Field of the Invention
[0001] This invention relates to an improved processing method for developing and/or desilvering
originating photographic elements and display photographic elements.
Background of the Invention
[0002] The basic image-forming process of color photography comprises exposing a silver
halide photographic recording material to light, and chemically processing the material
to reveal a useable image. The fundamental steps of this processing typically entail:
(1) treating the exposed silver halide with a color developer wherein some or all
of the silver halide is reduced to metallic silver while an organic dye is formed
from the oxidized color developer; and (2) removing the silver metal thus formed and
any residual silver halide by the desilvering steps of bleaching, wherein the developed
silver is oxidized to silver salts, and fixing, wherein the silver salts are dissolved
and removed from the photographic material. The bleaching and fixing steps may be
performed sequentially or as a single step, which is discussed herein as blixing.
In some methods of color image formation, additional color or black & white development
steps, chemical fogging steps and ancillary stopping, washing, accelerating and stabilizing
steps may be employed.
[0003] In many situations, the useable image is provided to a customer by a multi-stage
method which involves exposing a light sensitive originating element to a scene, and
developing and desilvering that originating element to form a color image. The originating
element may, for example, be a color negative film or a motion picture negative film.
The resultant color image is then used to modulate the exposure of a light sensitive
display element, with optional enlargement, in a printer. The display element may,
for example, be a color paper, an intermediate film, or a motion picture projection
film. The exposed display element is then developed and desilvered to form a useful
color image which duplicates the original scene.
[0004] Originating elements are typically designed to allow good exposure with available
light under a wide variety of lighting conditions, that is, good sensitivity (speed/grain)
and dynamic range (long latitude and low gamma) are desired. Conversely, display elements
are typically designed so as to allow a full range of density formation after well
defined exposure and process conditions in a printer, that is, good image discrimination
(high density and low fog), low dynamic range (short latitude and high gamma) and
easy and consistent processing are desired. These greatly different needs are typically
met by providing originating and display elements that differ markedly in silver halide
content and composition as well as in the layer orders and types and quantities of
image forming chemicals employed in each. One major difference in composition is evidenced
in the use of silver iodobromide emulsions in the originating element, a color negative
film for example, for their high sensitivity and desirable image structure properties
and the use of silver chloride or silver chlorobromide emulsions in the display element,
a color paper for example, for their low sensitivity, short latitude and good developability,
as well as their ease of reproducible desilvering.
[0005] Silver chloride emulsions are generally known for their rapid development properties.
Once reduction of silver has started, the silver chloride will rapidly reduce to silver
in most common photographic developers. The problem with silver chloride emulsions
in originating elements has been that the initiation of development or the latent
image detection that precedes the rapid development is slow, thus silver chloride
emulsions tend to have low sensitivity with high gamma. While these characteristics
are suitable for print materials, camera origination materials, as already noted,
must be highly sensitive and have a long latitude with relatively low gamma such as
a typical color negative film. Silver chloride emulsions can only achieve the low
gamma and long latitude when they are developed for very short times or in very weak
developers. These short development times do not appear to be sufficient to detect
the latent image of the grains receiving the least exposure, thus the sensitivity
is very low when the gamma and latitude are at the desired level.
[0006] What is needed is a method of developing high chloride silver halide originating
photographic elements which takes advantage of the high speed development potential
of silver chloride emulsions while still providing the sensitivity, gamma and latitude
requirements of such an element.
Summary of the Invention
[0007] This invention provides a method of processing an exposed originating silver halide
color photographic element comprising developing the photographic element in a color
devoloper containing a p-phenylenediamine color developing agent, in the presence
of a 1-phenyl pyrazolidin-3-one type compound;
wherein the originating silver halide photographic element comprises a radiation
sensitive emulsion in reactive association with a development inhibitor releasing
compound and containing a silver halide grain population comprised of at least 50
mole percent chloride, based on total silver forming the grain population projected
area, wherein at least 50 percent of total grain projected area is accounted for by
intrinsically stable tabular grains
(1) bounded by {100} major faces having adjacent edge ratios of less than 10 and
(2) each having an aspect ratio of at least 2, and wherein the silver halide content
of the photographic element comprises at least 50 mole % silver chloride and no more
than 2 mole % silver iodide.
[0008] The enhanced latent image detection provided by this invention allows the use of
short development times and development inhibitor releasing couplers to produce a
low gamma, long latitude imaging material while still maintaining high sensitivity.
It further allows emulsions to rapidly achieve their maximum sensitivity before rapid
and complete grain development takes place. The pyrazolidin compounds of this invention
increase photographic speed as much as 0.6 log E for development times of 1 minute
or less.
[0009] Development of silver chloride based films for short times or in weak developers
has several added advantages such as rapid access and low replenishment rates leading
to a more ecological process. The short development time and rapid latent image detection
also allows development inhibitor releasing couplers to be more effective at reducing
gamma and inducing interimage effects which can improve both color reproduction and
sharpness.
Brief Description of the Figures
[0010]
Figure 1 is a shadowed photomicrograph of carbon grain replicas of an emulsion of
the invention and
Figure 2 is a shadowed photomicrograph of carbon grain replicas of a control emulsion.
Detailed Description of the Invention
[0011] The originating silver halide photographic elements of this invention allow good
exposure with available light under a wide variety of lighting conditions. They provide
good speed with low graininess. At a minimum the originating elements of this invention
have an ISO speed rating of 25 or greater, with greater than 50 being preferred.
[0012] The speed or sensitivity of color negative photographic materials is inversely related
to the exposure required to enable the attainment of a specified density above fog
after processing. Photographic speed for color negative films with a gamma of about
0.65 has been specifically defined by the American National Standards Institute (ANSI)
as ANSI Standard Number PH 2.27 - 1979 (ASA speed) and relates to the exposure levels
required to enable a density of 0.15 above fog in the green light sensitive and least
sensitive recording unit of a multicolor negative film. This definition conforms to
the International Standards Organization (ISO) film speed rating.
[0013] It is appreciated that according to the above definition, speed depends on film gamma.
Color negative films intended for other than direct optical printing may be formulated
or processed to achieve a gamma greater or less than 0.65. For the purposes of this
application, the speeds of such films are determined by first linearly amplifying
or deamplifying the achieved density vs log exposure relationship (i.e. the gamma)
to a value of 0.65 and then determining the speed according to the above definitions.
[0014] The photographic emulsions used in the originating element may include, among others,
silver chloride, silver bromochloride, silver bromide, silver iodobromochloride, silver
iodochloride or silver iodobromide. Silver chloride and silver bromochloride emulsions
are preferred. Whatever the emulsion mix, the originating photographic element must
contain at least about 50 mole % silver chloride, with 70 mole % being preferrred
and over 98 mole % being most preferred. The total amount of silver iodide in the
photographic element must be less than about 2 mole %, and preferrably less than 1
mole %. The total amount of coated silver may be from about 1 to about 10 grams per
square meter, with less than 7 grams per square meter preferred, and less than 4 grams
per square meter being most preferred.
[0015] The originating photographic elements of this invention contain at least one radiation
sensitive silver halide emulsion containing a dispersing agent and a high chloride
silver halide grain population. At least 50 percent of total grain projected area
of the high chloride grain population is accounted for by tabular grains which (1)
are bounded by {100} major faces having adjacent edge ratios of less than 10 and (2)
each have an aspect ration of at least 2. The tabular grains of this invention are
intrinsically stable and do not require the use of stabilizers such as thiirane, thiepine,
thiophene, thiazole and other such cyclic sulfides; mercaptoacetic acids, cysteine,
penicillamine and other thiols; and acetylthiophenol and related thioesters and thiocarbanimides
to maintain their shape. Such stabilizers may restrain development.
[0016] It has further been discovered that the use of a certain class of development inhibitors
can inhibit the desilvering of the originating photographic elements of this invention.
Development inhibitors typically comprise a silver halide binding group having a sulfur,
selenium, tellurium or heterocyclic nitrogen or carbon with a free valence that can
form a bond to silver atoms, as well as a ballast moiety. Originating photographic
elements which contain development inhibitors having a sulfur with a free valence
that can form a bond to a silver atom appear to desilver more slowly than those containing
other classes of development inhibitors or no development inhibitor. Therefore, with
this invention it is preferred to use development inhibitors with a heterocyclic nitrogen
as a silver binding group, such as oxazoles, thiazoles, diazoles, triazoles, oxadiazoles,
thiadiazoles, oxathiazoles, thiatriazoles, benzotriazoles, tetrazoles, benzimidazoles,
indazoles, isoindazoles, benzodiazolesor benzisodiazoles. Development inhibitors having
a sulfur with a free valence can, however, have other advantages and may be utilized
in limited quantities which do not greatly effect desilvering.
[0017] The identification of emulsions satisfying the requirements of the invention and
the significance of the selection parameters can be better appreciated by considering
a typical emulsion. Figure 1 is a shadowed photomicrograph of carbon grain replicas
of a representative emulsion of the invention, described in detail in Example 1 below.
It is immediately apparent that most of the grains have orthogonal tetragonal (square
or rectangular) faces. The orthogonal tetragonal shape of the grain faces indicates
that they are {100} crystal faces.
[0018] The projected areas of the few grains in the sample that do not have square or rectangular
faces are noted for inclusion in the calculation of the total grain projected area,
but these grains clearly are not part of the tabular grain population having {100}
major faces.
