4.7 Article

Desalination by direct contact membrane distillation using mixed matrix electrospun nanofibrous membranes with carbon-based nanofillers: A strategic improvement

期刊

CHEMICAL ENGINEERING JOURNAL
卷 426, 期 -, 页码 -

出版社

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2021.131316

关键词

Dual-layered membranes; Triple-layered membranes; Electrospun nanofiber; Nanofillers protrusions; Electrospinning

资金

  1. Kempe Foundation
  2. Bio4energy program
  3. Spanish Ministry of Economy and Competitiveness [CTM2015-65348-C2-2-R]
  4. Spanish Ministry of Science, Innovation and Universities [RTI2018-096042-B-C22]

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Robust hydrophobic and superhydrophobic mixed matrix electrospun nanofibrous membranes were prepared and characterized for direct contact membrane distillation applications, showing improved performance through strategic layer design.
Robust hydrophobic and superhydrophobic mixed matrix electrospun nanofibrous membranes (MM-ENMs) have been prepared from low- and high- molecular weight polyvinylidene fluoride with either multi-walled carbon nanotubes or graphene oxide nanofillers (0.05-0.5 wt%). The polymer solutions' properties, including their electrical conductivity, viscosity, and surface tension, were determined and used to guide the design of single-, dual-, and triple-layered MM-ENMs combining layers with different hydrophobic character. All MM-ENMs were subsequently prepared and characterized in terms of their morphology, hydrophobicity, mechanical properties, and direct contact membrane distillation (DCMD) performance. A thinner hydrophobic layer with a thicker hydrophilic support layer in dual-layered MM-ENMs reduced water vapor transport resistance and improved DCMD performance relative to single-layer MM-ENMs. Conversely, placing an intermediate hydrophilic layer between two hydrophobic layers in triple-layered MM-ENMs promoted water condensation (water pocket formation) and thus reduced DCMD performance. Over 10 h DCMD, the best-performing dual-layered MM-ENM allowed ultra-high permeate fluxes of up to 74.7 kg/m2 h while maintaining a stable permeate electrical conductivity of around 7.63 mu S/cm and a salt (NaCl) rejection factor of up to 99.995% when operated with a feed temperature of 80 degrees C, a permeate temperature of 20 degrees C, and a feed solution containing NaCl at a concentration of 30 g/L.

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