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Oxidation of secondary alcohols using solid-supported hypervalent iodine catalysts

Frederic Ballaschk and Stefan F. Kirsch*
Organic Chemistry, Bergische Universität Wuppertal, Gaußstr. 20, 42119 Wuppertal, Germany. E-mail: sfkirsch@uni-wuppertal.de

Received 26th July 2019 , Accepted 25th September 2019

First published on 3rd October 2019


It is shown how secondary alcohols are oxidized to provide the corresponding ketones by use of Oxone® and solid-supported hypervalent iodine catalysts. Under experimentally simple conditions with acetonitrile at elevated temperatures, excellent conversions were achieved with low catalyst loadings (0.2–5 mol%) when employing the conjugates 5 and 6 derived from IBX and IBS. The catalysts are broadly applicable to a range of alcohol substrates. Of primary importance with respect to sustainability issues, the metal-free catalysts are easily removed from the reaction mixture through filtration, and they can be re-used in oxidation processes for multiple times, without loss of catalytic activity.


Introduction

The formation of carbonyls through alcohol oxidation is one of the most fundamental reactions in contemporary chemistry. A great plethora of methods already exist to fulfill this task, and hypervalent iodine reagents belong to the most applied oxidation agents.1–5 For example, the Dess–Martin periodiane (DMP) became the standard textbook reagent for all kinds of alcohol oxidation, after its invention in 1983.6 Its parent compound, 2-iodoxybenzoic acid (IBX, 1),7–9 is even older and was reported first in 1893 by Hartmann and Meyer (Scheme 1).10 Since then, IBX was mainly forgotten over more than half a century before it experienced a renaissance with the breakthrough reports by Frigerio and Santagostino in 1994: IBX was shown to be a moisture-stable and easy-to-handle reagent for the mild oxidation of alcohols in DMSO at room temperature.11,12 The IBX oxidation of alcohols then emerged as a standard transformation in organic synthesis with numerous applications in complex molecule synthesis.13 Nowadays IBX is considered one of the most versatile oxidizing agents, with an extraordinary array of reactivities beyond alcohol oxidation, including phenol oxidation,14–17 functional group transfer onto activated methylene compounds,18–22 and dehydrogenations.23,24
image file: c9gc02605c-s1.tif
Scheme 1 A) Structures of IBX and IBS. (B) DMAP–peptide conjugates through Fmoc-SPPS on Boc-Gly Merrifield resin. (C) Solid-supported oxidation catalysts derived from IBX and IBS.

Despite the many advantages IBX offers, several issues are unattractive to practitioners: (i) similar to many other beloved oxidation agents, stoichiometric amounts of the hypervalent iodine compound are required for alcohol oxidation. This is particularly problematic since IBX is reported to be shock- and heat-sensitive,25,26 at least under certain conditions, thus weakening its routine for large-scale applications. (ii) The regeneration of the IBX species from the 2-iodosobenzoic acid (IBA) formed during the oxidative process is typically avoided, resulting in significant amounts of “organic waste”.27 (iii) DMSO is the preferred solvent for all variants of IBX oxidations,28,29 requiring sophisticated work-up protocols to remove the remainder of the hypervalent iodine reagent, for example by addition of chlorinated solvents. It is therefore reasonable to summarize that IBX and its derivatives are not the ideal reagents with respect to the principles of Green Chemistry30,31 since they are mostly used as stoichiometric and non-recyclable reagents.

Several strategies were developed to tackle those issues. For example, modified IBX reagents32–37 for the use in common solvents other than DMSO and safer formulations38,39 of IBX with reduced explosive properties were described. Experimental procedures that aimed at the effective recovery of the reduced form of the hypervalent iodine compounds using biphasic protocols or fluorous techniques led to further improvements.40–44 Polymer-supported IBX reagents were also reported, with the goal to ease work-up protocols and to improve recyclability,45 including polymer-supported variants of IBX,46–50 IBX-amides,51–56 IBX-esters,57 and 2-iodylphenol ethers.58 In addition, the oxidation with catalytic amounts of IBX59–61 and particularly 2-iodoxybenzenesulfonic acid (IBS, 2)62–65 was shown to be highly efficient.66 Those catalytic methods typically rely on Oxone® as the stoichiometrically used co-oxidant,67–74 a reagent that is considered environmentally safe, non-toxic and non-explosive.75 To facilitate the recovery of the hypervalent iodine organocatalyst, fluorous IBX was recently introduced.76 However, the catalytic use of hypervalent iodine oxidants bound to a polymer support was not reported, until now. This is despite the fact that there would be obvious advantages: the iodine-based catalysts are an environmentally sustainable alternative to transition metals, relatively inexpensive and easily recoverable.77

