4.7 Article

Tailoring nanofiltration membrane with three-dimensional turing flower protuberances for water purification

Journal

JOURNAL OF MEMBRANE SCIENCE
Volume 621, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.memsci.2020.118985

Keywords

Three-dimensional; Nanofiltration membrane; Water flux; Turing structure; Water purification

Funding

  1. National Natural Science Foundation of China [21776147, 21606140, 61604086, 21905153, 51472174]
  2. International Science & Technology Cooperation Program of China [2014DFA60150]
  3. Department of Science and Technology of Shandong Province [ZR2018BB066, 2016GGX104010]
  4. Qingdao Municipal Science and Technology bureau [19-6-1-91-nsh]
  5. Postdoc Applied Research Project Funding of Qingdao [04000669]
  6. Department of Education of Shandong Province [J16LA14, J17KA013]
  7. Malmstrom Endowment Fund at Hamline University

Ask authors/readers for more resources

In this study, a three-dimensional flower nanofiltration membrane was prepared by filling a polyamide layer with MIL-101 (Cr) nanoparticles. The presence of flower-like protuberances greatly increased the surface area of the polyamide layer, leading to better water flux compared to pristine membranes. The membrane showed good separation performance for monovalent and divalent salts, indicating its potential for nanofiltration membrane modifications.
Three-dimensional flower nanofiltration membrane is prepared by filling polyamide layer with MIL-101(Cr) nanoparticles, and effects of different MIL-101(Cr) amounts on membrane properties (e.g., water flux and salt rejection) are investigated in different salt solutions under different pressures. Experiments demonstrate MIL-101 (Cr) nanomaterials are wrapped within the polyamide (PA) layer, and solvent remains in their pores. During vacuum upward evaporation process, residual solvent flows unevenly through the pores to result in the formation of flower-like bubbles on the membrane surface. The more MIL-101(Cr) nanomaterials are added, the more protuberances. The presence of flower-like protuberances greatly increases the surface area of polyamide layer. Therefore, the water flux of PA-flower membranes is better than that of PA-pristine membranes at different pressures. For example, under 1000 ppm Na2SO4 solution and 1 MPa pressure, water fluxes of PA-pristine, PAPVA and PA-flower (0.3 wt% MIL-101(Cr)) membranes are 35.40, 43.66 and 63.36 L/m(2).h; and their salt rejection rates are 89.45%, 89.27% and 89.86%, respectively. The separation performance of PA-flower membrane from high to low is R-MgSO4 > R-Na2SO4 > R-MgCl2 > R-NaCl, and the R(MgSO4 )and R-Na2SO4 can reach 97.13% and 88.27.% at 0.75 MPa. It proves that the PA-flower membrane is suitable for the separation of monovalent and divalent salts. The findings above will provide a new strategy for nanofiltration membrane modifications.

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