Organic Letters
Letter
reaction sequence (Scheme 3). A stream of acid chloride was
mixedwithaprotecteddiamineatroomtemperatureandambient
pressure to form the amide. The reaction stream was flowed into
an injection loop and injected into the Phoenix to deprotect the
indoline to give intermediate 15. After exiting the Phoenix, the
reaction solution was mixed with a stream of 4-chlorophenyl
chloroformate and heated to 60 °C for 100 s. The entire synthesis
took ∼8 min to complete, and following concentration of the
collected solution and purification on normal-phase silica, 22 was
obtained in 91% isolated yield. It is also worth noting that
intermediate 15 could be immediately coupled in this sequence,
which prevents the indole formation that was observed if the
reaction mixture containing 15 was dried (Scheme 1, footnote f).
A sulfonylation−deprotection−SNAr reaction sequence was
also carried out using the Phoenix (Scheme 4). In this sequence, a
protected diamine was sulfonylated and mixed with an aryl halide
at room temperature and ambient pressure. The reaction stream
was once again flowed into an injection loop and loaded into the
Phoenix reactor set to 300 °C and 100 bar. In this case, the
deprotected amine was immediately coupled to the aryl halide via
a high-temperature SNAr to give 23 in 81% yield following
purification by normal-phase flash chromatography.
Both processes shown in Schemes 3 and 4 are high-throughput
methods, capable of generating grams of material in a matter of
minutes. Coupling−deprotection−coupling reaction sequences
are highly prevalent in the medicinal chemistry community, and
the overall process is greatly telescoped using this methodology.
In the cases described, where the concentration of the substrate
was not optimized, the system generates 0.4 mmol of product per
minute, indicating that these procedures are suitable for both
small-scale medicinal chemistry efforts, as well as reaction scale-
up.
The mechanism of the flow-mediated Boc deprotection
appears to be thermolytic, as the outlet of the reactor is pH
neutral when only acetonitrile is flushed through the system. As
expected, the pH of the reaction solution is slightly basic (pH ∼8)
due to the pKa of the products eluting from the system.
In conclusion, we have developed a general, high-temperature
Boc deprotection in flow using the Phoenix flow reactor.13
Removal of the solvent is the only workup required, and
subsequent reactions can be carried out without purification or
concentration. The protocol demonstrates a high functional
group tolerance and can be readily used with substrates that have
multiple protecting groups. We also demonstrate the utility of the
Boc deprotection in two different multistep reaction sequences,
showing how diverse molecular structures can rapidly be
synthesized without any intermediate extractions or purifications
within a matter of minutes.
ACKNOWLEDGMENTS
■
We thank Justin Dietrich for helpful discussions, Rick Yarbrough,
Jan Waters, and Dave Whittern for structural chemistry support,
and Erin Jordan (AbbVie) for chiral chromatography support. All
authorsareemployeesorformeremployeesofAbbVie. Thisstudy
was sponsored by AbbVie. AbbVie contributed to the study
design, research, interpretation of data, writing, reviewing and
approving the manuscript.
REFERENCES
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injection loop, and the Phoenix Flow Reactor. The HPLC pump has a
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pressure regulator has a maximum pressure of 140 bar.
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ASSOCIATED CONTENT
* Supporting Information
■
S
(12) Reactions were run at either 0.1 or 0.2 M in acetonitrile, but it was
observed that higher concentrations could also be used without further
optimization. Using a 1.0 M solution of Boc-Phe-OMe gave a complete
conversion but resulted in far more vigorous off-gassing at the reactor
outlet.
TheSupportingInformationisavailablefreeofchargeontheACS
Experimental procedures and full characterization (1H and
13C NMR data and spectra, MS) (PDF)
(13) When taking into account solvent recycling, no waste is generated
during this process as no reagents or workups are required. For this
reason, E-factors for this flow process would be much lower compared to
traditional batch deprotection techniques.
AUTHOR INFORMATION
Corresponding Author
■
Notes
The authors declare no competing financial interest.
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Org. Lett. XXXX, XXX, XXX−XXX