In this paper, we present two new solid-supported hypervalent iodine reagents for the oxidation of secondary alcohols, derived from readily available starting materials: one is based on IBX, and the other is an IBS derivative. In the presence of Oxone®, the two reagents are shown to be highly effective catalysts when using a water–acetonitrile solvent mixture, with catalysts loadings as low as 1 mol%. We also demonstrate that the two metal-free organocatalysts are easily reusable, and work-up protocols consist of simple filtrations. Therefore, our hypervalent iodine compounds may become attractive ‘green catalysts’ in the ever-evolving fields of alcohol oxidations and other challenging oxidative processes.30,31,78–81

Results and discussion

We recently presented the use of solid-supported DMAP–peptide conjugates 3 for the highly regioselective acylation of polyhydroxylated small molecules (Scheme 1).82,83 We now expanded this concept to connect hypervalent iodine precursor units with peptide-modified resins. Our initial plan was to study conjugates 4 consisting of the glycine-modified Merrifield resin and a (poly)alanine linker, the N-terminus of which was connected to the iodine-containing catalyst. For reasons detailed below, we also generated the conjugates 5 and 6 where the (poly)alanine linker was attached to an aminoethyl polystyrene resin. While 5 is based on the same IBX-derived catalytically active unit used for 4, the solid-supported catalyst 6 was designed as a variant of IBS.

Synthesis of the solid-supported precatalysts 4, 5 and 6

We started the synthesis of the precatalyst 4 as summarized in Scheme 2A, using 2-iodobenzoic acid as the commercially available and cheap starting material. Nitration of the aromatic core gave the 5-nitro analogue in 65% yield, as pure substance after simple recrystallization. Subsequent conversion into the tert-butyl ester furnished 7 in excellent yields. Reduction of the nitro group with palladium on charcoal and H2 pressure (8 bar) led to the desired aniline derivative 8 in 82% yield. The iodobenzoic acid variant was coupled to a protected glutamic acid with classical conditions providing the unnatural amino acid 9 in 90% yield. The methyl ester was then saponified while the tert-butyl ester remained untouched: this step was achieved with lithium hydroxide in aqueous THF in 73% yield.
image file: c9gc02605c-s2.tif
Scheme 2 A) Synthesis of solid-supported precatalysts 4 and 5: (a) i) 0 °C, 15 min, (ii) rt, 30 min, (iii) 130 °C, 90 min, (H2SO4/HNO3), 65%; (b) Boc2O (2.5 eq.), DMAP (0.3 eq.), 70 °C, 4 h, (tBuOH), >99%; (c) H2 (8 bar), Pd/C (10 mol%), rt, 18 h, (EtOAc), 82%; (d) Fmoc-Glu(OMe)-OH (1.35 eq.), HATU (1.5 eq.), DIPEA (2 eq.), rt, 18 h, (DMF), 90%; (e) LiOH·H2O (1 eq.), 0 °C to rt, 18 h, (THF/H2O), 73%. (B) Synthesis of solid supported precatalyst 6: (a) H2SO4/SO3 (25%), (H2SO4), 69%; (b) i) NaOH (1.0 eq.), 0 °C, (ii) H2SO4 (20 eq.), 0 °C, (iii) NaNO2 (1.1 eq.), −2 °C, 60 min, (iv) urea (2.0 eq.), −2 °C, 60 min, (v) NaI (1.5 eq.), 0 °C to rt, 18 h, (water), 47%; (c) TBA-Oxone® (5 eq.), MeSO3H (5 eq.), rt, 5 h, (CH2Cl2).

