(394c) Effect of Surface Energy Evolution On Particle Nucleation Under Gas Anti-Solvent Precipitation Conditions
AIChE Annual Meeting
2013
2013 AIChE Annual Meeting
Separations Division
Poster Session: Developments in Crystallization Research
Tuesday, November 5, 2013 - 6:00pm to 8:00pm
We address here the problem of particle nucleation and growth under so-called Gas-Anti-Solvent-Precipitation (GASP-) conditions. This complex environment is of considerable interest for several currenttechnologies. In the pharmaceutical industry1 , which motivated the present work, GASP environment is used to produce the controlled precipitation of an Active Pharmaceutical Ingredient (API) from an organic solvent, often sprayed into compressed CO2. Of importance is the ability to predict and control the size distribution of the nucleated particles, with the usual goal of producing narrow distributions of ultrafine particles to facilitate rapid dissolution when administered. Our theoretical model2 is illustrated using the system: phenanthrene [as API-surrogate] precipitated from liquid toluene using CO2 as anti-solvent at ca. 60 bar and 298K). Our preliminary results demonstrate the need to account for the time evolution of not only the supersaturation (no surprise!) but also the surface energy of the particle/fluid interface(remarkably, rarely considered).
In our well-mixed single droplet theoretical model2 we consider the time-evolution of particle nucleation- and condensation-growth-rates, fully coupled to the evolving environmental conditions associated with CO2 uptake and solution volume change. Particle nucleation rates are conveniently approximated using Classical Nucleation Theory (CNT), and single particle growth rates are based on a molecular collision-theory-based kinetic model3, including Gibbs-Kelvin(-Ostwald) curvature corrections for recently born particles. However, the numerical method used to solve the Population Balance Equation governing the particle number density distribution function (NDDF) is not restricted to any particular choice of rate laws for nucleation or growth, nor does it presume or restrict the mathematical form of the NDDF. Our model identifies the dependence of the characteristic particle size and nucleation/growth time scales of the problem as a function of the control parameters in the nearly isobaric/isothermal GASP-environment (mainly pressure level and initial API under-saturation). Besides revealing the relevant dimensionless groups governing the performance of such systems, we demonstrate the importance of surface energy evolution (SEE) in determining the critical nucleus size, and associated nucleation rates, in this variable composition “carrier fluid”. Our model also reveals the effects of SEE on the ultimate particle NDDF. In this regard, we find that a non-monotonic time evolution of the critical nucleus size can give rise to multi-modal size distribution functions, without the need to involve physical processes other than particle nucleation. Our results also show that, for the system under consideration (phenanthrene precipitated from micron-size toluene solution droplets using CO2 as anti-solvent) typical particle growth times are considerably longer than the corresponding characteristic nucleation times. In such cases post-nucleation particle growth introduces only a small correction, and the finally observed precipitated particle NDDF basically betrays the integrated time history of the critical nucleus size convoluted with log(supersaturation). As a corollary, controlling the time evolution of the critical nucleus size (viaboth effective surface energy and supersaturation) enables NDDF-control, which, in some cases, can even yield (normally undesirable) multi-modal API particle populations.
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a Yale University, Department of Chemical and Environmental Engineering,
New Haven, CT, 06520-8286, USA
b Departmento de Física Matemática y de Fluidos, UNED, Madrid, Apdo 60141, 28080, Spain
References:
1. Martin, A. and Cocero, MJ, “Micronization Processes With Supercritical Fluids: Fundamentals and Mechanisms”, Advanced Drug Delivery Reviews(Elsevier),vol 60, pp 339-350(2008)
2. Rosner, DE and Arias-Zugasti, M, “Theory of Pharmaceutical Powder‘Micronization’ Using Compressed Gas Anti-solvent (Re-) Precipitation”; Paper # WG10S1O1, *European Aerosol Conference; Granada, Spain, September 6, 2012; J Supercritical Fluids(to be submitted) August , 2013
3. Rosner, DE, “Collision Theory Re-Interpretation of Kinetic Data for the Growth of Organic Crystal Surfaces; Part I. Melt Growth; Part
II . Physical Vapor–Growth, Part III. Solution–Growth; Implications for the Precipitation of Pharmaceuticals in Trans-critical Environments?"; Crystal Growth & Design (ACS), (to be submitted); Summer 2013