Top Banner
Combined use of Design of Experiment (DoE) and Process Automation for the Efficient Optimization of New Synthetic Transformations Universita’ dell’Insubria-Dipartimento di Chimica Via Valleggio n o 11 22100 Como (Italy) www.uninsubria.it R&D Chemistry Research Centre Via Lorenzini n o 8 20139 Milano (Italy) www.boehringer-ingelheim.it Literature meeting May 2 nd 2005 Federica Stazi Ph.D Thesis
38

Combined use of Design of Experiment (DoE) and Process Automation for the Efficient Optimization of New Synthetic Transformations Universita’ dell’Insubria-Dipartimento.

Apr 02, 2015

Download

Documents

Dalia Hess
Welcome message from author
This document is posted to help you gain knowledge. Please leave a comment to let me know what you think about it! Share it to your friends and learn new things together.
Transcript
  • Slide 1

Combined use of Design of Experiment (DoE) and Process Automation for the Efficient Optimization of New Synthetic Transformations Universita dellInsubria-Dipartimento di Chimica Via Valleggio n o 11 22100 Como (Italy) www.uninsubria.it R&D Chemistry Research Centre Via Lorenzini n o 8 20139 Milano (Italy) www.boehringer-ingelheim.it Literature meeting May 2 nd 2005 Federica Stazi Ph.D Thesis Slide 2 Reasons for DoE at the Chemistry Research Centre Boehringer Ingelheim Pharma KG CRC Milan, Italy Boehringer Ingelheim Pharma KG Biberach, Germany CRC Drug Development Drug Discovery Intermediates Building blocks Test compounds Pre-dev. Candidates Metabolites Process impurities D D iversity O O riented S S ynthesis T T arget O O riented S S ynthesis Slide 3 Target Oriented Synthesis (TOS) and DoE DoE-driven search for optimal conditions Target Slide 4 Diversity-Oriented Synthesis (DOS) and DoE Same starting material and rxn conditions different RX Same RX and rxn conditions different starting material DoE-driven search for optimal conditions Slide 5 The DoE Concept: Basic Principles Inputs x1x1 x2x2 xpxp Outputs System z1z1 z2z2 zqzq controllable factors uncontrollable factors y (starting materials) (products) Slide 6 OFAT (One Factor at A Time) Approach OFAT results in a set of experiment in which only one factors is varied S M P AB C incomplete picture of the overall process factor interactions are not revealed number of experiments not fixed not possible to perform experiments in parallel - Slide 7 DoE (Design of Experiment) Approach S M P AB C DOE results in a set of pre-planned experiments in which factors are varied at the same time factor interactions are revealed precise estimation of factors effect 2-level Factorial Design 12 34 5 6 87 experimental matrix mathematical model of the chemical process based on statistical analysis possibility to perform experiment in parallel Slide 8 Doe Simplified: Practical Tools for Effective Experimentation Mark J. Anderson, Patrick J. Whitcomb Productivity Press, 2000 Design and Optimization in Organic Synthesis R. Carlson Elsevier Science, 1997 Design and Analysis of Experiments, 5th Edition D.C. Montgomery Wiley, 2000 + Chemical Journals Statistical Background and DoE Tools Slide 9 Statistical Background and DOE Tools: Examples S.V. Ley et al. Organic Process Research Development, 2002, 6, 823 R: Et 4 F Res IV, 8 exps + 2 centres A.A. (equiv) PS-DIEA (equiv) Rnx time (hours) Conc.