Synthos 3000 Microwave Assisted Organic Synthesis Meanings & Model Applications www.anton-paar.com Contents What´s Microwave Assisted Organic Synthesis ? Why ? - Benefits of MAOS Instrumentation - Monomode vs. Multimode Getting Started Typical Applications Performance Verification - Model Applications 2 A. Stadler, 2005 MAOS Microwave Assisted Organic Synthesis Definition “Preparation of a desired organic compound from available starting materials via some (multi-step) procedure, involving microwave irradiation” 3 A. Stadler, 2005 Benefits of MW-Assisted Synthesis higher temperatures (superheating / sealed vessels) faster reactions, less byproducts, pure compounds absolute control over reaction parameters selective heating / activation of catalysts energy efficient, rapid energy transfer easy access to high pressure performance can do things that can´t be done conventionally 20 MeOH, 160 °C 200 15 150 10 100 5 50 0 0 60 120 180 240 Time (sec) 4 A. Stadler, 2005 300 0 360 Pressure (bar) Temperature (°C) Power (W) 250 Applicable Microwave Instrumentation Single Mode Instruments Domestic MW Oven MLS Ethos 1600 Emrys Liberator Initiator Mars-S Multimode Batch Reactors Discover 5 A. Stadler, 2005 Multimode vs. Monomode Cavities Basic Technical Differences: Multimode Cavity Monomode (Single Mode) Cavity antenna sample magnetron Mode stirrer sample Chaos 6 Wave guide magnetron antenna Standing Wave A. Stadler, 2005 Multimode vs. Monomode Cavities Practical Differences: Multimode Cavity Monomode (Single Mode) Cavity huge cavity large scale runs (5-1000 mL) simply applicable for scale-up high throughput by parallel synthesis field can be inhomogeneous lower power density high output power small scale experiments troublesome compact cavity small scale runs (0.5-50 mL) scale-up by flow-through technique throughput by automation highly homogeneous field high power density lower output power large scale runs time-consuming Choice depends mainly on desired application (combichem, medchem, process chemistry) and the scale, not on the chemistry ! 7 A. Stadler, 2005 Getting Started Initial Questions are solvent / reagents suitable for microwave irradiation what about thermal stability / decomposition expecting elaboration of pressure flash heating required fit limits of chemistry with equipment consider beneficial influence of selective heating 8 A. Stadler, 2005 Getting Started General Hints: use polar solvents with thermal stability (ROH, MeCN, NMP...) apply small volumes unless reaction is optimized starting point 10 min @ 120 °C max. 30 min hold time increase temperature rather than time passive heating elements for improved energy transfer consider solvents changing their properties at higher temperatures 9 A. Stadler, 2005 Converting Conventional Protocols Arrhenius Equation : k = A*e 10 Rule of thumb: 10° temperature increase = 2-fold rate acceleration –Ea/RT 80 °C 90 °C 100 °C 110 °C 120 °C 130 °C 140 °C 150 °C 160 °C 8h 4h 2h 1h 30 min 15 min 8 min 4 min 2 min A. Stadler, 2005 Converting Conventional Protocols Temp 20 °C 30 °C 40 °C 50 °C 60 °C 70 °C 80 °C 90 °C 100 °C 110 °C 120 °C 130 °C 140 °C 150 °C 160 °C 170 °C 180 °C 190 °C 200 °C 210 °C 220 °C 230 °C 240 °C 250 °C 11 Time - change in color represents change in unit 1 2 4 6 8 12 24 48 30 1 2 3 4 6 12 24 15 30 1 1.5 2 3 6 12 8 15 30 45 1 1.5 3 6 4 8 15 23 30 45 