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Towards Quality by Design: Modelling Nano-Particles & their - - PowerPoint PPT Presentation

Towards Quality by Design: Modelling Nano-Particles & their Formulation in Relation to Product Physical Properties Professor Kevin J Roberts, Institute of Process R&D Institute of Particle Science & Engineering School of Process,


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SLIDE 1

Towards Quality by Design: Modelling Nano-Particles & their Formulation in Relation to Product Physical Properties

Professor Kevin J Roberts, Institute of Process R&D Institute of Particle Science & Engineering School of Process, Environmental & Materials Engineering

Nanomedicines Expert’s Meeting, EMEA, London, Wednesday 24th April 2009

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SLIDE 2

Scope of Presentation

  • Industry, regulatory & market

pressures

Science-led QbD opportunities

  • Particle formation & purification

processes

  • Brief crystallisation science overview
  • Crystallisation modelling

Crystal shape modelling, interface roughening & product purity control Cluster modelling, polymorphic stability & crystallisability prediction Crystal/crystal interaction modelling & formulation design

  • Acknowledgement & Closure
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SLIDE 3

$0 $5 $10 $15 $20 $25 1 9 7 1 9 7 5 1 9 8 1 9 8 5 1 9 9 1 9 9 5 2

20 40 60

New Molecular New Molecular Entities

Productivity Paradox: Higher R&D Cost/Approved Product

Total R&D Investment (B$)

NPI NPI

Source: PhRMA annual survey, 2000 Source: PhRMA annual survey, 2000

Pharmaceutical industry getting more competitive but not any faster Molecular complexity & solid form (solubility) challenges increasing Emerging importance of material properties on production efficiency Increasing expectations from patient on product performance

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SLIDE 4

molecular design of product property Where we need to be Molecule Up products built from molecules dynamic control of properties step change in capability Where we are just now Process Down improvements incremental poor product enhancement potential processes discovered engineered to work products result from process

Science-Based Manufacture: A Cultural Change to QbD Much of this approach is routine in microelectronics, drug discovery etc. but not yet in process/product design

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SLIDE 5

Quality Attributes: Reducing Variability - Feedstock to Product

  • Important to control solid-form properties to achieve

high product quality, e.g.

  • physical properties: particle size/shape, density,

hardness/plasticity

  • chemical properties: purity, polymorphic form,

crystallinity, hygroscopicity

  • Solid-form feedstock properties impact on their
  • verall processability
  • hence on concomittant properties of formulated

products made downstream i.e. feedstock variability results in variability of products

Drivers: API physico-chemical properties designed-in to ensure product quality & optimal formulation behaviour

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SLIDE 6

Innovation or Stagnation: FDA’s 2004 White Paper “… pharmaceutical industry generally hesitant to introduce state-of-art science & technology into its manufacturing processes, part due to regulatory impact concerns leading to

  • high in process inventories
  • low factory utilisation
  • significant product wastage
  • compliance problems

“FDA has stimulated use of PAT to improve efficiency & flexibility whilst maintaining high quality standards” but driving up costs & decreasing productivity” Design in Quality (QbD) rather than end product testing

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SLIDE 7

QbD Innovation, Design Space & ICHQ8

  • QbD is major regulatory driver, notably

through ICHQ8 initiative stressing need for more detailed process understanding from R&D to manufacturing improved product quality moving culture sigma 2.5 (0.1% variability) to sigma 6 (few ppb variability)

  • Key need: improve science base

from products pragmatically engineered to work process registered: - little scope for process improvement to molecular design of products manufactured via PAT controlled processes design space registered: - flexible processes continuously improved

Challenge: developing & applying technical innovation & underpining science needed to deliver QbD

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SLIDE 8

Process R&D results in definition & approval of a “Control Space” for manufacturing process within a much wider “Knowledge Space” of possibilities concerning the process

Quality by Design (QbD) & Design Space

As product matures many factors can require changes in process control scheme, moving it from Control Space 1 to a new Control Space 2 but expensive regulatory approval needed ICHQ8 enables development of approvable Design Space in advance of commercial launch that anticipates & accommodates more than one Control Space – no need for subsequent regulatory approval

Neway, Aegis Analytical Corporation 2008

Opportunity: secure knowledge-intensive manufacturing science to ensure future industrial competitiveness

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SLIDE 9
  • Holistic approach needed

to optimise & control crystallisation processes

  • Molecule-centred

understanding

  • New unit processes &

strategies

  • Process analytics - R&D

to manufacturing

  • Over-arching high level

framework

Engineering Science for Advanced Pharmaceutical Manufacturing

  • Enablers for improving

crystal technology science base

  • Multi-scale computational

modelling

  • Precision controlled particle

formation processes

  • PAT, advanced chemometrics

& control

  • Systems engineering

& informatics

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SLIDE 10

Economics environmental impact production cost time to market Product Specifications particle size and shape polymorphic form crystal purity

