[0001] This invention relates to dye-receiving elements used in thermal dye transfer, and
more particularly to receiving elements having microvoided supports.
[0002] In recent years, thermal transfer systems have been developed to obtain prints from
pictures which have been generated electronically from a color video camera. According
to one way of obtaining such prints, an electronic picture is first subjected to color
separation by color filters. The respective color-separated images are then converted
into electrical signals. These signals are then operated on to produce cyan, magenta
and yellow electrical signals. These signals are then transmitted to a thermal printer.
To obtain the print, a cyan, magenta or yellow dye-donor element is placed face-to-face
with a dye-receiving element. The two are then inserted between a thermal printing
head and a platen roller. A line-type thermal printing head is used to apply heat
from the back of the dye-donor sheet. The thermal printing head has many heating elements
and is heated up sequentially in response to the cyan, magenta and yellow signals.
The process is then repeated for the other two colors. A color hard copy is thus obtained
which corresponds to the original picture viewed on a screen. Further details of this
process and an apparatus for carrying it out are contained in U.S. Patent No. 4,621,271
by Brownstein entitled "Apparatus and Method For Controlling A Thermal Printer Apparatus,"
issued November 4,1986.
[0003] Dye-receiving elements used in thermal dye transfer generally comprise a polymeric
dye image-receiving layer coated on a support. Supports are required to have, among
other properties, adequate strength, dimensional stability, and heat resistance. For
reflective viewing, supports are also desired to be as white as possible. Cellulose
paper, synthetic paper, and plastic films have all been proposed for use as dye-receiving
element supports in efforts to meet these requirements. Recently, microvoided films
formed by stretching an orientable polymer containing an incompatible organic or inorganic
material have been suggested for use in dye-receiving elements. U.S. Patent 4,778,782
of Ito et al., for example, discloses supports comprising a microvoided film obtained
by stretching a translucent plastic film containing fine fillers such as clay or talc.
By this stretching, bonds between the polymers and fillers in the film are destroyed,
whereby microvoids are considered to be formed in the film. The microvoids lower the
density of the film and also make it appear white and opaque. European Patent Application
0 322 771 discloses dye-receiving element supports comprising a polyester film containing
polypropylene and minute closed cells within the film formed upon stretching.
[0004] A problem exists with the microvoided supports discussed above, however, in that
it is difficult to manufacture films with a high degree of microvoiding. A high degree
of microvoiding is desirable as this increases the heat insulating property of the
support, and thereby the thermal efficiency of the dye transfer. EP 0 322 771 Comparative
Example 4, for example, shows that a high degree of microvoiding in polyester/polypropylene
stretched films, as evidenced by a relatively low specific gravity, results in poor
mechanical strength and frequent breakage of the film during stretching. The lowest
apparent specific gravity for an operable film in EP 0 322 771 is 0.71 (Example 2).
[0005] It would be desirable to provide a dye image-receiving element for thermal dye transfer
with a manufacturable microvoided support which would provide superior thermal efficiency.
[0006] These and other objects of the invention are achieved in accordance with this invention
which comprises a dye-receiving element for thermal dye transfer comprising a support
having thereon a polymeric dye image-receiving layer characterized in that the support
comprises a continuous oriented polymer matrix having dispersed therein microbeads
of a cross-linked polymer coated with a slip agent and which are at least partially
bordered by void space.
[0007] The combination of cross-linked microbeads and a slip agent coating allows supports
with a relatively high degree of microvoiding to be manufactured. The cross-linking
of the microbead polymer provides resiliency and elasticity while the slip agent permits
easier sliding between the microbeads and the matrix polymer to result in more effective
microvoiding. This allows films with a higher void percentage and thereby greater
insulating effect to be manufactured. Such films have been found to be particularly
advantageous for thermal dye transfer applications as the greater insulating effect
results in greater dye transfer efficiency.
