Open Access Article
Craig D.
Campbell
,
Caroline
Joannesse
,
Louis C.
Morrill
,
Douglas
Philp
and
Andrew D.
Smith
*
EaStCHEM, School of Chemistry, University of St Andrews, St Andrews, KY16 9ST, UK. E-mail: ads10@st-andrews.ac.uk
First published on 3rd February 2015
Triazolinylidenes promote γ-selective C-carboxylation (up to 99
:
1 regioselectivity) in the O- to C-carboxyl transfer of furanyl carbonates in contrast to DMAP that promotes preferential α-C-carboxylation with moderate regiocontrol (typically 60
:
40 regioselectivity). The generality of this process is described and a simple mechanistic and kinetic model postulated to account for the observed regioselectivity
:
40 mixture of α
:
γ products, an electron-donating C(5)-4-MeOC6H4 substituent favored α-functionalization (α
:
γ up to 92
:
8) while an electron-withdrawing C(5)-4-NCC6H4 substituent favored γ-functionalization (α
:
γ up to 20
:
80) (Fig. 1).
Building upon our interest in Lewis base catalysis7,8 and O- to C-carboxyl transfer rearrangements,9 we have recently developed a catalyst selective regiodivergent O- to C- or N-carboxyl transfer reaction of pyrazolyl carbonates (Fig. 2, eqn (1)).10 In this process, NHCs promote selective O- to C-carboxyl transfer, while DMAP promotes selective O- to N-transfer, with quantum mechanics calculations used to probe the observed catalyst selective divergence. In this manuscript we probe the generality of this principle by application to the O- to C-carboxyl transfer of furanyl carbonates. We sought to apply this catalyst selective11 regiodivergence to promote γ-C-carboxylation in this process that would be independent of the electronic nature of furanyl substitution, allowing a direct comparison with the electronic bias observed by Vedejs.12 In this manuscript (Fig. 2, eqn (2)), triazolinylidene NHCs promote highly γ-selective C-carboxylation of furanyl carbonates in this rearrangement process (regioselectivity up to 1
:
99 α
:
γ), while DMAP gives preferential, but modest, α-selectivity (regioselectivity typically 60
:
40 α
:
γ).
:
40 ratio of α-
:
γ-products 6
:
7 (Table 1, entries 1 and 3).13 The ability of triazolinylidene NHCs to catalyze the rearrangement of 5 was next investigated. Using KHMDS as the base to generate NHC 8 from the corresponding precatalyst gave efficient catalysis, generating a 16
:
84 ratio of α-
:
γ-regioisomers (individual isomers were isolated in 6% and 72% yield respectively) (entry 4). Alternative N-C6F5 and N-4-MeOC6H4 substituted triazolinylidenes 9 and 10 give identical preferential γ-regioselectivity (entries 5–6).14 Further investigation using NHC catalyst 8 showed that at higher NHC concentrations (∼85 mM, 22.5 mol%) an identical 16
:
84 ratio of α-
:
γ-carboxyl products 6
:
7 was obtained. However, upon sequentially lowering the NHC concentration (to 3.4 mM, 0.9 mol% entries 7–11) the reaction still progressed rapidly to completion (<5 min), giving a 2
:
98 ratio of α-
:
γ-products after five minutes (entry 10), which decayed to a 4
:
96 ratio of α-
:
γ-products after one hour (entry 11). Further lowering of the NHC concentration (1.7 mM, 0.45 mol%) and sampling the reaction before full consumption of the carbonate starting material (1 min) showed that at 90% conversion, exclusively the γ-carboxyl product 7 was formed (entry 12). After one hour, and at full conversion, a 2
:
98 ratio of α-
:
γ-products was observed (entry 13). Using DMAP gave a consistent 60
:
40 ratio of α-
:
γ-products irrespective of concentration (34 mM, 10 mol% or 3.4 mM, 1 mol%). Unfortunately, treatment of 5 with a number of archetypal chiral NHCs in an attempt to promote the regio- and enantioselective version of this transformation returned exclusively starting material in each case.
