Suresh Bhatia

Effects of Flange Adsorption Affinity and Membrane Porosity on Interfacial Resistance in Carbon Nanotube Membranes

Publisher: American Chemical Society (ACS)

Date: 11-09-2018

DOI: 10.1021/ACSAMI.8B08886

Abstract: We have used nonequilibrium molecular dynamics simulations to investigate the transport diffusion of methane, at 300 K and pressures of up to 15 bar, in 30 nm-long (10, 10) carbon nanotubes (CNTs) held between two flanges mounted at the ends to represent the surface layers of an embedding matrix material. Strong interfacial resistance to the entry and exit of molecules is found in the 30 nm-long CNTs, which reduces their permeability by more than 2 orders of magnitude. Increasing the adsorption affinity and surface area of the flange reduces the interfacial resistance and consequently enhances the methane diffusivity in CNT membranes. Curved streamlines near the flange surface make a significant contribution to the permeability, even when the adsorption on the matrix surface is negligible. We propose a model to calculate the separate components of the interfacial resistance, the flange resistance, which increases with increase in the membrane porosity, and the entrance-exit resistance, which is independent of the membrane porosity. While the flange resistance accounts for the reduction of interfacial resistance with decrease in the membrane porosity, the entrance-exit resistance is responsible for the reduction of interfacial resistance with increase in the flange adsorption affinity. The flange resistivity demonstrates a complex dependency on the flange adsorption affinity, which is attributed to the competition between the enhanced adsorption and the enhanced migration time of the molecules on the flange. It is concluded that the embedding matrix adsorption affinity and membrane porosity separately play critical roles in determining the interfacial resistance and permeability in CNT membranes. Our simulation results can help reduce the interfacial resistance and improve the permeance in CNT membranes by appropriate choice of intertube spacing and flange material and are readily applied to all nanoporous membranes with a passive matrix.

Diffusion of n-decane in mesoporous MCM-41 silicas

Publisher: Elsevier BV

Date: 11-2005

DOI: 10.1016/J.MICROMESO.2005.07.013

Porphyrin–graphene oxide frameworks for long life sodium ion batteries

Publisher: Royal Society of Chemistry (RSC)

Date: 2017

DOI: 10.1039/C7TA02370G

Abstract: Porphyrin–graphene oxide frameworks for ambient temperature sodium-ion storage are investigated. The presence of porphyrin caters for a stronger sodium ion–electrode interaction to realize high-performance sodium-ion batteries, which deliver a capacity of ∼200 mA h g −1 even after resting for one month.

Investigation and simulation of the transport of gas containing mercury in microporous silica membranes

Publisher: Elsevier BV

Date: 11-2018

DOI: 10.1016/J.CES.2018.06.006

Slow diffusion of methane in ultra-micropores of silicon carbide-derived carbon

Publisher: Elsevier BV

Date: 10-2014

DOI: 10.1016/J.CARBON.2014.05.061

Influence of Morphology on Transport Properties and Interfacial Resistance in Nanoporous Carbons

Publisher: American Chemical Society (ACS)

Date: 05-08-2019

DOI: 10.1021/ACS.JPCC.9B06270

Prediction of multilayer adsorption and capillary condensation phenomena in cylindrical mesopores

Publisher: Elsevier BV

Date: 11-2003

DOI: 10.1016/J.MICROMESO.2003.08.018

The transport of gases in macroporous α-alumina supports

Publisher: Elsevier BV

Date: 08-2012

DOI: 10.1016/J.MEMSCI.2012.03.003

Molecular dynamics, grand canonical Monte Carlo and expert simulations and modeling of water–acetic acid pervaporation using polyvinyl alcohol/tetraethyl orthosilicates membrane

Publisher: Elsevier BV

Date: 09-2018

DOI: 10.1016/J.MOLLIQ.2018.05.078

Molecular Simulation of CO₂ Adsorption in the Presence of Water in Single-Walled Carbon Nanotubes

Publisher: American Chemical Society (ACS)

Date: 20-06-2013

DOI: 10.1021/JP403477Y

A Modified Pore-Filling Isotherm for Liquid-Phase Adsorption in Activated Carbon

Publisher: American Chemical Society (ACS)

