(724b) Towards a Generic Model for Twin-Screw Wet Granulation: Linking Material Properties to PBM Parameters.
AIChE Annual Meeting
2021
2021 Annual Meeting
Particle Technology Forum
Population Balance Modeling for Particle Formation Processes: Nucleation, Aggregation and Breakage Kernels
Wednesday, November 17, 2021 - 8:17am to 8:34am
Several models to simulate the twin-screw wet granulation process have been published [1], [2], [5], [7]â[12]. However, a complete or more generic model involving material properties, process parameters and screw configurations is, to the authorsâ knowledge, not yet available in literature [13]. This work seeks to take the first steps to address the development of a generic model, which from an industrial perspective is desirable to reduce the number of experiments required to expedite the time to market for new products. A one-dimensional compartmental PBM for the twin-screw wet granulation process is presented to simulate the particle size distribution. Pure aggregation in the wetting zone and a combination of aggregation and breakage in the kneading zones are assumed as the primary phenomena in the granulator. The aggregation kernel in the wetting zone corresponds to a modification of the aggregation kernel originally presented in the work by Van Hauwermeiren et al., 2018 [14]. In particular, a strategy is applied to reduce the amount of unknown parameters of the model in each compartment using patterns detected from the collected experimental data reducing the complexity of the calibration process.
The PBM was calibrated for three different Active Pharmaceutical Ingredients (APIs) of different nature, both, hydrophilic and hydrophobic, at low and high concentrations. Then, six formulations were studied at different granulator process conditions (the granules analyzed in this study were produced in the high shear twin-screw wet granulator module of the ConsiGma-25 from GEA Pharma Systems, ColletteTM, Wommelgem, Belgium, continuous line). Subsequently, Partial Least Squares (PLS) models were built using the calibration results to predict the PBM parameters from the material properties and liquid-to-solid ratio conditions as inputs. This generic PBM for TSWG will greatly reduce the amount of material needed for experimentation and it can reduce the time-to-market and experimental product development costs for a new product.
Acknowledgments:
Pfizer Inc.
Janssen Pharmaceutica NV
UCB
References:
[1] A. Kumar et al., âLinking granulation performance with residence time and granulation liquid distributions in twin-screw granulation: An experimental investigation,â Eur. J. Pharm. Sci., 2016.
[2] D. Barrasso and R. Ramachandran, âQualitative Assessment of a Multi-Scale, Compartmental PBM-DEM Model of a Continuous Twin-Screw Wet Granulation Process,â J. Pharm. Innov., vol. 11, no. 3, pp. 231â249, 2016.
[3] A. D. Mcguire et al., âtwin-screw granulation Part 1 : Model description New Museums Site,â no. 191, 2017.
[4] L. G. Wang, S. U. Pradhan, C. Wassgren, D. Barrasso, D. Slade, and J. D. Litster, âA breakage kernel for use in population balance modelling of twin screw granulation,â Powder Technol., vol. 363, pp. 525â540, 2020.
[5] H. Y. Ismail, M. Singh, A. B. Albadarin, and G. M. Walker, âComplete two dimensional population balance modelling of wet granulation in twin screw,â Int. J. Pharm., vol. 591, no. April, p. 120018, 2020.
[6] M. Singh, A. Kumar, S. Shirazian, V. Ranade, and G. Walker, âCharacterization of Simultaneous Evolution of Size and Composition Distributions Using Generalized Aggregation Population Balance Equation,â Pharmaceutics, vol. 12, no. 12, p. 1152, Nov. 2020.
[7] D. Barrasso, S. Walia, and R. Ramachandran, âMulti-component population balance modeling of continuous granulation processes: A parametric study and comparison with experimental trends,â Powder Technol., vol. 241, pp. 85â97, 2013.
[8] A. D. Mcguire et al., âtwin-screw granulation Part 1 : Model description New Museums Site,â Chem. Eng. Sci., vol. 188, no. 191, pp. 18â33, 2017.
[9] D. Van Hauwermeiren et al., âOn the modelling of granule size distributions in twin-screw wet granulation: calibration of a novel compartmental population balance model,â Powder Technol., pp. 116â125, 2018.
[10] S. Shirazian, H. Y. Ismail, M. Singh, R. Shaikh, D. M. Croker, and G. M. Walker, âMulti-dimensional population balance modelling of pharmaceutical formulations for continuous twin-screw wet granulation: Determination of liquid distribution,â Int. J. Pharm., vol. 566, no. June, pp. 352â360, 2019.
[11] M. Singh, G. Kaur, T. De Beer, and I. Nopens, âSolution of bivariate aggregation population balance equation: a comparative study,â React. Kinet. Mech. Catal., vol. 123, no. 2, pp. 385â401, 2018.
[12] L. G. Wang, S. U. Pradhan, C. Wassgren, D. Barrasso, D. Slade, and J. D. Litster, âA breakage kernel for use in population balance modelling of twin screw granulation,â Powder Technol., vol. 363, 2020.
[13] P. Thapa, J. Tripathi, and S. H. Jeong, âRecent trends and future perspective of pharmaceutical wet granulation for better process understanding and product development,â Powder Technol., vol. 344, pp. 864â882, 2019.
[14] D. Van Hauwermeiren et al., âOn the modelling of granule size distributions in twin-screw wet granulation : Calibration of a novel compartmental population balance model,â Powder Technol., vol. 341, pp. 116â125, 2018.