[0008] The receiving elements of the invention use supports comprising a continuous thermoplastic
polymer phase having dispersed therein microbeads of polymer which are at least partially
bordered by voids. The microbeads of polymer have a size of 2 microns to 30 microns,
preferably 5 to 20 microns, and are present in an amount of 5% to 50% by weight based
on the weight of continuous phase polymer. The voids occupy up to 60% by volume of
the support, preferably from 30% to 60% by volume. Larger beads generate a greater
amount of void space upon stretching of the supports, but result in a rougher support
surface. The use of smaller beads results in a smoother support surface, but they
do not generate as much void volume. To obtain a support with both a high void volume
and a smooth surface, a dual layer support may be made. The bulk of such a support
comprises a layer made with relatively large beads in order to generate a large void
volume, and this layer is coated with a smoothing layer containing relatively small
beads or no beads at all.
[0009] The matrix polymer contains the generally spherical polymer microbeads which, according
to one aspect of the invention, are cross-linked to the extent of having a resiliency
or elasticity at orientation temperatures of the matrix polymer such that a generally
spherical shape of the cross-linked polymer is maintained after orientation of the
matrix polymer. The supports according to this invention in the absence of additives
or colorants are very white, and are very resistant to wear, moisture, oil, tearing,
etc.
[0010] The supports are preferably in the form of a paper like sheet having a thickness
of 50 to 300 microns. Preferably, the supports are made by biaxial orientation using
procedures well known in the art.
[0011] The continuous phase polymer may be any article-forming polymer such as a polyester
capable of being cast into a film or sheet. The polyesters should have a glass transition
temperature between 50°C and 150°C, preferably 60-100°C, should be orientable, and
have an intrinsic viscosity of at least 0.5, preferably 0.6 to 0.9. Suitable polyesters
include those produced from aromatic, aliphatic or cyclo-aliphatic dicarboxylic acids
of 4-20 carbon atoms and aliphatic or alicyclic glycols having from 2-24 carbon atoms.
Examples of suitable dicarboxylic acids include terephthalic, isophthalic, phthalic,
naphthalene dicarboxylic acid, succinic, glutaric, adipic, azelaic, sebacic, fumaric,
maleic, itaconic, 1,4-cyclohexane-dicarboxylic, sodiosulfoisophthalic and mixtures
thereof. Examples of suitable glycols include ethylene glycol, propylene glycol, butanediol,
pentanediol, hexanediol, 1,4-cyclohexanedimethanol, diethylene glycol, other polyethylene
glycols and mixtures thereof. Such polyesters are well known in the art and may be
produced by well-known techniques, e.g., those described in U.S. Patents 2,465,319
and 2,901,466. Preferred continuous matrix polymers are those having repeat units
from terephthalic acid or naphthalene dicarboxylic acid and at least one glycol selected
from ethylene glycol, 1,4-butanediol and 1,4-cyclohexanedimethanol. Poly(ethylene
terephthalate), which may be modified by small amounts of other monomers, is especially
preferred. Polypropylene is also useful. Other suitable polyesters include liquid
crystal copolyesters formed by the inclusion of a suitable amount of a co-acid component
such as stilbene dicarboxylic acid. Examples of such liquid crystal copolyesters are
those disclosed in U.S. Patent Nos. 4,420,607, 4,459,402 and 4,468,510.
[0012] Suitable cross-linked polymers for the microbeads are polymerizable organic materials
which are members selected from the group consisting of an alkenyl aromatic compound
having the general formula

wherein Ar represents an aromatic hydrocarbon radical, or an aromatic halohydrocarbon
radical of the benzene series and R is hydrogen or the methyl radical; acrylate-type
monomers including monomers of the formula

wherein R is selected from the group consisting of hydrogen and an alkyl radical containing
from 1 to 12 carbon atoms and R′ is selected from the group consisting of hydrogen
and methyl; copolymers of vinyl chloride and vinylidene chloride, acrylonitrile and
vinyl chloride, vinyl bromide, vinyl esters having the formula

wherein R is an alkyl radical containing from 2 to 18 carbon atoms; acrylic acid,
methacrylic acid, itaconic acid, citraconic acid, maleic acid, fumaric acid, oleic
acid, vinylbenzoic acid; the synthetic polyester resins which are prepared by reacting
terephthalic acid and dialkyl terephthalics or ester-forming derivatives thereof,
with a glycol of the series HO(CH₂)
nOH,
wherein n is a whole number within the range of 2-10 and having reactive olefinic
linkages within the polymer molecule, the hereinabove described polyesters which include
copolymerized therein up to 20 percent by weight of a second acid or ester thereof
having reactive olefinic unsaturation and mixtures thereof, and a cross-linking agent
selected from the group consisting of divinylbenzene, diethylene glycol dimethacrylate,
diallyl fumarate, diallyl phthalate and mixtures thereof.
