Background of the Invention
[0001] This invention relates to dry powder compositions suitable for use in electrographic
recording. More particularly, it relates to heat fusible and pressure fixable one
part developing powders that contain fluorinated carbon.
[0002] Known one-part developing powder formulations used in electrographic recording may
be either heat fusible or pressure fixable. Heat fusible developing powders are typically
fixed after image formation by raising the temperature of the powder to its melting
or softening point, causing the powder particles to coalesce, flow together, and adhere
to the substrate. Pressure fixable developing powders are typically fixed after image
formation by simply applying pressure to the powder particles causing them to coalesce
and adhere to the substrate.
[0003] Although both types of developing powders have been widely used and have enjoyed
commercial success, they suffer from certain disadvantages that are related to their
physical characteristics.
[0004] For example, the flow properties and developing characteristics of such powders are
affected by the nature of the carbon black used. It has been found that if electrically
resistive carbon black is employed, the powder has poor flow properties (i.e., it
cakes and resists flow), especially in conditions of high humidity. Generally, the
images produced with such powders have poor resolution, that is they exhibit fuzzy
edge definition and image "fill-in" (i.e., toner deposits inside of letters such as
A, B, D, 0).
[0005] Additionally, such powders frequently form clumps in conditions of high humidity
that may result in streaking on the finished copy. Still further, such powders are
susceptible to clogging in the development station leading to poor development and
transfer of the developing powder and consequently, poor copy quality.
[0006] Developing powders that employ conductive carbon-black also demonstrate poor flow
properties and produce images that have poor resolution. Moreover, only low concentrations
(e.g., about 0.5% by weight) of such carbon black can be utilized if an electrically
resistive developing powder is desired. However, low carbon black concentrations are
difficult to incorporate uniformly into the powder. Moreover, electrically conductive
carbon black is hydrophilic in nature and this aggravates the poor flow properties
of the developing powder compositions.
[0007] The foregoing disadvantages are overcome in the present invention. This is accomplished
through the incorporation of fluorinated carbon into the developing powder composition.
Summary of the Invention
[0008] In accordance with the present invention there is provided a flowable, dry powder
of particles that has a static conductivity of less than about 10-3 (and preferably
less than about 10
-10) ohm
-1 centimeter
1 in an electric field of 10,000 d.c. volts per centimeter. The dry powder comprises
(a) from about 30 to 80 (and preferably from about 35 to 45) parts by weight of a
thermoplastic binder that has a static conductivity of at most 10-12 ohm-1 centimeter-1, said binder being selected from the group consisting of waxes that have a melting
point in the range of about 45°C to 150°C (preferably between about 65°C and 125°C),
organic resins that have a softening point above about 60°C (preferably between about
120°C and 200°C), and mixtures of said waxes and resins; and correspondingly, from
about 70 to 20 (and preferably from about 65 to 55) parts by weight of a magnetically
responsive material; and
(b) from about 0.4 to 3 parts by weight per 100 parts by weight of (a) of fluorinated
carbon that has a degree of fluorination in the range of 10% to 63% (based upon the
weight of the carbon) and an average diameter below about 2 microns, and preferably
below about 100 millimicrons wherein said fluorinated carbon comprises a radially
dispersed layer or zone around the outer portions of the powder particles.
[0009] Preferably the fluorinated carbon preferably comprises from about 0.75 to 3 parts,
and most preferably from about 0.75 to 1.5 parts, by weight per 100 parts by weight
of (a), and is from about 15% to 30% fluorinated.
[0010] That static conductivity referred to herein is measured according to the technique
described at column 3, line 54 through column 4, line 47 of U.S. Patent 3,639,245.
The melting point referred to above is measured according to ASTM: D-127, while the
ring and ball softening point is measured according to ASTM:E28.
[0011] The powder of the present invention preferably comprises essentially spherical particles
wherein at least 95 number percent of the particles have a maximum dimension in the
range of about 4 to 30 microns.
[0012] The developing powder of the present invention possesses improved flow properties
and provides high resolution images. It does not significantly cake together even
in conditions of high humidity. The images produced from the powder are uniform, have
sharp edge definition, and exhibit virtually no image fill-in. Still further, backgrounding
i.e., background coloration caused by random deposition of developing powder particles
in non-image areas, is substantially reduced.
[0013] These results are achieved through the use of fluorinated carbon to at least partially
replace standard (i.e., non-fluorinated) carbon black. Fluorinated carbon is less
conductive than equivalent non-fluorinated carbon black. Consequently, a higher percentage
by weight of the fluorinated carbon can be employed to achieve a given conductivity,
thereby providing better uniformity in the final developing powder. Additionally,
fluorinated carbon is hydrophobic so that the developing powders of the invention
are less susceptible to the effects of moisture than are developing powders that employ
standard carbon.
[0014] Still further, the developing powder compositions of the invention become more negatively
charged during the copying process than do equivalent developing powders that employ
