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Gated Transport through Carbon Nanotube Membranes NIRT CBET-0709090

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Sangil Kim1,2, Francesco Fornasiero1, Michael Stadermann1, Alexander Chernov1, ... Colvin4, Aleksandr Noy1,4, Olgica Bakajin,1,2 and Costas P. Grigoropoulos3 ... – PowerPoint PPT presentation

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Title: Gated Transport through Carbon Nanotube Membranes NIRT CBET-0709090


1
Gated Transport through Carbon Nanotube
MembranesNIRT CBET-0709090
Sangil Kim1,2, Francesco Fornasiero1, Michael
Stadermann1, Alexander Chernov1, Hyung Gyu Park1,
Jung Bin In3, Ji Zang5, David Sholl5, Michael
Colvin4, Aleksandr Noy1,4, Olgica Bakajin,1,2 and
Costas P. Grigoropoulos3 1 Physical and Life
Sciences, LLNL 2 NSF Center for Biophotonics,
UC Davis 3Mechanical Engineering, UC Berkeley
4School of Natural Sciences, UC Merced,
5Chemical and Biochemical Engineering, Georgia
Tech
CARBON NANOTUBE MEMBRANEA NANOFLUIDIC PLATFORM
  • Strongly absorbing gas species (CO2, CH4, and
    C2H4) deviated from the scaled Knudsen permeance
  • Weakly absorbing gas species (He, N2, Ar, and
    SF6) did not show the deviation.
  • Unique surface properties of carbon nanotubes
    enable very rapid and very efficient transport of
    gases and liquids
  • We need to understand
  • Fundamental physics of transport through these
    nanoscale channels
  • Membrane selectivity and rejection properties
  • Fabrication issues associated with making CNT
    membranes with desired geometry and properties
  • Control of transport through CNT membranesAre
    artificial ion channels possible?

Rejection declines at larger salt solution
concentrations
CNT
Aquaporin
Gas transport in CNTs and other nanoporous
materials
K channel
K3Fe(CN)6
CH4/N2 and CO2/N2
KCl
K3Fe(CN)6
KCl
CNT MEMBRANE
  • Free standing membrane
  • Highly aligned DWCNTs
  • Inner diameter 1.6 nm
  • LPCVD Si3N4 pinhole-free matrix
  • Rejection constant when the Debye length is gtgt
    CNT diameter
  • At 263 K, the separation factor increased
    because of increased gas solubility at lower
    temperature.

Comparison with atomistic simulations (CH4/N2)
  • VA-CNT arrays grow from catalytic decomposition
    of carbon precursor, C2H4, over nanoscale Fe
    catalyst
  • Smaller tube has higher separation factor for
    CH4/N2.
  • Polydisperse of tube size in CNT membrane
    affects the separation factor.
  • Electrostatic interactions dominate the ion
    rejection mechanism
  • The largest ion in this series, Ru(bipy)3Cl2,
    permeates freely through the membrane suggesting
    that size effects are less important
  • Carbon nanotube membranes support high flux
    transport of liquids and gases
  • Nanotube growth kinetics studies allowed
    high-yield, high-quality growth of aligned
    nanotube arrays
  • CNT membranes show good ion rejection
    characteristics
  • Ion rejection mechanism is based on electrostatic
    repulsion and follows Donnan model predictions
  • Strongly absorbing gas species deviated from
    Knudsen permeance due to preferential
    interactions with CNTs side walls.
  • At low temperature gas separation factor
    increased because of increased gas solubility
    overall gas separation factors are still lower
    than necessary for practical gas separation

KINETICS OF CARBON NANOTUBE ARRAY GROWTH
  • CNT growth rates exhibit a non-monotonic
    dependence on total pressure and humidity.
    Optimal process pressure and water concentration
    produce growth rate of 30?m/min.
  • Nanotube growth rate remains essentially constant
    until growth reaches an abrupt and irreversible
    termination.
  • We developed a model that predicts termination
    kinetics
  • Selectivity ?A/B yA/(yB) / xA/(xB)
    yA/(1-yA) / xA/(1-xA)
  • where x the mole fractions of gas species at
    the feed side
  • y the mole fractions of gas species
    at the permeate side
  • Holt et. al., Science, 312, 1034 (2006)
  • Noy et. al., Nano Today, 2, 22 (2007)
  • Fornasiero et. al. Proc. Natl. Acad. Sci USA,
    105, 17217 (2008)
  • Stadermann et. al., Nano Letters, in revision
    (2008)

Part of the work at LLNL was performed under the
auspices of the U.S. Department of Energy by
Lawrence Livermore National Laboratory under
Contract DE-AC52-07NA27344.
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