2011 salinity summit contributions to permeation resistance in a vsep ro system treating brackish...

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2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of Civil and Environmental Engineering, University of Washington, Seattle, WA 98195

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Page 1: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

2011 Salinity Summit

Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine

Mark Benjamin and Wei Shi

Department of Civil and Environmental Engineering, University of Washington, Seattle, WA 98195

Page 2: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Reverse Osmosis (RO)

Reverse Osmosis (RO): Increasingly used in treatment of brackish water and brine for potable water

Fouling: Production

Time

Pressure

Time

Constant Pressure Constant Production

Page 3: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

VSEP

Vibratory Shear Enhanced Processing

Source: New Logic Research Inc. Emeryville, CA

Shear

Page 4: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

VSEP Applications

Landfill Leachate Manure Management Mining Petroleum Processing Pulp and Paper Desalination

Page 5: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

VSEP Operation

Concentrate

Feed

Pump

Feed tank

Amplitude: 13°

Frequency: 55Hz

TMP: 140 psi

Page 6: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

RO Feed Composition

Brackish water*

Brine: 10 times as concentrated

pH 8.0 Cl 175

Ca 275 as CaCO3 Ba 25

Mg 100 as CaCO3 Si 5

SO4 350 Fe 0.5

Na 175 Alk 150 as CaCO3

TDS 1050

* All units in mg/L, except for pH

Page 7: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Permeate FluxBrackish solution

0

10

20

30

40

50

0.0 0.2 0.4 0.6 0.8 1.0

Recovery

Flu

x (L

/m2-h

)

w/ vibrationw/o vibration

Page 8: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Permeate Flux

Brine

0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0

5

10

15

20

25w/o vibrationw/ vibration

Recovery

Flu

x (

L/m

2-h

)

Page 9: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Resistance Breakdown

Rm

RTOT

RFRF

= RTOT –Rm –RCP–Rπ

RCP

Page 10: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Contributions to Resistance

0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 0

10000000000000

20000000000000

30000000000000

40000000000000

50000000000000Membrane

Osmotic P

Fouling

CP

Total

Recovery

Re

sis

tan

ce

(m

-1)

w/ w/o vibrationBrackish solution

Page 11: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

inlet outlet

S1S2S3S4

w/o Vibration

w/ Vibration

Higher Shear

Page 12: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Painted Membrane Tests

Shaded Area

Ring for permeation

5.0

5.1

2,

22Re

2

F

R

Ar

h

rravg

(Jaffrin et al. 2002)

r

A

Page 13: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

0 100 200 300 400 5000.0

0.2

0.4

0.6

0.8

1.0

5, 0.6410, 0.32 5, 1.2710, 0.6413, 0.9510, 1.2710, 1.5913, 1.27

Specific Volume (L/m2)

Re

lati

ve

Flu

x (

J/J

0)

R, A

Painted Membrane Tests

Page 14: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Painted Membrane Tests

9.0 9.4 9.8 10.2 10.6 11.0-1.0

-0.8

-0.6

-0.4

-0.2

0.0

f(x) = 0.378849919316468 x − 4.28982761861908R² = 0.96729281987083

ln(γ)

ln(J

/J0

)

0.380/ 0.137 WJ J

Page 15: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Mechanisms to Generate Shear

Membrane Rotation

Ultrasound

Longitudinal Vibration

Shear- fouling relationship

Torsional Vibration

Page 16: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Conclusions

Membrane vibration Increases permeate flux Reduces the contribution of fouling

to the total resistance Changes scale morphology into

more porous structures

Shear Rate Governs fouling of RO

membranes Facilitate the design of similar

systems for fouling prevention/reduction

Page 17: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Acknowledgements

This work was supported by the Water Research Foundation (WRF) *.

The authors thank New Logic Research, Inc., for providing the test unit.

Yujung Chang and Pierre Kwan of HDR, Inc., and Sommer Carter of NLR provided valuable technical assistance during the project.

*The views expressed are those of the authors and do not necessarily reflect those of WRF.

Page 18: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

RO Membranes

inlet outlet

0.9 cm

10.0 cm

10.24 cm

Membrane BW-30 FE

MWCO (da) 50 30

MaterialPolyamid

ePolyamid

e

pH 1-12 2-11

Tmax (oC) 70 60

Cl2 Tolerance (mg/L)

<0.1 <0.1

Flux*(L/m2‑h)

71 90

Vendor Filmtec Saehan

*At a TMP of 2068 kPa

Page 19: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Solute Rejections

Brackish solution

Brine

0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1.0 0

200

400

600

800

1000

0

2000

4000

6000

8000

10000Permeate, w/o vibration

Permeate, w/ vibration

Feed, w/o vibration

Feed, w/ vibration

Recovery

Co

nd

uc

tiv

ity

(u

S/c

m)

Co

nd

uc

tiv

ity

(u

S)

Mg Ca Na Si Cl SO450

60

70

80

90

100 w/o vibration

w/ vibration

Re

jec

tio

n (

%)

0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0

600

1200

1800

2400

3000

0

20000

40000

60000

80000Permeate, w/o vibraitonPermeate, w/ vibrationFeed, w/o vibrationFeed, w/ vibration

Recovery

Co

nd

uc

tiv

ity

(u

S/c

m)

Co

nd

uc

tiv

ity

(u

S)

Mg Ca Na Si Cl SO450

60

70

80

90

100 w/o vibration

w/ vibration

Re

jec

tio

n (

%)

Page 20: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Solid Precipitation

EDAX spectrum of scales on the membrane surface

Page 21: 2011 Salinity Summit Contributions to Permeation Resistance in a VSEP RO System Treating Brackish Water or Brine Mark Benjamin and Wei Shi Department of

Gypsum

Aragonite

Solid Precipitation - XRD XRD spectrum of precipitates in the feed solution