[0019] A few grains may be observed that are acicular or rod-like grains (hereinafter referred
as rods). These grains are more than 10 times longer in one dimension than in any
other dimension and can be excluded from the desired tabular grain population based
on their high ratio of edge lengths. The projected area accounted for by the rods
is low, but, when rods are present, their projected area is noted for determining
total grain projected area.
[0020] The grains remaining all have square or rectangular major faces, indicative of {100}
crystal faces. To identify the tabular grains it is necessary to determine for each
grain its ratio of ECD to thickness (t)-i.e., ECD/t. ECD is determined by measuring
the projected area (the product of edge lengths) of the upper surface of each grain.
From the grain projected area the ECD of the grain is calculated. Grain thickness
is commonly determined by oblique illumination of the grain population resulting in
the individual grains casting shadows. From a knowledge of the angle of illumination
(the shadow angle) it is possible to calculate the thickness of a grain from a measurement
of its shadow length. The grains having square or rectangular faces and each having
a ratio of ECD/t of at least 2 are tabular grains having {100} major faces. When the
projected areas of the {100} tabular grains account for at least 50 percent of total
grain projected area, the emulsion is a tabular grain emulsion.
[0021] In the emulsion of Figure 1 tabular grains account for more than 50 percent of total
grain projected area. From the definition of a tabular grain above, it is apparent
that the average aspect ratio of the tabular grains can only approach 2 a minimum
limit. In fact, tabular grain emulsions of the invention typically exhibit average
aspect ratios of 5 or more, with high average aspect ratios (>8) being preferred.
That is, preferred emulsions according to the invention are high aspect ratio tabular
grain emulsions. In specifically preferred emulsions according to the invention average
aspect ratios of the tabular grain population are at least 12 and optimally at least
20. Typically the average aspect ratio of the tabular grain population ranges up to
50, but higher aspect ratios of 100, 200 or more can be realized. Emulsions within
the contemplation of the invention in which the average aspect ratio approaches the
minimum average aspect ratio limit of 2 still provide a surface to volume ratio that
is 200 percent that of cubic grains.
[0022] The tabular grain population can exhibit any grain thickness that is compatible with
the average aspect ratios noted above. However, particularly when the selected tabular
grain population exhibits a high average aspect ratio, it is preferred to additionally
limit the grains included in the selected tabular grain population to those that exhibit
a thickness of less than 0.3 µm and, optimally, less than 0.2 µm. It is appreciated
that the aspect ratio of a tabular grain can be limited either by limiting its equivalent
circular diameter or increasing its thickness. Thus, when the average aspect ratio
of the tabular grain population is in the range of from 2 to 8, the tabular grains
accounting for at least 50 percent of total grain projected area can also each exhibit
a grain thickness of less than 0.3 µm or less than 0.2 µm. Nevertheless, in the aspect
ratio range of from 2 to 8 particularly, there are specific photographic applications
that can benefit by greater tabular grain thicknesses. For example, in constructing
a blue recording emulsion layer of maximum achievable speed it is specifically contemplated
that tabular grain thicknesses that are on average 1 µm or or even larger can be tolerated.
This is because the eye is least sensitive to the blue record and hence higher levels
of image granularity (noise) can be tolerated without objection. There is an additional
incentive for employing larger grains in the blue record in that it is sometimes difficult
to match in the blue record the highest speeds attainable in the green and red record.
A source of this difficulty resides in the blue photon deficiency of sunlight. While
sunlight on an energy basis exhibits equal parts of blue, green and red light, at
shorter wavelengths the photons have higher energy. Hence on a photon distribution
basis daylight is slightly blue deficient.
[0023] The tabular grain population preferably exhibits major face edge length ratios of
less than 5 and optimally less than 2. The nearer the major face edge length ratios
approach 1 (i.e., equal edge lengths) the lower is the probability of a significant
rod population being present in the emulsion. Further, it is believed that tabular
grains with lower edge ratios are less susceptible to pressure desensitization.
[0024] In one specifically preferred form of the invention the tabular grain population
accounting for at least 50 percent of total grain projected area is provided by tabular
grains also exhibiting 0.2 µm. In other words, the emulsions are in this instance
thin tabular grain emulsions.
[0025] Surprisingly, ultrathin tabular grain emulsions have been prepared satisfying the
requirements of the invention. Ultrathin tabular grain emulsions are those in which
the selected tabular grain population is made up of tabular grains having an average
thickness of less than 0.06 µm. Prior to the present invention the only ultrathin
tabular grain emulsions of a halide content exhibiting a cubic crystal lattice structure
known in the art contained tabular grains bounded by {111} major faces. In other words,
it was thought essential to form tabular grains by the mechanism of parallel twin
plane incorporation to achieve ultrathin dimensions. Emulsions according to the invention
can be prepared in which the tabular grain population has a mean thickness down to
0.02 µm and even 0.01 µm. Ultrathin tabular grains have extremely high surface to
volume ratios. This permits ultrathin grains to be photographically processed at accelerated
rates. Further, when spectrally sensitized, ultrathin tabular grains exhibit very
high ratios of speed in the spectral region of sensitization as compared to the spectral
region of native sensitivity. For example, ultrathin tabular grain emulsions according
to the invention can have entirely negligible levels of blue sensitivity, and are
therefore capable of providing a green or red record in a photographic product that
exhibits minimal blue contamination even when located to receive blue light.
[0026] The characteristic of tabular grain emulsions that sets them apart from other emulsions
is the ratio of grain ECD to thickness (t). This relationship has been expressed quantitatively
in terms of aspect ratio. Another quantification that is believed to assess more accurately
the importance of tabular grain thickness is tabularity:
where
T is tabularity;
AR is aspect ratio;
ECD is equivalent circular diameter in micrometers (µm); and
t is grain thickness in micrometers.
The high chloride tabular grain population accounting for 50 percent of total grain
projected area preferably exhibits a tabularity of greater than 25 and most preferably
greater than 100. Since the tabular grain population can be ultrathin, it is apparent
that extremely high tabularities, ranging to 1000 and above are within the contemplation
of the invention.
[0027] The tabular grain population can exhibit an average ECD of any photographically useful
magnitude. For photographic utility average ECD's of less than 10 µm are contemplated,
although average ECD's in most photographic applications rarely exceed 6 µm. Within
ultrathin tabular grain emulsions satisfying the requirements of the invention it
is possible to provide intermediate aspect ratios with ECD's of the tabular grain
population of 0.10 µm and less. As is generally understood by those skilled in the
art, emulsions with selected tabular grain populations having higher ECD's are advantageous
for achieving relatively high levels of photographic sensitivity while selected tabular
grain populations with lower ECD's are advantageous in achieving low levels of granularity.
[0028] So long as the population of tabular grains satisfying the parameters noted above
accounts for at least 50 percent of total grain projected area a photographically
desirable grain population is available. It is recognized that the advantageous properties
of the emulsions of the invention are increased as the proportion of tabular grains
having {100} major faces is increased. The preferred emulsions according to the invention
are those in which at least 70 percent and optimally at least 90 percent of total
grain projected area is accounted for by tabular grains having {100} major faces.
It is specifically contemplated to provide emulsions satisfying the grain descriptions
above in which the selection of the rank ordered tabular grains extends to sufficient
tabular grains to account for 70 percent or even 90 percent of total grain projected
area.
[0029] So long as tabular grains having the desired characteristics described above account
for the requisite proportion of the total grain projected area, the remainder of the
total grain projected area can be accounted for by any combination of coprecipitated
grains. It is, of course, common practice in the art to blend emulsions to achieve
specific photographic objectives. Blended emulsions in which at least one component
emulsion satisfies the tabular grain descriptions above are specifically contemplated.
[0030] If tabular grains failing to satisfy the tabular grain population requirements do
not account for 50 percent of the total grain projected area, the emulsion does not
satisfy the requirements of the invention and is, in general, a photographically inferior
emulsion. For most applications (particularly applications that require spectral sensitization,
require rapid processing and/or seek to minimize silver coverages) emulsions are photographically
inferior in which many or all of the tabular grains are relatively thick-e.g., emulsions
containing high proportions of tabular grains with thicknesses in excess of 0.3 µm.
[0031] More commonly, inferior emulsions failing to satisfy the requirements of the invention
have an excessive proportion of total grain projected area accounted for by cubes,
twinned nontabular grains, and rods. Such an emulsion is shown in Figure 2. Most of
the grain projected area is accounted for by cubic grains. Also the rod population
is much more pronounced than in Figure 1. A few tabular grains are present, but they
account for only a minor portion of total grain projected area.
[0032] The tabular grain emulsion of Figure 1 satisfying the requirements of the invention
and the predominantly cubic grain emulsion of Figure 2 were prepared under conditions
that were identical, except for iodide management during nucleation. The Figure 2
emulsion is a silver chloride emulsion while the emulsion of Figure 1 additionally
includes a small amount of iodide.
[0033] Obtaining emulsions satisfying the requirements of the invention has been achieved
by the discovery of a novel precipitation process. In this process grain nucleation
occurs in a high chloride environment in the presence of iodide ion under conditions
that favor the emergence of {100} crystal faces. As grain formation occurs the inclusion
of iodide into the cubic crystal lattice being formed by silver ions and the remaining
halide ions is disruptive because of the much larger diameter of iodide ion as compared
to chloride ion. The incorporated iodide ions introduce crystal irregularities that
in the course of further grain growth result in tabular grains rather than regular
(cubic) grains.
