Table 2 Membrane-assisted technologies employed for the polishing of anaerobic effluents

From: Membrane-based technologies for post-treatment of anaerobic effluents

Ref.

Anaerobic effluent source

Membrane process

Treated species and inlet concentration

Reported efficiency (%)

Operating conditions

Tam et al.59

MBR

RO

COD 17.5 mg L−1

88.6

Pilot-scale study

Total nitrogen 3.7 mg L−1

91

RO flow rate 19

Total dissolved solid 337 mg L−1

87.5

m3 day−1

Apparent color 37 Hazen unit

97

MBR flow rate

Conductivity 0.57 mS cm−1

95.3

40 m3 day−1

E. coli 3.4 CFU per 100 mL

100

Pressure not

Viruses 1.2 PFU per 100 mL

100

reported

Estrogens 38.2 (μg L−1)

88

 

Andrade et al.60

MBR

NF

TOC 24.9 mg L−1

97.4

Feed flow rate

Total solid 1.482 mg L−1

64.8

5.6 L min−1

Color 36.8 Hazen unit

82.7

Pressure not reported

Conductivity 2.28 mS cm−1

89.3

Jacob et al.61

MBR

RO

TOC 7 mg L−1

96

Batch operation, size 500 mL

Conductivity 0.76 mS cm−1

97.5

Inlet pressure 8 bar

NF

TOC 7 mg L−1

93.5

Conductivity 0.7 mS cm−1

93

Grundestam and Hellstrom62

MBR

RO

TOC 17 mg L−1

88

Batch operation, size 1 m3

Kjeldahl-nitrogen 67 mg L−1

90.6

Pressure 40 bar

Total P 10

99.6

Al-Malack and Anderson63

EGSB

MF

COD 120 mg L−1

87.5

Permeate flow rate 0.27 L min−1

SS 35 mg L−1

91.4

PO4 2 mg L−1

86.5

Pressure not reported

E. coli 1.9 × 103 CFU mL−1

99.8

Streptococci 1 × 103 CFU mL−1

99.7

Fernández et al.64

EGSB

UF

COD 1978 mg L−1

70–75

Pressure 1.3 bar

Permeate flow rate 4.9 L min−1

Debik et al.65

SGBR

UF

COD 630 mg L−1

41

Pressure 3 bar

Color 400 Hazen unit

37.5

Conduct 9.87 mS cm−1

16

NF

COD 630 mg L−1

85

Pressure 10 bar

Color 400 Hazen unit

87.3

Conduct 9.87 mS cm−1

45.8

Duan et al.66

ASBR

UF

COD 96.5 ppm

38

Constant flux at

Turbidity 16 NTU

94.4

30 L m−2 h−1

Conductivity 1260 mS cm−1

91.2

Pressure between

VSS 16.2 ppm

99

1.1 to 1.2 bar

TSS 86 ppm

95.3

 

NF

COD 96.5 ppm

97

Constant pressure at 12.4 bar

Turbidity 16 NTU

99

Conductivity 1260 mS cm−1

89.8

VSS 16.2 ppm

99

TSS 86 ppm

99

  1. MBR membrane bioreactor, EGSB expanded granular sludge bed, SGBR static granular bed reactor, ASBR anaerobic sequencing batch reactor, VSS volatile suspended solid, TSS total suspended solid