July 2, 2017
BACHELOR THESIS
TRANSPORT PHENOMENA IN MONOLAYER GRAPHENE MEMBRANES
Koen F.A. Jorissen
Faculty of Science and Technology Soft Matter, Fluids and Interfaces group
Exam committee:
M. Ghosh, MSc Dr. J.A. Wood
Prof.Dr.Ir. R.G.H Lammertink
Dr. ir. D.W.F. Brilman
Abstract
Graphene ion exchange membranes were characterized using permselectivity, permporometry and
membrane permeability analysis. Donnan and diffusion based transport was analyzed for KCl,
LiCl, K
2SO
4and CaCl
2. Concentration-potential were found for KCl, LiCl and K
2SO
4. The data
is qualitatively discussed using Debye-Huckel theory. Physical properties of the membrane were
characterized fitting this data to Teorell-Meyer-Sievers theory. An attempt to determine pore size
and distribution was made, though results were inconclusive. Membrane permeance of water was
found negligible for pressures up to 4 bar. TMS theory was found somewhat applicable to the
graphene membrane. Ways of improving fitting and further areas of interest are suggested.
Symbols and Abbreviations
Symbols
v Velocity [
ms]
C
iConcentration component i [mM]
T Temperature [K]
D
iDiffusion constant of i [
ms2] z
iCharge number of i [-]
E Electric field [
Vm]
λ
DDebye length [m]
I Ionic strength [mM]
J
iFlux [
molm2
]
V Potential [V]
C
RFixed charge concentration [mM]
ζ Membrane selectivity [-]
β Membrane performance [-]
u
iIon mobility [
v∗sm2]
δ Membrane thickness [m]
γ
iIon activity of i [mM]
Constants
R Ideal Gas Constant 8.314
molKJF Faraday Constant 96 485
molCe Elementary Charge 1.602 ∗ 10
−19C k
BBoltzmann Constant 1.381 ∗ 10
−23 JKε
0Vacuum permittivity 8.854 ∗ 10
−12 FmAbbreviations TMS Teorell-Meyer-Sievers PET Polyethylene-terephthalate PMMA Polymethyl-methacrylate SEM Scanning Electron Microscopy MD Molecular Dynamics
All units are SI unless stated otherwise.
Contents
1 Introduction 1
1.1 Motivation and Background . . . . 1
1.2 Topic of Research . . . . 2
1.3 Ethics and Social Considerations . . . . 2
2 Theory 4 2.1 Physical Phenomena in Electrolytes . . . . 4
2.2 Membranes . . . . 5
2.3 Non-ideal Membranes . . . . 8
2.4 Mechanical and Material Limitations . . . . 8
2.5 Dielectric Exclusion . . . . 8
3 Experimental Approach 9 3.1 Sample Preparation . . . . 9
3.2 Permselectivity . . . . 9
3.3 Membrane Permeance . . . . 10
3.4 Pore Size and Size Distribution . . . . 10
4 Results and Discussion 12 4.1 Pore Size and Size Distribution . . . . 12
4.2 Permselectivity . . . . 13
4.3 Water Permeance . . . . 16
5 Conclusion 18
6 Future Recommendations 19
Bibliography 21
Appendix i
1 | Introduction
Global fresh water demand is rapidly rising, and this demand is not always met. While this is partly for economic reasons, large coastal areas in Africa and Asia suffer a physical water shortage.
This shortage can be met by desalination of seawater[1]. Methods of desalinating water include evaporation, electrodialysis, freezing and reverse osmosis[2]. Both electrodialysis and reverse osmosis processes use membranes to separate salts from water. Reverse osmosis is a pressure driven process, in which water is pumped through the membrane while ions are rejected. The method is commercially viable, although other techniques are more energy efficient[3, 4]. Recently, graphene has been researched as an ion-selective membrane which is expected to be applicable in reverse osmosis processes.
1.1 Motivation and Background
Figure 1.1: Graphical representa- tion of a graphene membrane.
Graphene is one of about 700 stable two-dimensional, one atom thick materials currently known[5]. Being one carbon atom thick, graphene has a thickness of 3.5Å[6]. Graphene was first observed in 1948 but only isolated in 2004[6]. Since then, new methods of pro- ducing graphene at higher purities, larger continuous crys- tals and lower costs have rapidly been developing[7].
It has shown great promise for a multitude of appli- cations. Graphene has shown unique electrical proper- ties, high mechanical strength and has been shown to be impermeable to nearly all substances. Due to its unique and promising properties, as well as its physi- cal simplicity as a two-dimensional material, research in graphene has grown exponentially since it was first iso- lated.
Graphene-based membranes such as graphene-oxide and
reduced graphene-oxide have been successfully used in reverse osmosis processes[8]. Their the- oretical and practical efficiency are comparable to commercially available polymer membranes.
More recently, porous graphene has been developed as a membrane. Using ion bombardement and etching technologies, size-controlled pores have been created in graphene[9].