[0034] It is believed that at the outset of nucleation the incorporation of iodide ion into
the crystal structure results in cubic grain nuclei being formed having one or more
screw dislocations in one or more of the cubic crystal faces. The cubic crystal faces
that contain at least one screw dislocation thereafter accept silver halide at an
accelerated rate as compared to the regular cubic crystal faces (i.e., those lacking
a screw dislocation). When only one of the cubic crystal faces contains a screw dislocation,
grain growth on only one face is accelerated, and the resulting grain structure on
continued growth is a rod. The same result occurs when only two opposite parallel
faces of the cubic crystal structure contain screw dislocations. However, when any
two contiguous cubic crystal faces contain a screw dislocation, continued growth accelerates
growth on both faces and produces a tabular grain structure. It is believed that the
tabular grains of the emulsions of this invention are produced by those grain nuclei
having two, three or four faces containing screw dislocations.
[0035] At the outset of precipitation a reaction vessel is provided containing a dispersing
medium and conventional silver and reference electrodes for monitoring halide ion
concentrations within the dispersing medium. Halide ion is introduced into the dispersing
medium that is at least 50 mole percent chloride-i.e., at least half by number of
the halide ions in the dispersing medium are chloride ions. The pCl of the dispersing
medium is adjusted to favor the formation of {100} grain faces on nucleation-that
is, within the range of from 0.5 to 3.5, preferably within the range of from 1.0 to
3.0 and, optimally, within the range of from 1.5 to 2.5.
[0036] The grain nucleation step is initiated when a silver jet is opened to introduce silver
ion into the dispersing medium. Iodide ion is preferably introduced into the dispersing
medium concurrently with or, optimally, before opening the silver jet. Effective tabular
grain formation can occur over a wide range of iodide ion concentrations ranging up
to the saturation limit of iodide in silver chloride. The saturation limit of iodide
in silver chloride is reported by H. Hirsch, "Photographic Emulsion Grains with Cores:
Part I. Evidence for the Presence of Cores", J. of Photog. Science, Vol. 10 (1962),
pp. 129-134, to be 13 mole percent. In silver halide grains in which equal molar proportions
of chloride and bromide ion are present up to 27 mole percent iodide, based on silver,
can be incorporated in the grains. It is preferred to undertake grain nucleation and
growth below the iodide saturation limit to avoid the precipitation of a separate
silver iodide phase and thereby avoid creating an additional category of unwanted
grains. It is generally preferred to maintain the iodide ion concentration in the
dispersing medium at the outset of nucleation at less than 10 mole percent. In fact,
only minute amounts of iodide at nucleation are required to achieve the desired tabular
grain population. Initial iodide ion concentrations of down to 0.001 mole percent
are contemplated. However, for convenience in replication of results, it is preferred
to maintain initial iodide concentrations of at least 0.01 mole percent and, optimally,
at least 0.05 mole percent.
[0037] In the preferred form of the invention silver iodochloride grain nuclei are formed
during the nucleation step. Minor amounts of bromide ion can be present in the dispersing
medium during nucleation. Any amount of bromide ion can be present in the dispersing
medium during nucleation that is compatible with at least 50 mole percent of the halide
in the grain nuclei being chloride ions. The grain nuclei preferably contain at least
70 mole percent and optimally at least 90 mole percent chloride ion, based on silver.
[0038] Grain nuclei formation occurs instantaneously upon introducing silver ion into the
dispersing medium. For manipulative convenience and reproducibility, silver ion introduction
during the nucleation step is preferably extended for a convenient period, typically
from 5 seconds to less than a minute. So long as the pCl remains within the ranges
set forth above no additional chloride ion need be added to the dispersing medium
during the nucleation step. It is, however, preferred to introduce both silver and
halide salts concurrently during the nucleation step. The advantage of adding halide
salts concurrently with silver salt throughout the nucleation step is that this permits
assurance that any grain nuclei formed after the outset of silver ion addition are
of essentially similar halide content as those grain nuclei initially formed. Iodide
ion addition during the nucleation step is particularly preferred. Since the deposition
rate of iodide ion far exceeds that of the other halides, iodide will be depleted
from the dispersing medium unless replenished.
[0039] Any convenient conventional source of silver and halide ions can be employed during
the nucleation step. Silver ion is preferably introduced as an aqueous silver salt
solution, such as a silver nitrate solution. Halide ion is preferably introduced as
alkali or alkaline earth halide, such as lithium, sodium and/or potassium chloride,
bromide and/or iodide.
[0040] It is possible, but not preferred, to introduce silver chloride or silver iodochloride
Lippmann grains into the dispersing medium during the nucleation step. In this instance
grain nucleation has already occurred and what is referred to above as the nucleation
step is in reality a step for introduction of grain facet irregularities. The disadvantage
of delaying the introduction of grain facet irregularities is that this produces thicker
tabular grains than would otherwise be obtained.
[0041] The dispersing medium contained in the reaction vessel prior to the nucleation step
is comprised of water, the dissolved halide ions discussed above and a peptizer. The
dispersing medium can exhibit a pH within any convenient conventional range for silver
halide precipitation, typically from 2 to 8. It is preferred, but not required, to
maintain the pH of the dispersing medium on the acid side of neutrality (i.e., <7.0).
To minimize fog a preferred pH range for precipitation is from 2.0 to 5.0. Mineral
acids, such as nitric acid or hydrochloride acid, and bases, such as alkali hydroxides,
can be used to adjust the pH of the dispersing medium. It is also possible to incorporate
pH buffers.
[0042] The peptizer can take any convenient conventional form known to be useful in the
precipitation of photographic silver halide emulsions and particularly tabular grain
silver halide emulsions. A summary of conventional peptizers is provided in
Research Disclosure, Vol. 308, December 1989, Item 308119, Section IX.
Research Disclosure is published by Kenneth Mason Publications, Ltd., Emsworth, Hampshire P010 7DD, England.
It is preferred to employ gelatino peptizers (e.g., gelatin and gelatin derivatives).
As manufactured and employed in photography gelatino peptizers typically contain significant
concentrations of calcium ion, although the use of deionized gelatino peptizers is
a known practice. In the latter instance it is preferred to compensate for calcium
ion removal by adding divalent or trivalent metal ions, such alkaline earth or earth
metal ions, preferably magnesium, calcium, barium or aluminum ions. Specifically preferred
peptizers are low methionine gelatino peptizers (i.e., those containing less than
30 micromoles of methionine per gram of peptizer), optimally less than 12 micromoles
of methionine per gram of peptizer. Generally at least about 10 percent and typically
from 20 to 80 percent of the dispersing medium forming the completed emulsion is present
in the reaction vessel at the outset of the nucleation step. It is conventional practice
to maintain relatively low levels of peptizer, typically from 10 to 20 percent of
the peptizer present in the completed emulsion, in the reaction vessel at the start
of precipitation. To increase the proportion of thin tabular grains having {100} faces
formed during nucleation it is preferred that the concentration of the peptizer in
the dispersing medium be in the range of from 0.5 to 6 percent by weight of the total
weight of the dispersing medium at the outset of the nucleation step. It is conventional
practice to add gelatin, gelatin derivatives and other vehicles and vehicle extenders
to prepare emulsions for coating after precipitation. Any naturally occurring level
of methionine can be present in gelatin and gelatin derivatives added after precipitation
is complete.
[0043] The nucleation step can be performed at any convenient conventional temperature for
the precipitation of silver halide emulsions. Temperatures ranging from near ambient-e.g.,
30°C up to about 90°C are contemplated, with nucleation temperatures in the range
of from 35 to 70°C being preferred.
[0044] Since grain nuclei formation occurs almost instantaneously, only a very small proportion
of the total silver need be introduced into the reaction vessel during the nucleation
step. Typically from about 0.1 to 10 mole percent of total silver is introduced during
the nucleation step.
[0045] A grain growth step follows the nucleation step in which the grain nuclei are grown
until tabular grains having {100} major faces of a desired average ECD are obtained.
Whereas the objective of the nucleation step is to form a grain population having
the desired incorporated crystal structure irregularities, the objective of the growth
step is to deposit additional silver halide onto (grow) the existing grain population
while avoiding or minimizing the formation of additional grains. If additional grains
are formed during the growth step, the polydispersity of the emulsion is increased
and, unless conditions in the reaction vessel are maintained as described above for
the nucleation step, the additional grain population formed in the growth step will
not have the desired tabular grain properties described above.
[0046] In its simplest form the process of preparing emulsions according to the invention
can be performed as a single jet precipitation without interrupting silver ion introduction
from start to finish. As is generally recognized by those skilled in the art a spontaneous
transition from grain formation to grain growth occurs even with an invariant rate
of silver ion introduction, since the increasing size of the grain nuclei increases
the rate at which they can accept silver and halide ion from the dispersing medium
until a point is reached at which they are accepting silver and halide ions at a sufficiently
rapid rate that no new grains can form. Although manipulatively simple, single jet
precipitation limits halide content and profiles and generally results in more polydisperse
grain populations.
