Sandeep S. Kahandala,
Sandip R. Kalea,
Manoj B. Gawande*b,
Radek Zborilb,
Rajender S. Varma*c and
Radha V. Jayaram*a
aDepartment of Chemistry, Institute of Chemical Technology (Autonomous), N. Parekh Marg, Matunga, Mumbai 400 019, India. E-mail: rv.jayaram@ictmumbai.edu.in; Fax: +91(22)24145614
bRegional Centre of Advanced Technologies and Materials, Faculty of Science, Department of Physical Chemistry, Palacky University, Šlechtitelů 11, 783 71 Olomouc, Czech Republic. E-mail: mbgawande@yahoo.co.in; manoj.gawande@upol.cz
cSustainable Technology Division, National Risk Management Research Laboratory, US Environmental Protection Agency, MS 443, 26 West Martin Luther King Drive, Cincinnati, Ohio 45268, USA. E-mail: Varma.Rajender@epamail.epa.gov
First published on 21st November 2013
An environmentally benign method for the selective monoiodination of diverse aromatic compounds has been developed using reusable sulphated ceria–zirconia under mild conditions. The protocol provides moderate to good yields and selectively introduces iodine at the para/ortho position in monosubstituted arenes. SO42−/Ce0.07Zr0.93O2 was found to be the best choice for the synthesis of aryl iodides in high yield, presumably due to the maximum number of acid sites (4.23 mmol g−1) among the various compositions of the catalyst system.
Numerous Pd coupling reactions including the Heck,6 Stille,7 Suzuki,8 and Sonogashira9 reactions require aromatic halides as precursors to prepare more complex targets and aromatic iodides are among the most versatile building blocks in this category. Although there are numerous examples (direct or indirect synthesis), where electrophilic aromatic substitution is used to replace an aryl hydrogen atom with a halogen group, iodination still remains a difficult transformation to facilitate.10 Iodo compounds are often synthesized via the reduction of nitroarenes followed by the Sandmeyer reaction. Bromination and chlorination easily proceed with, or sometimes without, Lewis acid catalysts, but iodination is usually more difficult owing to the low electrophilicity of iodide. Hence, efforts are being made towards the development of efficient, selective and mild methods for the direct introduction of iodine into organic compounds. Besides the use of volatile organic solvents as reaction media, most of the methods studied used harsh reaction conditions, such as the extensive use of strong acids or the use of heavy metal salts and the need for oxidants as activators for iodine;11 this requires special safety precautions in experimental handling and generates serious concerns regarding environmental and health issues.
PEG is a non-toxic, inexpensive, and non-volatile solvent, employed in synthetic chemistry for various organic transformations.12 It also has good thermal stability, and is miscible with a number of organic solvents.
The development of mild, cost effective and environmentally benign catalytic procedures for the iodination of aromatic compounds is a fertile area of research. Previously, heterogeneous metal oxides and sulfate catalysts have been deployed as acid or oxidative catalysts for iodination chemistry.13
Recently, we have found that ceria–zirconia mixed oxides can act as an efficient bifunctional catalyst system for the sequential epoxidation–aminolysis of styrenes.14 The sulphated form of these mixed oxides has been found to be a good catalyst for the modified Ritter reaction.15 In a continuation of research activities on the development of benign protocols using heterogeneous catalysts,16–18 we have now explored the catalytic activity of these oxides for the iodination of arenes. Herein, we report a mild and experimentally simple catalytic method for the synthesis of iodoarenes using sulphated ceria–zirconia as a heterogeneous, inexpensive and recyclable catalyst. The method does not require the addition of any oxidant or activator, such as heavy metals (lead, mercury and chromium). The mild reaction conditions and the use of PEG-200 as a green solvent make the process environmentally benign and hazard-free (Scheme 1).
