Table 1 Surface modification of polyamide TFC RO membranes

From: Chlorination disadvantages and alternative routes for biofouling control in reverse osmosis desalination

Materials

Treatment

Fabrication method

Salt rejection

Water permeability (L/m2 h), Operating pressure

Tolerance:(Chlorination and biofouling test), clorine testing period

Modification properties improving the tolerance

References

Metaphenylene diamine (MPD) and polyacyl chloride monomer (trimesoyl chloride, TMC)

Post-treatment (hydroxyl and cross-linking agents)

Interfacial polymerization

[NaCl]: 100 ppm, R: 90%

Flux 135, 60 psi, Ph l9.8

[NaClO]: 3450 ppm for 10 h, chlorine tolerance

Thermal cross-linking and cross-linking density of PA, cross-linking contain hydroxyl groups

63

Sulfonated poly(arylene ether) (SPAE) 1.End-group Cross linked 2.C-ESFx-BP Non-cross-linked N-ESFx-BP

Thermal treatment

Polycondensation interfacial polymerization

[NaCl]: 2000 ppm 1. R: 98.4% 2. R: 90.3%

1. 0.6 L μm/m2 h bar pH 4,1000 psi 2. 0.81 L μm/m2 h bar

[NaClO]: 4000 ppm for 30 days, chlorine tolerance

Partial fluorinated polymer membrane, cross-linking and the degree of sulfonation of the membrane

36

N,N’- DMMPD and 1,3,5-benzenetricarbonyl trichloride (TMC)

__

Interfacial polymerization

[NaCl]: 1500 ppm, R: 90.0%

48 L/m2 h, 1.5 MP

[NaClO]: 200 ppm [CaCl2]: 500 ppm 96 h, Chlorine tolerance

Electron-withdrawing properties for aromatic diamines and amide bonds is sterically hindered at ortho position

64

m-phenylene diamine (MPD) and 1,2,4,5-benzene tetracarbonyl chloride (BTC)

Thermal imidization

Interfacial polymerization

[NaCl]: 2000 ppm, R: 98.8%

32 L/m2 h, 1.5 MP

[NaClO]: 6000 ppm, chlorine resistance, 168 h.

Amide linkage replaced by imide linkage

65

Film poly(amide-urethane@imide)

__

Two-step interfacial polymerization

[NaCl]: 2000 ppm, R: 95%

35 L/m2 h 1.55 MPa

[NaOCl]: 8000 ppm, 24 h chlorine-tolerant property, antifouling property.

Formation of the imine-like and quinone-like

66

Hexafluoro alcohol(HFA)-and diamine and trimesoyl chloride (TMC)

Pre-treated PSF membrane with UV-Ozone

Interfacial polymerization

[NaCl]: 2000 ppm, R: 100%

65 L/m2 h 27.6 bar

[HOCl]: 1000 ppm, 24 h, chlorine-tolerant property

Steric hindrance and electron-withdrawing properties of the HFA group.

67

2,6-DAT and MPD

__

Interfacial polymerization

[NaCl]: 1000 ppm, R: 100%

0.23 L/m2 h 1 MPa

[NaClO]: 2000 ppm, 100 h chlorine-tolerant property

Electron donating (CH3 and OCH3) attached to the phenyl ring of MPD group

70

Sorbitol polyglycidyl ether (SPGE)

__

-Interfacial polymerization -In situ polymerization

0.2 wt% NaCl, R: 98%

44 L/m2 h 1.5 MP

[NaClO]: 100 ppm, 1 h chlorine-tolerant property

Glycerol prevented membrane drying out during the ring-opening reaction.

71

PA N,N’-dimethyl-m-phenylene diamine (N,N’-DMMPD)

Heat treatment

Interfacial condensation polymerization

[NaCl]:1500 ppm, R: 92%

22 L/m2 h 1.5 MP

[NaClO]: 200 ppm, [CaCl2]: 500 ppm, 96 h, chlorine-tolerant property

Secondary-to-tertiary amide replacement and a highly crosslinked structure.

73

Layered double hydroxide (LDH) FO

__

Induced immobilization

__

Over 0.015 L/m2 h

[NaClO]: 1000 ppm, 1 h Chlorine-resistant 96 times, resistance to organic fouling and reduce the attachment of bacteria.

The LDH layer served as a barrier

161

Zwitterionic polymers poly(sulfobetaine) and poly(carboxybetaine)

__

 

__

__

Biofouling property and has biomedical and industrial applications

Electrostatic interactions and steric repulsive barrier

79

Glycidoxypropyltrimethoxysilane (GPPTMS)

Heat treatment

Interfacial polymerization

[NaCl]: 2000 ppm R: 99.2%

21.26–4.90 L/m2 h 1.52 MPa

[NaClO]: 1000 ppm, at improve the chlorine tolerance

Hydrophilic epoxy compound

162