[0047] It is usually preferred to prepare photographic emulsions with the most geometrically
uniform grain populations attainable, since this allows a higher percentage of the
total grain population to be optimally sensitized and otherwise optimally prepared
for photographic use. Further, it is usually more convenient to blend relatively monodisperse
emulsions to obtain aim sensitometric profiles than to precipitate a single polydisperse
emulsion that conforms to an aim profile.
[0048] In the preparation of emulsions according to the invention it is preferred to interrupt
silver and halide salt introductions at the conclusion of the nucleation step and
before proceeding to the growth step that brings the emulsions to their desired final
size and shape. The emulsions are held within the temperature ranges described above
for nucleation for a period sufficient to allow reduction in grain dispersity. A holding
period can range from a minute to several hours, with typical holding periods ranging
from 5 minutes to an hour. During the holding period relatively smaller grain nuclei
are Ostwald ripened onto surviving, relatively larger grain nuclei, and the overall
result is a reduction in grain dispersity.
[0049] If desired, the rate of ripening can be increased by the presence of a ripening agent
in the emulsion during the holding period. A conventional simple approach to accelerating
ripening is to increase the halide ion concentration in the dispersing medium. This
creates complexes of silver ions with plural halide ions that accelerate ripening.
When this approach is employed, it is preferred to increase the chloride ion concentration
in the dispersing medium. That is, it is preferred to lower the pCl of the dispersing
medium into a range in which increased silver chloride solubility is observed. Alternatively,
ripening can be accelerated and the percentage of total grain projected area accounted
for by {100} tabular grains can be increased by employing conventional ripening agents.
Preferred ripening agents are sulfur containing ripening agents, such as thioethers
and thiocyanates. Typical thiocyanate ripening agents are disclosed by Nietz et al.,
U.S. Patent 2,222,264; Lowe et al., U.S. Patent 2,448,534; and Illingsworth, U.S.
Patent 3,320,069, the disclosures of which are here incorporated by reference. Typical
thioether ripening agents are disclosed by McBride, U.S. Patent 3,271,157; Jones,
U.S. Patent 3,574,628; and Rosencrantz et al., U.S. Patent 3,737,313, the disclosures
of which are here incorporated by reference. More recently crown thioethers have been
suggested for use as ripening agents. Ripening agents containing a primary or secondary
amino moiety, such as imidazole, glycine or a substituted derivative, are also effective.
Sodium sulfite has also been demonstrated to be effective in increasing the percentage
of total grain projected accounted by the {100} tabular grains.
[0050] Once the desired population of grain nuclei have been formed, grain growth to obtain
the emulsions of the invention can proceed according to any convenient conventional
precipitation technique for the precipitation of silver halide grains bounded by {100}
grain faces. Whereas iodide and chloride ions are required to be incorporated into
the grains during nucleation and are therefore present in the completed grains at
the internal nucleation site, any halide or combination of halides known to form a
cubic crystal lattice structure can be employed during the growth step. Neither iodide
nor chloride ions need be incorporated in the grains during the growth step, since
the irregular grain nuclei faces that result in tabular grain growth, once introduced,
persist during subsequent grain growth independently of the halide being precipitated,
provided the halide or halide combination is one that forms a cubic crystal lattice.
This excludes only iodide levels above 13 mole percent (preferably 6 mole percent)
in precipitating silver iodochloride, levels of iodide above 40 mole percent (preferably
30 mole percent) in precipitating silver iodobromide, and proportionally intermediate
levels of iodide in precipitating silver iodohalides containing bromide and chloride.
When silver bromide or silver iodobromide is being deposited during the growth step,
it is preferred to maintain a pBr within the dispersing medium in the range of from
1.0 to 4.2, preferably 1.6 to 3.4. When silver chloride, silver iodochloride, silver
bromochloride or silver iodobromochloride is being deposited during the growth step,
it is preferred to maintain the pCl within the dispersing medium within the ranges
noted above in describing the nucleation step.
[0051] It has been discovered quite unexpectedly that up to 20 percent reductions in tabular
grain thicknesses can be realized by specific halide introductions during grain growth.
Surprisingly, it has been observed that bromide additions during the growth step in
the range of from 0.05 to 15 mole percent, preferably from 1 to 10 mole percent, based
on silver, produce relatively thinner {100} tabular grains than can be realized under
the same conditions of precipitation in the absence of bromide ion. Similarly, it
has been observed that iodide additions during the growth step in the range of from
0.001 to <1 mole percent, based on silver, produce relatively thinner {100} tabular
grains than can be realized under the same conditions of precipitation in the absence
of iodide ion.
[0052] During the growth step both silver and halide salts are preferably introduced into
the dispersing medium. In other words, double jet precipitation is contemplated, with
added iodide salt, if any, being introduced with the remaining halide salt or through
an independent jet. The rate at which silver and halide salts are introduced is controlled
to avoid renucleation-that is, the formation of a new grain population. Addition rate
control to avoid renucleation is generally well known in the art, as illustrated by
Wilgus, German OLS No. 2,107,118; Irie, U.S. Patent 3,650,757; Kurz, U.S. Patent 3,672,900;
Saito, U.S. Patent 4,242,445; Teitschied et al., European Patent Application 80102242;
and Wey, "Growth Mechanism of AgBr Crystals in Gelatin Solution",
Photographic Science and Engineering, Vol. 21, No. 1, Jan./Feb. 1977, p. 14,
et seq.
[0053] In the simplest form of the invention the nucleation and growth stages of grain precipitation
occur in the same reaction vessel. It is, however, recognized that grain precipitation
can be interrupted, particularly after completion of the nucleation stage. Further,
two separate reaction vessels can be substituted for the single reaction vessel described
above. The nucleation stage of grain preparation can be performed in an upstream reaction
vessel (herein also termed a nucleation reaction vessel) and the dispersed grain nuclei
can be transferred to a downstream reaction vessel in which the growth stage of grain
precipitation occurs (herein also termed a growth reaction vessel). In one arrangement
of this type an enclosed nucleation vessel can be employed to receive and mix reactants
upstream of the growth reaction vessel, as illustrated by Posse et al., U.S. Patent
3,790,386; Forster et al., U.S. Patent 3,897,935; Finnicum et al., U.S. Patent 4,147,551;
and Verhille et al., U.S. Patent 4,171,224, here incorporated by reference. In these
arrangements the contents of the growth reaction vessel are recirculated to the nucleation
reaction vessel.
[0054] It is herein contemplated that various parameters important to the control of grain
formation and growth, such as pH, pAg, ripening, temperature, and residence time,
can be independently controlled in the separate nucleation and growth reaction vessels.
To allow grain nucleation to be entirely independent of grain growth occurring in
the growth reaction vessel down stream of the nucleation reaction vessel, no portion
of the contents of the growth reaction vessel should be recirculated to the nucleation
reaction vessel. Preferred arrangements that separate grain nucleation from the contents
of the growth reaction vessel are disclosed by Mignot, U.S. Patent 4,334,012 (which
also discloses the useful feature of ultrafiltration during grain growth); Urabe,
U.S. Patent 4,879,208 and published European Patent Applications 326,852; 326,853;
355,535 and 370,116; Ichizo, published European Patent Application 0 368 275, Urabe
et al., published European Patent Application 0 374 954, and Onishi et al., published
Japanese Patent Application (Kokai) 172,817-A (1990).
[0055] Although the process of grain nucleation has been described above in terms of utilizing
iodide to produce the crystal irregularities required for tabular grain formation,
alternative nucleation procedures have been devised, demonstrated in the Examples
below, that eliminate any requirement of iodide ion being present during nucleation
in order to produce tabular grains. These alternative procedures are, further, compatible
with the use of iodide during nucleation. Thus, these procedures can be relied upon
entirely during nucleation for tabular grain formation or can be relied upon in combination
with iodide ion during nucleation to product tabular grains.
[0056] It has been observed that rapid grain nucleations, including so-called dump nucleations,
in which significant levels of dispersing medium supersaturation with halide and silver
ions exist at nucleation accelerate introduction of the grain irregularities responsible
for tabularity. Since nucleation can be achieved essentially instantaneously, immediate
departures from initial supersaturation to the preferred pCl ranges noted above are
entirely consistent with this approach.
[0057] It has also been observed that maintaining the level of peptizer in the dispersing
medium during grain nucleation at a level of less than 1 percent by weight enhances
of tabular grain formation. It is believed that coalescence of grain nuclei pairs
can be at least in part responsible for introducing the crystal irregularities that
induce tabular grain formation. Limited coalescence can be promoted by withholding
peptizer from the dispersing medium or by initially limiting the concentration of
peptizer. Mignot, U.S. Patent 4,334,012 illustrates grain nucleation in the absence
of a peptizer with removal of soluble salt reaction products to avoid coalescence
of nuclei. Since limited coalescence of grain nuclei is considered desirable, the
active interventions of Mignot to eliminate grain nuclei coalescence can be either
eliminated or moderated. It is also contemplated to enhance limited grain coalescence
by employing one or more peptizers that exhibit reduced adhesion to grain surfaces.
For example, it is generally recognized that low methionine gelatin of the type disclosed
by Maskasky II is less tightly absorbed to grain surfaces than gelatin containing
higher levels of methionine. Further moderated levels of grain adsorption can be achieved
with so-called "synthetic peptizers"--that is, peptizers formed from synthetic polymers.