Entry | Catalyst | BET Surface area (m2 g−1) | Acidity (mmol g−1)b | Ei (mV)c | Conversion (%)d | Selectivity (%)e | Yield (%)f |
---|---|---|---|---|---|---|---|
a Reaction conditions: aniline (2 mmol), I2 (2 mmol), PEG-200 (2 ml), 12 h, RT, catalyst (15 wt% w.r.t. aniline).b Surface acidity values determined using the n-butylamine potentiometric titration method.c Ei initial electrode potential (mV).d Conversion determined using GC analysis.e Selectivity determined using GC analysis.f Isolated yields.g 24 h.h 7.5 (wt%) of each w.r.t. aniline. | |||||||
1g | 30 | 80/20 | 25 | ||||
2 | H2SO4 | — | — | — | 70 | 85/15 | 54 |
3 | ZrSO4 | — | — | — | 45 | 67/33 | 27 |
4 | ZrO2 | 12 | 0.8 | 55 | 60 | 93/7 | 48 |
5 | CeO2 | 10 | 0.3 | 27 | 45 | 91/9 | 35 |
6 | SO42−/ZrO2 | 37 | 2.07 | 168 | 84 | 96/4 | 77 |
7 | SO42−/CeO2 | 23 | 1.22 | 154 | 54 | 85/15 | 43 |
8 | Ce0.07Zr0.93O2 | 17 | 1.54 | 157 | 43 | 100 | 38 |
9h | SO42−/CeO2 + SO42−/ZrO2 | — | — | — | 65 | 88/12 | 55 |
10 | SO42−/Ce0.02Zr0.98O2 | 22 | 3.17 | 440 | 80 | 100 | 76 |
11 | SO42−/Ce0.07Zr0.93O2 | 53 | 4.23 | 560 | 100 | 100 | 97 |
12 | SO42−/Ce0.10Zr0.90O2 | 28 | 3.52 | 450 | 82 | 100 | 75 |
13 | SO42−/Ce0.15Zr0.85O2 | 14 | 3.50 | 460 | 62 | 98/2 | 55 |
14 | SO42−/Ce0.20Zr0.80O2 | 12 | 2.97 | 248 | 57 | 95/5 | 49 |
15 | SO42−/Ce0.25Zr0.75O2 | 10 | 2.17 | 197 | 53 | 95/5 | 44 |
16 | SO42−/Y0.04Zr0.96O2 | 34 | 1.23 | 148 | 56 | 92/8 | 46 |
17 | SO42−/Y0.08Zr0.92O2 | 43 | 1.64 | 195 | 54 | 90/10 | 48 |
18 | SO42−/Y0.12Zr0.88O2 | 52 | 1.93 | 310 | 68 | 90/10 | 57 |
19 | SO42−/Y0.16Zr0.84O2 | 75 | 4.19 | 530 | 92 | 94/6 | 86 |
20 | SO42−/Y0.20Zr0.80O2 | 35 | 2.91 | 330 | 69 | 99/1 | 65 |
21 | SO42−/Y0.24Zr0.76O2 | 29 | 2.65 | 248 | 60 | 100 | 56 |
Among the various catalysts tested in the study, SO42−/CexZr1−xO2 gave the maximum yield (97%) with preferential para selectivity. In the absence of a catalyst only a 25% yield of 4-iodoaniline was obtained even after 24 h under the present reaction conditions (Table 1, entry 1).
When the same reaction was carried out in the presence of other reported catalysts such as H2SO4, ZrSO4, low yields and poor regioselectivity were observed (Table 1, entries 2 and 3). Also, with single component oxides – CeO2 or ZrO2, only a 35–48% yield of 4-iodoaniline was obtained (Table 1, entries 4 and 5). However, upon sulphation, the yield of 4-iodoaniline increased to 43–77% (Table 1, entries 6 and 7) with improved selectivity. A physical mixture of SO42−/CeO2 and SO42−/ZrO2 (10 wt% of each) gives a 55% yield, with poor regioselectivity towards 4-iodoaniline (Table 1, entry 8). The investigation was further extended to several compositions of sulphated ceria–zirconia and sulphated yttria–zirconia catalysts. It was observed that the sulphated ceria–zirconia system gave better yields/regioselectivity for the synthesis of iodoanilne compared to sulphated yttria–zirconia catalysts (Table 1, entry 10–21).