[0013] Examples of typical monomers for making the cross-linked polymer include styrene,
butyl acrylate, acrylamide, acrylonitrile, methyl methacrylate, ethylene glycol dimethacrylate,
vinyl pyridine, vinyl acetate, methyl acrylate, vinylbenzyl chloride, vinylidene chloride,
acrylic acid, divinylbenzene, arylamidomethylpropane sulfonic acid, vinyl toluene,
etc. Preferably, the cross-linked polymer is polystyrene or poly(methyl methacrylate).
Most preferably, it is polystyrene and the cross-linking agent is divinylbenzene.
[0014] Processes well known in the art yield non-uniformly sized particles, characterized
by broad particle size distributions. The resulting beads can be classified by screening
to produce beads spanning the range of the original distribution of sizes. Other processes
such as suspension polymerization, limited coalescence, directly yield very uniformly
sized particles. Suitable slip agents or lubricants include colloidal silica, colloidal
alumina, and metal oxides such as tin oxide and aluminum oxide. The preferred slip
agents are colloidal silica and alumina, most preferably, silica. The cross-linked
polymer having a coating of slip agent may be prepared by procedures well known in
the art. For example, conventional suspension polymerization processes wherein the
slip agent is added to the suspension is preferred. As the slip agent, colloidal silica
is preferred.
[0015] It is preferred to use the "limited coalescance" technique for producing the coated,
cross-linked polymer microbeads. This process is described in detail in U.S. Patent
No. 3,615,972. Preparation of the coated microbeads for use in the present invention
does not utilize a blowing agent as described in this patent, however.
[0016] The following is an example illustrating a procedure for preparing the cross-linked
polymeric microbeads coated with slip agent. In this example, the polymer is polystyrene
cross-linked with divinylbenzene. The microbeads have a coating of silica. The microbeads
are prepared by a procedure in which monomer droplets containing an initiator are
sized and heated to give solid polymer spheres of the same size as the monomer droplets.
A water phase is prepared by combining 7 liters of distilled water, 1.5 g potassium
dichromate (polymerization inhibitor for the aqueous phase), 250 g polymethylaminoethanol
adipate (promoter), and 350 g LUDOX® (a colloidal suspension containing 50% silica
sold by DuPont). A monomer phase is prepared by combining 3317g styrene, 1421 g divinylbenzene
(55% active crosslinking agent, the other 45% is ethyl vinyl benzene which forms part
of the styrene polymer chain) and 45 g VAZO 52® (a monomer-soluble initiator sold
by DuPont). The mixture is passed through a homogenizer to obtain 5 micron droplets.
The suspension is heated overnight at 52°C to give 4.3 kg of generally spherical microbeads
having an average diameter of approximately 5 microns with narrow size distribution
(2-10 microns size distribution). The mol proportion of styrene and ethyl vinyl benzene
to divinylbenzene is approximately 6.1%. The concentration of divinylbenzene can be
adjusted up or down to result in 2.5-50% (preferably 10-40%) crosslinking by the active
cross-linker. Of course, monomers other than styrene and divinylbenzene can be used
in similar suspension polymerization processes known in the art. Also, other initiators
and promoters may be used as known in the art. Also, slip agents other than silica
may also be used. For example, a number of LUDOX® colloidal silicas are available
from DuPont. LEPANDIN® colloidal alumina is available from Degussa. NALCOAG® colloidal
silicas are available from Nalco and tin oxide and titanium oxide are also available
from Nalco.