The maximum quantity of peptizer compatible with limited coalescence of grain nuclei
is, of course, related to the strength of adsorption to the grain surfaces. Once grain
nucleation has been completed, immediately after silver salt introduction, peptizer
levels can be increased to any convenient conventional level for the remainder of
the precipitation process.
[0058] The emulsions of the invention include silver chloride, silver iodochloride emulsions,
silver iodobromochloride emulsions and silver iodochlorobromide emulsions. Dopants,
in concentrations of up to 10⁻² mole per silver mole and typically less than 10⁻⁴
mole per silver mole, can be present in the grains. Compounds of metals such as copper,
thallium, lead, mercury, bismuth, zinc, cadmium , rhenium, and Group VIII metals (e.g.,
iron, ruthenium, rhodium, palladium, osmium, iridium, and platinum) can be present
during grain precipitation, preferably during the growth stage of precipitation. The
modification of photographic properties is related to the level and location of the
dopant within the grains. When the metal forms a part of a coordination complex, such
as a hexacoordination complex or a tetracoordination complex, the ligands can also
be included within the grains and the ligands can further influence photographic properties.
Coordination ligands, such as halo, aquo, cyano cyanate, thiocyanate, nitrosyl, thionitrosyl,
oxo and carbonyl ligands are contemplated and can be relied upon to modify photographic
properties.
[0059] Dopants and their addition are illustrated by Arnold et al., U.S. Patent 1,195,432;
Hochstetter, U.S. Patent 1,951,933; Trivelli et al., U.S. Patent 2,448,060; Overman,
U.S. Patent 2,628,167; Mueller et al., U.S. Patent 2,950,972; McBride, U.S. Patent
3,287,136; Sidebotham, U.S. Patent 3,488,709; Rosecrants et al., U.S. Patent 3,737,313;
Spence et al., U.S. Patent 3,687,676; Gilman et al., U.S. Patent 3,761,267; Shiba
et al., U.S. Patent 3,790,390; Ohkubo et al., U.S. Patent 3,890,154; Iwaosa et al.,
U.S. Patent 3,901,711; Habu et al., U.S. Patent 4,173,483; Atwell, U.S. Patent 4,269,927;
Janusonis et al., U.S. Patent 4,835,093; McDugle et al., U.S. Patents 4,933,272; 4,981,781;
and 5,037,732; Keevert et al., U.S. Patent 4,945,035; and Evans et al., U.S. Patent
5,024,931, the disclosures of which are here incorporated by reference. For background
as to alternatives known to the art attention is directed to B. H. Carroll, "Iridium
Sensitization: A Literature Review",
Photographic Science and Engineering,Vol. 24, NO. 6, Nov./Dec. 1980, pp. 265-257, and Grzeskowiak et al., published European
Patent Application 0 264 288.
[0060] The invention is particularly advantageous in providing high chloride (greater than
50 mole percent chloride) tabular grain emulsions, since conventional high chloride
tabular grain emulsions having tabular grains bounded by {111} are inherently unstable
and require the presence of a morphological stabilizer to prevent the grains from
regressing to nontabular forms. Particularly preferred high chloride emulsions are
according to the invention that are those that contain more than 70 mole percent (optimally
more than 90 mole percent) chloride.
[0061] Although not essential to the practice of the invention, a further procedure that
can be employed to maximize the population of tabular grains having {100} major faces
is to incorporate an agent capable of restraining the emergence of non-{100} grain
crystal faces in the emulsion during its preparation. The restraining agent, when
employed, can be active during grain nucleation, during grain growth or throughout
precipitation.
[0062] Useful restraining agents under the contemplated conditions of precipitation are
organic compounds containing a nitrogen atom with a resonance stabilized p electron
pair. Resonance stabilization prevents protonation of the nitrogen atom under the
relatively acid conditions of precipitation.
[0063] Aromatic resonance can be relied upon for stabilization of the p electron pair of
the nitrogen atom. The nitrogen atom can either be incorporated in an aromatic ring,
such as an azole or azine ring, or the nitrogen atom can be a ring substituent of
an aromatic ring.
[0064] In one preferred form the restraining agent can satisfy the following formula:

where
Z represents the atoms necessary to complete a five or six membered aromatic ring
structure, preferably formed by carbon and nitrogen ring atoms. Preferred aromatic
rings are those that contain one, two or three nitrogen atoms. Specifically contemplated
ring structures include 2H-pyrrole, pyrrole, imidazole, pyrazole, 1,2,3-triazole,
1,2,4-triazole, 1,3,5-triazole, pyridine, pyrazine, pyrimidine, and pyridazine.
[0065] When the stabilized nitrogen atom is a ring substituent, preferred compounds satisfy
the following formula:

where
Ar is an aromatic ring structure containing from 5 to 14 carbon atoms and
R¹ and R² are independently hydrogen, Ar, or any convenient aliphatic group or
together complete a five or six membered ring. Ar is preferably a carbocyclic aromatic
ring, such as phenyl or naphthyl. Alternatively any of the nitrogen and carbon containing
aromatic rings noted above can be attached to the nitrogen atom of formula II through
a ring carbon atom. In this instance, the resulting compound satisfies both formulae
I and II. Any of a wide variety of aliphatic groups can be selected. The simplest
contemplated aliphatic groups are alkyl groups, preferably those containing from 1
to 10 carbon atoms and most preferably from 1 to 6 carbon atoms. Any functional substituent
of the alkyl group known to be compatible with silver halide precipitation can be
present. It is also contemplated to employ cyclic aliphatic substituents exhibiting
5 or 6 membered rings, such as cycloalkane, cycloalkene and aliphatic heterocyclic
rings, such as those containing oxygen and/or nitrogen hetero atoms. Cyclopentyl,
cyclohexyl, pyrrolidinyl, piperidinyl, furanyl and similar heterocyclic rings are
specifically contemplated.
[0066] The following are representative of compounds contemplated satisfying formulae I
and/or II: aniline, a-naphthylamine, b-naphthylamine, benzidine, carbazole, norharman,
pyrrole, indole, pyridine, quinoline, isoquinoline, acridine, 1,8-naphthyridine, 1,10-phenanthroline,
nicotine, benzoxazole, pyrazole, antipyrine, imidazole, indazole, pyrimidine, pyrazine,
2,2'-bipyrazine, pteridine, 1,2,3-triazole, 1,2,4-triazole, 3-amino-1,2,4-triazole,
3,5-diamino-1,2,4-triazole, benzotriazole, 1,2,4-triazine, and 1,3,5-triazine.
[0067] Selection of preferred restraining agents and their useful concentrations can be
accomplished by the following selection procedure: The compound being considered for
use as a restraining agent is added to a silver chloride emulsion consisting essentially
of cubic grains with a mean grain edge length of 0.3 µm. The emulsion is 0.2 M in
sodium acetate, has a pCl of 2.1, and has a pH that is at least one unit greater than
the pKa of the compound being considered. The emulsion is held at 75 °C with the restraining
agent present for 24 hours. If, upon microscopic examination after 24 hours, the cubic
grains have sharper edges of the {100} crystal faces than a control differing only
in lacking the compound being considered, the compound introduced is performing the
function of a restraining agent. The significance of sharper edges of intersection
of the {100} crystal faces lies in the fact that grain edges are the most active sites
on the grains in terms of ions reentering the dispersing medium. By maintaining sharp
edges the restraining agent is acting to restrain the emergence of non-{100} crystal
faces, such as are present, for example, at rounded edges and corners. In some instances
instead of dissolved silver chloride depositing exclusively onto the edges of the
cubic grains a new population of grains bounded by {100} crystal faces is formed.
Optimum restraining agent activity occurs when the new grain population is a tabular
grain population in which the tabular grains are bounded by {100} major crystal faces.
[0068] It is specifically contemplated to deposit epitaxially silver salt onto the tabular
grains acting as hosts. Conventional epitaxial depositions onto high chloride silver
halide grains are illustrated by Maskasky, U.S. Patent 4,435,501 (particularly Example
24B); Ogawa et al., U.S. Patents 4,786,588 and 4,791,053; Hasebe et al., U.S. Patents
4,820,624 and 4,865,962; Sugimoto and Miyake, "Mechanism of Halide Conversion Process
of Colloidal AgCl Microcrystals by Br⁻ Ions", Parts I and II,
Journal of Colloid and Interface Science, Vol. 140, No. 2, Dec. 1990, pp. 335-361; Houle et al., U.S. Patent 5,035,992; and
Japanese published applications (Kokai) 252649-A (priority 02.03.90-JP 051165 Japan)
and 288143-A (priority 04.04.90-JP 089380 Japan). The disclosures of the above U.S.
Patents are hereby incorporated by reference.
[0069] While any 1-phenyl pyrazolidin-3-one type compound may be used with this invention,
the more preferred compounds have the following Formulas I or II.

wherein:
R
8a is hydrogen;
R
8b and R
8c each independently represent a hydrogen, a substituted or unsubstituted alkyl group
having from 1 to 10 carbon atoms or a substituted or unsubstituted aryl group having
from 6 to 10 carbon atoms;
R
8d and R
8e each independently represent a hydrogen, a substituted or unsubstituted alkyl group
having from 1 to 10 carbon atoms or a substituted or unsubstituted aryl group having
from 6 to 10 carbon atoms; and
R
8f is independently a hydrogen, a halogen, a substituted or unsubstituted alkyl group
having from 1 to 8 carbon atoms, or a substituted or unsubstituted alkoxy group having
from 1 to 8 carbon atoms, or a sulfonamido group. R
8f may be present in the ortho, meta or para positions of the benzene ring. m is 1 to
3. When m is greater than 1, the R
8f substituents can be taken together to form a carbocyclic or a heterocyclic ring.