As the cerium content in SO42−/CexZr1−xO2 was increased from 0.02–0.07 mol%, the total acidity and surface area of the catalysts were also found to increase. A further increase in cerium content resulted in a decrease in both total acidity and surface area (see ESI†), which was also manifested in the activity and selectivity of the reaction.
When the reaction was carried out with SO42−/Ce0.07Zr0.93O2 catalyst, 97% yield with 100% selectivity for 4-iodoaniline was obtained, which is the highest among the various compositions of SO42−/CexZr1−xO2 studied (Table 1, entry 11). This could be due to the maximum value in the number of acid sites (4.23 mmol g−1) and acid strength as determined by potentiometric titration using n-butylamine.19 In this method, the initial electrode potential (Ei) indicates the strength of the acid sites and the end point of the titration is related to the number of acidic sites (mmol g−1). For comparison, a test reaction was also carried out with non-sulphated Ce0.07Zr0.93O2, which gave a 38% yield of 4-iodoaniline (Table 1, entry 8). We also explored the effect of surface ratio of (Ce/Zr) and surface density of sulphation. The highest surface sulphate ratio of Ce/Zr (0.075) was obtained with SO42−/Ce0.07Zr0.93O2, which was also found to have maximum acid sites (ESI Table 2†).
The effect of various reaction parameters such as catalyst loading, solvent system etc. was also investigated for the model reaction. An increase in initial catalyst loading, up to 15 wt%, results in an increased yield of the product while further increase has no profound effect (Table 2, entry 1–5).
The solvent plays a key role in catalyst activity and thus choice of the proper solvent is crucial (Table 3). The synthesis of iodoanilne under solvent-free conditions gave a 35% yield of the desired product (Table 3, entry 1). It was observed that non-polar solvents like 1,4 dioxane, n-hexane and mildly polar solvents like chloroform, ethyl acetate, tetrahydrofuran, dichloromethane, and dichloroethane gave good to moderate yields of the product (Table 3, entries 2–8). Polar solvents such as methanol, acetonitrile and ethanol, were found to be better reaction media for iodination (Table 3, entries 9–11). Interestingly, when the reaction was carried out in acetone (Table 3, entry 12), it reacted with aniline to form 2,2,4-trimethyl-1,2-dihydroquinoline as the exclusive product.
Entry | Solvent | Yield (%)b |
---|---|---|
a Reaction conditions: aniline (2 mmol), I2 (2 mmol), solvent (2 ml), 12 h, RT, SO42−/Ce0.07Zr0.93O2 catalyst (15 wt% w.r.t. aniline).b Isolated yields. | ||
1 | — | 35 |
2 | 1,4 Dioxane | 49 |
3 | n-Hexane | 54 |
4 | Chloroform | 60 |
5 | Ethyl acetate | 65 |
6 | Tetrahydrofuran | 67 |
7 | Dichloromethane | 78 |
8 | Dichloroethane | 80 |
9 | Methanol | 83 |
10 | Acetonitrile | 85 |
11 | Ethanol | 87 |
12 | Acetone | 0 |
13 | PEG-200 | 97 |
14 | PEG-400 | 85 |
15 | PEG-600 | 79 |
As the primary goal of this study was to develop a process that is ‘green’ and environmentally viable, the iodination reaction was conducted in polyethylene glycol (PEG); (Table 3, entries 13–15) PEG-200 gave the highest yield (97%) of 4-iodoaniline (Table 3, entry 13). Hayase et al. have studied the interaction of molecular iodine with PEG and proposed that the interatomic distance in the iodine molecule slightly increased when the concentration of PEG was larger than a limiting concentration, C1. It was observed that C1 decreased with an increase in the molecular weight of PEG in the case of molecular weights below 300 and was unaffected for higher molecular weights of PEG.20
In the iodination reaction, an increase in the interatomic distance would result in weakening of the I–I bond in molecular iodine, which in turn would favour the electrophilic aromatic substitution reaction. See ESI for UV-Vis spectra of I2+PEG-200-600.†λmax = 360 nm corresponds to diatomic I2, which is slightly shifted by interaction with the solvent (PEG).20
Interestingly, when the iodination reaction was carried out with ICl, poor regioselectivity was observed as evidenced by the presence of polyiodination products of aniline shown by GC and GC-MS analysis (m/z (%) = 345 (100%) M+) (Scheme 3 and Fig. 7 ESI†).
