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Nano Porous Membranes for
Water Purification
Shrinath Ghadge
27-705 Nanostructured Materials
Contents
2
 Motivation for water purification
 Issues of conventional and existing water purification technologies
 Carbon nanotube (CNT)-based water purification/desalination systems
 Various problems of CNT based desalination
 Promising solutions
 Conclusion
Why Water Purification?
3
1. Energy
2. Water
3. Food
4. Environment
5. Poverty
6. Terrorism
7. Disease
8. Education
9. Democracy
10. Population
Humanity’s Top Ten Problems for next 50 years
U.S. Energy Information Administration - EIA - Independent Statistics and Analysis https://www.eia.gov/
Abramovitz, Janet., Imperiled waters, impoverished future: The decline of freshwater
Ecosystems, Washington, DC: World watch Institute (1996, March)
Water distribution-Worldwide
http://www.acquainnovations.com/water-facts/ 4
Existing water purification methods
Distillation Ion-exchange
http://www.freedrinkingwater.com/water-education2/46-ion-exchange-principle.htmhttp://www.desalinatedwater.info/home.php 5
Energy input : 6.5–11 kWh/m3 Limited capacity
Waste-Water Treatment Plant
Preliminary Treatment
http://commalinn.blogspot.com/2015/04/process-of-wastewater-treatment-plant.html 6
Contd…
Reverse Osmosis
http://www.dynamicscience.com.au/tester/solutions1/chemistry/nanotechnology/nanotubes.html 7
Operated at very high pressure
P ~ 40 to 82 bar for Seawater desalination
Issues/Problems of conventions methods
 Very high energy requirement e.g. RO needs 3 - 5.5 kWh/m3 electricity
for sea water desalination
 Highly expensive processes
 Fouling of RO membranes
 Water quality (turbidity, pH) gets affected
 Can’t operate at high pressure
 Requires a large area of land
Das, R., et al., Desalination, 2014. 336: p. 97-109.
8
CNT membranes for water purification
 Surface area to volume ratio (~109 m-1)
 Excellent antimicrobial activity
 Higher mechanical stability
 No fouling issues ~ longer life
 Operation at atmospheric pressure
 Higher water permeability ~ very high water flux
 Tunable physical, chemical, electrical and structural properties
Das, R., et al., Desalination, 2014. 336: p. 97-109.
9
http://www.dynamicscience.com.au/tester/solutions1/chemistry/nanotechnology/nanotubes.htm
Pure water molecule
Impurities
Classification of CNT membranes
Single wall CNT
http://jnm.snmjournals.org/content/48/7/1039/F1.expansion
Multi wall CNT
10
Key issues for CNT based desalination
 Structural issues
 Irregularities /improper alignment in CNT’s structure
 Non-uniform pore diameter of CNT
 Properties based issues
 Moderate adsorption capacity of CNT membranes
 Difficulty in functionalization of CNT’s with desired functional
groups
 Induced toxicity in permeate water streams
 Other issues/challenges
 Very high cost of SWCNT’s
 Enhancing anti-microbial activity 11
Solutions for the structural issues
 Growth from template approach : Omachi et al.
 Structure of template organic molecules is reproduced in the
final structures of the CNT’s
 n-Cycloparaphenylenes (CPP): Template and Et-OH: C source
n  no. of benzene rings (12)
Omachi, H., et al., Nat. Chem., 2013. 5(7): p. 572-6.
12
Experimental details
 C-plane sapphire substrate plate (5 mm× 5 mm)
 Reaction temperature = 500oC
 Reaction time = 15 min
 Pressure ~ 1 torr (i.e. under vacuum)
Contd…
13
Omachi, H., et al., Nat. Chem., 2013. 5(7): p. 572-6.
Results and Conclusion
TEM of synthesized CNT’s
Conclusion:
 Crucial factors for efficient CNT’S
growth
• Reaction temperature
• Nature of reaction plate
• Carbon source
CNT’s diameter
D = 248cm-1/WRBM
~ 1. 3 to 1.7 nm
Contd…
14
Omachi, H., et al., Nat. Chem., 2013. 5(7): p. 572-6.
Solutions for the properties based issues
 Enhancing adsorption capacity of CNT membranes
 Synthesis of acid and plasma treated CNT membranes
CVD Fabrication and modification
Yang, H.Y., et al., Nat .Commun., 2013. 4: p. 2220.
