Samenvatting
Mass and heat transfer can put significant technological limitations to reactor and process design, which leads to far from ideal solutions for bulk processes. A discussion covers the design, construction, and testing of a single channel micro reactor integrated with a micro mixer to demonstrate the viability of a miniaturized reactor system for an industrial bulk process, based on micro reaction technological considerations; model reaction used, i.e., Beckmann rearrangement of cyclohexanone oxime to epsilon-caprolactam with oleum as a catalyst and solvent; the reaction mixture (consisting of caprolactam and oleum) as the key step in the industrial process; window of operation; critical parameters in mass transport models; and the creation of multi micro zones of oxime and oleum rich phases. This is an abstract of a paper presented at the 42nd Loss Prevention Symposium (New Orleans, LA 4/6-10/2008).
Originele taal-2 | Engels |
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Titel | Proceedings of the 10th International Conference on Microreaction Technology (IMRET-10), April, 06-10 2008, New Orleans, La |
Plaats van productie | New York, NY |
Uitgeverij | American Institute of Chemical Engineers (AIChE) |
Pagina's | 83f- |
ISBN van geprinte versie | 978-0-8169-1023-6 |
Status | Gepubliceerd - 2008 |
Evenement | 10th International Conference on Microreaction Technology, IMRET 2008 - Topical Conference at the 2008 AIChE Spring National Meeting - New Orleans, LA, Verenigde Staten van Amerika Duur: 1 apr. 2008 → 4 apr. 2008 Congresnummer: 410 |
Congres
Congres | 10th International Conference on Microreaction Technology, IMRET 2008 - Topical Conference at the 2008 AIChE Spring National Meeting |
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Verkorte titel | IMRET 2008 |
Land/Regio | Verenigde Staten van Amerika |
Stad | New Orleans, LA |
Periode | 1/04/08 → 4/04/08 |
Ander | AIChE spring national meeting ; (New Orleans, La.) : 2008.04.06-10 |