With the Fmoc-protected amino acid 10 in hand, the immobilization on glycin-modified Merrifield resin was accomplished using standard solid-phase peptide synthesis (see ESI for details). Of note, alanine was chosen as the linker amino acid because of the ease of its introduction with SPPS techniques, its lack of functional groups, and its stability toward oxidative conditions (particularly in comparison to glycine). We decided to start with the conjugate 4 having four alanines as linker unit since, at the outset of our studies, we expected that the use of an elongated and flexible linker that provides a spatial separation of the catalytically active part from the polymer body will be advantageous.51 The loading of the resin was determined to be around 0.46 mmol g−1 via UV-VIS measurements (see ESI). The amino acid 10 was also linked to the aminoethyl polystyrene resin giving conjugates 5. We constructed those conjugates with several linker lengths for further tests, with 5a having no alanine unit (n = 0), 5b having two alanines (n = 2) and 5c having four alanines (n = 4). In all cases, a loading between 0.3 and 0.4 mmol g−1 was achieved.

We next focused on the synthesis of the solid-supported precatalyst 6 (Scheme 2B), relying on our previous synthetic approach to the oxidant IBX-SO3K.37,84,85 We began with 4-aminobenzoic acid, which was selectively sulfonylated with fuming sulfuric acid to give the acid 11. Sandmeyer-type conditions furnished iodide 12. All the steps of this sequence are high-yielding without the need for a chromatographic purification, and multiple runs were successfully and reproducibly carried out in multigram scale. The carboxylic acid 12 was then coupled to the polymer resin bearing a single alanine linker to give the conjugate 6′ with a loading of 0.50 mmol g−1. We note that the direct coupling of 12 to the resin was slow and low-yielding when no alanine was involved. The polymer-supported iodoxy reagent 6 was easily obtained upon oxidation of 6′ with the Oxone® tetrabutylammonium salt (TBA-Oxone®).

Oxidations with the solid-supported precatalysts 4, 5 and 6

We then started to test the potential of our new catalytic system 4, choosing the oxidation of borneol 13a as a suitable benchmark reaction. Following previous reports on the catalysed oxidation with IBX and IBS with stoichiometric amounts of Oxone®, the oxidation was initially attempted with 1.6 equivalents of Oxone® at 70 °C in aqueous acetonitrile (70%), in the presence of 4 mol% of polymer bound IBX precatalyst 4. As shown in Table 1 (entry 2), borneol was completely converted into the corresponding ketone 14a under the conditions after 18 h; isolated yields of 14a were high. In a similar way, a range of secondary alcohols including 4-nonanol, menthol, 1,3-diphenylpropan-2-ol and 2,2-dimethyl-1-phenylpropan-1-ol were easily oxidized by use of catalyst 4. The formation of by-products was not detected via 1H NMR or GC-FID analysis of the crude reaction mixture. Hence, the performance of the oxidation reactions was easily screened by determining the ratio of starting substrate 13 and oxidation product 14 with GC-FID in a standardized way. In the absence of precatalyst 4, 8% conversion of the starting substrate were observed after 18 h, thus indicating a minor background reaction with no synthetic use (entry 1). However, it was truly disappointing that the polymeric system 4 lacked a main asset: it was not reusable. A loss of activity was already found in the second cycle when reusing 4 after simple filtration for the borneol oxidation (entry 3). A markedly lowered conversion of 82% was observed after 18 h, under otherwise identical conditions. This trend continued, and the fifth reaction with the same batch of catalyst gave only 15% conversion, demonstrating that resin-supported catalyst 4 had no recyclability of value.
Table 1 Recycling tests with precatalyst 4, 5, 6