Date: 02-02-2001

DOI: 10.1021/LA0009339

Understanding the diffusional tortuosity of porous materials: An effective medium theory perspective

Publisher: Elsevier BV

Date: 05-2014

DOI: 10.1016/J.CES.2013.09.050

Effect of structural anisotropy and pore-network accessibility on fluid transport in nanoporous Ti3SiC2 carbide-derived carbon

Publisher: Elsevier BV

Date: 07-2016

DOI: 10.1016/J.CARBON.2016.02.093

The transport of gases in a supported mesoporous silica membrane

Publisher: Elsevier BV

Date: 07-2013

DOI: 10.1016/J.MEMSCI.2013.03.042

Study of Hexane Adsorption in Nanoporous MCM-41 Silica

Publisher: American Chemical Society (ACS)

Date: 09-12-2003

DOI: 10.1021/LA0353430

Abstract: We study here the adsorption of hexane on nanoporous MCM-41 silica at 303,313, and 323 K, for various pore diameters between 2.40 and 4.24 nm. Adsorption equilibria, measured thermogravimetrically, show that all the isotherms, that are somewhat akin to those of type V, exhibit remarkably sharp capillary adsorption phase transition steps and are reversible. The position of the phase transition step gradually shifts from low to high relative pressure with an increase in the temperature as well as the pore sizes. The isosteric heats of adsorption derived from the equilibrium information using the Clapeyron equation reveal a gradual decrease with increasing adsorbed amount because of the surface heterogeneity but approach a constant value near the phase transition. A decrease in the pore size results in an increase in the isosteric heat of adsorption because of the increased dispersion forces. A simple strategy, based on the Broekhoff and De Boer adsorption theory, successfully interprets the hexane adsorption isotherms for the different pore size MCM-41 s les. The parameters of an empirical expression, used to represent the potential of interaction between the adsorbate and adsorbent, are obtained by fitting the monolayer region prior to capillary condensation and the experimental phase transition simultaneously, for some pore sizes. Subsequently, the parameters are used to predict the adsorption isotherm on other pore size s les, which showed good agreement with experimental data.

Kinetic modelling of molecular hydrogen transport in microporous carbon materials

Publisher: Royal Society of Chemistry (RSC)

Date: 2011

DOI: 10.1039/C0CP02235G

Abstract: The proposal of kinetic molecular sieving of hydrogen isotopes is explored by employing statistical rate theory methods to describe the kinetics of molecular hydrogen transport in model microporous carbon structures. A Lennard-Jones atom-atom interaction potential is utilized for the description of the interactions between H(2)/D(2) and the carbon framework, while the requisite partition functions describing the thermal flux of molecules through the transition state are calculated quantum mechanically in view of the low temperatures involved in the proposed kinetic molecular sieving application. Predicted kinetic isotope effects for initial passage from the gas phase into the first pore mouth are consistent with expectations from previous modeling studies, namely, that at sufficiently low temperatures and for sufficiently narrow pore mouths D(2) transport is dramatically favored over H(2). However, in contrast to expectations from previous modeling, the absence of any potential barrier along the minimum energy pathway from the gas phase into the first pore mouth yields a negative temperature dependence in the predicted absolute rate coefficients-implying a negative activation energy. In pursuit of the effective activation barrier, we find that the minimum potential in the cavity is significantly higher than in the pore mouth for nanotube-shaped models, throwing into question the common assumption that passage through the pore mouths should be the rate-determining step. Our results suggest a new mechanism that, depending on the size and shape of the cavity, the thermal activation barrier may lie in the cavity rather than at the pore mouth. As a consequence, design strategies for achieving quantum-mediated kinetic molecular sieving of H(2)/D(2) in a microporous membrane will need, at the very least, to take careful account of cavity shape and size in addition to pore-mouth size in order to ensure that the selective step, namely passage through the pore mouth, is also the rate determining step.