15
 Modification of UCNT-based membranes
(A) Acid treatment
• Membranes were immersed into 5N HNO3, refluxed for 2 h and
then washed with DI water
(B) Plasma treatment
• Remote inductively coupled
plasma configuration
16
Yang, H.Y., et al., Nat .Commun., 2013. 4: p. 2220.
Assembly and ObservationsContd…
Micro-channel device Cross-sectional SEM image of the pristine
UCNT–MCE membrane
SEM image of membrane after salt adsorption
Crystal lattice of NaCl NP’s embedded in the
CNT pores 17
Yang, H.Y., et al., Nat .Commun., 2013. 4: p. 2220.
Results and Conclusion
 Adsorption capacity of the plasma-modified CNT’s is ~ 400% w/w (i.e. 4
gg-1 or 4,000 mg g-1)
 Activated carbons ~ 2–20 mg g-1
 Driving force for desalination of CNT-based membranes is the free
energy of adsorption
 plasma treatment : Numerous defective sites
 Partially damage of graphitic structure of CNT’s  dangling bonds
 React with the ambient gases to form various functional/charged groups,
such as –COOH and –OH
18
Solutions for the properties based issues
 Removal of selective pollutants
Chromium (Cr)
 Application of magnetic NP’s to solve environmental problems
Synthesis of CNT/nano-iron oxide composites
 MWCNT + FeCl3.6H2O
 5 M NH4OH added drop wise to precipitate iron oxide
 Product separation by magnet
 Washing with DI
Gupta, V.K., S. Agarwal, and T.A. Saleh, Water research, 2011. 45(6): p. 2207-2212.
19
ResultsContd…
XRD of MWCNTs/nano-iron oxide
Mn: Magnetite (Fe3O4)
Mh: Maghemite (Fe2O3)
• ~ 90% adsorption after 60 min
• Additional adsorbing sites
provided by oxygen atoms of iron
oxide NP’s
20
Gupta, V.K., S. Agarwal, and T.A. Saleh, Water research, 2011. 45(6): p. 2207-2212.
Solutions for the properties based issues
(2) Removal of selective pollutants
Zinc (Zn+2)
 Application of NaClO treated CNT’s for Zn removal
The properties of CNTs such as purity, structure and nature of the surface were greatly
improved after purification
Lu, C. and H. Chiu, Chemical Engineering Science, 2006. 61(4): p. 1138-1145. 21
Adsorbent Avg. Pore diameter (nm)
SWCNT 7.6
Purified SWCNT 4.12 
MWCNT 8.35
Purified MWCNT 5.17 
SWCNT MWCNT
Contd…
22
Lu, C. and H. Chiu, Chemical Engineering Science, 2006. 61(4): p. 1138-1145.
Langmuir adsorption model
CNT
Langmuir Freundlich
a b R2 Kf n R2
SWCNT 43.66 0.19 0.999 13.24 0.292 0.945
MWCNT 32.68 0.22 0.999 11.84 0.244 0.945
Freundlich isotherm
Adsorption isotherms for Zn2+ with purified CNT’s
Contd…
23
Lu, C. and H. Chiu, Chemical Engineering Science, 2006. 61(4): p. 1138-1145.
Solutions for the properties based issues
 Lowering the toxicity
 Functionalization of CNT’s
Sayes, C.M., et al., Toxicol Lett, 2006. 161(2): p. 135-42.

Cytotoxicity study on human dermal fibroblast cell cultures
24
25
• As the degree of functionalization
on the surface of the CNT increases,
the cytotoxicity decreases
significantly.
Sayes, C.M., et al., Toxicol Lett, 2006. 161(2): p. 135-42.
• COO-, SO3
- groups attracts positive ions
• +ve ions attracts –ve ions
• Formation of Donnan Potential
Approaches for enhancing CNT’s performance
 Improvement in anti-microbial activity
Silver (Ag) NP’s-doped CNT membrane
Ihsanullah, et al., Desalination, 2015. 376: p. 82-93. 26
Porosity increases up-to 10% of Ag content
Results and Conclusion
• At high Ag content, the membrane
surface becomes more hydrophilic
• Flux increases
• Complete removal of all E. coli
bacteria at 60 min
• The combined antitoxic properties of
Ag and CNT’s led to enhanced
antibacterial properties
27
Ihsanullah, et al., Desalination, 2015. 376: p. 82-93.
