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Ultrafiltration fouling control

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Presentation on theme: "Ultrafiltration fouling control"— Presentation transcript:

1 Ultrafiltration fouling control
Demineralized water backwashing Sheng Li Sanitary Engineering, Delft University of Technology The Netherlands 2017年4月12日星期三

2 Content Introduction Hypotheses Results Conclusion 2017年4月12日星期三

3 Demi water is better than UF permeate for backwashing
Why is demineralized water better? No pre-treatment! No in-line coagulation! 2017年4月12日星期三

4 Difference between UF permeate and demineralized water for backwashing
Divalent ions Monovalent ions Organic matter 2017年4月12日星期三

5 Hypotheses of NOM fouling
Ca-bridging effect and/or Ca complexation Charge screening effect (DLVO theory) NOM molecule adsorption 2017年4月12日星期三

6 Ca-bridging effect (filtration)
2017年4月12日星期三

7 Ca-bridging effect (Backwash with permeate)
2017年4月12日星期三

8 Ca-bridging effect (Backwash with demi water)
2017年4月12日星期三

9 Charge screening effect (filtration)
2017年4月12日星期三

10 Charge screening effect (Backwash with permeate)
2017年4月12日星期三

11 Charge screening effect (Backwash with demi water)
2017年4月12日星期三

12 Results (Impact of calcium, flux: 85 lmh)
No pre-treatment! No in-line coagulation! 2017年4月12日星期三

13 Results (Impact of sodium, flux: 85 lmh)
No pre-treatment! No in-line coagulation! 2017年4月12日星期三

14 Experiment set-up and Material
UF set-up: “MFI-UF” (Kiwa Water Research, NL) Membrane: Capillary membrane, 0.8 UFC M5 (X-Flow), with a surface area of 0.07 m2 2017年4月12日星期三

15 Backwash solutions Demineralized water UF permeate
UF permeate after dialysis (organic matter is isolated)

16 Permeate after dialysis
MWCO of Dialysis bags:3.5K Da

17 Feed water: Schie canal water (Delft, NL)
Water quality parameter Feed Ca2+ (mg/l) 101 Na+ (mg/l) 58.57 Conductivity (µs/cm) 836 Turbidity (NTU) 4.5 DOC (mg/l) 20 2017年4月12日星期三

18 Composition of backwash solutions
Ca2+ (mg/l) Na+ DOC UF permeate 100 58.56 18.65 UF permeate after dialysis 20 8.7 17 Demineralized water <1 0.5

19 Impact of organic matter (flux:120 lmh)
No pre-treatment! No in-line coagulation! 2017年4月12日星期三

20 Effect of backwash solution on membrane surface charge
Two types of backwash solution were used in this study Milli Q water UF permeate 2017年4月12日星期三

21 Measurement set-up Wilbert van der Ven et al. 2008 Along fiber
Through pore Wilbert van der Ven et al. 2008 2017年4月12日星期三

22 Measurement method 1 mM KCl solution was used in this study as background electrolyte solution 2017年4月12日星期三

23 Streaming potential of membrane
Backwash with permeate Streaming potential were measured before and after 14 filtration cycles. One cycle consists of 15-minute filtration at a flux of 120 lmh and 1-minute backwash at a flux of 240 lmh 2017年4月12日星期三

24 Streaming potential of membrane
Backwash with Milli Q water 2017年4月12日星期三

25 Conclusions Backwashing with demineralized water is more efficient than UF permeate on fouling control Both Ca and Na in backwash water contribute to the fouling of UF, probably by maintaining the bridge effect or decreasing the zeta potential of the membrane and the foulant Organic matter in backwash water does not influence the fouling control of the UF membranes Backwashing with pure water can maintain the negative charge of membrane 2017年4月12日星期三


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