Described herein is an electrophoretic display device.
More particularly, described is an electrophoretic display device containing colorant
particles capable of field-induced charging. The electrophoretic display devices
herein are capable of generating images, including full color images. The electrophoretic
displays herein may be used for any display application, and particularly any display
application where the image displayed may be changed, including, for example, reimageable
paper, electronic books, electronic signage, watch, monitor and/or cell phone displays,
and the like.
One advantage of field-induced charging is that the colored
particles of the display may be made to more rapidly and reliably respond to an
electric field application in displaying an image, potentially with much lower energy
costs. This allows for the electrophoretic display device to be used in displays
requiring rapid image switching capabilities, for example such as monitors.
Electrophoretic displays are well known in the art. An
electrophoretic display generally comprises a suspension of one or two charged pigment
particles colloidally dispersed in a clear or colored liquid of matching specific
gravity and contained in a cell comprising two parallel and transparent conducting
electrode panels. The charged particles are transported between the electrode panels
under the influence of an electric field, and can therefore be made to display an
image through appropriate application of the electric field on the electrodes. The
advantages of electrophoretic displays as a means for providing information and
displaying images has been well appreciated.
Electrophoretic display is thus based on the migration
of charged particles suspended in an insulating fluid under the influence of an
electric field. The particles used in such displays to date have been charged by
adding a charge control agent, which is capable of ionic dissociation, to the dielectric
fluid during preparation of the non-aqueous display dispersion. Examples of charge
control agents used have included bis-(2-ethyl hexyl) sodium sulfosuccinate and
basic barium petronate (BBP). Dissociation of the charge control agent into positive
and negative ionic species in the dielectric fluid results in preferential surface
absorption of ions of one polarity by the particles. The particles therefore become
charged. The resulting dispersion contains a complex mixture of particles including
charged particles, excess free ions and counter-ions. Due to the presence of excess
free ions, such electrophoretic display inks are
characterized by high electrical conductivity. Conductivity has been shown to increase
with concentration of the added charge control agent, and is typically 100-1000
times higher compared to the dielectric fluid. High conductivity of the ink results
in increased power consumption and slower switching speed of the display.
While known electrophoretic display devices, compositions
and processes for displaying images with such known devices are suitable for their
intended purposes, a need remains for an electrophoretic display that remains stable
for long periods of time and that reliably and rapidly displays and/or changes an
image, and in particular a full color image.
BRIEF DESCRIPTION OF THE DRAWINGS
Figure 1 illustrates an embodiment of an electrophoretic
Figures 2-4 illustrate an embodiment wherein a fabric mesh
spacer layer is used to contain and segregate the display medium in the display
layer of the device.
Figure 5 illustrates a process for making the display device
with the fabric mesh display layer.
Figures 6 and 7 illustrate possible diffusion of display
medium within the fabric mesh if the fabric mesh is not compressed.
Figures 8 and 9 illustrate methods for compressing the
Figure 10 illustrates a display device including a color
Figure 11 illustrates a device for charging particles of
a display device.
Figures 12 to 17 illustrate charging characteristics of
particles for use in electrophoretic display devices.
Figures 18 to 21 illustrate methods of controlling the
color displayed by a cell of a display device.
The present invention provides in embodiments:
Display Device Structures
- (1) An electrophoretic display device, comprising a multiplicity of individual
reservoirs containing a display medium between conductive substrates, at least one
of which is transparent, wherein the display medium comprises one or more set of
colored particles in a dielectric fluid, and wherein the multiplicity of individual
reservoirs comprise mesh openings in a fabric mesh whose fibers or filaments segregate
- (2) The electrophoretic display device according to (1), wherein the mesh openings
of the fabric mesh have an average size of from about 5 microns to about 1,000 microns.
- (3) The electrophoretic display device according to (1), wherein the mesh openings
of the fabric mesh have an average size of from about 10 to about 175 microns.
- (4) The electrophoretic display device according to (1), wherein the fabric
mesh comprises a woven fabric mesh.
- (5) The electrophoretic display device according to (1), wherein the fibers
or filaments of the fabric mesh are comprised of polyamide, polyester, polyolefin,
polyetheretherketone, fluorine-containing polymers or combinations thereof
- (6) The electrophoretic display device according to (1), wherein the fabric
mesh has a thickness of from about 5 to about 2,000 µm.
- (7) The electrophoretic display device according to (1), wherein the fabric
mesh has a thickness of from about 25 to about 1,000 µm.
- (8) The electrophoretic display device according to (1), wherein the fabric
mesh is flattened.
- (9) The electrophoretic display device according to (1), wherein the display
medium has an electrical conductivity of about 10-11 to about 10-15
- (10) The electrophoretic display device according to (1), wherein the device
- (11) The electrophoretic display device according to (1), wherein the conductive
substrates comprise ITO coated glass or ITO coated polymer film.
- (12) The electrophoretic display device according to (1), wherein the one or
more set of colored particles comprises polyester emulsion aggregation particles,
styrene-acrylate emuslion aggregation particles or acrylate emulsion aggregation
- (13) The electrophoretic display device according to (12), wherein the one or
more set of particles has an average particle size of from about 0.5 to about 25
µm, an upper geometric standard deviation (GSD) by volume for (D84/D50) is
in the range of from about 1.1 to about 1.25, and an average circularity of about
0.92 to about 0.99.
- (14) The electrophoretic display device according to (1), wherein the display
medium comprises a set of black particles and a set of white particles.
- (15) The electrophoretic display device according to (1), wherein the display
medium comprises a set of cyan particles, a set of yellow particles, a set of magenta
particles and a set of black particles.
- (16) The electrophoretic display device according to (1), wherein the display
medium comprises a set of red particles, a set of green particles and a set of blue
- (17) An electrophoretic display device, comprising a multiplicity of individual
reservoirs containing a display medium between conductive substrates, at least one
of which is transparent, wherein the display medium comprises one or more set of
colored particles in a dielectric fluid, wherein the display medium has an electrical
conductivity of about 10-11 to about 10-15 S/m, and wherein
the multiplicity of individual reservoirs comprise mesh openings in a flattened
fabric mesh whose fibers or filaments segregate the reservoirs.
- (18) A method of forming an electrophoretic display device comprising a multiplicity
of individual reservoirs containing a display medium between conductive substrates,
at least one of which is transparent, wherein the display medium comprises one or
more set of colored particles in a dielectric fluid, and wherein the multiplicity
of individual reservoirs comprise mesh openings in a fabric mesh whose fibers or
filaments segregate the reservoirs, the method comprising
filling mesh openings of the fabric mesh with the display medium; and
locating the fabric mesh containing the display medium between the conductive substrates.
- (19) The method according to (18), wherein the filling comprises contacting
the fabric mesh with the display medium to allow the fabric mesh to wick the display
medium into the mesh openings.
- (20) The method according to (18), wherein the method further comprises, prior
to filling the mesh openings with the display medium, flattening the fabric mesh.
- (21) The method according to (20), wherein the flattening comprises applying
pressure to the fabric, applying heat to the fabric, or both.
- (22) The method according to (18), wherein the method further comprises, after
locating the fabric mesh containing the display medium between the conductive substrates,
sliding at least one of the conductive substrates onto or upon the fabric mesh to
remove air bubbles.
Structures of electrophoretic display devices in which
a display medium may be included will first be described. Use of the electrophoretic
display mediums described herein is not, however, necessarily limited to these embodiments,
and any other suitable design for an electrophoretic display device may be used
without limitation. As an example of a suitable electrophoretic display device design
not specifically described herein that may nevertheless be used with the present
U.S. Patent No. 6,788,449
As illustrated in Figure 1, an embodiment of an electrophoretic
display device comprising two conductive substrates 10 and 20 disposed oppositely
of each other, with an electrophoretic or display layer 40 therebetween. The display
layer may have a thickness of from, for example, about 5 to about 1,000 µm,
such as from about 10 to about 500 µm or from about 20 to about 350 µm.
Layer 40 may be comprised of a layer that includes spacers
therein, which spacers define a multiplicity of individual reservoirs that each
contain the display medium (30, 31 and 32) comprised of fluid and colored particles.
A multiplicity refers to, for example, from about 2 to about 100,000,000, or potentially
more, such as from about 100 to about 50,000,000 or from about 1,000 to about 1,000,000.
Thus, for example, if each of the multiplicity of reservoirs is about 100 microns
across, a square of 1,000 x 1,000 reservoirs (or about a 4 inch x 4 inch display)
would have about 1,000,000 total reservoirs. In this regard, each reservoir may
be thought to correspond to a pixel of the device. Reservoir refers to, for example,
any unit containing, or capable of containing, display medium therein, and includes,
for example, units separated by a spacer device, pockets, cavities or bubbles formed
in a single sheet or between two sheets, capsules or microcapsules is a sheet or
layer, and the like.
In the Figure 1 embodiment, the particles are shown to
include a set of black particles and a set of white particles. However, as will
be discussed more fully below, the particles may be comprised of at least one or
multiple differently colored particle sets, for example from 1 to about 10 particles
sets, such as from 1 to about 6 particle sets or from about 2 to about 4 particle
As the conductive substrates of the electrophoretic display
device, any suitable materials may be used without limitation, for example including
materials presently known and used or that may be used in the future in the art.
At least one of the conductive substrates, in particular at least the top conductive
substrate through which the images formed by the device may be viewed, should be
transparent in order to enable such viewing. Both substrates may be transparent,
if desired. The bottom or back substrate need not be transparent, and may instead
be, for example, a light reflecting or light absorbing material. As suitable materials
that may be used, mention may be made of conductive polymer films, for example polymer
films coated with a transparent conductive material such as indium tin oxide (ITO),
such as polyethylene terephthalate (PET) films, for example MYLAR (Du Pont), polyethylene
napthalate (PEN) films, polyethersulfone (PES) films and the like, conductive glass
films, such as ITO coated glass, and conductive thin metals. For transparency, ITO
coated polymer films and glass are suitable. The substrates may either be flexible
The substrates that sandwich the spacer layer therebetween
may have a length and width corresponding to the overall length and width of the
electrophoretic display device. The substrates thus may be continuous, unitary films
that are not present as just separated pieces over just individual reservoirs of
the display device, although a plurality of segregated substrates may also be used.
The substrates may be made to be as thin as possible while still maintaining appropriate
conductive properties and structural integrity. For example, the substrates may
have a height, or thickness, of from about 10 microns to about 500 microns, such
as from about 10 to about 250 microns or from about 20 to about 100 microns.
Between the conductive substrates are contained a multiplicity
of individual reservoirs (30, 31, 32), each filled with a display medium described
more fully below. Each of the individual reservoirs defines one container and/or
cell of the electrophoretic display device.
In embodiments, spacers may be used to keep the individual
reservoirs separate from one another. Any suitable spacer design may be used. For
example, the spacer may be of the type described in
U.S. Patent Publication No. 2003-0132925 A1
. The width and/or diameter of the individual reservoirs may be from, for
example, about 5 microns to about 400 microns, such as from about 5 to about 200
microns or from about 5 to about 50 microns. Also, the spacer layer 40 may be comprised
of more than one layer/sheet, such as from two to about eight layers or from about
two to about four layers, for example when pocket sheets having differently colored
display mediums therein are stacked together.
The display medium to be used within the reservoirs contains
particles of a size smaller than the reservoir width/diameter in order to function.
Where the spacer layer is comprised of a multiplicity of
individual reservoirs, a solid portion of the spacer separating the multiplicity
of reservoirs, that is, the spacing or partition between individual reservoirs of
the spacer layer, are desirably as thin as possible. Preferred spacing/partition
thicknesses are on the order of, for example, about 10 microns to about 100 microns,
such as from about 10 microns to about 75 microns or from about 15 to about 50 microns.
The display device may have any suitable overall length
and width as desired. The electrophoretic display device may also be made to have
any desired height, although a total height of from about 30 to about 1,000 microns,
such as from about 30 to about 400 microns or from about 50 to about 300 microns,
may be used in terms of size and ease of use of the device.
In forming the electrophoretic display device, the reservoirs,
for example pockets, of the spacer layer are filled with the display medium and
the spacer layer is located over a first, or bottom, conductive substrate. The filling
of the reservoirs and location of the spacer over the substrate may be done in any
suitable order. In embodiments, the spacer layer may be physically attached to the
first conductive substrate or intermediate films, which may be done by any suitable
method. Adhesive may be used for convenience, although other attachment methods
such as sputtering deposition of the conductive film may also be used. Once the
reservoirs are filled with display medium and the spacer is located over the first
conductive substrate, the second, or top, conductive substrate, is located over
the spacer layer. In non-pocket reservoirs and/or in displays not including any
intermediate layers, this may act to seal the reservoirs. The first and second substrates
may also be located in association with the spacer layer in reverse order, if desired,
and may also be associated with the spacer layer at the same time, for example where
the spacer layer comprises a sheet of individually enclosed pockets filled with
display medium. Again, the locating of the second conductive substrate in association
with the spacer layer may be done by attachment, if desired, by any suitable means,
including gluing with an adhesive. Additional intermediate layers may be included
between the spacer laver and conductive substrates as desired, and thus the location
and/or attachment as described above need not be a direct attachment or association
of the spacer to the conductive substrates.
In embodiments, the display device may be made to be flexible.
In such embodiments, the conductive substrates are each comprised of a flexible
material such as polymeric film such as MYLAR, polyethylene napthalate (PEN), polyethersulfone
(PES) and the like coated with a conductive material such as ITO and the like.
In embodiments, the display medium is segregated into individual
reservoirs in the display layer of the device through the use of a spacer comprised
of a fabric mesh material. Thus, in these embodiments, the display device includes
a display layer comprised of a fabric mesh defining a multiplicity of reservoirs,
wherein the display medium is contained within the reservoirs defined by the mesh
openings of the mesh fabric, the display layer being located between the conductive
substrates or electrodes of the device. A fabric mesh spacer 50 is shown in Figures
2-4. In Figures 3 and 4, the display medium is shown as particles in reservoirs
(mesh openings) 52 of the woven fabric mesh spacer. As shown in Figures 3 and 4,
the display medium is segregated and held in each mesh opening by the fibers or
filaments 56 of the fabric mesh. The display layer having the fabric mesh is sandwiched
between conductive substrates 57.
The width and/or length of the individual reservoirs of
the fabric mesh, that is, the size of the mesh openings in the fabric that comprise
and define the reservoirs, may be from, for example, about 5 microns to about 1,000
microns, such as from about 10 to about 300 microns or from about 10 to about 175
microns. Obviously, the display medium to be used within the reservoirs must contain
particles of a size smaller than the mesh opening width/length in order for the
display to function.