Solutions to lower the CNT’s cost
 CNT doping to other polymers or matrices for cost reduction
Das, R., et al., Desalination, 2014. 336: p. 97-109.
Filler Advantages
Polysulfonate • Increased water flux (160%)
Poly (vinylidene
fluoride)
• Eliminated E. coli cells (~2 μm) through size exclusion.
• Inactivated 80% of the bacteria within 20 min contact time.
Polyamide–
polysulfone
• Increased water permeability.
• Enhanced bacterial cytotoxicity (60%/h).
Polyether sulfone
• Increased water refluxing capacity.
• Greater antifouling activity against whey proteins
Poly (methyl
methacrylate)
• Increased water flux (62%) with improved selectivity and
sensitivity and Retained Na2SO4 (99%).
28
Conclusion
 CNT based membranes could potentially lead to more effective
means of filtration:
 Remove more impurities/ pollutants
 Faster
 Extended service life
 More economical
 Most promising method for future seawater desalination
 Exhaustive research still needed to assess any harmful effects of
CNT’s on environment and living beings.
29
References
• R. Das, M. E. Ali, S. B. A. Hamid, S. Ramakrishna, and Z. Z. Chowdhury, "Carbon nanotube
membranes for water purification: A bright future in water desalination," Desalination, vol. 336, pp.
97-109, 2014.
• H. Omachi, T. Nakayama, E. Takahashi, Y. Segawa, and K. Itami, "Initiation of carbon nanotube
growth by well-defined carbon nanorings," Nat Chem, vol. 5, pp. 572-6, 2013.
• C. Bower, W. Zhu, S. Jin, and O. Zhou, "Plasma-induced alignment of carbon nanotubes," Applied
Physics Letters, vol. 77, p. 830, 2000.
• L. Ding, A. Tselev, J. Wang, D. Yuan, H. Chu, T. P. McNicholas, et al., "Selective Growth of Well-
Aligned Semiconducting Single-Walled Carbon Nanotubes," Nano Letters, vol. 9, pp. 800-805, 200
• H. Y. Yang, Z. J. Han, S. F. Yu, K. L. Pey, K. Ostrikov, and R. Karnik, "Carbon nanotube membranes
with ultrahigh specific adsorption capacity for water desalination and purification," Nat Commun, vol.
4, p. 2220, 2013.
30
• Ihsanullah, T. Laoui, A. M. Al-Amer, A. B. Khalil, A. Abbas, M. Khraisheh, et al., "Novel anti-
microbial membrane for desalination pretreatment: A silver nanoparticle-doped carbon nanotube
membrane," Desalination, vol. 376, pp. 82-93, 2015.
• Ihsanullah, A. M. Al Amer, T. Laoui, A. Abbas, N. Al-Aqeeli, F. Patel, et al., "Fabrication and
antifouling behaviour of a carbon nanotube membrane," Materials & Design, vol. 89, pp. 549-558,
2016
• C. M. Sayes, F. Liang, J. L. Hudson, J. Mendez, W. Guo, J. M. Beach, et al., "Functionalization density
dependence of single-walled carbon nanotubes cytotoxicity in vitro," Toxicol Lett, vol. 161, pp. 135-
42, 2006
• V. K. Gupta, S. Agarwal, and T. A. Saleh, "Chromium removal by combining the magnetic properties
of iron oxide with adsorption properties of carbon nanotubes," Water research, vol. 45, pp. 2207-
2212, 2011.
• P. Yenphan, A. Chanachai, and R. Jiraratananon, "Experimental study on micellar-enhanced
ultrafiltration (MEUF) of aqueous solution and wastewater containing lead ion with mixed
surfactants," Desalination, vol. 253, pp. 30-37, 2010.
31
Thankyou!
http://www.newwatersupply.org/news/quotes.htm 32
*Supplementary slides*
33
MEUF for water purification
 Removal of heavy metal ions based on their charge
Yenphan, P., A. Chanachai, and R. Jiraratananon, Desalination, 2010. 253(1–3): p. 30-37.
• Removal of positive metal ions (Ni+2, Cu+2, Cd+2, Zn+2 etc.) using anionic surfactant
(e.g. SDS)
• Cationic surfactant : Trimethylhexadecyl ammonium chloride, to remove negative
metal ions (e.g. Br-)
34
Microwave plasma-enhanced chemical vapor
deposition (MPECVD) : Brower et al.
