2012
DOI: 10.1039/c2gc16679h
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An efficient recyclable peroxometalate-based polymer-immobilised ionic liquid phase (PIILP) catalyst for hydrogen peroxide-mediated oxidation

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Cited by 54 publications
(34 citation statements)
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“…Peroxometalate-based PIILP [PO 4 {WO(O 2 ) 2 } 4 ]@PIILP (2) was prepared by stoichiometric exchange of the bromide anions in pyrrolidinium-based ROMP-derived polymer 1 with [PO 4 {WO(O 2 ) 2 } 4 ] 3-(Scheme 1) 30a and the resulting amorphous white solid that precipitated was characterized by a combination of solid state P-31 NMR spectroscopy, ICP-OES (tungsten content), nitrogen sorption analysis, TEM and TGA/DSC. A series of catalytic reactions was first conducted under batch conditions to evaluate the efficiency of 2 as a catalyst for sulfide oxidation and to undertake preliminary optimization studies and recycle experiments.…”
Section: Catalyst Synthesis Batch and Recycle Studiesmentioning
confidence: 99%
See 1 more Smart Citation
“…Peroxometalate-based PIILP [PO 4 {WO(O 2 ) 2 } 4 ]@PIILP (2) was prepared by stoichiometric exchange of the bromide anions in pyrrolidinium-based ROMP-derived polymer 1 with [PO 4 {WO(O 2 ) 2 } 4 ] 3-(Scheme 1) 30a and the resulting amorphous white solid that precipitated was characterized by a combination of solid state P-31 NMR spectroscopy, ICP-OES (tungsten content), nitrogen sorption analysis, TEM and TGA/DSC. A series of catalytic reactions was first conducted under batch conditions to evaluate the efficiency of 2 as a catalyst for sulfide oxidation and to undertake preliminary optimization studies and recycle experiments.…”
Section: Catalyst Synthesis Batch and Recycle Studiesmentioning
confidence: 99%
“…S43 1 H and 13 C{ 1 H} NMR spectra and mass spectra for oxidation sulfoxides and sulfones S58Figure S44FT-IR Spectra of (a) fresh[PO 4 {WO(O 2 ) 2 } 4 ]@PIILP(2) and(b) catalyst isolated after the 6 th run of a methanol recycle experimentS59 Figure S45 Conversion-selectivity profile as a function of temperature for the continuous flow [PO 4 {WO(O 2 ) 2 } 4 ]@PIILP-catalysed sulfoxidation of thioanisole in acetonitrile with a residence time of 4 min S60 Figure S46 Conversion-selectivity profile as a function of temperature for the continuous flow [PO 4 {WO(O 2 ) 2 } 4 ]@PIILP-catalysed sulfoxidation of thioanisole in methanol with a residence time of 4 min S61 Figure S47 Conversion-selectivity profile as a function of residence time for the [PO 4 {WO(O 2 ) 2 } 4 ]@PIILP-catalyzed sulfoxidation of thioanisole in acetonitrile at 30 °C Conversion-selectivity profile as a function of residence time for the [PO 4 {WO(O 2 ) 2 } 4 ]@PIILP-catalyzed sulfoxidation of thioanisole in acetonitrile at 30 °C Conversion-selectivity profile as a function of residence time for the [PO 4 {WO(O 2 ) 2 } 4 ]@PIILP-catalyzed sulfoxidation of thioanisole in acetonitrile at 30 °C with 6 equivalents of H 2 O 2 . S66 Figure S52 Conversion-selectivity profile as a function of residence time for the [PO 4 {WO(O 2 ) 2 } 4 ]@PIILP-catalyzed sulfoxidation of thioanisole in acetonitrile at 30 °C with 12 equivalents of H 2 O 2 S67 Figure S53a,b Determination of rate constants for the formation of methyl phenyl sulfoxide (k a ) and methyl phenyl sulfone (k b ) in acetonitrile with 12 equivalents of H 2 O 2 by fitting the concentrationtime profile for the consumption of sulfide and the formation of product.…”
mentioning
confidence: 99%
“…For the catalysts POSS-IL 8 -PW containing different IL, POSS-BIM 8 - 15 PW having a C4 hydrophobic tail displays a 90% conversion (entry 8), which is lower than those of the catalysts POSS-OIM 8 -PW, POSS-DIM 8 -PW and POSS-HIM 8 -PW carrying C8, C12, and C16 alkyl chain, respectively (entries 5, 9 and 10). Also notably, for the POSS-free samples containing different IL, the 20 increase of the length of alkyl chain in IL leads to continuous increase in the catalytic conversion from 45% to 80% (entries [11][12][13][14]. However, they are much lower than those of the POSScontaining ones.…”
Section: Catalytic Activity In the Epoxidation Reactionmentioning
confidence: 99%
“…Due to these evident advantages, PW 4 has received significant attention as an active component for construction of heterogeneous epoxidation catalysts (Neumann and Miller, 1995;Neumann and Cohen, 1997;Hoegaerts et al, 2000;Sakamoto and Pac, 2000;Sels et al, 2000;Kovalchuk et al, 2007;Sofia et al, 2009;Maksimchuk et al, 2010;Leng et al, 2011;Doherty et al, 2012;Swalus et al, 2013;Nojima et al, 2015;Peng et al, 2016;Masteri-Farahani and Modarres, 2017;Shen et al, 2017;You et al, 2018). Silica modified by various cationic functional groups was widely used as support for immobilization of PW 4 (Neumann and Miller, 1995;Neumann and Cohen, 1997;Hoegaerts et al, 2000;Sakamoto and Pac, 2000;Kovalchuk et al, 2007;Sofia et al, 2009).…”
Section: Introductionmentioning
confidence: 99%
“…Some of the SiO 2 -supported catalysts were prone to leaching and/or had a poor recyclability Kovalchuk et al, 2007) (sometimes information about reusability was not provided Neumann and Miller, 1995;Sakamoto and Pac, 2000). Several catalysts based on ion-exchange organic polymers and PW 4 have been developed Doherty et al, 2012;Swalus et al, 2013;Peng et al, 2016;Shen et al, 2017;You et al, 2018). In general, catalysts PW 4 /polymer showed high selectivity for epoxides and most of them could be recycled without a decrease in attainable conversion and selectivity Swalus et al, 2013;Peng et al, 2016;Shen et al, 2017;You et al, 2018).…”
Section: Introductionmentioning
confidence: 99%