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Solve the rigid-short-fibers rheology constitutive models by two approaches numerically:
Spherical Harmonics approach;
Object Tensor approach.
Spherical Harmonic method capable of obtaining the 3D orientation distribution $\psi(\mathbf{p})$ and 3D fiber tumbling trajactories $\mathbf{p}(t)$, while Tensor Method couldn't.
Benke Li, Ying Guo, Paul Steeman, Markus Bulters, Wei Yu. "Wall effect on the rheology of short-fiber suspensions under shear." Journal of Rheology 2021, 65 (6), 1169–1185.
Then open the .ipynb files in the jupyter workspace, enjoy it. Usage of jupyter could be found in https://jupyter.org/.
The models were solved by: (a) object tensor approach (see examples in .ipynb files with the prefix of Demo_Tensor Method_), and (b) spherical harmonics approach (see examples in .ipynb files with prefix of Demo_SH Method_).
Background of models and spherical harmonic methods is shown in the following sections.
For rigid-short-fibers filled suspensions, their microsopic transient behaviors were mosted interested in two aspects:
Evolution of orientation distributions during flow, denoted as $\dot{\psi}(\mathbf{p})$ or $\frac{\mathrm{d}\psi(\mathbf{p})}{\mathrm{d}t}$. With the definition of the second moment as $\mathbf{A}=\oint\psi(\mathbf{p})\mathbf{pp}\mathrm{d}\mathbf{p}$, the evolution of tensor is denoted as $\mathbf{\dot{A}}$ or $\frac{\mathrm{d}\mathbf{A}}{\mathrm{d}t}$.
Rotation of single fiber during flow, denoted as $\mathbf{\dot{p}}$ or $\frac{\mathrm{d}\mathbf{p}}{\mathrm{d}t}$.
The evolution of the $\dot{\psi}(\mathbf{p})$ can be written as the flux of $\psi$ (orientation probability distribution):
Here $\mathbf{\nabla}_s$ is the surface gradient operator (Ref: Bird, R. B. et. al. "Dynamics of Polymeric Liquids. Vol. 1: Fluid Mechanics." Wiley, New York, 1987.). It could be written in the following form:
HD term (hydro dynamic term), also known as Jefferey term. (Ref: Jeffery, G. B., “The motion of ellipsoidal particles immersed in a viscous fluid.” Proc. R. Soc. London A1922, 102, 161–179.) Written as:
$$\begin{equation}
\begin{aligned}
\dot{\psi}^{HD}&=-\mathbf{\nabla}_s\cdot(\mathbf{\dot{p}}^{HD}\psi)\\\
\mathbf{\dot{A}}^{HD}&=+\mathbf{W}\cdot\mathbf{A}-\mathbf{A}\cdot\mathbf{W}+\xi(\mathbf{D}\cdot\mathbf{A}+\mathbf A\cdot\mathbf D-2\mathbb{A}_4:\mathbf D) \\\
\mathbf{\dot{p}}^{HD} &= +\mathbf{W}\cdot\mathbf{p}+\xi\left(\mathbf{D}\cdot\mathbf{p}-\mathbf{D}:\mathbf{ppp}\right)\\\
where \quad \mathbf{D}&=\frac{1}{2}(\mathbf{L}-\mathbf{L}^\mathrm{ T }) \\\
and \quad \mathbf{W}&=\frac{1}{2}(\mathbf{L}-\mathbf{L}^\mathrm{ T }) \\\
and \quad \mathbf{L}&=\mathbf{\mathit{\nabla v}} \\\
and \quad \xi&=\frac{a_r^2-1}{a_r^2+1}
\end{aligned}
\end{equation}$$
(1-3)
IRD term (isotropic diffusion term), also known as FT term. (Ref: Folgar, F., and C. L. Tucker, “Orientation behavior of fibers in concentrated suspensions.” J. Reinf. Plast. Compos.1984, 3, 98–119.) Written as:
ARD or iARD term (anisotropic diffusion term), introduced for slender fibers with a large aspect ratio. (Refs: Phelps, J. H. et. al. “An anisotropic rotary diffusion model for fiber orientation in short- and long-fiber thermoplastics.” J. Non-Newtonian Fluid Mech.2009, 156, 165–176. Tseng, H.-C. et. al. “An objective tensor to predict anisotropic fiber orientation in concentrated suspensions.” J. Rheol.2016, 60, 215–224.) Written as:
RSC term (reduced strain closure term), introduced to slow down the evolution of fiber orientation. (Ref: Wang, J. et. al. “An objective model for slow orientation kinetics in concentrated fiber suspensions: Theory and rheological evidence.” J. Rheol.2008, 52, 1179–1200.) Written as:
$$\begin{equation}
\begin{aligned}
\dot{\psi}^{RSC}&=-\mathbf{\nabla}_s\cdot(\mathbf{q})\\\
\mathbf{\dot{A}}^{RSC}&=-(1-\kappa)\sum^3_{i=1}\dot{\lambda}_i^{IRD/iARD}\mathbf{e}_i\mathbf{e}_i\\\
\mathbf{\dot{p}}^{RSC}&=-\frac{\mathbf{q}}{\psi} \\\
where \quad
\mathbf{q}&=\sum^3_{i=1}\beta_i(\mathbf{e}_i\mathbf{e}_i\cdot\mathbf{p}-\mathbf{e}_i\mathbf{e}_i:\mathbf{ppp})\\\
and \quad
\beta_i&=-\frac{5(1-\kappa)}{4\pi}\left[\xi(\lambda_i\mathbf{D}:\mathbf{e}_i\mathbf{e}_i-\mathbf{e}_i\mathbf{e}_i:\mathbb{A}_4:\mathbf{D})+C_I\dot\gamma(1-3\lambda_i)\right]
\end{aligned}
\end{equation}$$
Confined Term (Proposed in our on-going studies. Here $\mathbf{D}^*$ is the confinement induced virtual compression flow, while $\epsilon$ and $\alpha$ is the tunning parameter.
Ref: Montgomery-Smith, S.et. al. “A systematic approach to obtaining numerical solutions of Jeffery’s type equations using spherical harmonics.” Compos. Part A2010, 41, 827–835.
Expand the orientation distribution function $\psi(t)$ as spherical harmonics series:
Expand the above equation (2-2) by Math Operators of special function $Y_l^m$
These operators were defined in the source file: models/sph_harm_operator.py
$\qquad$ Here $\mathrm{d}s$ is the spherical surface unit, and $\mathrm{d}s=\sin\theta \mathrm{d}\theta \mathrm{d}\phi$.For $Y_l^m$ functions, the spherical surface integration results $\iint Y_l^m \mathrm{d}s$ is always zero except $\iint Y_0^0 \mathrm{d}s$. And:
$\qquad$ Here the coeficient $2\sqrt{\pi}$ depends on the normalization method during spherical harmonic calculations. Substitute the equation (2-1) and (2-3) to equation (2-4), with applying Mathematica, details see the source file Sph_Harm_Operators.nb, we got:
$\qquad$ Practically, this integration was applied the Guass-Legendre quadrature method. $\qquad$ Comparison of the spherical harmonic methods' results with the analytic solution of IRD model (or FT model), here the $Y_l^m$ expansion degree here is 100:
Fiber tumbling trajectory $\mathbf{p}(t)$, with parameter of $C_I=0.01,C_M=0,\kappa=1,\xi=1$, and $Y_l^m$ expansion degree is 100.
Influence of $Y_l^m$ expansion degree to the tumbling period. It seems that expansion degree of 50 could provide enough calculation precision.
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Solve the rigid-short-fibers rheology constitutive models by both spherical harmonics approach and object tensor approach numerically.