Hybrid Reverse Monte Carlo simulation of amorphous carbon: Distinguishing between competing structures obtained using different modeling protocols

Publisher: Elsevier BV

Date: 03-2015

DOI: 10.1016/J.CARBON.2014.11.013

Characterization of activated carbons using liquid phase adsorption

Publisher: Elsevier BV

Date: 07-2001

DOI: 10.1016/S0008-6223(00)00252-9

Simulation of binary gas separation through multi-tube molecular sieving membranes at high temperatures

Publisher: Elsevier BV

Date: 02-2013

DOI: 10.1016/J.CEJ.2012.12.063

The Use of Liquid Phase Adsorption Isotherms for Characterization of Activated Carbons

Publisher: Elsevier BV

Date: 12-2001

DOI: 10.1006/JCIS.2001.7863

Mitigating the Agglomeration of Nanofiller in a Mixed Matrix Membrane by Incorporating an Interface Agent

Publisher: MDPI AG

Date: 29-04-2021

DOI: 10.3390/MEMBRANES11050328

Abstract: Nanodiamonds (ND) have recently emerged as excellent candidates for various applications including membrane technology due to their nanoscale size, non-toxic nature, excellent mechanical and thermal properties, high surface areas and tuneable surface structures with functional groups. However, their non-porous structure and strong tendency to aggregate are hindering their potential in gas separation membrane applications. To overcome those issues, this study proposes an efficient approach by decorating the ND surface with polyethyleneimine (PEI) before embedding it into the polymer matrix to fabricate MMMs for CO2/N2 separation. Acting as both interfacial binder and gas carrier agent, the PEI layer enhances the polymer/filler interfacial interaction, minimising the agglomeration of ND in the polymer matrix, which is evidenced by the focus ion beam scanning electron microscopy (FIB-SEM). The incorporation of PEI into the membrane matrix effectively improves the CO2/N2 selectivity compared to the pristine polymer membranes. The improvement in CO2/N2 selectivity is also modelled by calculating the interfacial permeabilities with the Felske model using the gas permeabilities in the MMM. This study proposes a simple and effective modification method to address both the interface and gas selectivity in the application of nanoscale and non-porous fillers in gas separation membranes.

Scale-Up Design Analysis and Modelling of Cobalt Oxide Silica Membrane Module for Hydrogen Processing

Publisher: MDPI AG

Date: 05-08-2013

DOI: 10.3390/PR1020049

Use of liquid phase adsorption for characterizing pore network connectivity in activated carbon

Publisher: Elsevier BV

Date: 08-2002

DOI: 10.1016/S0169-4332(02)00066-1

Effects of structural properties of silicon carbide-derived carbons on their electrochemical double-layer capacitance in aqueous and organic electrolytes

Publisher: Springer Science and Business Media LLC

Date: 05-11-2013

DOI: 10.1007/S10008-013-2306-X

Stochastic models of free-molecular nanopore flows

Publisher: AIP Publishing

Date: 06-2023

DOI: 10.1063/5.0148289

Abstract: In gas transport systems of the nanoscale, fluid–surface interactions become the main forces governing the evolution of the flow state. In ideal nanoscale systems, such as atomically smooth carbon nanotubes, the characteristic lengths reduce to such an extent that the non-equilibrium entrance region comprises a large proportion of the domain. In this regime, the added effective resistance induced by the non-equilibrium entrance region becomes large enough that classical effusion models break down. The mechanisms behind the resistance in this regime are still poorly understood. A stochastic model of interfacial resistance is developed here, which allows for the determination of the effective diffusion coefficient via a novel finite-difference solution. We use this method to model free-molecular gas flow through long nanotubes, showing that such non-equilibrium effects may be present in systems of length scales currently within manufacturing capabilities. Finally, this model is used to discuss gas separation through aligned carbon nanotube arrays, with a focus on the effect of membrane length on the separation of a H2–CH4 mixture.