Batch Crystallisation Process Science

Molecular Scale nucleation rate growth rate growth mechanism yield

… batch prepared crystals are notoriously difficult to prepare in reproducible manner… … many process related factors need

  • ptimisation…

Integrated approach critical - encompassing multi- scale/phase analysis

Process Variables supersaturation solute concentration temperature, cooling ramp solvent/additives reactant phases seeding

4M – Model, Measure, Manipulate, Manufacture

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SLIDE 11

Manufacturing Molecules An Integrated Approach

{100} binding {101} rejection tapered surface

Model Measure Manufacture Manipulate

The 4Ms

Brian Scarlett, TU Delft

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SLIDE 12

Controlling competing demands of nucleation & growth Is key issue for process design & scale-up

Batch Crystallisation Engineering Science

  • Crystallisation (cooling, reactive, evaporative) key

step in pharmaceutical manufacture effects solid-liquid isolation & separation enables product purification

  • How does it do this?

molecular recognition on growth step controlled crystal surfaces through which growing crystal recognises host & rejects impurities

  • Two main fundamental steps

Nucleation - molecular assembly 3-D clusters (10-1000 molecules) dominant step - many small crystals Growth - 2-D growth on atomically smooth crystal surfaces (hkl) dominant step – fewer larger crystals

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SLIDE 13

3-D crystal is n 2-D crystals where n = numbers of faces

Shape: 3-D Nucleation & 2-D Growth Outcome

Each habit face has different surface chemistry & hence different processing properties Crystals exhibit well-defined shape below roughening transition with surfaces defined by low-indexed planes

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SLIDE 14

002 200 202 210 111 210 202 111

Predicting & Understanding Predicting & Understanding API Crystal Morphology API Crystal Morphology Focus: Little known about surface & interfacial chemistry

  • f pharmaceutical APIs despite their importance

in formulation design & product performance

Typical API morphology, i.e. plate like with a wide range

  • f particle sizes & shapes

30µm

Good correlation between predicted & observed Crystal morphology

Sildenafil Citrate (Viagra) Sildenafil Citrate (Viagra)

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SLIDE 15

Crystal Chemistry, Morphology & Solvent: e.g. Urea

Different growth environments vapour vs methanolic solutions yields different morphologies Crystal morphology relates to crystal surface chemistry

{110} {001}

Solvent binds to different crystal faces to different degrees & thus changes the crystal morphology

Solvent selection impacts on crystal form, notably particle morphology which effects product separation, e.g. filtration

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SLIDE 16

a) b) c) d) a) b) c) d)

(a) Crystal habit for aspirin as predicted via attachment energy model (b-d) Simulated crystal habits, using modified surface energies for mixed solvent (b), pure water (c) & pure ethanol (d)

Modelling Solvent- Mediated Morphologies

Experimental data provides more plate-like crystal morphology than predicted using a simple attachment energy calculation

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SLIDE 17

Process Ability: Impact

  • f Molecular Complexity
  • Well-known Murphy’s law:
  • high value-added products e.g. pharmaceuticals are

much harder to prepare

  • Often drug molecule molecular flexibility tends to make

materials difficult to self-assemble & crystallise

  • Process understanding is key to achieving control of

complex drug compound formation

  • process compounded by many new drugs having

very poorly solubility & hence bioavailability

  • Nano-particles and/or formulations offer key opportunity

for delivering enhanced physical & chemical properties

Need to understand & inter-relate molecular & incipient solid-form structures with their physical properties

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SLIDE 18
  • Controlling balance between nucleation & growth reflects on

crystal size i.e. high nucleation rate result from high solution supersaturation leading to small nucleation cluster sizes

  • Structure & thermodynamic stability of post nucleation

product clusters important in understanding inter-relationship between process conditions & product properties

Crystallization: Nucleation & Polymorphism

  • Supersaturation-control of cluster size at nucleation
  • Hence, controlling crystallization supersaturation could enable

direction of product polymorphic form, through i.e. via homogeneous nucleation theory

2 *

2 σ γν kT r =

Hypothesis that meta-stable forms are more thermodynamically stable at small cluster sizes shown for L-glutamic acid & D-mannitol

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SLIDE 19
  • Calculation of Cartesian coordinates of polyhedral corners with

shape corresponding to crystal morphology

  • Calculation of volume & surface area of crystal polyhedron &

defining the size of crystal polyhedron

  • Building facetted shaped molecular cluster
  • Determination of surface & bulk characteristics of molecular

clusters such as

  • Crystallinity & radial distribution function (RDF)
  • Surface/bulk molecular ratio & surface area/unit volume
  • Surface properties, roughness, surface charge, reactivity
  • Molecular disorder wrt reference structures

System-specific molecular modelling program for size, shape & structural anisotropy dependency characterization of particles

