[0001] The present invention relates to an electroviscous fluid which comprises a dispersion
of wet-method silica particles in an electrically insulating fluid.
[0002] Fluids whose viscosity can be varied by the application of an external voltage have
received attention in the last several years because they may be used for applications
such as drive power transmission, impact absorption, valve- like behavior, and so
forth.
[0003] Such fluids whose viscosity is increased by means of an electric field are generally
called "electroviscous fluids". However, in order to be able to withstand the severe
service in, for example, a clutch, engine mount, or shock absorber, a fluid is required
which undergoes a substantial increase in yield value at low voltages.
[0004] Various types of these fluids have already been proposed, and they are typified by,
for example, dispersions of porous inorganic particles (e. g., silica, alumina, talc)
in an electrically insulating fluid. In each case, through the formation of an electrical
double layer by means of water adsorbed on the particle surfaces, the particles become
oriented in response to an external electric field and the viscosity increases (more
specifically, the fluid is converted into a Bingham fluid, which exhibits a yield
value). This effect is called the "Winslow affect". The following disadvantages have
been associated with silica- based electroviscous fluids: they have limited application
temperatures (approximately 10°C to 80 ° C), they abrade the surrounding machinery,
and the particles form a sediment. Still, since silica is easily obtained on an industrial
basis and is highly susceptible to improvement and manipulation, it has been considered
potentially useful for certain sectors of application, for example, machinery which
would be used in a room temperature environment and which would undergo little abrading
motion. Silica-based electroviscous fluids are disclosed in United States Patent Number
3,047,507 and in Japanese Patent Application Laid Open [Kokai or Unexamined] Number
61-44998 [44,998/86], but in each case these exhibit an impractically weak Winslow
effect.
[0005] The present inventor carried out extensive investigations with a view to solving
the aforementioned problems, and discovered as a result that the aforementioned problems
are substantially reduced by the use of a particular type of wet-method silica in
such electroviscous fluids. The present invention was developed based on this discovery.
[0006] It is an object of the present invention to introduce an electroviscous fluid which
exhibits excellent properties, for example, which undergoes a substantial increase
in yield value at low voltages.
[0007] The object of this invention is also to provide an electroviscous fluid which comprises
a dispersion of wet- method silica particles in an electrically insulating fluid,
but which is further characterized by wet-method silica particles having an average
particle diameter of 10 to 500 micrometers and having a pH not exceeding 6.5 when
tested as a 4 percent aqueous suspension.
[0008] Figure 1 reports the relationship between the shear rate and shear stress for the
electroviscous fluid prepared in Example 1, and Figure 2 reports the relationship
between the shear rate and shear stress for the electroviscous fluid prepared in Comparison
Example 2.
[0009] The present invention utilizes wet-method silica particles which comprise the essential
component for imparting a strong Winslow effect. These wet-method silica particles
are prepared by the production of silica by the addition of acid under wet conditions
to water glass starting material. These wet-method silica particles are an ideal disperse
phase far electroviscous fluids because their surfaces possess a layer of adsorbed
water, which is ideal for the development of the Winslow effect, and because they
have optimal particle sizes. The average particle size should fall within the range
of 10 to 500 micrometers and preferably falls within the range of 50 to 200 micrometers.
When the particle size is less than 10 micrometers, the particles exhibit a large
orientability, but the interparticle forces are small and a satisfactory viscosity
will not be achieved. On the other hand, at particle sizes in excess of 500 micrometers,
the orientability is diminished and the thickening effect is reduced. Moreover, at
such dimensions, the particle size itself begins to pose significant problems. The
particle shape should be as close to truly spherical as possible. When the particles
substantially deviate from spherical, the effective interparticle contact area declines
and the cohesive forces are then weak. With regard to the particle size distribution,
the narrower the better. The particle orientability becomes increasingly uniform as
the particle size distribution becomes narrower, which provides for a more efficient
viscosity rise. Various methods can be devised for the production of silica particles
which have a narrow particle size distribution and are as close to spherical as possible,
but such particles are obtained mainly by devising a suitable drying process. For
example, spray drying methods are ideal.
[0010] In addition to the properties discussed above, the quantity of ion in wet-method
silica particles is also a crucial factor in determining the magnitude of the Winslow
effect. While not limiting the present invention with any particular theory, the inventor
believes that the principal ion present in the silica is the sodium ion, and this
is mainly the excess from the sodium ion used for neutralization of the solid acid
present as an impurity in the water glass starting material. Accordingly, the fluidity
of the silica is governed by the magnitude of this quantity of sodium ion. According
to experiments by the inventor, the presence of free ion in the silica brings about
a retardation in particle orientation. A clear example of this phenomenon is the instability
in shear stress at a constant or variable shear rate that is observed when an electric
field is applied to an electroviscous fluid prepared by the dispersion of free ion-
containing wet-method silica. In the case of free ion- containing particles, this
is thought to be due to an increase in the time required for orientation of the randomly
distributed particles due to the relatively long time associated with ion movement.