[0070] More preferably m is 2; the R
8f substituents are in the para and meta positions of the benzene ring and each is a
hydrogen or an alkoxy group having 1-4 carbon atoms, and R
8b and R
8c are each hydrogen or an alkyl group having 1-10 carbon atoms; provided that one of
R
8f is an alkoxy group or one of R
8b and R
8c is an alkyl group of 3-7 carbon atoms. Preferably at least one R
8f is an alkoxy group of 1-4 carbon atoms, R
8b is hydrogen or an alkyl group of 1-4 carbon atoms, and R
8c is hydrogen or a hydroxyalkyl group of 1-4 carbon atoms. The preferred compounds
for use are: 1-(4-methoxyphenyl)-3-pyrazolidone, 1-(3,4-dimethoxyphenyl)-3-pyrazolidone,
and 1-phenyl-4-n-pentylpryazolidone, with 1-(4-methoxyphenyl)-3-pyrazolidone being
most preferred.
[0071] The 1-phenyl pyrazolidin-3-one type compound may be present in the developer solution
at a concentration up to 5 g/l preferably in the range 0.05 to 0.5 g/l. It may also
be incorporated in the photographic element. When incorporated in the photographic
material it may be present in one or more layers thereof. When the compound is incorporated
in the photographic material, preferably it is in a form which is inactive until processing
takes place. For example, it could be inactivated by a blocking group which is hydrolysed
off when the material is immersed in the normally alkaline developing solution. The
compound could also be released from a coupler as a function of silver halide development.
[0072] Any developer which is suitable for use with low iodide, chloride containing elements
may be utilized with this invention. The color developing agent is a p-phenylenediamine.
The content of the color developing agent is generally 1 to 30 grams per liter of
the color developing solution, with 2 to 20 grams being more preferred and 3 to 10
grams being most preferred.
[0073] Examples of particularly useful p-phenylenediamines and especially the N-N-dialkyl-p-phenylenediamines
in which the alkyl groups or the aromatic nucleus can be substituted or unsubstituted
include: N-N-diethyl-p-phenylenediaminemonohydrochloride, 4-N,N-diethyl-2-methylphenylenediaminemonohydrochloride,
4-(N-ethyl-N-2-methanesulfonylaminoethyl)-2-methylphenylenediamine sesquisulfate monohydrate,
4-(N-ethyl-N-2-hydroxyethyl)-2-methylphenylenediamine sulfate, and 4-N, N-diethyl-2,
2'-methanesulfonylaminoethylphenylenediamine hydrochloride.
[0074] In addition to the primary aromatic amino color developing agent, the color developing
solutions used with this invention may contain a variety of other agents such as alkalies
to control pH, bromides, iodides, benzyl alcohol, anti-oxidants, anti-foggants, solubilizing
agents, brightening agents, and so forth.
[0075] The photographic color developing compositions may be employed in the form of aqueous
alkaline working solutions having a pH of above 7 and more preferably in the range
of from about 9 to about 13. To provide the necessary pH, they may contain one or
more of the well known and widely used pH buffering agents, such as the alkali metal
carbonates or phosphates. Potassium carbonate is especially preferred.
[0076] The originating element is desilvered after color development is performed. Desilvering
can be performed by one of the following methods (i) a method using a bleaching solution
bath and fixing solution bath; (ii) a method using a bleaching solution bath and a
blixing solution bath; (iii) a method using a blixing solution and a fixing solution
bath; and (iv) a method using a single blixing bath. Blixing may be preferred in order
to shorten the process time.
[0077] Examples of bleaching agents which may be used in the bleach solutions or blix solutions
of the current invention are ferric salts, persulfate, dichromate, bromate, red prussiate,
and salts of aminopolycaroxylic acid ferric complexes, with salts of aminopolycaroxylic
acid ferric complexes being preferred.
[0078] Preferred aminopolycarboxylic acid ferric complexes are listed below:
(1) ethylenediaminetetraacetic acid ferric complex;
(2) diethylenetriaminepentaacetic acid ferric complex;
(3) cyclohexanediaminetetraacetic acid ferric complex;
(4) iminodiacetic acid ferric complex;
(5) methyliminodiacetic acid ferric complex;
(6) 1,3-diaminopropanetetraacetic acid ferric complex;
(7) glycoletherdiaminetetraacetic acid ferric complex;
(8) beta-alanine diacetic acid ferric complex.
[0079] These aminopolycarboxylic acid ferric complexes are used in the form of a sodium
salt, potassium salt, or ammonium salt. An ammonium salt may be preferred for speed,
with alkali salts being preferred for environmental reasons.
[0080] The content of the salt of an aminopolycarboxylic acid ferric complex in the bleaching
solutions and blixing solutions of this invention is about 0.05 to 1 mol/liter. The
pH range of the bleaching solution is 2.5 to 7, and preferably 4.0 to 7.
[0081] The bleaching solution or the blixing solution can contain rehalogenating agents
such as bromides (e.g., potassium bromide, sodium bromide, and ammonium bromide),
chlorides (e.g., potassium chloride, sodium chloride, and ammonium chloride), and
iodides (e.g., ammonium iodide). They may also contain one or more inorganic and organic
acids or alkali metal or ammonium salts thereof, and, have a pH buffer such as boric
acid, borax, sodium methabrate, acetic acid, sodium acetate, sodium carbonate, potassium
carbonate, phosphorous acid, phosphoric acid, sodium phosphate, citric acid, sodium
citrate, and tartaric acid, or corrosion inhibitors such as ammonium mitrate and guanidine.
[0082] Examples of fixing agents which may be used in the this invention are water-soluble
solvents for silver halide such as: a thiosulfate (e.g., sodium thiosulfate and ammonium
thiosulfate); a thiocyanate (e.g., sodium thiocyanate and ammonium thiocyanate); a
thioether compound (e.g., ethylenebisthioglycolic acid and 3,6-dithia-1,8-octanediole);
and a thiourea. These fixing agents can be used singly or in a combination of at least
two agents. Thiosulfate is preferably used in the present invention.
[0083] The content of the fixing agent per liter is preferably about 0.2 to 2 mol. The pH
range of the blixing or fixing solution is preferably 3 to 10 and more preferably
5 to 9.
[0084] In order to adjust the pH of the fixing solution, hydrochloric acid, sulfuric acid,
nitric acid, acetic acid, bicarbonate, ammonia, potassium hydroxide, sodium hydroxide,
sodium carbonate, potassium carbonate,may be added.
[0085] The blixing and the fixing solution may also contain a preservative such as a sulfite
(e.g., sodium sulfite, potassium sulfite, and ammonium sulfite), a bisulfite (e.g.,
ammonium bisulfite, sodium bisulfite, and potassium bisulfite), and a metabisulfite
(e.g., potassium metabisulfite, sodium metabisulfite, and ammonium metabisulfite).
The content of these compounds is about 0 to 0.50 mol/liter, and more preferably 0.02
to 0.40 mol/liter as an amount of sulfite ion. Ascorbic acid, a carbonyl bisulfite,
acid adduct, or a carbonyl compound may also be used as a preservative.
[0086] It is known to those skilled in the art that numerous other auxillary processing
steps are often used including washing, stabilizing, rinsing, reversal processing
and neutralization. All of these processing steps may be utilized with the photographic
elements of this invention.
[0087] Apart from the features that have been specifically discussed previously for the
tabular grain emulsion preparation procedures and the tabular grains that they produce,
their further use in the color photographic elements of this invention can take any
convenient conventional form. Substitution in color photographic elements for conventional
emulsions of the same or similar silver halide composition is generally contemplated,
with substitution for silver halide emulsions of differing halide composition, particularly
other tabular grain emulsions, being also feasible. The low levels of native blue
sensitivity of the high chloride {100} tabular grain emulsions allows the emulsions
to be employed in any desired layer order arrangement in multicolor photographic elements,
including any of the layer order arrangements disclosed by Kofron et al., U.S. Patent
4,439,520, the disclosure of which is here incorporated by reference, both for layer
order arrangements and for other conventional features of photographic elements containing
tabular grain emulsions. Conventional features are further illustrated by the following
incorporated by reference disclosures:
- ICBR-1
- Research Disclosure, Vol. 308, December, 1989, Item 308,119;
- ICBR-2
- Research Disclosure, Vol. 225, January, 1983, Item 22,534;
- ICBR-3
- Wey et al., U.S. Patent 4,414,306, issued Nov. 8, 1983;
- ICBR-4
- Solberg et al., U.S. Patent 4,433,048, issued Feb. 21, 1984;
- ICBR-5
- Wilgus et al., U.S. Patent 4,434,226, issued Feb. 28, 1984;
- ICBR-6
- Maskasky, U.S: Patent 4,435,501, issued Mar. 6, 1984;
- ICBR-7
- Maskasky, U.S. Patent 4,643,966, issued Feb. 17, 1987;
- ICBR-8
- Daubendiek et al., U.S. Patent 4,672,027, issued Jan. 9, 1987;
- ICBR-9
- Daubendiek et al., U.S. Patent 4,693,964, issued Sept. 15, 1987;
- ICBR-10
- Maskasky, U.S. Patent 4,713,320, issued Dec. 15, 1987;
- ICBR-11
- Saitou et al., U.S. Patent 4,797,354, issued Jan. 10, 1989;
- ICBR-12
- Ikeda et al., U.S. Patent 4,806,461, issued Feb. 21, 1989;
- ICBR-13
- Makino et al., U.S. Patent 4,853,322, issued Aug. 1, 1989; and
- ICBR-14
- Daubendiek et al., U.S. Patent 4,914,014, issued Apr. 3, 1990.
