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NPTEL Chemical Engineering Interfacial Engineering Module 2: Lecture 5
Joint Initiative of IITs and IISc Funded by MHRD 1/22
Deposition of Thin Films on Solid Surfaces
Dr. Pallab Ghosh
Associate Professor
Department of Chemical Engineering
IIT Guwahati, Guwahati–781039
India
NPTEL Chemical Engineering Interfacial Engineering Module 2: Lecture 5
Joint Initiative of IITs and IISc Funded by MHRD 2/22
Table of Contents
Section/Subsection Page No. 2.5.1 Nucleation and film growth 3–20
2.5.1.1 Evaporation 5
2.5.1.2 Molecular beam epitaxy 7
2.5.1.3 Sputtering 9
2.5.1.4 Chemical vapor deposition 10
2.5.1.5 Atomic layer deposition 14
2.5.1.6 Electrochemical deposition 16
2.5.1.7 Langmuir–Blodgett films 16
Exercise 21
Suggested reading 22
NPTEL Chemical Engineering Interfacial Engineering Module 2: Lecture 5
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2.5.1 Nucleation and film growth
Deposition of thin films has been studied for almost a century. Some of the
techniques developed during the past five decades are widely used in the industries. The
methods for depositing a film can be divided into two categories: (i) vapor-phase
deposition (e.g., chemical vapor deposition, evaporation, molecular beam epitaxy,
sputtering and atomic layer deposition), and (ii) liquid-based deposition (e.g.,
electrochemical deposition, chemical solution deposition, Langmuir–Blodgett films and
self-assembled monolayers).
The film deposition involves heterogeneous processes such as heterogeneous
chemical reactions, evaporation, adsorption and desorption on growth surfaces.
Growth of films of nanoscale thickness involves nucleation and growth on the
surface of the substrate. The nucleation step is very important because it governs
the crystallinity and microstructure of the film. There are three basic modes of
nucleation: (i) island or Volmer–Weber, (ii) layer or Frank–van der Merwe, and
(iii) island–layer or Stranski–Krastonov nucleation. These three modes of
nucleation are illustrated in Fig. 2.5.1.
Fig. 2.5.1 Schematic illustration of three basic modes of initial nucleation in the
film growth.
Island growth occurs when the species are bound to each other more strongly than
to the substrate. The islands subsequently merge and form a continuous film.
Metals on insulators, alkali halides, graphite and mica display this type of
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mechanism during the initial film deposition. Subsequent growth results in the
islands to join to form a continuous film. The layer growth is the opposite of the
island growth. The species are bound more strongly to the substrate than to each
other. First a complete monolayer is formed and then the deposition of the second
layer begins. The epitaxial growth of single-crystal films is an important example
of layer growth. The island– layer growth mechanism is a combination of both
island and layer growths. Such a growth mode typically involves the stress, which
is developed during the formation of the nuclei or films.
The critical nucleus size r and the corresponding free energy barrier G are
given by the following equations.
2
3
2 sin 2cos 2
2 3cos cos
vf
vr
G
(2.5.1)
3
2
16 2 3cos cos
43
vf
v
GG
(2.5.2)
where is the contact angle. vf , fs and sv are the interfacial energies of
vapor–nucleus, nucleus–substrate and substrate–vapor interfaces, respectively,
and vG is the change in Gibbs free energy per unit volume of the solid phase.
For the layer growth, the deposit wets the substrate completely, and therefore, the
contact angle is zero. Thus, Young–Dupré equation becomes,
sv fs vf (2.5.3)
For island growth, the contact angle is larger than zero. According to Young–
Dupré equation, we have,
sv fs vf (2.5.4)
If the deposit does not wet the substrate at all, , and the nucleation is a
homogeneous nucleation.
The most important layer growth is the deposition of single crystal films through
either homoepitaxy (in which the depositing film has the same crystal structure
and chemical composition as that of the substrate), or heteroepitaxy (in which the
depositing film has a close matching crystal structure as that of the substrate).
