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Risk-Based  Development for Quality by Design Ken Morris Purdue University Department of Industrial and Physical Pharmacy FDA SAB Manufacturing Sub-Committee September, 17 th , 2003
Pharmaceutical cGMPs for the 21st Century: A Risk-Based Approach A science and risk-based approach to product quality regulation incorporating an integrated quality systems approach ,[object Object],[object Object],[object Object],[object Object],[object Object]
Pharmaceutical cGMPs for the 21st Century: A Risk-Based Approach What’s New? ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
The Issue: API, Formulation, and Process Variables and Dosage Form Performance Ajaz Hussain, Arden House 2003 Low Solubility - High Permeability - Acidic compound in SIF
 
Initial Drug Substance Characterization ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
[object Object],Pharmaceutical Technology Europe, 17, June 1994
Form Screening, Selection, and Control Hilden et.al., Crystal Growth and Design, 2003, in press
Cefotaxim Sodium Moisture Uptake - Ulrich Griesser, Univ. of Innsbruck, Simultaneous Multi-sample instrument Ulrich Griesser, PHANTA 9/03
Single Crystal Structure +PXRD Pattern experimental PXRD Pattern simulated BFDH Morphology Comb. Simple Forms Morphology +Index Major Faces SPO/DIFRAC Model Average Shape
Summary of Estimated Average Shapes and Areas 110 = 64% 001 = 31% -201 = 5% 110 = 43% 011 = 29 % 200 = 15% 001 = 7% -201 = 6% 002 = 60% 102 = 33% 100 = 4%
Formulation Design and API Process Development  ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Powder Flow Avalanche testing TSI Inc. Powder Rheology Freeman Tech. Shear Cell Virendra M. Puri, Penn State
Development of the Heckel Equation P A
Shape and Flow PROCESS 1 PROCESS 2
TREND BETWEEN MASS FLOW AND SHAPE
Processing/PAT ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]
Particle Size Reduction Models Rittinger’s law:  The work required in crushing is proportional to the new surface created.                      Where:  P =power required, dm/dt=feed rate to crusher, D sb  = ave diameter before crushing,  D SQ =ave after crushing,  K r =Rittinger’s coef. Kick’s law : the work required for crushing a given mass of material is constant for the same reduction ratio, that is the ratio of the initial particle size to the finial particle size                K k = Kick’s coef.                              
Powder Charging: Qualitative Trends in a Faraday Pail-Blender System David Engers, unpublished data Purdue
Modeling Blending : Cascade Region  For fine grains, the boundary between the  characteristic region and the remaining powder bed is parabolic in shape The powder bed below the boundary rotates with the mixer as a solid body. Characteristic region Blender head space
Blending Scaled “Down” 180kg Run 16kg Run
Dry Granulation  by Roller Compaction Unpublished CAMP data – A.Gupta ,[object Object],[object Object],[object Object]
[object Object],Dry Granulation by Roller Compaction  Unpublished CAMP data – A.Gupta
Monitoring and Modeling of  Fluid Bed Granulation Paul Findlay, Ph.D dissertation, Purdue Univ, 2003
At the capillary stage, the water may interact with the surface in such a way as to change the two prominent NIR bands (1450 and 1940 nm) differently.  Modeling  Wet Granulation Pendular Funicular Capillary Droplet Drying Over Wetting
NIR during granulation–wet massing and Particle size Unpublished CAMP data, Dr. Jukka Rantanen –   X2=255 rpm X1=110 g (=X3) NIR Treated Response
DRYING  : NIR -Exit Temp vs. Time for APAP Granulation Drying Time (min) MM55 Reading Temperature (°C) T MM55 0 30 25 20 15 10 5 K.R. Morris, S.L. Nail, G.E. Peck, S.R. Byrn, U.J. Griesser, J.G. Stowell, S.-J. Hwang, K. Park  Pharm Sci Tech Today   1   6  235–245 (1998). Evaporative Diffusive Critical moisture Temperature Moisture Content 40 60 80 100 120 140 160 180 45 47 49 51 53 55 57 59 61 63 65
Full Scale  Fast   Drying Trials of an Ibuprofen Granulation Morris et.al.,  Drug Dev. Ind. Pharm.,  26 (9) :985-988 (2000)
Drying Excursions and Dissolution CAMP unpublished data
Tablet CU : Testing a Model T. Li, et. al., in press Pharm. Res. BioMed Anal. CU for constant size portions of tablets must be larger than for the whole, so in spec using real time monitoring of “part” of the tablets means in spec for the whole tablet
COATING HPMC, Sulfanilamide and, Moisture Real-Time Measurements Unpublished CAMP data,  P. Findlay,In prep for JPS
Where do we stand? ,[object Object],[object Object],[object Object],[object Object]
The Business Case ,[object Object],[object Object],[object Object],[object Object],[object Object]