[0088] Photographically useful group (PUG)-releasing compounds can be incorporated in photographic
elements of the present invention by means and processes known in the photographic
art. A photographic element in which the dye image-forming and PUG-releasing compounds
are incorporated can be a monocolor element comprising a support and a single silver
halide emulsion layer, or it can be a multicolor, multilayer element comprising a
support and multiple silver halide emulsion layers. The above described compounds
can be incorporated in at least one of the silver halide emulsion layers and/or in
at least one other layer, such as an adjacent layer, where they are in reactive association
with the silver halide emulsion layer and are thereby able to react with the oxidized
developing agent produced by development of silver halide in the emulsion layer. Additionally,
the silver halide emulsion layers and other layers of the photographic element can
contain addenda conventionally contained in such layers.
[0089] A typical multicolor, multilayer photographic element can comprise a support having
thereon a red-sensitized silver halide emulsion unit having associated therewith a
cyan dye image-forming compound, a green-sensitized silver halide emulsion unit having
associated therewith a magenta dye image-forming compound, and a blue-sensitized silver
halide emulsion unit having associated therewith a yellow dye image-forming compound.
Each silver halide emulsion unit can be composed of one or more layers, and the various
units and layers can be arranged in different locations with respect to one another,
as known in the prior art and as illustrated by layer order formats hereinafter described.
[0090] In an element of the invention, a layer or unit affected by PUG can be controlled
by incorporating in appropriate locations in the element a layer that confines the
action of PUG to the desired layer or unit. Thus, at least one of the layers of the
photographic element can be, for example, a scavenger layer, a mordant layer, or a
barrier layer. Examples of such layers are described in, for example, U.S. Patents
4,055,429; 4,317,892; 4,504,569; 4,865,946; and 5,006,451. The element can also contain
additional layers such as antihalation layers, filter layers and the like. The element
typically will have a total thickness, excluding the support, of from 5 to 30 m. Thinner
formulations of 5 to about 25 m are generally preferred since these are known to provide
improved contact with the process solutions. For the same reason, more swellable film
structures are likewise preferred. Further, this invention may be particularly useful
with a magnetic recording layer such as those described in
Research Disclosure, Item 34390, November, 1992, p. 869.
[0091] In the following discussion of suitable materials for use in the elements of this
invention, reference will be made to the previously mentioned
Research Disclosure, December, 1989, Item 308119, the disclosures of which are incorporated herein by
reference.
[0092] Suitable dispersing media for the emulsion layers and other layers of elements of
this invention are described in Section IX of
Research Disclosure, December, 1989, Item 308119, and publications therein.
[0093] In addition to the compounds described herein, the elements of this invention can
include additional dye image-forming compounds, as described in Sections VII A-E and
H, and additional PUG-releasing compounds, as described in Sections VII F and G of
Research Disclosure, December, 1989, Item 308119, and the publications cited therein.
[0094] The elements of this invention can contain brighteners (Section V), antifoggants
and stabilizers (Section VI), antistain agents and image dye stabilizers (Section
VII I and J), light absorbing and scattering materials (Section VIII), hardeners (Section
X), coating aids (Section XI), plasticizers and lubricants (Section XII), antistatic
agents (Section XIII), matting agents (Section XVI), and development modifiers (Section
XXI), all in
Research Disclosure, December, 1989, Item 308119.
[0095] The elements of the invention can be coated on a variety of supports, as described
in Section XVII of
Research Disclosure, December, 1989, Item 308119, and references cited therein.
[0096] The photographic elements containing radiation sensitive {100} tabular grain emulsion
layers according to this invention can be imagewise-exposed with various forms of
energy which encompass the ultraviolet and visible (e.g., actinic) and infrared regions
of the electromagnetic spectrum, as well as electron-beam and beta radiation, gamma
ray, X-ray, alpha particle, neutron radiation and other forms of corpuscular and wave-like
radiant energy in either noncoherent (random phase) forms or coherent (in phase) forms
as produced by lasers. Exposures can be monochromatic, orthochromatic or panchromatic.
Imagewise exposures at ambient, elevated or reduced temperatures and/or pressures,
including high- or low-intensity exposures, continuous or intermittent exposures,
exposure times ranging from minutes to relatively short durations in the millisecond
to microsecond range and solarizing exposures, can be employed within the useful response
ranges determined by conventional sensitometric techniques, as illustrated by T. H.
James, The
Theory of the Photographic Process, 4th Ed., Macmillan, 1977, Chapters 4, 6, 17, 18 and 23. The photographic elements
may then be processed to form a visible dye image, as described in Sections XVIII
and XIX of
Research Disclosure, December, 1989, Item 308119.
[0097] The following examples are intended to illustrate, without limiting, this invention.
Examples
[0098] The invention can be better appreciated by reference to the following examples. Throughout
the examples the acronym APMT is employed to designate 1-(3-acetamidophenyl)-5-mercaptotetrazole.
The term "low methionine gelatin" is employed, except as otherwise indicated, to designate
gelatin that has been treated with an oxidizing agent to reduce its methionine content
to less than 30 micromoles per gram. The acronym DW is employed to indicate distilled
water. The acronym mppm is employed to indicate molar parts per million.
[0099] The following compounds are used in the Examples.

Emulsion Preparation Example 1
[0100] This example demonstrates the preparation of an ultrathin tabular grain silver iodochloride
emulsion satisfying the requirements of this invention.
[0101] A 2030 mL solution containing 1.75% by weight low methionine gelatin, 0.011 M sodium
chloride and 1.48 x 10⁻⁴ M potassium iodide was provided in a stirred reaction vessel.
The contents of the reaction vessel were maintained at 40°C and the pCl was 1.95.
[0102] While this solution was vigorously stirred, 30 mL of 1.0 M silver nitrate solution
and 30 mL of a 0.99 M sodium chloride and 0.01 M potassium iodide solution were added
simultaneously at a rate of 30 mL/min each. This achieved grain nucleation to form
crystals with an initial iodide concentration of 2 mole percent, based on total silver.
[0103] The mixture was then held 10 minutes with the temperature remaining at 40°C. Following
the hold, a 1.0 M silver nitrate solution and a 1.0 M NaCl solution were then added
simultaneously at 2 mL/min for 40 minutes with the pCl being maintained at 1.95.
[0104] The resulting emulsion was a tabular grain silver iodochloride emulsion containing
0.5 mole percent iodide, based on silver. Fifty percent of total grain projected area
was provided by tabular grains having {100} major faces having an average ECD of 0.84
µm and an average thickness of 0.037 µm, selected on the basis of an aspect ratio
rank ordering of all {100} tabular grains having a thickness of less than 0.3 µm and
a major face edge length ratio of less than 10. The selected tabular grain population
had an average aspect ratio (ECD/t) of 23 and an average tabularity (ECD/t²) of 657.
The ratio of major face edge lengths of the selected tabular grains was 1.4. Seventy
two percent of total grain projected area was made up of tabular grains having {100}
major faces and aspect ratios of at least 7.5. These tabular grains had a mean ECD
of 0.75 µm, a mean thickness of 0.045 µm, a mean aspect ratio of 18.6 and a mean tabularity
of 488.
[0105] A representative sample of the grains of the emulsion is shown in Figure 1.
Emulsion Preparation Example 2 (Comparative)
[0106] This emulsion demonstrates the importance of iodide in the precipitation of the initial
grain population (nucleation).
[0107] This emulsion was precipitated identically to that of Example 1, except no iodide
was intentionally added.
[0108] The resulting emulsion consisted primarily of cubes and very low aspect ratio rectangular
grains ranging in size from about 0.1 to 0.5 µm in edge length. A small number of
large rods and high aspect ratio {100} tabular grains were present, but did not constitute
a useful quantity of the grain population.
[0109] A representative sample of the grains of this emulsion is shown in Figure 2.
Example 3
Emulsion Precipitations
Emulsion A: silver chloride cubic emulsion
[0110] A monodisperse silver chloride cube with a cubic edge length of 0.59 µm was prepared
by simultaneous addition of 3.75 M silver nitrate and 3.75 M sodium chloride to a
well stirred solution containing 8.2 g/l of sodium chloride, 28.2 g/l of bone gelatin
and 0.212 g/liter of 1,8-dithiadioctanediol while maintaining the temperature at 68.3°C
and the pCl at 1.0. The temperature was reduced to 40° C and the emulsion was washed
by ultrafiltration to a pCl of 2.0, then adjusted to a pCl of 1.65 with sodium chloride.