NPTEL Chemical Engineering Interfacial Engineering Module 2: Lecture 5
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Homoepitaxy is a simple extension of the substrate, and there is virtually no
interface between the substrate and the depositing film. Although the deposit has
a chemical composition different from that of the substrate, the growth species
prefers to bind to the substrate rather than to each other. Because of the difference
in chemical composition, the lattice constants of the deposit are most likely to
differ from those of the substrate. Such a difference can lead to the development
of stress in the deposit. Stress is one of the common reasons for the island–layer
growth.
Most of film deposition and processing are carried out in vacuo. In a gas phase,
the molecules are continuously in motion. They collide among themselves as well
as with the walls of the container. The mean distance traveled by molecules
between successive collisions is called the mean free path. It is inversely
proportional to pressure. Under typical film deposition and characterization
conditions, the gas molecules virtually collide only with the walls of the vacuum
chamber, i.e., there is no collision among the gas molecules.
The gas impingement flux in film deposition is a measure of the frequency with
which the gas molecules impinge on or collide with a surface. Only those
molecules which impinge on the growth surface are able to contribute to the
growth process. The number of gas molecules that strike a surface per unit time
and area is defined as the gas impingement flux, which is proportional to
P MT , where P is pressure, M is molecular weight and T is temperature.
In the physical vapor deposition processes (which are discussed below), the
growth species is transferred from a source (or target) and deposited on a
substrate to form a film. The process is essentially atomistic and no chemical
reaction is involved. Various methods have been developed for this transfer
process. The thickness of the deposit can vary from ~1 nm to several millimeters.
2.5.1.1 Evaporation
Evaporation is the simplest physical deposition method for preparation of thin
films. The evaporation system consists of an evaporation source that vaporizes
the desired material and the substrate. Both the source and the substrate are
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placed in the vacuum chamber. The substrate faces the evaporation source. The
set-up is schematically shown in Fig. 2.5.2.
Fig. 2.5.2 A typical evaporation system depicting the source, substrate and the
vacuum chamber.
The substrate can be placed and heated as desired. The necessary vapor pressure
of the source material can be generated by simply heating the source as per the
requirements of the concentration of the growth species in the gas phase. The
equilibrium vapor pressure vP of an element can be estimated from the
Clausius–Clapeyron equation.
ln vH
P CRT
(2.5.5)
where H is the molar heat of evaporation, R is the gas constant, T is
temperature and C is a constant. The rate of evaporation is given by,
2A v hN P P
MRT
(2.5.6)
where is the coefficient of evaporation, AN is Avogadro’s number, hP is the
hydrostatic pressure acting on the source, vP is vapor pressure, M is the
molecular weight, R is gas constant and T is temperature.
Precautions need to be taken for pyrolysis, decomposition and dissociation of the
compound being heated. Deposition of thin films by evaporation is carried out at
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very low pressures (1 108 – 0.1 Pa). The molecules in the vapor phase do not
collide with each other prior to the arrival at the growth surface because the mean
free path is very large as compared to the distance between the source and the
substrate. The transport of molecules from the source to the growth substrate is
straight-forward along the line of sight. Therefore, the conformal coverage is
relatively poor and it is difficult to obtain a uniform film over a large area. To
overcome this difficulty, multiple sources are used and the substrate is rotated.
Laser beams have been used to evaporate the material. Pulsed laser beams are
used where high power density is required. This process is known as laser
ablation. The composition of the vapor can be controlled precisely using this
technique. Laser ablation has been used for depositing metal oxides in
superconductor films.
2.5.1.2 Molecular beam epitaxy
Molecular beam epitaxy (MBE) can be considered as a more sophisticated
version of the evaporation technique. In MBE, the vacuum is very high such that
the pressure inside the reactor is of the order of 81 10 Pa. At this pressure, the
mean free path of the gas molecules far exceeds the distance between the source
and the target. Apart from the ultrahigh vacuum system, MBE usually consists of
real time structural and chemical characterization capability. Other analytical
instruments may also be attached to the deposition chamber such that the grown
films can be transferred to and from the growth chamber without exposing to the
ambient. The MBE set-up is expensive, and a typical one may cost ~US$ 1
million. A MBE facility is shown in Fig. 2.5.3.
