2016
DOI: 10.1016/j.apcata.2016.03.028
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Corrigendum to “Esterification of levulinic acid with butanol over ion exchange resins” [Appl. Catal. A: Gen. 517 (2016) 56–66]

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Cited by 8 publications
(12 citation statements)
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“…The results in Fig. are shown for the conversion of CA and indicate that increasing loading of the catalyst enhances the conversion obtained for the esterification reaction , . This is because an increase in catalyst loading enhances the number of active acidic sites available in the ion‐exchange resin catalyst, which subsequently enhances the conversion of CA.…”
Section: Resultsmentioning
confidence: 86%
“…The results in Fig. are shown for the conversion of CA and indicate that increasing loading of the catalyst enhances the conversion obtained for the esterification reaction , . This is because an increase in catalyst loading enhances the number of active acidic sites available in the ion‐exchange resin catalyst, which subsequently enhances the conversion of CA.…”
Section: Resultsmentioning
confidence: 86%
“…[54] Therefore, it is worthy to note that large reactants ratio (methanol) does not necessarily translate to more conversion, especially when the active sites are insufficient. [16,55] In a different type of esterification study, Tejero et al [4] prepared butyl levulinate from the esterification reaction between levulinic acid and 1-butanol (BuOH) over ionic resins. Experimental setup conditions were set at 80°C, 2.5 MPa, catalyst loading 0.8% in a reactant ratio of 1 : 3 Al: BuOH.…”
Section: Esterification Reactionmentioning
confidence: 99%
“…[1,2] Figure 1 presents a resin structure made up of macro and micro pores; the macro pores providing routes for faster diffusion of reactants and a population of micro pores housing the ion exchange sites which are responsible for its activity. [3][4][5] The distribution of the macro and micro pores of the resin has a direct link to its effectiveness and functionality. [6] The specific and selective nature of ion exchange resins allows for its use in a wide range of separation processes.…”
Section: Introductionmentioning
confidence: 99%
“…Several strong inorganic acids such as sulfuric acid and hydrochloric acid were employed in the past for the esterification reaction. Even though these acid catalysts possess a strong activity, the application of such catalysts encounters limitation in terms of equipment corrosion, non-reusability, tedious separation process, and environmental concerns [3]. Owing to the requirement of sustainable development, the use of a heterogeneous solid acid catalyst for the esterification reaction was intensified.…”
Section: Introductionmentioning
confidence: 99%