As the fabric mesh, any suitable fabric mesh may be used.
The fabric mesh may be woven or non-woven, although woven fabric meshes may be more
desirable or more readily commercially available. The fibers or filaments comprising
the fabric mesh may take any suitable form. For example, the fibers or filaments
may be multifilaments, monofilaments, sheath-core filaments, and the like. Woven
monofilament mesh fabrics may desirably be used.
The fibers or filaments of the fabric mesh may be made
of any suitable material. For example, the fibers or filaments may be polyamide
such as nylon, for example polyamide 6 or polyamide 6,6 (for example, commercially
available as NITEX from Sefar America), polyester such as polyethylene terephthalate
(for example, commercially available as PETEX from Sefar America), polyolefin such
as polyethylene or polypropylene (for example, commercially available as PROPYLTEX
from Sefar America, or polypropylene mesh from INTERNET©) polyetheretherketone
(PEEK) (for example, commercially available as PEAKTEX from Sefar America), fluorine-containing
polymers such as polyvinylidene fluoride, polytetrafluoroethylene or ethylene-tetrafluoroethylene
(for example, commercially available as FLUORTEX from Sefar America), combinations
thereof, and the like. Additional commercial fabric mesh materials include NYTAL
and MEDIFAB, polyamide and polyethylene terephthalate fabrics available from Sefar
The fabric mesh may have a thickness of from about 5 to
about 2,000 µm, with thinner fabric mesh materials being more suitable for
use in preparing flexible display devices. For example, the fabric mesh may have
a thickness of from about 10 to about 1,500 µm or from about 25 to about 1,000
µm. The overall device including the fabric mesh spacer layer may have a thickness
of from about 20 µm to about 2,000 µm, for example from about 20 to about
1,500 µm or from about 25 to about 1,000 µm.
The mesh openings defining the reservoirs of the fabric
mesh spacer are filled with display medium, and the display medium-containing film
is sandwiched between the conductive substrates in forming the display device. Any
possible method of filling the mesh openings of the fabric mesh with the display
medium may be used. For example, the fabric mesh may be located on or over one of
the conductive substrates, or an intermediate film, and the display medium then
applied to the fabric mesh to be held in the mesh openings. The top conductive substrate
may then be applied.
Figure 5 illustrates a desirable process for making the
display device 89 with the fabric mesh display layer. In this process, the fabric
mesh 50 is first exposed, for example by dipping, coating and the like, to the display
medium. As a result of, among other factors, the relatively high viscosity of the
display medium and the relatively small mesh openings, the fabric mesh is able to
wick the display medium and hold it within the mesh openings. Display medium-containing
fabric mesh 51 is achieved. The wet mesh is then located between the two conductive
substrates 57, and sandwiched therebetween. Capillary action is able to hold the
device together. Moreover, it may be desirable to slide the top or bottom layers
of the display device on the wet mesh after locating the wet fabric mesh between
the conductive substrates or intermediate films, the effect being to remove any
trapped air bubbles. The wicking action of the fabric mesh enables more rapid preparation
of the display layer, and for example permitting the use of roll-to-roll manufacturing
of the display layer, particularly as compared to other techniques such as forming
patterned polymer grids or forming microcapsules trapped The edges of the conductive
substrates may be sealed to prevent any display medium from leaking therefrom. Any
suitable sealing material may be used, for example including epoxies and the like.
Another advantage associated with the use of fabric mesh
spacers is that the mesh lines are relatively small, and thus less area is occupied
by the segregating fibers or filaments of the fabric mesh. This enables the display
device to potentially have a greater contrast, that is, a greater number of reservoirs
or cells per unit area.
In embodiments, it may be desirable to subject the fabric
mesh to a flattening or compressing procedure prior to filling the mesh openings
with the display medium. For example, as shown in Figures 6 and 7, where a woven
fabric mesh is used such as polypropylene mesh, display medium may diffuse from
one mesh opening to adjacent openings, thereby potentially resulting in fewer particles
in some cells or reservoirs 54 and too many particles in other cells or reservoirs
58. This is because of the slightly open nature of the weave. When such diffusion
occurs, the effect is a poor display quality.
To address this potential issue, the fabric mesh may be
flattened so that the extent of openness between reservoirs, for example the extent
of openness in the weave, of the fabric mesh is substantially reduced.
To flatten or compress the fabric mesh, any suitable method
may be used, for example any method in which uniaxial pressure is applied to the
fabric mesh to effect the compression thereof Example methods of flattening the
fabric mesh include, for example, pressure applications, heating applications, or
both, such as pressing the fabric mesh in any suitable press, with or without heating,
feeding the fabric mesh between compression applying, or lamination, rollers, with
or without heating, heating to just below a melting point of the fabric mesh material
so as to tackify the fabric mesh, possibly also with the application of pressure
as above, heating to above the melting point of the fabric mesh, possibly also with
the application of pressure as above, and the like. For example, for a polypropylene
mesh, temperatures ranging from about 150°C to about 170°C and/or pressures
ranging from about 1 psi to about 15 psi, for times ranging from about 1 to about
60 minutes, may be used in creating flattened mesh.
Figures 8 and 9 illustrate two possible methods for flattening
the fabric mesh. In Figure 8, uniaxial pressure is applied to the fabric mesh 50
by locating the fabric mesh upon a suitable substrate 62, for example metal and
the like, and applying a press 63 in a substantially uniform manner in a uniaxial
direction that is substantially perpendicular to a planar surface side of the fabric
mesh to press the fabric mesh. The compression may be applied with or without heating
as discussed above. Achieved after pressing is flattened fabric mesh 65.
In Figure 9, the pressure is applied by two opposing lamination
rollers 66 and 67, again with or without heating as discussed above. For application
of a suitable pressure and/or temperature for a suitable time, a suitable feed rate
through the rollers may be about the same as a feed rate of a sheet of laminated
plastic passed through a commercial office laminator device, for example on the
order of about 0.5 to about 4 feet/minute. Flattened fabric mesh 65 is achieved
after pressing via the rollers.
The substantially continuous walls of the flattened fabric
mesh form a vertical barrier that substantially prevents any diffusion of the display
medium between reservoirs of the fabric mesh.
In embodiments, the conductive substrates may be non-flexible,
such as glass, for example ITO coated glass, and the like, or flexible, such as
a polymer film, for example ITO coated MYLAR, and the like.
ww In embodiments, the display device may also be made
to include an absorptive backplane, for example a light absorptive backplane. Very
thin display devices with substantially clear substrates such as ITO coated glass
or ITO coated polymer such as MYLAR may exhibit low optical density, and a washed
out appearance with low color saturation. A highly absorptive backplane may reduce
the light transmission through the device, thereby eliminating the washed out appearance
of the display. The contrast is greater, and the color saturation appears higher.
The absorptive backplane may desirably have a black color.
This may be achieved by any suitable method. For example, a black colored film or
paint may be added onto the back of a transparent substrate. The absorptive backplane
may be applied either before or after formation of the device, for example before
formation of a grid pattern on the substrate and/or assembly of the film into a
display device, or after assembly of the device but before electrode attachment.
Also, the coloring agent imparting the dark color such as black may be incorporated
directly into the conductive substrate layer itself, such that the conductive substrate
acts as both the conductive layer and the absorptive backplane.
The display device may also include a color filter. The
color filter may be placed over the display layer, over the top conductive substrate,
or between the top conductive substrate and the display layer(s) having the display
medium therein. A color filter is useful when the display device otherwise has a
two color capability, for example because it is comprised of a white colored particle
set in a colored, for example black, fluid, or because it is comprised of two differently
colored particles in a display fluid, for example black and white particles. The
color filter can impart fuller color capabilities to such display devices, for example
increasing the two color capability to eight total colors as described below.
A multiple color display thus may be achieved by placing
filters of different colors, for example red, green, blue, yellow, cyan or magenta,
etc., over the viewing side of individual cells. A color filter of the colors red,
green, and blue can be advantageously used. Moreover, the color filter may comprise
stripes of the different colors. The color filter is desirably comprised of transparent
materials such as transparent polymer films that are tinted with colorant such as
pigments, dyes or mixtures of pigments and dyes to have the appropriate color yet
remain substantially transparent. Thus, the colorant may be present in the transparent
material of the color filter in an amount of from about 0.1 % to about 10% by weight,
for example from about 0.5% to about 5% by weight.
By placing the color filter over a cell of the display
device that includes an appropriate number of color switchable reservoirs therein,
multiple colors may be achieved. For example, if each color of the color filter
has a switchable portion of the cell associated therewith so as to be independently
driven, multiple colors may be achieved. In other words, each colored section of
the color filter is associated with an underlying section of the display layer that
may be independently addressed via the conductive substrate so that control of each
section of the display layer may be made to control the color displayed, as explained
more fully below.
In embodiments, the color filter layer includes a multiplicity
of color filter sections, each comprised of the different colors of the color filter.
In this manner, a larger, full color display may be made by the device. In these
embodiments, the color filter sections may each correspond to a pixel of the display.
As such, the color filter layer may include from, for example, about 2 to about
100,000,000, or potentially more, such as from about 100 to about 50,000,000 or
from about 1,000 to about 10,000,000, color filter sections.
Figure 16 illustrates a display device 80 including a display
layer 82 with individual cells 84 of black and white particles therein. A color
filter 85 is placed over the cell, the color filter including a red 86, green 87
and blue 88 stripe. In this manner, eight colors may be displayed. For example,
red may be displayed by driving the cell to have white particles 83 display below
the red stripe, and black 81 below the blue and green. Green and blue may be similarly
displayed by having white particles displayed under these respective stripes of
the color filter with black under the other two color stripes. Yellow may be derived
by having black appear under the blue, and white under both the red and green. Cyan
can be derived with white particles displayed under the green and blue stripes,
with black under the red. Magenta may be displayed with white under the red and
blue stripes of the color filter, and black under the green. White is displayed
with white particles under all stripes of the color filter, and black is displayed
with black under all of the color filters. Other colors may of course be shown if
different color filter colors are selected.
Next, various embodiments of the electrophoretic display
mediums for use in the electrophoretic display device are described.
In embodiments, the display medium is comprised of at least
one fluid and at least one, for example at least two, such as from two to ten or
from two to four, set(s) of colored particles dispersed in the fluid.
In an embodiment herein, the display medium comprises one
or more sets of colored particles dispersed in a fluid system. The fluid may be
either clear/transparent, or it may exhibit a visible color, for example a different,
contrasting color from the color(s) exhibited by the sets of particles dispersed
therein. A colored fluid is typically used in a display employing a single set of
colored particles, for example white particles, with the color of the fluid being
a contrasting color other than white.
In embodiments, the fluid of the display medium and the
set(s) of particles therein may have densities that are substantially matched, for
example wherein the densities of these materials are within about 10% of each other,
or more specifically within 5% of each other or within 2% of each other. In other
embodiments, the fluid may comprise two immiscible fluids having different densities
such that the first immiscible fluid having a density less than that of the second
immiscible fluid rests on top of the second immiscible fluid, and each of the sets
of particles has a density in between the densities of the two immiscible fluids
such that the particles rest at an interface between the two immiscible fluids.
The fluid may comprise from about 10% to about 95% by weight
of the display medium, for example from about 30% to about 90% or from about 40%
to about 80% by weight of the display medium.
The fluid may be comprised of any suitable fluid known
in the art for use in electrophoretic displays. Fluid refers to, for example, a
material in a liquid state, and is not a gas or air. Of course, air or any other
gas may also be present in the reservoirs of the display device, but the fluid of
the display medium refers to a fluid in a liquid state. The choice of fluid may
be based on concerns of chemical inertness, density matching to the particles to
be suspended therein and/or chemical compatibility with the particles. In embodiments,
the suspending fluid may have a low dielectric constant (for example, about 4 or
less, such as about 0.5 to about 2). The viscosity of the fluid may be relatively
low at the temperatures of operation in order to permit the particles to move therein,
for example under the influence of an electrical field. In embodiments, the fluid
may have a kinematic viscosity in the range of about 0.25 centistokes to about 10
centistokes, for example from about 0.5 centistokes to about 5 centistokes or from
about 1 centistoke to about 2 centistokes, at about room temperature (about 23°C
to about 27°C). The fluid may be dielectric and substantially free of ions.
The fluid also may have minimum solvent action on the colored particles therein,
and a specific gravity substantially equal to the colored particles, for example
within about 10% of each other. Additionally, the fluid may be chosen to be a poor
solvent for some polymers, which is advantageous for use in the fabrication of particles
because it increases the range of polymeric materials useful in fabricating particles.
The fluid may include therein a thermally reversible gelling
agent having a melting point temperature of at least about 35°C, for example
as described in co-pending Application
Organic solvents such as halogenated organic solvents,
saturated linear or branched hydrocarbons, silicone oils, and low molecular weight
halogen-containing polymers are a few suitable types of fluids that may be used.
Organic solvents may include, for example, epoxides such as, for example, decane
epoxide and dodecane epoxide, vinyl ethers such as, for example, cyclohexyl vinyl
ether, and aromatic hydrocarbons such as, for example, toluene and naphthalene.
Halogenated organic solvents may include, for example, tetrafluorodibromoethylene,
tetrachloroethylene, trifluorochloroethylene, 1,2,4-trichlorobenzene, carbon tetrachloride,
mixtures thereof and the like. These materials may have high densities. Hydrocarbons
may include, for example, decane, dodecane, tetradecane, xylene, toluene, hexane,
cyclohexane, benzene, the aliphatic hydrocarbons in the ISOPAR™ (Exxon),
NORPAR™ (a series of normal paraffinic liquids from Exxon), SHELL-SOL™
(Shell), and SOL-TROL™ (Shell) series, naphtha, and other petroleum solvents.
These materials may have low densities. Examples of silicone oils include octamethyl
cyclosiloxane and higher molecular weight cyclic siloxanes, poly(methyl phenyl siloxane),
hexamethyldisiloxane and polydimethylsiloxane. These materials may have low densities.
Low molecular weight halogen-containing polymers may include, for example, poly(chlorotrifluoroethylene)
polymer or KRYTOX™ polymers (Dupont).
Typically, hydrocarbon fluids such as ISOPAR M are used
for electrophoretic ink applications due to their low cost, good dielectric strength,
low volatility, and nonreactivity.
In embodiments, the aliphatic hydrocarbons may cause degradation
of performance, for example when non-crosslinked emulsion aggregation particles
are used as the colored particles of the display medium and/or when the colored
particles are imparted with a charge by treatment with a surface coating that can
be desorbed from the particle surface in the presence of an aliphatic hydrocarbon.