 The CNT’s have been grown perpendicular to the local substrate surface
regardless of the substrate tilt or shape
Bower, C., et al., Applied Physics Letters, 2000. 77(6): p. 830.
35
Chemical vapor deposition : Ding et al.
 Substrates : single-crystal ST-cut quartz
 Carbon source : ethanol/methanol mixture
 Catalyst : Cu nanoparticles
SEM image • Diameter ~ 1.55-1.78 nm
• 95% of nanotubes being semiconducting due to
strong interaction between SWNT’s and the quartz latticeDing, L., et al., Nano Letters, 2009. 9(2): p. 800-805
36
Approaches for enhancing CNT’s performance
Improvement in anti-microbial activity
Silver (Ag) NP’s-doped CNT membrane
AgNO3 dissolved in Et-OH + CNT dissolved in Et-OH

Sonicating (homogeneity )

Evaporation of Et-OH in oven

Calcination for 4 h at 350 oC
Ihsanullah, et al., Desalination, 2015. 376: p. 82-93. 37
Approaches for enhancing CNT’s performance
(1) Improvement in membrane performance
Fe2O3 NP’s-doped CNT membrane
Ihsanullah, et al., Materials & Design, 2016. 89: p. 549-558.
Diametral compression test curves
Mechanical strength of 11.2 MPa at 20 % Fe2O3
A maximum removal of 90 and 88% of SA was
achieved for membranes with a 10 and 1%
Fe2O3 content, respectively, after 3 h
38
Dissolved air floatation (DAF)
http://commalinn.blogspot.com/2015/04/process-of-wastewater-treatment-plant.html 39
Anaerobic Sludge Digester
http://commalinn.blogspot.com/2015/04/process-of-wastewater-treatment-plant.html 40
Secondary sedimentation tank
http://commalinn.blogspot.com/2015/04/process-of-wastewater-treatment-plant.html 41
Operation of CNT membranes for water purification
http://mw.concord.org/modeler/showcase/nano/waterrace.html
 Water molecules with different initial velocities move through a cluster of CNTs
42

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Nano porous membranes for water purification by shrinath ghadge

  • 1. Nano Porous Membranes for Water Purification Shrinath Ghadge 27-705 Nanostructured Materials
  • 2. Contents 2  Motivation for water purification  Issues of conventional and existing water purification technologies  Carbon nanotube (CNT)-based water purification/desalination systems  Various problems of CNT based desalination  Promising solutions  Conclusion
  • 3. Why Water Purification? 3 1. Energy 2. Water 3. Food 4. Environment 5. Poverty 6. Terrorism 7. Disease 8. Education 9. Democracy 10. Population Humanity’s Top Ten Problems for next 50 years U.S. Energy Information Administration - EIA - Independent Statistics and Analysis https://www.eia.gov/ Abramovitz, Janet., Imperiled waters, impoverished future: The decline of freshwater Ecosystems, Washington, DC: World watch Institute (1996, March)
  • 5. Existing water purification methods Distillation Ion-exchange http://www.freedrinkingwater.com/water-education2/46-ion-exchange-principle.htmhttp://www.desalinatedwater.info/home.php 5 Energy input : 6.5–11 kWh/m3 Limited capacity
  • 6. Waste-Water Treatment Plant Preliminary Treatment http://commalinn.blogspot.com/2015/04/process-of-wastewater-treatment-plant.html 6
  • 8. Issues/Problems of conventions methods  Very high energy requirement e.g. RO needs 3 - 5.5 kWh/m3 electricity for sea water desalination  Highly expensive processes  Fouling of RO membranes  Water quality (turbidity, pH) gets affected  Can’t operate at high pressure  Requires a large area of land Das, R., et al., Desalination, 2014. 336: p. 97-109. 8
  • 9. CNT membranes for water purification  Surface area to volume ratio (~109 m-1)  Excellent antimicrobial activity  Higher mechanical stability  No fouling issues ~ longer life  Operation at atmospheric pressure  Higher water permeability ~ very high water flux  Tunable physical, chemical, electrical and structural properties Das, R., et al., Desalination, 2014. 336: p. 97-109. 9 http://www.dynamicscience.com.au/tester/solutions1/chemistry/nanotechnology/nanotubes.htm Pure water molecule Impurities
  • 10. Classification of CNT membranes Single wall CNT http://jnm.snmjournals.org/content/48/7/1039/F1.expansion Multi wall CNT 10
  • 11. Key issues for CNT based desalination  Structural issues  Irregularities /improper alignment in CNT’s structure  Non-uniform pore diameter of CNT  Properties based issues  Moderate adsorption capacity of CNT membranes  Difficulty in functionalization of CNT’s with desired functional groups  Induced toxicity in permeate water streams  Other issues/challenges  Very high cost of SWCNT’s  Enhancing anti-microbial activity 11
  • 12. Solutions for the structural issues  Growth from template approach : Omachi et al.  Structure of template organic molecules is reproduced in the final structures of the CNT’s  n-Cycloparaphenylenes (CPP): Template and Et-OH: C source n  no. of benzene rings (12) Omachi, H., et al., Nat. Chem., 2013. 5(7): p. 572-6. 12
  • 13. Experimental details  C-plane sapphire substrate plate (5 mm× 5 mm)  Reaction temperature = 500oC  Reaction time = 15 min  Pressure ~ 1 torr (i.e. under vacuum) Contd… 13 Omachi, H., et al., Nat. Chem., 2013. 5(7): p. 572-6.
