Flow of lubricated granular material on an inclined plane

2025-05-06 0 0 559.69KB 21 页 10玖币
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Flow of lubricated granular material on an inclined
plane
Ravindra S. Ghodakea,c, Pankaj Doshib,
, Ashish V. Orpea,c,
aChemical Engineering and Process Development Division, CSIR-National Chemical
Laboratory, Pune 411008 India
bWorldwide Research and Development, Pfizer Products India Private Limited, Mumbai
400051 India
cAcademy of Scientific and Innovative Research (AcSIR), Ghaziabad 201002 India
Abstract
We have studied the gravity driven flow of spherical shaped, millimetric sized
granular material coated with aspherical, micron-sized, near frictionless lubri-
cant particles. Experiments were performed on an inclined plane using two
different sized particles for varying concentrations of the lubricant. The par-
ticle volumetric flow rate exhibits a non-monotonic behavior with increasing
lubricant concentration. It shows an increase at smaller lubricant concentration
followed by a decrease at higher lubricant concentration. The lubricant parti-
cles adheres to the granular particle surface thereby reducing the inter-particle
friction. However, presence of lubricant particles at higher concentration damps
out inter-particle collision thereby reducing the inter-particle momentum trans-
fer. Non-monotonicity in the observed behavior is then conjectured to arise
due to competing effects of inter-particle friction and inter-particle collision.
The present work and the overall observed behavior therein provides a simple
experimental system to characterise the effects of added lubricant material in
pharmaceutical and other relevant industrial applications.
Keywords: granular, powder, lubrication, friction, inclined plane
Corresponding authors
Email addresses: pankaj.doshi@pfizer.com (Pankaj Doshi), av.orpe@ncl.res.in
(Ashish V. Orpe)
Preprint submitted to Powder Technology October 24, 2022
arXiv:2210.11758v1 [cond-mat.soft] 21 Oct 2022
1. Introduction
Can we simply alter the inter-particle interaction, a fundamental quantity
governing the overall behavior in a dry granular system? Doing so essentially
will require either some kind of chemistry to alter the particle surface or altering
the material itself. Both these methods will change the inter-particle friction
and collision characteristics thereby modifying the flow. However, both the
methods pose restrictions in terms of material availability and limited scope
and ease in use of chemical treatment. Alternatively, DEM simulations allow
for studying dry granular systems by suitable tuning of inter-particle friction
and collisional properties [1, 2, 3]. But the technique still presents limitations
in terms of availability of experimental studies for a detailed comparison in spite
of several reported studies [4]
As it turns out, addition of plate-like particles (typically Magnesium Stearate
or MgSt) alters the inter-particle interactions in dry systems substantially [5].
This technique is used routinely in pharmaceutical industries handling granular
material in various forms. The primary aim is to reduce the friction in the com-
pression die during the process of tablet compaction. As an additional benefit
the presence of MgSt also enhances the powder flowability. Typically, the MgSt
powder is added in tiny quantities (weight ratio of O[102]). The individual
particles, about 10 micron sized, adhere to the large particles and are expected
to reduce the friction between them due to their own frictionless nature thereby
enhancing the flowability. This flowability, using MgSt as lubricant, has been
studied previously to a reasonable effect [6, 7, 8, 9, 10, 11, 12]. However, all
these studies have primarily focused on characterising the optimality in terms
of lubricant concentration vis-a-vis flow characteristics. One of them have also
focussed on studying the avalanching and angle of repose behavior of pharma-
ceutical powders in presence of various types of lubricants [10]. It was observed
that the addition of lubricant decreases the angle of repose and the time for
avalanching. The observed behavior was explained based on particle morphol-
ogy using scanning electron microscopy (SEM) imaging. On the other hand
2
usage of powder as a lubricant between two planar solid surfaces is very well
known within the domain of tribology and its merits and demerits with respect
to conventional liquid lubricants have been well documented [13]. However, the
carryover of the flow [14, 15] and rheology [16] characteristics from these planar
surface studies to bulk flow of lubricant-granular particles is not known.
Over here we attempt to connect the presence of lubricant particles, their
influence on the inter-particle interactions and eventually on the shear flow
behavior in terms of flow and concentration profiles using flow visualization
techniques. Given that MgSt particles are soft in nature, their excessive presence
and effectively higher coating on the larger particles can render the latter to be
soft, thereby inducing a higher loss of momentum during collisions. This may
effectively nullify the advantage gained due to friction reducing properties of
