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. 2019 May 1;9(5):58. doi: 10.3390/membranes9050058

Table 4.

Performances of composite/NCP inorganic membranes in pervaporative desalination.

Composite/ NCP Inorganic Membranes Temperature (°C) Conditions in Feed Side Feed Concentration (g L−1) Conditions in Permeate Side Membrane Thickness (μm) Flux (kg m−2 h−1) Rejection (%) Ref.
NaA zeolite membrane 69 1.90 [81]
PVA a/MA b/silica hybrid membrane 22 6.93 [46]
2D MXene c 65 35.00 0.06 4.74 99.50 [133]
GO d/PAN e 90 100.00 0.03–1.40 3.62 99.80 [50]
GO d/PVA a/PVDF f 65 cross-flow velocity = 0.625 ms−1 100.00 vacuum pressure ~24,000 Pa 100.00 1.56 99.99 [134]
LiCl-S-PVA g 70 flow rate = 0.2 ms−1 35.00 pressure = 100 Pa 33.10 60.80 99.80 [135]
pristine PVA a 20/30/40 atmospheric pressure 35.00 3000 Pa 1.49/1.63/1.98 100.00/95.80/95.00 [255]
zeolite 3A-loaded PVA 20/30/40 atmospheric pressure 35.00 3000 Pa 1.82/2.36/2.57 100.00/96.10/96.00 [255]
PVA a/PAN e 20 5.00 vacuum 0.62 9.04 99.50 [80]
NaA zeolite membrane 69 Seawater vacuum 1.90 99.90 [81]
NaA zeolite membrane 77 29.00 vacuum 4.40 99.90 [81]
LTA h and MFI zeolite 25 0.13 vacuum 15.00 0.20 99.40 [111]
NaA zeolite 20 0.10 vacuum 10.00 1.43 99.83 [108]
clinoptilolite-phosphate 95 1.40 vacuum 15.00 95.00 [107]
silica from TEOS i and MTES j 25 700 kPa 3.00 vacuum 4.70 93.00 [256]
silica from TEOS i and MTES j 25 700 kPa 3.00 vacuum 2.20 99.90 [256]
CTS k 20 3.00 vacuum 3.20 97.00 [109]
CTAB l-silica 25 40.00 vacuum 0.21 2.60 99.90 [115]
templated silica 20 35.00 vacuum 0.50 3.70 98.50 [112]
nickel oxide silica 25 3.00 vacuum 7.00 99.90 [257]

a polyvinyl alcohol, b maleic acid, c Ti3C2Tx membranes, d graphene oxide, e polyacrylonitrile, f polyvinylidene difluoride, g 4-sulfonylphthalic acid cross-linked poly(vinyl alcohol), h linde type A, i tetraethyl ortho silicate, j methyl tri-ethoxy silane, k carbon template silica, and l cetyltrimethyl ammonium bromide.