Exceptionally high performance of charged carbon nanotube arrays for CO2 separation from flue gas

Publisher: Elsevier BV

Date: 12-2017

DOI: 10.1016/J.CARBON.2017.09.050

The induced orientation effect of linear gases during transport in a NaA zeolite membrane modified by alkali lignin

Publisher: Elsevier BV

Date: 02-2021

DOI: 10.1016/J.MEMSCI.2020.118971

Influence of Structural Heterogeneity on Diffusion of CH₄ and CO₂ in Silicon Carbide-Derived Nanoporous Carbon

Publisher: American Chemical Society (ACS)

Date: 21-05-2014

DOI: 10.1021/JP502929K

Fluorinated Carbide-Derived Carbon: More Hydrophilic, Yet Apparently More Hydrophobic

Publisher: American Chemical Society (ACS)

Date: 04-05-2015

DOI: 10.1021/JACS.5B01105

Abstract: We explore the effect of fluorine doping on hydrophobicity of nanoporous silicon carbide-derived carbon (SiCDC), and investigate the underlying barriers for adsorption and diffusion of water vapor and CO2 in the fluorinated and nonfluorinated structures. We develop atomistic models of fluorine-doped SiCDC at three different levels of fluorination, based on a hybrid reverse Monte Carlo constructed model of SiCDC, and develop a novel first-principles force field for the simulation of adsorption and transport of water and CO2 in the fluorine-doped carbon materials. We demonstrate an apparent dual effect of fluorination, showing that while fluorination generates more hydrophilic carbon surfaces, they actually act as more hydrophobic structures due to enhanced energy barriers in the disordered network of microporous carbon. While an increase in adsorption energy and in water uptake is seen for fluorine-doped carbon, large internal free energy barriers as well as the results of MD simulations demonstrate that the increased adsorption is kinetically limited and not experimentally observable on practical time scales. We show that an increase in apparent hydrophobicity due to fluorination is mediated by larger free energy barriers arising from stronger binding of fluid molecules inside the pore network, as opposed to repulsion or steric hindrance to the diffusion of molecules through narrow pore entries. For carbon dioxide, adsorption enthalpies and activation energy barriers are both decreased on fluorination, indicating weakened solid-fluid binding energies in the fluorinated systems.

Impact of H₂O on CO₂ Separation from Natural Gas: Comparison of Carbon Nanotubes and Disordered Carbon

Publisher: American Chemical Society (ACS)

Date: 23-12-2014

DOI: 10.1021/JP5099987

Wall Mediated Transport in Confined Spaces: Exact Theory for Low Density

Publisher: American Physical Society (APS)

Date: 18-09-2003

DOI: 10.1103/PHYSREVLETT.91.126102

Improved pore connectivity by the reduction of cobalt oxide silica membranes

Publisher: Elsevier BV

Date: 11-2015

DOI: 10.1016/J.SEPPUR.2015.09.065

Influence of Host-Framework Flexibility on Gas Transport Properties of Nanosheets and Finite-Size Nanomaterials

Publisher: American Chemical Society (ACS)

Date: 10-04-2023

DOI: 10.1021/ACS.JPCC.2C08833

Towards Determining the Interaction of Fluids with Nanostructured Carbons

Publisher: IEEE

Date: 2006

DOI: 10.1109/ICONN.2006.340711

Structural Modelling of Silicon Carbide-Derived Nanoporous Carbon by Hybrid Reverse Monte Carlo Simulation

Publisher: American Chemical Society (ACS)

Date: 07-2013

DOI: 10.1021/JP403929R

Ab initio modelling of basal plane oxidation of graphenes and implications for modelling char combustion

Publisher: Elsevier BV

Date: 2002

DOI: 10.1016/S0008-6223(02)00147-1

O-GlcNAc transferase suppresses necroptosis and liver fibrosis

Publisher: American Society for Clinical Investigation

Date: 11-2019

DOI: 10.1172/JCI.INSIGHT.127709

Investigation of Network Connectivity in Activated Carbons by Liquid Phase Adsorption

Publisher: American Chemical Society (ACS)

Date: 11-2000

DOI: 10.1021/LA000578M

The fluid dynamic effect on the driving force for a cobalt oxide silica membrane module at high temperatures

Publisher: Elsevier BV

Date: 05-2014

DOI: 10.1016/J.CES.2014.02.006

CHARACTERIZATION OF PORE STRUCTURE OF ACTIVATED CARBON BY GAS AND LIQUID PHASE ADSORPTION

Publisher: WORLD SCIENTIFIC

Date: 04-2000

DOI: 10.1142/9789812793331_0016

Effects of the Juxtaposition of Carbonaceous Slit Pores on the Overall Transport Behavior of Adsorbed Fluids