When different iodine sources were used for the synthesis of 4-iodoaniline, it was observed that molecular iodine gave better yield and selectivity over iodine monochloride and N-iodosuccinimide under similar experimental conditions (Table 4, entries 1–3).
To evaluate the applicability of the SO42−/Ce0.07Zr0.93O2 catalytic system for iodination, the reactions of structurally varied and electronically diverse amines and phenols were carried out with I2 and PEG-200 as a reaction medium; the results are summarized in Table 5. Iodination of aniline preferably takes place at the para position, with a high yield (97%) of the product (Table 5, entry 1). When reaction of 4-iodoaniline was carried out with I2, 2,4-diiodoaniline was obtained also with an excellent yield of 95% (Table 5, entry 2). The iodination reaction of various arenes exhibited a strong dependency on the electron withdrawing and donating nature of the substituents present in the aromatic ring. Reactions of substituted anilines containing a strong electron withdrawing nitro group (–NO2) at the ortho, meta and para positions gave moderate yield of the products (Table 5, entries 3–5). 3-Chloroaniline, gave 4-iodo-3-chloroaniline in an excellent yield, whereas with 4-chloroaniline under the same reaction conditions, only a moderate yield of 2-iodo-4-chloroaniline was obtained (Table 5, entries 6 and 7). Interestingly, it was found that when the reaction of diphenylamine and diphenyl ether was carried out with two equivalents of I2, only monoiodination occurred at one of the aromatic rings (Table 5, entries 8 and 9). The present reaction system was also applicable for the iodination of N,N-dimethylaniline, 4-methylaniline, 3-methoxyanisole and anisole (Table 5, entries 10–13).
Entry | Substrate | Product | Time (h) | Yield (%)b |
---|---|---|---|---|
a Reaction conditions: Arene (2 mmol), I2 (2 mmol), PEG-200 (2 ml), RT, SO42−/Ce0.07Zr0.93O2 catalyst (15 wt% w.r.t. arene).b Isolated yields, NR – no reaction. | ||||
1 | ![]() |
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12 | 97 |
2 | ![]() |
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12 | 95 |
3 | ![]() |
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12 | 52 |
4 | ![]() |
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12 | 70 |
5 | ![]() |
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12 | 61 |
6 | ![]() |
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12 | 95 |
7 | ![]() |
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12 | 60 |
8 | ![]() |
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12 | 85 |
9 | ![]() |
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12 | 35 |
10 | ![]() |
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12 | 99 |
11 | ![]() |
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12 | 96 |
12 | ![]() |
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12 | 85 |
13 | ![]() |
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12 | 95 |
14 | ![]() |
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12 | 82 |
15 | ![]() |
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12 | 75 |
16 | ![]() |
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15 | 75 |
17 | ![]() |
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15 | 70 |
18 | ![]() |
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15 | 45 |
19 | ![]() |
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15 | 30 |
20 | ![]() |
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24 | NR |
21 | ![]() |
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24 | NR |
To further expand the generality of the protocol, iodination of several phenols were carried out under the optimized reaction conditions (Table 5, entries 14–19). The reaction of phenol gave good yields of 4-iodophenol (Table 5, entry 14). The presence of electron donating and withdrawing substituents such as –CH3, –C(CH3)3, –CHO and –Cl (ortho and ortho, para), which strongly influence the substitution reaction gave moderate to good yields of the products (Table 5, entries 15–19). Iodination of benzene and benzoic acid did not take place even when the reaction was conducted for 24 h (Table 5, entries 20 and 21). This indicates that the present process requires the presence of an electron donating group on the aromatic ring to facilitate the electrophilic aromatic substitution reaction.
Footnote |
† Electronic supplementary information (ESI) available: Experimental details, catalyst characterization data and GCMS spectra of all prepared compounds. See DOI: 10.1039/c3ra46537c |
This journal is © The Royal Society of Chemistry 2014 |