(volumes) Pre DoE:40% Post DoE: 91% 5 different R groups Yields: 81-96% S.V. Ley et al. Synlett, 2000, 11, 1603 5 F ResIV, 16 exps + 4 centres PS-DCC (equiv) Conc. (volumes) Rnx time (hours) Solvent T1 Solvent T2 Post DoE: 97% 8 different R groups 10 different R groups 80 cpds. Hit rate 95% 4 F ResIV, 8 exps + 1 centre PS-DCC (equiv) Conc. (volumes) Amine (equiv) Slide 10 Advantage Series 2050 (Argonaut) SK233 React Array Workstation (Anachem) Carousel (Radley) ? ? ? ? Statistical background and DoE Tools Design Expert 6.0.4 by Stat-Ease MODDE 7.0.0 by Umetrics Slide 11 React. rack Reagent Solvent racks UV/Vis Detector PC Reaction Control HPLC control Needle Syringes HPLC Statistical Background and DOE Tools Slide 12 The Sequential Workflow of DoE 2. Planning the experiment: State experimental objectives Choice of factors, levels and response variable choice of experimental design 3. Performing the experiment 4. Data analysis and modeling 5. Interpretation and confirmations 6. Reiteration 1. Synthetic Problem ? Slide 13 1. cytochrome P450 2. UDPG transferases Putting the Theory into Practice Step 1. Defining the Synthetic Problem: a Problematic Glucuronidation Slide 14 Putting the Theory into Practice Step 1. Defining the Synthetic Problem: O-Glucuronidation Background UDPG transferases For a review, see: Stachulski, A. V.; Jenkins, N. J. Nat. Prod. Rep. 1998, 173. Slide 15 Putting the Theory into Practice Step 1. Defining the Synthetic Problem: O-Glucuronidation Background For a review, see: Stachulski, A. V.; Jenkins, N. J. Nat. Prod. Rep. 1998, 173. Slide 16 Putting the Theory into Practice Step 1. Defining the Synthetic Problem: A New Strategy Modified Koenigs-Knorr cond.: 25% yield (Ag 2 O, mol sieves, 18 h CH 3 CN + TMEDA 10 eq, R=Piv) Typical Koenigs-Knorr cond.: 3% yield (Ag 2 O, mol sieves, 18 h CH 3 CN, R=Ac or R=Piv) Slide 17 Step 2. Planning the Experiment Find the best starting point: small-scale parallel reagent screening (10 mg scale). Amine vs. Ag pKa : 11.0 9.110.310.4 9.2 HMTTA works best. The silver source does not significantly influence yields. influence of amine complexing ability a amine basicity silver source Step 2. Planning the Experiment 7 factors to be investigated in a screening factorial design A complete investigation of 7 factors over 2 levels requires: 2 7 = 128 exps 128 parameters are estimable: 1 constant term, 7 linear terms, 21 2-FI, 35 3-FI, 64 4/7-FI FI relative importance: 2-FI > 3-FI >> 4/7-FI Slide 21 Step 2. Planning the Experiment: Full vs. Fractional Factorial Designs n o of factors n o of experiments 2 3 45 6 78 9 4 8 16 32 64 128 256 Fractional Factorials exploit the redundancy of Full Factorials to reduce the n o of exps 7 factors can also be studied in only a fraction of the original full factorial design. Full Fractional Slide 22 Step 2. Planning the Experiment: Final Output of Pre-Experimental Plan 7 factors to be investigated in a 2 7-4 Resolution III design: 8 exps + 3 center points (50mg scale) Experimental matrix: center points for curvature detection for calculation of pure error Slide 23 Step 3. Performing the Experiment Use randomization to reduce the influence of nuisance factors If possible, operate in parallel since we rely on a previous experimental plan Monitor and record values of uncontrolled factors Perform a scoping study: check -- - vs. +++ and reproducibility. Slide 24 Step 4. Data Analysis and Modeling: ANOVA Testing (Analysis of Variance) of changing variable Ag 2 CO 3 Br-sugar HMTTA Slide 25 Step 5. Interpretation and Confirmation After stepwise modifying the insignificant terms we obtain the definitive linear model y = + * A+ * C - *D + * E + Is this linear model adequately modeling the response? Slide 26 Step 6. Reiteration: Altering Factors Ranges The contour plot directs us outside the investigated region modify factors ranges to explore a better experimental region Slide 27 Different options when the linear model is not adequate. Many are extensions of the 2-level factorial design 2-level FD CCDCCF3-level FD Factor levels 533 Number of Experiments 14+3 27+3 Geometries of the Explored Space sphericalcubic