2013
DOI: 10.1016/j.cej.2013.05.111
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Investigations on the kinetics and thermodynamics of dilute acid hydrolysis of Parthenium hysterophorus L. substrate

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Cited by 21 publications
(10 citation statements)
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“…Employing first order kinetic model only sugars production rate constants are calculated. According to Swati et al (2013), this model can be used for hydrolysis processes despising sugars decomposition, as shown in Table 2 rate constants obtained with first order model were lower in comparison to that obtained with Saeman and Saeman biphasic models, furthermore R 2 coefficients diminished. Experimental data for Furfural production were fitted to first order kinetic model (Figure 5), P o did not correspond to initial amount of holocellulose.…”
Section: S Ug Maxmentioning
confidence: 90%
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“…Employing first order kinetic model only sugars production rate constants are calculated. According to Swati et al (2013), this model can be used for hydrolysis processes despising sugars decomposition, as shown in Table 2 rate constants obtained with first order model were lower in comparison to that obtained with Saeman and Saeman biphasic models, furthermore R 2 coefficients diminished. Experimental data for Furfural production were fitted to first order kinetic model (Figure 5), P o did not correspond to initial amount of holocellulose.…”
Section: S Ug Maxmentioning
confidence: 90%
“…The k 2 rate constant observed in Saeman model corresponds to thermal decomposition of sugars into aldehydes, however, if this decomposition phase is not appreciated in experimental data first order kinetic model (Eq. 4) can be used as was reported by Swati et al (2013).…”
Section: Kinetic and Thermodynamic Parameters Calculationmentioning
confidence: 99%
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“…As a result, 86% of total sugars, which included glucose, 61% of the initial cellulose, were obtained in a 1 wt % formic acid solution . Although kinetic studies on actual biomass materials such as agricultural wastes, wood, , grasses, , medicinal plants, and waste newspaper have been reported under hydrothermal conditions, mostly in the presence of acids, those on pure fibrous cellulose samples rather than cellulose powder , are limited. From a practical point of view, these studies on the actual cellulosic biomass are of importance, but because of other ingredients such as hemicellulose and lignin in the systems, it is difficult to study the effects of reaction conditions on both the rates and product distributions.…”
Section: Introductionmentioning
confidence: 99%