
applications, e.g., in rotary vacuum lead-throughs, it
is essential that the carrier liquid has a very low vapor
pressure. In other applications, temperature—either
high, low, or both—may be a critical consideration.
Theoretically it should be possible to produce dis-
persions in any liquid thereby being able to tailor the
requirements of viscosity, surface tension, tempera-
ture and oxidative stability, vapor pressure, stability
in hostile environments, etc., to the particular appli-
cation in mind, whether it be technological or bio-
medical (see Ferrofluids: Applications).
In order to achieve a stable colloidal suspension,
and in this context stability refers to situations where
the ferrofluid is subjected to a magnetic field, mag-
netic field gradient, and/or gravitational field, the
magnetic particles generally have to be of approxi-
mately 10 nm in diameter. Particles of this size,
whether they are ferrite or metal, possess a single
magnetic domain only, i.e., the individual particles
are in a permanent state of saturation magnetization.
As a result, a strong long-range magnetostatic at-
traction exists between individual particles which
would inevitably lead to agglomeration of the parti-
cles and subsequent sedimentation unless a means of
achieving a repulsive interaction can be incorporated.
A repulsive mechanism (see Ferrofluids: Introduction)
can be achieved by coating the particles with a sur-
face-active material (surfactant) to produce an en-
tropic repulsion or by incorporating a charge on the
surface of the particles thereby producing an electro-
static repulsion. In the case of liquid–metal carriers,
no such interaction has yet been achieved to produce
a stable suspension.
The various methods by which small magnetic
particles can be prepared and subsequently colloidal-
ly dispersed is described in this article. The prepara-
tion of particles and ferrofluids has been the subject
of numerous patents and research publications. A
comprehensive bibliography of this information can
be found updated in each of Proceedings of the In-
ternational Conference on Magnetic Fluids (ICMF),
under the following authors Zahn and Shenton
(1980), Charles and Rosensweig (1983), Kamiyama
and Rosensweig (1987), Blums et al. (1990), Cabuil
et al. (1993), Bhatnagar and Rosensweig (1995). Re-
views of the subject have been given by Rosensweig
(1979, 1985, 1988), Charles and Popplewell (1980),
Martinet (1983) and Scholten (1978).
1. Preparation of Nano-sized Magnetic Particles
The preparation of nano-sized magnetic particles can
be conveniently considered under two headings; one
dealing with metal particles and the other with ferrites.
1.1 Metal Particles
There are a number of methods of producing small
magnetic metallic particles, the commonest of which
for ferrofluid preparation being the decomposition of
organometallic compounds. In addition, reduction of
solutions of metal salts and other miscellaneous
methods are available. The decomposition of organo-
metallic compounds will be discussed in most detail
as it is the easiest and most versatile method of pro-
ducing metal particles suitable for ferrofluids. In most
of these methods, the presence of a surfactant is cru-
cial. By selecting an appropriate surfactant, it has
been shown (Charles and Wells 1990) to be an effec-
tive method of controlling particle size.
There are two major advantages of using ferroflu-
ids based on metallic particles, such as cobalt and
iron particles. First, these metals have high saturation
magnetizations compared with ferrites and second,
they can be produced easily with very narrow size
distributions. However, there is also a major draw-
back which has restricted their use in most commer-
cial applications and that is their poor resistance to
oxidation and subsequent loss of magnetic properties.
Only by maintaining these fluids in an inert atmos-
phere can these fluids possess an extended lifetime.
(a) Decomposition of organometallic compounds
In the 1960s, several groups of workers (Thomas
1966, Hess and Parker 1966) reported the production
of colloidal-sized cobalt particles by the thermolysis
of dicobalt octa-carbonyl in hydrocarbon solutions
containing polymeric materials. The process is very
simple in that it only involves refluxing a solution of
the carbonyl, usually in toluene, until the reaction is
complete, with the formation of cobalt metal parti-
cles. Thomas (1966) showed that the particles possess
a very narrow size distribution ideal for the produc-
tion of stable colloids. The particles also possess an
f.c.c. structure instead of the b.c.c. structure of bulk
cobalt. The absence of a polymer in the thermolysis
leads to the formation of large particles (4100 nm).
A detailed investigation by Hess and Parker (1966) of
the presence of different copolymers of acrylonitrile-
styrene in the reaction solution showed that the
greater the concentration of polar groups along the
polymer chain, the smaller the size of the particles
formed.
It was Smith (1981) who proposed that the reaction
is polymer-catalyzed, which results in the formation
of a polymer–carbonyl complex which then decom-
poses to form elemental cobalt. Papirer et al. (1983)
showed that the decomposition could also be cataly-
zed by the presence of surfactants. They investigated
the evolution of carbon monoxide during the decom-
position in the presence of diethyl-2-hexyl sodium
sulphosuccinate (Manoxol-OT) and in its absence,
both experiments carried out as a function of tem-
perature. The results were consistent with the pres-
ence of ‘‘micro-reactors’’ and a diffusion mechanism
to control the growth. The higher the temperature
used, the smaller the particles produced. During the
208
Ferrofluids: Preparation and Physical Properties