2019
DOI: 10.1016/j.jiec.2018.09.008
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Aqueous acidified ionic liquid pretreatment for bioethanol production and concentration of produced ethanol by pervaporation

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Cited by 41 publications
(5 citation statements)
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“…The results are consistent with the characteristics of the membrane reported by the provider (500–1000 g m h , separation factor of 6; ethanol 5 , 5–10 mbar) and are consistent with the literature [ 57 ]. As observed in Figure 2 a, total permeate flux increased with both ethanol concentration and temperature, while the separation factor showed a slight drop with increasing of ethanol feed concentration and increased with temperature.…”
Section: Resultssupporting
confidence: 92%
“…The results are consistent with the characteristics of the membrane reported by the provider (500–1000 g m h , separation factor of 6; ethanol 5 , 5–10 mbar) and are consistent with the literature [ 57 ]. As observed in Figure 2 a, total permeate flux increased with both ethanol concentration and temperature, while the separation factor showed a slight drop with increasing of ethanol feed concentration and increased with temperature.…”
Section: Resultssupporting
confidence: 92%
“…This process uses the difference in ethanol concentrations on both sides of the asymmetric thick polymer membrane. The separation mechanism is based on the differences in the affinity of ethanol and water to the membrane (dissolving and diffusion capacity) and allows the final ethanol dehydration to be 99.8% [17,[181][182][183][184].…”
Section: Distillation and Dehydrationmentioning
confidence: 99%
“…Furthermore, Karadirek and Okkay have developed a statistical model to produce activated carbon using spent mushroom compost [31]. Kim et al [32] have developed the pyrolysis of Kraft lignin in a rotary kiln reactor, thus suppressing carbon agglomeration, and Trinh et al have published interesting pretreatment strategies to optimize bioethanol production and its concentration via pervaporation [33].…”
Section: Introductionmentioning
confidence: 99%