  • 14. Results and Conclusion TEM of synthesized CNT’s Conclusion:  Crucial factors for efficient CNT’S growth • Reaction temperature • Nature of reaction plate • Carbon source CNT’s diameter D = 248cm-1/WRBM ~ 1. 3 to 1.7 nm Contd… 14 Omachi, H., et al., Nat. Chem., 2013. 5(7): p. 572-6.
  • 15. Solutions for the properties based issues  Enhancing adsorption capacity of CNT membranes  Synthesis of acid and plasma treated CNT membranes CVD Fabrication and modification Yang, H.Y., et al., Nat .Commun., 2013. 4: p. 2220. 15
  • 16.  Modification of UCNT-based membranes (A) Acid treatment • Membranes were immersed into 5N HNO3, refluxed for 2 h and then washed with DI water (B) Plasma treatment • Remote inductively coupled plasma configuration 16 Yang, H.Y., et al., Nat .Commun., 2013. 4: p. 2220.
  • 17. Assembly and ObservationsContd… Micro-channel device Cross-sectional SEM image of the pristine UCNT–MCE membrane SEM image of membrane after salt adsorption Crystal lattice of NaCl NP’s embedded in the CNT pores 17 Yang, H.Y., et al., Nat .Commun., 2013. 4: p. 2220.
  • 18. Results and Conclusion  Adsorption capacity of the plasma-modified CNT’s is ~ 400% w/w (i.e. 4 gg-1 or 4,000 mg g-1)  Activated carbons ~ 2–20 mg g-1  Driving force for desalination of CNT-based membranes is the free energy of adsorption  plasma treatment : Numerous defective sites  Partially damage of graphitic structure of CNT’s  dangling bonds  React with the ambient gases to form various functional/charged groups, such as –COOH and –OH 18
  • 19. Solutions for the properties based issues  Removal of selective pollutants Chromium (Cr)  Application of magnetic NP’s to solve environmental problems Synthesis of CNT/nano-iron oxide composites  MWCNT + FeCl3.6H2O  5 M NH4OH added drop wise to precipitate iron oxide  Product separation by magnet  Washing with DI Gupta, V.K., S. Agarwal, and T.A. Saleh, Water research, 2011. 45(6): p. 2207-2212. 19
  • 20. ResultsContd… XRD of MWCNTs/nano-iron oxide Mn: Magnetite (Fe3O4) Mh: Maghemite (Fe2O3) • ~ 90% adsorption after 60 min • Additional adsorbing sites provided by oxygen atoms of iron oxide NP’s 20 Gupta, V.K., S. Agarwal, and T.A. Saleh, Water research, 2011. 45(6): p. 2207-2212.
  • 21. Solutions for the properties based issues (2) Removal of selective pollutants Zinc (Zn+2)  Application of NaClO treated CNT’s for Zn removal The properties of CNTs such as purity, structure and nature of the surface were greatly improved after purification Lu, C. and H. Chiu, Chemical Engineering Science, 2006. 61(4): p. 1138-1145. 21
  • 22. Adsorbent Avg. Pore diameter (nm) SWCNT 7.6 Purified SWCNT 4.12  MWCNT 8.35 Purified MWCNT 5.17  SWCNT MWCNT Contd… 22 Lu, C. and H. Chiu, Chemical Engineering Science, 2006. 61(4): p. 1138-1145.
