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Enantioselective Synthesis of Vinylglycine Derivatives Using Continuous-Flow Thermolysis

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Enantioselective Synthesis of

Vinylglycine Derivatives Using

Continuous-Flow Thermolysis

Cyclotron Research Centre (CRC) - A Luxen

Center for Integrated Technology and Organic Synthesis (CiTOS) - JC Monbaliu

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1. Introduction

• Most straightforward synthesis:

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2. Background

• Thermolysis step and side-products:

• Previously described methods: Conventional reflux:

 Universal glassware

 Long reaction time at high T

 T limited by solvent  Unusual solvents  High quantities of DHB  Low ee Kugelrohr apparatus:  High ee  Low amount of DHB  No solvent  Low yields

 Poor reproducibility (difficult to control vacuum and T)

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3. Finding a solution

• Flow chemistry (CHIM9265-1 )

• Side product formation (DHB + racemization)

 Pressure control

 Temperature not limited by the solvent

 Usual solvents

 Accurate control of residence time & reaction conditions

 As soon as Vgl is formed, it is no longer exposed to high T

 Larger scale accessible through numbering-up

 Promote formation of Vgl (kinetic product) over DHB

(thermodynamic product).

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computational studies were performed at the B3LYP/6-31+G* level of theory

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computational studies were performed at the B3LYP/6-31+G* level of theory

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computational studies were performed at the B3LYP/6-31+G* level of theory

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5. Mesofluidic device

Stainless steal L = 6 m

Øext = 1/16’’ Øint = 500 µm

for optimal heat exchange

Liquid toluene @ 250-290 °C (bp. 110 °C under STP)

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5. Experimental results

0 20 40 60 80 100 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 0.0 0.2 1.0 0.0 0.2 1.0 0.0 0.2 1.0 250 °C 270 °C 290 °C mL.min-1 eq. of scavenger

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5. Experimental results

0 20 40 60 80 100 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 0.0 0.2 1.0 0.0 0.2 1.0 0.0 0.2 1.0 250 °C 270 °C 290 °C mL.min-1 eq. of scavenger

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5. Experimental results

0 20 40 60 80 100 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 1 3 5 0.0 0.2 1.0 0.0 0.2 1.0 0.0 0.2 1.0 250 °C 270 °C 290 °C mL.min-1 eq. of scavenger

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5. Experimental results

MetO (%) Vgl (%) DHB (%) CBzNH-MetO-OMe 1.2 98.8 0 BocNH-MetO-OMe / / / FmocNH-MetO-OMe 1.6 98.4 0 NBOCNH-MetO-OMe 2.4 97.6 0 CbzNH-MetO-OBn 1.5 98.5 0 BocNH-MetO-OBn / / / FmocNH-MetO-OBn 2.1 97.9 0 NBOCNH-MetO-OBn 3.3 96.7 0

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6. Conclusion

• We designed and build a mesofluidic device capable of producing

11.5 g.day-1 (190 USD/g) of CbzNH-Vgl-OMe with high yields (~99%)

and ee (>95%).

• Best conditions also work for a variety of protecting groups.

• Contrary to batch methods, production can be continuously monitored and tune if necessary.

• Great reproducibility

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