Thus, it may be desirable to use as the fluid of the display medium a nonswelling
fluid such as a silicone fluid. A commercially available silicone fluid includes
DOW 200, a polydimethylsiloxane polymer available from Dow Corning. Other examples
of suitable silicone fluids include polydimethylsiloxane fluids available from Gelest
Corporation such as trimethylsiloxy terminated fluids DMS-T00, DMS-TO1, DMS-T01.5,
DMS-T02, DMS-T03, DMS-T05, DMS-T07, DMS-T11; cyclomethicones such as SI06700.0,
SID2650.0, SID4625.0 (also known as D4, D5, and D6 fluids, respectively); phenylmethylsiloxanes
such as PMM-0011, PDM-7040; fluorosilicones such as SIB 1816.0; polydiethylsiloxanes
such as DES-T03, DES-T11; branched and low viscosity phenyltris(trimethylsiloxy)silane
fluids such as SIP6827.0, phenethyltris(trimethylsiloxy)silane fluids such as SIP6722.8,
and the like.
If colored, the fluid may be colored by any suitable means
in the art, including through the inclusion of suitable dispersible colorants such
as dyes and/or dispersible pigments therein.
In embodiments, the fluid is substantially free of charge
control additives and other ionic species that may affect the charging behavior
of the display medium and/or the particles dispersed therein. However, in other
embodiments, the fluid may contain additives such as surface modifiers to modify
the surface energy or charge of the particles and such as charge control agents,
dispersants, and/or surfactants.
The display medium may be comprised of two immiscible liquids.
Such a two-layer fluid system may be achieved using two fluids with differing densities
and that are immiscible with each other. For example, 3M's fluoroether and Exxon's
ISOPAR™ are a suitable combination of immiscible fluids. Fluoroether, being
denser, rests on the bottom, while ISOPAR™, being less dense, rests on top.
The particles of the display medium may have a density that is in between the densities
of the two immiscible liquids so that they rest at the interface between the two
Advantages of using two immiscible liquids may include
that the rest position of the particles is at the interface of the two immiscible
liquids (which may be near the middle portion of the reservoir) rather than at the
bottom of the reservoir in which the display liquid is contained. This may avoid
potential adhesion between the particles and the reservoir bottom. In addition,
the switching time may be made faster because the particles only need to travel
a portion of the distance of the reservoir in switching positions to display a different
color to a viewer, and the particles rested at the interface may break loose more
easily compared to particles resting at the bottom, which may increase particle
stability and product life.
Various embodiments of particle sets to be dispersed in
the fluid of the display medium are next described.
In embodiments, the display medium includes at least one
set of particles exhibiting substantially the same color. The display medium may
be comprised of one set of colored particles, including at least two, such as from
two to ten or from two to four, sets of differently colored particles dispersed
in the fluid. Color refers to, for example, the overall absorption characteristic
within the range of wavelengths of the electromagnetic spectrum. Substantially the
same color herein refers to, for example, particles exhibiting substantially the
same hue and contrast (darkness/lightness) as other particles in the set. Colored
particles of different sets of particles in the display medium exhibit a color,
that is, an absorption characteristic, different from each other. For example, if
a first set of particles exhibits a yellow color, then a second differently colored
set of particles will exhibit a different shade (hue and/or contrast) of yellow
or a different color altogether, for example such as cyan or magenta.
A display medium may include two sets of differently colored
particles, for example black particles and white particles. In embodiments, the
display medium comprises at least three differently colored sets of particles. As
examples, the three sets of colored particles may comprise the three subtractive
primary colors yellow, cyan and magenta, or may comprise red, blue and green. An
example display medium containing four sets of differently colored particles may
comprise yellow, cyan, magenta and black. Additional differently colored sets of
particles, for example for highlight coloring, may be included as additional sets
of colored particles in any embodiment described herein.
Each set of same colored particles in the display medium
may comprise from about 5% to about 50% by weight, for example from about 5% to
about 40% or from about 5% to about 30% by weight, of the display medium.
In embodiments, described is a low electrical conductivity
electrophoretic display medium, for example having a conductivity on the order of
about 10-11 to about 10-15 S/m, such as from about 10-12
to about 10-14 S/m or from about 10-12 to about 10-13
S/m. The conductivity of the display medium is thus comparable to that of the dielectric
fluid. The particles of the display medium may become charged by the application
of a high electric field thereto, which may also be referred to as field-induced
or in situ charging, in which particle charging is dependent on, for example, the
field strength and the charging time (or number of charging cycles). Following charging,
the particles may have a charge (charge to mass ratio) on the order of microcoulombs
(µC) per gram (that is, on the order of 10-6 C/g), such as from
about ±0.1 to about ±20 µC/g, from about ±0.2 to about ±10
µC/g or from about ±0.3 to about ±5 µC/g.
In prior display mediums, the particles were typically
charged by adding a charge control agent, which is capable of ionic dissociation,
to the fluid during preparation of the non-aqueous ink dispersion. Dissociation
of the charge control agent into positive and negative ionic species in the dielectric
fluid results in preferential surface absorption of ions of one polarity by the
particles, and the particles therefore become charged. The resulting dispersion
contains a complex mixture of particles including charged particles, excess free
ions and counter-ions. Due to the presence of excess free ions, the electrophoretic
ink is also characterized by high electrical conductivity, which increases with
concentration of the added charge control agent and is typically 100-1000 times
higher compared with the dielectric fluid. High conductivity of the ink results
in increased power consumption and may result in slower switching speed of the display.
Moreover, the presence of excess free ions in the display medium makes it possible
for many of the particles to switch to a wrong sign/polarity during collisions between
particles in use, which may degrade image quality and response time.
The display medium, including the fluid and particle sets
therein, of embodiments herein may thus be made to be substantially free of charge
control additives and similar excess ionic species affecting the charging characteristics
and/or conductivity of the display medium. Substantially free of ions herein refers,
for example, to the display medium being free of ionic species to the extent that
the aforementioned conductivity values may be achieved. As a result, the display
medium herein is able to exhibit the aforementioned low conductivity properties.
As a result of the desired absence of charge control additives
in the display medium, the particles of the sets of particles of the display medium
need to be made to include a capability of exhibiting the low charging property
by other methods. Such may be accomplished, for example, by the formation of the
particles in the presence of a surfactant and/or water, wherein small amounts of
these materials may be incorporated into the particles during formation. Other components
that could impart the charge to the particles include polymerization initiators
such as APS (ammonium persulfate), chain transfer agents such as DDT (dodecylthiol),
or acidic/basic functional groups in the polymer backbone that may be exposed or
partially exposed on the particle surface. These materials may act as charge species
in the particles, imparting an almost negligible charge at time zero but that which
enables the particles to be charged, for example through application of a high electric
field as will be described more fully below, to the low charge values described
above. These materials are part of the particles and substantially do not become
dissociated in the display medium, thereby enabling the display medium to maintain
the low conductivity. Moreover, unlike prior systems requiring the presence of ionic
species in the medium that permit the display to degrade in performance over time,
for example through the generation of wrong sign particles and/or loss of sufficient
ionic species in the medium, the particles herein do not generate ionic species
and do not require the presence of ionic species for charging, and thus are not
subject to such degradation risks.
As the particles of the display medium, any particle made
by any suitable process may be used, so long as the particles are capable of exhibiting
the low charge property discussed above. Thus, particles made by both physical grinding
methods, in which the material of the particles is formed as a mass that is then
crushed and ground to the desired average particle size, and chemical build-up methods,
in which the particles are grown individually within a reaction medium to the desired
average particle size, both of which types of methods are well known in the toner
art, may be used. The particles may be made to have an average size of from, for
example, about 5 nm to about 100 µm, such as from about 10 nm to about 50 µm
or from about 0.5 µm to about 25 µm. The particles typically have a size
less than the size of the reservoirs of the display device in which the display
medium will be contained so that the particles are free to move within the reservoirs.
The particles may be neat pigments, dyed (laked) pigments,
pigment/polymer composites, dyed or pigmented agglomerated polymer particles and
the like. As the colorant of the particles, dyes, pigment, mixtures of dyes, mixtures
of pigments or mixtures of dyes and pigments may be used. Particles and/or colorant
of particles may also include laked, or dyed, pigments, in which a dye is precipitated
on the particles or the particles are stained with a dye such as metal salts of
readily soluble anionic dyes, for example dyes of azo, triphenylmethane or anthraquinone
structure containing one or more sulphonic or carboxylic acid groupings precipitated
by a calcium, barium or aluminum salt.
Typical manufacturing techniques for the above particles
are drawn from the liquid toner and other arts and include ball milling, attrition,
jet milling, and the like. A pigmented polymer particle may be made by, for example,
compounding a pigment in the polymer. The composite material is then (wet or dry)
ground to a desired size. It may then optionally be added to a carrier liquid and
milled under high shear for several hours to a final particle size and/or size distribution.
Chemical processes that may be used in forming the particles
include, for example, emulsion aggregation, dispersion polymerization, mini- or
micro-emulsion polymerization, suspension polymerization, precipitation, phase separation,
solvent evaporation, in situ polymerization, or any process of microencapsulation.
Polymers that may be used for the pigmented particles include,
for example, polystyrene, polyethylene, polypropylene, phenolic resins, ethylene-vinyl
acetate copolymers, polyesters, polyacrylates, polymethacrylates, ethylene acrylic
acid or methacrylic acid copolymers, acrylic copolymers and terpolymers and the
like. Specific example include, for example, polyethylene, polypropylene, polymethylmethacrylate,
polyisobutylmethacrylate, polystyrene, polybutadiene, polyisoprene, polyisobutylene,
polylauryl methacrylate, polystearyl methacrylate, polyisobornyl methacrylate, poly-t-butyl
methacrylate, polyethyl methacrylate, polymethyl acrylate, polyethyl acrylate, polyacrylonitrile,
and copolymers of two or more of these materials.
While pigment/polymer composite particles, for example
composite particles created by a physical-chemical process such as grinding/attrition
of pigment/polymer or by surface treatment/grafting of stabilizing polymeric groups
on the surface, may be used herein, such composite particles may have polydisperse
particles that exhibit variable charging characteristics. Thus, in embodiments,
the particles for the display medium are emulsion aggregation particles, for example
including polyester resin based emulsion aggregation particles and styrene-acrylate
or acrylate resin based emulsion aggregation particles. Such particles are chemically
grown and tend to be substantially monodisperse in size and substantially spherical
in shape. Another advantage to emulsion aggregation particles is that the particle
surface is substantially completely passivated by the binder resin, which may eliminate
the contribution of the colorant, such as pigment, to the particle charge.
Examples of suitable polyester resins for the emulsion
aggregation particles include polyethylene terephthalate, polypropylene terephthalate,
polybutylene terephthalate, polypentylene terephthalate, polyhexalene terephthalate,
polyheptadene terephthalate, polyoctalene terephthalate, polyethylene sebacate,
polypropylene sebacate, polybutylene sebacate, polyethylene adipate, polypropylene
adipate, polybutylene adipate, polypentylene adipate, polyhexalene adipate, polyheptadene
adipate, polyoctalene adipate, polyethylene glutarate, polypropylene glutarate,
polybutylene glutarate, polypentylene glutarate, polyhexalene glutarate, polyheptadene
glutarate, polyoctalene glutarate polyethylene pimelate, polypropylene pimelate,
polybutylene pimelate, polypentylene pimelate, polyhexalene pimelate, polyheptadene
pimelate, poly(propoxylated bisphenol fumarate), poly(propoxylated bisphenol succinate),
poly(propoxylated bisphenol adipate), poly(propoxylated bisphenol glutarate), mixtures,
copolymers or combinations thereof, and the like.
Polyester toner particles, formed by the emulsion aggregation
process, are illustrated in a number of patents, such as
U.S. Patent No. 5,593,807
U.S. Patent No. 5,290,654
U.S. Patent No. 5,308,734
U.S. Patent No. 5,370,963
. Further examples of suitable polyester particles include those having
lithium and/or sodium sulfonated polyester resin as disclosed in a number of patents,
U. S. Patents Nos. 6,387,581
. The polyester may comprise any of the polyester materials described in
the aforementioned references.
An example process for preparing the polyester based emulsion
aggregation particles may comprise charging a polyester resin emulsion, for example
an aqueous based emulsion optionally containing one or more surfactants, into a
reactor, and adding a colorant to the reactor while stirring. A wax dispersion may
optionally be added. The mixture is stirred and heated to a desired temperature,
for example from about 40°C to about 70°C, such as from about 45°C
to about 70°C or from about 40°C to about 65°C. A solution of an
aggregating agent is pumped into the mixture to initiate growth/aggregation of the
polyester particles. An additional amount of resin emulsion may then be added, where
it is desired to form a shell that is substantially free of coloring agent such
as dyes, pigments or mixtures thereof on the core aggregated colored particles.
The temperature of the reactor may then be raised towards the end of the reaction
to, for example, from about 45°C to about 75°C, such as from about 50°C
to about 75°C or from about 45°C to about 70°C, to allow for appropriate
spherodization and coalescence to achieve the desired average particle size and
shape. The slurry may be cooled, washed and dried.
Examples of suitable acrylate resin binders for the emulsion
aggregation particles include, for example, polymers such as poly(styrene-alkyl
acrylate), poly(styrene-1,3-diene), poly(styrene-alkyl methacrylate), poly(styrene-alkyl
acrylate-acrylic acid), poly(styrene-1,3-diene-acrylic acid), poly(styrene-alkyl
methacrylate-acrylic acid), poly(alkyl methacrylate-alkyl acrylate), poly(alkyl
methacrylate-aryl acrylate), poly(aryl methacrylate-alkyl acrylate), poly(alkyl
methacrylate-acrylic acid), poly(styrene-alkyl acrylate-acrylonitrile-acrylic acid),
poly(styrene-1,3-diene-acrylonitrile-acrylic acid), and poly(alkyl acrylate-acrylonitrile-acrylic
acid); the latex contains a resin selected from the group consisting of poly(styrene-butadiene),
poly(methylstyrene-butadiene), poly(methyl methacrylate-butadiene), poly(ethyl methacrylate-butadiene),
poly(propyl methacrylate-butadiene), poly(butyl methacrylate-butadiene), poly(methyl
acrylate-butadiene), poly(ethyl acrylate-butadiene), poly(propyl acrylate-butadiene),
poly(butyl acrylate-butadiene), poly(styrene-isoprene), poly(methylstyrene-isoprene),
poly(methyl methacrylate-isoprene), poly(ethyl methacrylate-isoprene), poly(propyl
methacrylate-isoprene), poly(butyl methacrylate-isoprene), poly(methyl acrylate-isoprene),
poly(ethyl acrylate-isoprene), poly(propyl acrylate-isoprene), poly(butyl acrylate-isoprene);
poly(styrene-propyl acrylate), poly(styrene-butyl acrylate), poly(styrene-butadiene-acrylic
acid), poly(styrene-butadiene-methacrylic acid), poly(styrene-butadiene-acrylonitrile-acrylic
acid), poly(styrene-butyl acrylate-acrylic acid), poly(styrene-butyl acrylate-methacrylic
acid), poly(styrene-butyl acrylate-acrylonitrile), and poly(styrene-butyl acrylate-acrylonitrile-acrylic
Acrylate toner particles created by the emulsion aggregation
process are illustrated in a number of patents, such as
U.S. Patent No. 5,278,020
U.S. Patent No. 5,346,797
U.S. Patent No. 5,344,738
U.S. Patent No. 5,403,693
U.S. Patent No. 5,418,108
U. S. Patent No. 5,364,729
. The acrylate may comprise any of the materials described in the aforementioned
references. In embodiments, the acrylate polymer may be a styrene-acrylate copolymer,
such as styrene-butyl acrylate that may also be comprised of &bgr;-carboxyethylacrylate.