Emulsion B: (100) surface high chloride tabular emulsion
[0111] A 1.5 L solution containing 3.52% by weight of low methionine gelatin, 0.0056 M sodium
chloride and 0.3 ml of polyethylene glycol antifoamant was provided in a stirred reaction
vessel at 40° C. While the solution was vigorously stirred, 45 ml of a 0.01 M potassium
iodide solution was added followed by 50 mL of 1.25 M silver nitrate and 50 mL of
a 1.25 M sodium chloride solution added simultaneously at a rate of 100 mL/min each.
The mixture was then held for 10 seconds with the temperature remaining at 40° C.
Following the hold, a 0.625 M silver nitrate solution containing 0.08 mg mercuric
chloride per mole of silver nitrate and a 0.621 M sodium chloride and 0.004 M potassium
iodide solution were added simultaneously at 10 mL/min for 30 minutes followed by
a linear acceleration from 10 mL/min to 15 mL/min over 125 minutes. This was followed
by constant flow rate growth for 30 minutes at 15 mL/min while maintaining the pCl
at 1.8. The pCl was then adjusted to 1.65 with sodium chloride. 50 g of phthalated
gelatin was added and the emulsion was washed and concentrated. The pCl after washing
was 2.0. 21 g of low methionine gel was added and the pCl was adjusted to 1.65 with
sodium chloride and the pH was adjusted to 5.7. The resulting emulsion was a tabular
grain silver chloride emulsion containing 0.036 mole percent iodide with a mean equivalent
circular grain diameter of 1.6 and a mean grain thickness of 0.125 µm.
Sensitization
Emulsion A:
[0112] An optimum green light sensitization was found by varying the level of sensitizing
dye, sensitizing agents and digestion time. The conditions for the optimum were as
follows: to a 0.05 mole quantity of Emulsion A melted at 40° C and well stirred, were
added the following; 600 mg/mole of potassium bromide, followed by 0.214 mmol/mole
of sensitizing dye A, then a 20 minute hold, then 0.036 mmol/mole of sensitizing dye
B followed by another 20 minute hold. To this was added 0.75 mg/mol of sodium thiosulfate
pentahydrate and 1.0 mg/mole of potassium tetrachloroaurate. The temperature was then
increased to 60 °C over 6 minutes, held for 10 minutes then ramped to 40 °C over 18
minutes. 70 mg/mole of 1-(3-acetamidophenyl)-5-mercaptotetrazole was then added and
the emulsion was chill set.
Emulsion B:
[0113] An optimum green light sensitization was found in a similar manner to Emulsion A.
The optimum condition were as follows: To a suitable quantity of well stirred emulsion
at 40 °C, 0.80 mmole of sensitizing dye A was added, followed by a 20 minute hold.
To this was added 3.0 mg/mole of sodium thiosulfate pentahydrate and 1.5 mg/mole of
potassium tetrachloroaurate. The temperature was then increased to 60 °C over 6 minutes,
held for 20 minutes then ramped to 40 °C over 18 minutes. 70 mg/mole of 1-(3-acetamidophenyl)-5-mercaptotetrazole
was then added and the emulsion was chill set.
Photographic Coatings
[0114] Each of the sensitized emulsions was coated on an antihalation support at 0.85 g/m²
of silver along with 1.1 g/m² of cyan dye forming coupler A, 2.7 g/m² of gelatin and
varying amounts (shown in Table 1) of development inhibitor releasing coupler B. These
were overcoated with 1.6 g/m² of gelatin and hardened with bis(vinyl-sulfonylmethyl)ether.
Exposure
[0115] Sensitivity to green light was measured by exposing the coatings for 0.01 seconds
using a step wedge sensitometer with a 3000K tungsten lamp filtered to simulate a
Daylight source and filtered to transmit only green and red light by a Kodak Wratten
9 filter.
Process
[0116] The coatings were processed as shown below using either Developer A or B. The photographic
response was evaluated for development times of 30, 60 and 120 seconds.
Process Solutions and Process Sequences Process
[0118] The results are shown in Table 1 below.
TABLE 1
| DIR coupler level g/m² |
development time seconds |
relative speed |
gamma |
minimum density |
| |
|
dev A (inv.) |
dev B (comp.) |
dev A (inv.) |
dev B (comp.) |
dev A (inv.) |
dev B (comp.) |
| |
| Emulsion A (cube): |
| 0 |
30 |
132 |
100 |
1.62 |
1.72 |
0.05 |
0.06 |
| 0 |
60 |
144 |
132 |
2.65 |
2.37 |
0.05 |
0.06 |
| 0 |
120 |
155 |
150 |
4.06 |
3.05 |
0.07 |
0.07 |
| 1.9E-4 |
30 |
143 |
108 |
1.00 |
0.95 |
0.05 |
0.06 |
| 1.9E-4 |
60 |
141 |
135 |
2.39 |
2.04 |
0.05 |
0.06 |
| 1.9E-4 |
120 |
157 |
153 |
2.46 |
2.28 |
0.07 |
0.07 |
| 3.8E-4 |
30 |
149 |
119 |
0.74 |
0.65 |
0.05 |
0.06 |
| 3.8E-4 |
60 |
140 |
143 |
2.22 |
1.23 |
0.05 |
0.06 |
| 3.8E-4 |
120 |
156 |
153 |
2.36 |
2.29 |
0.07 |
0.07 |
| Emulsion B (tabular): |
| 0 |
30 |
207 |
153 |
1.14 |
1.31 |
0.09 |
0.08 |
| 0 |
60 |
233 |
210 |
1.91 |
1.75 |
0.13 |
0.14 |
| 0 |
120 |
255 |
241 |
2.09 |
2.20 |
0.33 |
0.27 |
| 1.9E-4 |
30 |
215 |
152 |
1.06 |
1.19 |
0.10 |
0.08 |
| 1.9E-4 |
60 |
241 |
208 |
1.28 |
1.39 |
0.15 |
0.14 |
| 1.9E-4 |
120 |
254 |
243 |
1.69 |
1.60 |
0.33 |
0.28 |
| 3.8E-4 |
30 |
227 |
167 |
0.80 |
0.78 |
0.09 |
0.07 |
| 3.8E-4 |
60 |
240 |
215 |
1.45 |
1.19 |
0.14 |
0.13 |
| 3.8E-4 |
120 |
261 |
245 |
1.38 |
1.33 |
0.32 |
0.25 |
[0119] Table 1 shows that the speeds for both emulsions when developed for 30 seconds in
developer A are equal to or greater than the speeds when developed for 60 seconds
in developer B, while the gamma for the 30 second developer A process was significantly
lower than the gamma for the 60 second developer B process. The Dmin does not change
significantly. This shows that the inventive combination produces equivalent speeds
to the conventional process at lower gamma and at much shorter development times.
Also the speeds of Emulsion B, even at the shortest development times are much greater
than any speed attained by Emulsion A. This shows that the combination of a high chloride
tabular emulsion with the latent image detection enhanced developer produces the highest
speeds at low gamma and short development times.

Example 4 - Preparation and Processing of an Element Containing an Electron Transfer Agent-Releasing
Compound
A. Preparation of Elements
[0120] Samples 514 and 515 were prepared by applying the following layers to a clear support
in the order indicated. Quantities of components are expressed in grams per square
meter.
[0121] Layer 1 (antihalation layer) comprising gray silver and gelatin.
[0122] Layer 2 (light sensitive layer) comprising 0.538 g of a tabular AgCl emulsion with
an average ECD of 1.4 µm and an average thickness of 0.14 µm, tabular grains bounded
by {100} faces accounted for greater than 50% of the projected grain area; 1.82 g
gelatin; image dye forming coupler C-31 at 0.646 g; DIR compound D-3 at 0.054 g; and
compound B-1 at 0.054 g; and, in sample 515, the electron transfer agent-releasing
(ETAR) compound C-52 at 0.032 g.
[0123] Layer 3 (protective layer) comprising 2.15 g of gelatin.
[0124] The layers additionally comprised alpha-4-nonylphenyl-omega-hydroxy-poly(oxy-(2-hydroxy-1,3-propanediyl))
and (para-t-octylphenyl)-di(oxy-1,2-ethanediyl)-sulfonate as surfactants.
[0125] These films were hardened at coating with 2% by weight to total gelatin of bis-vinylsulfonylmethane.
B. Effect of an electron transfer agent-releasing (ETAR) compound on sensitivity,
gamma, and density of an element
[0126] Samples 514 and 515 were exposed to white light through a graduated density test
object and processed using the KODAK® C-41 process. The bleach used in the process
was modified to comprise 1,3-propylenediamine-tetraacetic acid. The relative sensitivities,
gammas, and maximum densities of the processed elements were determined. These values
are reported in Table 2.
Table 2
| Effect on photographic sensitivity, gamma and density formation produced by electron
transfer agent releasing (ETAR) compound. |
| Sample |
Image-Forming Coupler |
ETAR Compound (quantity) |
Sensitivity |
Relative Gamma |
Density |
| 514 |
C-31 |
none |
100.0% |
100.0% |
100.0% |
| 515 |
C-31 |
C-52 (0.032) |
407.4% |
115.1% |
113.8% |
[0127] As can be seen, the ETAR compound improved the sensitivity, density, and gamma of
the element of the invention containing it. As illustrated in this example, ETAR compounds
can also be used in combination with other PUG-releasing compounds described elsewhere
herein.