Publisher: American Chemical Society (ACS)

Date: 07-12-2004

DOI: 10.1021/LA047984G

Abstract: It is a common approximation in the modeling of adsorption in microporous carbons to treat the pores as slit pores, whose walls are considered to consist of an infinite number of graphitic layers. In practice, such an approximation is appropriate as long as the number of graphitic layers in the wall is greater than three. However, it is understood that pore walls in microporous carbons commonly consist of three or fewer layers. As well as affecting the solid--fluid interaction within a pore, such narrow walls permit the interaction of fluid molecules through the wall, with consequences for the adsorption characteristics. We consider the effect that a distributed pore-wall thickness model can have on transport properties. At low density we find that the only significant deviation in the transport properties from the infinite pore-wall thickness model occurs in pores with single-layer walls. For a model of activated carbons with a distribution of pore widths and pore-wall thicknesses, the transport properties are generally insensitive to the effects of finite walls, in terms of both the solid-fluid interaction within a pore and fluid-fluid interaction through the pore walls.

Pore accessibility of Ti3SiC2-derived carbons

Publisher: Elsevier BV

Date: 03-2014

DOI: 10.1016/J.CARBON.2013.11.031

Differences in the adsorption and diffusion behaviour of water and non-polar gases in nanoporous carbon: role of cooperative effects of pore confinement and hydrogen bonding

Publisher: Informa UK Limited

Date: 06-11-2014

DOI: 10.1080/08927022.2014.976640

Interfacial Resistance and Length-Dependent Transport Diffusivities in Carbon Nanotubes

Publisher: American Chemical Society (ACS)

Date: 15-11-2016

DOI: 10.1021/ACS.JPCC.6B09136

Effect of pore-network connectivity on multicomponent adsorption of large molecules

Publisher: Wiley

Date: 2003

DOI: 10.1002/AIC.690490108

Inhibitory Effect of Adsorbed Water on the Transport of Methane in Carbon Nanotubes

Publisher: American Chemical Society (ACS)

Date: 15-06-2017

DOI: 10.1021/ACS.LANGMUIR.7B01070

Abstract: We investigate the transport diffusion of methane at 300 K and pressures of up to 15 bar in dry and wetted carbon nanotubes (CNTs) having diameters ranging from 0.95 to 2.034 nm using nonequilibrium molecular dynamics (NEMD) simulation. Because of their strong hydrogen bonding, preadsorbed water molecules transport in the form of clusters and block the diffusion of methane, reducing the Onsager coefficient of methane dramatically compared to that in dry CNTs. The reduction in the methane Onsager coefficient is greater in narrower CNTs or at higher water densities. Because the diameter of the water clusters is almost invariant with water density, the Onsager coefficient of water in the (10, 10) CNT increases linearly with water density. It is further found that whereas decreasing the CNT diameter from 2.034 to 0.95 nm enhances the Onsager coefficient of pure methane by about 1 order of magnitude, the Onsager coefficient of water is almost independent of the CNT diameter at a water density of 0.05 g/cm

Kinetics of the Dehydroxylation of Serpentine

Publisher: American Chemical Society (ACS)

Date: 11-01-2012

DOI: 10.1021/EF201360B

Comparative Analysis of Structural and Morphological Properties of Large-Pore Periodic Mesoporous Organosilicas and Pure Silicas

Publisher: American Chemical Society (ACS)

Date: 29-09-2004

DOI: 10.1021/JP047479S

Special Issue on “Transport of Fluids in Nanoporous Materials”

Publisher: MDPI AG

Date: 2019

DOI: 10.3390/PR7010014

Abstract: Understanding the transport behavior of fluid molecules in confined spaces is central to the design of innovative processes involving porous materials and is indispensable to the correlation of process behavior with the material structure and properties typically used for structural characterizations such as pore dimension, surface texture, and tortuosity. [...]