In MBE, the evaporated atoms or molecules from one or more sources do not
interact with each other in the vapor phase under such a low pressure. Although
some gaseous sources are used in MBE, most molecular beams are generated by
heating the solid source material in effusion cells (known as Knudsen cells). The
material is raised to the desired temperature by resistive heating.
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Fig. 2.5.3 Molecular beam epitaxy system to grow and characterize thin crystalline films of oxides and ceramics.
The molecules strike on the single-crystal substrate resulting in the formation of
the desired epitaxial film. The extremely clean environment, slow growth rate
(~ 103 10 m/s) and independent control of evaporation of the source material
ensures precise formation of the film. Ultrahigh vacuum environment ensures
absence of impurity or contamination. Thus, a highly pure film can be readily
obtained. Individually controlled evaporation of sources permits the precise
control of chemical composition of the deposit at any given time. The slow
growth rate ensures sufficient surface diffusion and relaxation so that the
formation of crystal defects is kept minimal. The main attributes of MBE are:
(i) A low growth temperaure (e.g., 800 K) that limits diffusion and maintains
hyperabrupt interfaces, which are very important in fabricating two-dimensional
nanostructures or multilayer structures such as quantum wells.
(ii) A slow growth rate that ensures a well controlled two dimensional growth at a
typical rate of 1 micrometer per hour. A very smooth surface is achievable by
controlling the growth at the monoatomic layer level.
(iii) A simple growth mechanism compared to other film growth techniques ensures
better understanding due to the ability of individually controlled evaporation of
sources.
(iv) A variety of in situ analysis capabilities provide important information for the
understanding and refinement of the process.
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2.5.1.3 Sputtering
Sputtering involves use of energetic ions to knock molecules out from a target
which acts as one electrode and subsequently deposit them on the substrate that
acts as the second electrode. In a typical sputtering chamber, the source and
substrate electrodes face each other. An inert gas such as argon at low pressure
(~15 Pa) is used as the medium. When a high electric field (~10 kV/cm) is
applied to initiate the glow-discharge between the electrodes, free electrons are
accelerated by the electric field and ionize the argon atoms. The gas pressure
should not be too low, otherwise the electrons will simply strike the anode
without having gas-phase collision with the argon atoms. The Ar+ ions thus
generated strike the source electrode resulting in the ejection of neutral target
atoms. These atoms pass through the discharge and deposit on the substrate
electrode. In addition to the growth species (i.e., neutral atoms), other negatively
charged species under the electric field will also bombard and interact with the
surface of the substrate or grown film.
For the deposition of insulating films, an alternate electric field is applied to
generate plasma between two electrodes. Typical frequencies employed range
from 5 to 30 MHz. The key element in sputtering is that the target self-biases to a
negative potential and behaves like a DC target. Such a self-negative target bias is
a consequence of the fact that the electrons are considerably more mobile than
ions and have little difficulty in following the periodic change in the electric field.
To prevent simultaneous sputtering on the grown film or substrate, the sputter
target must be an insulator and be capacitively coupled to the generator. This
capacitor will have a low impedence and will allow the formation of a DC bias on
the electrodes.
The types of plasmas encountered in thin film processing systems are typiclly
formed by partially ionizing a gas at a pressure well below the atmospheric
pressure. These plasmas are very weakly ionized (the ionization fraction varies
between 51 10 0.1 ). The plasma based film processes differ from other film
deposition techniques such as evaporation, because the plasma process is not
thermal.
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A comparison between evaporation and sputtering is given in Table 2.5.1.