standard carbon. It is believed that this property accounts at least in part for the
ability of the developing powder compositions of the invention to provide such high
resolution images.
[0015] Although the use of fluorinated carbon in developing powder compositions has been
suggested, see, for example U.S. Patent 4,141,849 and Japanese application JA54-19343
published September 8, 1976, the present invention represents an improvement thereover.
These publications each disclose the use of graphite fluoride in two part developing
powder compositions (i.e., those that comprise a toner powder and a separate carrier).
The U.S. Patent specifies a minimum degree of fluorination of 50%, while the Japanese
application specifies a degree of fluorination in the range of 1 to 150%, based upon
the weight of the carbon. However, it has been found that such two part developing
powder compositions are not satisfactory. For example, such powders must rely on the
carrier particles to remove the toner powder from non-charged areas. Frequently, the
carrier does not do an effective job of this thereby giving rise to a significant
level of backgrounding. Furthermore, the developed images are frequently hollow, that
is, solid areas are not filled in, resulting in low fidelity development. Additionally,
copy quality degrades with time when two part developing powder compositions are employed.
This requires that the developing composition be purged and replaced by fresh material.
The developing powder composition of the present invention alleviates these problems.
Brief Description of The Drawings
[0016] The present invention will be better understood by reference to the accompanying
drawings wherein like reference numbers refer to the same elements throughout the
several views, and wherein each drawing is a photomicrograph at 8X magnification.
In the drawings
[0017] Figures 1 and 2 represent separate photomicrographs of copies of a graphic original
containing both typed and preprinted portions. The copy in Figure 1 was made using
a heat fusible developing powder of the invention, while the copy in Figure 2 was
made using a standard heat fusible developing powder. Both copies were made by a conventional
heat fusing copying process.
[0018] Figures 3 and 4 represent separate photomicrographs of copies of a graphic original
containing preprinted areas. The copy in Figure 3 was prepared using a pressure fixable
developing toner powder of the invention, while the copy in Figure 4 was prepared
using a standard pressure fixable developing powder. Both copies were made by a conventional
pressure fixing copying process.
Detailed Description of the Invention
[0019] Referring specifically to Figures 1 and 2, there are shown portions of electrostatic
copies prepared using heat fusible developing powders and conventional copying processes.
These Figures contain unmagnified typed areas 10 and 20; corresponding magnified typed
areas l0A and 20A; unmagnified preprinted areas 11 and 21; and corresponding magnified
preprinted areas 11A and 21A.
[0020] As can be seen by reference to areas l0A and 11A of Figure 1, typed characters 12A
and preprinted characters 13A do exhibit excellent resolution. They have well defined
edges 14A and virtually no image fill-in, see 15A. Additionally, the copies exhibit
virtually no backgrounding, see 16A.
[0021] The significant improvement in copy quality is shown by comparison of Figures 1 and
2. Thus, neither typed characters 22A nor preprinted characters 23A exhibit good resolution.
To the contrary, the characters have fuzzy edges 24A and a significant level of image-fill
in, see 25A. Furthermore, the copies exhibit a high degree of backgrounding, see 26A.
[0022] A comparison of Figures 3 and 4 further demonstrates the significant improvement
in copy quality achieved by the developing powders of the present invention. These
Figures contain magnified areas 30A and 40A.
[0023] The characters 31A in Figure 3 have sharper edges 32A, substantially less image fill-in
as shown at 33A than do characters 41A in Figure 4. Compare, for example edges 42A
and areas 43A of Figure 4. Moreover, characters 31A are more uniformly toned than
are characters 41A. See especially the a, c, d, and e.
[0024] Still further, the copy illustrated in Figure 3 demonstrates substantially less backgrounding
than does the copy illustrated in Figure 4. Compare especially areas 34A of Figure
3 with areas 44A of Figure 4.
[0025] These surprising results are achieved as a result of the use of fluorinated carbon
in the developing powder composition of the invention. The fluorinated carbon useful
in the invention comprises an inorganic compound made up of carbon chemically bonded
to fluorine by covalent bonds. The fluorinated carbon may comprise fluorinated graphite
(natural or artificial) or, alternatively, fluorinated petroleum coke, coal coke,
charcoal, carbon black, and mixtures thereof. Such materials are known as shown by,
for example, "Cermatic", 4(301) 1969; Denki Kagaku, 51, 756-761, 1963; Denki Kagaku,
35, 19-23, 1967.
[0026] Processes for the preparation of fluorinated carbon are known. For example, see "Cermatic",
supra, and other references. Other process for the preparation of fluorinated carbon
involve the direct fluorination of carbon at temperatures varying from ambient to
over 450°C. Fluorination is preferably carried out in an agitated reactor in an atmosphere
of fluorine plus an inert gas, although a non-agitated reactor may be employed if
desired.
[0027] The conditions utilized during fluorination in a agitated reactor may be varied so
as to obtain the desired degree of fluorination. Examples of such conditions, and
the degree of fluorination obtained, are set forth in Table 1. The carbon used to
obtain the data for this Table was Vulcan XC-72R, a conductive carbon black with a
maximum particle size of 30 millimicron sold by Cabot Corporation.