Characteristics: Box-Behnken 3 12+3 spherical Response Surface Modelling (RSM): an Overview Slide 28 Optimizing Glucuronidation Yield using CCD: Performing the Experiment factorial axial center 20 exps on (100mg scale) Slide 29 Optimizing Glucuronidation Yield using CCD: Data Analysis and Model Building Definitive coded model yield = 76.91 - 9.58 A + 0.70 B + 2.57 C- 0.75 A 2 + 1.44 A B + 2.51 A 3 Maximum Slide 30 Optimizing Glucuronidation Yield using CCD: Empirical Model Interrogation Program optimization tools indicate the best conditions found and the confidence intervals FactorNameLevel Low Level High Level AHMTTA0.700.22.5 BAg 2 CO 3 3.763.35.5 CBr-sugar2.422.02.5 PredictionSE Mean95% CI low95% CI high P yield86.51.3483.7189.33 Qty phenol in situ yield isolated yield 1 gr 86.0 80.6 1 gr 87.2 81.0 3.5 gr 85.7 80.0 Model validation Slide 31 Optimized conditions: Ag 2 CO 3 3.76 eq Br-sugar 2.4 eq HMTTA 0.7 eq 1h CH 3 CN in situ yield 86.0% isolated yield 80.5% Reagents Screening 10 exp DoE Factorial Screening 11 exp DoE CCD Optimization 20 exp Initial conditions: Ag 2 O 2.7 eq Br-sugar 1 eq mol sieves 18 h CH 3 CN isolated yield 3% Optimizing Glucuronidation Yield Using CCD: Conclusion Slide 32 Ag + Ag 2 O >> Ag 2 CO 3 Ag 2 CO 3 no Br-Sugar Ag + dissolution / activation Ag + competitive complexation Mechanistic Modelling: the Manifold Actions of HMTTA Ag+ active ! Slide 33 Mechanistic Modelling: the Manifold Actions of HMTTA Positive effects of HMTTA : competitive ligand for SM complexation activator of Ag + Max competitive binding to Ag + Max Ag + activation SM Complexation > Ag + activation F.Stazi, G. Palmisano, M. Turconi, S. Clini, and M. Santagostino, J. Org. Chem, 2004, 69, 1097-1103. The postulated irreversible binding of starting material (SM) to Ag + ions is really operative. The presence of the tetramine additive (HMTTA) influences the complexation equilibria. The relationship between complexation of SM and concentration of HMTTA is non-linear. Excess favours the formation of unwanted side product Base (pKa=9.23, 8.47, 5.36, 1.68) on the Br-sugar (-HBr) Negative effect of HMTTA : Consistent depletion of Br- sugar Slide 34 Scope and Limitation of the Methodology % isolated yield : optimized conditions% isolated yield: classical Koenigs-Knorr conditions + HMTTA 0.2-0.7 eq 71%80% 88%54% 86% 80% 30%74%85% 79% 0% 20% 3% 65% 0% 15%mix 0% Slide 35 Other Applications Pd-Catalysed Cyanation of aryl bromide at room temperature F.Stazi, G.Palmisano, M.Turconi, M.Santagostino Tetrahedron Letters, 46 (2005) 1815-1818. Regioseletive Alkylation of 3,4-dihydroxybenzaldehyde Unpublished Results Slide 36 Summary and Conclusions A mathematical regression model is generated. This model is empirical and valid only within the studied factor range. A better understanding and control of the process are gained by interacting with the model. Use of non-statistical knowledge of the problem for choosing factors and their levels, interpreting the results... Using statistics is no substitute for thinking about the problem. Design and analysis of Experiments D.C. Montgomery DOE results in a set of experiments in which factors are varied at the same time in an organized and systematic approach Slide 37 Suggestion If you find DoE applied to boring chemistry problem .. Using DoE to Spend Less Time in The Traffic Screening Ingredients (for Homemade Bread) Most Efficiently with Two- Level Design of Experiment Applied DoE to Microwave Popcorn and more and more. By Mark J. Anderson, consultant, Stat-Ease, Inc., Minneapolis, MN Slide 38 Acknowledgment Prof. Giovanni Palmisano Universita dellInsubria-Dipartimento di Chimica Dr. Marco Santagostino Boehringer-Ingelheim R&D Chemistry Research Centre