Table 2.5.1 Comparison between evaporation and sputtering
Evaporation Sputtering
Pressure: 1 108 – 0.1 Pa Pressure: 10–15 Pa
Atoms in the evaporation chamber do not
collide with each other prior to arrival at
the growth surface
Atoms and molecules collide with each
other prior to arrival at the growth surface
The process occurs under equilibrium The sputtering process is not governed by
thermodynamic equilibrium
The growth surface is not activated The growth surface is continuously
bombarded by electrons, and thus it is
highly energetic
The evaporated films consist of large
grains
The sputtered films consist of smaller
grains with better adhesion to the substrates
2.5.1.4 Chemical vapor deposition
Chemical vapor deposition (CVD) involves chemically reacting a volatile
compound with other gases to produce a nonvolatile solid that deposits
atomistically on a suitably placed substrate. The CVD process is widely used in
the manufacture of solid-state microelectronic devices.
Both gas phase and surface chemical reactions are involved in CVD, and they are
intricately combined. The gas phase reactions become progressively important
with increasing temperature and partial pressure of the reactants. An extremely
high concentration of reactants will make the gas phase reactions predominant,
leading to homogeneous nucleation. For deposition of good quality films,
homogeneous nucleation should be avoided. The major types of chemical
reaction are: pyrolysis, oxidation, reduction and disproportionation. Some
examples of the reactions are given below.
1. Pyrolysis (or thermal decomposition):
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4 2
4
SiH (g) Si(s) 2H g at 923 K
Ni CO (g) Ni(s) + 4CO (g) at 453 K
2. Oxidation:
4 2 2 2
3 2 2 5 2
SiH (g) O (g) SiO (s) + 2H (g) at 723 K
4PH (g) + 5O (g) 2P O (s) + 6H (g) at 723 K
3. Reduction:
4 2
6 2
SiCl (g) 2H (g) Si(s) + 4HCl(g) at 1473 K
WF (g) + 3H (g) W(s) + 6HF(g) at 573 K
4. Disproportionation:
2 42GeI (g) Ge(s) + GeI (g) at 573 K
The CVD process is versatile because for depositing a given film, many different
reactants or precursors may be used. From the same precursors and reactants,
different films can be obtained by varying the ratio of reactants and deposition
conditions. One of the important applications of CVD is to make diamond films
from gas phase deposition at low pressure.
Various types of CVD methods and reactors are used depending on the reactants,
reaction conditions and the forms of energy used to activate the reactions.
o When an organometallic compound is used as the precursor, the process is called
metalorganic CVD.
o When plasma is used to promote the reaction, the process is known as plasma-
enhanced CVD (PECVD).
o There are modified CVD processes such as low-pressure CVD (LPCVD), laser-
enhanced CVD and aerosol-assisted CVD (AACVD).
A set-up for CVD is shown in Fig. 2.5.4. Some of the most common types of
CVD reactors are horizontal, vertical, barrel and pan cake reactors. The reactors
used in the CVD processes can be classified into hot wall and cold wall types.
The hot wall reactors are usually tubular, and heating is accomplished by
surrounding the reactor with resistance elements. In cold wall reactors, the
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substrates are directly heated inductively by graphite susceptors and the chamber
walls are cooled by air or water.
Fig. 2.5.4 Microwave plasma-enhanced chemical vapor deposition (PECVD) system for the growth of ultrananocrystalline diamond films.
LPCVD differs from conventional CVD in the low pressure used, viz. ~0.1 kPa.
The low pressure enhances the mass flux of gaseous reactants and products
through the boundary layer between the laminar gas stream and substrates. In
PECVD processing, plasma is sustained within chambers where simultaneous
CVD reactions occur. Typically, the plasma is excited by an electric field with
frequency ranging from 100 kHz to 40 MHz at very low pressures, or by
microwave with a frequency of 2.45 GHz. Often the microwave energy is coupled
to the natural resonant frequency of the plasma electrons in the presence of a
static magnetic field. Such plasma is referred to as electron cyclotron resonance
plasma. The introduction of plasma results in much enhanced deposition rates,
which permits the growth of films at relatively low substrate temperatures.
