Acceleration of Chemical Reactions Using a Supercritical Water Microreaction System
-
Masahiro Sato
, Yutaka Ikushima , Kiyotaka Hatakeda and Tamio Ikeshoji
Water is an environmentally friendly chemical species that can be employed either as catalyst or as reactant. The use of water has attracted much interest for many acid-catalyzed organic syntheses. These reactions have been studied under hot water conditions with maximum formation of ions. Under these circumstances, long reaction times are required to obtain suitable yields however with poor selectivities given the influence of side reactions. The microreaction system of the present study can heat up a substrate solution very quickly from ambient conditions to the supercritical water state (scH2O) and can then quench rapidly the same solution to sufficiently low temperatures. This allows epsilon-caprolactam production with close to 100% selectivity and 80% yield in a acid free reaction system in less than 1-second reaction time. To justify these results, first principle molecular dynamics calculations and in situ IR measurements are employed as they can be applied to the structural and electronic properties of water in the near critical point region. Close to the critical point at low fluid densities, small clusters, mainly dimers and trimers, are the dominant features with no H-bonds expected. The significant reduction of H-bond strength in H2O, peculiar to near the critical point, leads to the activation of protons or H3O+. Hence, in the scH2O microreaction system, the acidic properties of H2O at the supercritical state are considered as the likely pathway promoter which prevents the hydrolysis and the pyrolysis of cyclohexanone-oxime as well as the pyrolysis of epsilon-caprolactam. It is also observed that dilute acids at supercritical conditions further enhance the epsilon-caprolactam process with close to 100% yield and 100% selectivity.
©2011 Walter de Gruyter GmbH & Co. KG, Berlin/Boston
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Articles in the same Issue
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- A Review of Short Residence Time Cracking Processes
- Microchannel Reactors: Applications and Use in Process Development
- Carbon Nanotube Synthesis: A Review
- Modelling the Hydrodynamics of Gas-Liquid Packed Beds via Slit Models: A Review
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- Simulation of the Storage of Molten Poly(Ethylene Terephthalate)
- Optimal Non-isothermal Reactor Network for Van de Vusse Reaction
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- iso-Amyl Acetate Synthesis by Catalytic Distillation
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- Comparative Study of Two-Phase Gas-Liquid Flow in the Ejector Induced Upflow and Downflow Bubble Column
- Hydrogenation of Acetylene: Kinetic Studies and Reactor Modeling
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- Effect of Temperature on Solids Mixing in a Bubbling Fluidized Bed Reactor
- Optimal Operation of Semi-Batch Processes with a Single Reaction
- Scale Effects on Fluidized Bed Hydrodynamics
- Ultrasonic Investigation of Hydrodynamics and Mass Transfer in a Gas-Liquid(-Liquid) Stirred Vessel
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- Numerical and Experimental Studies of Air Bubbles Coalescence in a Quiescent Water Column
- Mixing Time Studies in Bubble Column Reactor with and without Internals
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- Compact Direct Methanol Fuel Cells for Portable Applications: A Modeling Study
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- Direct Synthesis of Dimethyl Ether From (H2+CO) and (H2+CO2) Feeds. Effect of Feed Composition
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- Use of CFD for Wastewater Disinfection Process Analysis: E.coli Inactivation with Peroxyacetic Acid (PAA)
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