  • 23. Langmuir adsorption model CNT Langmuir Freundlich a b R2 Kf n R2 SWCNT 43.66 0.19 0.999 13.24 0.292 0.945 MWCNT 32.68 0.22 0.999 11.84 0.244 0.945 Freundlich isotherm Adsorption isotherms for Zn2+ with purified CNT’s Contd… 23 Lu, C. and H. Chiu, Chemical Engineering Science, 2006. 61(4): p. 1138-1145.
  • 24. Solutions for the properties based issues  Lowering the toxicity  Functionalization of CNT’s Sayes, C.M., et al., Toxicol Lett, 2006. 161(2): p. 135-42.  Cytotoxicity study on human dermal fibroblast cell cultures 24
  • 25. 25 • As the degree of functionalization on the surface of the CNT increases, the cytotoxicity decreases significantly. Sayes, C.M., et al., Toxicol Lett, 2006. 161(2): p. 135-42. • COO-, SO3 - groups attracts positive ions • +ve ions attracts –ve ions • Formation of Donnan Potential
  • 26. Approaches for enhancing CNT’s performance  Improvement in anti-microbial activity Silver (Ag) NP’s-doped CNT membrane Ihsanullah, et al., Desalination, 2015. 376: p. 82-93. 26 Porosity increases up-to 10% of Ag content
  • 27. Results and Conclusion • At high Ag content, the membrane surface becomes more hydrophilic • Flux increases • Complete removal of all E. coli bacteria at 60 min • The combined antitoxic properties of Ag and CNT’s led to enhanced antibacterial properties 27 Ihsanullah, et al., Desalination, 2015. 376: p. 82-93.
  • 28. Solutions to lower the CNT’s cost  CNT doping to other polymers or matrices for cost reduction Das, R., et al., Desalination, 2014. 336: p. 97-109. Filler Advantages Polysulfonate • Increased water flux (160%) Poly (vinylidene fluoride) • Eliminated E. coli cells (~2 μm) through size exclusion. • Inactivated 80% of the bacteria within 20 min contact time. Polyamide– polysulfone • Increased water permeability. • Enhanced bacterial cytotoxicity (60%/h). Polyether sulfone • Increased water refluxing capacity. • Greater antifouling activity against whey proteins Poly (methyl methacrylate) • Increased water flux (62%) with improved selectivity and sensitivity and Retained Na2SO4 (99%). 28
  • 29. Conclusion  CNT based membranes could potentially lead to more effective means of filtration:  Remove more impurities/ pollutants  Faster  Extended service life  More economical  Most promising method for future seawater desalination  Exhaustive research still needed to assess any harmful effects of CNT’s on environment and living beings. 29
  • 30. References • R. Das, M. E. Ali, S. B. A. Hamid, S. Ramakrishna, and Z. Z. Chowdhury, "Carbon nanotube membranes for water purification: A bright future in water desalination," Desalination, vol. 336, pp. 97-109, 2014. • H. Omachi, T. Nakayama, E. Takahashi, Y. Segawa, and K. Itami, "Initiation of carbon nanotube growth by well-defined carbon nanorings," Nat Chem, vol. 5, pp. 572-6, 2013. • C. Bower, W. Zhu, S. Jin, and O. Zhou, "Plasma-induced alignment of carbon nanotubes," Applied Physics Letters, vol. 77, p. 830, 2000. • L. Ding, A. Tselev, J. Wang, D. Yuan, H. Chu, T. P. McNicholas, et al., "Selective Growth of Well- Aligned Semiconducting Single-Walled Carbon Nanotubes," Nano Letters, vol. 9, pp. 800-805, 200 • H. Y. Yang, Z. J. Han, S. F. Yu, K. L. Pey, K. Ostrikov, and R. Karnik, "Carbon nanotube membranes with ultrahigh specific adsorption capacity for water desalination and purification," Nat Commun, vol. 4, p. 2220, 2013. 30
  • 31. • Ihsanullah, T. Laoui, A. M. Al-Amer, A. B. Khalil, A. Abbas, M. Khraisheh, et al., "Novel anti- microbial membrane for desalination pretreatment: A silver nanoparticle-doped carbon nanotube membrane," Desalination, vol. 376, pp. 82-93, 2015. • Ihsanullah, A. M. Al Amer, T. Laoui, A. Abbas, N. Al-Aqeeli, F. Patel, et al., "Fabrication and antifouling behaviour of a carbon nanotube membrane," Materials & Design, vol. 89, pp. 549-558, 2016 • C. M. Sayes, F. Liang, J. L. Hudson, J. Mendez, W. Guo, J. M. Beach, et al., "Functionalization density dependence of single-walled carbon nanotubes cytotoxicity in vitro," Toxicol Lett, vol. 161, pp. 135- 42, 2006 • V. K. Gupta, S. Agarwal, and T. A. Saleh, "Chromium removal by combining the magnetic properties of iron oxide with adsorption properties of carbon nanotubes," Water research, vol. 45, pp. 2207- 2212, 2011. • P. Yenphan, A. Chanachai, and R. Jiraratananon, "Experimental study on micellar-enhanced ultrafiltration (MEUF) of aqueous solution and wastewater containing lead ion with mixed surfactants," Desalination, vol. 253, pp. 30-37, 2010. 31