Laser has also been employed to enhance or assist the chemical reactions or
deposition. Two mechanisms are involved, viz. pyrolytic and photolytic
processes. In the pyroltic process, the laser heats the substrate to decompose gases
above it and enhances rates of chemical reactions, whereas in the photolytic
process, laser photons are used to directly dissociate the precursor molecules in
the gas phase. Aerosol assisted CVD is developed for the systems where no
gaseous precursors are available and the vapor pressures of liquid and solid
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precursors are too low. In this process, liquid precursors are atomized to form tiny
droplets, which are dispersed in a carrier gas and delivered to the deposition
chamber. Inside the deposition chamber, the precursor droplets decompose, react
and grow films on the substrate.
In addition to the growth of thin films on a planar substrate, CVD methods have
been modified and developed to deposit solid phase from gaseous precursors on
highly porous substrates or inside porous media. Two important varieties of CVD
for these applications are electrochemical vapor deposition (EVD) and chemical
vapor infiltration (CVI). EVD has been explored for making gas-tight dense solid
electrolyte films on porous substrates. One of the most studied system is yttria-
stabilized zirconia films on porous alumina substrates for solid oxide fuel cell
applications and dense membranes.
In EVD process for growing solid oxide electrolyte films, a porous substrate
separates metal precursors and the oxygen source. Typically chlorides are used as
metal precursors, whereas water vapor, oxygen, or air, or a mixture of them is
used as the source of oxygen. Initially, the two reactants inter-diffuse in the
substrate pores and react with each other only when they concur to deposit the
corresponding solid oxides. When the deposition conditions are appropriately
controlled, the solid deposition can be located at the entrance of the pores on the
side facing metal precursors, and plug the pores. The location of the solid deposit
is mainly dependent on the diffusion rate of the reactants inside the pores as well
as the concentrations of the reactants in the deposition chamber.
Under typical deposition conditions, reactant molecules diffuse inside the pores
by Knudsen diffusion, and the diffusion rate is inversely proportional to the
square root of the molecular weight. Oxygen precursors diffuse much faster than
metal precursors, and consequently, the deposit occurs normally near the entrance
of pores facing the metal precursor chamber. If the solid deposit is an insulator,
the deposition by the CVD process stops when the pores are plugged by the
deposit, since no further direct reaction between the two reactants can occur.
However, for solid electrolytes, particularly ionic–eletronic mixed conductors, the
deposition would proceed further by means of EVD, and the film may grow on
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the surface exposed to the metal precursor vapor. In this process, the oxygen or
water is reduced at the oxygen–film interface, and the oxygen transfers in the
film, as the oxygen vacancies diffuse in the opposite direction, and react with the
metal precursors at the film–metal interface to continuously form metal oxide.
Chemical vapor infiltration (CVI) involves the deposition of solid products onto a
porous medium. The primary focus of CVI is on the filling of voids in porous
graphite and fibrous mats to prepare carbon–carbon composites. Various CVI
techniques have been developed for infiltrating porous substrates with the main
goals to shorten the deposition time and to achieve homogeneous deposition.
Some of these techniques are:
o Isothermal and isobaric infiltration
o Thermal gradient infiltration
o Pressure gradient infiltration
o Forced flow infiltration
o Pulsed infiltration
o Plasma enhanced infiltration
Various hydrocarbons have been used as precursors for CVI. Typical deposition
temperatures range from 1000 to 1300 K. The deposition time ranges from 10 to
70 h. The rather long deposition time is due to the relatively low chemical
reactivity and gas diffusion into the porous media. The gas diffusion gets
progressivley slower with the increase in deposition of solid. To enhance gas
deposition, various techniques have been introduced such as forced flow, thermal
and pressure gradients.
2.5.1.5 Atomic layer deposition
Atomic layer deposition (ALD) is a unique method for depositing thin films. It is
also known as atomic layer epitaxy, atomic layer growth or atomic layer CVD. Its
most distinctive feature is that it has a self-limiting growth: each time only one
molecular layer can grow. Therefore, ALD offers a very good method for
depositing films having thickness in the nanometer range.