The result is the appearance of instability under dynamic conditions. It is for this
reason that wet-method silica particles depleted of free ion (e. g., sodium ion, etc.)
are optimal for the development of a useful Winslow effect. Pure wet-method silica
particles generally exhibit fluidity in the acid region, i. e., acidic silica is ideal.
The fluidity index according to the present invention is characterized by the following:
the pH of the 4 weight percent aqueous suspension of the silica particles must not
exceed 6.5, and more preferably does not exceed 5.5. A useful Winslow effect does
not appear at pH values in excess of 6.5. In order to obtain wet-method silica particles
which have such a fluidity index, the excess sodium ion must be removed to the maximum
possible extent, or, alternatively, a pure water glass which contains only traces
of solid acid must be employed as the starting material. The pH of the wet-method
silica particles are tested in a 4 weight percent aqueous suspension prior to addition
of the particles to the electrically insulating fluid.
[0011] No specific restrictions are placed on the wet-method silica particles employed by
the present invention as long as they satisfy the conditions discussed above. They
may be selected from among commercial wet-method silica particles, for example, Nipsil
AQ-S from Nippon Silica Kogyo Kabushiki Kaisha and its equivalents.
[0012] The electroviscous fluid according to the present invention comprises the dispersion
of wet-method silica particles as described hereinbefore in an electrically insulating
fluid. However, the electrically insulating fluid itself is not particularly restricted
as long as it is a liquid at room temperature and is electrically insulating. Such
electrically insulating fluids are exemplified by mineral oils, dibutyl sebacate,
chlorinated paraffins, fluorine oils, and silicone oils.
[0013] Among the preceding, silicone oils are preferred for their strong electrical insulation,
low temperature- dependent viscosity variation, and so forth. The silicone oils are
exemplified by the fluid diorganopolysiloxanes with the following chemical structure:

wherein each R denotes a monovalent hydrocarbon group as exemplified by alkyl groups
such as methyl, ethyl, and propyl, and aryl groups such as phenyl. It is preferred
that at least 30% of the R groups are methyl groups. Moreover, while the degree of
polymerization of n is not particularly specified, it is preferable that n does not
exceed 1,000 in order to achieve a practical viscosity range. Values not exceeding
100 are even more preferred. Silicone oils with this structure are available in the
form of a large number of commercial products, for example, SH200 from Toray Dow Corning
Silicone Company, Limited.
[0014] Furthermore, among the silicone oils, fluoroalkyl- containing diorganopolysiloxanes
are particularly preferred because they enhance the Winslow effect and inhibit the
particle sedimentation caused by specific gravity differences. These are concretely
expressed by the following structural formula:

wherein R is defined as above, R
2 is a fluoroalkyl group having 10 or fewer carbons, and m and p are integers with
values not exceeding 1,000.
[0015] The structure of the aforementioned C<10 fluoroalkyl group is not particularly specified,
but the 3,3,3-trifluoropropyl group is preferred from the standpoint of ease of synthesis.
In order to obtain a substantial enhancement of the Winslow effect, it will be preferable
for each molecule to contain at least 30 mole percent fluoroalkyl group. Furthermore,
methyl should comprise at least 30% of the R groups from the standpoints of material
acquisition and economics. While the degree of polymerization m is again not particularly
specified, it preferably does not exceed 1,000 in order to achieve a practical viscosity
range. Values not exceeding 100 are even more preferred. The mechanism by which the
fluoroalkyl group enhances the Winslow effect is not clear. While not limiting the
present invention with any particular theory, the inventor believes that a strong
intramolecular dipole is generated by the simultaneous presence in the molecule of
the electronegative fluorine atom and electropositive silicon atom separated by a
suitable distance. Polarization of the double layer is then promoted by contact between
this dipole and the electrical double layer on the wet-method silica particle. Otherwise,
fluorine-containing fluids tend to have larger specific gravities, which results in
a concomitant inhibition of silica particle sedimentation. These fluoroalkyl- containing
diorganopolysiloxanes are commercially available, for example, as FS1265 from Toray
Dow Corning Silicone Company, Limited.
[0016] The electroviscous fluid according to the present invention comprises the dispersion
of wet-method silica particles as described hereinbefore in an electrically insulating
fluid as described hereinbefore. The quantity dispersed should fall within the range
of 0.1 to 50 weight percent and preferably is in the range of 10 to 40 weight percent.
A satisfactory thickening effect is not obtained at less than 0.1 weight percent.
At values exceeding 50 weight percent, the viscosity of the electroviscous fluid is
so substantially increased as to be impractical.
