ACS Catalysis
Research Article
a
,
b
Scheme 2. Validation and Optimization of S 1 Alkylation of PH Gas Generated within a Two-Chamber Reactor System
N
3
a
b
Gas titration data are an average of two independent measurements and exhibit pseudo-first-order kinetics (Scheme 2B, inset). S 1 alkylation
N
conditions unless stated otherwise: aqueous HCl (5.0 M, 10 equiv) added to Zn P (0.5 equiv) at RT in chamber 1 to generate 1 equiv of PH ;
3
2
3
R′OTf (1 equiv) added to tert-amyl-OR (6 equiv) at RT in chamber 2. Yields are of isolated, pure material; yields in parentheses were determined
31
c
by P NMR spectroscopic analysis vs internal standard. Using 3 equiv of tert-amyl acetate.
ultimately limited in scope by the diversity of the tert-
To explore the viability of this strategy, we first confirmed
alkylmetal reagents that are available.
that generation of PH3 from Zn3P2 is indeed facile. As
determined by volumetric gas titration (Scheme 2B), complete
hydrolysis of Zn P occurs within 10 min of adding excess
−
+
We anticipated that an umpolung strategy (“P /C ”,
Scheme 1C) would provide unrivaled access to structurally
diverse DTAP building blocks and would eliminate the need
3
2
aqueous HCl. Under these conditions, gas evolution exhibits
pseudo-first-order kinetics with an effective half-life of 110 s
(Scheme 2B, inset), providing sufficient time for addition of
the acid before full gas pressure is achieved.
for wasteful redox adjustments at phosphorus. S 1 alkylation
N
would enable facile installation of sterically demanding
substituents and would open up a much wider pool of
+
−
alkylating agents than is available to the conventional P /C
Subsequently, we sought to identify conditions for S
alkylation of the ex situ generated PH gas (Scheme 2C). Prior
attempts to alkylate PH or its synthetic equivalents have
N
1
approach. In situ generation of both the P-nucleophile and the
C-electrophile would ultimately minimize the need to handle
reactive reagents and intermediates.
3
16
3
17
18
exploited S
neither of which allow installation of tert-alkyl substituents.
single example of S 1-type alkylation was recently reported by
Carrow, although a secondary phosphine nucleophilerather
than PH
was employed in order to generate the homoleptic
tertiary phosphine PAd As illustrated in entries 1−4, we
2
or hydrophosphination reactivity manifolds,
N
19
Herein we report realization of this umpolung approach to
A
secondary phosphine synthesis. By exploiting an S 1 manifold,
N
N
we demonstrate that di-tert-alkylphosphines can be prepared
selectively from readily available, bench-stable precursors. The
products are obtained as air-stable, odorless phosphonium salts
which can be isolated conveniently by filtration. The DTAP
building blocks that are accessible in this way enable facile
expansion of extant ligand classes by modification of a
previously invariant vector; we show that these modifications
affect the steric and electronic properties of the new ligands
and can be used to tune their performance in catalysis.
3
2
0
.
3
found that a combination of tert-amyl alcohol or tert-amyl
methyl ether with either HOTf or TMSOTf failed to afford
appreciable amounts of alkylphosphine products. While the
combination of tert-amyl acetate and HOTf proved similarly
unsuccessful (entry 5), the use of tert-amyl acetate and
TMSOTf resulted in high-yielding alkylation of PH (entry
3
21
6
). Notably, >95% of the phosphonium salt formed in this
way was recovered conveniently via precipitation and filtration
in air. The isolated material proved to be a free-flowing,
nonhygroscopic, and odorless solid that is soluble in organic
RESULTS AND DISCUSSION
■
Our proposed S 1 strategy (Scheme 1C) requires a synthon of
N
2
−
22
the type “HP ”. While phosphine gas (PH ) is an atom-
media and that can be stored on the bench for at least 1 year
3
economical and readily available synthetic equivalent to this
synthon, we were cognizant of the risks and practical
challenges associated with handling high-pressure, cylinderized
without noticeable degradation. Although the yield of 1a
suffered slightly when a lower stoichiometry of tert-amyl
acetate was employed (entry 7), these more economical
conditions proved generally applicable in subsequent studies
(vide infra).
1
3
PH3. We therefore sought to generate the gas on demand
and in precise stoichiometries by protonolysis of a metal
phosphide. Specifically, we identified zinc phosphide (Zn P )
3
2
The conditions outlined in entries 6 and 7 of Scheme 2C
confer excellent selectivity for dialkylation, with neither mono-
as a convenient source of PH because, unlike other metal
3
14
31
phosphides, it is both bench-stable and cheap (£48/kg).
While Zn P can be stored and handled under an ambient
nor trialkylation products observed by P NMR spectroscopy.
3
2
This remarkable selectivity can be explained by considering the
atmosphere, it is readily protonolyzed to PH under acidic
different basicities of primary, secondary, and tertiary
3
23
conditions. We anticipated that this reactivity could be
phosphines. The first-formed primary phosphine is, presum-
ably, insufficiently basic to be fully protonated by the HOTf
coproduct. A second alkylation may therefore occur, affording
a more basic secondary phosphine which is fully protonated
under the reaction conditions. This innate alkylation-depend-
exploited in the two-chamber “CO-ware” reactor system
15
developed by Skrydstrup, with PH generated in the first
3
chamber from Zn P and consumed in the second chamber by
3
2
SN1 alkylation (Scheme 2A).
5
455
ACS Catal. 2020, 10, 5454−5461