a
| Entry | Lewis base (mol%) | [Lewis base]/mM | Ratio 6(α) : 7(γ)b |
Yieldc (%) |
|---|---|---|---|---|
| a In all cases the NHCs were prepared by prior deprotonation of the corresponding triazolium precatalyst salt with a sub-stoichiometric quantity (0.9 equiv.) of KHMDS. b As shown by 1H NMR spectroscopic analysis of the crude reaction product. c Isolated yield; isomer shown in parentheses. d Reaction time 1 hour. e Reaction time 5 minutes. f Reaction time 1 minute. | ||||
| 1d | DMAP 3 (10) | 34 | 60 : 40 |
60 (α) |
| 2d | DMAP 3 (1) | 3.4 | 60 : 40 |
— |
| 3d | DHPB 4 (10) | 34 | 56 : 44 |
— |
| 4d | NHC 8 (9) | 34 | 16 : 84 |
72 (γ) |
| 5d | NHC 9 (9) | 34 | 16 : 84 |
— |
| 6d | NHC 10 (9) | 34 | 16 : 84 |
— |
| 7d | NHC 8 (22.5) | 85 | 16 : 84 |
— |
| 8d | NHC 8 (4.5) | 17 | 16 : 84 |
— |
| 9d | NHC 8 (1.8) | 6.8 | 10 : 90 |
— |
| 10e | NHC 8 (0.9) | 3.4 | 2 : 98 |
85 (γ) |
| 11d | NHC 8 (0.9) | 3.4 | 4 : 96 |
— |
| 12f | NHC 8 (0.45) | 1.7 | 0 : 100 |
— |
| 13d | NHC 8 (0.45) | 1.7 | 2 : 98 |
— |
These product distributions indicate that both DMAP 3 and NHC 8 are effective catalysts for this transformation, yet offer complementary product regioselectivities, with DMAP 3 favoring the α-isomer (with modest regiocontrol) and NHCs 8–10 the γ-isomer with excellent regiocontrol. To further investigate these mechanistic pathways, the individual regioisomeric products 6 and 7 were resubjected to the reaction conditions. Retreatment of both 6 and 7 with DMAP (17 mM, 5 mol%) for extended reaction times returned only the individual starting materials. However, treatment of the α-carboxyl product 6 with NHC 8 (17 mM, 4.5 mol%, five hour reaction time) returned a 16
:
84 ratio of α
:
γ products, consistent with significant regioisomeric exchange to favor the γ-carboxyl product 7 (Scheme 1, eqn (1)). Similarly, treatment of the γ-carboxyl regioisomer 7 with NHC 8 (17 mM, 4.5 mol%, five hour reaction time) delivered a 14
:
86 ratio of α
:
γ products (eqn (2)); both ratios within experimental error of the 14
:
86 ratio observed in Table 1 at higher catalyst loadings and concentration.
The variation in ratio of α-
:
γ-products with NHC concentration, catalyst loading, and reaction time, suggest the interconversion of the α- and γ-regioisomeric products during the NHC-catalyzed reaction. These findings suggest that C-carboxylation with DMAP is irreversible in this system, with moderate, but preferential α-regiocontrol. Under NHC-catalysis reversible C-carboxylation is observed, with initial preferential formation of the γ-isomer, with subsequent equilibration leading to a mixture of α-
:
γ-products.15 These observations contrast the irreversible C-carboxylation process observed in the rearrangement of oxazolyl carbonates with NHC 8.9a While the origin of the regioselectivity preference observed under either DMAP or NHC-mediated catalysis is currently unknown in this system, mechanistic studies indicate extensive carbonate crossover, consistent with rapid and reversible O-transcarboxylation as an initial reaction step as previously observed for oxazolyl carbonates.16
A simple kinetic framework for this NHC-mediated process can be constructed and simulated (Fig. 3) by recognizing that the behavior of this system can be explained by invoking three coupled equilibria. The first process involves the rapid and reversible C-carboxylation of the NHC by the furanyl carbonate. This process is characterized by Ki, which, in our kinetic model, is arbitrarily set at a large value of 1000. Additionally, the value for the forward rate constant for this process, ki, is the largest in the system. Formation of the α- and γ-products proceeds though two further equilibria, characterized by two further equilibrium constants Kγ and Kα. The ratio of these two equilibrium constants (Kγ/Kα = 5.67) reflects the final ratio of the α- and γ-products (∼85
:
15) reached at equilibrium. In this mechanism, free NHC is required both for reaction initiation from the furanyl carbonate and to allow equilibration of the C-carboxyl products. Since Ki is large with respect to both Kγ and Kα, the concentration of free NHC will be low up to conversions in excess of 90% (based upon 10 mol% added NHC), leading to preferential kinetic formation of the γ-furanyl product. However, with increasing time and NHC concentration the α- and γ- isomers can interconvert to generate the observed thermodynamic product ratio. Interestingly, for this model to mirror the observed selectivity for the γ-product at low conversions and/or low catalyst loadings, it is necessary to set kγ to be 100 × kα and for initiation (ki) to be at least 10 × kγ. Using this parameter set, this model correctly predicts the behavior of the experimental system – at short reaction times and low NHC loading; the system is highly γ-selective (red areas in Fig. 3). As the reaction time increases, the reactivation of the product (by addition of the NHC to product 7) drives the system towards the thermodynamic distribution of α- and γ- isomers (white area in Fig. 3). The reasons for the differential rates of transfer to the α- and γ- positions are unclear at this stage and in future work we intend to probe these issues computationally.
