Herein, we present a theoretical model of the VPNS rolling upstream along a microfluidic channel when a flow is applied. The micro swarm model is simplified to a thin-walled rigid disc of radius R and thickness t rotating about its normal. Observations and experiments show that upstream motion is possible when the linear velocity at the edge of the VPNS exceeds the fluid velocity. At an input magnetic field of 100 Hz, the rotational velocity of the micro swarm is considerably higher than the translational velocity, which implies the existence of a highly thin lubricated fluid layer at the contact area between the VPNS and the wall instead of pure rolling under dry friction. When the VPNS reaches the boundary layer, it is subject to multiple forces, as shown in Fig. S23. The low Reynolds number (
Re =
ρfUf ·
Lc/
μ = 0.1099) and low swarm-mass-to-fluid-viscosity ratio under these experimental conditions enabled the dynamics to become overdamped; hence, the VPNS operating under a super-viscous fluid was in a forced equilibrium [
21]. From a lateral view, the propulsive force
Ff due to wet friction being balanced by the viscous drag
FD of the fluid along the translation direction of the VPNS, where
FD = 6
πμR(
Up −
Uf)
f1(
h,
R), considering the disc shape of the VPNS and the small gap against the wall
f1(
h,
R). The additional term for the viscous drag is modified [
33] to
, where
Up and
Uf denote the upstream velocity of the VPNS and the fluid velocity at the center of mass, respectively. The balanced equation for the forces in the horizontal direction is
Ff =
FD. The forces experienced in the direction perpendicular to the propagation are more complex. At low Re, the time-reversal [
5] motion of the VPNS produces no net propulsion, and it requires a break in the symmetry of the rotational motion, its structure, or the surrounding geometry [
30]. The counterflow motion of VPNS in the experiment is mainly achieved by breaking the geometric symmetry during the rotational motion, close to the wall, and the irregular rheology. The Magnus effect (Fig. S24) indicates that both a rotating cylinder [
34] and a parallel linear stream with an annular flow around a cylinder [
35] produce a lateral lift on the cylinder, thereby causing it to move in a transverse direction; the schematic diagram of VPNS moving toward the wall is shown in Fig.
4A. The lift is due to the inconsistent flow rate between the 2 sides of the object, thus creating a lift from the high-pressure zone to the low-pressure zone. These forces are denoted by
FRLand
FSL in Fig. S23. In an application of this study, the lateral force
FRL generated by the rotation drags the VPNS toward the pipe wall, whereas the lateral force
FSL generated by the shear flow tends to push the VPNS away from the pipe wall. In 1965, Saffman et al. [
26] demonstrated that the lift force generated by rotation is approximately one order of magnitude smaller than the shear, except when the particle rotates at a considerably faster speed than the shear. This precisely satisfies the conditions for the upstream mobility of the VPNS. Thus, the agreement between the experimental and numerical analysis results validates the theory. Figure
4B shows the side view in which the VPNS is moving toward the wall by the Magnus force, and this allows the VPNS to reach the low flow velocity boundary layer in the vessel, thus triggering upstream migration. Figure
4C shows the simulation of this process with the help of finite-element software, the VPNS rotating at high speed in the blood flow is considered as a rigid disc, and the lateral force generated by its rotation drags the VPNS to the vessel surface while generating vortices around it.