Granulation of hydrophobic powders
Graphical abstract
Nucleation can occur by the “solid spreading” nucleation mechanism where particles spread around a template drop to form a “liquid marble”. This paper describes single drop solid-spreading nucleation experiments where the formation of the powder shell is observed. Experimental results and observations for some model systems are presented, together with a preliminary framework for liquid marble formation.
Introduction
Wet granulation is a particle size enlargement process where small particles are agglomerated using a liquid binder to form larger granules. Traditional reasons for granulating a material include improving flow and handling properties, increasing bulk density, reducing dust formation, and reducing segregation of materials [1]. More recently, granulation is motivated by a desire to design structured agglomerates for specialty products such as pharmaceuticals, controlled dissolution detergents and “instant” food powders such as sauces [2]. Problems during granulation of specialty products can cause enormous downstream processing problems and product that does not meet regulatory and quality specifications.
Great progress has being made in understanding and controlling granulation mechanisms (e.g. [3], [4], [5], [6]) focusing on producing granules with a consistent, reproducible size distribution. This understanding has been applied to many industrial granulation processes, including pharmaceuticals [7], and detergents [8], [5] to improve their performance. However, granulation of poorly wetting powders has not been addressed in the above works but is commonly performed in pharmaceutical, minerals and fertilizer granulation.
Granulation of hydrophobic powders is frequently required in the pharmaceutical industry. The structural complexity of new drug molecules mean that is increasingly common for entire classes of drug compounds to be poorly wetting (contact angles approx 70–90°) or highly hydrophobic (contact angle ≥ 90°). The poor wetting properties can create considerable difficulty in understanding, controlling and trouble-shooting these industrial granulation processes.
A surfactant is often added to the granulation fluid and/or powders to improve the wetting characteristics of the formulation but this is not possible in some applications such as iron ore granulation or certain pharmaceutical formulations due to either the cost of the surfactant or chemical interactions that may occur. For these industries, the current body of granulation theory is often not applicable, as it is inherently assumed in all current granulation research that the liquid must wet the powder in order for granulation to be successful. We review below the state of knowledge of hydrophobic powder granulation.
Section snippets
Granulation of hydrophobic powders
The contact angle is defined as the internal angle formed by a liquid drop placed on a solid surface at the three phase contact line [9]. Measuring contact angles on powders are generally difficult and the reliable experimental methods have been recently reviewed [10]. In this paper, a hydrophobic powder system is defined as a powder or combination of powders which have a contact angle with the granulating fluid greater than 90°.
The contact angle of the system directly affects the
Experimental
A loosely packed powder bed was formed by lightly sieving the powder into a petri dish and scraping level to produce a smooth powder surface. A loosely packed bed approximates the powder state in an agitated granulator [34]. A 100 μl Hamilton precision syringe with a 22 gauge needle was positioned just above the bed surface. Drops (4 μl volume) were allowed to detach and gently fall 1–2 mm before landing on the bed surface. This distance was selected to minimize drop bouncing and rolling, and
Results
Experiments initially focused on screening material combinations to find suitable systems for further study. Table 3 summarizes the experimental observations and some pictures of liquid marbles are shown in Fig. 5. Water was able to form a liquid marble with all the powders tested, and glycerol was able to form liquid marbles with all powders except ethoxybenzamide. The addition of 1%SDS surfactant to the water eliminated liquid marble formation by reducing the contact angle below 90° allowing
Discussion
The solid-over-liquid spreading coefficient λSL [16] may provide a quantitative method to predict whether a given formulation will form liquid marbles. However, our results also suggest that bulk motion of the drop, due either to rolling or impact, is required for solid-spreading nucleation to occur. It is also possible that solid-spreading motion is driven entirely by a physical flow mechanism (refer to Fig. 2), where the degree of surface coverage is proportional to the size of the bulk flow
Conclusion
We report here the first stage of ongoing work studying the granulation of hydrophobic powders by the solid-spreading nucleation mechanism [17]. Several combinations of hydrophobic powders and fluids have been shown to exhibit solid-spreading nucleation and to form “liquid marbles” [30], [31]. The liquid marble structure seems superficially consistent with the long established spreading coefficients [16], although we also propose an alternate mechanism where bulk motion within the drop creates
Nomenclature
- Bo
Bond Number representing dimensionless ratio of gravity forces to surface tension forces acting on a drop (B0 = ρgR2R2/γLV)
- dd
Diameter of the droplet (m)
- dp
Diameter of the particle (m)
- F
Fraction of powder component in Eq. (1) (−)
- G
Gravitational acceleration (9.8 m2/s)
- Oh
Ohnesorge number representing dimensionless ratio of viscosity and surface tension (Oh = μ/(ρLγLVR)0.5)
- R
Drop radius ( = dd/2)
- V
Velocity of the fluid drop (m/s)
- We
Weber number representing dimensionless ratio of inertia to surface tension (
Acknowledgements
The authors gratefully acknowledge the valuable contributions of Dr. Leslie Yeo, Dept Mechanical Engineering in the early stages of this project. The authors would also like to acknowledge the Monash University Engineering Faculty and Australian Research Council Discovery Projects program (DP0770462) for providing financial support for this work as well as the Monash Graduate Research School for providing scholarship support for B. Khanmohammadi.
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