[0028] Other carbon materials may also be used in the present invention. Representative
of such materials are Conductex 950 (maximum particle size of 21 millimicron) sold
by Cities Service, Raven 1800 (maximum particle size of 18 millimicron) sold by Columbia
Chemicals, Ketjenblack EC sold by Noury, and Thermax MT sold by R. T. Vanderbilt.
[0029] The thermoplastic binder useful in the present invention has a static conductivity
as set forth above and is selected from waxes that have a melting point in the range
of 45°C to 150°C and organic resins that have a ring and ball softening point above
about 60°C. Waxes useful in the invention are normally selected from the group consisting
of aliphatic compounds such as waxes (natural or synthetic), fatty acids, metal salts
of fatty acids, hydroxylated fatty acids or amides, low molecular weight ethylene
homopolymers, or a mixture of two or more of these materials. Aromatic and polymeric
wax-like materials can also be used. All of these materials are well known in the
art.
[0030] Representative useful aliphatic waxes include paraffin wax, microcrystalline wax,
caranauba wax, montan wax, ouricury wax, ceresin wax, candellila wax, and sugar cane
wax.
[0031] Representative useful fatty acids include stearic acid, palmitic acid, and behenic
acid. Representative useful metal salts of fatty acids include aluminum stearate,
lead stearate, barium stearate, magnesium stearate, zinc stearate, lithium stearate,
and zinc palmitate. Representative amide hydroxy waxes include N(betahydroxyethyl)-ricinoleamide
(commercially available under the trade name "Flexricin 115"), N,N'ethylene-bis-ricinoleamide
(commercially available under the trade name "Flexricin 185"), N(2-hydroxyethyl)-12-hydroxystearamide
(commercially available under the trade name "Paracin 220"), and N,N'-ethylene-bis-12-hydroxystearamide
(commercially available under the trade name "Paracin 285").
[0032] Representative fatty acid derivatives include castor wax (glyceryl tris-12-hydroxy
stearate), methyl hydroxy stearate (commercially available under the trade name "Paracin
I"), ethylene glycol monohydroxy stearate (commercially available under the trade
name "Paracin 15") and hydroxy stearic acid.
[0033] Representative ethylene homopolymers include the low molecular weight polyethylenes
such as the Bareco Polywaxes such as Polywax 655, 1000, and 2000 sold by the Bareco
Division of Petrolite Corporation. Other ethylene homopolymers include oxidized, high
density, low molecular weight polyethylenes such as Polywax E-2018 and E-2020 sold
by Bareco Division of Petrolite Corporation; and the Epolene@ series of low molecular
weight polyethylene resins such as Epolene@ E-14 available from Eastman Chemical Products
Incorporated.
[0034] Representative useful aromatic wax-like materials include dicyclohexylphthalate,
diphenylphthalate and the Be Square series of waxes from the Bareco Division of Petrolite
Corporation, such as Be Square 195. The Be Square waxes are high melting point waxes
that consist of paraffines and naphthenic hydrocarbons.
[0035] Representative of organic resins useful as the thermoplastic binder are the polyamides
(e.g., "Versamid 950", commercially available from General Mills); polystyrenes (e.g.,
2000 mol. wt.); bisphenol A epoxy resins (e.g., "Epon 1004", commercially available
from Shell Chemical Corp); acrylic resins (e.g., "Elvacite 2044", and N-butyl methacrylate
commercially available from DuPont); vinyl resins such as polyvinyl butyral (e.g.,
"Butvar B72-A," commercially available from Monsanto Company), polyvinyl acetates
(e.g., "Gelva V-100", commercially available from Monsanto Company); vinyl copolymers
such as vinyl chloride/vinyl acetate (e.g., "VYHH", commercially available from Union
Carbide Corp.), ethylene/vinyl acetate copolymers; cellulose esters such as cellulose
acetate butyrate (e.g., "EAB-171-25", commercially available from Eastman Chemical
Products, Inc.), cellulose acetate propionate (e.g., "CAPPLES 70", commercially available
from Celanese Corp.); and cellulose ethers.
[0036] When a heat fusible developing powder is prepared the thermoplastic binder preferably
comprises the organic resin. Most preferably the organic resin has a softening point
between about 120°C and 200°C and comprises a bisphenol A epoxy resin.
[0037] When a pressure fixable developing powder is prepared, the thermoplastic binder may
comprise either the wax or a combination of the wax and the organic resin. Preferably
the weight ratio of organic resin to wax is in the range of about 0:1 to 1:1. Most
preferably ratio is about 0:1. In either event, the wax preferably is selected from
a microcrystalline wax, a low molecular weight polyethylene resin, or a combination
of both, while the organic resin, when present, comprises a bisphenol A epoxy resin.
[0038] The magnetically responsive material employed in the developing powder composition
preferably is homogeneously distributed throughout the binder. Additionally, it preferably
has an average major dimension of one micron or less. Representative examples of useful
magnetically responsive materials include magnetite, barium ferrite, nickel zinc ferrite,
chromium oxide, nickel oxide, etc.
[0039] Various other materials may also be usefully incorporated in or on the developer
composition particles of the present invention. Such materials include, for example,
colorants such as powdered flow agents, pigments and, dyes, plasticizers, etc.
[0040] Representative powdered flow agents inclue small size Si0
2 such as "Cab-O-Sil" sold by the Cabot Corporation and "Aerosil" R-972 sold by the
DeGussa Corporation.
[0041] Representative colorants are carbon blacks, particularly conductive carbon blacks.
These may be used in conjunction with the fluorinated carbon employed in the invention.
[0042] The developing powders of the invention may be prepared by known processing techniques.
Thus, for example, heat fusing developing powders may be prepared by the techniques
described in U.S. Patent 3,639,245 at column 5, lines 3 to 36. Pressure fixable developing
powders may be prepared by the techniques described in U.S. Patent 3,925,219 at column
4, lines 25-59. Preferably the powder particles are spherical.
[0043] In these processes, the fluorinated carbon is incorporated into the developing powder
in the same fashion as is the conductive particles referred to therein. The resultant
powder possesses a radially dispersed layer or zone of electrically conductive carbon.
[0044] The present invention is further illustrated by means of the following examples wherein
the term "parts" refers to parts by weight unless otherwise indicated.
EXAMPLE 1
[0045] Heat-fusible developing powders were prepared using the ingredients and amounts shown:

[0046] The "Epon" and the Magnetite were blended thoroughly on a conventional heated-roll
rubber mill. The resulting blend was pulverized in an attrition-type grinder and then
classified in a standard air centrifugal type machine. These particles were sharp
edged and pseudocubical in shape. They were spheroidized such that most of the particles
were transformed into sphere-like shapes or round-edged particles by the following
process. The mixture was fed to an air aspirator in a uniform stream of about 800
grams per hour. The aspirator sucked the particles into the air stream and dispersed
them forming an aerosol. The aerosol was directed at 90° into a heated air stream
the temperature of which was about 510-540°C. The powder was then allowed to settle
and was collected by filtration.
[0047] The spheroidized particles were combined with either the fluorinated or the non-fluorinated
carbon and then blended first at room temperature for 3 hours and then at 65°C for
about 8 hours. The carbon was then radially dispersed or embedded into the resin by
the spheroidization process described above except that the temperature of the hot
air stream was adjusted to 650°C and the powder was fed to the air stream at a rate
of about 36 kilograms per hour. The resultant developing powder compositions were
collected and classified so that 95% by weight of the product was greater than 6.5
microns average diameter and only 5% by weight was greater than 19 microns average
diameter.
[0048] The final step in the process was to blend 0.05 parts per hundred parts of developing
powder composition of a small size Si0
2 flow agent (i.e., Aerosil R-972 sold by the DeGussa Corporation with the composition.
The resultant compositions were tested for static conductivity. The results are given
in Table 2.