1.5 3 2 4 8 11 15 23 45 1.5 56 2 4 6 8 11 23 45 28 56 2 3 4 6 11 23 14 28 56 1 2 3 6 11 7 14 28 42 56 1 3 6 4 7 14 21 28 42 1 3 2 4 7 11 14 21 42 1 53 2 4 5 7 11 21 42 26 53 2 3 4 5 11 21 13 26 53 1 2 3 5 11 7 13 26 40 53 1 3 5 3 7 13 20 26 40 1 3 2 3 7 10 13 20 40 1 1 2 3 5 7 10 20 40 1 2 2 3 5 10 20 1 1 2 2 5 10 1 1 2 5 1 2 1 (h/ min / sec) 96 172 48 86 24 43 12 22 6 11 3 5 1.5 3 45 1 23 40 11 20 6 10 3 5 1 3 42 1 21 38 11 19 5 9 3 5 1 2 40 1 20 35 10 18 5 9 2 4 e.g. a thermal reaction for 8h at 80°C works at 2 min at 160°C in the MW ©AstraZeneca, A. Stadler, 2005 Macclesfield, UK MAOS Applications Principle Enhancement of... • every thermal accelerated process • time consuming experiments • sealed vessel reactions • conversion rates / product purity Major Benefits • super heating effect (solvents above their bp) • powerful temperature/pressure conditions • electronic parameter-control / unattended runs • software-supported experiment documentation MW make experimental work more convenient 12 A. Stadler, 2005 Typical MAOS Applications Solid Phase Synthesis • significant rate enhancement (10 min vs. 48 h) • less material strain of solid support • reduction of reagent excess Eur. J. Org. Chem. 2001, 919 Metal Catalysis • decreased reaction time (10-30 min vs. > 24 h) • reduced catalyst amount (environmentally friendly) • simplified reaction mixtures • improved purity of products 13 A. Stadler, 2005 Org. Lett. 2002, 3541 Typical MAOS Applications J. Comb. Chem. 2001, 624 Focused Library Generation • shortened optimization sequence (hours vs. days) • automated reaction process, high throughput • evident reduced over-all production time (days vs. weeks) High Pressure Chemistry • simplified use of pre-pressurized vessels • reduced reaction times • easy application of gaseous reagents • excess of reagents minimized 14 Org. Process Res. Dev. 2003, 707 Org. Biomol. Chem. 2004, 154 A. Stadler, 2005 Remarkable MAOS Applications Metal Catalyzed Carbonylations J. Comb. Chem. 2003, 350 Org. Lett. 2003, 4875 • ultra-fast chemistry (6-10 sec) • utilizing solid CO-sources (not practicable conventionally) • less catalyst needed Reactions in Near Critical Water Eur. J. Org. Chem. 2005, 3672 • chemistry at extreme conditions (>280°C, >60 bar) • easy approach without toilsome accessories • exact parameter control • comprehensive safety features 15 A. Stadler, 2005 The Idea of MAOS Changing Meanings of Microwave Instruments: So far... covering a niche in Organic Chemistry to investigate new pathways supporting the routine labwork ...and now: use MW instead of classic methods remove all other heating sources replace autoclaves powerful tool for all chemistries in any scale develop / investigate / optimize produce the compounds representing a valuable laboratory equipment for various applications from R&D to Production 16 A. Stadler, 2005 Synthos 3000 Scaling Up Microwave Assisted Organic Synthesis www.anton-paar.com Typical Operation Range Method Development 0.2 - 5.0 mL volume 0.1 - 10 mmol scale 5 - 30 min reaction time 100 - 200 °C 20 - 250 mg product First Grade Synthesis > 5.0 mL volume > 10 mmol scale minimum reaction time optimized temperature 100 - 1000 mg high throughput approach 18 Reaction Optimization 0.2 - 5.0 mL volume 0.1 - 5 mmol scale 1 - 30 min reaction time 100 - 200 °C 10 - 100 mg product Batch Synthesis > 100 