image file: c9gc02605c-u1.tif

Entry Catalyst (mol%) Cycle no.a 13a/14ab
a Recycling and reuse of catalyst by filtration.b Ratio 13a/14a was determined via GC-FID (calibrated with stock solutions of 13a and 14a) after 18 h.c With 40 mol% of nBu4NHSO4, 2 h, MeCN.
1 92/8
2 4 (4) 1 (initial) 0/100
3 4 (4) 2 (1st reuse) 18/82
4 4 (4) 3 (2nd reuse) 64/36
5 4 (4) 4 (3rd reuse) 82/18
6 4 (4) 5 (4th reuse) 85/15
7 5c (5) 1 (initial) 0/100
8 5c (5) 2 (1st reuse) 0/100
9 5c (5) 3 (2nd reuse) 0/100
10 5c (5) 4 (3rd reuse) 0/100
11 5c (5) 5 (4th reuse) 19/81
12c 6 (1) 1 (initial) 21/79
13c 6 (1) 2 (1st reuse) 14/86
14c 6 (1) 3 (2nd reuse) 12/88
15c 6 (1) 4 (3rd reuse) 14/86
16c 6 (1) 5 (4th reuse) 19/81
17c 6 (1) 6 (5th reuse) 22/78


The failure of 4 was attributed to the weakness of the ester bond between the Merrifield resin and the glycine linker toward hydrolysis under the reaction conditions. Indeed, control experiments showed that esters were partly hydrolysed in aqueous acetonitrile at 70 °C in the presence of Oxone® while amide bonds remained fully stable. As a result, column chromatography was required to obtain analytically pure oxidation products when employing precatalyst 4. Simple filtration, on the other hand, gave the ketones with traces of impurities that were not unequivocally identified, but may certainly stem from the partial hydrolysis of 4. The design error of 4 then led us to carefully study the systems 5 and 6 where the hypervalent iodine precursor units were connected to the aminoethyl polystyrene resin via more stable amide bonds.

Gratifyingly, it was easily possible to reuse the catalysts 5 and 6 for multiple times, after recycling of the resins through simple filtration. As shown in Table 1 (entries 7–11), the IBX-derived system 5c kept its activity over five cycles, and complete oxidation of borneol was achieved using 5 mol% of the catalyst with 1.6 equivalents of Oxone® at 70 °C in aqueous acetonitrile. Lower catalyst loadings (<2.5 mol%) were shown to provide incomplete conversions, even after elongated reaction times. The IBS variant 6 was effectively reused for five times (Table 1, entries 12–17), accomplishing a constant conversion between 78% and 88%, albeit with lowered catalyst loading (1 mol%) and reduced reaction times (2 h). As a result of the recycling tests, we decided that both systems 5 and 6 based on the aminoethyl polystyrene resin qualify well for catalyzing the oxidation of secondary hydroxy groups under the premise that they deliver easy work-up and multiple reuses.

Our optimization attempts with catalyst 5c then showed that a broad range of reaction conditions is feasible, and the oxidation proceeds equally well in water-free MeNO2, aqueous MeNO2 (30% water) and aqueous MeCN (5–30% water). However, the use of dry acetonitrile as solvent led to significantly diminished yields. Best conversions were achieved between 70 °C and 90 °C, while temperatures below 60 °C did not provide the product of oxidation. To our surprise, the linker length had almost no influence on the catalyst efficiency. As summarized in Table 2, similar conversions were achieved when using 2.5 mol% of the polymers 5a, 5b for the oxidation of nonanol 13b.

Table 2 Effect of the linker length of precatalysts 5a, 5b, 5c

image file: c9gc02605c-u2.tif

Entry Catalyst 13b/14ba
a Ratio 13b/14b was determined via GC-FID (calibrated with stock solutions of 13b and 14b) after 18 h.
1 5a 1/99
2 5b 3/97
3 5c 3/97


The IBS-derived catalyst system 6 turned out to be markedly more active, compared to 5: Table 3 demonstrates that 3 mol% of 6 or of its unoxidized precursor 6′ are sufficient to achieve an excellent conversion at 70 °C in aqueous acetonitrile. The required reaction times were notedly shorter than with IBX derivative 5. Under non-aqueous conditions in acetonitrile or nitromethane, the oxidation proceeded slowly, and the weak conversions were attributed to the low solubility of Oxone® (entries 3 and 4). The addition of substoichiometric amounts of nBu4NHSO4 as phase transfer catalyst resulted in a tremendous rate enhancement.62 In the presence of 0.4 equivalents of nBu4NHSO4, it was easily possible to use 6 with extremely low catalysts loadings of 1 mol% and 0.2 mol% to accomplish useful conversions (entries 8 and 9). Under the conditions, a TON up to 455 was reached with regard to each catalytic center (with a TOF of around 5.3 × 10−3 s−1).

