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Reverse osmosis and nanofiltration fouling Chuyang Y. Tang ([email protected]) Associate Professor Department of Civil Engineering The University of Hong Kong 1 Forward Osmosis for Desalination and Wastewater Treatment DSD International Conference, Hong Kong, Nov 11-12, 2014

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Page 1: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

Reverse osmosis and nanofiltration

fouling

Chuyang Y. Tang ([email protected])

Associate Professor

Department of Civil Engineering

The University of Hong Kong

1

Forward Osmosis for

Desalination and

Wastewater Treatment

DSD International Conference, Hong Kong, Nov 11-12, 2014

Page 2: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

Outline

• Forward osmosis (FO) background

• Potential FO applications in Hong Kong

• FO membrane performance

• Conclusion

2

Page 3: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

Reverse osmosis

(RO)

Pressure retarded osmosis

(PRO)

Forward osmosis

(FO)

Water flux

Applied pressure Dp, Osmotic

pressure

High concentration solution

Membrane

Low concentration solution

FO, P = 0 (low energy!!!)

High concentration solution

Membrane

Low concentration solution

PRO, P < Dp

High concentration solution

Membrane

Low concentration solution

RO, P > Dp

3

Xu et al, JMS 348, 298-309, (2010)

RO, FO, & PRO

Page 4: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

The National Geography Magazine

http://ngm.nationalgeographic.com/big-idea/09/desalination-pg2

Forward osmosis

• Key features – High rejection (like RO membranes)

– Low pressure (low energy consumption)

– Low fouling

– Potential for resource recovery

• Potential applications – Seawater desalination

– Wastewater treatment

– Brine (and other difficult streams)

treatment

– Food processing

Page 5: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

Forward osmosis

Pressure retarded osmosis

McCutcheon, J. R.; McGinnis, R. L.; Elimelech, M., A novel ammonia-carbon dioxide forward (direct)

osmosis desalination process. Desalination 2005, 174, (1), 1-11.

Aaberg, R.J., Osmotic Power: A new and powerful renewable energy source? Refocus, 2003. 4(6): p. 48-50.

5

FO PRO

Page 7: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

Potential applications in Hong Kong

7

Wastewater reclamation and energy recovery

L. Chen, Y. Gu, C. Cao, J. Zhang, J.-W. Ng and C.Y. Tang, Water Research, 2014, 50, 114-123.

FO-MBR and FO anaerobic MBR

Page 8: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

8

Potential applications in Hong Kong

Wastewater reclamation and energy recovery

L. Chen, Y. Gu, C. Cao, J. Zhang, J.-W. Ng and C.Y. Tang, Water

Research, 2014, 50, 114-123.

Page 9: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

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Potential applications in Hong Kong

Waste volume reduction and resource recovery

Recovering Nutrients (N, K, P) from Urban Source-Separated Urine

J. Zhang, Q. She, V. W. C. Chang, C. Y. Tang and R. D. Webster, Environmental Science & Technology,

2014, 48, 3386-3394.

Page 10: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

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Potential applications in Hong Kong

Household

wastewater

Wastewater

with reduced

volume

Diluted seawater

for toilet flushing

Reclaim wastewater for toilet flushing

Page 11: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

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Potential applications in Hong Kong

Osmotic pump for reducing pumping energy

Osmotic pressure p

of seawater = 2.5 MPa

As long as P < p

Osmotic condition will

be maintained

Osmotic pumping can

provide a hydrostatic

head of up to 250 m!

Enough pressure to

deliver seawater w/o

mechanical pumping

for a 50-storey building

Diluted seawater

Household

wastewater

Wastewater

with reduced

volume

Hydrostatic

Pressure = gH

Page 12: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

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Ideal FO

membranes

Rejection layer

High A value

Low B value

Support layer

Small S value

Thinner

more porous

lower tortuosity

tS

DS DS FW FW

FO performance modeling

feed

wdraww

AB

JAB

S

DJ

p

pln

feedw

draww

AJB

AB

S

DJ

p

pln

Lee et al. JMS 1981, 8, 141-171.

Loeb et al. JMS 1997, 129, 243-249.

C. Y. Tang et al., JMS 2010, 354, 123-133.

Page 13: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

FO performance simulation

13 Other simulation conditions: S = 0.4 mm and D = 1.69 x 10-9 m2/s (NaCl).

Wastewater treatment scenario Osmotic pressure:

Feed: 50 kPa (wastewater)

Draw: 2.5 MPa (seawater)

Desalination scenario Osmotic pressure:

Feed: 2.5 MPa (wastewater)

Draw: 10 MPa (seawater)

Page 14: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

FO performance simulation

14

Desalination scenario Feed: 2.5 MPa (wastewater) Draw: 10 MPa (seawater)

Page 15: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

15 C. Y. Tang*; Q. She; W.C.L. Lay; R. Wang; Fane, A. G. JMS 2010, 354, 123-133.

Model verification

FO water flux

Porous support

Draw solution

Feed solution

Porous support

Feed solution

Draw solution

AL-DS

AL-FS

Page 16: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

FO fabrication – Thin film composite A flat sheet FO A hollow fiber FO

Wang, R.; Shi, L.; Tang, C. Y.; Chou, S.; Qiu, C.; Fane, A. G., Characterization of novel

forward osmosis hollow fiber membranes. Journal of Membrane Science 2010, 355, 158–167.

Chou, S.; Shi, L.; Wang, R.; Tang, C. Y.; Qiu, C.; Fane, A. G., Characteristics and potential

applications of a novel forward osmosis hollow fiber membrane. Desalination 2010, 261,

365-372.

Wei, J.; Qiu, C.; Tang, C. Y.; Wang, R.; Fane, A. G., Synthesis and Characterization of Flat-

sheet Thin Film Composite Forward Osmosis Membranes. Journal of Membrane Science

2011, 372, 292-302.

Wei, J.; Qiu, C.; Tang, C. Y.; Wang, R., Influence of Monomer Concentrations on the

Performance of Polyamide-based Thin Film Composite Forward Osmosis Membrane.

Journal of Membrane Science 2011, in press

Page 17: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

FO membrane prepared on nanocomposite substrate (PSfN0.5-TFC)

TFC PSfN0.5-TFC TFC PSfN0.5-TFC0

10

20

30

40

50

60

70

80

90

100

AL-FSW

ate

r F

lux (

Jv, L/m

2-h

)AL-DS

DS = 0.5 M NaCl

DS = 1.0 M NaCl

DS = 2.0 M NaCl

(a)

Mixed matrix substrate for

controlling ICP

Ma et al., Nanocomposite Substrates for Controlling Internal Concentration

Polarization in Forward Osmosis Membranes, Journal of Membrane Science,

accepted for publication.

Page 18: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

Summary

• FO applications

– Wastewater

– Seawater

• FO membrane performance

– Membrane properties performance

– High performance FO membranes

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Page 19: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

• Collaborators

– Wang Rong, Tony Fane, You Shijie, Victor Chang

• Students/Post-docs

– Qiu Changquan, Ma Ning, Wei Jing, Qi Saren, Wang

Yining, She Qianhong, Gao Yiben, Li Weiyi

• Support from Singapore Membrane Technology

Centre

Acknowledgements

Page 20: Reverse osmosis and nanofiltration Forward Osmosis forB5-2).pdf · Reverse osmosis and nanofiltration fouling Chuyang Y. Tang (TangC@hku.hk) Associate Professor Department of Civil

C.Y. Tang ([email protected])

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