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Safe Generation and Synthetic Utilization of Hydrazoic Acid in a Continuous Flow Reactor.

Safe Generation and Synthetic Utilization of Hydrazoic Acid in a Continuous Flow Reactor.
B. Gutmann, J.-P. Roduit, D. Roberge, C. O. Kappe, J. Flow Chem. 2012, 2,8-19.
http://www.akademiai.com/content/l622j82k3171t080/?p=0213e26b691f494d8eb782308d34fe77&pi=2
Authors
1Christian Doppler Laboratory for Microwave Chemistry and Institute of Chemistry, Karl-Franzens-University Graz A-8010 Heinrichstrasse 28 Graz Austria
2Microreactor Technology, Lonza AG CH-3930 Visp Switzerland
Abstract
Hydrazoic acid (HN3) was used in a safe and reliable way for the synthesis of 5-substitued-1H-tetrazoles and for the preparation of N-(2-azidoethyl)acylamides in a continuous flow format. Hydrazoic acid was generated in situ either from an aqueous feed of sodium azide upon mixing with acetic acid, or from neat trimethylsilyl azide upon mixing with methanol.
For both processes, subsequent reaction of the in situ generated hydrazoic acid with either organic nitriles (tetrazole formation) or 2-oxazolines (ring opening to β-azido-carboxamides) was performed in a coil reactor in an elevated temperature/pressure regime. Despite the explosive properties of HN3, the reactions could be performed safely at very high temperatures to yield the desired products in short reaction times and in excellent product yields.
The scalability of both protocols was demonstrated for selected examples. Employing a commercially available benchtop flow reactor, productivities of 18.9 g/h of 5-phenyltetrazole and 23.0 g/h of N-(1-azido-2-methylpropan- 2-yl)acetamide were achieved.

Keywords
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Process Intensification
Creating competitive advantage through Improved and consistent quality, high efficiencies and maximum flexibility.
Safer, Cleaner, Smaller, Cheaper and Smarter processes , The basic principle of Process Intensification is to fit the equipment to the process and not process to the equipment, as is the case now.
Process Intensification can achieve drastic improvement in the time cycle and yields as well as converting batch processes to continuous process using specialized set of equipment. The design philosophy in process intensification is to design a process which has Chemical Kinetics as its only limitation. See the illustration below
“Process Intensification by Kinetics alone controlling the reaction, using specialized equipments; modification / telescoping of process steps achieves drastic reduction in time cycles and converts batch processes to continuous ; Reduced energy consumption, Reduced by-product formation; sustainability , hazard-containment, compliance to QbD and PAT and importantly a much faster time-to-market”
Illustrative examples are as follows:
- Watt’s aldol reaction: Time needed to reach 100 % conversion 20 minutes against 24 hours in batch process
- Fisher Esterification:
gives 83% yield against 15% in batch process - Grignard Reaction:
gives 78% yield against 49% in batch process - Nitration Reaction: Product purity increase from 56% to 78% and yield of mononitrate increases 55% to 75%.
- Other Reactions: Acetylation, Amine Protection, Carbonylation, Claisen Schmidt Reaction, Esterification, Hydrogenation, Hydrolysis, Methylation, Oxidation, Phosgenation, Sulphonation, Suzuki Coupling Ring Expansion
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CEO
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some pics from hall 5 -H-47 at cphi mumbai india dec 3 2014


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