[0017] Normally, for the polymer to have suitable physical properties such as resiliency,
the polymer is crosslinked. In the case of styrene crosslinked with divinylbenzene,
the polymer is 2.5-50% cross-linked, preferably 20-40% cross-linked. By percent crosslinked,
it is meant the mol % of crosslinking agent based on the amount of primary monomer.
Such limited crosslinking produces microbeads which are sufficiently coherent to remain
intact during orientation of the continuous polymer. Beads of such crosslinking are
also resilient, so that when they are deformed (flattened) during orientation by pressure
from the matrix polymer on opposite sides of the microbeads, they subsequently resume
their normal spherical shape to produce the largest possible voids around the microbeads
to thereby produce articles with less density.
[0018] The microbeads are referred to herein as having a coating of a "slip agent". By this
term it is meant that the friction at the surface of the microbeads is greatly reduced.
Actually, it is believed this is caused by the silica acting as miniature ball bearings
at the surface. Slip agent may be formed on the surface of the microbeads during their
formation by including it in the suspension polymerization mix.
[0019] Microbead size is regulated by the ratio of silica to monomer. For example, the following
ratios produce the indicated size microbead:

[0020] The supports according to this invention are prepared by:
(a) forming a mixture of molten continuous matrix polymer and cross-linked polymer
wherein the cross-linked polymer is a multiplicity of microbeads uniformly dispersed
throughout the matrix polymer, the matrix polymer being as described hereinbefore,
the cross-linked polymer microbeads being as described hereinbefore,
(b) forming a shaped article from the mixture by extrusion, casting or molding,
(c) orienting the article by stretching to form microbeads of cross-linked polymer
uniformly distributed throughout the article and voids at least partially bordering
the microbeads on sides thereof in the direction, or directions of orientation.
[0021] The mixture may be formed by forming a melt of the matrix polymer and mixing therein
the cross-linked polymer. The cross-linked polymer may be in the form of solid or
semi-solid microbeads. Due to the incompatibility between the matrix polymer and cross-linked
polymer, there is no attraction or adhesion between them, and they become uniformly
dispersed in the matrix polymer upon mixing.
[0022] When the microbeads have become uniformly dispersed in the matrix polymer, a shaped
article is formed by processes such as extrusion, casting or molding. Examples of
extrusion or casting would be extruding or casting a film or sheet, and an example
of molding would be injection or reheat blow-molding a bottle. Such forming methods
are well known in the art. If sheets or film material are cast or extruded, it is
important that such article be oriented by stretching, at least in one direction.
Methods of unilaterally or bilaterally orienting sheet or film material are well known
in the art. Basically, such methods comprise stretching the sheet or film at least
in the machine or longitudinal direction after it is cast or extruded an amount of
1.5-10 times its original dimension. Such sheet or film may also be stretched in the
transverse or cross-machine direction by apparatus and methods well known in the art,
in amounts of generally 1.5-10 (usually 3-4 for polyesters and 6-10 for polypropylene)
times the original dimension. Such apparatus and methods are well known in the art
and are described in such U.S. Patent No. 3,903,234.
[0023] The voids, or void spaces, referred to herein surrounding the microbeads are formed
as the continuous matrix polymer is stretched at a temperature above the Tg of the
matrix polymer. The microbeads of crosslinked polymer are relatively hard compared
to the continuous matrix polymer. Also, due to the incompatibility and immiscibility
between the microbead and the matrix polymer, the continuous matrix polymer slides
over the microbeads as it is stretched, causing voids to be formed at the sides in
the direction or directions of stretch, which voids elongate as the matrix polymer
continues to be stretched. Thus, the final size and shape of the voids depends on
the direction(s) and amount of stretching. If stretching is only in one direction,
microvoids will form at the sides of the microbeads in the direction of stretching.
