K. A. Farley et al.
starting materials (SMs), 2R,4R, and 2S,4S pyranol isomers (SM1 and
SM2, respectively).[13] This is followed by a subsequent kinetic reso-
lution key step as shown in Scheme 1. The authors devised a batch
cell followed by a benchtop low field 42.5 MHz flow NMR using
commercial 1/16 in. PFA (Norell, Inc. Morganton, N.C., USA) tubing
(Fig. 1). Anhydrous tetrahyrdrofuran (THF) solvent was pumped
through the priming port and pressure transducer of the flow
system at 0.2 ml/min rate to equilibrate the on-line analytical instru-
ments and allow for temperature equilibration prior to the reaction.
A 1 M stock solution containing a mixture of pyranal cis alcohols
[SM1: SM2 (1:1)] and vinyl butyrate (0.45 eq.) in THF was pumped
through the packed enzyme at specified rates (0.25–0.75 ml/min)
and 1H NMR and IR spectra were recorded and processed on-line.
Samples were also collected as 2 ml fractions for off-line analysis
using a high field 400 MHz flow 1H NMR and chiral gas chromato-
graphic (GC) analysis.
resolution process with a commercially available immobilized lipase
™
enzyme (Novozyme
435, Novozymes North America, Inc.
Franklinton, NC, USA) supported on a resin as one option toward
a large scale synthesis. During any kinetic resolution of a racemic
mixture, one desires the relative kinetic rate of acylation by the
enzyme to favor transesterification of one isomer over the other
during the reaction period (i.e. kSM1> kSM2). In practice, up to half
an equivalent of vinyl butyrate (SM3) is available and is fully con-
sumed as an acyl transfer reagent to furnish a mixture of optically
pure cis- methylpyranylbutyrate (P1), unreacted cis alcohol enantio-
mer (SM2), and volatile acetaldehyde (P3) by-product. The isolation
process takes advantage of the differences between alcohol and es-
ter properties such as aqueous/organic solvent solubility, and the
unreacted alcohol can be purged via extraction, or other isolation
methods such as chromatography. Upon batch scale up, concerns
around conversion or chiral purity can quickly arise because of
prolonged enzyme contact or ‘residence time’ resulting in unde-
sired products (P2, SM1). Additional side products may form via
chiral erosion, e.g. hydrolysis, or transesterification of SM2. Other
issues such as enzyme stability, enzyme deactivation, or other scal-
ing parameter effects can also be problematic. For instance, erosion
of enantiomeric excess (e.e.) was observed in earlier batches when
the recommended 2 h batch conditions were extended to 22 h
(97% e.e. to 86% e.e.), suggesting larger scale delivery would have
to be carefully controlled. One option to mitigate scaling risk is to
devise a flow process where all of the parameters (flow rate, concen-
tration, ‘residence time’, temperature, etc.) can be optimized and
fixed on a small scale. This leaves the integrity of the enzyme over
time as the predominant variable, which can impact the chiral purity
or yield of a larger scale continuous flow production. In view of this
monitoring requirement, a proof of concept portable flow system
was designed to track this key step in real time and vary those
parameters that mimic enzyme performance changes over time.
Reaction Monitoring
Benchtop and high field flow NMR
To determine viability of the low field 42.5MHz benchtop flow
NMR instrument to monitor the reaction, a 400 MHz Agilent
NMR using a Protasis microflow probe with 10 μl flow cell was also
connected to the flow stream. For this setup, a 1H-NMR was
recorded every 15s for comparison with the low field data. The
instrument was prepared using THF-d8 to establish an adequate
shim set using the deuterium lock signal, followed by 1H FID shim-
ming of fully protonated THF. Because the reaction concentration
was high enough, no solvent suppression was needed to observe
key reactant and product signals in spectra using a single scan
(Fig. 2A). Flow rates ranging from 50 to 150 μl/min through the
flow probe were tested and signal-to-noise ratios began to dimin-
ish in the 90–100 μl/min range. For the spectra in Fig. 2B, a flow
rate of 100 μl/min was used. As the reaction volume in the flow
cell was being completely replaced in the 15 s timeframe, a 90
degree pulse was utilized for maximum signal-to-noise without
concern for signal saturation.[14] To achieve the optimum 0.5ml/
min flow rate for the enzyme column, a splitter was employed
to link the output from the Omnifit (Diba Industries Inc, Danbury,
CT, USA) column directly to the flow NMR probe. The spectra
collected on the high field instrument not only generated better
resolution than the benchtop NMR but also gave us confidence
that we were not missing any intermediates that the low field
instrument was unable to detect.
Experimental setup
This process was executed using a Vapourtec R2/R4 flow setup with
™
a simple glass Omnifit column packed with Novozyme 435 en-
zyme [248 mg (0.68 ml resin bed)]. The flow synthesis system was
configured with an on-line benchtop IR equipped with a microflow
Scheme 1. Kinetic resolution of racemic cis pyranols.
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Copyright © 2016 John Wiley & Sons, Ltd.
Magn. Reson. Chem. 2016