Table 3 Optimization of the oxidations with IBS-derived catalysts 6 and 6′

image file: c9gc02605c-u3.tif

Entry Catalyst (mol%) Additive Solvent 13b/14ba
a Ratio 13b/14b was determined via GC-FID (calibrated with stock solutions of 13b and 14b).b 6 h.c 2 h.d 4 h.e 24 h.
1b 6′ (3) MeCN–H2O (7[thin space (1/6-em)]:[thin space (1/6-em)]3) 5/95
2b 6 (3) MeCN–H2O (7[thin space (1/6-em)]:[thin space (1/6-em)]3) 3/97
3c 6 (2.5) MeCN 94/6
4c 6 (2.5) MeNO2 91/9
5c 6 (2.5) nBu4NHSO4 (10 mol%) MeCN 43/57
6c 6 (2.5) nBu4NHSO4 (10 mol%) MeNO2 63/37
7c 6 (2.5) nBu4NHSO4 (20 mol%) MeCN 3/97
8d 6 (1) nBu4NHSO4 (40 mol%) MeCN 2/98
9e 6 (0.2) nBu4NHSO4 (40 mol%) MeCN 9/91
10d nBu4NHSO4 (40 mol%) MeCN 94/6


The scope of the catalyzed oxidation of secondary alcohols with Oxone® was then explored, using the solid-supported compounds 5c and 6 under standardized conditions. As summarized in Table 4, various structurally diverse secondary alcohols 13 were examined as substrates using method A [5c (5 mol%), Oxone® (1.6 equiv.), 18 h, 70 °C, MeCN–H2O (7[thin space (1/6-em)]:[thin space (1/6-em)]3)] and method B [6 (5 mol%), Oxone® (1.6 equiv.), nBu4NHSO4 (0.4 equiv.), 18 h, 70 °C, MeCN]. We point out that the addition of the phase transfer agent was only required when using non-aqueous conditions (method B); aqueous solvent mixtures (method A) do not require the additive since Oxone® is easily dissolved under the conditions. A general trend was that the performance of the IBS-derived catalyst 6 was superior. In particular, sterically demanding secondary alcohols (e.g., 13a, 13d, 13f and 13k) were easier oxidized to the corresponding ketones using method B. The reaction times until full conversion of the starting substrate were also markedly shorter with 6, compared to 5c (method A). Another advantage of catalyst 6 was that it was employed in a combination with nBu4NHSO4 under non-aqueous conditions, allowing to use other solvents than acetonitrile if required due to solubility issues of the substrate. For example, 5α-cholestan-3β-ol 13s was successfully oxidized with Oxone® and 6 in toluene under otherwise identical conditions (entry 19). The main advantage of method A (with 5c) was the simple work-up protocol consisting only of filtration to remove 5c and subsequent extraction of the aqueous layer. If the starting material was completely converted, further purification by column chromatography was typically not necessary. In the case of method B (with 6), an additional filtration over silica for the removal of the tetrabutylammonium salts was required to obtain analytically pure compounds; the phase transfer agent was not recovered.

