Separation and Purification Technologies in Biorefineries 2013
DOI: 10.1002/9781118493441.ch18
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Cellulosic Bioethanol Production

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Cited by 9 publications
(6 citation statements)
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“…The studies described throughout this review demonstrate the feasibility of producing ethanol from different pulp and paper industry wastes. However, in many studies using Kraft pulp (Table 3), SSL (Table 4), or PPMS (Table 5), the concentrations of ethanol obtained in the fermentation broth were much lower than the recommended minimum of 4 wt % that is required to have a lower energy demand in the recovery step [93]. The most used method in the recovery of ethanol, distillation, is energy-intensive, accounting for 60−80% of the total separation cost of bioethanol from water, particularly due to low ethanol concentrations in the fermented broth [94].…”
Section: Future Prospectsmentioning
confidence: 97%
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“…The studies described throughout this review demonstrate the feasibility of producing ethanol from different pulp and paper industry wastes. However, in many studies using Kraft pulp (Table 3), SSL (Table 4), or PPMS (Table 5), the concentrations of ethanol obtained in the fermentation broth were much lower than the recommended minimum of 4 wt % that is required to have a lower energy demand in the recovery step [93]. The most used method in the recovery of ethanol, distillation, is energy-intensive, accounting for 60−80% of the total separation cost of bioethanol from water, particularly due to low ethanol concentrations in the fermented broth [94].…”
Section: Future Prospectsmentioning
confidence: 97%
“…Distillation is energy-intensive, accounting for 60−80% of total separation cost of bioethanol from water, particularly due to low ethanol concentration in the broth. In order to be blended with gasoline, anhydrous ethanol (>99.5 wt % ethanol) should be obtained and a dehydration step after distillation is required [93,94]. In the past, dehydration was usually achieved by azeotropic distillation [52].…”
Section: Recovery and Dehydrationmentioning
confidence: 99%
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“…“First generation” bioethanol has been produced from food sources and is not sustainable because it competes with food crops. Instead, “second generation” bioethanol is obtained from nonedible materials, such as cellulose obtained from lignocellulosic biomass (LBM). The economic assessment of lignocellulosic ethanol production has also been extensively studied. , LBM, earth’s most abundant biopolymer-based material, is mainly composed of cellulose (40–50 wt %), hemicellulose (25–35 wt %), and lignin (15–30 wt %) biopolymers and a small percentage of minerals and extractives . Cellulose, the main biopolymer present in lignocellulosic biomass, is a linear, regular, microcrystalline homopolymer H­(C 6 H 10 O 5 ) n OH, where n (degree of polymerization) is some thousands.…”
Section: Introductionmentioning
confidence: 99%
“…Energy-intensive separation is required to produce fuel-grade ethanol (FGE) of high purity, mainly due to low ethanol concentration in the broth and the presence of minimum-boiling azeotrope of ethanol and water (95.6 wt % ethanol at 78.15 °C and 1 atm). The main energy requirement is for ethanol recovery (also known as preconcentration) from 4 to 12 wt % ethanol to about 95 wt % ethanol; this recovery step accounts for 60–80% of total separation cost of bioethanol from water. Ethanol dehydration (also known as purification) from near azeotropic composition to FGE specification (>99.5 wt % ethanol), is complex and has been of significant research interest. Bioethanol separation in the present paper refers to the entire separation process of recovery and dehydration together.…”
Section: Introductionmentioning
confidence: 99%