If stretching is in two directions (bidirectional stretching), in effect such stretching
has vector components extending radially from any given position to result in a doughnut-shaped
void surrounding each microbead.
[0024] The dye image-receiving layer of the receiving elements of the invention may comprise,
for example, a polycarbonate, a polyurethane, a polyester, polyvinyl chloride, poly(styrene-co-acrylonitrile),
poly(caprolactone) or mixtures thereof. The dye image-receiving layer may be present
in any amount which is effective for the intended purpose. In general, good results
have been obtained at a concentration of from 1 to 5 g/m². In a preferred embodiment
of the invention, the dye image-receiving layer is a polycarbonate. The term "polycarbonate"
as used herein means a polyester of carbonic acid and a glycol or a dihydric phenol.
Examples of such glycols or dihydric phenols are p-xylylene glycol, 2,2-bis(4-oxyphenyl)propane,
bis(4-oxyphenyl)methane, 1,1-bis(4-oxyphenyl)ethane, 1,1-bis(oxyphenyl)butane, 1,1-bis(oxyphenyl)cyclohexane,
2,2-bis(oxyphenyl)butane, etc. In a particularly preferred embodiment, a bisphenol-A
polycarbonate having a number average molecular weight of at least 25,000 is used.
Examples of preferred polycarbonates include General Electric LEXAN® Polycarbonate
Resin and Bayer AG MACROLON 5700®.
[0025] A dye-donor element that is used with the dye-receiving element of the invention
comprises a support having theron a dye containing layer. Any dye can be used in the
dye-donor employed in the invention provided it is transferable to the dye-receiving
layer by the action of heat. Especially good results have been obtained with sublimable
dyes such as

or any other dye conventionally used for thermal dye transfer such as the dyes disclosed
in U.S. Patent 4,541,830. The above dyes may be employed singly or in combination
to obtain a monochrome. The dyes may be used at a coverage of from 0.05 to 1 g/m²
and are preferably hydrophobic.
[0026] The dye in the dye-donor element is dispersed in a polymeric binder such as a cellulose
derivative, e.g., cellulose acetate hydrogenphthatate, cellulose acetate, cellulose
acetate propionate, cellulose acetate butyrate, cellulose triacetate; a polycarbonate;
poly(styrene-co-acrylonitrile), a poly(sulfone) or a poly(phenylene oxide). The binder
may be used at a coverage of from 0.1 to 5 g/m².
[0027] The dye layer of the dye-donor element may be coated on the support or printed thereon
by a printing technique such as a gravure process.
[0028] The reverse side of the dye-donor element can be coated with a slipping layer as
is known in the art to prevent the printing head from sticking to the dye-donor element.
Such a slipping layer would comprise a lubricating material such as a surface active
agent, a liquid lubricant, a solid lubricant or mixtures thereof, with or without
a polymeric binder. The amount of the lubricating material to be used in the slipping
layer depends largely on the type of lubricating material, but is generally in the
range of from 0.001 to 2 g/m². If a polymeric binder is employed, the lubricating
material is present in the range of 0.1 to 50 weight %, preferable 0.5 to 40, of the
polymeric binder employed.
[0029] As noted above, the dye-donor elements and receiving elements of the invention are
used to form a dye transfer image. Such a process comprises imagewise-heating a dye-donor
element as described above and transferring a dye image to a dye-receiving element
to form the dye transfer image.
[0030] The dye-donor element may be used in sheet form or in a continuous roll or ribbon.
If a continuous roll or ribbon is employed, it may have only one dye thereon or may
have alternating areas of different dyes, such as sublimable cyan, magenta, yellow,
black, etc., as described in U.S. Patent 4,541,830. Thus, one-, two- three- or four-color
elements (or higher numbers also) are included within the scope of the invention.
[0031] In a preferred embodiment, the dye-donor element comprises a poly(ethylene terephthalate)
support coated with sequential repeating areas of cyan, magenta and yellow dye, and
the above process steps are sequentially performed for each color to obtain a three-color
dye transfer image. Of course, when the process is only performed for a single color,
then a monochrome dye transfer image is obtained.