mL volume > 1 mol scale optimum time/temperature conditions > 100 g product Need for proper Scale-Up techniques A. Stadler, 2005 A Versatile and Modular Microwave Platform System High performance rotors & vessels Built-in magnetic stirrer Dual remote temperature sensing Sophisticated accessories IR 19 A. Stadler, 2005 Extended Operation Limits Synthos Main Experimental Average 3000 Multimode LimitsRange Limits 120 H2O MeOH 100 Pressure (bar) EtOH 80 Acetone MeCN 60 Ethylacetate THF 40 Cyclohexane DMF 20 DCM 0 0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 Temperature (°C) 20 A. Stadler, 2005 Performance Verification Individual Scalability • Protocol for 1 mmol should work for xxx mmol without modifications • Verified for various examples using Synthos 3000 Emrys Synthos 3000 Biginelli 4 mmol: 52% 640 mmol: 48% Heck 2 mmol: 78% 80 mmol: 79% Kindler 4 mmol: 92 % 40 mmol: 90% Negishi 1 mmol: 81 % 20 mmol: 77 % Key publication: A. Stadler, B. Yousefi, D. Dallinger, P. Walla, E. Van der Eycken, N. Kaval, and C. O. Kappe Organic Process Research & Development 2003, 707-716 21 A. Stadler, 2005 Performance Verification Homogeneity • Parallel rotors should provide identical field distribution at any position • Proved by parallel Biginelli synthesis for Synthos 3000 NO2 O T 120 O Me 100 Temperature (°C) NH N H IR 1-8 Vessel 1 12.1 g 1400 Vessel 2 Vessel 3 Vessel 4 Vessel 5 Vessel 6 12.3 g 12.2 g 12.1 g 12.4 g 12.2 g Vessel 7 12.5 g Vessel 8 Total 12.3 g 98.1 g 1200 O 1000 Mol. Wt.: 319,31 80 1600 800 60 600 40 400 20 P 200 2520 2400 2280 2160 2040 1920 1800 1680 1560 1440 1320 1200 1080 960 840 720 600 480 360 240 120 0 0 0 Power (W) 140 Time (s) 22 A. Stadler, 2005 47.3% 48.1% 47.8% 47.3% 48.5% 47.8% 48.9% 48.1% 48.0 % Performance Verification Reproducibility Repeating experiments must yield similar results Verified with Heck Couplings in Rotor 8: Exp. 1: 8x 20 mmol, homogeneous catalysis Overall yield: 79% NC 3-cyano cinnamic acid Exp. 2: 8x 20 mmol, 4x homogeneous, 4x heterogeneous catalysis Overall yield: 78% Exp. 3: 8x 20 mmol, parallel synthesis, various substrates Yield of model compound: 79% 23 COOH A. Stadler, 2005 Model Reactions 1) Biginelli Multicomponent Reaction X X O O O + R R1 H O NH2 H2N O EtOH/HCl 120 °C, 20 min R R1 NH N H O effective multicomponent reaction optimized conditions tolerable to broad range of building blocks library generation in multi-gram scale (up to 80 mmol/vessel) 16 different targets within one run Org. Process Res. Dev. 2003, 707-716 24 A. Stadler, 2005 Model Reactions 2) Kindler Thioamide Synthesis Cl Cl S H2N HN NMP O H + S8 + F 140 °C, 10 min F efficient synthesis of valuable building blocks for biologically relevant heterocyclic scaffolds (40 mmol/vessel) significantly reduced reaction times unproblematic use of large amounts of elemental sulfur suitable reaction for library generation Org. Process Res. Dev. 2003, 707-716 25 A. Stadler, 2005 Model Reactions 3) Heck Couplings COOH [Pd], TEA, MeCN + NC Br 180 °C, 15 min R NC COOH R a) R = H b) R = F most important C-C bond forming reaction no interference of metal layer with microwaves parallel synthesis (20 mmol/vessel) with broad range of substrates and varying catalysts unproblematic use of significant amounts of Pd catalyst (1 mol%) Org. Process Res. Dev. 2003, 707-716 26 A. Stadler, 2005 Model Reactions 4) Negishi