:
1) is observed at lower NHC concentrations and using short reaction times, allowing the isolation of the γ-isomer in 67–91% yield.
| R1 | Ar | R2 | Lewis base (mM, mol%) | Ratio α : γ a |
Yieldb (%) | |
|---|---|---|---|---|---|---|
| a As shown by 1H NMR spectroscopic analysis of the crude reaction product. b Isolated yield. | ||||||
| 1 | Me | Ph | Ph | DMAP 3 (34, 10) | 60 : 40 |
60 (α) |
| 2 | NHC 8 (34, 9) | 16 : 84 |
72 (γ) | |||
| 3 | NHC 8 (3.4, 0.9) | 2 : 98 |
85 (γ) | |||
| 4 | Bn | Ph | Ph | DMAP 3 (34, 10) | 64 : 36 |
45 (α) |
| 5 | NHC 8 (34, 9) | 19 : 81 |
67 (γ) | |||
| 6 | NHC 8 (3.4, 0.9) | 4 : 96 |
67 (γ) | |||
| 7 | Bn | Ph | CMe2CCl3 | DMAP 3 (34, 10) | 62 : 38 |
56 (α); 26 (γ) |
| 8 | NHC 8 (34, 9) | 4 : 96 |
80 (γ) | |||
| 9 | NHC 8 (3.4, 0.9) | 1 : 99 |
91 (γ) | |||
| 10 | Bn | Ph | CH2CCl3 | DMAP 3 (34, 10) | 54 : 46 |
44 (α); 37 (γ) |
| 11 | NHC 8 (34, 9) | 5 : 95 |
71 (γ) | |||
| 12 | NHC 8 (3.4, 0.9) | 1 : 99 |
86 (γ) | |||
| 13 | Et | Ph | Ph | DMAP 3 (34, 10) | 47 : 53 |
32 (α) |
| 14 | NHC 8 (34, 9) | 21 : 79 |
54 (γ) | |||
| 15 | NHC 8 (3.4, 0.9) | 1 : 99 |
71 (γ) | |||
| 16 | 4-BrBn | Ph | Ph | DMAP 3 (34, 10) | 53 : 47 |
43 (α) |
| 17 | NHC 8 (34, 9) | 10 : 90 |
80 (γ) | |||
| 18 | Allyl | Ph | Ph | DMAP 3 (34, 10) | 61 : 39 |
54 (α); 32 (γ) |
| 19 | NHC 8 (34, 9) | 31 : 69 |
24 (α); 50 (γ) | |||
| 20 | NHC 8 (3.4, 0.9) | 6 : 94 |
81 (γ) | |||
| 21 | Me | 4-FC6H4 | Ph | DMAP 3 (34, 10) | 71 : 29 |
52 (α) |
| 22 | NHC 8 (34, 9) | 12 : 88 |
67 (γ) | |||
| 23 | NHC 8 (3.4, 0.9) | 10 : 90 |
71 (γ) | |||
| 24 | Me | 4-FC6H4 | CH2CCl3 | DMAP 3 (34, 10) | 67 : 33 |
60 (α) |
| 25 | NHC 8 (34, 9) | 15 : 85 |
76 (γ) | |||
| 26 | NHC 8 (3.4, 0.9) | 4 : 96 |
87 (γ) | |||
| 27 | Bn | 4-FC6H4 | Ph | DMAP 3 (34, 10) | 71 : 29 |
56 (α) |
| 28 | NHC 8 (34, 9) | 20 : 80 |
56 (γ) | |||
| 29 | NHC 8 (3.4, 0.9) | 7 : 93 |
78 (γ) | |||
| 30 | Et | 4-FC6H4 | Ph | DMAP 3 (34, 10) | 48 : 52 |
46 (α) |
| 31 | NHC 8 (34, 9) | 20 : 80 |
61 (γ) | |||
| 32 | NHC 8 (3.4, 0.9) | 4 : 96 |
83 (γ) | |||
To further probe the structural factors necessary for γ-selectivity in this NHC-mediated transformation, the rearrangement of a C(3)-phenyl–C(5)-methyl furanyl carbonate 11 was investigated. Treatment of 11 with DMAP 3 (10 mol%) gave poor regiocontrol (α
:
γ 57
:
43), while NHC 8 (34 mM, 9 mol% or 3.4 mM, 0.9 mol%) showed excellent control for the γ-isomer even after extended reaction time, consistent with γ-selective O- to C-carboxyl transfer under NHC-mediated catalysis not requiring a C(5)-aryl unit as a necessary structural feature (Table 3).18
:
1 regioselectivity) in the O- to C-carboxyl transfer of furanyl carbonates, in contrast to DMAP that promotes preferential α-C-carboxylation with moderate regiocontrol. Current work from within our laboratory is focused upon demonstrating further applications of NHC-mediated organocatalytic transformations in the construction of poly-functionalized building blocks for synthesis.
Footnote |
| † Electronic supplementary information (ESI) available: Full experimental procedures and characterisation, as well as 1H and 13C NMR spectra for novel compounds. See DOI: 10.1039/c4ob02629b |
| This journal is © The Royal Society of Chemistry 2015 |