[0049] This data demonstrates that the use of fluorinated carbon enables a larger quantity
of conductive material to be employed in the developing powder compositions in order
to achieve a given static conductivity. This in turn provides improved flow characteristics
even under conditions of high humidity.
[0050] Each of the developing powder compositions was used in a conventional heat-fusing
copying process to provide images on a plain paper substrate. The developing powder
composition of Example la provided copies with images that were sharply defined and
had virtually no image fill-in. Additionally there was. virtually no backgrounding.
A photomicrograph of a copy prepared from the powder of Example la, is shown in Figure
1. The developing powder composition of Example lb provided cop. es with images that
were not sharply defined and had substantial amounts of image fill-in. Furthermore,
there was a significant degree of backgrounding. A photomicrograph of a copy prepared
from the powder of Example lb is shown in Figure 2.
EXAMPLE 2
[0051] A heat-fusible developing powder composition was prepared as described in Example
1 except that embedment was carried out at 430°C. The following ingredients and amounts
shown were used.

[0052] The resultant developing powder composition was classified so that 95% by weight
of the powder was greater than 8 microns average diameter and only 5% by weight was
greater than 20 microns average diameter. The static conductivity of the developing
powder was 2.8 x 10
-15 mhos/cm in a 10,000 volt/cm d.c. field. The developing powder was used in a heat-fusing
copying process to provide a copy with,well defined images and virtually no image
fill-in or backgrounding on a plain paper substrate.
EXAMPLE 3
[0053] Example 1 was repeated except that embedment was carried out at about 430°C. In Example
3a, 0.49 parts by weight of fluorinated Vulcan XC-72R (8.4% fluorination) was employed,
while in Example 3b, 0.42 parts by weight of non-fluorinated Vulcan XC-72R was used.
The static conductivity of the resultant developing powder compositions is reported
in Table 3.