Thus, the binder may be specifically comprised of a styrene-alkyl
acrylate, for example a styrene-butyl acrylate copolymer resin, or a styrene-butyl
acrylate-&bgr;-carboxyethyl acrylate polymer resin.
The monomers used in making the acrylate polymer binder
may include any one or more of, for example, styrene, acrylates such as methacrylates,
butylacrylates, &bgr;-carboxyethyl acrylate (&bgr;-CEA), etc., butadiene, isoprene,
acrylic acid, methacrylic acid, itaconic acid, acrylonitrile, benzenes such as divinylbenzene,
etc., and the like. Known chain transfer agents can be utilized to control the molecular
weight properties of the polymer. Examples of chain transfer agents include dodecanethiol,
dodecylmercaptan, octanethiol, carbon tetrabromide, carbon tetrachloride, and the
like in various suitable amounts, for example of about 0.1 to about 10 percent by
weight of monomer, and preferably of about 0.2 to about 5 percent by weight of monomer.
Also, crosslinking agents such as decanedioldiacrylate or divinyl benzene may be
included in the monomer system in order to obtain higher molecular weight polymers,
for example in an effective amount of about 0.01 percent by weight to about 25 percent
by weight, preferably of about 0.5 to about 10 percent by weight.
An example method for making acrylate based emulsion aggregation
particles may include first mixing resin emulsion, for example an aqueous based
emulsion optionally containing one or more surfactants, a colorant, and a coagulating
agent at a temperature at or above the glass transition temperature (Tg) of the
resin, such as 5°C to about 50°C above the Tg of the resin, which Tg is
usually in the range of from about 50°C to about 80°C or is in the range
of from about 52°C to about 65°C. The particles are permitted to grow
or aggregate to a desired size. An outer shell material for the aggregated particles,
for example consisting essentially of binder resin that is substantially free of
coloring agent such as dyes, pigments or mixtures thereof on the core aggregated
colored particles, may then be added, for example to form a shell on the aggregated
particles having a thickness of about 0.1 to about 2 micron. The aggregation is
then halted, for example with the addition of a base. The particles may then be
coalesced, for example at an elevated temperature such as from about 60°C to
about 98°C, until a suitable shape and morphology is obtained. Particles are
then optionally subjected to further processing, for example wet sieved, washed
by filtration, and/or dried.
As surfactants for use in making emulsion aggregation particles
as discussed above, examples include anionic, cationic, nonionic surfactants and
The toner preparation is typically carried out in an aqueous
(water) environment as detailed above, and the electrophoretic ink is an non-aqueous
environment (oil). When the toner is prepared, it is given a final water wash to
remove excess surfactant. Trace amounts of residual surfactant on the surface of
the toner particle, or trapped within the particle itself, may remain and contribute
to the low conductivity of the particles. However, the amount of surfactant that
actually gets into the oil is very low, since it prefers to be in water. As a result,
the fluid medium has a desired low conductivity.
In embodiments, the emulsion aggregation particles are
made to have an average particle size of from about 0.5 to about 25 µm, for
example about 5 to about 15 µm or about 5 to about 12 µm. The particle
size may be determined using any suitable device, for example a conventional Coulter
The emulsion aggregation particles also may have a substantially
monodisperse size such that the upper geometric standard deviation (GSD) by volume
for (D84/D50) is in the range of from about 1.1 to about 1.25. The particle diameters
at which a cumulative percentage of 50% of the total toner particles are attained
are defined as volume D50, and the particle diameters at which a cumulative percentage
of 84% are attained are defined as volume D84. These aforementioned volume average
particle size distribution indexes GSDv can be expressed by using D50 and D84 in
cumulative distribution, wherein the volume average particle size distribution index
GSDv is expressed as (volume D84/volume D50). The upper GSDv value for the toner
particles indicates that the toner particles are made to have a very narrow particle
The emulsion aggregation particles also may be made to
be highly circular, thereby exhibiting better flow properties with respect to movement
within the display medium. In other words, rounder/smoother particles have a higher
electrophoretic mobility, and thus a faster response time within the display. The
circularity is a measure of the particles closeness to a perfect sphere. A circularity
of 1 identifies a particle having the shape of a perfect circular sphere. The emulsion
aggregation particles may have an average circularity of about 0.92 to about 0.99,
for example from about 0.94 to about 0.98 or from about 0.95 to about 0.97. The
circularity may be determined using the known Malvern Sysmex Flow Particle Image
In embodiments, the binder of the particles is comprised
of a mixture of two binder materials of differing molecular weights, such that the
binder has a bimodal molecular weight distribution (that is, with molecular weight
peaks at least at two different molecular weight regions). For example, the binder
may be comprised of a first lower molecular weight binder, for example a non-crosslinked
binder, and a second high molecular weight binder, for example a crosslinked binder.
The first binder may have a number average molecular weight (Mn), as measured by
gel permeation chromatography (GPC), of from, for example, about 1,000 to about
30,000, and more specifically from about 5,000 to about 15,000, a weight average
molecular weight (Mw) of from, for example, about 1,000 to about 75,000, and more
specifically from about 25,000 to about 40,000, and a glass transition temperature
of from, for example, about 40°C to about 75°C. The second binder may
have a substantially greater number average and weight average molecular weight,
for example over 1,000,000 for Mw and Mn, and a glass transition temperature of
from, for example, about 35°C to about 75°C. The glass transition temperature
may be controlled, for example, by adjusting the amount of acrylate in the binder.
For example, a higher acrylate content can reduce the glass transition temperature
of the binder. The second binder may be referred to as a gel, which is a highly
crosslinked polymer, due to the extensive gelation and high molecular weight of
the latex. In this embodiment, the gel binder may be present in an amount of from
about 0% to about 50% by weight of the total binder, preferably from about 8% to
about 35% by weight of the total binder.
The first, lower molecular weight binder may be selected
from among any of the aforementioned polymer binder materials. The second gel binder
may be the same as or different from the first binder. For example, for acrylate
binders, the second gel binder may be comprised of highly crosslinked materials
such as poly(styrene-alkyl acrylate), poly(styrene-butadiene), poly(styrene-isoprene),
poly(styrene-alkyl methacrylate), poly(styrene-alkyl acrylate-acrylic acid), poly(styrene-alkyl
methacrylate-acrylic acid), poly(alkyl methacrylate-alkyl acrylate), poly(alkyl
methacrylate-aryl acrylate), poly(aryl methacrylate-alkyl acrylate), poly(alkyl
methacrylate-acrylic acid), poly(styrene-alkyl acrylate-acrylonitrileacrylic acid),
and poly(alkyl acrylate-acrylonitrile-acrylic acid), and/or mixtures thereof In
embodiments, the gel binder is the same as the first binder, and both are a styrene
acrylate, for example a styrene-butyl acrylate or styrene-butyl acrylate of styrene-butyl
acrylate-&bgr;-carboxy ethyl acrylate. The higher molecular weight of the second
gel binder may be achieved by, for example, including greater amounts of styrene
in the monomer system, including greater amounts of crosslinking agent in the monomer
system and/or including lesser amounts of chain transfer agents.
In still further embodiments, the emulsion aggregation
particles have a core-shell structure. In this embodiment, the core is comprised
of the particle materials discussed above, including at least the binder and the
colorant. Once the core particle is formed and aggregated to a desired size, a thin
outer shell is then formed upon the core particle. The shell may be comprised of
only binder material, although other components may be included therein if desired.
The shell may be comprised of a latex resin that is the same as a latex of the core
particle. The shell latex may be added to the core aggregates in an amount of about
5 to about 40 percent by weight of the total binder materials, for example in an
amount of about 5 to about 30 percent by weight of the total binder materials. The
shell or coating on the aggregates may have a thickness wherein the thickness of
the shell is about 0.2 to about 1.5 µm, for example about 0.3 to about 1.2
µm or from about 0.5 to about 1 µm.
The total amount of binder, including core and shell if
present, may be in the range of from about 60 to about 95% by weight of the emulsion
aggregation particles (toner particles exclusive of external additives) on a solids
basis, for example from about 70 to about 90% by weight of the particles.
The particles may also be made by emulsion aggregation
starting from seed particles derived via a stable free-radical polymerization method.
Such stable free-radical polymerization (SFRP) processes are known in the art, for
example as described in
U.S. Patent No. 5,322,912
. In the SFRP processes, propagating chains of the polymer are referred
to as "pseudo-living" because the stable free-radical agent adds to a propagating
chain and the chain is temporarily, but reversibly, terminated. This allows for
the formation of block copolymers that can incorporate monomers that will enhance
the particle charge. The monomers due to this block character can be at the particle
surface (especially if they are formed from hydrophilic monomers) and thus the charge
of the particle will be enhanced. Such monomers can be amines such as aminoethylacrylate
or methacrylate, sulfonates such as styrenesulfonates, acids such as &bgr;-carboxyethytacrylate
or methacrylate, or any heteroatom monomers that can be ionized or quaternized.
The resultant polymers of SFRP are dispersed in an aqueous phase to form the starting
latex of the emulsion aggregation processes discussed above. Thus, SFRP may be used
to form any of the polymers described above as binders for the emulsion aggregation
In addition to the polymer binder and the colorant, the
particles may also contain a wax dispersion. Linear polyethylene waxes such as the
POLYWAX® line of waxes available from Baker Petrolite are useful. Of course,
the wax dispersion may also comprise polypropylene waxes, other waxes known in the
art, including carnauba wax and the like, and mixtures of waxes. The toners may
contain from, for example, about 1 to about 15% by weight of the particles, on a
solids basis, of the wax, for example from about 3 to about 12% or from about 5
to about 10% by weight.
In addition, the colored particles may also optionally
contain a coagulant and/or a flow agent such as colloidal silica. Suitable optional
coagulants include any coagulant known or used in the art, including the well known
coagulants polyaluminum chloride (PAC) and/or polyaluminum sulfosilicate (PASS).
The coagulant is present in the toner particles, exclusive of external additives
and on a dry weight basis, in amounts of from 0 to about 3% by weight of the toner
particles, for example from about greater than 0 to about 2% by weight of the toner
particles. The flow agent, if present, may be any colloidal silica such as SNOWTEX
OL/OS colloidal silica. The colloidal silica is present in the toner particles,
exclusive of external additives and on a dry weight basis, in amounts of from 0
to about 15% by weight of the toner particles, for example from about greater than
0 to about 10% by weight of the toner particles.
Although not required, the toner may also include additional
known positive or negative charge additives in effective suitable amounts of, for
example, from about 0. 1 to about 5 weight percent of the toner, such as quaternary
ammonium compounds inclusive of alkyl pyridinium halides, bisulfates, organic sulfate
and sulfonate compositions such as disclosed in
U.S. Patent No. 4,338,390
, cetyl pyridinium tetrafluoroborates, distearyl dimethyl ammonium methyl
sulfate, aluminum salts or complexes, and the like.
In embodiments, one or more sets of the colored particles
incorporated into the display medium comprise crosslinked emulsion aggregation particles.
The crosslinking may be achieved by any suitable method, including, for example,
thermal curing or radiation, for example UV, curing. Crosslinked refers to, for
example, the high molecular weight state achieved by including crosslinkable monomer
or oligomer additives in a composition along with an initiator and exposing the
composition to a curing environment (for example, elevated temperature for thermal
curing or UV light for radiation curing) to effect curing of the additives. Other
components of the composition, for example the other binder resin components, may
also participate in the crosslinking.
Gel content may be used to define the extent of crosslinking
in the particles. The crosslinking forms a gel portion that has significantly increased
strength and less solvent solubility with respect to the individual polymer chains.
Gel content refers to the proportion of the polymer chains of the polymer particles
that have been crosslinked, thereby constituting a part of the gel network. In embodiments,
the particles may have a gel content from about 10 percent to about 100 percent,
for example from about 20 to about 80 percent or from about 25 to about 75 percent.
The gel content of the polymer particles is quantitatively
measured, for example by continuously extracting, for example by soxhlet extraction,
the reaction product after crosslinking processing is complete, by which the weight
of the crosslinked polymer material can be obtained. A continuous extraction method
allows polymers that are soluble to be removed from the mass of crosslinked polymer
that typically is not soluble in most or any solvents. Accordingly, the use of a
solvent in which the polymer is soluble, and in which the crosslinked portions are
insoluble, is used for the procedure. By dividing the weight of the crosslinked
polymer material by the total weight of the material that was continuously extracted,
and multiplying by 100, the gel content value may be obtained. The degree of crosslinking
may be regulated by controlling the time and/or intensity of the crosslinking procedure,
and/or by the concentration of the crosslinkable materials in the particles.
As was discussed above, hydrocarbon fluids such as ISOPAR
M are a desirable fluid to use for an electrophoretic display medium. However, using
such a fluid system with emulsion aggregation particle sets may result in device
degradation, for example as a result of the fluid causing swelling of the emulsion
aggregation resin and leaching out of the component materials such as wax, surface
treatment reagents, etc., from the swollen particles.
Crosslinkable particles may be prepared by including in
the binder one or more crosslinking additives. After the emulsion aggregation particle
formation process described above, the toner particles are subjected to a radiation
curing step, for example comprising UV radiation, to effect the crosslinking process,
resulting in a robust particle with excellent resistance to solvent swelling, and
also having enhanced resistance to softening/melting at elevated temperatures.