the lubricant. We strive to understand these possible contrasting behaviors
in this work through detailed experimentation. To obtain the necessary shear
flow, we have chosen chute (inclined plane) system, which is very well studied
in literature [4, 17, 1, 18, 2, 19, 20, 21] covering various flow aspects and is,
moreover, simple in its handling and usage. The choice of the experimental
system is purely incidental and the purpose of this work is not to delve into
the details of inclined plane mechanics, but simply to create a shear flow which
will allow for studying and understanding the lubricant influence on the flow
behavior.
2. Methodology
Experiments are performed on a chute inclined at an angle (θ) as shown in
fig. 1. The system comprises two sections. The uppermost section of length
450 mm, width 50 mm and height 400 mm functions as a hopper filled with
granular material. The rest of the section, of length 1350 mm, width 50 mm
and height 200 mm, functions as a chute. The material from the hopper flows
on to the chute through a gap of height 30 mm which can be opened or closed
using a manually operated gate. The side walls of the entire system are made
3
Figure 1: Schematic of the chute flow system. (a) Side view exhibiting hopper, chute, collection
system and relevant dimensions. (b) Imaging of the flow at one of the chute side wall (c)
Sample image captured using a high speed camera. See text for more details
out of stainless steel (SS316), except for a transparent acrylic window of length
600 mm and height 200 mm, located downstream (600 mm from chute end) for
imaging the flow. The base of the chute (of width 50 mm) is made from glass
and is roughened by gluing glass beads of desired diameter (d) on it.
Nearly spherical glass beads (Jaygo Inc., USA) of diameter d= 2 and 3 mm,
with a polydispersity of 15% are used as granular material, while Magnesium
Stearate (MgSt) powder (Loba Chemie, India) is used as a lubricant material.
The individual particles of MgSt powder have plate-like structure, equivalent
sphere volume diameter of 10 µm with polydispersity of 10% and are nearly
frictionless with respect to each other. For each experiment, a pre-defined, but
very tiny, quantity of MgSt powder was mixed with granular beads of either
size in a mixer. The mixer comprises an open plastic tank (diameter 185 mm
and height 100 mm) fitted with an overhead stirrer. The mixing, for each
experiment, was carried out by rotating the stirrer at a speed of 30 revolutions
per minute (rpm) over a duration of 5 minutes. The glass beads were colored
4
using blue ink (Camlin Inc.) for ease in imaging and analysis. The MgSt powder,
white in color and slightly cohesive in nature, adheres itself to the surface of the
glass beads during the mixing process. The weight ratio of MgSt to glass beads
was varied between O(105) and O(103) across all experiments. For a given
weight ratio, the lubricant concentration was defined cl=Ml/Ap, where Mlis
the total mass of lubricant, Ap=d2is the total surface area of particles, dis
particle diameter and nis the number of particles. The value of nis determined
as (6d3)(Mpp), where Mpis total mass of particles, ρpis the particle density
(2.5g/cm3) and Mppis the total particle volume.
Given the tiny amounts of added MgSt powder and the small size of indi-
vidual particles, it was not possible to quantify the homogeneity of mixing as
well as any loss of MgSt powder in the mixing vessel. We, thus, resorted to
visual inspection, ensuring that the mixed material has whitish appearance and
no obvious traces were left on the mixer wall and stirrer surface. To ensure
consistency of the mixture, the mixing procedure, including mixing time and
speed, was maintained constant across all the experiments. The surface of par-
ticles after mixing with lubricant was imaged using FE-SEM (Field Emission
Scanning Electron Microscopy) to confirm the altered texture and the adherence
of the lubricant. Figure 2 shows the images of 3 mm glass beads at two differ-
ent magnifications for three different lubricant concentrations. A clean surface
is visible in fig. 2b which gets progressively patchy with increasing lubricant
concentration as seen in fig. 2d and f. Multiple layers of lubricant are visible
at the highest lubricant concentration. Similar surface texture variation is also
observed for 2 mm glass beads (not shown).
For every experiment, the chute hopper was filled upto 25% of its total
volume with the mixture of glass beads and MgSt while keeping the opening
closed. This ensured adequate supply of continuous feed to achieve steady flow
for reasonable duration in the experiment. The gate was opened manually to
allow gravity induced flow of material down the chute surface. Given that
our primary objective was to study the effect of lubricant on the flow and not
chute flow mechanics, we kept all the operating parameters constant throughout,
5
摘要:

FlowoflubricatedgranularmaterialonaninclinedplaneRavindraS.Ghodakea,c,PankajDoshib,,AshishV.Orpea,c,aChemicalEngineeringandProcessDevelopmentDivision,CSIR-NationalChemicalLaboratory,Pune411008IndiabWorldwideResearchandDevelopment,P zerProductsIndiaPrivateLimited,Mumbai400051IndiacAcademyofScienti ...

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