[0017] The electroviscous fluid according to the present invention as described above is
useful as the working oil or functional oil in particular types of machinery, for
example, machinery which will be employed in the vicinity of room temperature and
where there will be little abrading motion.
[0018] The present invention will be explained in greater detail below through the use of
illustrative and comparison examples. In the examples, parts = weight parts, cs =
centistokes, and the viscosity is the value at 25 ° C.
[0019] The electroviscous behavior was measured as follows. The test fluid was placed in
an aluminum cup (interior diameter = 42 millimeters (mm)) into which an aluminum rotor
(diameter = 40 mm, length = 60 mm) was subsequently inserted. The resulting cylindrical
cell was set up vertically, and the cup was linearly accelerated from a shear rate
(D) of zero to 330 s-
1 over 40 seconds. During this period, the torque applied to the rotor was measured
with a torque sensor, and this was converted into the shear stress (S) and the D-versus-S
curve was drawn on an X-Y recorder. In addition, the rotor was electrically grounded
and D-versus-S curves were also recorded while applying a direct-current voltage to
the cup. The intersection of the extrapolation of the linear segment with the S-axis
was designated as the yield value at the particular field strength. The stability
of the shear stress and the sedimentability of the wet-method silica particles were
also examined.
[0020] In the following examples all amounts (parts and percentages) are by weight unless
otherwise indicated.
Example 1
[0021] 15 Parts wet-method silica particles (Nipsil AQ-S from Nippon Silica Kogyo Kabushiki
Kaisha) with an average particle size of 100 micrometers and a pH of 5.5 to 6.5 (pH
was tested in a 4 weight percent aqueous suspension) was added with stirring to 85
parts aliphatic hydrocarbon oil with a viscosity of 100 cs (Rubber Swelling Oil No.
3 from Nippon Sekiyu Kabushiki Kaisha) to afford an electroviscous fluid in the form
of a suspension in which the wet-method silica particles were dispersed in the aliphatic
hydrocarbon oil.
[0022] The electroviscous behavior of this fluid was then measured, and the measurement
results are reported in Table I and Figure 1 below. The three lines in Figure 1 represent
the yield values tested at 0, 1, and 2 KV/mm.
Example 2
[0023] 15 Parts wet-method silica particles (Nipsil AQ-S from Nippon silica Kogyo Kabushiki
Kaisha) with an average particle size of 100 micrometers and pH of 5.5 to 6.5 (pH
was again tested in a 4 weight percent aqueous suspension) was added with stirring
to 85 parts trimethylsiloxy-terminated polydimethylsiloxane (viscosity = 100 cs) to
give an electroviscous fluid in which the wet-method silica was uniformly dispersed
in the polydimethylsiloxane.
[0024] The electroviscous behavior of this fluid was then measured, and the measurement
results are reported in Table I below.
Example 3
[0025] An electroviscous fluid was prepared as in Example 2, but in this case using a trimethylsiloxy-terminated
poly(methyl-3,3,3-trifluoropropyl)siloxane (viscosity = 300 cs) in place of the polydimethylsiloxane
(viscosity = 100 cs) used in Example 2. The properties of this fluid were measured
as in Example 2, and these measurement results are reported in Table I below.
Comparison Example 1
[0026] An electroviscous fluid was prepared as in Example 2, but in this case using wet-method
silica particles (Nipsil L- 300 from Nippon Silica Kogyo Kabushiki Kaisha) with an
average particle size of 4 micrometers and pH = 5.5 To 6.5 (pH again was tested in
a 4 weight percent aqueous suspension) in place of the wet-method silica particles
with average particle size = 100 micrometers used in Example 2. The properties of
this fluid were measured as in Example 2.
[0027] These measurement results are also reported in Table I.
Comparison Example 2
[0028] An electroviscous fluid was produced as in Example 2, but in this case using wet-method
silica particles (Nipsil NA-R from Nippon Silica Kogyo Kabushiki Kaisha) with an average
particle size of 85 micrometers and pH = 10.0 to 11.0 (tested in a 4 weight percent
aqueous suspension) in piece of the wet-method silica with average particle size =
100 micrometers used in Example 2. The electroviscous behavior of this fluid was then
measured, end the results reported below in Table I and Figure 2 were obtained. Again,
the three lines in Figure 2 represent the yield values tested at 0, 1, and 2 KV/mm.

[0029] The Examples delineated hereinabove show the electroviscous fluid according to the
present invention which employs wet-method silica particles with an average particle
size of 10 to 500 micrometers and a pH (hydrogen ion concentration) not exceeding
6.5, wherein the pH of the wet- method silica particles was tested in a 4 weight percent
aqueous suspension prior to addition of the particles to the the electrically insulating
fluid. The fluids of the invention display excellent electroviscous behavior, i.e.,
a substantial increase in yield value at low voltages and an excellent shear stability.