[0032] Thermal printing heads which can be used to transfer dye from the dye-donor elements
to the receiving elements are available commercially. There can be employed, for example,
a Fujitsu Thermal Head (FTP-040 MCSOO1), a TDK Thermal Head F415 HH7-1089 or a Rohm
Thermal Head KE 2008-F3.
[0033] A thermal dye transfer assemblage of the invention comprises:
a) a dye-donor element as described above, and
b) a dye-receiving element as described above,
the dye-receiving element being in a superposed relationship with the dye-donor element
so that the dye layer of the donor element is in contact with the dye image-receiving
layer of the receiving element.
[0034] The above assemblage comprising these two elements may be preassembled as an integral
unit when a monochrome image is to be obtained. This may be done by temporarily adhering
the two elements together at their margins. After transfer, the dye-receiving element
is then peeled apart to reveal the dye transfer image.
[0035] When a three-color image is to be obtained, the above assemblage is formed on three
occasions during the time when heat is applied by the thermal printing head. After
the first dye is transferred, the elements are peeled apart. A second dye-donor element
(or another area of the donor element with a different dye area) is then brought in
register with the dye-receiving element and the process repeated. The third color
is obtained in the same manner.
[0036] The following examples are provided to further illustrate the invention.
Preparation of Microvoided Supports
[0037] A Welders Engineering Twin Screw Compounding Extruder heated to 282°C was used to
mix polystyrene microbeads (sizes, crosslinking %, and slip agent coatings as indicated
in the table below) and poly(ethylene terephthalate)("PET", commercially available
as #7352 from Eastman Chemicals). Both components were metered into the compounder
and one pass was sufficient for dispersion of the beads into the PET matrix.
[0038] Cast sheets of the above bead/PET dispersion with a poly(ethylene terephthalate)
smoothing layer were coextruded using a Killion Sample Coextruder System (a 1.5 inch
Killion Extruder was used to produce the bead/PET melt stream, and a 1 inch Killion
Extruder was used for the PET smoothing layer meltstream). The two meltstreams at
282°C were fed into a 7 inch "coat-hanger" type single manifold die also heated at
282°C. As the coextruded sheet emerged from the die, it was cast onto a quenching
roll set at 55°C. The final dimensions of the continuous cast sheet were 18 cm wide
and 1270 microns thick. The bead/PET layer was 1016 microns thick and the PET smoothing
layer was 254 microns thick.
[0039] The cast sheet (18 x 18 cm) were then stretched at 110°C and 50 mm/sec using an Iwamoto
Seisakusho Co. LTD Model BIX7025 Sample stretcher first 3.75 times in the X-direction
and then 3.5 times in the Y-direction. The stretched sheets were annealed at 117-122°C
for 90 sec and were allowed to cool at room temperature, and were then removed from
the stretcher.
[0040] The following microvoided supports each with the indicated composite densities were
produced. Each support had the same PET smoothing layer of approximately 20 microns
thickness after stretching.

[0041] The void percentages were calculated using approximate densities of 1.4 g/cm³ for
PET and 1 g/cm³ for polystyrene.
[0042] Three control supports were also evaluated:
- C-1:
- Eastman Radiographic Intensifying Screen
(A non-microvoided support of poly(ethylene terephthalate) of 180 microns thickness,
1.41 g/cm³ density, containing approximately 8% titanium dioxide.)
- C-2:
- ICI Corp. MELINEX 571®
(A non-microvoided support of poly(ethylene terephthalate) of 180 microns thickness,
1.35 g/cm³ density, containing approximately 18% barium sulfate.)
- C-3:
- Oji Yuka Goseishi YUPO FPG150®
(A microvoided support of polypropylene of 150 microns thickness, 0.78 g/cm³ density,
containing calcium carbonate.)