The crosslinking additives may be added to any type of
emulsion aggregation resin binder to permit the particles made therefrom to be UV
crosslinkable. The one or more crosslinking additives thus may be included in either
acrylate or polyester type emulsion aggregation resins. The additive may be present
in an amount of from, for example, about 0.5 to about 50% by weight, for example
from about 0.5 to about 25% by weight or from about 1 to about 20% by weight of
the total binder in the particles.
Examples of the crosslinking additives include multifunctional
acrylates such as diacrylates, triacrylates, tetraacrylates, and the like. For example,
the multifunctional acrylate monomer or oligomer, may include diacrylates such as
propoxylated neopentyl glycol diacrylate (available from Atofina as Sartomer SR
9003), 1,6-hexanediol diacrylate (Sartomer SR 238), tripropylene glycol diacrylate,
dipropylene glycol diacrylate, aliphatic diacrylate oligomer (CN 132 from Atofina),
aliphatic urethane diacrylate (CN 981 from Atofina), aromatic urethane diacrylate
(CN 976 from Atofina) and the like, triacrylate or higher functionality monomers
or oligomers such as amine modified polyether acrylates (available as PO 83 F, LR
8869, and/or LR 8889 from BASF Corporation), trimethylol propane triacrylate (Sartomer
SR 351), tris (2-hydroxy ethyl) isocyanurate triacrylate (Sartomer SR 368), aromatic
urethane triacrylate (CN 970 from Atofina), dipentaerythritol penta-/hexa-acrylate,
pentaerythritol tetraacrylate (Sartomer SR 295), ethoxylated pentaerythritol tetraacrylate
(Sartomer SR 494), dipentaerythritol pentaacrylate (Sartomer SR 399) and the like,
or mixtures of any of the foregoing. Additional examples of suitable crosslinking
additives include chlorinated polyester acrylate (Sartomer CN 2100), amine modified
epoxy acrylate (Sartomer CN 2100), aromatic urethane acrylate (Sartomer CN 2901),
and polyurethane acrylate (Laromer LR 8949 from BASF). Other unsaturated curable
resins that may be used are described in
U.S. Patent Publication No. 2005/0137278 A1
A crosslinking initiator is also included in the crosslinking
additives. Photoinitiators such as 2,4,6-trimethylbenzoyldiphenylphosphine oxide
(available as BASF Lucirin TPO), 2,4,6-trimethylbenzoylethoxyphenylphosphine oxide
(available as BASF Lucirin TPO-L), bis(2,4,6-trimethylbenzoyl)-phenyl-phosphine
oxide (available as Ciba IRGACURE 819) and other acyl phosphines, 2-benzyl 2-dimethylamino
1-(4-morpholinophenyl) butanone-1 (available as Ciba IRGACURE 369), titanocenes,
and isopropylthioxanthone, 1-hydroxy-cyclohexylphenylketone, benzophenone, 2,4,6-trimethylbenzophenone,
diphenyl-(2,4,6-trimethylbenzoyl) phosphine oxide, 2,4,6-trimethylbenzoylphenylphosphinic
acid ethyl ester, oligo(2-hydroxy-2-methyl-1-(4-(1-methylvinyl)phenyl) propanone),
2-hydroxy-2-methyl-1-phenyl-1-propanone, benzyl-dimethylketal, and mixtures thereof
may be used. Amine synergists, for example such as ethyl-4-dimethylaminobenzoate
and 2-ethylhexyl-4-dimethylamino benzoate, may also be used. This list is not exhaustive,
and any known photoinitiator that initiates the free radical reaction upon exposure
to a desired wavelength of radiation such as UV light can be used.
The total amount of photoinitiator included in the particles
with respect to the radically curable component may be from, for example, about
0.5 to about 20%, for example preferably from about 1 to about 15% or from about
1 to about 10%, by weight.
In making the crosslinkable particles, the particles may
be made the same as any of the aforementioned emulsion aggregation methods, with
the modification that the one or more crosslinking additives and photoinitiators
is included in the emulsion. The particles are then aggregated and/or coalesced
as normal. Following completion of the particle formation, the particles may then
be subjected to radiation such as thermal or UV radiation to initiate and effect
the crosslinking. Following radiation curing, the particles still have substantially
the same size and shape, but are crosslinked and thus much more resistant to solvents
and to melting at higher temperatures.
In embodiments, one or more sets of the colored particles
incorporated into the display medium comprise emulsion aggregation particles derived
from polymers having maleic anhydride and/or maleic acid functionality incorporated
into the resin. In the presence of water, the maleic anhydride groups are hydrolyzed
to carboxylic acid groups (maleic acid). Depending on the mode of preparing the
polymer resin used to make the particles, the degree of hydrolysis of the maleic
anhydride groups can be altered. In the emulsion aggregation process, the introduced
acid groups permit aggregation into larger particles as well as impart a substantially
uniform negative charge to the particles. In other words, in emulsion aggregation
processes, the acid functionality is used as an aggregation/coalescence site permitting
larger size particles to be grown from the polymer latex. Moreover, it is believed
that the acid functionality, for example carboxylic (COOH) acid functionality, may
impart the substantially uniform negative charge to the particles.
An advantage in the use of these particles is that the
negative charge of the particles is substantially uniform among the particles of
the set. Substantially uniform charge among the particles of a same colored set
of particles refers to, for example, a charge distribution such that the charge
among any two given particles of the set is within about 20%, such as within about
10%, of each other. As a result, the electrophoretic mobility of all of the particles
in the set is substantially the same, allowing the particles in the set to have
a substantially same response time upon application of an electric field. Ensuring
a substantially uniform charge, and thus a substantially uniform mobility and response
time upon application of an electric field, is advantageous to avoid unintended
mixing of one set of colored particles with a differently colored set of particles,
for example because some of the particles of the colored set did not adequately
respond to the electric field and permitted differently colored particles of a different
set to integrate into the set of colored particles. Color degradation of the intended
image could result from a lack of uniformity in charge among particles of the set.
The formation of polymers having maleic anhydride functionality
is described in Application
No. 11/139,543, filed May 31, 2005
. Specifically, any of the polymers/donor monomers, free radical initiators,
stable free radical agents, optional additives or other components described in
the above-identified application may be suitably used herein. Example polymers/donor
monomers that may be made to include maleic anhydride functionality include, for
example, styrene, butyl acrylate, carboxy ethyl acrylate, mixtures thereof, and
The maleic anhydride functionality may be incorporated
into the polymer at any stage of making the polymer, and the degree of conversion
to the maleic acid can also be altered by the mode of preparation. For example,
the maleic anhydride functionality may be introduced into the polymer at a bulk
polymerization step, or at the latex formation step, which latex is used in the
subsequent formation of the particles, for example by emulsion polymerization, and
the like. In bulk polymerization, the procedure is carried out in the absence of
water, and the maleic anhydride functionality is left intact. When this resin is
emulsified into a latex, only the surface maleic anhydride groups are converted
to the acid form. Conversely, when the maleic anhydride functionality is added to
a waterborne polymer latex, all of the maleic anhydride groups are hydrolyzed to
the acid form. The particles may be made by emulsion polymerization and the like,
using the maleic anhydride functional polymer latex mentioned above as a starting
latex, via any of the emulsion aggregation procedures discussed above.
In emulsion aggregation processes, aggregation is conducted
using latex(es) in an aqueous medium. As a result, acid functionality, for example
carboxylic acid groups, is imparted to the particles because maleic anhydride hydrolyzes
in the aqueous medium. Excess acid functionality not necessary for the aggregation
procedure may provide the negative charge exhibited by the particles.
In embodiments, one or more sets, for example one to ten,
such as one to four or two to four sets, of the colored particles incorporated into
the display medium comprise particles, for example emulsion aggregation particles
such as emulsion aggregation polyester or emulsion aggregation acrylate particles,
surface treated with a cationic polymer that imparts a substantially uniform positive
charge to the particles of the particles set. Thus, an advantage in the use of these
particles is that the positive charge of the particles is substantially uniform
among the particles of the set. Substantially uniform charge among the particles
of a same colored set of particles refers to, for example, a charge distribution
such that the charge among any two different particles of the set is within about
20%, such as within about 10%, of each other. As a result, the electrophoretic mobility
of all of the particles in the set is substantially the same, allowing the particles
in the set to have a substantially same response time upon application of an electric
field. Ensuring a substantially uniform charge, and thus a substantially uniform
mobility and response time upon application of an electric field, is advantageous
to avoid unintended mixing of one set of colored particles with a differently colored
set of particles, for example because some of the particles of the colored set did
not adequately respond to the electric field and permitted differently colored particles
of a different set to integrate into the set of colored particles. Color degradation
of the intended image could result from a lack of uniformity in charge among particles
of the set.
In embodiments, the cationic polymer is a methacrylate
polymer or copolymer, for example an aminomethacrylate polymer such as EUDRAGIT
EPO (Rohm America), that imparts a positive charge to the particles. Other examples
of specific cationic polymers that may be selected are EUDRAGIT RL and RS (Rohm
Pharma), which are copolymers synthesized from acrylic and methacrylic esters with
a low content of quaternary ammonium groups. EUDRAGIT RL and RS differ in the molar
ratios of the ammonium groups to the remaining neutral (meth)acrylic acid esters
(1:20 and 1:40, respectively). EUDRAGIT NE is an aqueous dispersion of a neutral
copolymer based on ethyl acrylate and methyl methacrylate. EUDRAGIT RD 100 is a
powder form of copolymers of acrylates and methacrylates with a quaternary ammonium
group in combination with sodium carboxymethylcellulose. Another cationic polymer
is EUDRAGIT RTM E (Rohm America), which is a copolymer of dimethylaminoethylmethacrylate
and neutral methacrylic esters.
By varying the concentration of the cationic polymer used,
the degree of charging can be varied. For example, lower concentration of cationic
polymer means less positive charge on the particles. By creating a substantially
uniform coating of the cationic polymer on the particles, a consistent surface charge
can be attained, and particle mobility is the same for all particles. Macroscopically,
the toner particles all appear to move at once, giving a faster, cleaner color transition.
The EUDRAGIT methacrylate polymers such as EUDRAGIT EPO
are cationic, and are pH dependent and soluble in solutions up to pH 5. The particles
of the colored particle set may thus be surface treated with the cationic polymer
by adding the cationic polymer in its dissolved form to an acidified slurry of the
particles. The pH is then slowly increased to above 5, for example to about 7 to
about 12 such as about 10 to about 12, so that the cationic polymer precipitates
on the surface of the particles. The cationic polymer is believed to surface treat
the particles by forming a film around the particle's surface upon the evaporation
of water. The surface of the treated particles acquires the cationic characteristics
of the cationic polymer, resulting in a positive charged toner.
In further embodiments, one or more sets, for example one
to ten, such as one to four or two to four sets, of the colored particles incorporated
into the display medium comprise particles, for example emulsion aggregation particles
such as emulsion aggregation polyester or emulsion aggregation acrylate particles,
having deposited thereon multiple layers of alternating cationic and anionic layers
that impart either a substantially uniform positive charge or a substantially uniform
negative charge, depending on the surface layer of the multi-layer coating, to the
particles of the particle set. For example, where the surface layer of the multi-layer
coating is a cationic material, the particles will exhibit a substantially uniform
positive charge, and where the surface layer of the multi-layer coating is an anionic
material, the particles will exhibit a substantially uniform negative charge.
As was discussed above, when emulsion aggregation particles
are made, such particles will typically include anionic groups on the surfaces thereof,
for example carboxylic acid groups or sodio-sulfonate groups inherited from excess
surfactant used in the process, inherited from the latex resin, and the like. Emulsion
aggregation particles thus typically possess the negative charge discussed above,
and exhibit a negative electrophoretic mobility in water and in dielectric fluid.
This charge, while desirable and suitable for the use of the particles in an electrophoretic
display as described above, may be non-uniform. However, the presence of anionic
groups on the surfaces of the particles provides sites for additional cationic and
anionic materials to be built up on the particles, and this property can be advantageously
used to provide a more uniform charge among the particles.
For example, the anionic groups on the particle surface
enable an ionic exchange between mobile cations on the surface with a cationic material.
The result is the formation of a substantially uniform nanoscale coating around
the toner particle surface, which coating imparts a positive charge to the particles.
Moreover, as the cationic and anionic materials, polyelectrolyte
materials may be used. In this manner, alternating layers of cationic and anionic
materials may be built up. That is, following formation of a layer of cationic polyelectrolyte,
ionic exchange may then be conducted between the ionic species of the surface cationic
polyelectrolyte and an anionic polyelectrolyte to deposit a uniform nanoscale anionic
coating on the surface, which coating imparts a negative charge to the particles.
The deposition process is conducted in an aqueous solution,
which process is therefore very compatible with the emulsion aggregation particle
formation processes discussed above.
It is desirable to deposit multiple alternating layers
of the cationic and anionic polyelectrolyte materials. For example, the coating
may contain from 2 to about 20 total layers, such as from 2 to about 10 or from
2 to about 8 total layers. Each layer is approximately nanoscale in thickness, having
a thickness of from about 0.1 to about 30 nm, for example from about 0.5 to about
10 nm or from about 1 to about 3 nm. Deposition of alternating layers enables complete
coverage of the particles, which may not occur with only a single layer deposition.
This enables the particles to have a more uniform charge density.
In general, the zeta potential (mV) achieved through deposition
of polyelectrolytes may vary from about 5 to about 100 mV, for example from about
5 to about 75 mV or about 10 to about 50 mV, for cationic polyelectrolyte surface
layers, and from about -5 to about -120 mV, for example between about -5 to about
-100 mV or about -10 to about -80 mV, for anionic polyelectrolyte surface layers.
In general, each particle dispersed in a solution is surrounded by oppositely charged
ions typically referred to as a fixed layer. Outside the fixed layer, there are
varying compositions of ions of opposite polarities, forming a cloud-like area,
typically referred to as a diffuse double layer, and the whole area is electrically
neutral. When a voltage is applied to the solution in which the particles are dispersed,
particles are attracted to the electrode of the opposite polarity, accompanied by
the fixed layer and part of the diffuse double layer, or internal side of a "sliding
surface." Zeta potential is considered to be the electric potential of this inner
area including this "sliding surface." As this electric potential approaches zero,
particles tend to aggregate.
The deposition of multiple alternating layers also enables
the creation of different charge densities among different colored particle sets.