POLYPACK Cluster Building Programme

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SLIDE 20

a c b

Centre

⎟ ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎜ ⎝ ⎛ Z Y X

Building Facetted Clusters: Example Aspirin

Crystal unit cell Unit cell with calculated centres of gravity Lattice grid of centres of gravities Location of polyhedron at the coordinate system origin Shift polyhedron to the middle of the lattice overlaying two models. Optimize its position to maximize lattice points Delete molecules outside the polyhedron From each centre of gravity calculate the atomic co-ordinates

Molecular model for a crystalline particle produced enabling particulate processing properties to be predicted

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SLIDE 21

α-form β-form L-glutamic acid has two polymorphic forms: α & β Meta-stable α-form: produced under kinetic control Transformation form α to b occurs in solution L-Glutamic acid

Cluster Stability: L-Glutamic Acid Different molecular conformations & hence inter-molecular packing between these two polymorphic forms

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SLIDE 22

www.lipse.org +44 (0)113 343 2404 k.k.jutlla@leeds.ac.uk

L-Glutamic Acid Facetted Clusters

α-form α α-

  • form

form β-form β β-

  • form

form Experimental morphologies Predicted morphologies Facetted molecular clusters Shaped molecular clusters built on basis of predicted crystal morphologies

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SLIDE 23

Energetic Stability of Facetted L-Glutamic Acid Clusters

Controlling crystallization supersaturation enables control of critical cluster size therefore directing the final product polymorphic form

Meta-stable form is more thermodynamically stable at small cluster size

Journal of Physical Chemistry B 109 (2005) 19550

Homogeneous nucleation theory

2 *

2 σ γν kT r =

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SLIDE 24

Energetic Stability of Spherical L-Glutamic Acid Clusters

Meta-stable form more energetically stable at small cluster size for minimized & relaxed clusters but effect not so strong as for facetted clusters Overall effect is a combination of both shape & size

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SLIDE 25

β α β α

T1 T2 T1 T2

T1 reflects position of amino group T2 reflects conformation

  • f carbon chain

Molecule in crystal structure-red line

Cluster Conformation Analysis of L-Glutamic Acid

Nano-size cluster disorder links to ease of nucleation as assessed via crystallisation measurements Cluster Conformation Analysis of L-Glutamic Acid

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SLIDE 26
  • Pair of molecules considered treated

as rigid bodies

  • First molecule fixed - other subjected

to grid search

  • Search defined by 6 degrees of

freedom of second molecule (3 translational & 3 rotational)

  • Intermolecular search defined by 2

angles & a radial distance

  • Configuration accepted or rejected

based on intermolecular pair energy

  • Typical van der Waals radii used to

define minimum separation distance between centres of two molecules

* Hammond et al Journal of Physical Chemistry B 107 (2003) 11820

Grid Search: Exploring Inter-Molecular Packing Space

Mobile molecule Fixed molecule M(θx, θy,θz)-rotational matrix R-position vector λ-translational magnitude

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SLIDE 27

Grid Search: Salt Selection

Salt structure

86 673 2265 5501 10219 4556 15781 5664 1154 289 334 78 4000 8000 12000 16000

  • 46.5
  • 45.5
  • 44.5
  • 43.5
  • 42.5
  • 41.5

Energy (Kcal/mol) Number of structures

Energy minimisation

1 2

⎟ ⎟ ⎟ ⎟ ⎟ ⎟ ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎜ ⎜ ⎜ ⎜ ⎜ ⎜ ⎝ ⎛

= Z Y X ~ R

⎟ ⎟ ⎟ ⎟ ⎟ ⎟ ⎟ ⎟ ⎠ ⎞ ⎜ ⎜ ⎜ ⎜ ⎜ ⎜ ⎜ ⎜ ⎝ ⎛

= z θ y θ x θ ~ θ

~ R

φ θ x y z C O O C N N N H H

SYSTSEARCH: Dimer intermolecular search Crystal structure modelling X-ray validation

1,3,4,6,7,8-hexahydro- 2H-pyrimido [1,2-a] acetate

Molecular grid search methods - in-silico predictive capability for use in automated salt selection process

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SLIDE 28

Impurity Segregation in Solid Caprolactam

  • Caprolactam precursor in production of nylon-6.
  • Polymerization process influenced by presence of impurities
  • Molecular modelling used to study crystal impurity incorporation

O H O O H O O O N O H N O H + 3 H2 Ni as cat. 200

  • C, 40 atm.

+ 1/2 O 2 150

  • C

10 atm.

+O2

150

  • C

10 atm.

+H2

O

+

+ 2 H2 CuO + Cr

2

O

3as cat.

