Title: Ultrafiltration fouling control
1Ultrafiltration fouling control
- Demineralized water backwashing
Sheng Li Sanitary Engineering, Delft University
of Technology The Netherlands
2Content
- Introduction
- Hypotheses
- Results
- Conclusion
3Demi water is better than UF permeate for
backwashing
Why is demineralized water better?
No pre-treatment! No in-line coagulation!
4Difference between UF permeate and demineralized
water for backwashing
- Divalent ions
- Monovalent ions
- Organic matter
5Hypotheses of NOM fouling
- Ca-bridging effect and/or Ca complexation
- Charge screening effect (DLVO theory)
- NOM molecule adsorption
6Ca-bridging effect(filtration)
7Ca-bridging effect(Backwash with permeate)
Ca
Ca
Ca
Ca
Ca
8Ca-bridging effect(Backwash with demi water)
9Charge screening effect(filtration)
10Charge screening effect(Backwash with permeate)
11Charge screening effect(Backwash with demi water)
12Results(Impact of calcium, flux 85 lmh)
No pre-treatment! No in-line coagulation!
13Results(Impact of sodium, flux 85 lmh)
No pre-treatment! No in-line coagulation!
14Experiment 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
15Backwash solutions
- Demineralized water
- UF permeate
- UF permeate after dialysis (organic matter is
isolated)
16Permeate after dialysis
MWCO of Dialysis bags3.5K Da
17Feed 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
18Composition of backwash solutions
Ca2 (mg/l) Na (mg/l) DOC (mg/l)
UF permeate 100 58.56 18.65
UF permeate after dialysis 20 8.7 17
Demineralized water lt1 lt1 0.5
19Impact of organic matter(flux120 lmh)
No pre-treatment! No in-line coagulation!
20Effect of backwash solution on membrane surface
charge
- Two types of backwash solution were used in this
study - Milli Q water
- UF permeate
21Measurement set-up
Along fiber
Through pore
Wilbert van der Ven et al. 2008
22Measurement method
- 1 mM KCl solution was used in this study as
background electrolyte solution
23Streaming potential of membrane
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
24Streaming potential of membrane
- Backwash with Milli Q water
25Conclusions
- 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