Coupling CN CN Br PdCl2(PPh3)2, THF + H ZnBr H 160 °C, 1 min O O short reaction times even at larger scale (20 mmol/vessel) protection of sensitive reagents by inert gas flush use of dummy loads did not affect the reaction progress Org. Process Res. Dev. 2003, 707-716 27 A. Stadler, 2005 Model Reactions 5) Suzuki Cross-Coupling Cl Cl F3C Cl Pd(OAc)2/PPh3 Et3N, DME/H2O + N H O OMe B(OH)2 OMe F3C 150 °C, 30 min N H O powerful general Suzuki protocol (4 mmol/vessel) suitable for parallel synthesis with various substrates efficient scaffold decoration for valuable building blocks T. N. Glasnov, W. Stadlbauer, C. O. Kappe J. Org. Chem. 2005, 3864-3870 28 A. Stadler, 2005 Model Reactions 6) Solid Phase Synthesis Cl MeNH2, H2O 150 °C, 5 min N H Me efficient batch synthesis utilizing solid supports (5 g per vessel) non-adhesive PTFE-liners filtration unit for simplified work-up drastically enhanced reaction rates reduced thermal stress due to short reaction times Org. Process Res. Dev. 2003, 707-716 29 A. Stadler, 2005 Model Reactions 7) Diels-Alder Cycloaddition Cl Ph N O N Cl C2H4 (7 bar), DCB 190 °C, 30 min O Cl N NaOH 70 °C, 30 min Ph N O Cl N Ph N OH Cl simplified employing of gaseous reagents gas loading in assembled rotor individual pre-pressurizing parallel performance of pressurized reactions considerably reduced reaction times N. Kaval , W. Dehaen , C. O. Kappe, E. Van der Eycken Org. Biomol. Chem. 2004, 2, 154-156 Org. Process Res. Dev. 2003, 707-716 30 A. Stadler, 2005 Model Reactions 8) Near Critical Water Chemistry O O R H2O OH 295 °C, 77 bar, 30-240min 7 mmol R = OEt, NH2 Ester/Amide Hydrolysis NCWC at temperatures >250°C and pressures >40 bar easily accessible with Rotor 8 SXQ80 conditions can be maintained up to 4 hours enabling development of new reaction pathways Green Chemistry approach J. M. Kremsner, C. O. Kappe Eur. J. Org. Chem., 2005, 3672-3679 31 A. Stadler, 2005 Model Reactions 8) Near Critical Water Chemistry NC NC Me H2O Me 295 °C, 77 bar, 20 min Me + Me Diels-Alder Cycloaddition (7.6 mmol/vessel) H N Me O NH2 + Me H2O Me Me 270 °C, 49 bar, 20 min N H Fischer Indole Synthesis (10 mmol/vessel) Me Me OH Me OH Me H2O 270 °C, 49 bar, 30 min O Me Me Me Me Pinacol Rearrangement (3 mmol/vessel) J. M. Kremsner, C. O. Kappe Eur. J. Org. Chem., 2005, 3672-3679 32 A. Stadler, 2005 Summary Direct scalability up to 1 L reaction volume Parallel synthesis up to 48 derivatives in gram-scale Comprehensive performance verification (scalability, homogeneity, reproducibility) Simultaneous pressure sensing Dual remote temperature measurement (IR control & precise immersing temperature probe) Simplified access to special applications (SPOS, gaseous reagents, sub-critical solvents, pre-pressurizing) Sophisticated accessories serving extraordinary reaction conditions (quartz vessels, heating elements, gas-loading station, filtration unit, UV lamps) 33 A. Stadler, 2005 MAOS – Latest News Comprehensive Review & MAOS Guide: Kappe, C. Oliver / Stadler, Alexander Microwaves in Organic and Medicinal Chemistry Methods and Principles in Medicinal Chemistry (Volume 25) • Microwave Theory • Equipment Review • Microwave Processing Techniques • Getting started with Microwaves • Comprehensive Literature Survey 1. Edition - June 2005 420 Pages, >400 References, Hardcover ISBN 3-527-31210-2 - Wiley-VCH, Weinheim 34 A. Stadler, 2005