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Journal Name
COMMUNICATION
DOI: 10.1039/C9GC00318E
Fig. 4 Recycling of the enzyme and NADES (30% v/v) after extraction with pentane in the bioreductions of acetophenone with LbADH (left), 2-octanone with
ADH-T (middle) and propiophenone with RasADH (right): A) Blue bars are reactions carried out in 50 mM buffer, extracted with pentane and reusing the
NADES-buffer plus the enzyme; B) Red bars are reactions carried out in 200 mM buffer, extracted with pentane and reusing the NADES-buffer plus the
enzyme; C) Green bars are reactions carried out in 200 mM buffer, filtering the enzyme, extracting with pentane and reusing the NADES-buffer plus the
enzyme; D) Purple bars are reactions carried out in 200 mM buffer, filtering the enzyme, extracting with pentane, readjusting the pH of the NADES-buffer
mixture up to 7.5 and reusing the NADES-buffer plus the enzyme. Numerical values are given in the ESI.
For these semi-preparative transformations, we performed a simple
Acknowledgements
Financial support from the Spanish Ministry of Economy and
Competitiveness (MEC, Project CTQ2016-75752-R) is gratefully
acknowledged. A.M.-I. thanks MEC for a predoctoral fellowship
inside the FPI program.
quantification of the E-factor23 to obtain an overview of the
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environmental impact of this methodology. Hence, the EATOS tool
was used focusing on the relevance of the reaction conditions
regarding the reagents, catalysts and solvents employed (excluding
water), and taking into account the waste generated. As can be
seen in the ESI (Figure S1), the values obtained were between 236-
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86. While these numbers are still high, it can be seen that the
Notes and references
highest percentage of these numbers come from the solvents
employed, in particular from EtOAc used to extract the final
products. Since at big scale the recycling of organic solvents is a
common applied technique, we are sure that these numbers could
be further optimised.
1
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Overall, a ChCl:Glu mixture has been used as a designer natural DES
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NADES in up to 50% v/v ratio has provided two main advantages.
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the GDH-catalysed reaction for the nicotinamide cofactor recycling.
On the other hand, the bioreductions were run at higher substrate
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glucose/GDH, and the development of practical protocols in terms
of excellent conversions were possible in up to 100 mM
concentration with excellent selectivities. After optimisation of the
reaction conditions, the bioreductions were carried out in semi-
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Conflicts of interest
There are no conflicts to declare.
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