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In a typical ALD process, the surface is first activated by chemical reaction, e.g.,
to deposit a titania film by ALD, the substrate is hydroxylated. When the
precursor is introduced in the deposition chamber, the molecules of the precursor
react with the surface species and forms bonds with the substrate. Since the
precursor molecules do not react with each other, a film of only a single
molecular thickness can be deposited. In the next step, the monolayer is activated
again by surface reaction and a layer of the same or a different precursor is
deposited on top of the layer of the previous precursor molecules. A few layers of
the same or different precursors can be deposited by this procedure.
The choice of appropriate precursors is a very important aspect of the ALD
process. A major disadvantage of the ALD method is the slow deposition rate.
The typical deposition rate is 0.2 nm per cycle (i.e., less than half a monolayer per
cycle) with the theoretical maximum of one monolayer per cycle.
Hausmann et al. (2002) have deposited layers of amorphous silicon dioxide and
aluminum oxide nanolaminates at rates of 12 nanometers per cycle, which is
equivalent to more than 32 monolayers per cycle. Vapors of trimethylaluminum
(Me3Al) and tris(t-butoxy)silanol [(ButO3SiOH] were supplied in alternating
pulses to the heated surface on which transparent, smooth films of alumina-doped
silica grew. To test whether the ALD reactions saturate by a self-limiting
mechanism, they deposited films on a silicon wafer in which deep, narrow holes
had previously been itched. After depositing four ALD cycles, the wafer was
cleaved and cross-sectional scanning electron micrographs were recorded.
The micrographs of the cross-sections of the top, middle and bottom parts of a
hole are shown in Fig. 2.5.5. The images show uniform, conformal coating
indicative of an ideal self-limiting ALD reaction.
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Fig. 2.5.5 Cross-sections of holes 7 m deep and 0.1–0.2 m in diameter. Magnified images of the (a) top, (b) middle and (c) bottom parts of a hole coated
conformally with a uniform silica film 46 nm thick made by four ALD cycles (Hausmann et al., 2002) (reproduced by permission from The American
Association for the Advancement of Science, 2002).
2.5.1.6 Electrochemical deposition
Electrochemical deposition is a well-established method for thin film deposition.
It is a special kind of electrolysis resulting in the deposition of solid material on
an electrode. The electrochemical deposition process involves oriented deposition
of charged growth species (e.g., cations) through a solution when an external
electric field is applied, and reduction of the charged growth species at the
deposition surface which also serves as an electrode.
Generally this method is applicable to the electrically conductive materials such
as metals, alloys, semiconductors and conductive polymers. The electrochemical
deposition method is widely used for making metallic coatings, which is known
as electroplating. A somewhat similar method is electrophoretic deposition. It has
been explored for the deposition of ceramic and organoceramic materials from
colloidal dispersions. The material in this case need not be electrically
conductive. The colloid particles are stabilized by electrostatic double layer or
steric forces.
2.5.1.7 Langmuir–Blodgett films
Langmuir–Blodgett films (commonly known as LB films) are layers of
amphiphilic molecules transferred from a gas–liquid interface onto a solid
substrate. In 1920, Irving Langmuir introduced the technique for transferring a
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floating monolayer to a solid surface by slowly raising the hydrophilic solid
through the liquid surface. In 1934, Katharine Blodgett announced the discovery
that sequential transfer of monolayer could be accomplished to build-up
multilayer films. In addition to the vertical deposition mode, Langmuir and
Schaefer (1938) suggested a horizontal deposition method by which the floating
monolayer can be transferred to a hydrophobic solid surface by allowing the
horizontal solid surface to touch the monolayer. Only one monolayer can be
deposited by this method.
The Langmuir film balance can be used for building up highly organized
multilayers. This is accomplished by successively dipping a solid substrate up and
down through the monolayer while simultaneously keeping the surface pressure
constant by a computer controlled feedback system between the electrobalance
measuring the surface pressure and the barrier-moving mechanism. In this way,
multilayer structures of hundreds of layers can be produced. The deposition
process is schematically shown in Fig. 2.5.6.
Fig. 2.5.6 Formation of Langmuir–Blodgett film.
Traditionally the deposition is carried out in the solid phase, where the surface
tension is very low so that the monolayer does not fall apart during the transfer to
the solid substrate. This also ensures the build-up of homogeneous multilayers.