Graphene is shown to have great promise as a membrane in theory[10]. Graphene and graphene- based membranes are extensively modeled using MD and other modeling techniques in literature.
Ionic selectivity is shown to persist for pore diameters up to twenty nanometer[11]. Graphene based
ion exchange membranes are shown to have high theoretical efficiency due to graphene’s high
hydrophobicity[12] and low membrane thickness. Due to hydrophobic interaction, water transport
through pores in graphene has low friction. A graphic representation of a graphene membrane is given in figure 1.1.
Graphene production over large areas and at low costs is still challenging, though methods are rapidly developing[6]. Therefore, it is reasonable to believe suitable areas of graphene membranes will become commercially viable in the future.
There are two ion rejection principles at work in nanofiltration membranes. These transport limiting phenomena are known as Donnan exclusion and dielectric exclusion[13], and are expanded upon in the theory section. Either cations or anions are selectively passed through the ion exchange membrane. A net charge can not exist between the two phases, so transport driving forces of the ion to which the membrane is selective work against the other ion species’ rejection force.
1.2 Topic of Research
In this thesis, the relevant transport phenomena like Donnan exclusion and dielectric exclusion will be identified for nanoporous graphene. This is done by studying the transport through the membrane with different salt concentrations (tuning the Debye length). Both mono and bivalent salts will be used to identify the effects of dielectric exclusion and Donnan exclusion. Additionally, size distribution of pores and pore distribution will be studied. This can be done through two methods;
permporometry and Scanning Electron Microscopy (SEM). The SEM imaging will mainly be used to characterize PET, whereas permporometry will be used to study the graphene membranes (due to SEM resolution restrictions). Through these techniques, the pore size and spacial distribution may be studied. The effects of this variance may then be studied using electrochemistry. The relation between the physical properties of nanoporous graphene to the selectivity of ions will be developed.
1.3 Ethics and Social Considerations
If water purification through graphene membranes approaches its theoretical efficiency on an industrial scale, this will have effects on water related politics. It will play a particularly important role in coastal areas of drought, which are abundant in Africa and Asia as can be seen in figure 1.2.
Figure 1.2: Global physical water shortage per river basin, reproduced from [1].
As can be seen from figure 1.2, areas of drought span multiple political regions. Localization of
water sources near the coast due to viability of reverse osmosis plants may yield significant political
and economical power to the controllers of these plants. The control of desalination water plants
must therefore be carefully considered. Although political implications of more centralized water
production are an important consideration, an economical or politically stemmed water shortage is
preferred to a physical shortage. Therefore, this research will contribute to solving the problem.
2 | Theory
Modeling of ion-exchange membranes is well established[14]. Conventional ion exchange mem- branes are orders of magnitude thicker than graphene membranes. Some membrane parameters, such as fixed pore concentration, are less physically correct for a graphene membrane considering its thickness. The low membrane thickness makes the concentration have little meaning. In this theory section, two ion transport models for membranes will be presented. Finally, some theory regarding non-ideality of membranes and the unique properties of graphene will be discussed.
2.1 Physical Phenomena in Electrolytes
In order to understand the processes surrounding an ion-exchange membrane, the transport driving forces and electric screening forces within the membrane must be understood. Commonly used theories describing these forces are introduced.
The Nernst-Planck Equation
One of the most common methods of describing ion transport in fluids is the Nernst-Planck electrodiffusion equation. It describes ion flux for three different additive driving forces. The one-dimensional transport of ion i in an electrolyte is given by equation 2.1[15].
J
i= vC
iConvection
|{z}
−D ¯
id ¯ C
idx − D
idln ¯ γ
idx
| {z }
Di f f usion
− z
iD ¯
iC
iF RT
dE dx
| {z }
Migration
(2.1)
The fundamental understanding in the formulation of the Nernst-Planck equation is the additivity (and independence) of the diffusion and electrodiffusion factors. The Nernst Planck equation is the foundation of TMS theory, discussed in section 2.2
Electric Field Screening
The electric field induced by an ion in an electrolyte is screened by both dielectric effects of water and those of other ions. Electrostatic interaction between two charged particles can be described by Coulombs law. In describing the interaction, it is calculated for each ion pair in the system.
Two particle interactions scale exponentially with the amount of particles in the system. For larger systems, the amount of interactions grows to be incalculable[16].
In the Debye-Hückel approach, the many interactions are averaged through mean-field approach.
Each particle is approached as if it is in a homogeneous field, induced by the distribution of
surrounding particles. Interaction for each particle must now only be calculated with the mean
electric field in the electrolyte, and identical particles now give identical interactions as they are no
longer dependent on their environment. The result is the Debye-Hückel equation[17], equation 2.2.
λ
D−1= s
2e
2I
ε
0k
BT (2.2)
Here the Debye layer is introduced. It is the length in which the electric field induced by the ion decays by
1e. Negative screening allows transport for cations, while anions are repelled. As can be seen in the equation, the Debye length is dependent on ionic strength I. The ionic strength is given by I =
12∑
i