Effect of Non-reactive Powder Particle Properties on Dry Agglomeration in a High Shear Mixer

Hongyuan Wei , Bohao Feng , Guangzong Zhao , Xiao Tian , Leping Dang

Transactions of Tianjin University ›› 2018, Vol. 24 ›› Issue (5) : 442 -452.

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Transactions of Tianjin University ›› 2018, Vol. 24 ›› Issue (5) : 442 -452. DOI: 10.1007/s12209-017-0108-4
Research Article

Effect of Non-reactive Powder Particle Properties on Dry Agglomeration in a High Shear Mixer

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Abstract

The effect of non-reactive powder particle properties on the detergent dry agglomeration process in a high shear mixer was investigated. Three types of micron-scale silica were chosen as the non-reactive fine powders and a semi-solid alkyl ethyl ethoxy sulfate (AES) paste with ultra-high viscosity was chosen as the binder. The granules were characterized using mass-based granule size distribution, scanning electron microcopy, and bulk density tests. The results revealed that powder particle size plays a leading role in agglomeration behavior. A decrease in the median particle size results in enhanced dispersion of silica particles in the AES paste binder droplets, which leads to the formation of uniform granules that are slightly affected by compacting forces. Agglomerate quality, using silica with high oil absorption as well as optimum particle size, was satisfactory, and the product exhibited a smaller median particle size, narrower size distribution, and superior anti-caking capacity under the same liquid-to-solid ratio (L/S).

Keywords

Dry agglomeration / Particle size distribution / Agglomerate formation / Granulation kinetics

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Hongyuan Wei, Bohao Feng, Guangzong Zhao, Xiao Tian, Leping Dang. Effect of Non-reactive Powder Particle Properties on Dry Agglomeration in a High Shear Mixer. Transactions of Tianjin University, 2018, 24(5): 442-452 DOI:10.1007/s12209-017-0108-4

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References

[1]

Davies JF, Knight PC, Travill AW et al (1994) Process for manufacture of detergent powder: EP, EP0215637

[2]

Smirani-Khayati N, Falk V, Bardin-Monnier N, et al. Binder liquid distribution during granulation process and its relationship to granule size distribution. Powder Technol, 2009, 195(2): 105-112.

[3]

Tardos GI, Khan MI, Mort PR. Critical parameters and limiting conditions in binder granulation of fine powders. Powder Technol, 1997, 94(3): 245-258.

[4]

Iveson SM, Litster JD, Ennis BJ. Fundamental studies of granule consolidation Part 1: effects of binder content and binder viscosity. Powder Technol, 1996, 88(1): 15-20.

[5]

Saleh K, Vialatte L, Guigon P. Wet granulation in a batch high shear mixer. Chem Eng Sci, 2005, 60(14): 3763-3775.

[6]

Mirza Z, Liu JT, Glocheux Y, et al. Effect of impeller design on homogeneity, size and strength of pharmaceutical granules produced by high-shear wet granulation. Particuology, 2015, 23: 31-39.

[7]

Iveson SM, Litster JD, Hapgood K, et al. Nucleation, growth and breakage phenomena in agitated wet granulation processes: a review. Powder Technol, 2001, 117(1–2): 3-39.

[8]

Franceschinis E, Santomaso AC, Trotter A, et al. High shear mixer granulation using food grade binders with different thickening power. Food Res Int, 2014, 64: 711-717.

[9]

Borchers G. Design and manufacturing of solid detergent products. J Surfactants Deterg, 2005, 8(2): 123-128.

[10]

Reynolds GK, Biggs CA, Salman AD, et al. Non-uniformity of binder distribution in high-shear granulation. Powder Technol, 2004, 140(3): 203-208.

[11]

Tan MXL, Hapgood KP. Foam granulation: binder dispersion and nucleation in mixer-granulators. Chem Eng Res Des, 2011, 89(5): 526-536.

[12]

Balashanmugam M, Cheong YS, Alam Z, et al. Dispersion of a semi-solid binder in a moving powder bed during detergent agglomeration. Chem Eng Res Des, 2016, 110: 32-42.

[13]

Chitu TM, Oulahna D, Hemati M. Wet granulation in laboratory-scale high shear mixers: effect of chopper presence, design and impeller speed. Powder Technol, 2011, 206(1–2): 34-43.

[14]

Tan BM, Loh ZH, Soh JL, et al. Distribution of a viscous binder during high shear granulation—sensitivity to the method of delivery and its impact on product properties. Int J Pharm, 2014, 460(1–2): 255-263.