The value of surface pressure, 0s (where 0 is the surface tension of
pure water and is the surface tension of the solution) that gives the best results
depends on the nature of the monolayer. It is usually established empirically.
However, monolayers can seldom be successfully deposited at 10s mN/m. At
40s mN/m, monolayers can collapse and the film-rigidity can pose problems.
When the solid substrate is hydrophilic (e.g., glass or SiO2), the first layer is
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deposited by raising the solid substrate from the liquid subphase through the
monolayer. On the other hand, if the solid substrate is hydrophobic (e.g., silanized
SiO2), the first layer is deposited by lowering the substrate into the subphase
through the monolayer.
The quantity and the quality of the deposited monolayer on a solid sustrate is
measured by the transfer ratio . It is defined as,
decrease in area of Langmuir monolayer
area of the transferred film on the solid substrate (2.5.7)
If all the area lost from the floating monolayer is a result of deposition (rather
than loss through evaporation, dissolution or collapse) then 1 , which indicates
successful deposition, but it may not produce a well-ordered film. During vertical
dipping to deposit monolayers on hydrophilic solid surfaces, both the film and a
thin water layer are actually applied to the solid surface. Under certain conditions,
the substrate is visibly wet immediately after the transfer. This layer of water may
be expelled by either drainage or evaporation, leaving the monolayer on the solid
substrate.
The rate at which the water layer is removed is known as the speed of the
deposition. Langmuir introduced the term zipper angle to refer to the angle
formed by the water meniscus against the solid plate as it is withdrawn. If the
plate emerges wet, the zipper angle is zero. A large zipper angle 6 rad is
observed when the monolayer becomes tightly bound to the solid, expelling water
rapidly in a zipper-like action. The zipper angle is largest when the interaction
between the monolayer and the solid is large, and the term ‘reactive’ has been
used for such depositions. When the deposition of a monolayer takes place with
an intervening hydrous layer the zipper angle is almost zero, and such a
deposition is known as ‘nonreactive’ deposition.
There are three types of LB deposition which are designated as X, Y and Z. When
a solid plate is inserted in and out of a monolayer-covered liquid surface, it is
often found that once the first layer has been deposited, an additional layer is
deposited each time the plate enters or removed from the liquid. This two-way
deposition is called Y-type deposition. This is shown in Fig. 2.5.7.
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Fig. 2.5.7 Langmuir–Blodgett films of X, Y and Z types.
The molecules in the deposited film are arranged head-to-head and tail-to-tail as
shown in the figure. Under certain conditions, a layer is deposited only as the
plate enters the liquid. This is known as X-type deposition in which the molecules
are arranged head-to-tail. The deposition is called Z-type if it only takes place as
the plate is withdrawn from the liquid. Intermediate structures are sometimes
observed for some LB multilayers. They are known as XY-type multilayers.
Surface pressure, dipping speed, properties of the solid substrate and the pH of
the subphase are some of the important factors that govern the LB films.
The commonest and most easily produced multilayers are those from Y-type
deposition. X-ray diffraction measurements have shown that the spacing of the
metal ions incorporated in the film during deposition is nearly twice the single-
layer thickness, confirming the head-to-head, tail-to-tail arrangement. The Y-type
films exhibit high contact angles for water 2 rad (i.e. they are
hydrophobic) which supports the structure shown in the figure that the outer
surface of the films is composed of the hydrophobic chain.
It might be expected from the deposition characteristics that the X-type films
prepared by the one-way mechanism would have a different structure to the Y-
films. Since deposition occurs only on the in-stroke, the outer surface should be
hydrophilic as shown in the figure. However, for some materials (e.g., fatty
acids), it has been found that these films are hydrophobic and give contact angles
similar to those on Y-films. In addition, the spacing between metal ions in
multilayers is the same whether the deposition is X- or Y-type. Therefore, it is
likely that the molecules in these X-films rearrange during or after deposition to
give a structure identical to that of the Y-type films.
