2023
DOI: 10.1016/j.jclepro.2023.136481
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Recent progress in pervaporation membranes for furfural recovery: A mini review

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Cited by 6 publications
(6 citation statements)
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“…The Hildebrand solubility parameters for methanol, ethanol, isopropanol, and 1-butanol are 29.6, 26.2, 23.6, and 23.3 MPa 0.5 , respectively. ,, 1-Butanol exhibits relatively closer compatibility with PDMS (14.9 MPa 0.5 ), leading to a stronger affinity for PDMS . Second, the molecular dynamics radius of methanol, ethanol, isopropanol, and 1-butanol are 0.195, 0.225, 0.235, and 0.25 nm, respectively. ,, The molecular kinetic radius gradually approaches the r 3 of ME-PDMS. Once bulkier molecules diffuse through the network cavity, the water endures a greater transport resistance coupled with the high hydrophobicity of the ME-PDMS membrane itself, leading to a decrease in water flux and an increase in alcohol flux.…”
Section: Resultsmentioning
confidence: 98%
See 1 more Smart Citation
“…The Hildebrand solubility parameters for methanol, ethanol, isopropanol, and 1-butanol are 29.6, 26.2, 23.6, and 23.3 MPa 0.5 , respectively. ,, 1-Butanol exhibits relatively closer compatibility with PDMS (14.9 MPa 0.5 ), leading to a stronger affinity for PDMS . Second, the molecular dynamics radius of methanol, ethanol, isopropanol, and 1-butanol are 0.195, 0.225, 0.235, and 0.25 nm, respectively. ,, The molecular kinetic radius gradually approaches the r 3 of ME-PDMS. Once bulkier molecules diffuse through the network cavity, the water endures a greater transport resistance coupled with the high hydrophobicity of the ME-PDMS membrane itself, leading to a decrease in water flux and an increase in alcohol flux.…”
Section: Resultsmentioning
confidence: 98%
“…However, the microorganisms in the fermentation broth are often subject to end-product inhibition due to solvent toxicity . The combination of fermentation and separation technologies is proposed, which aims to optimize solvent production while reducing the associated costs. , Compared with conventional separation techniques, e.g., distillation, pervaporation (PV) offers competitive advantages in the separation of azeotropic mixtures, thermosensitive compounds, and organic–organic mixtures, while PV outperforms distillation in selectivity and energy efficiency . This makes PV a very attractive separation technology …”
Section: Introductionmentioning
confidence: 99%
“…1 Non-edible and abundant lignocellulosic biomass materials are considered among the most promising feedstocks for the production of chemicals, fuels, and materials. 2 Biomass mainly consists of 40–60% cellulose, 20–40% hemicellulose, and 10–25% lignin along with minor extractives and minerals. 3 Therefore, the valorization of the three polymers into chemicals is critical for the efficient utilization of biomass and has recently received significant attention.…”
Section: Introductionmentioning
confidence: 99%
“…8 However, the PDMS homogeneous membrane has the problems of low permeation flux and low separation factor. 9 Recently, the mixed matrix membranes (MMMs) prepared by mixed dispersion or in situ synthesis of hydrophobic nanoparticles (such as zeolite, 10,11 silica, 12,13 carbon molecular sieve (CMS), 14 metal organic framework (MOFs), 15 calixarene, 16 etc.) in PDMS matrix have been proven to be an effective method to improve the separation performance of PDMS membrane.…”
Section: Introductionmentioning
confidence: 99%