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Hybrid Membrane Processes for Water Reuse Background Results Objectives Materials and Methods Conclusions References = = −1 L∙m −2 ∙h −1 = = ∙∀ −1 g∙m −2 ∙h −1 50% On 0 4 8 12 0.0 0.5 1.0 1.5 2.0 2.5 3.0 Specific Reverse Salt Flux Temperature (°C) Specific Reverse Salt Flux (g/L) Elapsed Time (hour) 0 10 20 30 40 50 60 70 Draw Solution Temperature FO-DCMD Bench Scale System = 1− ∙ 100 % / - + - - + + - + - - + + Bench-scale FO Rejection Bench-scale DCMD Rejection FO-DCMD System Rejection TOC TN TOC TN TOC TN 97% 68% 68% 97% 98% 98% Acknowledgements

Hybrid Membrane Processes for Water Reuse - core.ac.uk · PDF fileHybrid Membrane Processes for Water Reuse Background Results Objectives Materials and Methods Conclusions References

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Page 1: Hybrid Membrane Processes for Water Reuse - core.ac.uk · PDF fileHybrid Membrane Processes for Water Reuse Background Results Objectives Materials and Methods Conclusions References

Hybrid Membrane Processes for Water Reuse

Background

Results

Objectives

Materials and Methods Conclusions

References

𝑊𝑎𝑡𝑒𝑟 𝐹𝑙𝑢𝑥 = 𝐽𝑤 =𝑑∀

𝑑𝑡∙ 𝐴𝑚

−1 L ∙ m−2 ∙ h−1

𝑅𝑒𝑣𝑒𝑟𝑠𝑒 𝑆𝑎𝑙𝑡 𝐹𝑙𝑢𝑥 = 𝐽𝑠 =𝑑𝑐𝑓

𝑑𝑡∙ ∀𝑓 ∙ 𝐴𝐹𝑂

−1 g ∙ m−2 ∙ h−1

50% On

0 4 8 120.0

0.5

1.0

1.5

2.0

2.5

3.0

Specific Reverse Salt Flux

Tem

pera

ture

(°C

)

Specific

Revers

e S

alt F

lux (

g/L

)

Elapsed Time (hour)

0

10

20

30

40

50

60

70 Draw Solution Temperature

FO-DCMD Bench Scale System

𝑅𝑒𝑗𝑒𝑐𝑡𝑖𝑜𝑛 = 1 −𝐶𝑝

𝐶𝑓∙ 100 %

𝐽𝑠/𝐽𝑤

𝐽𝑤

𝐽𝑐

𝑪𝑭 𝑪𝑫𝑺 𝑪𝑫

𝐽𝑤

𝐽𝑐𝒅𝑽

𝒅𝒕

-

𝑽𝑭 𝑽𝑫𝑺+

- -+ +

- + - -+ +

𝒅𝑽

𝒅𝒕

𝐽𝑆

Bench-scale FO

Rejection

Bench-scale DCMD

Rejection

FO-DCMD System

Rejection

TOC TN TOC TN TOC TN

97% 68% 68% 97% 98% 98%

Acknowledgements