[15]

Badawy SI, Narang AS, Lamarche K, et al. Mechanistic basis for the effects of process parameters on quality attributes in high shear wet granulation. Int J Pharm, 2012, 439(1–2): 324

[16]

Chitu TM, Oulahna D, Hemati M. Wet granulation in laboratory scale high shear mixers: effect of binder properties. Powder Technol, 2011, 206(1–2): 25-33.

[17]

Björn IN, Jansson A, Karlsson M, et al. Empirical to mechanistic modelling in high shear granulation. Chem Eng Sci, 2005, 60(14): 3795-3803.

[18]

Knight PC, Seville JPK, Wellm AB, et al. Prediction of impeller torque in high shear powder mixers. Chem Eng Sci, 2001, 56(15): 4457-4471.

[19]

Schaefer T, Taagegaard B, Thomsen LJ, et al. Melt pelletization in a high shear mixer. V. Effects of apparatus variables. Eur J Pharm Sci, 1993, 1(3): 133-141.

[20]

Kristensen HG, Holm P, Schaefer T. Mechanical properties of moist agglomerates in relation to granulation mechanisms. Part I. Deformability of moist, densified agglomerates. Powder Technol, 1985, 44(3): 227-237.

[21]

Keningley ST, Knight PC, Marson AD. An investigation into the effects of binder viscosity on agglomeration behaviour. Powder Technol, 1997, 91(2): 95-103.

[22]

Johansen A, Schaefer T. Effects of physical properties of powder particles on binder liquid requirement and agglomerate growth mechanisms in a high shear mixer. Eur J Pharm Sci, 2001, 14(2): 135-147.

[23]

Börner M, Michaelis M, Siegmann E, et al. Impact of impeller design on high-shear wet granulation. Powder Technol, 2016, 295: 261-271.

[24]

Schaefer T. Melt pelletization in a high shear mixer. VI. Agglomeration of a cohesive powder. Int J Pharm, 1996, 132(1–2): 221-230.

[25]

Johansen A, Schaefer T. Effects of interactions between powder particle size and binder viscosity on agglomerate growth mechanisms in a high shear mixer. Eur J Pharm Sci, 2001, 12(3): 297-309.

[26]

Pietsch W (2008) Chapter 6. Industrial applications of size enlargement by agglomeration. In: Agglomeration in industry: occurrence and applications. Wiley, Germany, pp 59–478. https://doi.org/10.1002/9783527619795.ch6

[27]

Balashanmugam M, Cheong YS, Hounslow MJ, et al. Semi-solid paste binder dispersion in a moving powder bed. Proc Eng, 2015, 102: 626-633.

[28]

Li J, Tao L, Buckley D, et al. Effect of physical states of binders on high-shear wet granulation and granule properties: a mechanistic approach toward understanding high-shear wet granulation process, part 3: effect of binder rheological properties. J Pharm Sci, 2012, 101(5): 1877-1887.

[29]

Leuenberger H. Granulation, new techniques. Pharm Acta Helv, 1982, 57(3): 72-82.

[30]

Hancock BC, York P, Rowe RC. An assessment of substrate-binder interactions in model wet masses. 1: mixer torque rheometry. Int J Pharm, 1994, 102(1–3): 167-176.

[31]

Schaefer T. Growth mechanisms in melt agglomeration in high shear mixers. Powder Technol, 2001, 117(1–2): 68-82.

[32]

Kristensen HG, Holm P, Jaegerskou A, et al. Granulation in high speed mixers. Part 4: effect of liquid saturation on the agglomeration. Pharmazeutische Industrie, 1984, 46: 760-768.

[33]

Mort PR. Scale-up of binder agglomeration processes. Powder Technol, 2005, 150(2): 86-103.

[34]

Adetayo AA, Litster JD, Pratsinis SE, et al. Population balance modelling of drum granulation of materials with wide size distribution. Powder Technol, 1995, 82(1): 37-49.

[35]

Tapper GI, Lindberg NO. The granulation of some lactose qualities with different particle size distributions in a domestic-type mixer. Acta Pharmaceutica Suecica, 1986, 23(1): 47-56.

[36]

Iveson SM, Litster JD. Fundamental studies of granule consolidation. Part 2: quantifying the effects of particle and binder properties. Powder Technol, 1998, 99(3): 243-250.

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