2022
DOI: 10.1016/j.jtice.2022.104277
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12-Tungstophosphoric acid-encapsulated metal-organic framework UiO-66: A promising catalyst for the esterification of acetic acid with n-butanol

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Cited by 19 publications
(10 citation statements)
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“…Interestingly, the increase in relative intensity in the composite (Cu-BTC_PMA) compared with the parent MOF (Cu-BTC) was observed and may be due to high crystallinity which was previously reported by Zhang et al 89 Thermal gravimetric analysis (TGA) (Figure S20b) showed that the thermal stability of composite catalyst (Cu-BTC_PMA) was found to be superior to that of the parent MOF (Cu-BTC). 60,90,91 This may be due to the enhancement of crystallinity in the Cu-BTC_PMA catalyst after the incorporation of PMA in the Cu-BTC framework which is also supported by the PXRD results.…”
Section: ■ Results and Discussionmentioning
confidence: 80%
“…Interestingly, the increase in relative intensity in the composite (Cu-BTC_PMA) compared with the parent MOF (Cu-BTC) was observed and may be due to high crystallinity which was previously reported by Zhang et al 89 Thermal gravimetric analysis (TGA) (Figure S20b) showed that the thermal stability of composite catalyst (Cu-BTC_PMA) was found to be superior to that of the parent MOF (Cu-BTC). 60,90,91 This may be due to the enhancement of crystallinity in the Cu-BTC_PMA catalyst after the incorporation of PMA in the Cu-BTC framework which is also supported by the PXRD results.…”
Section: ■ Results and Discussionmentioning
confidence: 80%
“…The highest yield obtained was 83.6% and 88.8% when utilised 4 wt.% of glycerol-SO 3 H and glycerol-ClSO 3 H, respectively. However, yield reduction was found (73.3% and 76.5%) for the reaction of 5 wt.% catalyst loading due to mass transfer difficulty initiated for reversable reaction, as discussed by Ma et al [ 27 ]. Therefore, 3 wt.% of catalyst loading was selected for further esterification reaction.…”
Section: Resultsmentioning
confidence: 96%
“…Figure 2 displayed the evaluation of solid glycerol catalysts for acid properties by NH 3 -TPD method and the amount of total acidity strength as tabulated in Table 1 . A sharp and intense peak presented at a low-temperature range of 150–450 °C, possessing the weak Brönsted acid sites that consist of phenolic (-OH) and carboxylic groups interacted during adsorption-desorption with ammonia gas [ 27 ]. The interaction between NH 3 and SO 3 H/ClSO 3 H species demonstrated a desorption curve such as strong Brönsted acid sites that occurred at temperatures 450–700 °C, respectively [ 28 ].…”
Section: Resultsmentioning
confidence: 99%
“…This is despite their high activity, solubility in many polar solvents, and very low surface area, which limit their application for catalysis. Therefore, the loading of various HPAs on Zr-based MOF materials has been performed [ 47 , 48 ].…”
Section: Zr-based Mof Catalystsmentioning
confidence: 99%