Abstract The dynamics involved in powder mixing remains a topic of interest for many researchers; however the theory still remains underdeveloped. Most of the mixers are still designed and scaled up on empirical basis. In many industries, including pharmaceutical, the majority of blending is performed using “tumbling mixers”. Tumbling mixers are hollow containers which are partially loaded with materials and rotated for some number of revolutions. Some common examples include horizontal drum mixers, v-blenders, double cone blenders and bin blenders. In all these mixers while homogenization in the direction of rotation is fast, mediated by a convective mixing process, mixing in the horizontal (axial) direction, driven by a dispersive process, is often much slower. In this paper, we experimentally investigate a new tumbling mixer that rotates with respect to two axes: a horizontal axis (tumbling motion), and a central symmetry axis (spinning motion). A detailed study is conducted on mixing performance of powders and the effect of critical fundamental parameters including blender geometry, speed, fill level, presence of baffles, loading pattern, and axis of rotation. In this work Acetaminophen is used as the active pharmaceutical ingredient and the formulation contains commonly used excipients such as Avicel and Lactose. The mixing efficiency is characterized by extracting samples after pre-determined number of revolutions, and analyzing them using Near Infrared Spectroscopy to determine compositional distribution. Results show the importance of process variables including the axis of rotation on homogeneity of powder blends.
[1]
Troy Shinbrot,et al.
V-blender segregation patterns for free-flowing materials: effects of blender capacity and fill level.
,
2004,
International journal of pharmaceutics.
[2]
B Buisson,et al.
A model of surface renewal with application to the coating of pharmaceutical tablets in rotary drums
,
2003
.
[3]
Fernando J. Muzzio,et al.
A study of the mixing and segregation mechanisms in the Bohle Tote blender via DEM simulations
,
2006
.
[4]
Jpk Seville,et al.
The effect of binder viscosity on particle agglomeration in a low shear mixer/agglomerator
,
2000
.
[5]
Gene R. Woodle,et al.
Particle motion and mixing in a rotary kiln
,
1993
.
[6]
J. Davidson,et al.
The no-flow problem for granular material in rotating kilns and dish granulators
,
2000
.
[7]
Richard Turton,et al.
The scale-up of spray coating processes for granular solids and tablets
,
2005
.
[8]
Julio M. Ottino,et al.
Radial segregation of granular mixtures in rotating cylinders
,
1997
.
[9]
Troy Shinbrot,et al.
Powder technology in the pharmaceutical industry: the need to catch up fast
,
2002
.
[10]
Fernando J. Muzzio,et al.
Quantitative characterization of mixing of free-flowing granular material in tote (bin)-blenders
,
2002
.
[11]
Fernando J. Muzzio,et al.
Characterizing mixing and lubrication in the Bohle Bin blender
,
2006
.
[12]
Julio M. Ottino,et al.
Transverse flow and mixing of granular materials in a rotating cylinder
,
1997
.