(642g) Selection of Functional Solvent Factory for Automatic Aldehyde and Ketone Separation in Aldol Reaction: A Combined Simulation and Experimental Approach | AIChE

(642g) Selection of Functional Solvent Factory for Automatic Aldehyde and Ketone Separation in Aldol Reaction: A Combined Simulation and Experimental Approach

Authors 

Zhang, C. - Presenter, Eindhoven University of Technolog
Song, Z., Max Planck Institute for Dynamics of Complex Technical Systems
Jin, C., Zhejiang University of Technology
Nijhuis, J., Eindhoven University of Technology
Zhou, T., Max Planck Institute for Dynamics of Complex Technical Systems
Noël, T., Eindhoven University of Technology
Gröger, H., Bielefeld University
Sundmacher, K., Max Planck Institute for Dynamics of Complex Technical Systems
van Hest, J., Eindhoven University of Technology
Hessel, V., Eindhoven University of Technology
We present a new microfluidic concept based on complex multiphase systems, which may be switched by temperature to a higher or lower number of fluidic phases. This would allow to fluidically open and close interim reaction compartments - close when reaction is required (= bringing all reaction components together) and open when separation is required (= giving each reaction component at best an own phase). We termed this ‘Green-Spaciant Solvent Factory’ (create spaces = ‘spaciant’) which provides ‘horizontal hierarchy’ – as opposed to the ‘vertical hierarchy’ of common multi-step flow syntheses (or batches) with their many consecutive reactors-separators. This is inspired by nature, as the cell with its internal organelles is a horizontally compartmentalized soft-matter reactor. The vision of the FET-OPEN project ‘ONE-FLOW’ (www.one-flow.org) is that such flow processing suits multi-step cascade reactions, since it ideally just needs one reactor passage for a complex synthesis task.

The 2-step cascade from 3-chlorobenzaldehyde to (1R,3S)-1-(3-chloro-phenyl)butane-1,3-diol, well-established by Groeger’s group, [1] is studied as a model system. This is part of a chemoenzymatic cascade combining organo- and biocatalysis, which represents in general an attractive process concept for producing pharmaceutical medicines. In this work, we are exploring to achieve the functionalities of product separation and reactant/catalyst recovery solely by multi-phases with designer solvents. This would allow to reduce complex reaction and separation equipment as well as catalyst modification to one single tube reactor using a standard catalyst (one-flow). Firstly, a large database of conventional organic solvent and/or ionic liquids (ILs) is generated from the COSMOthermX software. Then, the reactivity potential of different families of solvent with the reactants is considered to narrow the screening space. Furthermore, relevant physical properties and the environmental effect of solvents (LCA assessment) is taken into account to screen out the suitable solvents. Afterwards, the top solvent candidates were carefully evaluated by experiments.[2, 3] The whole ‘One-Flow’ solvent screening methodology for aldol reaction is given in Scheme 1 [2].

As key result, dodecane as best aldol reaction solvent and two 1-butyl-3-methylimidazolium based ionic liquids as candidate solvents in enzymatic reduction are identified. Up to 92mol% conversion and with (R)-aldol product yield (63 mol%) for aldol reaction is obtained, shown in Figure 1.

Meanwhile, we propose the compatibility of nanoreactor into the micro-flow reactor to protect and separate catalysts. Our final goal is to achieve multi-step reactions in one run (ONE-FLOW) in multi-phasic systems using this methodology, i.e. to mimic the metabolic cascades of nature. In Scheme 2, [2] we have envisioned how such Spaciant Solvent Factory for a two-step catalytic reaction may look alike.

Acknowledgements

The research work is supported by FET-Open EU project ONE-FLOW (grant no. 737266). The authors acknowledge the "Deutsche Forschungsgemeinschaft" SFB/TRR 63 project InPROMPT and the grant (15120868/218) of the University of Adelaide.

References

[1] Rulli G, et al. Angewandte Chemie International Edition, 2011, 50(34): 7944-7947.

[2] Zhang C, Song Z, Jin C, et al. Chemical Engineering Journal, 2020, 385: 123399.

[3] Morales-Gonzalez O M, Zhang C, Li S, et al. Chemical Engineering Science: X, 2019, 3: 100024.

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