120 laminarShear | Switch for collisions due to laminar shear | yes | none
121 \endtable
122
123SourceFiles
124 PrinceBlanch.C
125
126\*---------------------------------------------------------------------------*/
127
128#ifndef PrinceBlanch_H
129#define PrinceBlanch_H
130
131#include "coalescenceModel.H"
132
133// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
134
135namespace Foam
136{
137namespace diameterModels
138{
139namespace coalescenceModels
140{
141
142/*---------------------------------------------------------------------------*\
143 Class PrinceBlanch Declaration
144\*---------------------------------------------------------------------------*/
145
146class PrinceBlanch
147:
148 public coalescenceModel
149{
150 // Private data
151
152 //- Optional coefficient C1, defaults to 0.089
154
155 //- Initial film thickness, defaults to 1e-4m
157
158 //- Critical film thickness, defaults to 1e-8m
160
161 //- Switch for considering turbulent collisions
162 Switch turbulence_;
163
164 //- Switch for considering buoyancy-induced collisions
165 Switch buoyancy_;
166
167 //- Switch for considering buoyancy-induced collisions
168 Switch laminarShear_;
169
170
171public:
172
173 //- Runtime type information
174 TypeName("PrinceBlanch");
175
176 // Constructor
177
179 (
180 const populationBalanceModel& popBal,
181 const dictionary& dict
182 );
183
184
185 //- Destructor
186 virtual ~PrinceBlanch() = default;
187
188
189 // Member Functions
190
191 //- Add to coalescenceRate
192 virtual void addToCoalescenceRate
193 (
194 volScalarField& coalescenceRate,
195 const label i,
196 const label j
197 );
198};
199
200
201// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
202
203} // End namespace coalescenceModels
204} // End namespace diameterModels
205} // End namespace Foam
206
207// * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * //
208
209#endif
210
211// ************************************************************************* //
A simple wrapper around bool so that it can be read as a word: true/false, on/off,...
Definition: Switch.H:78
Base class for coalescence models.
Model of Prince and Blanch (1990). The coalescence rate is calculated by.
Definition: PrinceBlanch.H:243
virtual void addToCoalescenceRate(volScalarField &coalescenceRate, const label i, const label j)
Add to coalescenceRate.
Definition: PrinceBlanch.C:96
TypeName("PrinceBlanch")
Runtime type information.
PrinceBlanch(const populationBalanceModel &popBal, const dictionary &dict)
Definition: PrinceBlanch.C:59
Class that solves the univariate population balance equation by means of a class method (also called ...
A list of keyword definitions, which are a keyword followed by a number of values (eg,...
Definition: dictionary.H:126
Namespace for OpenFOAM.
dimensioned< scalar > dimensionedScalar
Dimensioned scalar obtained from generic dimensioned type.
GeometricField< scalar, fvPatchField, volMesh > volScalarField
Definition: volFieldsFwd.H:82
dictionary dict
#define TypeName(TypeNameString)
Declare a ClassName() with extra virtual type info.
Definition: typeInfo.H:73