NPTEL Chemical Engineering Interfacial Engineering Module 2: Lecture 5
Joint Initiative of IITs and IISc Funded by MHRD 20/22
Only a few examples of the Z-type films have been reported in the literature.
Substituted anthracene derivatives containing short chain carboxylic acid groups
and molecules possessing an -amino carboxylic acid head-group and two amide
groups along the chain have been reported to form Z-type multilayers under
suitable conditions. Arachidic and behenic acid also deposit Z-type films onto
freshly-cleaved mica surfaces when the subphase contains no added electrolyte at
pH < 5.
The Langmuir–Blodgett films have potential applications in optical and electronic
devices, which are similar to the thin films produced by molecular beam epitaxy
(MBE) or chemical vapor deposition (CVD). The organic thin films have very
bright future prospects because their richness of chemical functionality. The LB
films of phospholipids and proteins can be used for the development of
biosensors and biochemical probes.
The potential of the LB films for these applications is sensitive to the details of
their molecular packing. Also, these applications require that the layers have a
defect-free periodic structure. Defects in the LB films have been studied by
conventional surface analysis such as X-ray and electron diffraction. These
techniques, however, are not sensitive to defects such as the pinholes or tears
within the layers. The presence of such defects has restricted the practical
applications of the LB films.
Atomic force microscopy (AFM) has proved to be a nearly-ideal, non-destructive
and high resolution method to investigate the LB film structure and detect defects
at length scales from 0.1 nm to 10 m. A variety of LB films such as lipid and
protein films, polymer films, and specially functionalized molecular films have
been studied by AFM.
NPTEL Chemical Engineering Interfacial Engineering Module 2: Lecture 5
Joint Initiative of IITs and IISc Funded by MHRD 21/22
Exercise
Exercise 2.5.1: Answer the following questions clearly.
(a) Mention three methods for deposition of thin films on solid substrates.
(b) Describe the basic modes of nucleation for the development thin films on a
substrate.
(c) Explain how thin films can be deposited by evaporation.
(d) What is laser ablation?
(e) Explain molecular beam epitaxy.
(f) What is chemical vapor deposition?
(g) Explain atomic layer deposition. How can the speed of this method be enhanced?
(h) What is surface pressure? How is it related to surface tension?
(i) Explain X-, Y- and Z- types of Langmuir–Blodgett films.
(j) Give five applications of the Langmuir–Blodgett films.
Exercise 2.5.2: Explain the difference between (a) evaporation and sputtering, and (b)
chemical vapor deposition and atomic layer deposition.
NPTEL Chemical Engineering Interfacial Engineering Module 2: Lecture 5
Joint Initiative of IITs and IISc Funded by MHRD 22/22
Suggested reading
Textbooks
G. Cao, Nanostructures and Nanomaterials, Imperial College Press, London,
2004, Chapter 5.
P. Ghosh, Colloid and Interface Science, PHI Learning, New Delhi, 2009,
Chapters 8 & 11.
Reference books
S. M. Sze, Semiconductor Devices: Physics and Technology, Wiley, New York,
1985, Chapters 6 & 8.
M. Ohring, The Materials Science of Thin Films, Academic Press, San Diego,
CA, 1992, Chapter 5.
R. J. Stokes and D. F. Evans, Fundamentals of Interfacial Engineering, Wiley-
VCH, New York, 1997, Chapter 10.
Journal articles
B. P. Binks, Adv. Colloid Interface Sci., 34, 343 (1991).
D. Hausmann, J. Becker, S. Wang and R. G. Gordon, Science, 298, 402 (2002).
I. Langmuir, Trans. Faraday Soc., 15, 62 (1920).
I. Langmuir and V. J. Schaefer, J. Am. Chem. Soc., 60, 1351 (1938).
I. Langmuir, Science, 87, 493 (1938).
J. A. Zasadzinski, R. Viswanathan, L. Madsen, J. Garnaes, and D. K. Schwartz,
Science, 263, 1726 (1994).
K. B. Blodgett, J. Am. Chem. Soc., 56, 495 (1934).
K. B. Blodgett, J. Am. Chem. Soc., 57, 1007 (1935).