#import "@preview/charged-ieee:0.1.3": ieee

#show: ieee.with(
  title: [Stokes flow - Particle interaction in low Reynolds Number environments],
  abstract: [
    This report describes the key overview of creeping flow, also called Stokes Flow, in the context of particle-particle and particle-fluid
    interactions relevant to porous media behaviour. Beginning from the Navier-Stokes equations, the transition to the Stokes Flow is assumed
    by a low Reynolds number $"Re"$. Solutions and more modern approaches are reviewed, including the lubrication effects and near-contact
    dynamics. The influence of these interactions on clogging and permeability reduction are discussed, followed by a brief overview of
    intended modelling techniques such as the Lattice-Boltzmann-Method(LBM), the Immersed Boundary Method(IBM) and the Homogenized Lattice-Boltzmann
    -Method(HLBM).
  ],
  authors: (
    (
      name: "Claudius Holeksa",
      department: [CSSR],
      organization: [NORCE Research AS],
      location: [Bergen, Norway],
      email: "clho@norceresearch.no"
    ),
  ),
  index-terms: ("Fluid Mechanics", "Review"),
  bibliography: bibliography("refs.bib"),
  figure-supplement: [Fig.],
)

= Introduction

Flow in porous subsurface structures often is dominated by extremely low velocity and high viscous fluids with low Reynolds numbers $"Re" << 1$.
In such a condition, the flow enters a state called the Stokes Flow or creeping flow, where inertial forces can be assumed to be zero and viscous
forces dominate the whole connected set.
This kind of flow is found in geological processes, in carbohydrate recovery, filtration systems and CO_2 storage where the pore-scale motion
of particles and their interaction with the surrounding porous medium strongly influence macroscopic properties such as the permeability of
rock layers.
Undestanding particle transport, bridging and in general clogging phenomena is critical for the effective use and management of subsurface
reservoirs.
The tiniest changes can alter the established path in a porous geometry and transport behaviour over time.
Thus, the behaviour of individual particles in Stokes Flow form the foundation upon which complex processes such as particle accumulation
in porous structures.

The study of the Stokes Flow has a long history, beginning with Stokes' study of flow past a rigid sphere@stokes1851.\
Subsequent work expanded his work to include a multitude of shapes and the interaction of multiple particles, different geometries and
boundary other conditions.
More recently, research was performed in the understanding of creeping flow, the particle transport and the clogging associated with it, and how those microscopic properties impact the macroscopic development. These carry implications which are essential in water treatment, medicine,
carbohydrate recovery and CO2 storage. // CITE

This report delves into the central aspects governing the known behaviour of Stokes Flow and the key extension results towards past single and multiple spheres.
Explores the effect of it in porous media and examines the more recent particle bridging behaviour found in porous structures.


== Stokes Flow

// Write about Navier
The incompressible Navier Stokes equations are a set of equations defined with the density $rho$, the dynamic viscosity $mu$ and the
velocity field $u(x,t)$

#math.equation(
block: true,
$ ρ((∂)/(∂t)u + (u · ∇)u) = −∇p + μ∇²u + f,\
∇ · u = 0 $
)

While we are often interested in Navier-Stokes flows, a generalized analytical solution does not exist,
most analytical approaches rely on a set of restrictions or assumptions.
With the Reynolds number defined by
$ "Re" = (rho U L ) / mu
$

Luckily we decided to work on a fluid which tends $"Re" arrow 0$ or at least $"Re" << 1$ where due to the viscous forces
the inertial term is negligable and is assumed to be zero.
Which is why we arrive at this term

// Stokes
#math.equation(
block: true,
$ μ∇²u + f = ∇p,\
∇ · u = 0 $
)

An additional restriction by the creeping flow equations is the selection of boundary criteria where it depends on
an infinite space with a set solid boundary interface.
For simplicity a no-slip boundary condition is selected for the solid boundary.

#math.equation(
block: true,
$ v = U "at particles boundary",\
v arrow 0 "as" |x| arrow infinity
$
)

== Solid-Fluid single sphere interaction with Stokes flow

With the previous assumptions a solid sphere of radius $r$ moving with a relative velocity $v$ in an unbounded creeping flow,
we receive the drag force provided by Stokes

#math.equation(
block: true,
$ F_S = 6 pi mu r v $
)

with our boundary conditions specified as

#math.equation(
block: true,
$ u = v "at" a = r,\
u arrow 0 "as" a arrow infinity
$
)

where according to Proudman and Pearson@proudman_pearson_1957 at a Reynolds number of 0.05 the predicted drag is two percent lower
than the possibly more correct value by Proudman and Pearson@proudman_pearson_1957.

//#math.equation(
//block: true,
//$ F = F_S ( 1 + (3/8)"Re" + (9/40)("Re")^2 * (log "Re" + gamma + (5/3) log 2 - (323/360)) + (27/80)*"Re"^3 log "Re" ) $
//)

//Using spherical coordinates $(r,theta,phi.alt)$ and no external force we receive the velocity components

//#math.equation(
//block: true,
//$ v_r = U cos theta (1- (3r)/(2a) + r^3 / (2a^3)) $
//$ v_theta = - U cos theta (1- (3r)/(4a) + r^3 / (4a^3)) $
//)

== Lubrication Forces for Near Contact

When spheres or a sphere near a straight wall approach each other with a small separation $h<<r$ the flow in the gap is dominated by
lubrication forces. For a sphere approaching a straight wall with velocity $U$ normal to the wall we
have 

#math.equation(
block: true,
$ F_(L) tilde.eq (6 pi mu r^2 U) / h (1-(9h)/(16r) + ...) $
)

With two spheres of equal radius r and otherwise the same conditions approaching

#math.equation(
block: true,
$ F_(L) tilde.eq (6 pi mu r^2 U) / h (1-(h)/(5r) + ...) $
)

These forces diverge the smaller $h$ becomes.
This is due to the viscous stress increasing on small films of
fluid which then in turn dominate the interaction.

== Clogging of porous structures

Modifying a poiseulle channel flow by narrowing the channel we can observe mainly three different ways how the porosity is reduced.
By sieving, bridging and aggregation of surface deposition.
The least interesting phenomenon is sieving which results purely from a single particle having a too large of a volume to fit into the
pore. While bridiging occurs when multiple particles arrive at a passage at the exact time, forming a stable arch which blocks the flow.  
Aggregation involves the deposition of particles gradually  narrowing the channel.
And while sieving and bridging results from purely mechanical forces aggregation results from electrostatic interactions between particles, the fluid and surface boundaries at micrometer scales@laurez2025bridging.


== Discusion

The arches resulting from clogging are often inherently unstable, but with the progression of aggregation arrive at less unstable states.
Which in turn makes a stochastic analysis of particles in different conditions@laurez2025bridging based on different widths feasible.

Laurez@laurez2025bridging goes into detail based on CITE FIG how probable clogging mechanisms are, while these are quite indepth, opportunities
in relation to multiphase fluid interaction with the solid structures.
An interesting case 


// Insert png

== Lattice-Boltzmann-Method

=== Immersed Boundary Method

=== Homogenized Lattice-Boltzmann