Sodium ion storage in reduced graphene oxide

Publisher: Elsevier BV

Date: 10-2016

DOI: 10.1016/J.ELECTACTA.2016.08.058

Preparation of 3D open ordered mesoporous carbon single-crystals and their structural evolution during ammonia activation

Publisher: Royal Society of Chemistry (RSC)

Date: 2018

DOI: 10.1039/C8CC05318A

Abstract: Three-dimensional ordered mesoporous carbon single-crystals with well-interconnected open mesoporous structures are obtained via a simple and facile soft-template strategy.

Enhanced CO₂ sorption efficiency in amine-functionalised 2D/3D graphene/silica hybrid sorbents

Publisher: Royal Society of Chemistry (RSC)

Date: 2018

DOI: 10.1039/C8CC06373G

Abstract: Owing to the geometrical features of 2D graphene intercalated into 3D mesoporous silica, CO 2 sorption increased by 51% and the heat of sorption reduced by up to 27% as compared to a pure 3D mesoporous silica sorbent without graphene.

Correction to “System Size-Dependent Transport Properties in Materials of Nanoscale Dimension”

Publisher: American Chemical Society (ACS)

Date: 16-02-2022

DOI: 10.1021/ACS.JPCC.2C00706

The transport of gases in a mesoporous γ-alumina supported membrane

Publisher: Elsevier BV

Date: 02-2013

DOI: 10.1016/J.MEMSCI.2012.10.015

Modeling molecular transport in slit pores

Publisher: AIP Publishing

Date: 08-03-2004

DOI: 10.1063/1.1647516

Abstract: We examine the transport of methane in microporous carbon by performing equilibrium and nonequilibrium molecular dynamics simulations over a range of pore sizes, densities, and temperatures. We interpret these simulation results using two models of the transport process. At low densities, we consider a molecular flow model, in which intermolecular interactions are neglected, and find excellent agreement between transport diffusion coefficients determined from simulation, and those predicted by the model. Simulation results indicate that the model can be applied up to fluid densities of the order to 0.1–1 nm−3. Above these densities, we consider a slip flow model, combining hydrodynamic theory with a slip condition at the solid–fluid interface. As the diffusion coefficient at low densities can be accurately determined by the molecular flow model, we also consider a model where the slip condition is supplied by the molecular flow model. We find that both density-dependent models provide a useful means of estimating the transport coefficient that compares well with simulation.

System Size-Dependent Transport Properties in Materials of Nanoscale Dimension

Publisher: American Chemical Society (ACS)

Date: 23-03-2021

DOI: 10.1021/ACS.JPCC.1C01043

Complementary Effects of Pore Accessibility and Decoordination on the Capacitance of Nanoporous Carbon Electrochemical Supercapacitors

Publisher: American Chemical Society (ACS)

Date: 17-12-2015

DOI: 10.1021/ACS.JPCC.5B10712

Molecular Simulation and Computational Modeling of Gas Separation through Polycarbonate/p-Nitroaniline/Zeolite 4A Mixed Matrix Membranes

Publisher: American Chemical Society (ACS)

Date: 18-08-2020

DOI: 10.1021/ACS.IECR.0C02827

Adsorption of flavour esters on granular activated carbon

Publisher: Wiley

Date: 10-2000

DOI: 10.1002/CJCE.5450780506

Barriers to diffusion of CO2 in microporous carbon derived from silicon carbide

Publisher: Elsevier BV

Date: 07-2015

DOI: 10.1016/J.CARBON.2015.02.064

Interpreting gas sorption isotherms in glassy polymers using a Bayesian framework: A view on parameter uncertainty propagation into mixture sorption predictions

Publisher: Elsevier BV

Date: 2024

DOI: 10.1016/J.MEMSCI.2023.122159

Adsorption and transport of gases in a supported microporous silica membrane

Publisher: Elsevier BV

Date: 06-2014

DOI: 10.1016/J.MEMSCI.2014.02.028

Computational investigation on CO2 adsorption in titanium carbide-derived carbons with residual titanium

Publisher: Elsevier BV

Date: 2017

DOI: 10.1016/J.CARBON.2016.10.037

Adsorption of CH4 and CH4/CO2 mixtures in carbon nanotubes and disordered carbons: A molecular simulation study