  • 34. MEUF for water purification  Removal of heavy metal ions based on their charge Yenphan, P., A. Chanachai, and R. Jiraratananon, Desalination, 2010. 253(1–3): p. 30-37. • Removal of positive metal ions (Ni+2, Cu+2, Cd+2, Zn+2 etc.) using anionic surfactant (e.g. SDS) • Cationic surfactant : Trimethylhexadecyl ammonium chloride, to remove negative metal ions (e.g. Br-) 34
  • 35. Microwave plasma-enhanced chemical vapor deposition (MPECVD) : Brower et al.  The CNT’s have been grown perpendicular to the local substrate surface regardless of the substrate tilt or shape Bower, C., et al., Applied Physics Letters, 2000. 77(6): p. 830. 35
  • 36. Chemical vapor deposition : Ding et al.  Substrates : single-crystal ST-cut quartz  Carbon source : ethanol/methanol mixture  Catalyst : Cu nanoparticles SEM image • Diameter ~ 1.55-1.78 nm • 95% of nanotubes being semiconducting due to strong interaction between SWNT’s and the quartz latticeDing, L., et al., Nano Letters, 2009. 9(2): p. 800-805 36
  • 37. Approaches for enhancing CNT’s performance Improvement in anti-microbial activity Silver (Ag) NP’s-doped CNT membrane AgNO3 dissolved in Et-OH + CNT dissolved in Et-OH  Sonicating (homogeneity )  Evaporation of Et-OH in oven  Calcination for 4 h at 350 oC Ihsanullah, et al., Desalination, 2015. 376: p. 82-93. 37
  • 38. Approaches for enhancing CNT’s performance (1) Improvement in membrane performance Fe2O3 NP’s-doped CNT membrane Ihsanullah, et al., Materials & Design, 2016. 89: p. 549-558. Diametral compression test curves Mechanical strength of 11.2 MPa at 20 % Fe2O3 A maximum removal of 90 and 88% of SA was achieved for membranes with a 10 and 1% Fe2O3 content, respectively, after 3 h 38
  • 39. Dissolved air floatation (DAF) http://commalinn.blogspot.com/2015/04/process-of-wastewater-treatment-plant.html 39
  • 42. Operation of CNT membranes for water purification http://mw.concord.org/modeler/showcase/nano/waterrace.html  Water molecules with different initial velocities move through a cluster of CNTs 42

Editor's Notes

  1. In the grit chamber, heavy particles, such as a small stones, eggs shells, and coffee grounds settle to the bottom and are removed. These abrasive materials can damage pumps and cause equipment to fail prematurely the grit is removed and washed in the grit classifier before it is properly disposed. Bar screens catch rags, sticks, plastic containers, and other objects floating in these large items are removed so that they do not clog pumps or interfere with other equipment process. Grit chambers are nothing but like sedimentation tanks, designed to separate the intended heavier inorganic materials 
  2. increase the pressure on the salt side of the RO and force the water across the semi-permeable RO membrane, leaving almost all (around 95% to 99%) of dissolved salts behind in the reject stream. The amount of pressure required depends on the salt concentration of the feed water. The more concentrated the feed water, the more pressure is required to overcome the osmotic pressure. s the feed water enters the RO membrane under pressure (enough pressure to overcome osmotic pressure) the water molecules pass through the semi-permeable membrane and the salts and other contaminants are not allowed to pass and are discharged through the reject stream (also known as the concentrate or brine stream) Osmosis is a naturally occurring phenomenon and one of the most important processes in nature. It is a process where a weaker saline solution will tend to migrate to a strong saline solution. 