[0054] When each of these compositions was employed in a heat fixing copying process to
produce images on a plain paper substrate, no difference could be seen between the
quality of the copies produced. Thus, in each case the images had poor edge definition
and a fair degree of image fill in. Consequently, this example demonstrates that the
Fluorinated carbon must have a degree of fluorination of at least 10%.
EXAMPLE 4
[0055] Pressure-fixable developing powders were prepared using the following ingredients
in the amounts stated:

[0056] The Polywax and the Be Square were first heated to melting after which the magnetite
was added, with stirring, and heated until a homogeneous dispersion was obtained.
The temperature of the dispersion was raised to 193°C and then sprayed through a nozzle
at a rate of about 91 kg/hr to Corm discrete particles. The particles were classified
so that 95% by weight were greater than 6.5 microns and no more than 5% by weight
were greater than 20 microns in average diameter.
[0057] The substantially spherical particles were then combined with the fluorinated or
non-fluorinated carbon black and blended for 3 hours at room temperature. The particles
were then spheroidized and the carbon embedded therein as described in Example 1.
Embedment was carried out at about 430°C.
[0058] The developing powder compositions were then classified so that 95% by weight of
the powder was greater than 6.5 microns average diameter and only 5% by weight was
greater than 20 microns average diameter. The static conductivities of these developing
powder compositions were measured and are reported in Table 4.

[0059] Each of the developing powder compositions was used in a pressure-fixing copying
process to provide images on a plain paper substrate. The developing powder composition
of Example 4a provided copies whose images were sharply defined and had virtually
no image fill-in. Moreover, the copies had virtually no backgrounding. A photomicrograph
of a copy prepared using the developing powder of Example 4a is shown in Figure 3.
The developing powder composition of Example 4b, on the other hand, provided copies
whose images had poor edge definition and a high degree of image fill-in. Additionally,
the background areas of the copies produced from the developing powder composition
of Example 4b had a high degree of backgrounding. A photomicrograph of a copy prepared
using the developing powders of Example 4b is shown in Figure 4.
EXAMPLE 5
[0060] Example 4 was repeated except that Vulcan XC-72R (1.6 parts by weight) that had a
degree of fluorination of 20.8% was utilized in Example 5a and 0.62 parts by weight
of non-fluorinated Vulcan XC-72R was used in Example 5b. The developing powder compositions
were classified so that 95% by weight of the powder was greater than 8 microns average
diameter and only 5% by weight was greater than 20 microns average diameter. The static
conductivity of the resultant developing powder compositions is reported in Table
5.

[0061] Each of the developing powder compositions was used in a pressure-fixing copying
process to provide images on a plain paper substrate. The developing powder composition
of Example 5a provided copies whose images were sharply defined and had virtually
no image fill-in. The copies exhibited little backgrounding. The developing powder
composition of Example 5b provided copies whose images were not sharply defined and
had substantial amounts of image fill-in. The copies exhibited substantial backgrounding.
EXAMPLE 6
[0062] Example 4 was repeated using the following ingredients in the amounts shown:

[0063] The developing powder compositions were classified so that 95% by weight of the powder
was greater than 8 microns average diameter and only 5% by weight was greater than
20 microns average diameter. The static conductivity of the resultant developing powder
compositions is reported in Table 6.