Publisher: Elsevier BV

Date: 2015

DOI: 10.1016/J.CES.2014.07.041

Computational fluid dynamics applied to high temperature hydrogen separation membranes

Publisher: Springer Science and Business Media LLC

Date: 17-02-2012

DOI: 10.1007/S11705-011-1161-5

Diffusion of Linear Paraffins in Nanoporous Silica

Publisher: American Chemical Society (ACS)

Date: 05-03-2005

DOI: 10.1021/IE048931X

Kinetic analysis for cyclic CO₂ capture using lithium orthosilicate sorbents derived from different silicon precursors

Publisher: Royal Society of Chemistry (RSC)

Date: 2018

DOI: 10.1039/C8DT01617H

Abstract: The illustration of the CO 2 sorption process in Li 4 SiO 4 .

Solubility of selected esters in supercritical carbon dioxide

Publisher: Elsevier BV

Date: 09-2003

DOI: 10.1016/S0896-8446(02)00190-0

Nonuniformity of Transport Coefficients in Ultrathin Nanoscale Membranes and Nanomaterials

Publisher: American Chemical Society (ACS)

Date: 30-11-2021

DOI: 10.1021/ACSAMI.1C18659

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Medical University Of South Carolina

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Linkage - International - Grant ID: LX0561185

Start Date: 2005

End Date: 12-2007

Amount: $46,800.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP210101698

Start Date: 01-2021

End Date: 2024

Amount: $240,000.00

Funder: Australian Research Council

Linkage Projects - Grant ID: LP0560407

Start Date: 05-2005

End Date: 05-2008

Amount: $596,607.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP0877925

Start Date: 2008

End Date: 12-2010

Amount: $390,000.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP0449628

Start Date: 2004

End Date: 12-2007

Amount: $230,000.00

Funder: Australian Research Council

Linkage Projects - Grant ID: LP0453494

Start Date: 2004

End Date: 12-2007

Amount: $241,698.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP150101996

Start Date: 2015

End Date: 12-2017

Amount: $393,800.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP150101824

Start Date: 2015

End Date: 12-2021

Amount: $537,100.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP0771344

Start Date: 2007

End Date: 12-2009

Amount: $330,000.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP1092437

Start Date: 2010

End Date: 07-2015

Amount: $1,000,000.00

Funder: Australian Research Council

Linkage Projects - Grant ID: LP0455471

Start Date: 07-2004

End Date: 03-2008

Amount: $241,624.00

Funder: Australian Research Council

Linkage Projects - Grant ID: LP0882574

Start Date: 11-2008

End Date: 09-2012

Amount: $785,221.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP0208804

Start Date: 2004

End Date: 12-2006

Amount: $292,000.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP0556342

Start Date: 2005

End Date: 12-2007

Amount: $258,000.00

Funder: Australian Research Council

Linkage Infrastructure, Equipment And Facilities - Grant ID: LE0989675

Start Date: 2009

End Date: 04-2010

Amount: $180,000.00

Funder: Australian Research Council

Linkage Infrastructure, Equipment And Facilities - Grant ID: LE0882357

Start Date: 2008

End Date: 01-2009

Amount: $500,000.00

Funder: Australian Research Council

Linkage Projects - Grant ID: LP0348032

Start Date: 07-2003

End Date: 07-2006

Amount: $660,000.00

Funder: Australian Research Council

ARC Centres Of Excellence - Grant ID: CE230100017

Start Date: 12-2023

End Date: 12-2030

Amount: $34,956,464.00

Funder: Australian Research Council

Discovery Projects - Grant ID: DP120101480

Start Date: 2012

End Date: 12-2014

Amount: $330,000.00

Funder: Australian Research Council

Linkage Projects - Grant ID: LP160100512

Start Date: 12-2016

End Date: 12-2021

Amount: $430,000.00

Funder: Australian Research Council

Linkage Infrastructure, Equipment And Facilities - Grant ID: LE120100109

Start Date: 04-2012

End Date: 03-2015

Amount: $370,000.00

Funder: Australian Research Council