200

  • C, pressure

NH

3

OH

+

HSO

4

100

  • C

20% Oleum heat Cyclohexane

  • xime

Caprolactam

Synthesis of Caprolactam: Source of Impurities

Impurity molecules overlaid in context of host crystal lattice: a) cyclohexane, b) cyclohexanol, c) cyclohexanone, d) caprolactim. Optimal position of impurity cyclohexanol in ε-caprolactam lattice

Ease of Impurity incorporation predicted hence enabling direction the synthetic route to optimise product purity

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SLIDE 29
  • Processes involving solid phases tend to result in more

manufacturing problems reflecting heterogeneity & high molecular density of solid phases compared to gaseous or liquid phases

  • Reactions between solid phases dominated by

surface properties of interacting particles inter-particle contact area

  • Molecular shape/size factors yield pharmaceuticals

crystallising in low symmetry structures producing highly anisotropic physical & chemical properties notably facetted particulate products

  • Also, inherent heterogeneity in production-scale

processes, e.g. crystallisation reactors leads to variation in crystal size & distribution creating problems for product formulation

Crystal/Crystal Interfaces & Product Formulation Molecular scale modelling tools are needed to predict particle-particle interactions

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SLIDE 30

time/months Final power reading

Low API loading High API loading Different batches within a campaign Different campaigns

Morphology, Crystal/Crystal Interfaces & Formulation

  • High API loading: physical properties effect granulation
  • Batch-to-batch, & hence product quality, variability
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SLIDE 31

Granulator Impeller Power Binder weight addition Power spike due to inhomogeneous mixing

Batch to batch variability related to API physical particle properties In-process monitoring of granulation Process (power & water addition)

Granulation Performance Manufacturing Variability

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SLIDE 32

Modelling Binding Between Crystal Particles

b)

001 _ 101 _ _ 101 _ 111 111 _ _ 001 101 101 _ 111 __ 111 __

101 _ _ 101 _ 020 _ 021 _ 021 __ 101 101 _ 020 021 021 _

e)

  • Limiting
  • Distance
  • Include only these
  • molecules in the
  • calculations
  • Distance between two centres
  • Limiting
  • Distance
  • Include only these
  • molecules in the
  • calculations
  • Distance between two centres
  • Limiting
  • Distance
  • Include only these
  • molecules in the
  • calculations
  • Limiting
  • Distance
  • Include only these
  • molecules in the
  • calculations
  • Distance between two centres

Experimental data (Ferrari & Davey) Crystal Growth & Design 4 (2003) 1061

Predicted morphologies of α- & β - L glutamic acid with interacting faces highlighted Most stable configuration at distance 35Å show interaction between (101) face β- form with (11-1) face of α-form

Modelling Correctly Predicts Binding Between Particles

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SLIDE 33

H-Bonding & Understanding Inter-Particle Binding Strength

Examining structural interfacial chemistry for various stable inter-particle interactions for different inter-particle distances

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SLIDE 34

Inter-particle interface β-form α-form needle axes Inter-particle interface β-form α-form needle axes

Inter-Particle H-Bonds at (111)/(101) Interface

Amino group found to be most important functional group in hydrogen bond pattern between the interacting surfaces

Challenge: to reverse engineer this approach to provide reliable predictive capability ab-initio

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SLIDE 35

α 002 β 101 β 020 α 111 α 002 β 101 β 020 α 111

α (111) & β (101) show surface amino group (circled in solid line) not actively involved in H-bonding hence available molecular with agglomerating particles α (002) & β (020), in contrast, have amino group fully H- bonded & not available for inter-particle binding

LGA Surface Chemistry & Interacting Crystal Surfaces

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SLIDE 36

Very Grateful Thanks & Acknowledgements

Royal Academy of Engineering & AstraZeneca for supporting my industrial secondment from which I gained a greater insight into current needs of the speciality chemical sector

  • particularly hosts Simon Ruddick & Mark Hindley

Molecular & crystal modelling studies for particle design involved collaborations with Durham & Strathclyde Universities with funding from EPSRC, AstraZeneca, GSK, Pfizer & Sanofi Numerous researchers in the Institute of Particle Science & Engineering at University of Leeds

  • particularly Klimentina Pencheva & Robert Hammond for their work on

cluster modelling

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SLIDE 37

I will be most happy to attempt to answer questions!

In this talk, I have tried to…

  • Overview industrial need for science-based process technology to

maintain the EU’s chemicals manufacturing sector’s competitive position Once again, many thanks to EMEA for the invitation to visit, for the

  • pportunity to present this talk & also for your kind attention

Closure and Thanks

  • Describe some recent modelling-based research
  • Morphological modelling for predicting particle shape
  • Modelling crystal precursor molecular clusters relating their

structure to polymorph selection & crystallisability

  • Predicting down-stream product formulation via modelling

crystal/crystal interactions

  • Given a very indecent “head-up” on crystallisation science theory,

notably achieving balance between 3-D nucleation & 2-D growth processes