[0064] Each of the developing powder compositions was used in a pressure fixing copying
process to provide images on a plain paper substrate. The developing powder composition
of Example 6a provided copies whose images were sharply defined and had virtually
no image fill-in. The copies exhibited little backgrounding. The developing powder
composition of Example 6b provided copies whose images were not sharply defined and
had substantial amounts of image fill-in. The copies also exhibited substantial backgrounding.
EXAMPLE 7
[0065] Example 4 was repeated using the following ingredients in the amounts shown:

[0066] The resultant developing powder compositions were collected and classified so that
95% by weight of the products was greater than 8 microns average diameter and only
5% by weight was greater than 20 microns average diameter. The dynamic conductivities
of the resultant compositions are reported in Table 7.

[0067] Each of the developing powder compositions was used in a heat-fusing copy process
to provide images on a plain paper substrate. The developing powder composition of
Example 7a provided copies whose images were sharply defined and had virtually no
image fill-in. The copies exhibited very little backgrounding. The developing powder
composition of Example 7b provided copies whose images were not sharply defined and
had substantial amounts of image fill-in. The copies also exhibited substantial backgrounding.
EXAMPLE 8
[0068] A pressure-fixable developing powder was prepared as described in Example 4 using
the following ingredients in the amounts shown:

[0069] The resulting developing powder composition was collected and classified so that
95% by weight of the product was greater than 9 minus average diameter and only 5%
by weight was greater than 22 microns average diameter. The composition had a dynamic
conductivity of 5.3 x 10
-13 Mhos/cm in a 10,000 volt/cm electric fold. The composition was used in a heat fusing
copy process one claim per substrate and provided copies whose images were sharply
defined and exhibited virtually no image fill-in. Furthermore, the copies exhibited
very little backgrounding.
1. A flowable, dry powder of particles that has a static conductivity of less than
about 10-3 mhos per centimeter in an electric field of 10,000 d.c. volts per centimeter
comprising
(a) from about 30 to 80 parts by weight of a thermoplastic binder that has a static
conductivity of at most about 10 -12 mhos per centimeter, said binder being selected from the group consisting of waxes
that have a melting point in the range of about 45°C to 150°C, organic resins that
have a softening point above about 60°C, and mixtures of said waxes and said resins;
and correspondingly, from about 70 to 20 parts by weight of a magnetically responsive
material and
(b) from about 0.4 to 3 parts by weight per 100 parts by weight of (a) of fluorinated
carbon that has a degree of fluorination in the range of 10% to 63% and an average
diameter below about 2 microns; wherein said fluorinated carbon comprises a radially
dispersed zone around the outer portions of said powder particles.
2. A powder in accordance with claim 1 that has a static conductivity less than about
10 -10 mhos per centimeter in an electric field of 10,000 d.c. volts per centimeter.
3. A powder in accordance with either of the preceding claims wherein at least about
95 percent of said particles have a maximum dimension in the range of about 4 to 30
microns.
4. A powder in accordance with any one of claims 1, 2 and 3 wherein said particles
are essentially spherical.
5. A powder in accordance with any one of claims 1, 2, 3 and 4 wherein said fluorinated
carbon has an average diameter of below about 100 millimicrons.
6. A powder in accordance with any one of claims 1, 2, 3, 4 and 5 wherein said fluorinated
carbon comprises from about 0.75 to parts by weight per 100 parts by weight of (a)
and wherein said fluorinated carbon has a degree of fluorination in the range of 15%
to 30%.
7. A powder in accordance with claim 6 wherein (a) comprises from about 35 to 45 parts
by weight of said thermoplastic binder, and, correspondingly, from about 65 to 55
parts by weight of said magnetically responsive material.
8. A powder in accordance with any one of claims 1 to 7 wherein the weight ratio of
said organic resin to said wax in said binder is in tie range of about 0:1 to 1:1,
and wherein said powder is pressure-fixable.
9. A powder in accordance with any one of claims 1 to 8 wherein said binder comprises
said organic resin and wherein said powder is heat fusible.
10. A powder in accordance with any one of claims 1 to 9 wherein said fluorinated
carbon comprises fluorinated carbon black.