For example, a first particle set having a multi-layer coating in which each layer
is comprised of the same cationic and anionic polyelectrolytes will exhibit a certain
charge density, whereas a similar particle set in which one or more layers of the
multi-layer coating use a cationic polyelectrolyte or an anionic polyelectrolyte
different than the other polyelectrolytes of the multi-layer coating can exhibit
a charge density different from the first particle set. The use of different polyelectrolytes
in a multi-layer coating thus enables different charge densities to be achieved
among different particle sets. This permits different particle sets to be used in
a same display medium and to be controlled differently in view of the different
charge densities possessed by the different particle sets. Of course, in a similar
manner, different charge densities among different particle sets may also be achieved
through the use of entirely different cationic polyelectrolytes and/or anionic polyelectrolytes
in the making of the different multi-layer coatings of the different particle sets.
In embodiments, although it is necessary to use a polyelectrolyte
to build up the multiple layer coating, it is not necessary to use a polyelectrolyte
as the surface layer of the coating. A cationic or anionic non-polyelectrolyte,
for example a cationic polymer as discussed above, may be used as the surface layer
of the coating.
As the cationic polyelectrolyte, any suitable polyelectrolyte
may be used. Polyelectrolyte refers to, for example, any chemical compound capable
of ionizing when dissolved. Specific examples of cationic polyelectrolytes include
poly(diallyldimethylammonium) (PDAD) chloride:
wherein n is from, for example, about 100 to about 8,000 such as from about 500
to about 5,000 (PDAD(C1) may have a weight average molecular weight of from about
50,000 to about 500,000), poly(allylamine) hydrogenchloride ((PAH)Cl):
wherein n is from, for example, about 10 to about 5,000 such as from about 100 to
about 1,000 (PAH(Cl) may have a weight average molecular weight of about 10,000
to about 100,000), and polyethyleneimine:
wherein x and y may each independently be from 1 to about 1,000 such as from 1 to
about 500 (polyethyleneimine may have a weight average molecular weight of about
200 to about 50,000). Other variants of polyethyleneimine can be used, such as:
or C6H21N5, a mixture of linear and branched chains,
with a weight average molecular weight ranging from about 1,200 to about 750,000,
and where n may vary from about 7 to about 5,000.
As the anionic polyelectrolyte, any suitable polyelectrolyte
may be used. Specific examples of anionic polyelectrolytes include poly(styrenesulfonate)
wherein n is from, for example, about 10 to about 5,000 such as from about 100 to
about 1,000 (poly(styrenesulfonate) sodium salt) may have a weight average molecular
weight of about 75,000 to about 250,000), polystyrene sulfonic acid, polystyrene
sulfonic acid ammonium salt, polyacrylic acid:
wherein n is from, for example, about 10 to about 75,000 such as from about 10 to
about 60,000 (polyacrylic acid may have a weight average molecular weight of about
2,000 to about 5,000,000), and polyacrylic acid partial sodium salt.
An additional advantage that may be realized through the
use of a multiple layer coating of alternating cationic and anionic polyelectrolytes
is that the particles may be made to more readily disperse in the fluid of the electrophoretic
display medium. For example, the presence of cationic and/or anionic species on
the surface of the particles may either themselves promote dispersion of the particles
in the display medium, or may be exchanged with additional ionic species that promote
such dispersion. As one example, the anion, for example a Cl ion, associated with
the surface of the particles as a result of the surface layer being a cationic polyelectrolyte,
may be exchanged with a dispersion enhancing ionic species such as sodium dioctylsulfosuccinate:
In this particular example, the resulting particles are hydrophobic.
Other dispersion enhancing species include nonionic surfactants
such as SPAN 20 (sorbitan monolaurate), SPAN 60 (sorbitan monostearate), SPAN 80
(sorbitan monooleate), SPAN 85 (sorbitan trioleate), mixtures thereof and the like,
as well as OLOA (polyisobutylenesuccinimide), or other anionic surfactants such
as SDS (sodium dodecyl sulfate) or SDBS (sodium dodecylbenzene sulfonate).
The resulting particles having a dispersion enhancing ionic
species thereon may readily disperse in the display medium, for example in a medium
such as ISOPAR or DOW 200 5cSt silicone oil. This is because the dispersion enhancing
species compatibilizes better with the oil as a result of being a bigger, bulkier
material that is more compatible with the oil compared to a single species such
As dyes for the colorant of the particles, preferred are
solvent dyes; within the class of solvent dyes, spirit soluble dyes are preferred
because of their compatibility with the ink vehicles of the present invention. Examples
of suitable spirit solvent dyes include Neozapon Red 492 (BASF); Orasol Red G (Ciba);
Direct Brilliant Pink B (Global Colors); Aizen Spilon Red C-BH (Hodogaya Chemical);
Kayanol Red 3BL (Nippon Kayaku); Spirit Fast Yellow 3G; Aizen Spilon Yellow C-GNH
(Hodogaya Chemical); Cartasol Brilliant Yellow 4GF (Clariant); Pergasol Yellow CGP
(Ciba); Orasol Black RLP (Ciba); Savinyl Black RLS (Clariant); Morfast Black Conc.
A (Rohm and Haas); Orasol Blue GN (Ciba); Savinyl Blue GLS (Sandoz); Luxol Fast
Blue MBSN (Pylam); Sevron Blue 5GMF (Classic Dyestuffs); Basacid Blue 750 (BASF),
and the like. Neozapon Black X51 [C.I. Solvent Black, C.I. 12195] (BASF), Sudan
Blue 670 [C.I. 61554] (BASF), Sudan Yellow 146 [C.I. 12700] (BASF), and Sudan Red
462 [C.I. 260501] (BASF).
Examples of pigments that may be used as the particles
herein, or that may be used as the colorant in polymer particles, include neat pigments
such as, for example, titania, barium sulfate, kaolin, zinc oxide, carbon black
and the like. The pigment should be insoluble in the suspending fluid.
In polymer particles, the colorant may be included in the
particles in an amount of from, for example, about 0.1 to about 75% by weight of
the particle, for example from about 1 to about 50% by weight or from about 3 to
about 25% by weight of the particle.
In any of the foregoing particle embodiments, the particles
may also include one or more external additives on the surfaces thereof Such external
additives may be applied by blending, for example with a Henschel blender. In embodiments,
the external additive package may include one or more of silicon dioxide or silica
(SiO2), titanium dioxide or titania (TiO2), titanic acid,
cerium oxide, calcium or zinc stearate, and the like. The particles may have an
average size (diameter) of from about 5 nm to about 250 nm. Mixtures of differently
sized particles may also be used, for example a first silica having an average primary
particle size, measured in diameter, in the range of, for example, from about 5
nm to about 50 nm, such as from about 5 nm to about 25 nm or from about 20 nm to
about 40 nm and a second silica having an average primary particle size, measured
in diameter, in the range of, for example, from about 100 nm to about 200 nm, such
as from about 100 nm to about 150 nm or from about 125 nm to about 145 nm. The external
additive particles may also be treated with a surface material.
In embodiments, the external additives may be used to impart
charge to the particles. For example, a silica particle treated with polydimethylsiloxane
(PDMS) or hexamethyldisilane (HMDS) can impart a positive charge. A titanic acid
treated wtih isobutyl trimethoxysilane can impart a negative charge.
The density of the particles for the display medium may
be substantially matched to that of the suspending fluid. For example, a suspending
fluid may have a density that is "substantially matched" to the density of the particles
dispersed therein if the difference in their respective densities is from about
zero to about 2 g/ml, for example from about zero to about 0.5 g/ml.
Displaying of Images
In a display medium comprising the above-described low
conductivity particle sets, the particles are first charged, for example through
application of an electric field thereto, for an appropriate time and with an appropriate
electric field. This field-induced or in situ charging imparts the appropriate charging
characteristics to each of the sets of particles in the display medium. As will
be further explained below, each of the sets of particles has a substantially zero
charge at time t=0.
Through application of the high electric field, each set of particles is charged
to an appropriate level. Differently colored particle sets may be charged to different
charge levels, thereby enabling the particles of each of the different sets to have
different mobility rates within the fluid.
The field-induced or in-situ charging of the particles
herein may be accomplished by any suitable method. One such method is illustrated
in Figure 17. The device 100 of Figure 17 includes a cell 140 in which the display
medium may be loaded, the cell being located between a pair of electrodes such as
parallel-plate electrodes 150, 160. An appropriate electric field may be generated
via control generator 120 and power supply 110, and the charging monitored by electrometer
170, which monitors the transient current. The reflection densitometer 130 monitors
the change in reflectance of the display medium loaded in the cell 140 as it is
switched back and forth by the electric field. The reflection densitometer may be
controlled by, for example, LabVIEW interface software and a PC 180. In embodiments,
the field strength applied may range from about 0.05 V/µm to about 5 V/µm,
for example from about 0.25 V/µm to about 3 V/µm or from about 0.5 V/µm
to about 2 V/µm. The field may be applied for about 0.001 seconds to about
5 hours, for example from about 0.005 seconds to about 2 hours or from about 0.01
seconds to about 1 hour or from about 1 second to about 30 minutes. The field may
take any form, and may specifically be a square waveform, a triangular waveform,
a sinusoidal waveform and the like.
The charging electric field may be applied to the display
fluid after formation, that is, after addition of all of the differently colored
particle sets thereto. Moreover, the field may be applied to the display fluid after
the display fluid is located in a multiplicity of reservoirs of the display device
to form a display layer of the device, or it may be applied to the display fluid
prior to inclusion in the multiplicity of reservoirs of a display layer of the display
device. If field induced charging is conducted on the display medium with multiple
particle sets therein, the different particle sets should be chosen so as to each
charge to a different charge level under application of a same charging field.
Application of different waveforms and field strengths,
as well as properties of the display medium such as size of the particles therein,
surfactants used in the manufacture of the particles, the composition of the polymers
of the particles and/or inclusion on or in the particles of charge agents such as
discussed above, and the like, affect the charging behavior of the particles in
the display medium. The following examples illustrate the foregoing.
Figure 18 shows the transient current characteristics for
a display medium comprised of a yellow toner (Imari MF, a yellow emulsion aggregation
styrene butylacrylate toner) dispersed in ISOPAR M (the solids loading of toner
in ISOPAR M is 8% by weight) and using square-wave electric fields. Figure 19 shows
the total charge of the particles in the display medium acquired at different field
strengths as determined from the integrated area under a current-time curve. Note
that the charge values identified in the Figures refer to the total charge in the
test cell in nC. To calculate the charge per unit mass (in µC/g), the total
charge in the test cell is divided by the mass of toner in the test cell. The total
mass is derived from the ink density. Herein, a standard value of 14 mg was used,
which is typical for the mass of toner in an 8 wt. % ink in the cell. It can be
seen from Figures 18 and 19 that the electrophoretic particles become charged by
the electric field, and that charging increases with increasing electric field strength.
Figure 20 shows the transient current characteristics for
the same display medium used for Figures 18 and 19 using a triangular-wave electric
field (300 millihertz) as a function of charging cycling time. The electric field
is reported in units of V/µm, wherein µm is the gap between the electrodes.
A peak is reflected where the particles jump from one side of the gap to the other,
which temporarily peaks the current. An electric field peak around 1 V/µm indicates
that for an electrode gap of 50 µm, a 50 V field is required to effect the
jump. The total charge of the particles is shown in Figure 21. The results again
demonstrate that particles are charged by the electric field and that charging increases
with cycling time. Also, the charging may be manipulated as a result of the type
of wave applied for charging. The ink conductivity, given by the slope of the straight
line portion of the current versus field curve, is about 1,9 x 10-12
S/m, indicating that there are very few free ions in the display medium. The electric
field strength, the cycling frequency (waveform), and the display medium materials
are the parameters which appear to most significantly influence how fast the particles
are charged. Similar results are obtained for differently colored particles, for
example magenta, cyan and black Imari MF toners.
Figure 22 shows an example of the charging characteristics
for electrophoretic ink particles having three different sizes (7.2 µm, 9.3
µm and 16.8 µm). Each display medium is comprised of the indicated size
of SFRP cyan styrene butylacrylate toner particles dispersed in ISOPAR M (the solids
loading of toner in ISOPAR M is 8% by weight). As shown in Figure 22, the smallest
particles are able to acquire the highest charge, whereas the largest particles
obtain the least charge, when charged for the same time and using the same charging
As also can be seen in Figures 19, 21 and 22, the particles
may be made to possess a different charge, depending on how long the particles are
subjected to the electric field. In other words, the particles may exhibit dynamic
charging characteristics wherein the charge possessed by the particles may be ramped
up where the field is applied longer and/or stronger. This enables differently colored
but similarly composed and sized particle sets to be used together in a display
device, since each of the similar but differently colored particle sets may still
be made to have different charges so as to have different electrophoretic mobilities
in the display device. In other words, the charge level of a given set of colored
particles in embodiments is tunable via application of the charging field.
Figure 23 shows a different charging behavior. Specifically,
Figure 23 shows the charging characteristics of an electrophoretic display medium
composed of a conventional cyan polyester toner dispersed in ISOPAR M. The solids
loading of toner in ISOPAR M is 8% by weight. This polyester toner is prepared via
a conventional physical grinding process, not a chemical process such as emulsion
aggregation. The conventional process for making polyester toner is a condensation
polymerization of a diol (such as propylene glycol) and acid (such as terephthalic
acid). The bulk polymer is then mechanically pulverized via extrusion in the presence
of pigment to make fine toner particles. As can be seen in Figure 23, the charging
behavior is static, that is, the particles obtain substantially the same charge
regardless of the length of time the field is applied. A factor for the static charging
exhibited by the polyester toner is the absence of surfactants, coagulants, and
other ionic species that are present in the emulsion aggregation toner preparation
As was discussed above, the different particle sets included
in a display medium may each be made to have a different electrophoretic mobility,
for example through having a different charge. For example, in a display medium
containing four differently colored particle sets such as cyan, yellow, magenta
and black, the cyan may be controlled to have a charge of about 3 µC/g, the
yellow a charge of about 2 µC/g, the magenta a charge of about 1 µC/g
and the black a charge of about 0.5 µC/g. The sets of differently colored particles
thus should not have a substantially similar charge level, and thus for example
each particle set should have a charge differing by at least about 0.1 µC/g
from another differently colored set of particles, for example from about 0.3 µC/g
or about 0.7 µC/g from each other, or more.
Under application of an appropriate AC or DC current to
the display medium following the field induced charging, the charged particles in
the display medium having different charge levels will move at different rates in
response to the field, enabling the needed control over the movement of the particles
to permit different colors to be displayed. Thus, through selection of appropriate
differently colored particles, for example including the selection of particles
composed of different materials, made by different methods, having different sizes,
having different dynamic versus static charging characteristics, and the like, and/or
through control over the charging of the differently colored particles, a multiple
color and/or full color display can be obtained by including differently charged,
differently colored particle sets in the display medium.