Preparation of Dye-Receiving Elements
[0043] The smooth side of the microvoided supports were first coated with a subbing layer
of poly(acrylonitrile-co-vinylidene chloride-co-acrylic acid)(14:80:6 wt. ratio)(0.11
g/m²) from butanone. On top of this layer, a dye receiving layer of Bayer AG MAKROLON
5700® (a bis-phenol A polycarbonate) (2.9 g/m²), 3M Corp. FLUORAD FC-431® (a fluorinated
surfactant)(0.02 g/m²), and Dow Corning DC-510® Silicone Fluid (0.01 g/m²) was coated
from dichloromethane. Each control support was coated with the same dye-receiving
layer.
Preparation of Dye-Donor Elements
[0044] Cyan dye-donor elements were prepared by coating the following layers in the order
recited on a 6 µm poly(ethylene terephthalate) support:
1) A subbing layer of duPont TYZOR TBT® titanium tetra-n-butoxide (0.12 g/m²) from
1-butanol; and
2) A layer containing the cyan dye

and Shamrock Tech. S-363® (a micronized blend of hydrocarbon wax particles)(0.016
g/m²) in a cellulose acetate butyrate (17% acetyl and 28% butyryl) binder (0.66 g/m²)
coated from a cyclopentanone, toluene and methanol solvent mixture.
[0045] Magenta dye-donor elements were prepared by coating the following layers in the order
recited on a 6 µm poly(ethylene terephthalate) support:
1) A subbing layer of duPont TYZOR TBT® (0.12 g/m²) from 1-butanol; and
2) A layer containing the magenta dyes

and Shamrock Tech. S-363® (a micronized blend of hydrocarbon wax particles)(0.016
g/m²) in a cellulose acetate butyrate (17% acetyl and 28% butyryl) binder (0.40 g/m²)
coated from a cyclopentanone, toluene and methanol solvent mixture.
[0046] On the back sides of the cyan and magenta dye-donor elements was coated:
1) A subbing layer of duPont TYZOR TBT® (0.12 g/m²) from 1-butanol; and
2) A slipping layer of Acheson Colloids EMRALON 329® polytetrafluoroethylene dry film
lubricant (0.59 g/m²), Petrarch Systems PS-513® (an amino terminated polydimethyl
siloxane)(0.005 g/m²), BYK-Chemie BYK-320® (a polyoxyalkylene siloxane)(0.005 g/m²),
and Shamrock Tech. S-232® (a micronized blend of polyethylene and carnauba wax particles)(0.016
g/m²) coated from a n-propyl acetate, toluene, 2-propanol, and 1-butanol solvent mixture.
Evaluation of Dye-Transfer
[0047] The dye layer sides of cyan and magenta donor element strips of approximately 9 cm
x 12 cm in area were placed in contact with the image-receiving layer of receiving
elements of the same area. Each assemblage was fastened in the jaws of a stepper motor
driven pulling device, and laid on top of a 14 mm diameter rubber roller. A TDK Thermal
Head L-133 (No. 6-2R16-1) was pressed with a spring at a force of 3.6 kg against the
donor element side of the contacted pair pushing it against the rubber roller.
[0048] The imaging electronics were activated causing the pulling device to draw the assemblage
between the printing head and roller at 3.1 mm/sec. Coincidentally the resistive elements
in the thermal print head were pulsed at a per pixel pulse width of 8 msec to generate
a maximum density image. The voltage supplied to the print-head was approximately
25 V representing approximately 1.6 watts/dot (13. mjoules/dot).
[0049] After printing the dye images to maximum density, the receivers were separated from
the donors. The Status A Green transmission density of the magenta donors and the
Status A Red transmission density of the cyan donors were measured both before and
after dye transfer. The greater the change in transmission density, the greater the
amount of dye transferred to the receiver, demonstrating greater thermal efficiency.

[0050] The above data demonstrates that the use of the thermal dye transfer receiving elements
of the invention results in improved transfer efficiency as a greater amount of dye
is transferred from dye donor elements used with such receiving elements.