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Quality by design

  • 1. Risk-Based Development for Quality by Design Ken Morris Purdue University Department of Industrial and Physical Pharmacy FDA SAB Manufacturing Sub-Committee September, 17 th , 2003
  • 2.
  • 3.
  • 4. The Issue: API, Formulation, and Process Variables and Dosage Form Performance Ajaz Hussain, Arden House 2003 Low Solubility - High Permeability - Acidic compound in SIF
  • 5.  
  • 6.
  • 7.
  • 8. Form Screening, Selection, and Control Hilden et.al., Crystal Growth and Design, 2003, in press
  • 9. Cefotaxim Sodium Moisture Uptake - Ulrich Griesser, Univ. of Innsbruck, Simultaneous Multi-sample instrument Ulrich Griesser, PHANTA 9/03
  • 10. Single Crystal Structure +PXRD Pattern experimental PXRD Pattern simulated BFDH Morphology Comb. Simple Forms Morphology +Index Major Faces SPO/DIFRAC Model Average Shape
  • 11. Summary of Estimated Average Shapes and Areas 110 = 64% 001 = 31% -201 = 5% 110 = 43% 011 = 29 % 200 = 15% 001 = 7% -201 = 6% 002 = 60% 102 = 33% 100 = 4%
  • 12.
  • 13. Powder Flow Avalanche testing TSI Inc. Powder Rheology Freeman Tech. Shear Cell Virendra M. Puri, Penn State
  • 14. Development of the Heckel Equation P A
  • 15. Shape and Flow PROCESS 1 PROCESS 2
  • 16. TREND BETWEEN MASS FLOW AND SHAPE
  • 17.
  • 18. Particle Size Reduction Models Rittinger’s law: The work required in crushing is proportional to the new surface created.                     Where: P =power required, dm/dt=feed rate to crusher, D sb = ave diameter before crushing, D SQ =ave after crushing, K r =Rittinger’s coef. Kick’s law : the work required for crushing a given mass of material is constant for the same reduction ratio, that is the ratio of the initial particle size to the finial particle size                K k = Kick’s coef.                              
  • 19. Powder Charging: Qualitative Trends in a Faraday Pail-Blender System David Engers, unpublished data Purdue
  • 20. Modeling Blending : Cascade Region For fine grains, the boundary between the characteristic region and the remaining powder bed is parabolic in shape The powder bed below the boundary rotates with the mixer as a solid body. Characteristic region Blender head space
  • 21. Blending Scaled “Down” 180kg Run 16kg Run
  • 22.
  • 23.
  • 24. Monitoring and Modeling of Fluid Bed Granulation Paul Findlay, Ph.D dissertation, Purdue Univ, 2003
  • 25. At the capillary stage, the water may interact with the surface in such a way as to change the two prominent NIR bands (1450 and 1940 nm) differently. Modeling Wet Granulation Pendular Funicular Capillary Droplet Drying Over Wetting
  • 26. NIR during granulation–wet massing and Particle size Unpublished CAMP data, Dr. Jukka Rantanen – X2=255 rpm X1=110 g (=X3) NIR Treated Response
  • 27. DRYING : NIR -Exit Temp vs. Time for APAP Granulation Drying Time (min) MM55 Reading Temperature (°C) T MM55 0 30 25 20 15 10 5 K.R. Morris, S.L. Nail, G.E. Peck, S.R. Byrn, U.J. Griesser, J.G. Stowell, S.-J. Hwang, K. Park Pharm Sci Tech Today 1 6 235–245 (1998). Evaporative Diffusive Critical moisture Temperature Moisture Content 40 60 80 100 120 140 160 180 45 47 49 51 53 55 57 59 61 63 65
  • 28. Full Scale Fast Drying Trials of an Ibuprofen Granulation Morris et.al., Drug Dev. Ind. Pharm., 26 (9) :985-988 (2000)
  • 29. Drying Excursions and Dissolution CAMP unpublished data
  • 30. Tablet CU : Testing a Model T. Li, et. al., in press Pharm. Res. BioMed Anal. CU for constant size portions of tablets must be larger than for the whole, so in spec using real time monitoring of “part” of the tablets means in spec for the whole tablet
  • 31. COATING HPMC, Sulfanilamide and, Moisture Real-Time Measurements Unpublished CAMP data, P. Findlay,In prep for JPS
  • 32.
  • 33.