  3. Due to its fine membrane construction, reverse osmosis not only removes harmful contaminants present in the water, but it also may remove many of the desirable minerals from the water
  4. In such circumstances…CNT based …gathered immmse atten for desal.. due to unique …proper…such as…
  5. Althought cnt desd has shown promisinn reulsu , thre rvarious problkems duw ro which commersoal is not achieved ..i claaisdirf in 3 grps frictionless transport of water molecules through hollow CNT, which ultimately enhances the water flux has been the special research for
  6. To resolve an issue of irregular alignment in CNT’s structure and non-uniform pore diameter of CNT’s, Omachi et al. employed the growth from template) approach in which the structure of template organic molecules is reproduced in the final structures of the CNT’s.18
  7. Vaccum to avoid any oxidation Under these conditions, CPP was successfully converted into CNT’s
  8. ..reactions at higher temperatures (550–650 8C) did not produce CNTs at all, presumably because of the competing decomposition of
  9. ultra long CNT’s (UCNT’s) was deposited onto a mixed cellulose ester (MCE) porous support.
  10. For plasma modification, the membranes were placed in a plasma chamber with a ‘remote’ inductively coupled plasma configuration (Supplementary Fig. S3). The plasma was generated by a radio frequency power operated at frequency of 13.56 MHz and power of 600 W, with 40 sccm Ar gas at a pressure of 2 Pa.
  11. Cooh, oh grp functionalise with water , hydrphilicity increses, fluz increses, foulding decrsess
  12. chromium nitrateThe purification process usingHNO3 was performed to remove impurities if any and to modify the surface of the tube with carbonyl and hydroxyl groups. The purification process was accomplished by stirringMWCNTs in concentrated nitric acid at 70 Cfor 12 h, followed by filteringandwashing with distilled water,and thendrying at 110 C for 6 h A mixed solution of 0.1 M ferric chloride hexahydrate and 0.05 M ferrous chloride tetrahydrate with a molar ratio of one to two was prepared. Subsequently, a specific amount of oxidized MWCNTs was suspended in the mixed solution for 2 h. Then, at constant temperature of 70 C, 5 M- NH4OH solution was added drop wise to precipitate iron oxides
  13. To confirm the presence of iron---XRD
  14. The author states that the large amount of metal catalysts and amorphous carbon appearing within raw (unpurified) CNT’s was removed after NaClO treatment which was further confirmed by TEM analysis, is the major attribution for decrease in pore diameter and improved Zn+2 rejection from water.
  15. Cooh, oh grp functionalize with water , hydrophilicity increases, flux increases, fouling decreases
  16. slight decrease in porositywas observedwhen increasing silver amount from10 to 20%. This might be because,with the increase in silver content, the spaces between CNTs network were most likely covered by larger silver particles and hence the porosity was slightly reduced
  17. The presence of silver transformed the CNT-basedmembrane fromhydrophobic to philic, hence flux increses as Ag increses the permeate flux increased as the silver content increased. The high permeate flux obtained for membranes with high silver loading can be explained as follows. At high silver content, the membrane surface becomes more hydrophilic, as confirmed by the contact angle. The hydrophilic nature of the membrane facilitates the rapid transport of water molecules through it leading to an enhanced permeate flux. It is worth mentioning
  18. Anionoic = -ve head Cat = + head
  19. 1.0 mM CuCl2/poly(vinylpyrrolidone) alcohol solution was used to deposit catalyst on to the substrate.
  20. Waste activated sludge is thickened in dissolved air floatation (DAF) tank to reduce the volume of sludge. Under the effect of air bubbles flowing upwards, the sludge solids are carried to surface and skimmed out.
  21. The goal is to reduce the amount of sludge that needs to be disposed. The most widely employed method for sludge treatment is anaerobic digestion. In this process, a large fraction of the organic matter (cells) is broken down into carbon dioxide (CO2) and methane (CH4), and this is accomplished in the absence of oxygen. About half of the amount is then converted into gases, while the remainder is dried and becomes a residual soil-like material.
  22. Biological nutrient removal (BNR Biological Nutrient Removal (BNR) is a process used for nitrogen and phosphorus removal from wastewater before it is discharged into surface or ground water.