2019
DOI: 10.1016/j.mcat.2019.03.012
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Succinimide-KI: An efficient binary catalyst system for mild, solvent-free cycloaddition of CO2 to epoxides

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Cited by 30 publications
(6 citation statements)
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“…Interestingly, halides such as NaI and KI can be extracted from waste biomass such as seaweed . Nevertheless, group I halides, when used alone, are sluggish catalysts for the target reaction , due to poor solubility and low Lewis acidity, and they require the assistance of or activation by additional catalytic components; potassium iodide has been frequently applied as a source of nucleophilic halides in the presence of catalytic components such as amino acids , and other homogeneous ,, or heterogeneous , hydrogen bond donors, N-heterocyclic carbenes, , crown ethers, and others . However, the reaction conditions associated with such systems are generally relatively harsh, especially in the case of partially heterogeneous systems where the additional, and often more expensive, catalytic moiety is recovered (80–120 °C, 10–20 bar CO 2 ). ,, This is even more the case of sodium halides as their application in the solventless cycloaddition of CO 2 to epoxides is relatively uncommon and generally requires high reaction temperatures (120–130 °C) and pressures (20–40 bar) to afford reasonable to high yields of cyclic carbonates.…”
Section: Introductionmentioning
confidence: 99%
“…Interestingly, halides such as NaI and KI can be extracted from waste biomass such as seaweed . Nevertheless, group I halides, when used alone, are sluggish catalysts for the target reaction , due to poor solubility and low Lewis acidity, and they require the assistance of or activation by additional catalytic components; potassium iodide has been frequently applied as a source of nucleophilic halides in the presence of catalytic components such as amino acids , and other homogeneous ,, or heterogeneous , hydrogen bond donors, N-heterocyclic carbenes, , crown ethers, and others . However, the reaction conditions associated with such systems are generally relatively harsh, especially in the case of partially heterogeneous systems where the additional, and often more expensive, catalytic moiety is recovered (80–120 °C, 10–20 bar CO 2 ). ,, This is even more the case of sodium halides as their application in the solventless cycloaddition of CO 2 to epoxides is relatively uncommon and generally requires high reaction temperatures (120–130 °C) and pressures (20–40 bar) to afford reasonable to high yields of cyclic carbonates.…”
Section: Introductionmentioning
confidence: 99%
“…S8 †). 14 Subsequently, the apparent activation energy and pre-exponential factors can be obtained by using the Arrhenius equation (Fig. 4b).…”
mentioning
confidence: 99%
“…The result for ln­[PO] ~ t and lnk obs ~ T –1 can be obtained experimentally (Figure ), from which the pre-exponential factor A and the apparent activation energy ( E a ) can be estimated (see the details in Supporting Information), being 2.703 × 10 2 min –1 and 33.30 kJ·mol –1 , respectively. Because the E a for the cycloaddition catalyzed by KI alone was 43.0 kJ·mol –1 , AM and KI lead to activation energy reduction by 9.7 kJ·mol –1 .…”
Section: Resultsmentioning
confidence: 99%