Table 4 Scope of the oxidations with catalysts 6 and 5c

image file: c9gc02605c-u4.tif

Entry Alcohol 13 # Ketone 14 Yield [%]a,b Entry Alcohol 13 # Ketone 14 Yield [%]a,b
A B A B
a Isolated yield.b n.r. = experiment was not run.c 3 h.d 24 h.e 72 h in acetone.f 90% from benzoin.g 18 h in toluene.h Determined via GC-FID (calibrated with stock solutions of 13t/14t).
1 image file: c9gc02605c-u5.tif a image file: c9gc02605c-u6.tif 79 91c 11 image file: c9gc02605c-u7.tif k image file: c9gc02605c-u8.tif 76 98
2 image file: c9gc02605c-u9.tif b image file: c9gc02605c-u10.tif 70 79c 12 image file: c9gc02605c-u11.tif l image file: c9gc02605c-u12.tif 82 84
3 image file: c9gc02605c-u13.tif c image file: c9gc02605c-u14.tif 80 85c 13 image file: c9gc02605c-u15.tif m image file: c9gc02605c-u16.tif 71 97f
4 image file: c9gc02605c-u17.tif d image file: c9gc02605c-u18.tif 32 65d 14 image file: c9gc02605c-u19.tif n image file: c9gc02605c-u20.tif n.r. 89
5 image file: c9gc02605c-u21.tif e image file: c9gc02605c-u22.tif 71 83 15 image file: c9gc02605c-u23.tif o image file: c9gc02605c-u24.tif 0 66c
6 image file: c9gc02605c-u25.tif f image file: c9gc02605c-u26.tif 0 32e 16 image file: c9gc02605c-u27.tif p image file: c9gc02605c-u28.tif 0 66c
7 image file: c9gc02605c-u29.tif g image file: c9gc02605c-u30.tif 82 85 17 image file: c9gc02605c-u31.tif q image file: c9gc02605c-u32.tif 95 96
8 image file: c9gc02605c-u33.tif h image file: c9gc02605c-u34.tif 84 84 18 image file: c9gc02605c-u35.tif r image file: c9gc02605c-u36.tif 0 61
9 image file: c9gc02605c-u37.tif i image file: c9gc02605c-u38.tif n.r. 98c 19 image file: c9gc02605c-u39.tif s image file: c9gc02605c-u40.tif 0 78g
10 image file: c9gc02605c-u41.tif j image file: c9gc02605c-u42.tif 75/58/69/82/63 86/79/85/86/82 20 image file: c9gc02605c-u43.tif t image file: c9gc02605c-u44.tif n.r. 75h


We point out that primary alcohols also provide oxidation products under the conditions of method B. However, aldehydes were produced in markedly reduced yields and mixed with various products of over-oxidation, thus limiting the use of the catalytic system tremendously. In the case of primary allylic alcohols 15, it was possible to isolate the corresponding aldehydes in pure form and moderate yields, as outlined for 16a and 16b in Scheme 3. Two other limitations of our catalyst system for the oxidation of secondary alcohols were identified in the course of our studies: (1) phenols are not stable under the conditions,14,15 and (2) amines are not tolerated due to various competing condensation and oxidation reactions that were not further analyzed.


image file: c9gc02605c-s3.tif
Scheme 3 Oxidation of primary allylic alcohols 15 by use of 6.

Method B using IBS-derived polymer 6 is also easily applicable to larger scales, as demonstrated in Scheme 4 for the conversion of secondary alcohol 13b into ketone 14b: 50 mmol of 13b led to the isolation of the desired ketone with 80% yield after 5 h, using only 1 mol% of catalyst 6. Of note, 95% of the supported catalyst were recovered for re-uses.


image file: c9gc02605c-s4.tif
Scheme 4 Oxidation of 13b on a 50 mmol-scale by use of 6.

Conclusions

We have presented two new catalytic systems 5c (based on IBX) and 6 (based on IBS) that are outstanding tools for the oxidation of secondary alcohols with Oxone® under ketone formation. The catalysts, derived from hypervalent iodine reagents linked to a polymer support, are highly active, and a broad scope is demonstrated for both catalysts. However, the catalytic oxidation with 6 proceeded more rapidly and cleanly. After completion of the reaction, the catalysts were recovered through simple filtration, and it was possible to reuse them for multiple times, thus rendering them highly attractive for the objectives of Green Chemistry: recoverable and prepared from readily available starting materials consisting of abundant chemical elements.

Our future studies will make use of the catalyst systems for chemoselective oxidations, by varying the linker units. We will also show in due course how the immobilized catalysts are of use in flow chemical oxidation processes.

Conflicts of interest

There are no conflicts to declare.

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Footnote

Electronic supplementary information (ESI) available: Experimental procedures, analytical data and copies of 1H, 13C NMR-spectra. See DOI: 10.1039/c9gc02605c

This journal is © The Royal Society of Chemistry 2019