The field induced charging may be conducted on the display
medium prior to use of the display device containing the display medium in forming
images. Also, the field induced charging procedure may be repeated during the lifetime
of the display device in order to renew or refresh the charges carried by the particles
in the display medium. This permits the device to have a longer life, even where
the particles in the display medium exhibit charge degradation over time. Here again,
because the particles have low conductivity and do not depend on excess free ions
in the display medium for charging, the particles are able to re-charge to substantially
the same levels upon reapplication of the field induced charging field, thereby
enabling the device to have a longer useful life. For this refreshing or recharging
embodiment, it is again desirable to employ display mediums with multiple particle
sets wherein the different particle sets each charge to a different charge level
under application of a same electric field, so that no two sets of differently colored
particles are made to acquire a substantially similar charge following the refreshing
In operating the electrophoretic display device so as to
form an image therewith, an electric field, in particular a reversible direct current
or an alternating current, is applied to the reservoirs of the device in order to
move a desired color set of particles in the reservoirs so as to be displayed.
In embodiments of the display device, each of the individual
reservoirs may be individually addressable, that is, a separate field may be applied
to each individual reservoir of the device in order to generate an appropriate color
at that individual reservoir or capsule. Appropriate sets or groups of different
ones of the individual reservoirs may also be associated with a same driving electrode.
For example, in a display, each reservoir or a set of reservoirs may represent a
pixel or sub-pixel of an image, and each pixel or sub-pixel may thus be separately
controlled to generate a desired overall image from the device. Control methods,
including hardware/software, for controlling each reservoir of the display device
in a manner enabling an overall image to be shown are known in the display arts,
and any such control method may be applied herein. To permit individual addressability,
the size of the electrodes may be the same as or smaller than the size of the individual
reservoirs of the display device, enabling individual control of each. In this manner,
the electric field applied to each reservoir/capsule can be individually controlled.
Also, the size of the electrodes can be different from (for example, larger than)
the size of the reservoirs, thereby enabling more than one reservoir to be controlled
by a single electrode where the electrode is larger than the reservoir/capsule,
or also enabling only a portion of the reservoir to be controlled (turned on and
off) by an electrode where the electrode is smaller than the size of a reservoir.
That is, the pattern of the electrodes does not need to line up with the reservoirs.
Any of the foregoing can be done by, for example, appropriate patterning of the
conductive path on the bottom conductive substrate. An example of the patterning
of electrodes can be found in, for example,
U. S. Patent No. 3,668,106
Control of the color displayed by an individual reservoir
of a display device may be demonstrated through the following explanation. In this
example, the display medium contains at least four differently colored particle
sets of cyan, yellow, magenta and black, the cyan having a charge of about 3 µC/g
the yellow a charge of about 2 µC/g the magenta a charge of about 1 µC/g
and the black a charge of about 0.5 µC/g. As a result of each differently colored
particle set having a different charge, specifically a different low conductivity
charge, each differently colored particle set will respond differently to an applied
electric field (that is, each differently colored particle set exhibits a different
electrophoretic mobility). In this example, the cyan particles carry the highest
charge level, and thus respond most rapidly under an applied electric field. Thus,
to display the cyan particles to a viewer, the particles may first be pulled (attracted)
to the rear substrate by application of an electric field. Upon reversal of the
electric field, the cyan particles will be most rapidly attracted to the front facing
electrode, such that the viewer will perceive only cyan at that reservoir/capsule.
The set of yellow particles has the second highest charge
level. To display the yellow particles, the electric field from the cyan color display
above is again reversed to pull the particle sets back toward the rear electrode.
However, the field is applied for only so long as necessary for the cyan particles
to move past the yellow particles toward the rear electrode. Once the cyan particles
have moved past the yellow particles, the yellow color is perceived by a viewer
since at this point the yellow particles are closest to the front electrode. If
the reversal of the field is applied for a longer time, then the yellow particles
will move past the magenta particles toward the rear electrode. Halting application
of the field at this transition point will enable magenta to be perceived by the
viewer since at this point the magenta particles will be closest to the front electrode.
Finally, as the black particles in this example move slowest because they possess
the lowest charge, maintaining the reversal of the field until the magenta particles
move past the black particles, for example maintaining the reversal of the field
until the particle sets in the display medium are pulled to the back electrode,
enables the black particles to be perceived by the viewer since at this point the
black particles will be closest to the front electrode.
The strength of the electric field that may be applied
to effect movement of the particles may be defined as the voltage divided by the
thickness of the gap between the two electrodes. Typical units for electric field
are volts per micron (V/µm). Figure 19 shows the charge level of the particle
vs. the applied electric field. The electric field ranges from 0.5 to 3 V/µm.
Applied electric fields may range from about 0.1 V/µm to about 25 V/µm,
for example from about 0.25 V/µm to about 5 V/µm, or from about 1 V/µm
to about 2 V/µm, or any ranges in between. The duration of electric field application
can range from about 10 msec to about 5 seconds, or from about 100 msec to about
1 second, or any ranges in between. Generally, the greater the charge on the particles,
the faster the particles will move for a given electric field strength. For example,
by looking at Figure 18, the transit time is the highest peak of the curve. This
transit time represents the average time for all the particles to jump from one
electrode to the other. Clearly, for the 600 V curve, the transit time peak occurs
at just past 0.02 sec (20 msec). Using Figure 18 as an example, if one imagined
that the various voltage curves represented various particle groups' mobilities,
at 20 msec one set of particles (the 600 V trace) would have crossed the gap, but
the other sets of particles (represented by the other traces) would be only 1/2
or 1/3, or maybe only 1/4 of the way across the gap. This information thus can be
used to determine the field strengths and application durations necessary to display
each of the colors of a multiple color display medium.
Of course, any colored particle set in the display medium
may be made to move more rapidly than a differently colored particle set without
restriction, and the ordering of mobilities in this example is arbitrary for illustration
As another specific example of controlling color display
is a multi-color display medium, reference is made to Figures 24 to 27. Here, yellow
particles (Y) are made to have a high positive charge and magenta particles (M)
to have a low positive charge, with cyan (C) having a high negative charge and black
(K) a low negative charge. The particles with the higher charge are shown larger
in the Figures, but this larger size is to depict the larger charge and not necessarily
the actual size relationship among the particles. The particles may all have the
same size, or the larger charge particles may actually be smaller in size than the
lower charge particles.
To enable the selective migration of the desired set of
colored particles, the driving voltage waveform is changed from positive to negative
polarity or vice versa. When the top plate is charged + (Figure 25), the - charged
pigments are attracted to this electrode. The higher charge particles, in this case
cyan, will be the first particles to move to this electrode, followed by the lower
mobility black particles, and thus cyan is displayed. When the top plate potential
is switched from + to - (Figure 24), the fast moving + particles, in this case yellow,
are attracted first, followed by the slower moving magenta species. The viewing
of the highly charged particles is thus relatively straightforward, as they will
be always be the first particles to reach the oppositely charged electrode.
In order to selectively view the lower mobility species,
the voltage waveform is modified by the addition of a brief switching voltage pulse
as shown in Figures 26 and 27. This selective pulse reverses the polarity of the
current/electric field across the conductive substrates and thus reverses movement
of the highly charged particles for a brief instant, and causes these particles
to move toward the middle of the cell. The electric field is then removed once the
higher mobility particles have moved past the lower mobility particles toward the
rear substrate, and before the additional particle sets of opposite polarity are
moved closer to the front viewing conductive substrate than the lower mobility particles.
What remains on the outside (that is, a viewable side) are the slow moving low mobility
particles, as they are much less sensitive to this pulsed electric field. Thus,
by pulsing the electric field to attract negative charge particles to the rear substrate,
the lower charge black negative particles are displayed in place of the higher negative
charge cyan particles (Figure 27). Similarly, when the higher positive charge yellow
particles are displayed, by pulsing the electric field to attract the positive charge
particles to the rear substrate, the lower positive charge magenta particles are
displayed in place of yellow (Figure 26).
In embodiments, the higher mobility particles may have
a charge of from about ±1 to about ±5 µC/g for example from about
±2 to about ±3 µC/g and the lower mobility particles a charge of
from about ±0.1 to about ±1 µC/g for example from about ±0.1
to about ±0.7 µC/g.
The above controls over the display of colors in a multi-color
system may be applied to a display medium containing any number of differently colored
particle sets, for example including two, three, four or even more particle sets.
Highlight color particle sets, for example blue highlight color, red highlight color,
green highlight color and the like highlight color particle sets may be included
in multi-color particle sets to add additional color range capabilities to the display,
and the control of the colors may be effected as described above. The total particle
sets, including highlight color particle sets, in the display medium thus may be
five, six, seven, eight or even more.
Upon removal of the electric field, the particles may be
maintained in the selected color state through any suitable means. For example,
the sets of particles may be made to have a slightly different density from the
display fluid such that upon removal of the field, the particles float to the top
or bottom of the display. Because no field is applied, the particles should substantially
maintain the color order at the time the field was removed during such settling
movement. Alternatively, the fluid may have a sufficiently thick viscosity to maintain
the particle color order upon removal of the electric field. For example, a viscosity
range of 0.65 to 20 cSt, such as from about 1 to about 20 cSt or from about 5 to
about 20 cSt, may be appropriate. To facilitate a sufficiently viscous fluid, the
fluid may contain a gellant, for example as described in
U.S. Patent Application No. 11/169,924
. The gellant acts to thicken the fluid viscosity at lower temperatures
or when an electric field is not applied, enabling images to be fixed within the
reservoir/capsule. Other methods for fixing the displayed image could come in the
form of other means of altering the fluid viscosity. Phenomena such as electrorheological
effects (where the fluid viscosity changes upon the application of an electric field),
magnetic field effects (where the fluid viscosity changes in response to a magnetic
field), and the like could be utilized, if desired.
Embodiments will now be further illustrated by way of the
In this example, use of emulsion aggregation particles
in a two particle electrophoretic display is demonstrated.
Preparation of negatively charged emulsion aggregation
cyan particles. Cyan toner particles are prepared via aggregating dispersions of
a styrene/butylacrylate/carboxylic acid terpolymer non-crosslinked resin particles,
a second crosslinked copolymeric resin of styrene/butylacrylate/carboxylic acid
with divinyl benzene, and a cyan pigment in the presence of two cationic coagulants
to provide aggregates which are then coalesced at temperatures above the non-crosslinked
resin Tg to provide spherical particles. These particles are then washed (4x) with
deionized water, dried, and dry-blended with an additive package comprising at least
a silica surface treated with polydimethylsiloxane (PDMS) and having a primary particle
size of about 40 nm. Another additive that may be used is a titanic acid with alkyl
group functionality having a primary particle size of about 40 nm.
Preparation of positively charged emulsion aggregation
magenta polyester particles. A surface treated polyester-type emulsion aggregation
toner is used for the magenta particles. The surface treatment additive is the cationic
methacrylate copolymer EUDRAGIT EPO. The cationic polymer is added in its dissolved
form to the acidified toner slurry. The pH is slowly increased to 10 to 12 so that
the cationic polymer precipitates on the surface of the toner.
Preparation of display medium. The two colors of particles
were mixed with DOW 200 5cSt (5 centistokes) fluid, a polydimethylsiloxane polymer
available from Dow Corning, in a 1:1 mass ratio for a solids loading of about 25%.
Zirconia beads were added as mixing aids to evenly disperse the mixture of particles
in the fluid. No additional external charge control agents were added. The ink was
sandwiched between 2 parallel plates separated by a 145 µm spacer gasket. A
square wave voltage of +/- 200V was applied to the two plates, and the color transition
was observed as the two toners migrated back and forth between the two plates.
The charge of the particles enables rapid particle translation
in an electric field, and very fast response to changes in the electric field. The
device may be switched at rates of about 15 to about 20 Hz or more. As a result,
the electrophoretic display may be used for video display, as the device exhibits
switching rates suitable for video rates, which require a frame rate of up to 30
fps (standard video rate).
In this example, use of a silicone fluid as a fluid in
a display medium with emulsion aggregation particles is demonstrated.
Two colors of emulsion aggregation toner particles were
mixed with DOW 200 5cSt fluid, in a 1: 1 mass ratio for a solids loading of about
25%. Zirconia beads were added as mixing aids to evenly disperse the mixture of
toner particles in the fluid. No additional external charge control agents were
The display medium was sandwiched between two parallel
plates separated by a 145 µm spacer gasket. A square wave voltage of +/- 200V
was applied to the two plates, and color transition was observed as the two toners
migrated back and forth between the two plates.
Incorporation of maleic anhydride into an emulsion aggregation
particle at the latex step. To a bulk polymerized styrene/butylacrylate (200 ml,
~20% conversion, Mn = 1,900) was added maleic anhydride (16 g). The mixture was
heated to ~50°C until all the maleic anhydride dissolved. This was added to
an aqueous solution (600 g water and sodium dodecylbenzenesulfonate (SDBS), 16 g)
and stirred for 5 minutes. The resulting mixture was piston homogenized 3 times
at 500 BAR and then transferred to a 1L BUCHI reactor. Pressurizing with argon and
then depressurizing (5 times) deoxygenated the latex mini-emulsion. This was then
heated to 135°C. After 1 hour at temperature, a solution of ascorbic acid (8.5
ml of a 0.1 g/ml concentration) was added via pump at the rate of 0.03 5 ml/minute.
The reaction was cooled after 6 hours to afford a resin in the latex of~200 microns
with a solids content of 24.9% and Mn=9,700 and Mw=23,000.
Aggregation of latex using diamines. To a stable free radical
polymerization latex (707 g, 23.48% solids content) was added 660 ml of water and
pigment (cyan blue, BTD-FX-20, 47.8 g). This was stirred at room temperature and
a diamine (JEFFAMINE D-400, 6.89 g in 100 ml water) was added over a 10 minute period.
The resulting thickened suspension was heated to 55°C over a 1 hour period.
The suspension was then basified using NaOH (concentrated) to a pH of 7.3. This
was subsequently heated to 95°C over a 2 hour period and maintained at temperature
for 5 hours. The suspension was then cooled, filtered, and washed 5 times with water
until the filtrate conductivity was less than 15 microSiemens/cm2. The
resulting powder was resuspended in minimal water and freeze dried to give 130 g
of a 13.4 µm particle.
Incorporation of maleic anhydride into an emulsion aggregation
particle at the bulk polymerization step. A stock solution of styrene (390 mL) and
butylacrylate (110 ml) was prepared and to 400 ml was added TEMPO (3.12 g, 0.02
mole) and vazo 64 initiator (2.0 g, 0.0125 mole). This was heated under a nitrogen
atmosphere to 135°C (bath temperature) and then added to it dropwise a solution
of maleic anhydride (9.8 g) in 100 mL of the styrene/butylacrylate stock solution
that had been deoxygenated using nitrogen. The addition was done over a 30 minute
period after which it was stirred for 5 more minutes and then cooled to afford a
poly(styrene/maleic anhydride-b-styrene/butylacrylate) (Mn = 4,990 with PD=1.23)
solution in styrene/butylacrylate monomer.
Preparation of poly(SMA-b-S/BA) latex. A polymer solution
of the above (300 ml), styrene (117 ml), butylacrylate (33 ml) and TEMPO (0.6 g)
was added to a solution of SDBS (36 g, 1.21 water) and stirred for 5 minutes. Then
the mixture was piston homogenized once at a pressure of about 500 BAR and then
discharged into a 2L BUCHI reactor. This was heated to 135°C (reactor temperature)
and when the reactor reached temperature a solution of ascorbic acid (2.4 g in 12
ml water) was added dropwise at a rate of 0283 ml/minute for a total of 8.5 ml.
After 6 hours at reaction temperature the reactor was cooled and 1,401.3 g of latex
was discharged affording a poly(styrene/maleic anhydride-b-styrene/butylacrylate)
(Mn = 39,168 with a polydispersity (PD) = 1.64).
Aggregation/coalescence of latex using diamine as aggregant.
To the above latex (50 ml) was added 50 ml of water and stirred at room temperature
while adjusting the pH to -1.78. To this was added dropwise 2.89 g of a JEFFAMINE
D400 solution (20% w/w in water) at 23-25°C and then slowly heated up to 60°C
over ~1 hour. The particle size grew from about 200 nm to 6.8 µm. The solution
pH was adjusted to pH 9.04 with dilute NaOH and then further heated slowly to 95°C
over the course of ~1. 5 hour and maintained at temperature for 1. 5 hours to afford
a coalesced white particle of 6.68 µm size (Mn = 39,168).
Preparation of positively charged emulsion aggregation
polyester toner particles.
Comparative Example (Control): A pilot plant batch of toner
comprised of a linear sulfonated polyester resin (12% solids) (the composition of
the polyester resin consists of approximately an equimolar amount of glycol monomers
and aromatic diester molecules), 9% carnauba wax dispersion and 6% by weight of
FLEXIVERSE BLUE (Pigment Blue 15:3, BFD1121, 47.1% solids) dispersion (Sun Chemical
Co.) was prepared. Aggregation of cyan polyester toner particles was done at 58°C
in a 30-gallon stainless steel reactor (of which only 20 kg of the toner yield was
used for bench scale studies). The agitation rate was set initially to 100 RPM.
A 5% zinc acetate solution was added as the coagulant, where 60-80% of the total
zinc acetate solution was added quickly (600 g/min for the first 30 minutes) and
the remainder (80-100 g/min thereafter) is added at a reduced rate. The amount of
zinc acetate equaled approximately 11% of the total resin in the emulsion. After
7 hours of aggregation, the particle size reached 5.24 µm with a geometric
standard deviation (GSD) of 1.2. Full cooling was applied and particles were sieved
at 30-35°C through a 25 µm nylon filter bag. A portion of the toner slurry
was washed in the lab three times with deionized water after mother liquor removal,
resuspended to approximately 25% by weight solids and freeze-dried for 48 hours
to give the untreated parent toner.
Example: EUDRAGIT EPO solution (1%) was prepared by dissolving
1.26 g in 124.7 g of 0.3 M HNO3; the pH of the solution was lowered to
about 2 by adding 1.0 M HNO3. Lowering the pH to 2 ensured complete solubility
of the polymer in solution. The total percentage of EPO to toner was to equal 3%
by weight of dry toner.
The above pilot plant toner was treated in the lab via
a pH shifting procedure where EPO is soluble or insoluble in aqueous solution depending
on the pH of the aqueous solution. A 327 g quantity of the aqueous toner suspension
(12.89% by weight solids), which was separated from its mother liquor, was stirred
in a 1L glass Erlenmeyer flask on a stir plate at 250 - 300 rpm. The pH of the toner
slurry was lowered from 5.5 to 2.4 with 0.3 M HNO3. The EPO solution
was added drop wise to the toner slurry and stirred for 1 hour at room temperature.
After 1 hour, the pH of the toner slurry was increased to 12.2 with 1.0 M NaOH and
left to stir overnight at 300 under ambient temperature. The surface treated toner
was then filtered and washed four times. The filtercake was then resuspended to
approximately 25% by weight solids and freeze-dried. The pH of the filtrates was
always greater than 9.5 and showed no sign of precipitated EPO; it can be assumed
that all EPO polymer was transferred to the toner surface. The charge on these particles
was measured to be about 0.8 µC/g.
Preparation of multilayer coating on emulsion aggregation
Cationic layer: 20 g of yellow emulsion aggregation polyester
toner in which the base resin is a linear polyester containing about 3.75 mol% sulphonation,
the aggregating agent is Zn(OAc)2, and the pigment if YFD from Sun Chemicals,
was dispersed in 920 ml deionized water by mechanical stirring. 40 wt% NaCl solution
(ca 75 ml) was added to the solution, followed by 2 wt% poly(diallyldimethylammonium)
chloride (PDAD) (25 ml) (Mw of 100-200k). The overall solution contains 2 wt% toner
in 0.25M NaCl with 0.1 1 wt% PDAD. The solution was mechanically stirred for 1 hour,
filtered, and the wet toner cake was then washed with water (900 ml) for 3 times.
The particles exhibit a positive zeta potential, for example of about 15 mV, in
water, ISOPAR and silicone oil.
Anionic layer: The positively charged particles are redispersed
in 920 ml deionized water by mechanical stirring. 40 wt% NaCl solution (ca 75 ml)
was added to the solution, followed by 2 wt% poly(styrenesulfonate, sodium salt
(PSS) (25 ml) (Mw of <100k). The overall solution contains 2 wt% toner in 0.25M
NaCl with 0.1 wt% PSS. The solution was mechanically stirred for 1 hour, filtered,
and the wet toner cake was then washed with water (900 ml) for 3 times. The particles
exhibit a negative zeta potential, for example of about -25 mV, in water, ISOPAR
and silicone oil.
Multilayer formation: The positive PDAD and negative PSS
layers were then deposited in alternating manner until a desired number of layers
was formed, in this case 10 total layers. Each alternating layer exhibited the aforementioned
positive or negative zeta potential.
Preparation of multilayer coating on emulsion aggregation
Cationic layer: 10 g of cyan emulsion aggregation poly(styrene
acrylate) toner with 10% crosslinked gel content was dispersed in 400 ml deionized
water by mechanical stirring. 40 wt% NaCl solution and 2 wt% PDAD (25 ml) (Mw of
100-200k) was added to the solution. The overall solution comprised 0.25M NaCl and
0.1 wt% PDAD. The solution was mechanically stirred for 1 hour, filtered, and the
wet toner cake was then washed with water (900 ml) for 3 times. The particles exhibit
a positive zeta potential in water, ISOPAR and silicone oil.
Anionic layer: The positively charged particles are redispersed
in 400 ml deionized water by mechanical stirring. 40 wt% NaCl solution was added
to the solution, followed by 2 wt% (PSS) (25 ml) (Mw of <100k). The overall solution
comprised 0.25M NaCl and 0.1 wt% PSS. The solution was mechanically stirred for
1 hour, filtered, and the wet toner cake was then washed with water (900 ml) for
3 times. The particles exhibit a negative zeta potential in water, ISOPAR and silicone
Multilayer formation: The positive PDAD and negative PSS
layers were then deposited in alternating manner until a desired number of layers
was formed, in this case 4 total layers.
Preparation of highlight color emulsion aggregation toner
Preparation of crosslinked latex B. A crosslinked latex
emulsion comprised of polymer particles generated from the emulsion polymerization
of styrene, butyl acrylate and beta carboxy ethyl acrylate (&bgr;-CEA) was prepared
as follows. A surfactant solution of 4.08 kilograms of NEOGEN™
RK (anionic emulsifier) and 78.73 kilograms of deionized water was prepared by mixing
these components for 10 minutes in a stainless steel holding tank. The holding tank
was then purged with nitrogen for 5 minutes before transferring the resulting mixture
into the above reactor. The reactor was then continuously purged with nitrogen while
the contents were being stirred at 100 RPM. The reactor was then heated up to 76°C,
and held there for a period of 1 hour.
Separately, 1.24 kilograms of ammonium persulfate initiator
was dissolved in 13.12 kilograms of deionized water. Also separately, monomer emulsion
was prepared in the following manner. 47.39 Kilograms of styrene, 25.52 kilograms
of butyl acrylate, 2.19 kilograms of &bgr;-CEA, 2.92 kilogram of divinyl benzene
(DVB) crosslinking agent, 1.75 kilograms of NEOGEN™ RK (anionic surfactant),
and 145.8 kilograms of deionized water were mixed to form an emulsion. One (1) percent
of the emulsion was then slowly fed into the reactor, while the reactor was being
purged with nitrogen, containing the aqueous surfactant phase at 76°C to form
seeds. The initiator solution was then slowly charged into the reactor and after
40 minutes the remainder of the emulsion was continuously fed in using metering
pumps over a period of 3 hours.
Once all the monomer emulsion was charged into the above
main reactor, the temperature was held at 76°C for an additional 4 hours to
complete the reaction. Cooling was then accomplished and the reactor temperature
was reduced to 35°C. The product was collected into a holding tank. After drying,
the resin latex onset Tg was 53.5°C. The resulting latex was comprised of 25
percent crosslinked resin, 72.5 percent water and 2.5 percent anionic surfactant.
The resin had a ratio of 65:35:3 pph:4 pph of styrene:butyl acrylate:&bgr;-CEA:DVB.
The mean particle size of the gel latex was 50 nanometers as measured on disc centrifuge,
and the resin in the latex possessed a crosslinking value of about 50 percent as
measured by gravimetric method.
Toner preparation. Preparation of a Blue toner (PB. 15.0)
- highlight blue. 310.0 Grams of the above prepared latex emulsion (Latex A) and
100 grams of an aqueous blue pigment dispersion containing 36.8 grams of Blue pigment
(PB 15.0) available from Sun Chemical Corporation, having a solids loading of 54.0
percent, were simultaneously added to 500 milliliters of water with high shear stirring
by means of a polytron. To this mixture was added a 23.5 grams (grams) of polyaluminum
chloride (PAC) solution containing 3.5 grams of 10 percent solids and 20 grams of
0.2 molar nitric acid, over a period of 2 minute, followed by the addition of 23.5
grams of cationic surfactant solution containing 3.5 grams of the coagulant SANIZOL
B™ (60 percent active ingredients) and 20 grams of deionized water and blended
at speed of 5,000 rpm for a period of 2 minutes. The resulting mixture was transferred
to a 2 liter reaction vessel and heated at a temperature of 50°C for 210 minutes
hours resulting in aggregates of a size of 5.7 microns and a GSD of 1.22 To this
toner aggregate was added 150 grams of the above prepared latex (latex B) followed
by stirring for an additional 30 minutes and the particle size was found to be 5.8
and a GSD of 1.20. The pH of the resulting mixture was then adjusted from 2.6 to
7.5 with aqueous base solution of 4 percent sodium hydroxide and allowed to stir
for an additional 15 minutes. Subsequently, the resulting mixture was heated to
90°C and retained there for a period of 1 hour where the particle size measured
was 5.9 microns and a GSD of 1.20, followed by the reduction of the pH to 4.5 with
2.5 percent nitric acid solution. The resultant mixture was then allowed to coalesce
for an additional 5 hrs. The morphology of the particles was spherical particles.
The particle size was 6 microns with a GSD of 1.2. The reactor was then cooled down
to room temperature and the particles were washed 4 times, where the first wash
was conducted at pH of 11, followed by two washes with deionized water, and the
last wash carried out at a pH of 4. The particles were then dried. The charge on
these particles was measured to be about 0.02 to 0.15 µC/g.
Preparation of crosslinked emulsion aggregation particles.
Following the completion of a standard preparation of an emulsion (a latex (colloidal
dispersion in water) of very small seed particles made of polystyrene/butyl acrylate
copolymer), the temperature is lowered to about 60°C and the emulsion particle
swollen with a solution of multifunctional acrylates and photoinitiator. The multifunctional
acrylate solution consisted of 4 parts 1,6-hexanediol diacrylate (Sartomer SR 238),
4 parts trimethylolpropane triacrylate (Sartomer SR 351), 2 parts pentaerythritol
tetraacrylate (Sartomer SR 295), and 0.2 parts BASF LUCIRIN TPO-L photoinitiator.
This solution is added gradually to the latex, which is 90 parts solids. Following
aggregation and coalescence, the suspended particles are crosslinked by circulating
the suspension by a UV light source under nitrogen, in this case a Super Mix Photochemical
Reaction Vessel (Model 7868 Ace Glass) equipped with an immersion well, lamp and
power source. Following irradiation, the particles are washed.
Polyester resin (SPAR II, a commercially available unsaturated
polyester resin available from DOW Chemical) (90 parts) is combined with the multifunctional
acrylate solution identified in the prior example in the same proportions. The mixture
is then taken through the polyester emulsion aggregation process and irradiated
as in Example 9.
Ten parts dipentaerythritol pentaacrylate (Sartomer SR
399), 90 parts Sartomer CN 959, a high viscosity (180,000 cPs) blend aliphatic urethane
diacrylate and monomer diluent, 0.2 parts BASF LUCIRIN TPO-L photoinitiator and
3 parts surfactant are emulsified using a high pressure piston homogenizer. The
emulsion is then used in aggregation and coalescence steps to produce particles.
The particles are then crosslinked as in Example 9 above.
Formation of a display device with a fabric mesh display
A 2.54 cm by 2.54 cm square of NITEX nylon fabric mesh
having a mesh opening size of 150 µm (available from Sefar America) is dipped
into a display medium comprised of two differently colored emulsion aggregation
colored particle sets in 5 cSt silicone fluid. Excess ink is allowed to drip off
of the sheet. Next, the sheet is placed on a square of ITO coated glass, and covered
with a top square of ITO coated glass. By sliding the top square of glass onto the
wet fabric mesh, air bubbles are removed from the film. Excess display medium is
removed from the edges of the sandwich structure, and a two-part epoxy is used to
seal the edges. A device showing two color states is acheived.
It will be appreciated that various of the above-disclosed
and other features and functions, or alternatives thereof, may be desirably combined
into many other different systems or applications. Also, various presently unforeseen
or unanticipated alternatives, modifications, variations or improvements therein
may be subsequently made by those skilled in the art, and are also intended to be
encompassed by the following claims.